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Применить Всего найдено 22186. Отображено 200.
27-12-2008 дата публикации

СИСТЕМА И СПОСОБ ОБРАБОТКИ КИСЛОТНЫХ СТОЧНЫХ ВОД

Номер: RU2342330C2
Принадлежит: ОТВ С.А. (FR)

Изобретение относится к обработке кислотных промышленных сточных вод. Способ удаления фторидов из выходящего потока сточных вод включает установление начального значения рН поступающего потока на уровне меньше, чем примерно 3,5 или поддержание рН поступающего потока на уровне меньше, чем примерно 3,5. Затем направляют сточные воды в первую систему обратного осмоса и удаляют часть фторидов из сточных вод. Поддерживают рН сточных вод на уровне меньше, чем примерно 3,5 по меньшей мере до тех пор, пока идет обработка в первой системе обратного осмоса. Затем направляют сточные воды из первой системы обратного осмоса во вторую систему обратного осмоса и удаляют фториды из сточных вод. После обработки в первой системе обратного осмоса устанавливают высокий рН. В результате использования первой и второй систем обратного осмоса удаляют по меньшей мере 90% фторидов из сточных вод, 2 н. и 23 з.п. ф-лы, 6 ил., 2 табл.

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12-02-2020 дата публикации

Способ очистки воды для бытового использования

Номер: RU2714186C2

Изобретение относится к водоподготовке и может быть использовано для обеспечения населения питьевой водой. Сначала проводят предварительную механосорбционую очистку воды до остаточных включений размером не более 1 мкм в блоке, содержащем картриджи 4 и 5 с фильтрами, заполненными кварцевым песком и активированным углем, и картриджи 6 и 7 микронной и ультрамикронной очистки. Затем поток воды пропускают через зону генератора 8 магнитного поля до входа в насос 9 высокого давления, выход которого сообщён с камерой кавитационного реактора 10. Далее воду очищают, последовательно пропуская её под давлением через мембрану обратноосмотической установки 11 и через фильтры 12 и 13 с активированным углем и с шунгитосеребряной загрузкой. Очищенную воду перед отпуском потребителю направляют в минерализатор 14 и в накопитель 15, в котором проводят стерилизацию ультрафиолетовыми лампами для поддержания в воде отсутствия бактериальной составляющей. Подаваемую потребителю воду, охлаждённую в соответствующем ...

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08-02-2017 дата публикации

МОДИФИЦИРОВАННЫЕ СУЛЬФИРОВАННЫЕ БЛОК-СОПОЛИМЕРЫ И ИХ ПОЛУЧЕНИЕ

Номер: RU2610265C2

Изобретение относится к модифицированному сульфированному блок-сополимеру, мембране, устройству, электродеионизационной установке, а также к изделию с покрытием. Блок-сополимер содержит по меньшей мере два концевых полимерных блока А, и по меньшей мере один внутренний полимерный блок В. Каждый блок А, по существу, не содержит сульфокислотных или сульфонатных функциональных групп. Каждый блок В содержит мономерные звенья, чувствительные к сульфированию, и содержит в расчете на количество чувствительных к сульфированию мономерных звеньев от 10 до 100 мол.% функциональной группы формулы (I):или ее соли, где Rпредставляет собой фрагмент -(A-NR)Rили фрагмент-(А-NR)-A-Z; Rпредставляет собой атом водорода, алкил или один из фрагментов R; или Rи Rвместе с атомом азота, к которому они присоединены, образуют необязательно замещенный 5-7-членный цикл, состоящий из 1-3 атомов азота, 2-6 атомов углерода и необязательно 1 или 2 несмежных кольцевых атомов кислорода и/или серы, x имеет значение 0, 1, 2 ...

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10-07-2015 дата публикации

ИЗВЛЕЧЕНИЕ ОБРАТИМО РАСТВОРИМОГО РАСТВОРЕННОГО ВЕЩЕСТВА ДЛЯ ПРЯМООСМОТИЧЕСКОЙ ВОДООЧИСТКИ

Номер: RU2556662C2
Принадлежит: ТРЕВИ СИСТЕМЗ ИНК. (US)

Изобретения могут быть использованы для обессоливания морской, жесткой и/или загрязненной воды прямым осмотическим обессоливанием. Для осуществления способа очистки загрязненной воды поток загрязненного питающего раствора, содержащего воду и имеющего первое осмотическое давление, пропускают через полупроницаемую мембрану на сторону выведения, имеющую поток выводящего раствора со вторым осмотическим давлением на стороне выведения полупроницаемой мембраны. Поток разбавленного выводящего раствора нагревают, агломерируют выводимое растворенное вещество в двухфазный выходящий поток, содержащий жидкую фазу агломерированного выводимого растворенного вещества и жидкую водную фазу. Затем отделяют агломерированное растворенное вещество и получают водообогащенный поток, который охлаждают с получением охлажденного однофазного водообогащенного потока, который очищают от остаточного растворенного вещества с получением очищенной воды. Изобретения обеспечивают повышение качества прямоосмотической водоочистки ...

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30-06-2020 дата публикации

УСТРОЙСТВО И СПОСОБ ОБРАБОТКИ ВОДОСОДЕРЖАЩЕЙ ЖИДКОСТИ

Номер: RU2725257C2
Принадлежит: БРИТА ГМБХ (DE)

Изобретение относится к устройству для кондиционирования водосодержащей жидкости. Устройство для кондиционирования водосодержащей жидкости включает в себя по меньшей мере один впуск; по меньшей мере одно устройство обработки жидкости для обработки жидкости с помощью ионного обмена, включающее себя катионообменный материал, по меньшей мере часть которого находится в водородной форме, и являющееся эффективным для выделения водорода при обмене на катионы карбонатных минералов в обрабатываемой жидкости, таким образом, повышая количество свободного диоксида углерода; мембранное фильтрационное устройство и секцию, предназначенную для обработки фильтрата, производимого с помощью мембранного фильтрационного устройства, причем секция включает в себя устройство обработки жидкости для растворения по меньшей мере одного минерала, способствующего карбонатной жесткости в воде, в по меньшей мере части жидкости, проходящей через секцию, по меньшей мере один из по меньшей мере одного впуска соединен с впуском ...

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10-01-2010 дата публикации

ФИЛЬТР ОЧИСТКИ ВОДЫ, ЛЕГКО ЗАМЕНЯЕМЫЙ С ПОМОЩЬЮ СОЕДИНИТЕЛЯ, И СИСТЕМА ОЧИСТКИ ВОДЫ, В КОТОРОЙ ИСПОЛЬЗОВАН ЭТОТ ФИЛЬТР

Номер: RU2378034C2
Принадлежит: ПИКОГРАМ КО., ЛТД. (KR)

Изобретение относится к фильтру очистки воды, легко заменяемому с помощью соединителя, а также к системе очистки воды, в которой используется такой фильтр. Фильтр очистки воды содержит соединитель (55), имеющий впускное отверстие (50), корпус контрольного клапана (54), который имеет канал подаваемой воды (50А) и канал выпуска воды с концентрированными примесями (53), выпускное отверстие (52) и отверстие управления водой с концентрированными примесями (76), служащее для выпуска наружу воды с концентрированными примесями. Кроме того, фильтр содержит корпус (57), служащий для размещения фильтра (56) с мембраной обратного осмоса, запирающее средство, служащее для разъемного крепления корпуса фильтра (57) к соединителю (55), и направляющую (63) переключения каналов. Изобретение позволяет упростить соединительное устройство системы очистки воды и позволяет легко заменять фильтр путем простого разъединения картриджа фильтра от системы очистки воды. 3 н. и 21 з.п. ф-лы, 22 ил.

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06-03-2019 дата публикации

УСТАНОВКА ДЛЯ ОЧИСТКИ СТОЧНЫХ ВОД НА БОРТУ СУДОВ

Номер: RU2681458C2

Изобретение относится к очистке сточных вод на борту судов. Установка для очистки сточных вод на борту судов содержит по меньшей мере один сборный резервуар, соединенный с впуском фекальных сточных вод и бытовых сточных вод, образующихся на борту; блок первичной очистки, содержащий по меньшей мере один ленточный фильтр; блок вторичной очистки, содержащий по меньшей мере один фильтр для микрофильтрации или ультрафильтрации; блок третичной очистки, содержащий по меньшей мере один модуль озонирования; средство для непрерывной подачи фекальных сточных вод и бытовых сточных вод из указанного по меньшей мере одного сборного резервуара в блок первичной очистки; средство для подачи фильтрата из блока первичной очистки в блок вторичной очистки; средство для подачи фильтрата из блока вторичной очистки в блок третичной очистки. Достигается эффективность установки для повторного использования воды для различных целей или для осуществления последующего сброса за борт судна. 2 н. и 8 з.п. ф-лы, 3 ил.

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27-10-2009 дата публикации

АППАРАТ АВТОМАТИЧЕСКОЙ ПРОМЫВКИ МЕМБРАННОГО ФИЛЬТРА В ОЧИСТИТЕЛЕ ВОДЫ

Номер: RU2371236C2

Изобретение относится к аппаратам автоматической промывки мембранного фильтра в очистителе воды. Очиститель воды включает седиментационный фильтр, предварительный угольный фильтр и мембранный фильтр для последовательной фильтрации сырой воды. Аппарат автоматической промывки мембранного фильтра включает датчик низкого давления (ДНД) для детектирования давления воды в водяной трубе, соединяющей седиментационный фильтр с предварительным угольным фильтром, насос для нагнетания воды, подаваемой из седиментационного фильтра в предварительный угольный фильтр, регулятор, обеспечивающий регулирование слива воды из внутренней части мембранного фильтра от момента времени, когда обнаружено напряжение нагнетания, и сливной регулируемый вентиль для открывания сливной трубы мембранного фильтра. Технический результат: удаление накипи из внутренней части мембранного фильтра под действием давления слива воды из него через сливной регулируемый вентиль. 2 з.п. ф-лы, 3 ил.

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27-12-2009 дата публикации

СПОСОБ И УСТРОЙСТВО ДЛЯ КОНТРОЛЯ И ОГРАНИЧЕНИЯ ЗАГРЯЗНЕНИЯ МИКРООРГАНИЗМАМИ В КОНТУРАХ УВЛАЖНЯЮЩИХ СРЕДСТВ

Номер: RU2377187C2

Изобретение относится к технологии уменьшения загрязнения микроорганизмами контуров с водными средами. Способ и устройство для уменьшения загрязнения микроорганизмами контуров с водными средами включает в себя стадию электрохимической обработки водной среды, причем упомянутый контур представляет собой контур увлажняющего средства, при этом упомянутую электрохимическую обработку осуществляют путем приложения напряжения к по меньшей мере двум электродам, при этом упомянутое напряжение является переменным напряжением с диапазоном от 5 до 50 Вольт. Изобретение позволяет уменьшить число микроорганизмов при уже имеющемся загрязнении, а также предотвратить их новообразование. 4 н. и 20 з.п. ф-лы, 2 ил.

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10-08-2009 дата публикации

УСТАНОВКА ДЛЯ НЕПРЕРЫВНОГО ОБЕССОЛИВАНИЯ ВОДЫ В ЗАМКНУТОМ КОНТУРЕ ПРИ ПЕРЕМЕННОМ ДАВЛЕНИИ В ОДНОМ КОНТЕЙНЕРЕ

Номер: RU2363663C2
Принадлежит: ЕФРАТИЙ Ави (IL)

Изобретение предназначено для опреснения морской и обессоливания жесткой воды. Установка непрерывного ступенчатого обессоливания солевого водного раствора обратным осмосом включает контур замкнутого цикла с одним или несколькими модулями обессоливания, соединенными параллельно, средство создания противодавления, средство циркуляции для обеспечения рециркуляции обессоленного раствора в указанном замкнутом контуре и контейнер для замены концентрированного солевого раствора свежим питающим раствором. Установка дополнительно снабжена средствами контроля и клапанным механизмом, обеспечивающим отключение контейнера и подключение его к замкнутому контуру, замену концентрированного соляного раствора на свежий питающий раствор из контейнера, а также нагнетание давления и декомпрессию контейнера. Каждый из модулей обессоливания включает один или более мембранных элементов. Изобретение также относится к способу обессоливания солевого водного раствора посредством указанной установки. Изобретение позволяет ...

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23-03-2020 дата публикации

УСТОЙЧИВЫЕ К ХЛОРУ ГИДРОФИЛЬНЫЕ ФИЛЬТРАЦИОННЫЕ МЕМБРАНЫ НА ОСНОВЕ ПОЛИАНИЛИНА

Номер: RU2717512C2

Изобретение относится к устойчивым к хлору фильтрационным мембранам, содержащим N-алкилзамещенные производные полианилина, для применения, например, для очистки воды и к способам их получения и применения. 6 н. и 17 з.п. ф-лы, 8 ил., 3 табл.

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25-09-2018 дата публикации

УСТАНОВКА ОЧИСТКИ И ОБЕЗЗАРАЖИВАНИЯ ВОДЫ

Номер: RU2668036C2

Изобретение может быть использовано для очистки и обеззараживания воды из природных сильно загрязненных источников. Установка очистки и обеззараживания воды содержит фильтр 1 предварительной очистки воды, подключенный входом к источнику исходной воды, а выходом - к контактной ёмкости 3, к которой подключен источник озона. Выход обработанной озоном воды ёмкости 3 сообщён с ультрафильтрационным модулем 4. Выход очищенной воды ультрафильтрационного модуля 4 сообщён с модулем обратного осмоса 5. Контактная ёмкость 3 снабжена насосом 6 подачи обработанной озоном воды и эжектором 7, сообщённым с источником озона. Ультрафильтрационный модуль 4 подключён входом к выходу насоса 6 посредством трубопровода, на котором последовательно по ходу обработанной озоном воды установлены обратный клапан 9 и регулировочный клапан 10. Полость ультрафильтрационного модуля 4 перед ультрафильтрационной мембраной через сбросной кран 11 сообщена с канализацией, а полость после ультрафильтрационной мембраны подключена ...

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27-12-2014 дата публикации

УСТРОЙСТВО ДЛЯ ВЫРАБОТКИ СВЕРХЧИСТОЙ ВОДЫ

Номер: RU2536993C2
Принадлежит: ФЁЛЬКЕР Манфред (DE)

Изобретение относится к устройству для очистки воды по принципу обратного осмоса. Устройство для выработки сверхчистой воды по принципу обратного осмоса содержит фильтр обратного осмоса, который мембраной обратного осмоса разделен на первичную камеру и вторичную камеру, первичный контур, через который к первичной камере подводится сырая вода и из нее отводится концентрат, а также вторичный контур для подвода пермеата по меньшей мере к одному потребителю, предпочтительно аппарату для диализа. В трубопровод первичного контура встроен насос, а в трубопровод концентрата первичного контура встроен клапан со сливом. В или на первичном контуре и/или вторичном контуре расположено устройство для регистрации органических и/или неорганических отложений, соединенное с устройством обработки данных, а во вторичный контур встроен эластичный, способный расширяться буферный сосуд, приспособленный для выполнения обратной промывки мембраны пермеатом. Устройство для регистрации органических и/или неорганических ...

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15-04-2022 дата публикации

СПОСОБ ОПРЕСНЕНИЯ МОРСКОЙ ВОДЫ

Номер: RU2770360C1

Изобретение может быть использовано для сельскохозяйственного, промышленного и бытового водоснабжения. В способе опреснения морской воды используют пониженное гидростатическое давление столба воды в акватории. Для достижения давления, необходимого при опреснении морской воды, используют насос объемного действия с возвратно-поступательным движением рабочего органа 4, обеспеченным за счет использования энергии морских волн, снимаемой при возвратно-поступательном движении буя 2 с положительной плавучестью, скрепленного с корпусом 3 насоса, и эластичной мембраны 6, с нижней стороны скрепленной с пригрузом 9 на дне моря, а с верхней стороны соединенной жестко с рабочим органом 4. Давление в насосе повышают за счет разницы площадей эластичной мембраны 6 и поперечного сечения рабочего органа 4. Внутри корпуса 3 для предотвращения утечек морской воды располагают соединённый с ним гибкий герметичный рукав 5. Для уменьшения трения между гибким герметичным рукавом 5 и рабочим органом 4 используют ...

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10-02-2020 дата публикации

Номер: RU2018127003A3
Автор:
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17-04-2019 дата публикации

КОМПОЗИЦИОННЫЙ ФИЛЬТРУЮЩИЙ КАРТРИДЖ, БЛОК КОМПОЗИЦИОННОГО ФИЛЬТРУЮЩЕГО КАРТРИДЖА ДЛЯ ВОДООЧИСТИТЕЛЯ И ВОДООЧИСТИТЕЛЬ

Номер: RU2685313C2
Принадлежит: МИДЕА ГРУП КО., ЛТД. (CN)

Предложены композиционный фильтрующий картридж (100), блок композиционного фильтрующего картриджа для водоочистителя и водоочиститель. Композиционный фильтрующий картридж (100) содержит фильтрующий картридж для предварительной обработки (110), фильтрующий картридж для тонкой фильтрации (120) и фильтрующий картридж с активированным углем (130), расположенные последовательно снаружи внутрь. Фильтрующий картридж для тонкой фильтрации (120) содержит первую водосборную трубу (121) и мембрану для тонкой фильтрации (122). Фильтрующий картридж с активированным углем (130) содержит вторую водосборную трубу (131), наружную окружную стенку второй водосборной трубы, исключая ее нижний конец, и внутреннюю окружную стенку первой водосборной трубы, находящиеся на расстоянии друг от друга; и активированный уголь (132), причем нижние концы активированного угля (132) и второй водосборной трубы (131) находятся в герметичном соединении. Выпускное отверстие для воды (132a) выполнено в активированном угле и ...

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10-09-2013 дата публикации

СПОСОБ ОБОГАЩЕНИЯ ВОДЫ КИСЛОРОДОМ ПОСРЕДСТВОМ ЭЛЕКТРОЛИТИЧЕСКОГО ПРОЦЕССА, ВОДА ИЛИ НАПИТОК, ОБОГАЩЕННЫЕ КИСЛОРОДОМ, И ИХ ПРИМЕНЕНИЕ

Номер: RU2492146C2

Изобретение относится к воде или напитку, обогащенным кислородом посредством электролитического процесса, и способу их получения. Способ обогащения воды кислородом посредством электролиза включает в себя следующие последовательные этапы: a) электролиз минерализованной, но освобожденной от ионов Clи Brводы, в электролизере (3), в котором анод и катод разделены газонепроницаемой мембраной, проницаемой для электрических зарядов; b) получение воды, обогащенной кислородом, из анодного отделения электролизера (3b); c) обратное введение воды, вышедшей из катодного отделения электролизера (3a) и освобожденной от водорода, в воду, обогащенную кислородом, полученную на этапе (b); d) упаковывание (5) воды, полученной на этапе (c). Технический результат - получение воды или напитка, в котором кислород является биологически доступным. 4 н. и 7 з.п. ф-лы, 9 ил., 7 табл., 4 пр.

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10-10-2013 дата публикации

УСТАНОВКА ДЛЯ УМЯГЧЕНИЯ ВОДЫ ОБРАТНЫМ ОСМОСОМ

Номер: RU2494971C2
Принадлежит: ФЁЛЬКЕР Манфред (DE)

Изобретение относится к устройствам для очистки воды по принципу обратного осмоса и может быть использовано для приготовления диализирующей жидкости. Устройство для выработки высокочистой воды по принципу обратного осмоса содержит фильтр обратного осмоса, который посредством мембраны обратного осмоса разделен на первичную камеру и вторичную камеру, и насос, который прокачивает жидкость через первичную камеру, а также расположенное выше по потоку от мембраны обратного осмоса, необходимое для создания давления в первичной камере гидравлическое сопротивление. В первичном контуре находятся по меньшей мере одна камера очистки с устройствами для умягчения воды и сливной клапан, причем поток жидкости в первичном контуре регулируется с помощью клапана и первичный контур выполнен с возможностью промывки его объема по типу подтопления путем открывания клапанов. Технический результат - увеличение эффективности очистки и снижение энергозатрат. 8 з.п. ф-лы, 11 ил.

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20-06-2011 дата публикации

УЗЕЛ ХРАНЕНИЯ ФИЛЬТРОВАННОЙ ВОДЫ ДЛЯ НАКОПИТЕЛЬНОГО УСТРОЙСТВА СИСТЕМЫ ОЧИСТКИ ВОДЫ, НАКОПИТЕЛЬНОЕ УСТРОЙСТВО СИСТЕМЫ ОЧИСТКИ ВОДЫ (ВАРИАНТЫ), СИСТЕМА ОЧИСТКИ ВОДЫ (ВАРИАНТЫ)

Номер: RU2421270C1

Изобретения относятся к средствам для обработки воды, преимущественно питьевой воды, и могут быть использованы в бытовых системах очистки воды. Предложенный узел хранения фильтрованной воды для накопительного устройства системы очистки воды включает в себя корпус, расположенную в нем эластичную камеру для фильтрованной воды и образованную пространством между стенками камеры и корпуса зону нагнетания неочищенной воды, причем эластичная камера выполнена из термоэластопласта и состоит из выполненных заедино тела камеры и горловины, жестко закрепленной в корпусе, причем тело камеры выполнено из модифицированного термоэластопласта двухосноориентированной структуры, в частности из термопластичных полиолефиновых эластомеров или термопластичных стирольных эластомеров. Также группа изобретений включает 2 варианта Накопительного устройства системы очистки воды и 2 варианта Системы очистки воды, включающей накопительное устройство и узел хранения фильтрованной воды. Изобретения предложенной группы ...

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06-02-2023 дата публикации

Способ получения воды с заданными свойствами и устройство для его осуществления

Номер: RU2789531C1

Заявленная группа изобретений относится к области получения воды с заданными свойствами по степени чистоты и водородному показателю. Способ состоит из процессов предварительной подготовки воды, мембранной фильтрации, получения католита и анолита в электролизере, а также их смешения. Мембранную фильтрацию осуществляют по меньшей мере на одном устройстве мембранной фильтрации. Подачу очищаемой воды во входное отделение по меньшей мере первого устройства мембранной фильтрации осуществляют с помощью по меньшей мере одного водоструйного эжектора, через который одновременно подают озоно-воздушную или озоно-кислородную смесь для озонирования этой воды. Вместе с этим в технологическую схему процесса предварительной подготовки воды подают католит до достижения значения водородного показателя (рН) в интервале от 8,0 до 11,0 в фильтруемой воде на стадии предварительной подготовки и по меньшей мере первого устройства мембранной фильтрации. Технический результат: повышение степени очистки воды от органических ...

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20-10-1998 дата публикации

МЕДИЦИНСКАЯ ЖИДКОСТЬ ДЛЯ КОНСЕРВАТИВНОГО ЛЕЧЕНИЯ (ВАРИАНТЫ), СПОСОБ ЕЕ ПОЛУЧЕНИЯ И ДИАЛИЗНОЕ УСТРОЙСТВО (ВАРИАНТЫ)

Номер: RU2120413C1
Принадлежит: Нихон Трим Ко., Лтд. (JP)

Может быть использовано в медицине при консервативном лечении. Сущность изобретения заключается в том, что предлагается жидкость для консервативного лечения, которая может уничтожать супероксидный анион-радикал (САР), являющийся побудителем различных заболеваний. Сырую воду, которая содержит по меньшей мере ионы натрия, калия, магния и кальция, подают в катодную камеру и анодную камеру. Для того чтобы осуществить электролиз сырой воды, в течение 0,5 - 5 с через катодный электрод и анодный электрод пропускают ток в диапазоне от 0,16 до ~ 3,2 мА/см2 в расчете на два электрода и одну диафрагму. По этому способу получают воду для консервативного лечения, которая имеет величину окислительно-восстановительного потенциала (в диапазоне) не менее -150 мВ при измерении с использованием платинового электрода. Вода для консервативного лечения может удалять из крови пациента САР, который становится причиной различных заболеваний. 3 с. и 14 з.п. ф-лы, 8 ил., 3 табл.

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07-10-2019 дата публикации

СПОСОБ ПРОМЫВКИ И ПРОМЫВОЧНАЯ МАШИНА

Номер: RU2702245C1

Изобретение относится к способу промывки и к промывочной машине. В способе промывки согласно настоящему изобретению в промывочной машине подготавливают воду, обладающую способностью окислительного и дезинфицирующего воздействия, и используют в качестве промывочной воды или добавляют к промывочной воде. Для подготовки воды, обладающей способностью окислительного и дезинфицирующего воздействия, поток сырой воды подают в устройство обратного осмоса и разделяют в нем на поток концентрата и поток пермеата, вырабатывают озон посредством озонного генератора и указанный озон вводят в выходящий из устройства обратного осмоса поток пермеата, при этом введение озона в поток пермеата связано с эксплуатацией устройства обратного осмоса. Для осуществления вышеупомянутого способа промывки предложена также промывочная машина. Технический результат – более эффективная система очистки (процедура озонирования), предупреждающая появление неприятного запаха, например, на бокалах для вина и стаканах для воды ...

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11-03-2019 дата публикации

СИСТЕМА ФИЛЬТРАЦИИ ВОДЫ

Номер: RU2681629C1
Автор: ЯН Люй (CN)

Изобретение относится к водоочистке. Система (100) фильтрации воды содержит впуск (100а) для исходной воды, выпуск (100b) для чистой воды, выпуск (100c) для очищенной воды, выпуск (100d) для сточной воды, объединенный фильтрующий картридж (1) и путь (101) возвратного потока. Объединенный фильтрующий картридж (1) имеет первое отверстие (10а), второе отверстие (10c), третье отверстие (10b) и четвертое отверстие (10d). Выпуск (100с) для очищенной воды и выпуск (100d) для сточной воды соединены с третьим отверстием (10c). Устройство (2) для хранения воды предусмотрено по меньшей мере на одном из четвертого отверстия (10d) и пути потока, соединенного с выпуском (100b) для чистой воды. Путь (101) возвратного потока имеет первый конец, присоединенный между первым отверстием (10а) и впуском (100а) для исходной воды, и второй конец, присоединенный между выпуском (100d) для сточной воды и третьим отверстием (10с). Изобретение позволяет улучшить коэффициент извлечения системы фильтрации воды и обеспечить ...

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22-01-2019 дата публикации

СИСТЕМА ОЧИСТКИ ВОДЫ

Номер: RU2678062C1

Изобретение может быть использовано для очистки воды. Система очистки воды (100) содержит блок композиционного фильтрующего картриджа (1), бустерный насос (4), электромагнитный клапан (7) для сточной воды и устройство для хранения воды (91). Блок композиционного фильтрующего картриджа (1) содержит фильтрующий корпус (11) и композиционный фильтрующий картридж (12). Фильтрующий корпус (11) имеет впуск (111) неочищенной воды, отверстие (114) для чистой воды, выпуск (112) чистой воды и выпуск (113) концентрированной воды. Композиционный фильтрующий картридж (12) содержит фильтрующий блок и улучшающий вкус фильтрующий картридж (123), расположенный ниже по потоку относительно фильтрующего блока. Отверстие (114) для чистой воды соединяется с выпускающим воду концом фильтрующего блока и впускающим воду концом улучшающего вкус фильтрующего картриджа (123). Бустерный насос (4) соединен с впуском (111) неочищенной воды. Электромагнитный клапан (7) для сточной воды соединен с выпуском (113) концентрированной ...

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09-08-2018 дата публикации

Способ создания систем прямоточного обратноосмотического фильтрования, система обратноосмотического фильтрования (варианты) и помповый блок системы обратноосмотического фильтрования (варианты)

Номер: RU2663739C1
Автор:

Изобретение относится к средствам очистки воды. Помповый блок системы обратноосмотического фильтрования содержит корпус 18, внутри которого установлены блок питания 19 и подключенные к нему насос 20, первый 21 и второй 22 датчики давления, контроллер 26, регулируемый клапан 23, электромагнитный клапан 24. Технический результат: повышение качества и степени эффективности очистки. 5 н. и 21 з.п. ф-лы, 8 ил.

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20-12-2015 дата публикации

СПОСОБ ОЧИСТКИ ЖИДКОСТИ И СИСТЕМА ДЛЯ ЕГО РЕАЛИЗАЦИИ

Номер: RU2014123820A
Принадлежит:

... 1. Способ очистки жидкости, заключающийся в пневматически запускаемом цикле фильтрации жидкости с рециркуляцией, в котором на первой стадии цикла заполняют исходной жидкостью емкость для исходной жидкости, являющуюся частью блока рециркуляции жидкости, входящего в блок очистки жидкости, после чего блоку рециркуляции при помощи средства создания давления сообщают энергию сжатого газа, за счет которой в блоке рециркуляции жидкости устанавливается давление достаточное для протекания фильтрации жидкости в блоке фильтрации, являющемся частью блока очистки, на второй стадии цикла, отличающийся тем, что цикл фильтрации жидкости включает три стадии, проходящие с возможностью непрерывного возврата всей дренажной жидкости в систему очистки до окончания цикла фильтрации жидкости.2. Способ очистки жидкости по п. 1, отличающийся тем, что на первой стадии цикла фильтрации жидкости передачу энергии сжатого газа или сжатой смеси газа и жидкости осуществляют, но, не ограничиваясь только этим, через не проницаемую ...

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29-07-2020 дата публикации

УСТРОЙСТВО И СПОСОБ ОБРАБОТКИ СОЛЕСОДЕРЖАЩЕЙ ВОДЫ ПОСРЕДСТВОМ ОБРАТНОГО ОСМОСА

Номер: RU2728347C1
Принадлежит: БВТ АКВА АГ (CH)

Изобретение относится к устройству и способу обработки солесодержащей воды посредством обратного осмоса. Устройство содержит впуск для солесодержащей воды, выпуск для пермеата, выпуск для концентрата, причем впуск и выпуски встроены в базовый блок, выполненный с возможностью стационарной установки, устройство обратного осмоса, выполненное в виде сменного блока, соединенного с базовым блоком с возможностью отсоединения, и смесительное устройство, посредством которого предусмотрена возможность смешения пермеата, вытекающего из устройства обратного осмоса, с солесодержащей водой, при этом смесительное устройство выполнено в виде клапана и содержит канал, ограниченный стенкой, причем в стенке канала выполнена по меньшей мере одна прорезь, через которую в канал предусмотрена возможность поступления солесодержащей воды, и корпус клапана, установленный внутри канала с возможностью осевого и/или вращательного смещения. Изобретение обеспечивает снижение содержания солей в обрабатываемой воде более ...

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01-10-2018 дата публикации

УСТРОЙСТВО ДЛЯ УДАЛЕНИЯ ПРИМЕСЕЙ ИЗ ПОТОКА ФЛЮИДА

Номер: RU2668436C1

Группа изобретений относится к устройству и способу для удаления примесей из потока флюида, например потока жидкости, такой как вода. Устройство для сепарации материалов, взвешенных в потоке флюида, содержит несущую конструкцию, сепараторный узел, вращательно закрепленный на несущей конструкции, устройства для вращения сепараторного узла на несущей конструкции, сепараторный узел, имеющий продольную ось вращения, пролегающую через продольную трубу, расположенную по центру внутри сепараторного узла. При этом продольная труба соединена или выполнена с возможностью соединения с источником находящегося под давлением флюида, нуждающегося в сепарации, и продольная труба имеет одно или более отверстий для приема потока под давлением из указанного источника и одно или более боковых отверстий для введения флюида в сепараторный узел. Сепараторный узел, дополнительно к продольной трубе, содержит камеру центробежной сепарации для сепарации взвешенных материалов из потока флюида, коллектор для сбора ...

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13-05-2020 дата публикации

СПОСОБ И УСТРОЙСТВО ДЛЯ ПЕРЕРАБОТКИ НАВОЗНОГО ШЛАМА

Номер: RU2720866C1
Принадлежит: ВАЛИО ЛТД (FI)

Изобретение относится к способу переработки навозного шлама, включающему стадии: обеспечения навозного шлама, подвергания навозного шлама разделению с получением первой сухой фракции и первой жидкой фракции, подвергания первой жидкой фракции стадии центрифугирования с получением второй сухой фракции и второй жидкой фракции, подвергания второй жидкой фракции одной или более последовательным стадиям фильтрации обратным осмосом (RO) с получением одного или более RO-ретентатов и одного или более RO-пермеатов, причем сырьем для каждой последующей стадии RO-фильтрации является RO-пермеат, полученный на предыдущей стадии RO-фильтрации. Изобретение касается также устройства для переработки навозного шлама. Техническим результатом является повышение эффективности переработки навозного шлама с получением удобрения различных фракций. 2 н. и 21 з.п. ф-лы, 3 табл., 2 пр., 3 ил.

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20-10-1996 дата публикации

СПОСОБ ПОЛУЧЕНИЯ И ПОДГОТОВКИ МОЕЧНОЙ ВОДЫ ДЛЯ МОЕЧНОЙ УСТАНОВКИ И МОЕЧНАЯ УСТАНОВКА

Номер: RU94046281A
Принадлежит:

Изобретение относится к способу получения и подготовки моечной воды для моечной установки. Для расходования сравнительно небольших количеств моечной воды отведенную моечную воду повторно используют, в основном в замкнутом циркуляционном контуре для последующих моечных процессов, для этого отведенную моечную воду собирают и подают к фильтровальной установке или подобному подготовительному устройству, при этом частичное количество полученного в подготовительном устройстве фильтрата или подобной чистой воды подают для одного последующего моечного процесса в качестве моечной воды. Изобретение относится также к моечной установке, в частности установке для мойки автомобилей, содержащей душевую головку или подобный выпуск для моечной воды, который предусмотрен для подачи моечной воды на автомобиль или подобный очищаемый предмет. Отличительные признаки изобретения: установка содержит улавливающее устройство для сбора моечной воды по окончании каждого моечного процесса и соединено с водоподготовительным ...

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01-03-2019 дата публикации

СИСТЕМА ФИЛЬТРАЦИИ ВОДЫ

Номер: RU2017130284A
Автор: ЯН Люй (CN)
Принадлежит:

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10-06-2013 дата публикации

СПОСОБ ПЕРЕРАБОТКИ ОБРАЗУЮЩИХСЯ НА ЯДЕРНЫХ ОБЪЕКТАХ ЖИДКИХ РАДИОАКТИВНЫХ ОТХОДОВ ПРАЧЕЧНЫХ

Номер: RU2011149348A
Принадлежит:

Способ переработки образующихся на ядерных объектах жидких радиоактивных отходов прачечных, включающий сбор жидких отходов стадий стирки и полоскания, очистку от механических загрязнений жидких отходов и введение в них ассоциирующих добавок, ультрафильтрацию образующейся смеси, возврат пермеата ультрафильтрации на прачечную и передачу концентрата загрязнений на кондиционирование, отличающийся тем, что после сбора жидких отходов стадии стирки и стадии полоскания их смешивают, а перед возвратом пермеата ультрафильтрации на прачечную его разделяют обратным осмосом на концентрат обратного осмоса, который направляют на стадию стирки, и пермеат обратного осмоса, который направляют на стадию полоскания.

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10-10-2014 дата публикации

МЕМБРАНА ДЛЯ ОБРАТНОГО ОСМОСА

Номер: RU2013113670A
Принадлежит:

... 1. Модуль обратного осмоса, содержащий соответственно трубу (2) модуля с дном (20) модуля и крышкой (22) модуля и расположенную в трубе (2) модуля мембрану (3) обратного осмоса с пермеатной собирающей трубой (9), отличающийся тем, что мембрана (3) обратного осмоса имеет постоянный, заранее заданный диаметр и выбранную из заранее заданной градации длин длину.2. Модуль обратного осмоса по п.1, отличающийся тем, что заранее заданный диаметр составляет от 4,7 дюйма (~120 мм) до 5 дюймов (~127 мм), предпочтительно 4,9 дюйма (~125 мм), и возможные градации длин составляют примерно 40 дюймов (~1020 мм), 23 дюйма (~585 мм) и 12 дюймов (~305 мм).3. Модуль обратного осмоса по п.1, отличающийся тем, что производительность мембраны (3) обратного осмоса составляет 500 л/час, 250 л/час и 100 л/час.4. Модуль обратного осмоса по п.1, отличающийся тем, что площадь мембраны (3) обратного осмоса составляет 15 м, 6,6 ми 2,8 м.5. Модуль обратного осмоса по п.1, отличающийся тем, что поток через мембрану находится ...

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20-05-2014 дата публикации

СПОСОБ ОЧИСТКИ ХИМИЧЕСКИХ СОЕДИНЕНИЙ СТОЧНЫХ ВОД ЦЕЛЛЮЛОЗНО-БУМАЖНЫХ КОМБИНАТОВ

Номер: RU2012147024A
Принадлежит:

... 1. Способ обогащения или выделения целевого соединения из сточных вод целлюлозно-бумажного комбината, при этом способ предусматривает следующие стадии:- получение конденсата из выпарного аппарата или ретентата процесса обратного осмоса (RO) конденсатов на целлюлозно-бумажном комбинате, или обоих, при этом конденсат, ретентат или оба из них по существу не содержат высокомолекулярную целлюлозу и/или лигнин, и/или происходящие из лигнина материалы,- экстрагирование конденсата органическим растворителем методом твердофазной экстракции (SPE), экстракции в системе жидкость-жидкость или твердое тело-жидкость с получением экстракта, содержащего указанные целевые соединения, и- необязательно очистка целевого соединения из экстракта путем термического фракционирования, хроматографического разделения (такого как нормально-фазовое, обращенно-фазовое, афинное или их комбинации), рекристаллизации, ионного обмена, хелатирования, адсорбции/десорбции, лиофилизации и сублимации или их комбинаций.2. Способ ...

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27-03-2014 дата публикации

УСТРОЙСТВО ДЛЯ ВЫРАБОТКИ СВЕРХЧИСТОЙ ВОДЫ

Номер: RU2012140697A
Принадлежит:

... 1. Устройство для выработки сверхчистой воды по принципу обратного осмоса с фильтром обратного осмоса, который мембраной обратного осмоса разделен на первичную камеру и вторичную камеру, с первичный контуром, через который к первичной камере подводится сырая вода и из нее отводится концентрат, а также вторичным контуром для подвода пермеата по меньшей мере к одному потребителю, предпочтительно аппарату для диализа,отличающееся тем, чтов или на первичном контуре (1, 4, 5, 9, 17, 18) и/или вторичном контуре (8, 15, 16) расположено устройство для регистрации органических и/или неорганических отложений, которое соединено с устройством обработки данных.2. Устройство по п.1, отличающееся тем, что устройство обработки данных соединено с устройством индикации измеряемых значений.3. Устройство по п.1, отличающееся тем, что устройство обработки данных при достижении или превышении предварительно заданного граничного измеряемого значения выдает предупредительный сигнал.4. Устройство по п.1, отличающееся ...

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27-02-2013 дата публикации

УСТАНОВКА ДЛЯ УМЯГЧЕНИЯ ВОДЫ ОБРАТНЫМ ОСМОСОМ

Номер: RU2011135436A
Принадлежит:

... 1. Устройство для выработки высокочистой воды по принципу обратного осмоса с фильтром обратного осмоса, который посредством мембраны обратного осмоса разделен на первичную камеру и вторичную камеру, и насосом, который прокачивает жидкость через первичную камеру, а также расположенным выше по потоку от мембраны обратного осмоса, необходимым для создания давления в первичной камере гидравлическим сопротивлением, отличающееся тем, что в первичном контуре (1, 4, 5, 9, 17, 18) находятся по меньшей мере одна камера (21) очистки с устройствами для умягчения воды и сливной клапан (26), и что поток жидкости в первичном контуре является регулируемым с помощью клапана (20).2. Устройство по п.1, отличающееся тем, что камера (21) очистки имеет емкостные и/или электромагнитные устройства.3. Устройство по п.1, отличающееся тем, что объем в первичном контуре выполнен с возможностью промывки по типу подтопления путем открывания клапанов (20, 26).4. Устройство по п.1, отличающееся тем, что часть потока первичного ...

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23-01-2023 дата публикации

СПОСОБ ПОЛУЧЕНИЯ МЕТАВОЛЬФРАМАТА АММОНИЯ

Номер: RU2788598C2

Изобретение может быть использовано в химической промышленности. Для получения концентрированного раствора метавольфрамата аммония (МВА) водный раствор метавольфрамата аммония направляют по меньшей мере через одну обратноосмотическую ячейку с получением концентрата и пермеата. Обратный осмос выполняют в высоконапорной обратноосмотической ячейке при давлении более 90 бар, способ осуществляют непрерывно. Предложены также применение высоконапорной обратноосмотической ячейки и устройство для получения концентрированного раствора МВА. Изобретения позволяют снизить расход энергии при концентрировании МВА. 3 н. и 11 з.п. ф-лы, 1 ил., 1 пр.

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22-07-1993 дата публикации

Conditioning of rinse water from chemical and/or electrolytic surface treatment - includes passing rinse water from 1st tank of multistage rinse to electrodialysis unit and concentrate to treatment bath via selective ion exchanger and/or evaporator

Номер: DE0004200849A1
Принадлежит:

Conditioning process for rinse water from chemical and/or electrolytic surface treatment of metals, in which fresh rinse water in introduced to the last rinse tank of a multi-stage rinse, returned successively via individual rinse tanks to the first rinse tank and drawn off for cleaning there. The rinse water drawn off is passed through at least one filter to an electrodialysis unit for concentration, the resulting diluate is passed to the last and/or second last rinse tank and the concentrate is returned to the treatment bath via a selective ion exchanger and/or evaporator. Process equipment is also claimed. USE/ADVANTAGE - Used for conditioning rinse water from chemical and/or electrolytic surface treatment processes for metals, the recovery of carry-over and recirculation of rinse water. The process also removes extraneous ions from the rinse water and ensures environmentally sound preparation of treatment soln. and rinse water ...

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14-08-2013 дата публикации

Treating process water obtained from a hydrothermal carbonization process, comprises supplying the process water charged with working pressure into membrane, which divides process water into permeate emerging through membrane, and retentate

Номер: DE102012002590A1
Принадлежит:

Treating process water (5) obtained from a hydrothermal carbonization (HTC) process (1), comprises supplying the process water charged with working pressure into a membrane, which divides the process water into a permeate (7) emerging through the membrane, and a retentate (6) that is retained from the membrane, where the retentate is supplied again to the HTC process.

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08-07-2004 дата публикации

Sea water desalination plant operated by liquid nitrogen, has evaporator pressurizing reverse osmosis unit and employs liberated gas to drive control equipment and liquids

Номер: DE202004003175U1
Автор:
Принадлежит: SCHMID HEINRICH, SCHMID, HEINRICH

The liquid nitrogen (4) tank (1) feeds the evaporator unit (5), producing nitrogen gas (3) under pressure. This applies pressure to sea water (8) in the sea water tank (12) of the reverse osmosis unit (9). The sea water is forced through a membrane. Heat exchange with the sea water takes place in the evaporator. Constant evaporation of liquid nitrogen displaces sea water from the tank (12), filling it with nitrogen. The nitrogen gas under pressure, is then removed from the sea water tank by a pressure line (7) and stored as an energy source in the buffer tank (11). It is used to supply control equipment (10, 14). It is also be used for pressurization and transport of sea- and potable water (16). Wind-, solar-, water- or magnetic motor energy drives an associated air liquefaction plant to make liquid air and/or nitrogen. This is then used to make potable water autonomously, as described. Other liquefied gases may be used. The plant is static or mobile. A remote upright or horizontal tank ...

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21-09-2017 дата публикации

Modulares Verfahren und Abwasserbehandlungsanordnung zur effizienten Reinigung von Abwasser, insbesondere von unterschiedlich belasteten Industrieabwässern

Номер: DE102016105071A1
Принадлежит:

Die Erfindung betrifft eine Abwasserbehandlungsanordnung zur effizienten Reinigung von unterschiedlich belasteten Abwasserteilströmen (20, 21, 22, 23, 24), insbesondere von Industrieabwässern, gekennzeichnet durch die folgenden Kompenenten – Eine Elektrodialyseeinheit (1) – Einen Havariespeicher (9), – Einen Pufferbehälter (2), wobei – der Pufferbehälter (2) von Abwasserteilströmen (22, 23, 24) indirekt über die Elektrodialyseeinheit (1) und/oder direkt erreichbar ausgebildet ist und dass – • der Pufferbehälter (2) von den Abwasserteilströmen (20, 21) indirekt über den Havariespeicher (9) und/oder direkt erreichbar ausgebildet ist und dass – • Nach dem Pufferbehälter (2) ein erster Flotationsbehälter (11), ein Anaerobreaktor (14) und eine SBR-Einheit (17) vor dem Ablauf (19) in Reihe geschaltet angeordnet sind.

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29-11-2012 дата публикации

Transportable Wasserreinigungsvorrichtung

Номер: DE202012009129U1
Автор:
Принадлежит: DULGER VIKTOR, DULGER, VIKTOR

Transportable Wasserreinigungsvorrichtung, das als Einzelstandgerät für den Haushalt, mit einer Filtund Verunreinigungen mindestens bis zu einer Größe von Bakterien aufzuhalten ausgestattet ist und wobei das zu reinigende Wasser mittels einer elektrisch betriebenen Membranpumpe aus einem Behälter (Reservoir), der im Bodenteil des Standgerätes angeordnet ist, angesaugt und mit mindestens einem bar durch die Filtereinrichtung gedrückt wird und das gereinigte Wasser (Permeat) in einem Behälter aufgefangen wird und der andere Teil des Wassers (Konzentrat) zurückgeführt wird, dadurch gekennzeichnet, dass im Bodenteil (1) des Standgerätes als Reservoir ein schubladenartiger, herausziehbarer Behälter (7) angeordnet ist, der dazu dient sowohl das zu reinigende Wasser als auch das zurückzuführende Konzentrat aufzunehmen und der Membranpumpenantrieb bei Erreichen eines vorgegebenen Druckes in der Zuführungsleitung und/oder beim Anstieg der Leitfähigkeit des der Filtereinrichtung (15) zugeführten ...

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29-06-1989 дата публикации

WASTE TREATMENT METHOD AND DEVICE

Номер: DE0003570427D1
Принадлежит: AXELROD BURTON, AXELROD, BURTON

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30-04-2020 дата публикации

GLATTE POLYMERMEMBRANEN UND ELEKTROSPRAYDRUCKVERFAHREN ZU DEREN HERSTELLUNG

Номер: DE112018003852T5
Принадлежит: CHOWDHURY MAQSUD R, Chowdhury, Maqsud R.

Ein Verfahren zur Herstellung einer Polymermembran, das Verfahren enthaltend Bereitstellen einer ersten Monomerlösung mit einem ersten Lösemittel, einer zweiten Monomerlösung mit einem zweiten Lösemittel, und eines Substrats mit einer Oberfläche, und enthaltend Elektrosprühen der ersten Monomerlösung auf die Substratfläche und Elektrosprühen der zweiten Monomerlösung auf die Substratfläche zur Bildung der Polymermembran auf mindestens einem Teil der Substratfläche.

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06-05-1970 дата публикации

Vorrichtung zum Durchfuehren einer umgekehrten Osmose

Номер: DE0001953417A1
Принадлежит:

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19-11-2015 дата публикации

Wasseraufbereitungsverfahren

Номер: DE102010043711B4
Принадлежит: EUMANN MICHAEL, EUMANN, MICHAEL

Wasseraufbereitungsverfahren, bei dem Betriebswasser mittels einer Umkehrosmose aus Rohwasser gewonnen wird, wobei das Rohwasser vor einem ersten Umkehrosmoseschritt mit einem zweiten Fällungsmittel versetzt und nachfolgend ein bei dieser Fällungsreaktion entstandenes Fällungsprodukt abgetrennt wird, wobei aus dem so behandelten Rohwasser bei dem ersten Umkehrosmoseschritt Betriebswasser gewonnen wird, wobei ein bei dem ersten Umkehrosmoseschritt anfallendes erstes Rohwasserkonzentrat nachfolgend mit einem ersten Fällungsmittel versetzt wird, wobei das Rohwasser und das erste Rohwasserkonzentrat jeweils mittels eines statischen oder dynamischen Mischers (34) mit dem jeweiligen Fällungsmittel vermischt werden, wobei ein bei den Fällungsreaktionen entstandenes Fällungsprodukt jeweils mittels einer Vorrichtung zur Membranfiltration (36, 36') abgetrennt wird und wobei ein im Wege der Fällungsreaktion aus dem ersten Rohwasserkonzentrat gebildetes zweites Rohwasserkonzentrat nachfolgend wiederum ...

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02-10-2003 дата публикации

Seawater reverse osmosis desalination process involves use of assembly raising and lowering closed loop pipe of deep sea modules and collector tanks

Номер: DE0010211788A1
Автор:
Принадлежит:

In a reverse osmosis (RO) seawater desalination process, one or more RO modules (5) and product water tanks (1) are linked, with or without a separation foil (8), and lowered into the sea. The modules and tanks are lowered to a depth of e.g. 500 to 600 mat which depth there is sufficient osmotic pressure to desalinate seawater without supplementary energy. The resulting fresh drinking water is lifted to the surface by the combined use of the anchorage (4) and movement (6) systems. The fresh water is collected for use and the empty modules and tanks returned to the depths. The RO modules and fresh water tanks are arranged in an endless, flexible pipe which is continually pulled over the mother vessel. An Independent claim is included for the process assembly.

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09-02-1995 дата публикации

Process and plant for treating salt brine

Номер: DE0004427478A1
Принадлежит:

The invention relates to a process for treating salt brine, containing common salt, resulting from the pickling of vegetables, in particular sauerkraut, which is characterised in that - in a preliminary stage, preferably immediately following the said initial stage, the particles of suspended matter, cloud (haze)-forming substances and/or fibrous materials - together with microorganisms or microorganism agglomerates adhering thereto or deposited thereon - and if appropriate high-molecular-weight organic compounds are separated and removed, for example by gravity separation, in particular by centrifugation or filtration, from the brine which is considerably diluted by the removal of water from the fresh vegetable resulting from the salt treatment, in that, if appropriate after passing through an intermediate stage with intermediate storage, intermediate purification or the like, in addition - in a main stage the salt concentration of 1-3.5% by mass, in particular 1.5-2.5% by mass, is decreased ...

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12-11-2009 дата публикации

Hybridprozess zur Meerwasserentsalzung

Номер: DE502007001619D1
Принадлежит: CHMIEL HORST, CHMIEL, HORST

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20-06-1996 дата публикации

Anaerobic digestion of organic material

Номер: DE0004444462A1
Автор: NICHTNENNUNG
Принадлежит:

Anaerobic digestion of degradable organic material is effected in a single 2-stage reactor equipped for controlled recycle of water drained from the reactor ...

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28-08-2003 дата публикации

Distribution unit for the permeate from a reverse osmosis membrane, for the supply of purest water to a dialysis apparatus, has a secondary ring channel at the primary channel, to prevent contamination

Номер: DE0020217081U1
Автор:
Принадлежит: VOELKER MANFRED, VOELKER, MANFRED

The supply system for the delivery of the purest water to a dialysis apparatus, together with a reverse osmosis unit, has at least one secondary ring channel with its upstream section (5) concentric within the primary channel (1) to distribute the permeate from the reverse osmosis membrane. The secondary ring channel has a connection section outside the primary channel, and its downstream end (8) opens into the primary channel. The upstream section of the secondary ring channel is a straight section, from the curve (4) of the primary channel between its two straight and parallel sections (3), which can contain a throttle (10).

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26-11-1998 дата публикации

Wasserreinigungsvorrichtung mit Abwasserwiedergewinnungsfunktion

Номер: DE0029814561U1
Автор:

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25-04-2013 дата публикации

Verfahren und Vorrichtung zur Aufbereitung von anfallendem Abwasser einer Entsalzungsanlage

Номер: DE102011116699A1
Принадлежит:

Verfahren und Vorrichtung zur Aufbereitung von anfallendem Abwasser einer Entsalzungsanlage, indem ein wirtschaftliches Gefrierverfahren eingesetzt wird zur Gewinnung von reinem Wasser, ohne chemische Vor- und Nachbehandlung, wobei die anfallende Wärme zur Vorkühlung des anfallenden Abwassers genutzt und somit ein effizientes und wirtschaftliches Verfahren dargestellt wird.

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30-10-1975 дата публикации

Номер: DE0002046064B2

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10-06-2014 дата публикации

Rückverkeimungs-Schutz-System für Osmose-Anlagen

Номер: DE202014003627U1
Автор:
Принадлежит: SHANNON HARRY, SHANNON, HARRY

Rückverkeimungs-Schutz-System für Osmose-Anlagen bestehend aus einem Rückschlagventil sowie einem angeschlossenem Gehäuse, welches mit Silber oder silberhaltigen Produkten als Gewebe, Folien, Pulver, Gestrick oder gewickelten Silberdraht gefüllt ist und somit eine Durchkeimung in Richtung Osmose-Anlage verhindert, ohne den Wasserdruck oder die Fließgeschwindigkeit maßgeblich zu verändern.

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17-11-2005 дата публикации

WASSERBEHANDLUNGSVERFAHREN

Номер: DE0069828821T2

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13-10-2011 дата публикации

Obtaining drinking water from sea water, comprises carrying out reverse osmosis by osmosis, in which the high pressure of the sea water required for reverse osmosis is provided by a osmosis process

Номер: DE102010014464A1
Принадлежит:

Obtaining drinking water from sea water, comprises carrying out reverse osmosis by osmosis, in which the high pressure of the sea water required for reverse osmosis is provided by a osmosis process, in which the salt solutions with correspondingly different concentrations are separated through a membrane into the concentrated solution, and the required pressure is produced, which is then transferred using a pressure exchanger to a sea water stream (1), and sea water stream is then subjected to reverse osmosis for the actual water production. The process gets along without fossil fuel energy.

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10-07-2008 дата публикации

REINWASSERPRODUKTIONSSYSTEM

Номер: DE602004014144D1

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10-10-2007 дата публикации

Process

Номер: GB0000717102D0
Автор:
Принадлежит:

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03-11-1971 дата публикации

Номер: GB0001251825A
Автор:
Принадлежит:

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01-10-1975 дата публикации

WASHING APPARATUS

Номер: GB0001407894A
Автор:
Принадлежит:

... 1407894 Washing and rinsing system L E NEWENS 27 June 1973 30470/73 Heading C1C [Also in Division B7] Apparatus for washing vehicles includes a washing and rinsing means and a reclaiming means for reclaiming wash and rinse water; used wash water receiving means (10b and 10c) for receiving wash water draining from the surface of the vehicle being washed; sludge separating means (18) for separating sludge from the used wash water; conveying means (20) operable to convey used wash water from said receiving means to said sludge separating means; a storage area (10a) operable to receive and hold used wash water after separation of sludge; conveying means (12 and 14) operable to convey wash water from said storage area to the washing means (16) in the wash operation; used rinse water receiving means (30b and 30c) for receiving rinse water draining from the surface of the vehicle being rinsed; used rinse water filtering means (40 and 46); conveying means (38, 42 and 44) operable to convey used ...

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06-09-1989 дата публикации

TREATMENT FOR REDUCING IMPURITIES IN AQUEOUS LIQUOR

Номер: GB0008916486D0
Автор:
Принадлежит:

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16-05-2012 дата публикации

Steam plant and method of operating the same

Номер: GB0201205630D0
Автор:
Принадлежит:

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23-09-2015 дата публикации

Water treatment systems,devices and methods for fluid preparation

Номер: GB0201514184D0
Автор:
Принадлежит:

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11-05-1994 дата публикации

Method of production of a beverage for human consumption

Номер: GB0002272214A
Принадлежит:

A process for the manufacture of a beverage for human consumption having beneficial effects relating to countering the effects of oxygen depletion in the human body, and the beverage produced by the process, which includes the steps of conditioning potable water to remove hardness, filtering the water to remove inorganic and organic matter, ozonating the water to purify it and to increase the level of dissolved oxygen in the water to at least 6 mg/l, adding potassium gluconate and immediately sealing within a container.

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29-11-2000 дата публикации

Treatment of water

Номер: GB0002335153B

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18-06-2008 дата публикации

Device and methods for the desalination of brackish water

Номер: GB0002444709A
Принадлежит:

The device comprises a reverse osmosis cell 12 containing a semi-permeable membrane 14, an outlet 16 for the desalinated water 18, and an inlet 20 for the brackish water 10. The inlet is an open inlet leading directly to said membrane, that is without the use of a pump. A method of desalinating sea water for use on board a moving sea-going vessel comprises the use of the device, the inlet of said device being positioned towards the direction of movement of said vessel wherein the relative movement of the water past the vessel provides the necessary pressure to drive the reverse osmosis. Further, the relative movement may be provided by seawater under tidal flow or river water. With no moving parts or pump, the device is simpler to construct and less prone to breakdown.

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30-01-2013 дата публикации

Cooling process

Номер: GB0201222999D0
Автор:
Принадлежит:

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07-09-1994 дата публикации

Method of treating cooling tower water

Номер: GB0009414736D0
Автор:
Принадлежит:

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22-10-1997 дата публикации

Water purifier with means for determining filtering efficiency

Номер: GB0002312176A
Принадлежит:

A water purifier 20 comprises replaceable filters 27, 29, 31 through which water is fed from a pipe 25 into a storage tank 35. A first sensor (101) senses the purity of the water to be filtered, and a second sensor (102) senses the purity of the water after passage through the filters. The output signals from the sensors are compared electronically to produce a signal corresponding to the purifying efficiency of the filtering means. This is displayed by the display (170). One of the filters may be a reverse osmotic filter.

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17-06-1998 дата публикации

Modular home dialysis system - debubblers

Номер: GB0002320209A
Принадлежит:

An apparatus for removing air bubbles from blood is disclosed. The debubbler comprises front and rear covers (1002, 1008 respectively) with a fluid circuit board (1004) arranged between the two covers. A blood chamber is defined between cover (1002) and circuit board (1004) and an air chamber is defined between covers (1008) and circuit board (1004). A microporous membrane (1006) separates the blood and air chambers. A support means (1024) supports membrane (1006) from the air side of the membrane. A blood pressure sensor is provided between covers (1002, 1008). The debubbler has a blood inlet port (1022) and a blood outlet port (1020) for conducting blood to and from the blood chamber. An air port (1012) is provided in communication with the air chamber, to allow air passing through membrane (1006) to escape.

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31-12-2002 дата публикации

Water purifier

Номер: GB0002376902A
Принадлежит:

A water purifier that assures easier change of a used filter comprises a base, at least one filter replaceably attached to the base and including a first end with a first fluid port and a second end with a second fluid port, a first connector supporting the first end of the filter in a separable manner and including a connector port connected to the first fluid port of the filter, a second connector spaced apart from the first connector to accomodate the filter therebetween and including a bore aligned with the second fluid port of the filter, a spool fitted into the bore of the second connector for movement between an extended position allowing fluid flow and a contracted position preventing fluid flow, and a spool actuator for slidingly moving the spool between the extended position and the contracted position.

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02-10-2013 дата публикации

Steam plant with reverse osmosis unit

Номер: GB0002500685A
Принадлежит:

A steam plant 10 comprises a processing unit 12 arranged to treat raw water, a boiler 18 arranged to generate steam, a blowdown vessel 20 in fluid communication with the boiler so as to receive hot blowdown water from the boiler and a reverse osmosis unit 14. The reverse osmosis unit is in fluid communication with the processing unit through an inflow water line 24, with the boiler through a permeate line 60 and with the processing unit 12 and/or the blowdown vessel 20 through a concentrate line 74, 76, 78, 80, 82. In use, the reverse osmosis unit receives treated inflow water from the processing unit and generates permeate which is provided to the boiler through the permeate line and concentrate which is provided to the processing unit and/or the blowdown vessel through a concentrate line. Preferably, the processing unit comprises a softener vessel 30, 32 and a brine tank 34. There is also disclosed a method of operating a steam plant and a method of upgrading an existing steam plant.

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20-12-2006 дата публикации

Thermal desalination plant integrated upgrading process and apparatus

Номер: GB0000622329D0
Автор:
Принадлежит:

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14-03-2007 дата публикации

Method of treating liquid waste

Номер: GB0000702157D0
Автор:
Принадлежит:

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27-06-2018 дата публикации

Membrane cleaning method and apparatus

Номер: GB0002557610A
Принадлежит:

A method and system for cleaning a semi-permeable membrane (3) in a pressure vessel (2) preferably of a desalination plant. The membrane having a feed side (FS) and an opposite permeate side (PS) and extending between a front end and a rear end of the vessel. The vessel has a front end feed port (12) and a rear-end brine port (14) in communication with the feed side of the membrane. At least one permeate port (16, 17) is in communication with the permeate side of the membrane. In a normal separation process through the membrane feed water passes from the feed side to the permeate side to provide residual brine water (BS) from the rear-end brine port and a permeate water from the permeate port. In a cleaning process a washing water is delivered from an external source to the permeate side under higher pressure than the permeate pressure during the normal separation process. The higher permeate pressure causing a change in a net driving differential pressure across the membrane to cause a ...

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16-12-2009 дата публикации

Thermal desalination

Номер: GB0000918916D0
Автор:
Принадлежит:

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19-05-2021 дата публикации

A water desalination process

Номер: GB0002588953A
Принадлежит:

A water desalination process comprises the steps of submerging, in saltwater, a container 3 having a charging inlet 5 covered by a reverse osmosis (RO) membrane 7 to a filling depth where the water pressure external the container adjacent the RO membrane exceeds the osmotic pressure of the RO membrane, preferably wherein the filling depth is at least 270m; filling the container with permeate water and harvesting the permeate water from the interior of the container. The permeate harvesting may involve raising the container from the filling depth such that at least part of the container is above the saltwater surface. In this instance, the permeate can be harvested sequentially from a series of discharge outlets which are spaced apart along the height of the container. Alternatively, the permeate harvesting may involve pumping the water from the submerged container. The submerging can comprise driving the container downwards along a guide assembly 11 comprising a pulley 15, a cable 13 led ...

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04-11-2015 дата публикации

Water desalination system

Номер: GB0002525632A
Принадлежит:

A water desalination system comprises: a pump 05 powered by renewable energy and in fluid communication with a water source 06; a reverse osmosis membrane unit 16 in fluid communication with the pump; an energy recovery device 14 disposed between the pump and reverse osmosis unit which intensifies the feed pressure to the reverse osmosis unit; and a water storage unit 10 in fluid communication with the pump and reverse osmosis unit. The water storage unit is at a greater elevation than one or both of the energy recovery device and the reverse osmosis unit. When renewable energy is available, for example solar irradiance, water may be pumped towards T-splitter 8 so that a portion of the water is pumped towards the reverse osmosis unit and the remaining portion of water is pumped to the water storage unit. When no renewable energy is available, the pump is no longer powered and water may flow towards the reverse osmosis unit from the water storage tank by gravity.

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29-11-1972 дата публикации

Номер: GB0001297650A
Автор:
Принадлежит:

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14-11-2018 дата публикации

Система очистки воды из артезианских скважин от природных радионуклидов

Номер: RU0000184928U1

Установка предназначена для очистки воды из артезианских скважин от природных радионуклидов. Содержит последовательно соединенные трубопроводной системой фильтр грубой очистки 1, аэрационный блок 2, насосную станцию второго подъема 3 и ультрафиолетовый стерилизатор 4, установленную перед аэрационным блоком установку обратного осмоса 5, разделяющую поток воды на фильтрат, аккумулирующийся в аэрационном блоке и высокоминерализованный концентрат, сбрасываемый в дренаж и комплекс 6 дозирования реагента для подачи ингибитора солеотложения на мембранных элементах, расположенный перед установкой обратного осмоса 5. При нормальном качестве исходной воды установка включает дополнительную линию 7 подмеса исходной воды, расположенную после фильтра грубой очистки 1, на выделенной отдельной трубопроводной системе, минующей установку обратного осмоса 5 и включающую регулировочный механизм 8 заполнения аэрационного блока 2. Воздух в аэрационный блок 2 нагнетается с помощью низконапорного компрессора 9. Система исключает риск возникновения аварийной остановки системы по причине формирования отложений в резервуаре, насосном оборудовании и разводящей сети. Трубопроводная система установки состоит из двух частей, последовательно соединенных через аэрационный блок. 1 ил. РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 184 928 U1 (51) МПК C02F 9/08 (2006.01) C02F 1/32 (2006.01) C02F 1/44 (2006.01) C02F 1/58 (2006.01) C02F 1/74 (2006.01) B01D 36/00 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ПОЛЕЗНОЙ МОДЕЛИ К ПАТЕНТУ (52) СПК C02F 1/325 (2006.01); C02F 1/441 (2006.01); C02F 1/58 (2006.01); C02F 1/74 (2006.01); B01D 36/00 (2006.01) (21)(22) Заявка: 2017145686, 25.12.2017 25.12.2017 (73) Патентообладатель(и): Бондарев Антон Анатольевич (RU) Дата регистрации: 14.11.2018 Приоритет(ы): (22) Дата подачи заявки: 25.12.2017 ООО "Водэко", Минск, 2016, с. 17, рис. 5, 2124, 84-88, 96-99. RU 2275337 C1, 27.04.2006. RU 2383498 C1, 10.03.2010. EP 2580168 B1, 07.05.2014. (45) ...

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08-03-2012 дата публикации

Process for the purification of an aqueous stream coming from the fischer-tropsch reaction

Номер: US20120055868A1
Принадлежит: Eni Spa

Process for the purification of an aqueous stream coming from the Fischer-Tropsch reaction which comprises: —feeding said aqueous stream containing the organic by-products of the reaction to a distillation column, obtaining two output streams: —an aqueous stream (i) exiting from the column head, enriched with alcohols having from 1 to 20 carbon atoms, preferably from 1 to 9 carbon atoms, and other optional volatile compounds; an aqueous stream (ii) exiting from the column bottom, enriched with organic acids having from 1 to 10 carbon atoms, preferably from 2 to 6 carbon atoms; —subjecting said aqueous stream (ii) to an anaerobic biological treatment obtaining a purified aqueous stream (iii); wherein said anaerobic biological treatment is carried out with a hydraulic retention time lower than 15 hours, preferably ranging from 4 hours to 10 hours, more preferably ranging from 5 hours to 8 hours.

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15-03-2012 дата публикации

Seawater desalination system and energy exchange chamber

Номер: US20120061309A1
Принадлежит: Ebara Corp

A seawater desalination system which can solve a problem of wear of a sliding member and can suppress mixing of concentrated seawater and seawater by making an energy exchange chamber no-piston configuration is provided. In a seawater desalination system for producing fresh water from seawater by passing the seawater pressurized by a pump through a reverse-osmosis membrane-separation apparatus ( 4 ) to separate the seawater into fresh water and concentrated seawater, an energy exchange chamber ( 20 ) for utilizing pressure energy of the concentrated seawater discharged from the reverse-osmosis membrane-separation apparatus ( 3 ) as energy for pressurizing part of the seawater is provided. The energy exchange chamber includes a concentrated seawater port (P 1 ) for introducing and discharging the concentrated seawater, a seawater port (P 2 ) for introducing and discharging the seawater, and a plurality of partitioned fluid passages (R) provided in the chamber to allow the concentrated seawater port (P 1 ) and the seawater port (P 2 ) to communicate with each other.

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05-04-2012 дата публикации

Ozone and anaerobic biological pretreatment for a desalination process

Номер: US20120080374A1
Принадлежит: Pacific Advanced Civil Engineering Inc

In one embodiment, a method of treating a source water containing at least one toxin is provided, the method comprising: (i) exposing a source water to a gas comprising ozone under a condition that promotes an interaction between the toxin and the ozone; and then (ii) subjecting the treated source water to a biological treatment.

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05-04-2012 дата публикации

Thin film composite membranes incorporating carbon nanotubes

Номер: US20120080380A1
Принадлежит: General Electric Co

Processes for manufacturing a thin film composite membrane comprising multi-walled carbon nanotubes include contacting under interfacial polymerization conditions an organic solution comprising a polyacid halide with an aqueous solution comprising a polyamine to form a thin film composite membrane on a surface of a porous base membrane; at least one of the organic solution and the aqueous solution further including multi-walled carbon nanotubes having an outside diameter of less than about 30 nm.

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17-05-2012 дата публикации

Water treatment apparatus and water treatment method

Номер: US20120118824A1
Принадлежит: Sumitomo Electric Industries Ltd

There is provided a water treatment apparatus, including: first membrane filtration means in which a filtration membrane having an average pore diameter of 1 μm or more is used; second membrane filtration means for treating water filtered by the first membrane filtration means, by using a microfiltration membrane or ultrafiltration membrane; and reverse osmosis membrane filtration means for treating water filtered by the second membrane filtration means. In particular, there is provided a water treatment apparatus, wherein a hydrophobic polymer membrane that is not subjected to hydrophilicizing processing is used as the filtration membrane having an average pore diameter of 1 μm or more. There is also provided a water treatment method that can be implemented by these water treatment apparatuses.

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07-06-2012 дата публикации

Use of electromagnetic pulses in cross-flow filtration systems

Номер: US20120138517A1
Автор: David W. Alley
Принадлежит: CLEARWATER SYSTEMS Corp

A cross-flow filtration system includes a first filter element having a first conduit for receiving a flow of a first aqueous feed stream, a second conduit operable to discharge a flow of first permeate water and a third conduit operable to discharge a flow of first retentate water. The cross-flow filtration system includes a coil assembly disposed about the first conduit. The first coil assembly is operable to subject the first aqueous feed stream to electromagnetic pulses. A second filter element is in fluid communication with the first filter element via the third conduit. The second filter element is operable to receive the first retentate water via the third conduit. A second coil assembly is disposed about the third conduit and is operable to subject the first retentate water to electromagnet pulses.

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21-06-2012 дата публикации

Method for Treating Water In Order to Desalinate Said Water, Including Treating Concentrates

Номер: US20120152721A1

The invention relates to a method for treating water in order to desalinate said water, including a step of reverse osmosis or distillation of said water in order to produce water that is at least partially desalinated and a first concentrate. According to the invention, said method includes: a first demineralisation step including a step of nanofiltering said first concentrate such as to produce a nanofiltrate and a second concentrate; a second step of demineralising said second concentrate by means of at least one active material including cationic and/or anionic ion-exchange resins, said second demineralisation step including the extraction of a third concentrate and the extraction of at least partially demineralised water, said at least partially demineralised water being mixed with said at least partially desalinated water; a step of regenerating said at least one active material, said regeneration step including a step of recirculating said nanofiltrate.

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28-06-2012 дата публикации

Separator assembly

Номер: US20120160758A1
Принадлежит: General Electric Co

A novel separator assembly for a spiral flow reverse osmosis apparatus is provided. In one embodiment, the separator assembly comprises a central core element comprising at least one permeate exhaust conduit and at least one concentrate exhaust conduit. Each exhaust conduit defines an exhaust channel and one or more openings allowing fluid communication between an exterior surface of the exhaust conduit and the exhaust channel, said exhaust conduits independently defining a cavity between said conduits. The cavity is configured to accommodate a first portion of a membrane stack assembly comprising at least one feed carrier layer, at least one permeate carrier layer, and at least one membrane layer. A first portion of the membrane stack assembly is disposed within the cavity, and a second portion of the membrane stack assembly is wound around the central core element and forms a multilayer membrane assembly disposed around the central core element.

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05-07-2012 дата публикации

Method of making pure salt from frac-water/wastewater

Номер: US20120171091A1
Принадлежит: FRACPURE HOLDINGS LLC

The present invention relates to a method for making pure salt comprises recapturing post-drilling flowback water from hydro-fracturing; removing oil from the flowback water; filtering the flowback water using an ultra filter with a pore size of about 0.1 microns or less to remove solid particulates and large organic molecules, such as benzene, ethylbenzene, toluene, and xylene, from the water; concentrating the flowback water to produce a brine that contains from about 15 wt % to about 40 wt % of salt relative to the total weight of the flowback brine; performing one or more chemical precipitation process using an effective amount of reagents to precipitate out the desired high quality commercial products, such as, barium sulfate, strontium carbonate, calcium carbonate; and crystallizing the chemically treated and concentrated flowback brine to produce greater than 99.5% pure salt products, such as sodium and calcium chloride.

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12-07-2012 дата публикации

Food Waste Concentration System and Related Processes

Номер: US20120174639A1
Автор: John R. Herron
Принадлежит: Individual

A forward osmosis system and process for producing fertilizer and recycling water from a food waste methane digester wastewater stream. The process includes: forming a residual wastewater stream from food waste using digesters; coarse filtering the residual wastewater stream; acid treating the filtered, residual wastewater stream so that ammonium is retained therein; diverting the acid treated, filtered, residual wastewater stream to one side of at least one forward osmosis membrane; and concentrating the acid treated, filtered, residual wastewater stream to form fertilizer by contacting a saturated salt brine in a forward osmosis draw loop to an opposite side of the at least one forward osmosis membrane and osmotically pulling water across the at least one forward osmosis membrane from the acid treated, filtered, residual wastewater stream to the saturated salt brine, thereby diluting the saturated salt brine.

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06-09-2012 дата публикации

Method for recovering a boron adsorbent

Номер: US20120225957A1
Принадлежит: Toshiba Corp

The present embodiment relates to a method for recovering a boron adsorbent, including: preparing water having an electric resistivity of 0.01 MΩ·cm or more and kept at a temperature within a temperature range; and contacting the water with the boron adsorbent to release boron adsorbed at the boron adsorbent.

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04-10-2012 дата публикации

Curable Compositions And Membranes

Номер: US20120248029A1
Принадлежит: FUJIFILM MANUFACTURING EUROPE BV

A curable composition comprising: (i) 2.5 to 50 wt % crosslinker comprising at least two acrylamide groups; (ii)12 to 65 wt % curable ionic compound comprising an ethylenically unsaturated group and a cationic group; (iii) 10 to 70 wt % solvent; (iv) 0 to 10 wt % of free radical initiator; and (v) lithium and/or calcium salt. The compositions are useful for preparing ion exchange membranes.

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04-10-2012 дата публикации

Curable Compositions And Membranes

Номер: US20120248030A1
Принадлежит: FUJIFILM MANUFACTURING EUROPE BV

A curable composition comprising: (i) 2.5 to 50 wt % crosslinker comprising at least two acrylamide groups; (ii) 12 to 65 wt % curable ionic compound comprising an ethylenically unsaturated group and a cationic group; (iii) 15 to 70 wt % solvent; and (iv) 0 to 10 wt % of free radical initiator; and (v) 2 to 50 wt % of non-curable salt; wherein the composition has a pH of 1 to 12. The compositions are useful for preparing ion exchange membranes.

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25-10-2012 дата публикации

Osmotic separation systems and methods

Номер: US20120267307A1
Автор: Robert L. Mcginnis
Принадлежит: Individual

Separation processes using osmotically driven membrane systems are disclosed generally involving the extraction of solvent from a first solution to concentrate solute by using a second concentrated solution to draw the solvent from the first solution across a semi-permeable membrane. Enhanced efficiency may result from using low grade waste heat from industrial or commercial sources. Pre-treatment and post-treatment may also enhance the osmotically driven membrane processes.

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25-10-2012 дата публикации

Recovery of retrograde soluble solute for forward osmosis water treatment

Номер: US20120267308A1
Принадлежит: Trevi Systems Inc

Improved systems and processes for forward osmosis water purification or desalination are herein disclosed. According to one embodiment a process for purifying contaminated water is provided wherein a contaminated feed solution stream comprising water and with a first osmotic pressure is passed through a semipermeable membrane to a draw side having a draw solution stream with a second osmotic pressure on a draw side of the semipermeable membrane. The diluted draw solution stream is heated, agglomerated and cooled to produce a cooled single phase water rich stream that is purified to produce a water product stream.

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08-11-2012 дата публикации

Continuous process batch-operated reverse osmosis system with in-tank membranes and circulation

Номер: US20120279923A1
Автор: Eli Oklejas, Jr.
Принадлежит: Fluid Equipment Development Co LLC

A reverse osmosis system and method for operating the same includes a pressure tank having a first end and a second end, the pressure tank has a first volume adjacent to the first end and a second volume adjacent to the second end and a third volume between the first volume and the second volume and a fluid passage fluidically coupling the second volume to the first volume. The reverse osmosis system also includes a plurality of membranes disposed within the third volume generating permeate and a permeate manifold receiving permeate from the membranes and fluidically communicating permeate out of the pressure tank. A feed line couples feed fluid into the pressure tank. A first pump pressurizes the feed line. A second pump is disposed within the tank and circulates brine fluid from the second volume through the fluid passage.

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29-11-2012 дата публикации

Systems and methods for filtration

Номер: US20120298578A1
Принадлежит: Individual

Filtration systems ( 40 ) utilize a pre-treatment method to cause scale formation to occur on particles ( 94 ) in the fluid stream ( 96 ) rather than on the filter surface and may also destroy microorganisms in the fluid stream. More specifically, but not limited to, a filtration device can be a filtration membrane, such as spiral wound filtration membrane ( 60 ), that utilizes an open feed spacer ( 80 ), such for example an embossed or printed pattern on the membrane, to create a thin feed spacer channel which replaces a conventional feed spacer mesh material. System ( 40 ) further utilizes a treatment device ( 54 ) to enable a pulsed power, magnetic, electro-magnetic, electro-static, or hydrodynamic fluid treatment scheme to condition particles in the fluid stream ( 96 ) such that scale forming elements precipitate ( 94 ) on to the particles in the fluid stream rather than on the filtration surfaces.

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06-12-2012 дата публикации

Water producing system

Номер: US20120305459A1
Принадлежит: TORAY INDUSTRIES INC

A water producing system is provided that produces fresh water by treating treatment target water A at a first semipermeable membrane treatment plant, that mixes concentrate resulted by the treatment carried out at the first semipermeable membrane treatment plant with treatment target water B, and that treats the mixed water at a second semipermeable membrane treatment plant to produce fresh water. A bypass line allows the treatment target water A to be mixed with the treatment target water B or the concentrate while bypassing the first semipermeable membrane treatment plant, so that the second semipermeable membrane treatment plant can operate even when any trouble occurs at the first semipermeable membrane treatment plant and treatment cannot be carried out thereby.

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31-01-2013 дата публикации

Water treatment system

Номер: US20130026083A1
Принадлежит: Miura Co Ltd

According to one embodiment, a water treatment system includes: a membrane separation device and a water softening device including a valve unit switching between a softening process in which soft water is obtained by passing raw water through a cation exchange resin bed downward and a regeneration process in which a whole of the cation exchange resin bed is regenerated by generating an opposite flow of a regenerant by supplying the regenerant from both sides of a top portion and a bottom portion of the cation exchange resin bed and collecting a liquid at an intermediate portion of the cation exchange resin bed, and a regenerant supply supplying the regenerant in a volume which gives a regeneration level of 1 to 6 eq/L-R, to a hardness leakage prevention region set in a predetermined depth on the bottom portion of the cation exchange resin bed, in the regeneration process.

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31-01-2013 дата публикации

Spiral wound element and seal assembly

Номер: US20130026090A1
Принадлежит: Dow Global Technologies LLC

A spiral wound element and a seal assembly comprising: a ring-shaped seal disposed about a portion of an outer periphery of the element, a secondary pathway and a valve that selectively permits fluid flow through the secondary pathway.

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07-02-2013 дата публикации

Integrated membrane system for distributed water treatment

Номер: US20130032533A1
Принадлежит: ENVEERA Inc

Integrated membrane treatment systems for treatment of an aqueous solution. In embodiments, components, such as an MBR, are integrated with means to recover energy from the system, for example from an RO concentrate, to operate the other components. In embodiments including biological treatment, RO is integrated with other components, such as an MBR with the ROs ability to remove inorganic nitrogen enabling biological treatment to be performed with only partial nitrification and the MBR operated without active pH control. In embodiments, RO is integrated with a chlorine generator to convert chlorides present in the RO concentrate for an in-situ source of oxidizing biocides for disinfection purposes. Chloramines may be generated in-situ from residual ammonia and chlorides in the RO reject. In embodiments, carrier media is employed in a membrane tank to enhance removal of residual organics by the MBR and to also improve effectiveness of membrane scouring.

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04-04-2013 дата публикации

Fresh Water Generating Apparatus and Fresh Water Generating Method

Номер: US20130082001A1
Принадлежит: Kobelco Eco Solutions Co Ltd

An object of the present invention is to provide a fresh water generating apparatus that is capable of efficiently producing fresh water according to an intended use, while utilizing wastewater. Provided is a fresh water generating apparatus equipped with a seawater-treating reverse osmosis membrane device that produces fresh water from seawater by a reverse osmosis membrane, which includes: a mixing section that mixes wastewater as dilution water with a portion of seawater to be subjected to membrane treatment to produce mixed water; a first seawater-treating reverse osmosis membrane device that acts as the seawater-treating reverse osmosis membrane device to filter the mixed water; and a second seawater-treating reverse osmosis membrane device that acts as the seawater-treating reverse osmosis membrane device to filter the remaining portion of the seawater to be subjected to membrane treatment, in an unmixed state with the dilution water.

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02-05-2013 дата публикации

Static pressure desalination assembly

Номер: US20130105394A1
Автор: Garry R. Whyte
Принадлежит: OCEAN ARTESIA LLC

A desalination device that uses the natural and constant static pressure of the ocean depths to cause seawater to push against a reverse osmosis membrane with sufficient force to separate the molecules of water and salt. The resulting water, the permeate, is pumped to the surface using normal subsurface pumps.

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23-05-2013 дата публикации

Systems, Apparatus, and Methods for a Water Purification System

Номер: US20130126430A1
Принадлежит: DEKA Products Limited Partnership

A water purification system comprising a cross-flow filter is arranged to permit recirculation of the retentate or reject water from the retentate outlet of the filter to the inlet of the filter. A first pump is configured to pump source water into the feed water path of the filter, and to raise the fluid pressure in the feed water path and recirculation path. A second pump is configured to recirculate water from the retentate outlet of the filter to the inlet of the filter at a flow rate substantially higher than the flow rate of water generated by the first pump. A drain path connected to the recirculation path or feed water path may include a flow restrictor to permit removal of highly concentrated reject water while maintaining a minimum fluid pressure within the recirculation flowpath. 1. A water purification apparatus comprising:a feed water conduit configured to fluidly connect a source of water to an inlet of a cross-flow filter;a first pump fluidly connected to the feed water conduit and configured to pump source water to the inlet of the cross-flow filter;a recirculation conduit configured to recirculate water from a retentate outlet of the cross-flow filter to the inlet of the cross-flow filter; anda second pump fluidly connected to the recirculation conduit and configured to recirculate water from the retentate outlet to the inlet of the cross-flow filter, whereinthe first pump is configured to raise the water pressure between the source of water and the feed water conduit or the recirculation conduit, and the second pump is configured to pump water in the recirculation conduit at a flow rate greater than a flow rate generated by the first pump.2. The water purification apparatus of claim 1 , further comprising a drain conduit fluidly connected to the feed water conduit or the recirculation conduit and configured to remove water from the feed water conduit or the recirculation conduit claim 1 , the drain conduit including a flow restrictor configured to ...

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06-06-2013 дата публикации

FRESH WATER PRODUCING APPARATUS AND METHOD FOR OPERATING SAME

Номер: US20130140233A1
Принадлежит:

A fresh water producing apparatus for producing fresh water from raw water containing solutes is disclosed. The fresh water producing apparatus comprises a first semipermeable membrane unit and a second semipermeable membrane unit. A first raw water supply line for supplying the raw water is connected to the first semipermeable membrane unit. A second raw water supply line for supplying the raw water is connected to the second semipermeable membrane unit. The first semipermeable membrane unit and the second semipermeable membrane unit are connected by a concentrated water line for supplying concentrated water of the first semipermeable membrane unit to the second semipermeable membrane unit. 1. A fresh water producing apparatus to produce fresh water from solute-containing raw water which comprises a first semipermeable membrane unit and a second semipermeable membrane unit , wherein a first raw water feed line for feeding raw water is connected to the first semipermeable membrane unit , while a second raw water feed line for feeding raw water is connected to the second semipermeable membrane unit , and wherein the first semipermeable membrane unit and the second semipermeable membrane unit are connected together with a concentrated water line that feeds concentrated water from the first semipermeable membrane unit to the second semipermeable membrane unit.2. The fresh water producing apparatus according to claim 1 , wherein the raw water to be fed to the first raw water feed line and the second raw water feed line is a mixture of at least two types of raw water having different compositions.3. The fresh water producing apparatus according to claim 1 , wherein a booster pump or a non-powered pressurization unit is provided at a position in the second raw water feed line located midway between a merger point of the second raw water feed line connected to the second semipermeable membrane unit and the concentrated water line attached to the first semipermeable ...

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06-06-2013 дата публикации

DESALINATION SYSTEM

Номер: US20130140235A1
Автор: Voutchkov Nikolay
Принадлежит:

The invention provides methods and an apparatus for more efficiently and economically producing purified water from sea water or some other salty or brackish water source. The efficiency is derived from the co-location with a power plant or other thermal generating source that will heat the feed water. Reverse osmosis membrane filtration systems work optimally when the feed water is at certain higher temperature, where that temperature is typically higher than the feed water at ambient temperatures. By using the heated sea water as the byproduct of the power plant electricity generating process and if necessary mixing it with ambient temperature sea water, if needed to lower the water temperature, and using this feed water with a higher temperature than ambient water temperature, the efficiency of the reverse osmosis system can be increased. 117-. (canceled)18. A method of desalinating salty water at a desalination plant located in proximity to an electricity generating power plant , the electricity generating power plant having a salty water intake , the salty water intake being coupled to a source of salty water and to the electricity generating power plant , the salty water intake being configured for providing salty water to the electricity generating power plant for cooling power generating equipment in the electricity generating power plant , the method comprising the steps of:coupling a feed water line to the salty water intake of the electricity generating power plant;coupling the feed water line to the desalination plant;receiving a first portion of salty feed water at the desalination plant through the feed water line; anddesalinating at least part of the first portion of the salty feed water at the desalination plant to produce a condensate having a higher salt concentration than that of the first portion of salty feed water and a permeate having a lower salt concentration that that of the first portion of salty feed water.19. The method of claim 18 , ...

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06-06-2013 дата публикации

Hollow fiber type reverse osmosis membrane and method for manufacturing the same

Номер: US20130140236A1
Принадлежит: Toyobo Co Ltd

A hollow fiber type reverse osmosis membrane including cellulose acetate, characterized in that the filtration rate and the salt rejection rate when an aqueous solution having sodium chloride concentration of 1,500 mg/L is filtered from outer side to inner side of the hollow fiber type reverse osmosis membrane at 25° C. and 1.5 MPa pressure are 180 to 350 L/m 2 /day and 90.0 to 99.0%, respectively and the outer diameter, the inner diameter and the hollow rate of the hollow fiber type reverse osmosis membrane are 100 to 280 μm, 50 to 200 μm and 24 to 42%, respectively. The hollow fiber type reverse osmosis membrane preferably has a dense layer near the outer surface, and thickness of the dense layer is 0.1 to 7 μm.

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13-06-2013 дата публикации

FLUID PURIFICATION METHODS, DEVICES, AND SYSTEMS

Номер: US20130146541A1
Принадлежит: NXSTAGE MEDICAL, INC.

A fluid purification system has cells whose purifying capability can be regenerated. Some of the cells are arranged in series to reach a high level of purification. An automatic valve network is controlled to cycle the cells in a way that levels the loads on each, thereby maximizing the service interval for replacing expired cells, enabling all of the cells to be replaced at the same time after having each contributing approximately equally to the purification load, and operated such that at any one time, at least one cell is regenerated so as to enable continuous up-time. 132-. (canceled)33. An installation for a fluid purification system that is operable after the attachment of cells adapted for purifying fluid , comprising:a fluid transport network with fluid channels, a controller, and valves operable by the controller;the fluid transport network including cell connectors adapted to receive cells adapted for purifying fluid and to direct forward and reverse flows through connected cells;the fluid transport network having connections for source fluid, purified product fluid, and waste fluid;the fluid transport network and controller being configured such that the controller operates the valves so that, at a first time, fluid is directed from the source through connected first cells in a forward direction, in series, such that multiple purifications stages are defined, the first cells forming a series with a first series cell being in a first position of the series and receiving the source fluid, a last series cell being in a last position of the series outputting product fluid, and intermediate series cells;the fluid transport network and controller being configured such that the controller operates the valves so that at said first time, fluid is directed in a reverse direction through a connected second cell whereby simultaneous multi-stage purification and cell regeneration may be achieved;the fluid transport network and controller being configured to operate ...

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18-07-2013 дата публикации

Positive Displacement Energy Recovery Systems and Methods

Номер: US20130180921A1
Автор: Chancellor Dennis
Принадлежит: WORLD WIDE WATER SOLUTIONS

The inventive subject matter provides apparatus, systems and methods in which a feed fluid entering a filtration system is mixed with a portion of a reject fluid. The re-introduced reject fluid is preferably pressurized using a positive displacement pump, and more preferably using a work exchange pump having a translatable piston. The re-introduced reject fluid is preferably pressurized to within 10 psi, or more preferably to within 5 psi, of the uncombined feed fluid. The filtration system can have one or more filters. 1. A filtration system , comprising:a pump configured to pressurize a feed fluid to produce a first pressurized feed fluid stream;a first filter configured to receive the first pressurized feed fluid stream, and produce therefrom a permeate stream and a reject stream;a work exchange energy recovery unit fluidly coupled to the first filter, configured to pressurize a portion of the reject stream to produce a second pressurized feed fluid stream; andwherein the second pressurized feed fluid stream is mixed with the first pressurized feed fluid stream upstream of the first filter.2. The filtration system of claim 1 , wherein the energy recovery unit comprises a positive displacement pump.3. The filtration system of claim 1 , wherein the positive displacement pump comprises a cylinder having a translatable piston.4. The filtration system of claim 1 , wherein the positive displacement pump is configured to pressurize the second pressurized feed fluid stream to a pressure within 10 psi of the a pressure of the first pressurized feed fluid stream entering the first filter.5. The filtration system of claim 1 , wherein the positive displacement pump is configured to pressurize the second pressurized feed fluid stream to a pressure within 5 psi of the a pressure of the first pressurized feed fluid stream entering the first filter.6. The filtration system of claim 1 , further comprising a second filter downstream of the first filter claim 1 , fluidly ...

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25-07-2013 дата публикации

Low energy forward osmosis membrane water processing system

Номер: US20130186822A1
Принадлежит: HYDRATION SYSTEMS LLC

Described herein are systems and processes employing a low energy forward osmosis membrane water processing system to simultaneously (1) detoxify reverse osmosis (RO) residual (reject) brines from ground water treatment, and (2) expand available industrial and agricultural ground water supplies.

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25-07-2013 дата публикации

METHOD FOR HIGH EFFICIENCY REVERSE OSMOSIS OPERATION

Номер: US20130186825A1
Автор: MUKHOPADHYAY DEBASISH
Принадлежит:

A process for treatment of water. Hardness and non-hydroxide alkalinity are removed from feedwaters to an extent sufficient to avoid scaling when concentrated. Sparingly ionizable components in the feedwater are urged toward increased ionization by increasing the pH of the feedwater. In this manner, species such as silica become highly ionized, and (a) their rejection by membranes used in the process is significantly increased, and (b) their solubility in the reject stream from the membrane process is significantly increased. Sparingly ionized species such as boron, silica, and TOC are highly rejected. Recovery ratios of ninety percent (90%) or higher are achievable with many feedwaters, while simultaneously achieving a substantial reduction in cleaning frequency of membranes used in the process. 1. A process for treatment of a feedwater stream in membrane separation equipment , said membrane separation equipment comprising a number N of membrane separation units , N being a positive integer , to produce a low solute containing product stream and a high solute containing reject stream , said process comprising:(a) providing a feedwater stream containing solutes therein, said solutes comprising (i) hardness, (ii) alkalinity, and (iii) at least one molecular species which is sparingly ionized when in neutral or near neutral pH aqueous solution, said at least one molecular species comprising one or more of (1) at least some TOC, or (2) at least some silica, or (3) at least some boron;(b) effectively eliminating the tendency of said feedwater to form scale when said feedwater is concentrated to a preselected concentration factor at a selected pH, by effecting, in any order, two or more of the following: (i) removing hardness from said feedwater stream; (ii) removing substantially all non-hydroxide alkalinity from said feedwater stream; (iii) removing dissolved gases, whether initially present or created during said hardness or said alkalinity removal step;(c) raising ...

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01-08-2013 дата публикации

WATER SEPARATION METHOD AND APPARATUS

Номер: US20130193072A1
Автор: Booth Donald W.
Принадлежит: NG INNOVATIONS, INC.

A system for treating fractionated water from an oil and gas well. The system comprising a filter system, a diffusive membrane system, a plurality of membrane sensors, and at least one membrane controller. The filter system is fluidly connected to the diffusive membrane system, wherein the filter system comprises a plurality of straining filter banks. The diffusive membrane system comprises a plurality of membrane banks each having an inlet and an outlet. The plurality of membrane sensors are positioned at the outlet of each of the plurality of membrane banks, and the plurality of membrane sensors are configured to detect the total dissolved solids level at the outlet of each of the plurality of membrane banks. The at least one membrane controller is programmed to selectively disengage and isolate at least one of the plurality of membrane banks from fluid communication with the system upon detection if the total dissolved solids level at the outlet of one or more of the membrane banks is above about 20,000 ppm. A method is also provided. 1. A system for treating fractionated water from an oil and gas well , the system comprising:a filter system, a diffusive membrane system, a plurality of membrane sensors, and at least one membrane controller, wherein filtered water is transferred from the filter system to the diffusive membrane system,wherein the filter system comprises a plurality of straining filter banks,wherein the diffusive membrane system comprises a plurality of membrane banks each having an inlet and an outlet,wherein the plurality of membrane sensors are positioned at the outlet of each of the plurality of membrane banks, and the plurality of membrane sensors are configured to detect the total dissolved solids level at the outlet of each of the plurality of membrane banks,wherein the at least one membrane controller is programmed to selectively disengage and isolate at least one of the plurality of membrane banks from fluid communication with the system ...

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01-08-2013 дата публикации

Water treatment device and water treatment method

Номер: US20130193087A1
Принадлежит: Tokyo Electron Ltd

Provided is a water treatment device with which organic substances contained in raw water to be treated are decomposed to thereby alleviate the load to be imposed on a downstream filter and with which it is possible to avoid corrosion of the piping or the like. The water treatment device 12 includes a large-bore channel 22 , a small-bore channel 23 , and a pressure pump 24 which pressurize raw water 15 a to a given pressure, the raw water containing organic substances, and further includes a laser light source 25 and a condensing lens 26 which irradiates laser light 37 upon the pressurized raw water 15 a to heat the raw water to a given temperature, wherein the laser light 27 emitted from the laser light source 25 is condensed by the condensing lens 26 on a region 29 that is located in the small-bore channel 23 through which the pressurized raw water 15 a flows and that is separated from the wall of the channel, thereby heating the raw water 15 a present in this region 29 and yielding supercritical water or subcritical water to decompose the organic substances contained in the raw water 15 a.

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15-08-2013 дата публикации

Tanning wastewater treatment and recycling method based on nano-catalytic electrolysis technology and membrane technology

Номер: US20130206692A1
Автор: Shiwen Zhang

A tanning wastewater treatment and recycling method based on nano-catalytic electrolysis technology and membrane technology relates to a tanning wastewater treatment. The tanning wastewater treatment and recycling method based on the nano-catalytic electrolysis technology and the membrane technology and a device thereof has a high COD removal rate, a low chemicals consumption, few sludges, thorough treatment, and a high reuse rate of water. The tanning wastewater treatment and recycling device based on the nano-catalytic electrolysis technology and the membrane technology includes: a coarse grid filtering machine, a regulating pool, a hydraulic sieve, a nano-catalytic electrolytic machine, a reaction pool, a sedimentation pool, an air flotation device, a biochemical pool, a secondary sedimentation pool, a secondary nano-catalytic electrolytic machine, a filter and a membrane system. The method includes: nano-catalytic electrolysis, flocculation, biochemical treatment, secondary catalytic electrolysis, filtration, and membrane filtration.

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15-08-2013 дата публикации

Fresh Water Generating Apparatus and Fresh Water Generating Method

Номер: US20130206697A1
Принадлежит: Kobelco Eco Solutions Co Ltd

An object is to provide a fresh water generating apparatus that is capable of efficiently and stably producing fresh water. Provided is a fresh water generating apparatus equipped with a seawater-treating reverse osmosis membrane device that produces fresh water from seawater by a reverse osmosis membrane, including a mixing section that mixes wastewater as dilution water with seawater to produce mixed water, and a first seawater-treating reverse osmosis membrane device that acts as the seawater-treating reverse osmosis membrane device to filter the mixed water, in which the apparatus is configured so that used water that is wastewater resulting from the use of the produced fresh water as service water is mixed as dilution water with seawater at the mixing section.

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22-08-2013 дата публикации

Cooling tower blow-down, groundwater and wastewater re-use process and system

Номер: US20130213888A1
Принадлежит: Tempest Environmental Systems Inc

A cooling tower blow-down, groundwater and wastewater re-use process and system is provided, which system may further include a cooling tower evaporation recovery system and process. Thus, blow-down from cooling equipment may be reused by appropriate treatment of the blow-down water, or treatment of other sources of water such as groundwater or wastewater, for use as make-up water in a cooling tower or other cooling equipment, and the capture of evaporation from cooling equipment is conducted to increase the efficiency and lower costs in the operation of such equipment.

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22-08-2013 дата публикации

METHOD FOR HIGH EFFICIENCY REVERSE OSMOSIS OPERATION

Номер: US20130213889A1
Автор: MUKHOPADHYAY DEBASISH
Принадлежит:

A process for treatment of water. Hardness and non-hydroxide alkalinity are removed from feedwaters to an extent sufficient to avoid scaling when concentrated. Sparingly ionizable components in the feedwater are urged toward increased ionization by increasing the pH of the feedwater. In this manner, species such as silica become highly ionized, and (a) their rejection by membranes used in the process is significantly increased, and (b) their solubility in the reject stream from the membrane process is significantly increased. Sparingly ionized species such as boron, silica, and TOC are highly rejected. Recovery ratios of ninety percent (90%) or higher are achievable with many feedwaters, while simultaneously achieving a substantial reduction in cleaning frequency of membranes used in the process. 1. A process for treatment of a feedwater stream with reverse osmosis membrane separation equipment , to produce a low solute containing product stream and a high solute containing reject stream , said process comprising:(a) providing a feedwater stream containing solutes therein, said solutes comprising (i) hardness, (ii) alkalinity, and (iii) at least one molecular species which is sparingly ionized when in neutral or near neutral pH aqueous solution, said at least one molecular species comprising one or more of (1) at least some TOC, or (2) at least some silica, or (3) at least some boron;(b) effectively eliminating the tendency of said feedwater to form scale when said feedwater is concentrated at a selected pH, by treating the feedwater stream in a hydrogen form cation exchange resin to (i) remove substantially all hardness from said feedwater stream, (ii) remove substantially all alkalinity from said feedwater stream, and (iii) remove dissolved carbon dioxide created during removal of said hardness and said alkalinity;(c) raising the pH of the product from step (b) to a selected pH of ten (10) or more, by adding a selected alkali thereto, to urge said at least one ...

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29-08-2013 дата публикации

REVERSE OSMOSIS NEGATIVE-ION WATER DISPENSER

Номер: US20130220903A1
Принадлежит:

A reverse osmosis negative-ion water dispenser comprising a PP filter element, a granular active carbon filter element and a compressed active carbon filter element inside a housing; a low pressure switch, booster pump, an inlet solenoid valve, a RO filter bottle, a RO membrane and two water outlets for concentrated water and pure water respectively are also provided, wherein the water outlet for concentrated water is connected with a flush solenoid valve and a waste water proportioner assembly, the water outlet for pure water is connected with a storage tank through a high pressure switch and a float switch; the storage tank is provided with a high-low level three-line water level switch and connected to a combined hot and cold exchange tank. A negative-ion generating device comprising a solenoid valve, a fast heating equipment and a negative-ion filter device is provided to generate negative-ion. 1. A reverse osmosis negative-ion water dispenser comprising a housing , wherein a PP filter element , a granular active carbon filter element and a compressed active carbon filter element are arranged inside the housing in the processing sequence of water purification; a low pressure switch is arranged between the PP filter element and the granular active carbon filter element; filtered tap water flows into a booster pump through an inlet solenoid valve; the booster pump is connected with a RO filter bottle at its water outlet end; the RO filter bottle is equipped with a RO membrane inside and disposed with two water outlets for concentrated water and pure water respectively , wherein the water outlet for concentrated water is connected with a flush solenoid valve as well as a waste water proportioner assembly , and the water outlet for pure water is connected with a storage tank through a high pressure switch and a float switch consecutively; the storage tank is provided with a high-low level three-line water level switch and its water outlet on the bottom is connected ...

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29-08-2013 дата публикации

Apparatus for the use of nanoparticles in removing chemicals from aqueous solutions with subsequent water purification

Номер: US20130220933A1
Принадлежит: BLUFLOW TECHNOLOGIES Inc

An apparatus for removing target chemicals from water includes a reaction chamber, a source of an aqueous solution of the target chemicals that can be supplied on demand to the reaction chamber, a timer that times a reaction between the particles and the target chemicals such that a concentration of the target chemicals in the aqueous solution reaches a predetermined low level in a desired time, and elements for removing the aqueous phase from the reactor while keeping the particles entrained inside the reactor using a microfilter configured to be back flushed, adding aqueous solution to the reactor from the source and continuing cycles until the particles are saturated, removing and replacing the particles in a final cycle of a particle charge lifetime, and recovering the target chemicals from the particles such that the particles can be reused.

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29-08-2013 дата публикации

Ultraviolet oxidation device, ultrapure water production device using same, ultraviolet oxidation method, and ultrapure water production method

Номер: US20130220934A1
Принадлежит: UBE Industries Ltd

Disclosed is an ultraviolet oxidation device for decompositing organic materials present in water in low energy consumption and low cost, an ultrapure water production device using the same, an ultraviolet oxidation method, and an ultrapure water production method. An ultraviolet oxidation device including: a flow tank 10; photocatalyst fibers 12; an ultraviolet radiating unit 14; and an ultraviolet radiating unit housing unit 16 which is arranged to occupy an entire cross-section of the flow tank intersecting with flowing direction of the water to be processed in the flow tank 10; wherein the ultraviolet radiating unit housing unit 16 is constructed such that the water to he processed flows toward the ultraviolet radiating unit 14 from an upstream side, and after flowing in the housing unit 16, the water to be processed flows out to a downstream side, and is formed of a material that allows the ultraviolet rays from the ultraviolet radiating unit 14 to radiate the photocatalyst fibers 12.

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05-09-2013 дата публикации

POLYMER COATINGS THAT RESIST ADSORPTION OF PROTEINS

Номер: US20130228520A1
Принадлежит:

The invention provides membranes useful for filtration of water and other liquids. The membrane may be a composite membrane having a polymer layer incorporating quaternary phosphonium or ammonium groups. The polymer layer may be resistant to protein adsorption in an aqueous environment. The membrane may also be a surface-modified membrane in which a polymer having quaternary phosphonium or ammonium groups is covalently attached to the membrane surface. Methods for making and using the membranes of the invention are also provided. 2. The membrane of wherein the polymeric layer is crosslinked.4. The membrane of wherein the polymerizable group is selected from the group consisting of an acrylate group claim 3 , a methacrylate group claim 3 , a styrene group claim 3 , a vinylether group claim 3 , an acrylamide group claim 3 , a methacrylamide group.5. The membrane of wherein R claim 3 , Rand R claim 3 , independently from one another claim 3 , are selected from the group consisting of methyl claim 3 , ethyl claim 3 , propyl claim 3 , isopropyl claim 3 , n-butyl claim 3 , t-butyl claim 3 , isobutyl claim 3 , pentyl claim 3 , hexyl groups claim 3 , —(CH)—OH where n is from 1 to 5 claim 3 , —(CHCHO)—CHwhere n is 1 is from 2 claim 3 , —(CHCHO)—H where n is from 1 to 2.6. The membrane of where X is selected from the group consisting of Br claim 3 , I claim 3 , BF claim 3 , Cl claim 3 , TfN and OAc7. The membrane of wherein the thickness of the polymeric layer is between 0.01 μm and 10 μm.8. The membrane of wherein the support membrane is porous with a pore size between about 2.5 nm and about 120 nm.9. The membrane of claim 8 , wherein the composite membrane is permeable to a aqueous solution when a pressure difference of 2 MPa or less is applied across the membrane.10. A method of purifying water claim 8 , the method comprising the comprising the steps of:{'claim-ref': {'@idref': 'CLM-00001', 'claim 1'}, 'a. bringing water containing impurities into contact with a first side ...

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12-09-2013 дата публикации

Seawater desalination system and energy recovery apparatus

Номер: US20130233785A1
Принадлежит: Ebara Corp

An energy recovery apparatus exchanges pressure energy between concentrated seawater discharged from a reverse-osmosis membrane-separation apparatus and a part of seawater to be treated by the reverse-osmosis membrane-separation apparatus in a seawater desalination system for producing fresh water from the seawater. The energy recovery apparatus includes two perforated plates provided at a concentrated seawater port side in a chamber, and two perforated plates provided at a seawater port side in the chamber. The two perforated plates comprises a first perforated plate and a second perforated plate. The first perforated plate and the second perforated plate at the concentrated seawater port side and the seawater port side are arranged to meet certain requirements including one of an open area ratio of the first perforated plate, an open area ratio of the second perforated plate, and a distance between the first perforated plate and the second perforated plate.

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03-10-2013 дата публикации

MEMBRANE FOR REVERSE OSMOSIS

Номер: US20130256209A1
Автор: Völker Manfred
Принадлежит:

Reverse-osmosis modules, each containing a module tube with a module bottom and a module lid, and a reverse osmosis membrane arranged in the module tube and comprising a permeate collection tube, are characterized in that the reverse osmosis membrane has a fixed predetermined diameter and a length selected from predetermined length values. 1. A reverse-osmosis module comprising:a module tube with a module bottom and a module lid,a reverse osmosis membrane arranged in the module tube and comprising a permeate collection tube, andthe reverse osmosis membrane has a fixed predetermined diameter and a length selected from predetermined length values.2. The reverse osmosis module according to claim 1 ,wherein the predetermined diameter is between 4.7 inches and 5.0 inches, preferably 4.9 inches, and the possible length values are about 40 inches, 23 inches and 12 inches.3. The reverse osmosis module according towherein the capacity of the reverse osmosis membrane is about 500 l/h, 250 l/h, and 100 l/h.4. The reverse osmosis module according to wherein the membrane areas of the reverse osmosis membranes are 15 m claim 1 , 6.6 mand 2.8 m.5. The reverse osmosis module according to wherein the transmembranic flow is between 30 l/mand 40 l/m claim 1 , preferably about 33 l/m.6. The reverse osmosis module according to wherein the reverse osmosis membrane is inserted with an end section into a membrane collar and is sealed relative thereto with a ring seal claim 1 , the membrane collar being fastened to the module bottom and comprising an anti-telescope star.7. The reverse osmosis module according to wherein the module bottom comprises a feed-water supply bore claim 1 , which terminates in a ring gap underneath the membrane collar claim 1 , a concentrate discharge bore which terminates radially inside the membrane collar underneath the reverse-osmosis membrane claim 1 , and a bore connected to the end of the permeate collection tube.81. The reverse osmosis module according to ...

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10-10-2013 дата публикации

SEA REVERSE OSMOSIS DEVICE

Номер: US20130264259A1
Автор: Jin Jifan
Принадлежит:

A lifting device includes: at least one first magnetic body, which is positioned on a platform and driven by a driving unit so as to move along a predetermined track; at least one second magnetic body, which is positioned above a part of track of the first magnetic body by a supporting device, and the magnetism of which is repulsive to that of the first magnetic body; and a lifting mechanism, which is fixedly connected to the second magnetic body, the second magnetic body is lifted or lowered according to the first magnetic body passing through or leaving from the second magnetic body during its movement course so as to cause the lifting mechanism to be lifted, lowered or swung. The lifting device can lift heavy objects by magnetic energy existing in the nature and has a simple structure, broad applicability, energy saving and high environmental protectionability. A power generation device and a sea reverse osmosis device that have the lifting device are disclosed. 115-. (canceled)16. A seawater reverse osmosis device which is installed in the seawater comprising: at least one first magnetic body, the said first magnetic body is positioned on a platform and driven by a driving unit so as to move along a predetermined track;', 'at least one second magnetic body, the said second magnetic body is positioned above part of track of the said first magnetic body whose magnetism is repulsive to that of the first magnetic body;', 'a lifting mechanism which is positioned on a supporting device and connected to the second magnetic body, wherein the lifting mechanism is a disk-shaped piston with a lifting rod fixedly positioned below the disk-shaped piston;', "wherein, the second magnetic body is lifted or lowered vertically in cycle according to the said first magnetic body's passing through or leaving from the second magnetic body in cycle at a set speed, so as to drive the said lifting mechanism to be lifted, lowered or swung;"], 'a lifting device comprisingan osmosis ...

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17-10-2013 дата публикации

APPARATUS AND METHODS FOR SOLUTION PROCESSING USING REVERSE OSMOSIS

Номер: US20130270186A1
Автор: Wohlert Calvin
Принадлежит:

Equipment, systems, processes and techniques for conducting reverse osmosis processing of solutions are described. The techniques can be applied to provide diluted solution (i.e. purified solvent), concentrate solution or each. A variety of specific equipment, example systems and processes are depicted and described. 1. A reverse osmosis system to treat water containing contaminant and produced by a process; the system comprising:(a) passing the water through a plurality of selective reverse osmosis membrane units in which the concentration of the contaminant is gradually decreased until clean water is produced.2. The reverse osmosis system of claim 1 , wherein passing the water comprises:(a) mixing the water with a first recycle stream of water to create a first water solution;(b) applying pressure to the first water solution sufficient to past the water solution through a first selective reverse osmosis membrane creating: a solution of salt from that portion of the water solution that did not pass through the first selective reverse osmosis membrane; and, a receiving solution from that portion of the water solution that did pass through the first selective reverse osmosis membrane; the solution of salt being induced by pressure to flow back into the first recycle stream;(c) mixing the receiving solution with a second recycle stream of water creating a second water solution;(d) applying pressure to the second water solution sufficient to pass the second water solution through a second selective reverse osmosis membrane creating: a second solution of salt from that portion of the water solution that did not pass through the second selective reverse osmosis membrane; and, a second receiving solution from that portion of the second water solution that did pass through the second selective reverse osmosis membrane; the solution of salt being induced by pressure to flow back into the second recycle stream; and,(e) continuing to mix the receiving solution with a recycle ...

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17-10-2013 дата публикации

Using the solid waste-quicklime membrane swqm process for the production of sodium hydroxide

Номер: US20130272934A1
Принадлежит: Individual

The proposed invention uses ion exchange technology to produce dilute caustic soda liquor from calcium hydroxide liquor Ca(OH) 2 followed by the reaction of carbon dioxide CO 2 with caustic soda to produce dilute sodium carbonate solution. Multiple reverse osmosis and acidic CO 2 sparging can concentrate the Na 2 CO 3 liquor to 6-7%. The 6-7% liquor is treated with waste heat to produce 50% or solid Na2CO3. The 6-7% liquor can be treated with Ca(OH) 2 to produce 6-7% NaOH liquor then can be transformed to 50% or solid NaOH. The output of many industrial processes generates waste heat, brine water and CO2 and the present invention combines these components in the production of solid Na 2 CO3, NaOH or their high % liquors. Availability of waste heat sources can lead to higher efficiency in Na 2 CO 3 and NaOH production. The process is not electrochemical chloro alkali technology or Solvay process.

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24-10-2013 дата публикации

Desalination system and elements thereof

Номер: US20130277286A1
Принадлежит: IDE Technologies Ltd

According to one aspect of the present invention, there is provided a desalination system comprising a plurality of elongated pressure vessels (PV). Each PV has a longitudinal axis, oriented such that the longitudinal axis thereof is of a vertical orientation. Each of the PVs is adapted to receive therein a plurality n of desalination membranes. The membranes located above the lowermost membrane within the PV have a total weight allowing them to function as a mechanism limiting axial expansion of the lowermost membrane, whereby the PV is free of any additional limiting mechanism.

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24-10-2013 дата публикации

REVERSE OSMOSIS SYSTEM WITH ENERGY RECOVERY DEVICES

Номер: US20130277310A1
Автор: JR. Eli, Okeljas
Принадлежит:

A reverse osmosis system according to the present disclosure includes a first membrane array, a second membrane array, a hydraulic pressure booster, and a motor-generator. The first membrane array is configured to generate a first permeate stream and a first brine stream from a feed stream. The second membrane array is configured to generate a second permeate stream and a second brine stream from the first brine stream. The booster is configured to use energy from the second brine stream to increase pressure of at least one of the feed stream and the first brine stream. The motor-generator is coupled to the hydraulic pressure booster and is operable to use energy from a power supply to drive the hydraulic pressure booster. The motor-generator is also operable to use energy from the second brine stream to provide power to the power supply. 1. A reverse osmosis system comprising:a pump operable to pressurize a feed stream;a first membrane array configured to receive the feed stream and to generate a first permeate stream and a first brine stream from the feed stream;a second membrane array configured to receive the first brine stream and to generate a second permeate stream and a second brine stream from the first brine stream;a first hydraulic pressure booster configured to receive at least a first portion of the second brine stream and to use energy from the first portion of the second brine stream to increase a pressure of at least one of the feed stream and the first brine stream; anda motor-generator coupled to the first hydraulic pressure booster, operable to use energy from a power supply to drive the first hydraulic pressure booster, and operable to use energy from the second brine stream to provide power to the power supply.2. The reverse osmosis system of wherein the first membrane array is configured to receive the feed stream directly from the pump.3. The reverse osmosis system of wherein the first hydraulic pressure booster is configured to increase the ...

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07-11-2013 дата публикации

WATER DESALINATION MECHANISM

Номер: US20130292334A1
Автор: Rapoport Uri
Принадлежит:

A water desalination mechanism, including: a running pipe, for fresh water; a venturi arrangement, having a first venturi nozzle, a second venturi nozzle and a branch between; the first and second nozzles; a container divided by a reverse osmosis membrane into a first side and a second side and having: a first side inlet, for contaminated water; a first side outlet, for remaining salts and/or minerals; and a second side outlet, for desalinated water.

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21-11-2013 дата публикации

Methods and apparatus for delivery system for water enhancements

Номер: US20130306152A1
Автор: Jon-Andrew V. Sigona
Принадлежит: Perfect Water Tech Inc

A delivery system for water enhancements according to various aspects of the present invention is configured to provide a controlled amount of a water enhancement to a water supply. In one embodiment, the delivery system comprises an enhancing device that operates under pressure to provide a controlled rate of diffusion of an enhancing element into the water supply to form an enhanced water supply for use or consumption. The delivery system may also be configured to buffer the enhanced water supply prior to use or consumption.

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28-11-2013 дата публикации

PROCESSES AND FILTERS FOR DESALINATION OF WATER

Номер: US20130313196A1
Принадлежит: Ticona LLC

In a process for the desalination of water, an impure, salt-containing water feed is passed through one or more filter media to remove from the feed impurities having a particle size greater than 50 μm and produce a first filtered water stream. The first filtered water stream is then passed through at least one further filter having an average pore size of 1 μm to 60 μm produced from sintered polyethylene particles having a molecular weight of at least 4×10g/mol as determined by ASTM-D 4020 to remove at least a portion of the impurities having a particle size less than or equal to 50 μm from the first filtered water stream and produce a second filtered water stream. The second filtered water stream is passed directly to a reverse osmosis membrane to produce a purified water stream. 1. A process for the desalination of water , the process comprising:(a) passing an impure, salt-containing water feed through one or more filter media to remove from the feed impurities having a particle size greater than 50 μm and produce a first filtered water stream;{'sup': '5', '(b) passing the first filtered water stream through at least one further filter having an average pore size from 1 μm to 60 μm and comprising a porous sintered composition comprising polyethylene particles having a molecular weight of at least 4×10g/mol as determined by ASTM-D 4020 to remove at least a portion of the impurities having a particle size less than or equal to 50 μm from the first filtered water stream and produce a second filtered water stream; and'}(c) passing said second filtered water stream directly to a reverse osmosis membrane to produce a purified water stream.2. The process of claim 1 , wherein the polyethylene particles have a molecular weight up to 10×10g/mol claim 1 , preferably from 3×10to 9×10g/mol claim 1 , as determined by ASTM-D 4020.3. The process of claim 1 , wherein the polyethylene particles have an average particle size claim 1 , d claim 1 , from 1 to 500 μm.4. The process of ...

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05-12-2013 дата публикации

Method for improving rejection of reverse osmosis membrane, treatment agent for improving rejection, and reverse osmosis membrane

Номер: US20130324664A1
Принадлежит: Kurita Water Industries ltd

A method capable of effectively improving a rejection of a reverse osmosis membrane without remarkably reducing a permeation flux, even if the membrane is seriously degraded. An aqueous solution containing a first organic compound having a molecular weight of less than 200, a second organic compound having a molecular weight of 200 to less than 500, and a third organic compound having a molecular weight of 500 or more is passed through the reverse osmosis membrane. The first organic compound is preferably an amino acid or an amino acid derivative. The total concentration of the first organic compound and the second organic compound and the concentration of the third organic compound are each preferably 1 to 500 mg/L.

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19-12-2013 дата публикации

Separation membrane module

Номер: US20130334124A1
Принадлежит: Nitto Denko Corp

Provided is a separation membrane module including: a tubular pressure container 7 in which a raw liquid is filtered through a separation membrane to produce a permeate liquid; and an internal member 5 A provided in the pressure container 7. The internal member 5 A is equipped with a sensor for detecting characteristics of at least one of the raw liquid and the permeate liquid. A detected signal generated by the sensor is transmitted from an antenna 65. The internal member 5 A has an antenna holding portion 54 in which the antenna 65 is embedded. A gap between the antenna holding portion 54 and an inner peripheral surface 7 a of the pressure container 7 is sealed with a sealing member 42.

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26-12-2013 дата публикации

Porous Film

Номер: US20130341277A1
Принадлежит:

A reverse osmosis (RO) membrane can include a porous substrate, a multilayer film arranged on the substrate, which includes a first layer including a polyelectrolyte and a second layer including a plurality of clay particles, where the first layer is arranged adjacent to the second layer. The multilayer film can be prepared by a spray-LbL process. The resulting RO membrane can provide high water permeability combined with high salt rejection. 1. A reverse osmosis membrane comprising:a porous substrate;a multilayer film arranged on the substrate, wherein the multilayer film includes:a first layer including a polyelectrolyte; anda second layer including a plurality of clay particles;wherein the first layer is arranged adjacent to the second layer.2. The reverse osmosis membrane of claim 1 , wherein the multilayer film includes a plurality of bilayers claim 1 , each bilayer including:a first layer including a polyelectrolyte; anda second layer including a plurality of clay particles arranged adjacent to the first layer.3. The reverse osmosis membrane of claim 1 , wherein the multilayer film includes a series of alternating layers claim 1 , the series alternating between a first layer including a polyelectrolyte and a second layer including a plurality of clay particles arranged adjacent to the second layer.4. The reverse osmosis membrane of claim 1 , wherein the porous substrate is a nanoporous membrane.5. The reverse osmosis membrane of claim 1 , wherein the polyelectrolyte is positively charged when in a neutral aqueous solution.6. The reverse osmosis membrane of claim 5 , wherein the polyelectrolyte includes PDAC.7. The reverse osmosis membrane of claim 5 , wherein the clay particles are negatively charged when in a neutral aqueous solution.8. The reverse osmosis membrane of claim 7 , wherein the clay particles are plate-shaped.9. The reverse osmosis membrane of claim 7 , wherein the clay particles include a laponite clay.10. The reverse osmosis membrane of claim 2 ...

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16-01-2014 дата публикации

Oscillatory crossflow membrane separation

Номер: US20140014578A1
Принадлежит: Rockwater Resource LLC

Oscillatory crossflow membrane separation apparatus and methods are disclosed for effluent treatment. The apparatus include a membrane module with a housing containing a membrane element, said module having an input for receiving effluent for treatment and a treated effluent output. A crossflow pump is connected for moving oscillating fluid through the membrane module and a feed pressure pump is connected with the membrane module for applying membrane operating pressure. A fluid oscillator is active with either pump for pulsating fluid received thereat.

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23-01-2014 дата публикации

Mobile Water Purification System

Номер: US20140021115A1
Автор: Jesper Ellegaard
Принадлежит: Pure H2O AS

The present invention relates to a mobile water purification system employing crossflow filtration, such as reverse osmosis filtration. One embodiment of the invention discloses a mobile water purification system comprising a housing, a pump unit and a piping system for providing fluid communication between a water inlet, a pre-filtration unit, a crossflow filtration unit, a disinfection unit and an outlet for supply of purified water, wherein the pre-filtration unit comprises sediment/cartridge filtrations means and dechlorination means, the cross-flow filtration unit comprises a plurality of parallel and/or sequentially arranged membrane filters, and the piping system is reconfigurable such that the crossflow filtration unit can be bypassed. The present water purification system is adapted to be deployed in remote areas substantially anywhere in the world.

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23-01-2014 дата публикации

Filter And Method For The Desalination Of Water By Means Of Reverse Osmosis Of The Centrifugal Type, Involving The Generation Of Dean Vortices

Номер: US20140021134A1
Принадлежит:

This invention concerns a method for desalination of sea water and a design and construction of a centrifugal filter for desalination of water. The process uses the filter developed based on reverse osmosis technology as a fundamental component that uses hollow fiber membrane modules arranged in a spiral manner around a central support pipe and distributed in concentric rings around the periphery of the rotating section to favor the formation of Dean vortices. Wherein the membrane is built with a structure of an aromatic polyamide as the first layer, followed by a layer of polyestersulfone and a support layer of polyester; applying the material Kevlar 49 in position 1 and 4 on the aromatic chain structure to increase the structure and resistance of the membrane. 1. A filter for sea water desalination by centrifugal reverse osmosis with the generation of Dean vortices , wherein the filter consists of a static housing , the lower part of which is an inverted cone with a truncated tip where a feed pipe crosses and in which the permeated water is collected that drains from the top of the assembly of hollow fiber modules down the inner wall of the housing , and a closed cylindrical section on its upper end that inside supports a rotating assembly which is rotated from the exterior by a motor , reducer , pulleys and belts and wherein the rotating assembly is determined by two rotating tank disks , a lower one through which the water to be treated is fed towards the membrane modules and an upper one through which the reject water with a high concentration of salts is removed , wherein the upper and lower disks are joined by a central duct and modules that contain hollow fiber membranes , characterized in that the hollow fiber membrane modules consist of a central PVC piping to support the hollow fiber membranes wound in a spiral manner in the direction of the rotation of the rotor to favor Dean vortices to cause self cleaning of the membranes and because said module have ...

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13-02-2014 дата публикации

Reverse osmosis membrane element

Номер: US20140042080A1
Автор: Qiang Wang, Yizhi Hou

A reverse osmosis membrane element has a relatively high recovery rate. In the present invention, water ports of the reverse osmosis membrane element are located at both ends thereof, and a waterproof adhesive tape is coated between a flow guide net and a reverse osmosis membrane of the reverse osmosis membrane element, including a plurality of adhesive tapes parallel with an axial direction of the reverse osmosis membrane element, so that fed water is discharged from the water outlet after circuitously flowing between adjacent adhesive tapes along the axial direction of the reverse osmosis membrane element. In the technical solution of the present invention, a circuitous flow passage is available in the reverse osmosis membrane element, which increases the fluid flow rate, and decreases the surface pollution rate of the reverse osmosis membrane, thereby contributing to the improvement of the recovery rate of the reverse osmosis membrane element.

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20-02-2014 дата публикации

Seawater desalination apparatus

Номер: US20140048467A1
Автор: Kazuo Matsuura
Принадлежит: NANOMIST TECHNOLOGIES Co Ltd

A seawater desalination apparatus includes a spray ( 1 ), a gas supplier ( 9 ), an atomizing electrode ( 2 ), a high voltage power supply ( 3 ), a mist classifier ( 4 ), and a mist collector ( 5 ). The spray includes apertures for producing a seawater mist. The supplier supplies gas for carrying the mist from the spray. The electrode electrostatically produces fine droplets from the mist from the spray. The power supply is connected to the electrode and the spray, and applies high voltage between the electrode and the spray for the production of fine droplets from the mist from the atomizer. The classifier separates the fine droplets in the mist from the electrode. The collector collects the mist discharged from the classifier thereby producing fresh water.

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13-03-2014 дата публикации

CROSS FLOW FILTRATION SYSTEM USING ATMOSPHERIC BLADDER TANK

Номер: US20140069869A1
Принадлежит: 3M INNOVATIVE PROPERTIES COMPANY

A fluid treatment system is disclosed comprising a cross flow filter () comprising a feed portion, a concentrate portion, and a permeate portion. The treatment system further comprises a permeate storage apparatus () fluidly connected to the permeate portion and comprising a pressure boundary comprising an inner wall surrounding a pliable bladder (), the pliable bladder fluidly separating a permeate chamber from an atmospheric chamber (). The treatment system may further comprise a permeate pressurizing device () fluidly connecting the permeate chamber to a system output. 1. A fluid treatment system comprising:a cross flow filter comprising a feed portion, a concentrate portion, and a permeate portion; 'a pressure boundary comprising an inner wall surrounding a pliable bladder, the pliable bladder fluidly separating a permeate chamber from an atmospheric chamber which communicates with the surrounding atmosphere via an aperture in the pressure boundary such that the pressure in the atmospheric chamber remains in substantial equilibrium with the pressure of the surrounding atmosphere; and', 'a permeate storage apparatus fluidly connected to the permeate portion and comprisinga permeate pressurizing device fluidly connected between the permeate chamber and a system output.2. The fluid treatment system of further comprising a pressure switch fluidly connected to one of the permeate portion or the permeate chamber to monitor a permeate pressure claim 1 , the pressure switch operable to disrupt a fluid flow to the feed portion when the permeate pressure exceeds a permeate pressure setpoint.3. The fluid treatment system of wherein the permeate chamber comprises the inner wall.4. The fluid treatment system of wherein the atmospheric chamber does not comprise the inner wall.5. The fluid treatment system of wherein the pressure boundary is designed to withstand a constant fluid pressure of at least 30 psi (2.07e+005 N/m) bearing against the inner wall.6. The fluid treatment ...

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20-03-2014 дата публикации

LOW ENERGY REVERSE OSMOSIS PROCESS

Номер: US20140076807A1
Автор: Chidambaran Ravi
Принадлежит:

We provide a system and method for reverse osmosis treatment of water, including seawater and brackish water. Methods and systems of embodiments of the invention may include, for example, ultrafiltration followed by biofoulant removal, both of which precede reverse osmosis. In preferred embodiments the system is run at a low flux. For example, a flux of 6-8 GFD may be used with seawater. 1. A method for desalination by reverse osmosis and reverse osmosis membrane cleaning , comprising:providing a feed stream of water to be desalinated;removing turbidity including bacteria and virus from said feed stream in an ultrafiltration membrane;removing biofoulants, bacteria and virus from said feed stream; andremoving salt from the feed stream by reverse osmosis, wherein the reverse osmosis is conducted at an operating flux, wherein the operating flux results in an energy consumption, and wherein conducting the reverse osmosis at a flux lower than the operating flux does not reduce the energy consumption by more than 10%; and 'regulating flow to the feed side reverse osmosis membrane, thereby allowing a reject water to remain in the feed side and causing flow of a permeate water from the permeate side to the feed side due to a concentration differential, wherein the concentration differential is maintained by adding RO concentrate as a makeup water to the feed side.', 'cleaning at least one reverse osmosis membrane used in removing salt from the feed stream by reverse osmosis, comprising, for a reverse osmosis membrane having a feed side and a permeate side2. The method of claim 1 , wherein the step of removing turbidity is conducted prior to the step of removing biofoulants.3. The method of claim 1 , wherein said ultrafiltration membrane reduces SDI of the feed stream to less than 3-5 SDI.4. The method of claim 3 , wherein said ultrafiltration membrane reduces turbidity of the feed stream to less than 0.1.5. The method of claim 1 , wherein said biofoulant removal step ...

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20-03-2014 дата публикации

Water purification systems and methods

Номер: US20140076812A1
Автор: Kevin E. Munro
Принадлежит: Individual

Systems, components, and methods for water purification are described. In an example, a system may comprise an array of light-focusing elements, a heat exchanger device, a turbine generator, or other components and can be configured to use a source of light (e.g., sunlight) to filter water from a water source and to generate electricity. The electricity may be looped back into the system to further produce filtered water.

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20-03-2014 дата публикации

Optimizing egg production characteristics via seawater mineralization

Номер: US20140079803A1
Принадлежит: LUBERSKI Inc (DBA HIDDEN VILLA RANCH)

Aspects for utilizing a seawater fluid to optimize egg-production characteristics are disclosed. In one aspect, a method is provided, which includes identifying a desired optimization, determining a corresponding seawater to non-seawater ratio, and generating a seawater fluid according to the ratio. An egg-cultivation method is also provided, which includes ascertaining a desired optimization, selecting a corresponding seawater to non-seawater ratio, and providing a seawater fluid comprising the ratio to a hen. In another egg-cultivation method, hens are provided with a mixed feed comprising a feed to seawater-mineralized produce ratio selected according to a desired optimization. A method to grow produce is also provided, which includes mineralizing soil with a seawater fluid comprising a seawater to non-seawater ratio corresponding to a preferred optimization. In another aspect, a method to produce feed is disclosed, which includes mixing feed with mineralized produce according to a ratio corresponding to a desired optimization.

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27-03-2014 дата публикации

SYSTEMS AND METHODS FOR TREATING PRODUCED WATER

Номер: US20140083942A1
Принадлежит:

Embodiments relate to systems and methods for treating produced water and other contaminated water that can be customized or adapted to particular characteristics of the water and/or its contaminants or other contents while minimizing costs related to treating the water. In an embodiment, a method of treating produced water comprises degrading solid particles in the produced water using beneficial bacteria; filtering solid particles from the produced water; reducing pathogenic bacteria in the produced water by introducing ozone into the produced water; reducing contaminants in the produced water by passing the produced water through at least one filter; reducing salts in the produced water using a reverse osmosis system; and providing treated produced water. 1. A method of treating produced water comprising:degrading solid particles in the produced water using beneficial bacteria;filtering solid particles from the produced water;reducing pathogenic bacteria in the produced water by introducing ozone into the produced water;reducing contaminants in the produced water by passing the produced water through at least one filter;reducing salts in the produced water using a reverse osmosis system; andproviding treated produced water.2. The method of claim 1 , further comprising filtering hydrocarbons from the produced water.3. The method of claim 2 , wherein filtering hydrocarbons comprises:absorbing hydrocarbons by passing the produced water through absorbent materials;pressing the hydrocarbons from the absorbent materials; andcapturing the pressed hydrocarbons in a container.4. The method of claim 1 , wherein degrading solid particles comprises:dissolving oxygen-rich air in the produced water to promote growth of the beneficial bacteria.5. The method of claim 1 , wherein filtering solid particles comprises:dissolving air in the produced water under pressure;releasing the air in the produced water at atmospheric pressure such that the released air adheres to solid ...

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03-04-2014 дата публикации

MOBILE WATER FILTRATION UNIT AND CONTROL SYSTEM, AND RELATED DEVICES, COMPONENTS, SYSTEMS AND METHODS

Номер: US20140091041A1
Автор: Nielsen Elo
Принадлежит:

A standardised, modular mobile water purification unit for the production of safe potable water and for treatment of wastewater is disclosed to fulfill the water need for humans, animals and households. In one embodiment, the unit can be based on a standardized climate-controlled container that is robust both physically and functionally, can be easily transported and quickly set up in remote regions and disaster areas. The unit may work for purification of water of brackish, sea or polluted surface water, and of wastewater, and can be customised to the given water type based on easy changeable treatment modules. The unit includes a rigid frame that can be removed from the container, and also includes a control system for remote monitoring and control of the unit. 1. A mobile water filtration unit for treating water in areas with limited infrastructure , comprising:a rigid frame defining an interior space configured to be removably disposed within a shipping container;at least one source water intake configured to receive untreated source water into the mobile water filtration unit from an external water source;a plurality of treatment modules connected to the rigid frame within the interior space such that the source water received from the at least one source water intake passes through and is treated by the plurality of treatment modules in series, thereby converting the untreated source water into treated water;at least one treated water output configured to receive the treated water from the plurality of treatment modules and output the treated water into a water receptacle.2. The mobile water filtration unit of claim 1 , wherein the plurality of treatment modules comprises a microfilter module configured to remove particles larger than 50 microns from the source water.3. The mobile water filtration unit of claim 1 , wherein the plurality of treatment modules comprises an oxidation module configured to oxidize dissolved inorganic matter in the source water into ...

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02-01-2020 дата публикации

SYSTEM AND METHOD FOR WASHING ITEMS

Номер: US20200000309A1
Автор: Hansson Per
Принадлежит:

A system and method for washing items with water, includes a water inlet and a container for receiving the items to be washed. The system comprises a water purification apparatus for purifying water introduced through said water inlet to produce purified water. The water purification apparatus comprises at least one filter for filtering off particulate solids, a reverse osmosis device, and at least one deionizing filter. The system further comprises a reservoir for storing purified water produced by the water purification apparatus, said reservoir being connected to said water purification apparatus and said container, so that the items are washable inside the container with the purified water. 1. A system for washing items with water , comprising a water inlet and a container for receiving the items to be washed , wherein the system comprises a water purification apparatus for purifying water introduced through said water inlet to produce purified water , the water purification apparatus comprising:at least one filter for filtering off particulate solids,a reverse osmosis device, andat least one deionizing filter, and,wherein the system further comprises a reservoir for storing purified water produced by the water purification apparatus, said reservoir being connected to said water purification apparatus and said container, so that the items are washable inside the container with the purified water.2. The system according to claim 1 , wherein the water inlet is arranged for connection to a municipal water supply network.3. The system according to claim 1 , comprising a pump for obtaining a working pressure of the reverse osmosis device and the deionizing filter of 600-800 kPa.4. The system according to claim 1 , wherein the reverse osmosis device is arranged between the filter and the deionizing filter.5. The system according to claim 1 , wherein the water purification apparatus comprises claim 1 , arranged in consecutive order claim 1 , a sediment filter claim 1 , ...

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06-01-2022 дата публикации

VOLUMETRIC PRESSURE EXCHANGER WITH BOOSTER EFFECT AND INTEGRATED FLOW MEASUREMENT, FOR A SEAWATER DESALINATION PLANT

Номер: US20220001330A1
Автор: Giraud Yves
Принадлежит:

At least one pressure exchange unit with a hollow cylindrical body, a piston sliding in the body, the piston including a piston head separating the interior of the cylindrical body into a downstream chamber and an upstream chamber, the downstream chamber being provided with a device for the admission and discharge of water to be treated, the upstream chamber being provided with a five-way distributor linkage including, for hydraulic balancing, two pressurized liquid supply orifices, two orifices for the evacuation of the liquid and an opening in communication with the upstream chamber. 1. A volumetric pressure exchanger with a booster effect and flow measurement , comprising at least one pressure exchange unit with a hollow cylindrical body , a piston sliding in said body , said piston comprising a piston head separating an interior of said cylindrical body into a downstream chamber and an upstream chamber , said downstream chamber being provided with a device for an admission and discharge of water to be treated , wherein said upstream chamber is provided with a five-way distributor linkage comprising , for hydraulic balancing , two pressurized liquid supply orifices , two orifices for evacuating said liquid and an opening which is in communication with said upstream chamber.2. The exchanger according to claim 1 , wherein said distributor linkage is hydraulically balanced in order to remove axial stress on an axis of rotation of the distributor.3. The exchanger according to claim 1 , wherein the motorized distributor linkage provides for recovery of a pressure due to a pressure drop from the ROM with a very high efficiency claim 1 , without an external pump or consumption of flow.4. The exchanger according to claim 1 , wherein cranks of the distributor linkage have symmetrical openings which are shaped so as to allow alternate fluid communication and an end to fluid communication with the supply and evacuation orifices of the exchanger.5. The exchanger according to ...

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01-01-2015 дата публикации

METHOD AND APPARATUS FOR RECYCLING WATER

Номер: US20150000914A1
Принадлежит:

We provide an evaporation based zero-liquid discharge method for generation of steam for enhanced oil recovery (EOR) processes utilizing once-through steam generators (OTSGs). The method includes feeding the OTSG(s) with produced water, vaporizing a fraction of this water for steam injection and blowing down the balance of the water. This water, referred to as OTSG blowdown, can be flashed to produce a vapor stream and a liquid that is fed to a mechanical vapor compression (MVC) evaporative process. The latent energy contained in the vapor stream generated by the upstream flash is beneficially recycled to substantially reduce or eliminate the energy consumption of the MVC process. The evaporative process can be used to reduce the liquid waste for disposal or eliminate the need for liquid disposal by achieving zero liquid discharge. 1. A method of water recovery from once-through steam generator (“OTSG”) blowdown water , comprising:a) providing a water stream;b) feeding the water stream to a once-through steam generator as feed water (“OTSG Feed”) and producing steam;c) blowing down a fraction of the OTSG feed water not used to produce steam (“OTSG BD”) to a flash chamber;d) flashing a fraction of the OTSG BD stream to produce a vapor phase and a liquid phase in the flash chamber;e) flowing the vapor phase to an evaporator, where the vapor phase transfers latent heat to the evaporator and condenses to form condensate, and wherein the evaporator produces distillate;f) flowing the liquid phase from the flash chamber to the evaporator, thereby concentrating the dissolved solids in the water and producing a more highly concentrated blowdown liquid stream;g) blowing down the subsequent concentrated liquid phase from the evaporator; andh) recycling the distillate as OTSG feedwater.2. The method of claim 1 , wherein the water stream is produced water from heavy oil production.3. The method of claim 2 , further comprising claim 2 , prior to feeding the water stream to the ...

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06-01-2022 дата публикации

SEA WATER DE-SALINATION METHODS AND APPARATUSES

Номер: US20220002170A1
Автор: PHATAK Dhananjay
Принадлежит:

Systems, apparatus and methods for desalination of ocean water using gravity force are described. One example method of desalinating ocean water includes providing a structure having a reverse osmosis membrane affixed to a first end, submerging the structure to a depth in a reservoir of salt water, wherein the depth is a function of a critical pressure of activation of operation of the reverse osmosis membrane, allowing a hydrostatic pressure at the depth to force salt water from the reservoir through the reverse osmosis membrane to cause fresh water to accumulate within a cavity on an inside of the structure; and making the fresh water available for an external use. 1. A method of desalinating ocean water , comprising:providing a structure having a reverse osmosis membrane affixed to a first end;submerging the structure to a depth in a reservoir of salt water, wherein the depth is a function of a critical pressure of activation of operation of the reverse osmosis membrane;allowing a hydrostatic pressure at the depth to force salt water from the reservoir through the reverse osmosis membrane to cause fresh water to accumulate within a cavity on an inside of the structure; andmaking the fresh water available for an external use.2. The method of claim 1 , wherein the structure is elongated and the first end is a bottom surface of the structure.3. The method of claim 1 , wherein a shape claim 1 , a size or an orientation of the structure is optimized for an energy efficiency and/or an ease of membrane replacement or a maintenance.4. The method of claim 1 , wherein the structure comprises multiple structures or collection pods configured to deliver the fresh water into a storage tank for holding the fresh water before it is lifted/raised through a height D to a surface of the reservoir for the external use.5. The method of claim 1 , wherein the making the fresh water available for external use is performed by pumping the fresh water out of the cavity.6. The method of ...

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01-01-2015 дата публикации

WATER TREATMENT SYSTEM, AND WATER TREATING METHOD IN WATER TREATMENT SYSTEM

Номер: US20150001151A1
Принадлежит:

In a water treatment system, fouling is made earlier detectable, considering additionally the effect of spacers arranged between its separating membrane layers. 1. A water treatment system , comprising:a pre-treating unit for pre-treating a raw water;a desalting unit, having a separating membrane unit which has an RO membrane element in which separating membrane layers arranged as said separating membrane and spacers for keeping said separating membrane layers apart from each other are formed to be wound into a spiral form, for separating substance to be separated from said raw water pre-treated in said pre-treating unit using a separating membrane; anda monitoring unit between said pre-treating unit and said desalting unit,said monitoring unit further comprising:a monitor device, fitted to a bypass pipe of a pipe through which said pre-treating unit and said desalting unit are connected to each other, for having a closed vessel having at least one transparent or semitransparent surface; andan image-pickup device for making said raw water flowing in said closed vessel visible through said transparent or semitransparent surface,wherein said closed vessel includes a fouling-generating member imitating said separating membrane and said spacers, said image-pickup device makes it possible to pick up an image of said raw water flowing in said fouling-generating member through said transparent or semitransparent surface, and said monitor device has a structure in which fouling is more easily generated than in the structure which said desalting unit has.2. The water treatment system according to claim 1 , wherein said fouling-generating member of said monitor device has fibers claim 1 , in each of which dots are formed at intervals of a predetermined distance claim 1 , are arranged in a direction perpendicular to said flow of a water supplied to said RO membrane claim 1 , and the positions of said dots of any adjacent two of said fibers are designed to be in a zigzag ...

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07-01-2021 дата публикации

METHODS, SYSTEMS, AND COMPOSITIONS FOR DELIVERY OF NANOBUBBLES IN WATER TREATMENT SYSTEMS

Номер: US20210001273A1
Принадлежит:

Methods, systems, and devices for water treatment or for preventing fouling of components of water treatment systems can include the upstream introduction of nanobubbles in-line and/or in close proximity to a reverse osmosis membrane in the water treatment system. The nanobubbles can bind to and cluster (flocculate) nanoparticles (and possible larger solid particles) so that they can be removed and not foul water purification components such as reverse osmosis membranes. The nanobubbles can also interact with and change some characteristics of nanoparticles and thereby reduce fouling of some system components, such as reverse osmosis membranes, or other components. The systems, methods, and devices disclosed herein can help produce potable water safe for human consumption in a more cost-effective manner, e.g., by reducing maintenance costs and in some cases manufacturing costs. 160-. (canceled)61. A method for treating raw water containing suspended particles including suspended nanoparticles by way of introduction of nanobubbles for interacting with the suspended nanoparticles , the method comprising:collecting raw water in a reservoir, the water including suspended nanoparticles of calcium carbonate and other contaminates;filtering an amount of the other contaminates out of the water, thereby generating filtered water containing nanoparticles of calcium carbonate;detecting a concentration of the nanoparticles of calcium carbonate in the filtered water;mixing nanobubbles into the filtered water so as to raise a concentration of nanobubbles in the filtered water to a concentration at least as high as the concentration of the nanoparticles of calcium carbonate in the filtered water, thereby creating a mixture of filtered water and nanobubbles;pumping the mixture of filtered water and nanobubbles to a reverse osmosis membrane device having a membrane with pores having a size from 0.01 to 0.05 nanometers, wherein the mixture of filtered water and nanobubbles do not ...

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07-01-2021 дата публикации

REVERSE OSMOSIS MEMBRANE, MANUFACTURING METHOD THEREFOR, AND WATER TREATMENT MODULE

Номер: US20210001279A1
Принадлежит:

Provided is a reverse osmosis membrane comprising: a support layer comprising a support and a polysulfone layer; and an active layer, wherein a compression modulus is from 20 MPa to 40 MPa, to a method for manufacturing the same, and a water-treatment module. 1. A reverse osmosis membrane , comprising:a support layer comprising a support and a polysulfone layer; andan active layer,wherein a compression modulus of the reverse osmosis membrane is from 20 MPa to 40 MPa.2. The reverse osmosis membrane of claim 1 , wherein the support comprises a non-woven fabric.3. The reverse osmosis membrane of claim 1 , wherein the support has a thickness of 90 μm to 120 μm claim 1 , and the polysulfone layer has a thickness of 25 μm to 80 μm.4. The reverse osmosis membrane of claim 1 , wherein the polysulfone layer is formed with a polymer solution comprising polysulfone claim 1 , and a content of the polysulfone comprised in the polysulfone-comprising polymer solution is from 15% by weight to 20% by weight based on a total weight of the polysulfone-comprising polymer solution.6. The reverse osmosis membrane of claim 1 , which has a rate of defect occurrences of 0% to 5% when assembling the reverse osmosis membrane.7. A water-treatment module comprising one or more of the reverse osmosis membranes of .8. A method for forming the reverse osmosis membrane of claim 1 , the method comprising:forming a support layer comprising a support and a polysulfone layer; andforming an active layer on the support layer.9. The method of claim 8 , wherein the forming the active layer is performed by:dipping the support layer into an aqueous m-phenylenediamine (mPD) solution to form an mPD layer; anddipping the support layer comprising the mPD layer into a solvent solution comprising an organic trimesoyl chloride, the mPD layer being brought into contact with the organic trimesoyl chloride, and interfacially polymerizing to form a polyamide active layer. This application is a National Stage ...

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07-01-2016 дата публикации

Universal Scalable and Cost-Effective Surface Modifications

Номер: US20160001236A1
Принадлежит:

Disclosed are fouling resistant filtration membranes comprising a polymeric thin-film membrane comprising a surface. Also disclosed are methods of modifying thin-film filtration membranes, thereby improving, for example, the anti-fouling properties of the membranes. Also disclosed are methods of purifying water using the disclosed membranes. This abstract is intended as a scanning tool for purposes of searching in the particular art and is not intended to be limiting of the present invention. 2. (canceled)3. The membrane of claim 1 , wherein the membrane comprises at least one polyamide.4. (canceled)5. The membrane of claim 1 , wherein L is —O.6. The membrane of claim 1 , wherein L is selected from —OQ and —NRQ.7. The membrane of claim 1 , wherein Q is hydrogen.8. The membrane of claim 1 , wherein Q is a hydrophilic polymer.9. The membrane of claim 8 , wherein the hydrophilic polymer comprises at least one moiety selected from poly(ethylene glycol) claim 8 , poly(ethyleneimine) and polyaniline claim 8 , or a mixture thereof.12. The membrane of claim 1 , wherein Z is selected from —CHand —C(═NH)NH—.13. The membrane of claim 1 , wherein m is 0.14. The membrane of claim 1 , wherein each of Rand Ris hydrogen.15. The membrane of claim 1 , wherein each of Rand Ris halogen.16. The membrane of claim 1 , wherein Ris halogen and Ris hydrogen.17. The membrane of claim 1 , wherein the halogen is selected from —F and —Cl.18. The membrane of claim 1 , wherein the halogen is —F.19. The membrane of claim 1 , wherein Ris —CO claim 1 , Ris —NH claim 1 , and Ris hydrogen.20. The membrane of claim 1 , wherein Ris —CO claim 1 , and each of Rand Ris hydrogen.21. The membrane of claim 1 , wherein Ris —NH claim 1 , and each of Rand Ris hydrogen.2224-. (canceled)2630-. (canceled)31. The method of claim 25 , wherein the surface comprises at least one —NH— and/or —C═C— residue.3245-. (canceled)46. The method of claim 25 , further comprising activating the azide claim 25 , thereby forming a ...

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07-01-2016 дата публикации

ASYMMETRICALLY POROUS MEMBRANES MADE OF CROSS-LINKED THERMOPLASTIC SILICONE ELASTOMER

Номер: US20160001237A1
Автор: HALBACH Tobias
Принадлежит:

The invention relates to a covalently cross-linked, asymmetrically porous membranes (M) made of thermoplastic silicone elastomers; a method for producing the covalently cross-linked, asymmetrically porous membranes (M), in which, in a first step, a solution of a silicone composition SZ, which contains thermoplastic silicone elastomer S1 with alkenyl groups and contains cross-linker V, and a solvent L is produced, in a second step, the solution is brought into a mold, in a third step, the solution brought into a mold is brought into contact with a precipitation medium F, wherein a covalently non-cross-linked membrane is formed. In a fourth step, the solvent L and the precipitation medium F are removed from the non-cross-linked membrane and, in a fifth step, the membrane is subjected to a cross-linking, wherein the covalently cross-linked membrane M is formed; the membranes (M) produced according to the method; and to the use of the membranes (M) for the separation of material mixtures or for coating. 1. (canceled)3. (canceled)424. The method as claimed in claim , wherein the radicals Rcomprising alkenyl groups are alkenyl radicals having 2 to 12 carbon atoms.5. The method as claimed in claim 2 , wherein the crosslinker V is selected from the group consisting of organosilicon compounds comprising at least two SiH functions per molecule claim 2 , peroxides claim 2 , and azo compounds.6. The method as claimed in claim 2 , wherein the form in the second step is a film or a hollow fiber.7. The method as claimed in claim 2 , wherein claim 2 , in the third step claim 2 , the solutions brought into form are immersed into a precipitation bath filled with precipitation medium F.8. The method as claimed in claim 2 , wherein claim 2 , in the fourth step claim 2 , residues of solvent L and precipitation medium F are removed from the noncrosslinked membrane by evaporation.9. Covalently crosslinked claim 2 , asymmetrically porous membranes (M) made of thermoplastic silicone ...

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02-01-2020 дата публикации

Stacked type falling film evaporator, zero liquid discharge system comprising the same, and zero liquid discharging method using the same

Номер: US20200001197A1

A stacked type falling film evaporator includes a first evaporator, a second evaporator, a first vapor recovering device, a second vapor recovering device and a vapor recompressor. The first evaporator and the second evaporator respectively have evaporation tubes of a length of 5 m to 10 m, and are stacked in such a manner that wastewater passes through the first evaporator and the second evaporator in order. The first vapor recovering device collects vapor generated from the wastewater in the first evaporator and supplies the collected vapor to the second evaporator. The second vapor recovering device collects vapor generated from the wastewater in the second evaporator and supplies the collected vapor to the first evaporator. The vapor recompressor compresses the vapor collected in the second vapor recovering device before the vapor is supplied to the first evaporator.

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04-01-2018 дата публикации

Integrated Reverse Osmosis Module with Energy Recovery for Desalination

Номер: US20180001264A1
Автор: Law Wing-Keung, Song Jie
Принадлежит:

A system includes a first fluid inlet and a single reverse osmosis membrane module having a permeate outlet and a first inlet/outlet channel and a second fluid inlet/outlet channel in fluid communication with the first fluid inlet. An energy transfer system has a second fluid inlet, a brine outlet, a first energy exchanging module and a second energy exchanging module. The first and second energy exchanging modules are adapted to reversibly operate in opposite flow phases where a flow direction for the expulsion flow phase in each energy exchanging module is constant and where a flow direction for the energy recover flow phase in each energy exchanging module is constant. The single reverse osmosis membrane module is adapted to reversibly receive a feed flow through one of the first and second fluid inlet/outlet channels and produce a brine outflow through the other of the first and second inlet/outlet channels. 114-. (canceled)15. A system comprising:a first fluid inlet;a single reverse osmosis membrane module having a permeate outlet and a first inlet/outlet channel and a second fluid inlet/outlet channel in fluid communication with the first fluid inlet; andan energy transfer system having a second fluid inlet, a brine outlet, a first energy exchanging module and a second energy exchanging module, the first and second energy exchanging modules each in fluid communication with the second fluid inlet and the brine outlet in an expulsion flow phase and in fluid communication with the first and second fluid inlet/outlet channels of the single reverse osmosis membrane module in an energy recovery flow phase;wherein the first and second energy exchanging modules are adapted to reversibly operate in opposite flow phases where a flow direction for the expulsion flow phase in each energy exchanging module is constant and where a flow direction for the energy recover flow phase in each energy exchanging module is constant; andwherein the single reverse osmosis membrane ...

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03-01-2019 дата публикации

SPIRAL MEMBRANE ELEMENT

Номер: US20190001274A1
Принадлежит:

The object of the present invention is to provide a spiral membrane element that can make a composite semipermeable membrane high in effective membrane area, and that can restrain the composite semipermeable membrane from being lowered in rejection ratio by a deformation of this membrane while ensuring the flow rate of a permeation liquid flowing in a permeation-side flow-channel sufficiently. The spiral membrane element comprises a layered body which comprises a composite semipermeable membrane, a supply-side flow-channel member, and a permeation-side flow-channel member; and the permeation-side flow-channel member comprises a tricot knitted fabric having a plurality of ribs each formed by repeating loops in a linear form in a longitudinal direction, and a plurality of grooves present between the ribs; has a membrane support index of 60 to 135, the membrane support index being calculated in accordance with the specified numerical relationship. 1. A spiral membrane element , comprising: a layered body which comprises a composite semipermeable membrane having a porous support and a separating functional layer on/over a surface of the porous support , a supply-side flow-channel member , and a permeation-side flow-channel member; a perforated central pipe around which the layered body is wound; and a sealing portion that prevents a supply-side flow-channel from being mixed with a permeation-side flow-channel;the porous support of the composite semipermeable membrane having a thickness of 70 to 120 μm;the permeation-side flow-channel member comprising a tricot knitted fabric having a plurality of ribs each formed by repeating loops in a linear form in a longitudinal direction, and a plurality of grooves present between the ribs;the permeation-side flow-channel member having a membrane support index of 60 to 135, the membrane support index being calculated in accordance with “the number (wale) of grooves per 25-mm”×{rib width (mm)/groove width (mm)}, and{'sup': '2', 'the ...

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07-01-2021 дата публикации

ENVIRONMENTALLY FRIENDLY SEA WATER INTAKE PROCESS AND APPARATUS

Номер: US20210002146A1
Автор: LIBERMAN Boris
Принадлежит:

A sea water intake unit comprising a source of air (), a substantially vertical pipe () having an air inlet and a sea water inlet for air lifting sea water in the substantially vertical pipe to a height above sea level, the depth of the inlet below sea level being sufficient to promote air lifting of the sea water to the height above sea level. The air lift delivers sea water to a pre-treatment filter unit () in fluid communication with the vertical pipe in which the rate of flow of the sea water is such as to separate out small marine life in an upper portion of the water from the lower filtered portion, and a discharge pipe () to return at least some of the sea water and marine life back to the sea. The intake unit may deliver the lower filtered water to a desalination plant () provided on a disused offshore platform (). 1. A method for delivering sea water to a water treatment plant , the method comprising the steps of:(a) delivering air to at least one inlet in a substantially vertical pipe having at least one sea water inlet at a depth below sea level and air lifting sea water in the pipe to a height above sea level, the depth of the inlet below sea level being sufficient to promote air lifting of the sea water to said height above sea level;(b) passing at least part of the sea water through a pre-treatment filter media at a flow rate sufficiently low to retain small fish, eggs and other small marine life in another part of the sea water above the filter media;(c) discharging the small fish, eggs and other marine life to the sea with a proportion of the airlifted seawater; and(d) delivering the remaining proportion of sea water comprising the pre-treated filter water to a treatment plant.2. The method according to wherein the flow rate of the water passing through the filter media is less than 0.01 m per second or less than 10 mm per second.3. The method according to claim 1 , further comprising periodically backwashing said filter media.4. The method according ...

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07-01-2021 дата публикации

MEMBRANE FILTRATION APPARATUS AND PROCESS FOR REUSE OF INDUSTRIAL WASTEWATER

Номер: US20210002160A1
Принадлежит: KEMCO SYSTEMS CO. LLC.

Laundry, industrial or food processing wastewater is purified to the degree that it can be reused. Water quality is ensured through the final process of reverse osmosis (“RO”) which removes dissolved contaminants such as mineral hardness, soils and residual detergents. The process combines a ceramic tubular cross-flow membrane filter to remove the suspended solids, oils and greases ahead of the RO. The RO process employs high temperature, low fouling membranes. This enables the RO process to operate sustainably, i.e. without fouling, plugging or membrane degradation. 121-. (canceled)22. A water filter comprising a ceramic membrane filter system and a reverse osmosis membrane filter system , comprising:said ceramic membrane filter system includes:a source of water to be filtered;a first recirculation loop;said source of water connected to said first recirculation loop;a ceramic filter element in said first recirculation loop;said ceramic filter element includes abrasion resistant ceramic filter membranes;said abrasion resistant ceramic filter membranes of said ceramic filter elements are tubular and oriented in-line with the direction of the flow of said water;said tubular abrasion resistant ceramic filter membranes have pores, said pores have a diameter;particles in said water having a diameter greater than said diameter of said pores are retained within said recirculation loop;filtrate, which said filtrate is the cleaned water, is removed perpendicularly from said ceramic membrane filter system into to a filtrate discharge header;said reverse osmosis membrane filter system includes:a second recirculation loop:said filtrate of said ceramic membrane filter system connected to said second recirculation loop;a high temperature low fouling membrane assembly in said second recirculation loop;said high temperature low fouling membrane assembly includes: a perforated central tube which carries permeate axially therein; a spiral wound thin film polymeric concentric membrane ...

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07-01-2016 дата публикации

METHOD OF OPERATING REVERSE OSMOSIS MEMBRANE APPARATUS

Номер: US20160002071A1
Принадлежит: MITSUBISHI HEAVY INDUSTRIES, LTD.

To enable energy-saving operation and stable supply of permeate water while water quality level of the permeate water is satisfied during operation, clarified seawater sw subjected to pretreatment and stored in to-be-treated water tank is supplied to reverse osmosis membrane module via clarified seawater supply passage Permeate water pw obtained by an earlier stage element of the reverse osmosis membrane elements of the reverse osmosis membrane module is sent to a subsequent process from permeate water sending passage and permeate water pw obtained by the reverse osmosis membrane element is circulated into the to-be-treated water tank via permeate water circulation passage The flow rate of the clarified seawater sw supplied to the reverse osmosis membrane module is controlled by variable flow rate high-pressure pump provided in the clarified seawater supply passage and opening degree of flow regulating valve provided in the permeate water circulation passage is controlled, whereby the circulation flow rate of the permeate water is controlled. 1. A method of operating a reverse osmosis membrane apparatus employing a reverse osmosis membrane module having a plurality of reverse osmosis membrane elements arranged in series inside a high pressure vessel , and being configured to separate to-be-treated water obtained by pretreatment of raw water into concentrated water and permeate water with the reverse osmosis membrane elements sequentially from a first stage element of the reverse osmosis membrane elements , to mix the permeate water separated by a later stage element of the reverse osmosis membrane elements with the to-be-treated water , and to subject the mixture to re-separation by using the reverse osmosis membrane module , the method comprising:a membrane separation step of supplying the reverse osmosis membrane module with the to-be-treated water subjected to pretreatment and stored in a to-be-treated water tank, and separating the to-be-treated water into the ...

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07-01-2016 дата публикации

Reverse osmosis membrane apparatus and method of operating same

Номер: US20160002072A1
Принадлежит: Mitsubishi Heavy Industries Ltd

A reverse osmosis membrane apparatus has a plurality of high pressure vessels 12 a and 12 b in parallel with each other with respect to introducing passage 18 of clarified seawater obtained by subjecting raw seawater to sterilization and removal of relatively large foreign substances. The high pressure vessels 12 a and 12 b have first-stage reverse osmosis membrane elements 14 a and 14 b , respectively. Concentrated seawater subjected to membrane separation in the high pressure vessels 12 a and 12 b flows into a high pressure vessel 16 . In the high pressure vessel 16 , a plurality of reverse osmosis membrane elements 42 are arranged in series. When a detected value obtained by a differential pressure meter 56 a or 56 b provided for the high pressure vessel 12 a or 12 b exceeds a threshold value, introduction of the clarified seawater is stopped, and the reverse osmosis membrane element is washed or replaced.

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07-01-2016 дата публикации

ADVANCEMENTS IN OSMOTICALLY DRIVEN MEMBRANE SYSTEMS INCLUDING MULTI-STAGE PURIFICATION

Номер: US20160002074A1
Принадлежит: Porifera, Inc.

An example water purification system for purifying high concentration feed solutions includes a high rejection forward osmosis module, one or more low rejection modules, and a high rejection reverse osmosis module. The low rejection modules may have different rejection levels. The system may be pressurized by one or more pumps. One or more of the low rejection modules may include one or more nanofiltration (NF) membranes. The draw solution may comprise a monovalent salt, a multivalent salt, or a combination of both. 1. An apparatus , comprising:a forward osmosis module configured to receive a feed stream and a high concentration draw stream, wherein the forward osmosis module is further configured to produce a first stream comprising water from the feed stream and the high concentration draw stream;a pump configured to pressurize the first stream;a low rejection membrane module configured to receive the pressurized first stream and to produce the high concentration draw stream and a low concentration stream; anda reverse osmosis module configured to receive the low concentration stream and to produce a product stream and a reverse osmosis reject stream.2. The apparatus of claim 1 , further comprising a second pump configured to pressurize the low concentration stream provided to the reverse osmosis module.3. The apparatus of claim 1 , wherein the first stream is pressurized to less than 3000 psi.4. The apparatus of claim 1 , further comprising an energy recovery device configured to reduce the pressure of the high concentration draw stream produced by the low rejection module.5. The apparatus of claim 4 , wherein the energy recovery device and the pump are an integrated component.6. The apparatus of claim 1 , further comprising a feed pump configured to provide the feed stream to the forward osmosis module.7. The apparatus of claim 1 , wherein the reverse osmosis reject stream is combined with the first stream provided to the low rejection module.8. The apparatus of ...

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07-01-2016 дата публикации

MULTIVALENT ION SEPARATING DESALINATION PROCESS AND SYSTEM

Номер: US20160002082A1
Принадлежит: Saltworks Technologies Inc.

A multivalent ion separating desalination system and associated process employs at least one multivalent ion separator subsystem to split sparingly soluble multivalent ion species from saltwater into highly soluble salts comprising multivalent cations and monovalent anions and salts comprising monovalent cations and multivalent anions. 1. A process for desalinating saltwater , the input saltwater comprising multivalent ion pairs and the process comprising:(a) circulating the input saltwater through a common fluid circuit comprising a multivalent cation-extracting branch and a multivalent anion-extracting branch, wherein a portion of the cation-extracting branch and a portion of the anion-extracting branch are distinct from each other;(b) removing multivalent cations from the input saltwater when the input saltwater is in the portion of the cation-extracting branch distinct from the anion-extracting branch, wherein the multivalent cations are removed using a multivalent cation-extracting stack comprising alternating cation exchange membranes and monovalent anion exchange membranes; and(c) removing multivalent anions from the input saltwater when the input saltwater is in the portion of the anion-extracting branch distinct from the cation-extracting branch, wherein the multivalent anions are removed using a multivalent anion-extracting stack comprising alternating anion exchange membranes and monovalent cation exchange membranes.2. The process of further comprising:(a) transferring the multivalent cations removed from the input saltwater to a multivalent cation fluid circuit distinct from the common fluid circuit; and(b) transferring the multivalent anions removed from the input saltwater to a multivalent anion fluid circuit distinct from the common fluid circuit and the multivalent cation fluid circuit.3. The process of or further comprising adding monovalent ion species to the input saltwater upstream of the portions of the anion-extracting and cation-extracting ...

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05-01-2017 дата публикации

WATER TREATMENT SYSTEM AND WATER TREATMENT METHOD

Номер: US20170001883A1
Принадлежит: Hitachi, Ltd.

Provided are a water treatment system and a water treatment method capable of downsizing a facility and inexpensively producing freshwater. A water treatment system includes: a first reverse osmosis treatment device for separating wastewater into desalinated permeate water and concentrated wastewater; a mixing unit for mixing the separated concentrated wastewater and intake seawater; a second reverse osmosis treatment device for separating mixed water obtained by mixing the concentrated wastewater and the seawater into desalinated permeate water and concentrated mixed water; and a return pipe for returning a portion of the separated concentrated mixed water to the mixing unit. The water treatment method includes the following steps: mixing intake seawater with wastewater; separating the mixed water into permeate water and concentrated mixed water; re-mixing a portion of the concentrated mixed water with the mixed water; and producing freshwater by re-separating the re-mixed water into permeate water and concentrated mixed water. 1. A water treatment system , comprising:a first reverse osmosis treatment device for separating wastewater or treated wastewater into desalinated permeate water and concentrated wastewater by reverse osmosis treatment;a mixing unit for mixing the separated concentrated wastewater and intake seawater;a second reverse osmosis treatment device for separating mixed water obtained by mixing the concentrated wastewater and the seawater into desalinated permeate water and concentrated mixed water by reverse osmosis treatment; anda return pipe for returning a portion of the separated concentrated mixed water to the mixing unit.2. The water treatment system according to claim 1 , further comprisinga supply pipe for supplying the wastewater or the treated wastewater to the mixing unit.3. A water treatment method comprising the following steps:mixing intake seawater with wastewater or treated wastewater;separating mixed water obtained by mixing the ...

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05-01-2017 дата публикации

Fluid Treatment Methods and Systems

Номер: US20170001890A1
Принадлежит: EnergySolutions, Inc.

Methods and systems for treatment of wastewater. In some embodiments, the system may comprise one or more modules such as an electrochemical module, an electrocoagulation module, a flotation module, an evaporation module, and an ultrafiltration module. One or more detection modules may also be provided to analyze the concentration of one or more wastewater components in the wastewater. Data from such modules may be used to adjust one or more operational parameters or conditions in the treatment system. The system may also comprise one or more features designed to minimize adverse effects on the environment, such as avoiding adding chemicals to the stream, extracting salt or other chemicals for re-use, and/or use of carbon dioxide gas from on-site combustion processes. 113-. (canceled)14. A method for treating wastewater comprising:analyzing the composition of the wastewater in real-time to produce real-time data;modifying one or more modules or parameters in a wastewater treatment system using the real-time data; andincreasing a pH of the wastewater using an electrochemical treatment process and without adding any chemicals to the wastewater.15. The method of wherein the composition of the wastewater is analyzed before the water is treated by the wastewater treatment system.16. The method of wherein analyzing the composition of the wastewater includes analyzing the composition of the wastewater using Laser-Induced Breakdown Spectroscopy.17. The method of wherein analyzing the composition of the wastewater includes analyzing the concentration of one or more constituents in the wastewater.18. The method of wherein modifying one or more modules or parameters in the wastewater treatment system comprises at least one of disabling one or more modules in the wastewater treatment system claim 14 , adjusting an operational parameter of one or more modules in the wastewater treatment system claim 14 , diverting the wastewater to bypass one or more modules in the wastewater ...

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04-01-2018 дата публикации

WATER-SAVINGS ADIABATIC SPRAY SYSTEM

Номер: US20180002198A1
Принадлежит:

A water savings system and method for reducing the amount of water needed for adiabatic cooling including the use of a softener and a reverse osmosis device, in which tap water, softened if necessary, is delivered to a reverse osmosis device and softened water alone, reverse osmosis reject water, or softened water combined with reverse osmosis reject water is delivered to spray nozzles for cooling, and reverse osmosis pure water is stored and used periodically to flush the coils to inhibit and/or prevent corrosion from dissolved salts and other solids in the spray water. 1. A water supply system for delivering cooling water to a heat exchanger , comprising:a water softener configured to receive water from a water source;a reverse osmosis device configured to receive softened water from said water softener;an RO-permeate storage tank configured to receive RO-permeate water from said reverse osmosis device;a spray pump configured to deliver softened water to spray nozzles;a flush pump configured to deliver RO-permeate water from said RO-permeate storage tank to surfaces of coils of said heat exchanger.2. A water supply system according to claim 1 , further comprising a RO-reject storage tank configured to receive RO-reject water from said reverse osmosis device; wherein said spray pump is configured to receive cooling water from said RO-reject storage tank for delivery to said spray nozzles.3. A water supply system according to claim 2 , wherein said system is piped to permit delivery of RO-permeate water in said RO-permeate storage tank to said spray nozzles via said spray pump.4. A water supply system according to claim 1 , further comprising a combining and storage tank configured to receive softened water directly from said softener claim 1 , and RO-reject water from said reverse osmosis device claim 1 , and wherein said spray pump is configured to deliver combined water softened and RO-reject water from said combining and storage tank to said spray nozzles.5. A ...

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02-01-2020 дата публикации

Ultraviolet light activated oxidation process for the reduction of organic carbon in semiconductor process water

Номер: US20200002198A1
Принадлежит: Evoqua Water Technologies LLC

In a system for decomposing organic compounds in water for use in semiconductor manufacturing, a chemical reactor vessel having a fluid inlet and a fluid outlet, a persulfate anion addition system upstream of the reactor vessel, and a light emitting device contained within the reactor vessel. The light emitting device provides light capable of decomposing persulfate anions.

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04-01-2018 дата публикации

Treating Water

Номер: US20180002212A1
Автор: Englram Paul
Принадлежит:

Systems and methods for treating produced water and/or flowback water from fracking operations include: an oil water separator; a first filter downstream of the oil water separator; and an electrocoagulation unit downstream of the first filter. Systems and methods can be used for producing a concentrated brine for use in industrial applications and a separate stream of fresh water 1. A system for treating produced water and/or flowback water from fracking operations , the system comprising:an oil water separator;a first filter downstream of the oil water separator; andan electrocoagulation unit downstream of the first filter.2. The system of claim 1 , wherein the oil water separator comprises a housing claim 1 , a specific gravity section claim 1 , a gas flotation system downstream of the specific gravity section claim 1 , and the coalescing media pack downstream of the gas flotation system claim 1 , wherein the specific gravity section claim 1 , the gas flotation system claim 1 , and the coalescing media pack are disposed within the housing.3. The system of claim 2 , wherein the gas flotation system comprises a source of an oxygenated gas and a distribution element configured to impart the oxygenated gas into water being treated in the form of microbubbles.4. The system of claim 3 , wherein the oxygenated gas comprises air.5. The system of claim 3 , wherein the microbubbles have a characteristics size of between 5 and 50 microns.6. The system of claim 1 , wherein the first filter comprises an oleophilic media.7. The system of claim 1 , comprising a clarifier downstream of the electrocoagulation unit.8. The system of claim 7 , comprising a reverse osmosis system downstream of the clarifier.9. The system of claim 8 , comprising a second filter downstream of the clarifier and upstream of the reverse osmosis system.10. The system of claim 8 , comprising an ion exchange system downstream of the clarifier and upstream of the reverse osmosis system.11. The system of claim ...

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03-01-2019 дата публикации

METHOD AND AN APPARATUS FOR MONITORING AND CONTROLLING DEPOSIT FORMATION

Номер: US20190002304A1
Принадлежит: KEMIRA OYJ

A method and apparatus for monitoring deposit formation in a process having an aqueous flow is provided. According to exemplary embodiments, a feed flow of an aqueous liquid is provided onto a receiving surface to be monitored. At least part of a receiving surface is illuminated with at least one light source. Visual data is collected across the receiving surface and analyzed. The quality and type of deposition attached to the receiving surface is classified based on information obtained from the analyzed visual data, and a quantitative scaling and/or fouling indication is computed based on the classification. 1. A method for monitoring deposit formation in a process involving an aqueous flow , said method comprising:providing a feed flow of an aqueous liquid onto a receiving surface to be monitored, wherein the monitoring includes:illuminating at least part of said receiving surface with at least one light source;collecting visual data at a multitude of positions across said receiving surface;analyzing said visual data;classifying a quality and type of deposition attached to said receiving surface based on information obtained from said analyzed visual data; andcomputing a quantitative scaling and/or fouling indication of said receiving surface based on said classification.2. A method according to claim 1 , wherein the method comprises:adding to said feed flow of an aqueous liquid at least one fluorescent dye capable of staining at least one type of microbes;illuminating at least part of said receiving surface with at least two light sources, at least one of which uses light with a selected wavelength that excites a biofouling deposition stained by said at least one fluorescent dye; andclassifying a quality and type of biofouling deposition on said receiving surface based on fluorescence emission from said depositions in said analyzed visual data.3. A method according to claim 1 , wherein at least one of said light sources is emitting ultraviolet light.4. A method ...

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05-01-2017 дата публикации

CATALYTIC FAST PYROLYSIS PROCESS WITH IMPURITY REMOVAL

Номер: US20170002270A1
Принадлежит:

The present invention provides an improved catalytic fast pyrolysis process for increased yield of useful and desirable products. In particular, the process comprises an improved catalytic fast pyrolysis process for producing aromatic compounds, such as, for example, benzene, toluene and xylenes, from biomass feedstock containing impurities, such as, for example alkali and alkaline earth metal, sulfur and nitrogen components. 1. An improved catalytic fast pyrolysis process comprising steps of:a) treating biomass containing alkali and alkaline earth metal components to reduce alkali and alkaline earth metal content to result in treated biomass,b) feeding the treated biomass of step a), catalyst composition, and transport fluid to a catalytic fast pyrolysis process fluidized bed reactor maintained at reaction conditions to manufacture a raw fluid product stream,c) feeding the raw fluid product stream of step b) to a solids separation and stripping system to produce separated solids and a fluid product stream,d) feeding the fluid product stream of step c) to a vapor/liquid separation system to produce a liquid phase stream comprising components selected from the group consisting of water, char, coke, ash, catalyst fines, water soluble organics and heavy organics, and combinations thereof, and a vapor phase stream comprising benzene, toluene xylenes, olefins having carbon numbers of 2 to 4, methane, carbon monoxide, and carbon dioxide, ande) feeding the vapor phase stream of step d) to a product recovery system to recover benzene, toluene, xylenes and, optionally, olefins.2. The process of wherein step a) comprises steps 1) sizing the biomass to ≦20 cm size particles claim 1 , 2) washing the sized biomass of step 1) in at least one washing cycle with a washing fluid sufficiently to reduce the content of alkali and alkaline earth metals claim 1 , 3) optionally rinsing the washed biomass of step 2) with rinsing fluid claim 1 , 4) drying the biomass to reduce water content ...

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05-01-2017 дата публикации

Thermal Power Plant for Recovering Water from Exhaust Gas and a Method for Treating Recovered Water of Thermal Power Plant Thereof

Номер: US20170002694A1
Принадлежит:

A thermal power plant for recovering water from exhaust gas comprising: a gas turbine; a heat recovery steam generator for generating steam by supplying exhaust combustion gas exhausted from the gas turbine as heat source; a water recovery system installed on the downstream side of the heat recovery steam generator for condensing and recovering water in the exhaust combustion gas through direct gas/liquid contact between the exhaust combustion gas coming down from the heat recovery steam generator and water; a recovered water system for supplying a part of the water recovered by the water recovery system, thereby allowing the water to be circulating as circulating water; a feed water system for supplying the heat recovery steam generator with other part of the water recovered by the water recovery system as feed water; a first pH adjusting system installed in the recovered water system to adjust the circulating water flowing through the recovered water system to a first pH value (hydrogen ion concentration index); a second pH adjusting system installed on the feed water system to adjust the feed water flowing through the feed water system to a second pH value (hydrogen ion concentration index); and a control system for controlling the volumes of the pH adjusters supplied from the first pH adjusting system and the second pH adjusting system. 1. A thermal power plant for recovering water from exhaust gas comprising:a gas turbine;a heat recovery steam generator for generating steam by supplying exhaust combustion gas exhausted from the gas turbine as heat source;a water recovery system installed on the downstream side of the heat recovery steam generator for condensing and recovering water in the exhaust combustion gas through direct gas/liquid contact between the exhaust combustion gas coming down from the heat recovery steam generator and water;a recovered water system for supplying a part of the water recovered by the water recovery system, thereby allowing the ...

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02-01-2020 дата публикации

SUBMERGED REVERSE OSMOSIS SYSTEM

Номер: US20200003232A1
Принадлежит:

A submersible reverse osmosis desalination apparatus and method employs airlift to remove desalinated water from the apparatus via as annular flow regime over a substantial portion of the product water discharge conduit. Use of a high air fraction for airlift operation and an annular flow regime significantly lowers the weight of the product water column, as well as the backpressure on the downstream side of the osmotic membranes and at the bottom of the discharge water conduit. This permits deployment of the apparatus at reduced depths and in many eases closer to shore. In preferred embodiments the apparatus relies wholly upon hydrostatic pressure to drive seawater through the osmotic membranes, and continuously desalinates seawater and delivers pure water to the discharge water conduit without using any submerged moving parts subject to wear or breakage. 138-. (canceled)39. A submerged reverse osmosis desalination system comprising a reverse osmosis desalination apparatus comprising:a) one or more submerged osmotic membranes each having an inlet surface supplied with saltwater at least partially under hydrostatic pressure and an outlet surface that provides desalinated water to a submerged product water collector in fluid communication with the outlet surface(s),b) an air supply for removing water from the collector via airlift, andc) an at least partially submerged water discharge conduit in fluid communication with the collector and containing desalinated water lifted by the supplied air in an annular flow regime over 10% or more of the airlift depth.40. A system according to wherein the apparatus relies wholly upon hydrostatic pressure to drive seawater through the osmotic membranes.41. A system according to wherein the apparatus does not include submerged frictional sliding surfaces claim 39 , a submerged mechanical pump or a submerged valve.42. A system according to wherein the air supply further comprises an onshore claim 39 , ship-borne or platform-mounted ...

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13-01-2022 дата публикации

SYSTEMS AND METHODS FOR SUPPLYING LOW SALINITY INJECTION WATER

Номер: US20220008868A1

A desalination system includes a desalination platform, a first skid disposed on a first deck of the desalination platform, the first skid including at least one of a first filtration unit configured to produce a first filtrate stream, and a first permeate unit configured to produce a first permeate stream, a first interconnecting pipework coupled to the first skid, and a first pipework support disposed on the first deck, wherein the first interconnecting pipework is disposed on the first pipework support. 1. A desalination system , comprising:a desalination platform;a first skid disposed on a first deck of the desalination platform, the first skid comprising at least one of a first filtration unit configured to produce a first filtrate stream, and a first permeate unit configured to produce a first permeate stream;a first interconnecting pipework coupled to the first skid; anda first pipework support disposed on the first deck, wherein the first interconnecting pipework is disposed on the first pipework support.2. The desalination system of claim 1 , wherein:the first skid comprises a membrane skid and the first permeate unit comprises a reverse osmosis (RO) membrane separation unit; andthe first permeate stream comprises a RO permeate stream.3. The desalination system of claim 1 , wherein:the first skid comprises an ultrafiltration (UF) skid and the first filtration unit comprises an UF filtration unit; andthe first filtrate stream comprises an UF filtrate stream.4. The desalination system of claim 1 , wherein the interconnecting pipework is configured receive at least one of the first filtrate stream and the first permeate stream from the first skid claim 1 , and provide an inlet feed stream to the first skid.5. The desalination system of claim 1 , wherein the first skid comprises:a support structure comprising an upper frame positioned at a top of the first skid and a lower frame positioned at a base of the first skid;an inlet pipework coupled between an inlet ...

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08-01-2015 дата публикации

HOLLOW FIBER TYPE SEMIPERMEABLE MEMBRANE, METHOD FOR MANUFACTURING THE SAME, MODULE, AND WATER TREATMENT METHOD

Номер: US20150008185A1
Принадлежит: TOYOBO CO., LTD.

A hollow fiber type semipermeable membrane which achieves both water permeability and selectivity in high level and performs efficient treatment using small membrane area utilizing the concentration difference from high concentration liquid having high osmotic pressure. The hollow fiber type semipermeable membrane is characterized in that, when an aqueous solution of 25° C. having NaCl concentration of 35 g/L and pressure of 1.0 MPa is flown into an outer side of the hollow fiber type semipermeable membrane having length of about 70 cm while freshwater of 25° C. having NaCl concentration of 0 g/L is flown into an inner side of one open end of the hollow fiber type semipermeable membrane and discharged from another open end at 10 kPa or less, the permeation flow rate is 30 to 70 L/m/day. An inner diameter thereof is 50 to 200 μm; and the hollow ratio thereof is 24 to 42%. 1. A hollow fiber type semipermeable membrane which is characterized in that , when an aqueous solution of 25° C. having sodium chloride concentration of 35 g/L and pressure of 1.0 MPa is flown into and contacted with an outer side of the hollow fiber type semipermeable membrane having length of about 70 cm while freshwater of 25° C. having sodium chloride concentration of 0 g/L is flown into an inner side of one open end of the hollow fiber type semipermeable membrane and discharged from another open end at 10 kPa or less , the permeation flow rate is 30 to 70 L/m/day , wherein said permeation flow rate is measured under such a condition that twice of the permeation flow rate flown from the inner side to the outer side of the hollow fiber type semipermeable membrane utilizing the concentration difference as a driving force is equal to a flow rate flown into the outer side of the hollow fiber type semipermeable membrane and that the discharged flow rate from the inner side of the hollow fiber type semipermeable membrane is equal to 10% of said permeation flow rate; the hollow fiber type ...

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03-01-2019 дата публикации

Microbial fuel cell arrangement and method for operating it

Номер: US20190006693A1
Принадлежит: KEMIRA OYJ

The invention relates to a microbial fuel cell arrangement comprising a cell reactor. The cell reactor comprises a membrane, which has an active surface and a support surface, as well as a pore size of ≤10 nm and/or a divalent ion rejection of ≥50%; an anode and a cathode, which are connected with each other through an external electrical circuit; an influent inlet for liquid medium arranged at the active surface side of the membrane and at least one permeate outlet arranged at the support surface side of the membrane; an influent line connected to the influent inlet; a concentrate outlet, arranged at the active surface side of the membrane and connected to a concentrate line; and pressurisation means for creating pressure difference between the active surface side and support surface side of the membrane. The invention relates also to a method for operating a microbial fuel cell.

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12-01-2017 дата публикации

Antimicrobial Batch Dilution System

Номер: US20170008783A1
Принадлежит:

An antimicrobial supply system employs a process water supply and incorporates a metallic ion supply connected to the process water supply to provide a high ion concentrate to an output. A dilution reservoir is connected to the metallic ion supply output and has an input from the process water supply. A pump is connected to an output of the reservoir. A manifold connected to the pump provides a dilute concentrate to at least one washing system and a recirculation loop to the dilution reservoir for enhanced mixing of the dilute concentrate. An electronics control module is connected to a first flow controller between the process water supply and the metallic ion supply and a second flow controller between the metallic ion supply and the reservoir for dilution control establishing a desired metallic ion concentration. 112-. (canceled)13. An antimicrobial supply system comprising:a process water supply;a metallic ion supply comprising an output for providing a high metal ion concentrate;a dilution reservoir connected to the metallic ion supply output and having an input from the process water supply;a manifold connected to an output of the reservoir and at least one washing system, and,an electronics control module connected to a first flow controller between the process water supply and the reservoir and a second flow controller between the metallic ion supply and the reservoir, wherein the controller controls a concentration of a dilute concentrate comprising the metal ion concentrate and process water in the dilution reservoir.14. The antimicrobial supply system of claim 13 , wherein the electronics control module is connected to a third flow controller that controls the flow of the dilute concentrate to the at least one wash system.15. The antimicrobial supply system of claim 13 , wherein the process water supply comprises a deionizer.15. The antimicrobial supply system of claim 13 , wherein the process water supply comprises a reverse osmosis filter.16. The ...

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11-01-2018 дата публикации

Liquid Purification System

Номер: US20180008934A1
Принадлежит:

A liquid purification system includes a system raw liquid feed unit and a filtration unit, which includes a liquid concentration device having an internal partition dividing a variable volume collection cavity for raw liquid coming from an initial stage of liquid filtration and for mixing therein concentrate and a raw liquid displacement cavity. The cavity is connected to a secondary line that supplies raw liquid to the cavity to displace concentrate from the collection cavity and to recycle raw liquid from the displacement cavity through the secondary line under pressure exerted by concentrate and raw liquid in the collection cavity. A filtration unit provides long-term contact between raw liquid and concentrate in the variable-volume collection cavity to provide smooth increase in the concentration of liquid supplied to a liquid purification device. 1. A liquid purification system comprising: a container,', 'a primary raw liquid supply line, and', 'a secondary raw liquid supply line having an inlet connected via a connection element to the primary raw liquid supply line before a pressurizing means mounted in the primary raw liquid supply line,', 'wherein an outlet of the secondary raw liquid supply line is connected to the container;, 'a system raw liquid feed unit comprising a mixing line configured to mix concentrate formed by a liquid filtration cycle with raw liquid, the mixing line connected via a connection element to the primary raw liquid supply line after the pressurizing means,', 'at least one liquid purification means connected with liquid velocity increasing means,', 'a recycling line configured to recycle at least a portion of the concentrate to the container, the recycling line connected to a concentrate exit of the at least one liquid purification means,', 'a drain discharge line with a drain discharge valve mounted thereon,', 'a purified liquid supply line connected to a purified liquid exit of the at least one liquid purification means,, 'a ...

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14-01-2016 дата публикации

Membrane filtration system

Номер: US20160009572A1
Принадлежит: Toshiba Corp

According to one embodiment, a membrane filtration system includes a raw water tank, a pretreatment membrane module, a raw water feed line, a high-pressure RO membrane module, a high-pressure line, a preceding power recovery unit which pressurize the pretreated water by transmitting the pressure of the concentrate to the pretreated water, a succeeding power recovery unit which pressurize the raw water by transmitting a remaining pressure of the concentrate to the raw water, a concentrate discharge line, a first pressure transmission line communicating to the power recovery unit by being branched from the high-pressure line, a second pressure transmission line communicating to the power recovery unit by being branched from the raw water feed line, and a valve provided in the drain line to regulate a discharge of the concentrate from the power recovery unit in accordance with a pressure loss in the pretreatment membrane module.

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14-01-2016 дата публикации

Methods and Systems For Treating Produced Water

Номер: US20160009582A1
Принадлежит:

Produced water from a crude oil or natural gas production process is purified using a membrane purification system for petroleum production, agricultural, commercial and domestic uses. The produced water is pretreated to remove, at least, particulates and oil from the produced water. The minimally pretreated water is then purified in a membrane purification system, that is operated at conditions such that membrane scaling is reduced or prevented. In particular, the membrane purification system is operated to maintain the turbidity of clarified water feed to the system or intermediate aqueous streams that are cascading through the membrane purification system. Ensuring that the turbidity of the reject streams generated in the membrane system are useful in achieving long membrane operating life. 2. The method of claim 1 , wherein the first pH is in a range from 9 to 11.5 and the second pH is in a range from 3 to 7.9 claim 1 , and wherein the first permeate stream contains at most 0.5 mg/L boron.3. The method of claim 1 , wherein the first pH is in a range from 3 to 7.9 and the second pH is in a range from 9 to 11.5 claim 1 , and wherein the first permeate stream contains at most 25 mg/L ammonia.4. The method of claim 1 , wherein pretreating the produced water includes filtering the produced water using microfiltration claim 1 , ultrafiltration claim 1 , nanofiltration and combinations thereof.5. The method of claim 1 , further comprising passing the produced water through an ultrafiltration membrane claim 1 , wherein the produced water contains greater than 100 claim 1 ,000 ppm TDS.6. The method of claim 1 , wherein pretreating the produced water includes partially softening the produced water to a hardness in a range from 1 to 50 ppm.7. The method of claim 6 , wherein partially softening the produced water warm lime softening at a temperature in a range from 150° F. to 200° F.8. The method of claim 7 , further comprising partially softening produced water containing ...

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