Настройки

Укажите год
-

Небесная энциклопедия

Космические корабли и станции, автоматические КА и методы их проектирования, бортовые комплексы управления, системы и средства жизнеобеспечения, особенности технологии производства ракетно-космических систем

Подробнее
-

Мониторинг СМИ

Мониторинг СМИ и социальных сетей. Сканирование интернета, новостных сайтов, специализированных контентных площадок на базе мессенджеров. Гибкие настройки фильтров и первоначальных источников.

Подробнее

Форма поиска

Поддерживает ввод нескольких поисковых фраз (по одной на строку). При поиске обеспечивает поддержку морфологии русского и английского языка
Ведите корректный номера.
Ведите корректный номера.
Ведите корректный номера.
Ведите корректный номера.
Укажите год
Укажите год

Применить Всего найдено 35472. Отображено 100.
05-01-2012 дата публикации

Hydrophobic magnetic particles

Номер: US20120003689A1

A process for making a particulate material comprising mesoporous particles having granules of a metal containing species in at least some of the pores thereof, said process comprising: allowing a compound of the metal to enter pores of hydrophobic mesoporous particles, said compound being thermally decomposable at a decomposition temperature to form a metal containing species and said particles being substantially thermally stable at said decomposition temperature; and heating the hydrophobic mesoporous particles having the compound in the pores thereof to the decomposition temperature so as to decompose the compound and to form the mesoporous particles having granules of the metal containing species in at least some of the pores thereof.

Подробнее
27-03-2006 дата публикации

УСТАНОВКА ДЛЯ ИЗГОТОВЛЕНИЯ КАТАЛИЗАТОРА ДЛЯ РЕКОМБИНАЦИИ ВОДОРОДА И КИСЛОРОДА

Номер: RU0000052341U1

1. Установка для изготовления катализатора для рекомбинации водорода и кислорода, выполненного в виде пакета каталитических элементов на основе керамических носителей, содержащая ванны с пропиточным раствором и суспензией гидрофобизатора и печь для прокаливания элементов в процессе их изготовления, отличающаяся тем, что она дополнительно содержит устанавливаемый над указанными ваннами штатив с закрепленными на них держателями для подвешивания каталитических элементов. 2. Установка по п.1, отличающаяся тем, что она дополнительно содержит соединенный со штативом вибратор. РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) 52 341 (13) U1 (51) МПК B01J 37/02 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ, ПАТЕНТАМ И ТОВАРНЫМ ЗНАКАМ (12) ОПИСАНИЕ ПОЛЕЗНОЙ МОДЕЛИ К ПАТЕНТУ (21), (22) Заявка: 2005136238/22 , 23.11.2005 (24) Дата начала отсчета срока действия патента: 23.11.2005 (45) Опубликовано: 27.03.2006 (73) Патентообладатель(и): Закрытое Акционерное Общество Инвестиционная Научно-производственная Компания РУССКИЕ ЭНЕРГЕТИЧЕСКИЕ ТЕХНОЛОГИИ (RU) U 1 5 2 3 4 1 R U Ñòðàíèöà: 1 U 1 Формула полезной модели 1. Установка для изготовления катализатора для рекомбинации водорода и кислорода, выполненного в виде пакета каталитических элементов на основе керамических носителей, содержащая ванны с пропиточным раствором и суспензией гидрофобизатора и печь для прокаливания элементов в процессе их изготовления, отличающаяся тем, что она дополнительно содержит устанавливаемый над указанными ваннами штатив с закрепленными на них держателями для подвешивания каталитических элементов. 2. Установка по п.1, отличающаяся тем, что она дополнительно содержит соединенный со штативом вибратор. 5 2 3 4 1 (54) УСТАНОВКА ДЛЯ ИЗГОТОВЛЕНИЯ КАТАЛИЗАТОРА ДЛЯ РЕКОМБИНАЦИИ ВОДОРОДА И КИСЛОРОДА R U Адрес для переписки: 111024, Москва, ул. Войтовича, 46А, 14/23, ЗАО ИНПК РЭТ (72) Автор(ы): Келлер Владимир Дмитриевич (RU), Кошманов Дмитрий Евгеньевич (RU), Шепелин Владимир Андреевич (RU) U 1 U 1 5 2 3 4 1 5 ...

Подробнее
10-03-2007 дата публикации

КАТАЛИТИЧЕСКИЕ МИКРОКАНАЛЬНЫЕ ПЛАСТИНЫ

Номер: RU0000061589U1

1. Каталитические микроканальные пластины, характеризующиеся тем, что в качестве пористого металлического носителя они содержат пенометаллы различной пористости, металлический войлок, металлическую вату, количество каналов составляет от 2 до 30 штук на 1 см длины и зависит от размера пор в металле, при этом ширина канала и ширина стенки между каналами должна как минимум в пять раз быть больше размера пор в используемом металле. 2. Каталитические микроканальные пластины, отличающиеся тем, что каналы расположены как с одной стороны, так и на обеих сторонах пластины. РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) 61 589 (13) U1 (51) МПК B01J 37/025 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ, ПАТЕНТАМ И ТОВАРНЫМ ЗНАКАМ (12) ОПИСАНИЕ ПОЛЕЗНОЙ МОДЕЛИ К ПАТЕНТУ Адрес для переписки: 630090, г.Новосибирск, пр. Академика Лаврентьева, 5, Институт катализа им. Г.К. Борескова, патентный отдел, Т.Д. Юдиной (73) Патентообладатель(и): Институт катализа им. Г.К. Борескова Сибирского отделения Российской Академии наук (RU) (24) Дата начала отсчета срока действия патента: 29.06.2006 U 1 6 1 5 8 9 R U Ñòðàíèöà: 1 U 1 Формула полезной модели 1. Каталитические микроканальные пластины, характеризующиеся тем, что в качестве пористого металлического носителя они содержат пенометаллы различной пористости, металлический войлок, металлическую вату, количество каналов составляет от 2 до 30 штук на 1 см длины и зависит от размера пор в металле, при этом ширина канала и ширина стенки между каналами должна как минимум в пять раз быть больше размера пор в используемом металле. 2. Каталитические микроканальные пластины, отличающиеся тем, что каналы расположены как с одной стороны, так и на обеих сторонах пластины. 6 1 5 8 9 (54) КАТАЛИТИЧЕСКИЕ МИКРОКАНАЛЬНЫЕ ПЛАСТИНЫ R U (45) Опубликовано: 10.03.2007 (72) Автор(ы): Макаршин Лев Львович (RU), Грибовский Александр Георгиевич (RU), Андреев Дмитрий Валерьевич (RU), Пармон Валентин Николаевич (RU) (21), (22) Заявка: 2006123228/22 , 29.06.2006 RU 5 ...

Подробнее
27-10-2008 дата публикации

УСТАНОВКА ДЛЯ ПОЛУЧЕНИЯ ЭЛЕКТРОКАТАЛИТИЧЕСКОЙ КОМПОЗИЦИИ

Номер: RU0000077609U1

1. Установка для получения электрокаталитической композиции, содержащая аппарат для полимеризации пиррола, бункеры с исходными реагентами, соединенные с рабочей камерой аппарата, отличающаяся тем, что она дополнительно снабжена контейнером, заполненным радикальным инициатором, и контейнером с органическим растворителем, оснащена смесителем этих компонентов, аппарат также оснащен вакуум-насосом и инициатором в виде излучателя акустических волн ультразвукового диапазона частот; рабочая камера аппарата и смеситель имеют устройства для регулирования температуры композиционной системы, при этом аппарат своим входным патрубком соединен со смесителем, а выходным патрубком - с камерой, сообщенной с емкостью, заполненной органическим растворителем. 2. Установка по п.1, отличающаяся тем, что бункеры заполнены реагентами, соответственно, один - платинированной сажей, второй - поверхностно-активной добавкой. 3. Установка по п.1 или 2, отличающаяся тем, что второй бункер заполнен продуктом взаимодействия третичного амина и окиси пропилена в этилцеллозольве. РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) 77 609 (13) U1 (51) МПК C08G 83/00 (2006.01) B01J 37/00 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ, ПАТЕНТАМ И ТОВАРНЫМ ЗНАКАМ (12) ОПИСАНИЕ ПОЛЕЗНОЙ МОДЕЛИ К ПАТЕНТУ (21), (22) Заявка: 2008107058/22 , 27.02.2008 (24) Дата начала отсчета срока действия патента: 27.02.2008 (45) Опубликовано: 27.10.2008 (73) Патентообладатель(и): Институт Высокомолекулярных соединений Российской академии наук (ИВС РАН) (RU) Ñòðàíèöà: 1 U 1 7 7 6 0 9 U 1 Формула полезной модели 1. Установка для получения электрокаталитической композиции, содержащая аппарат для полимеризации пиррола, бункеры с исходными реагентами, соединенные с рабочей камерой аппарата, отличающаяся тем, что она дополнительно снабжена контейнером, заполненным радикальным инициатором, и контейнером с органическим растворителем, оснащена смесителем этих компонентов, аппарат также оснащен вакуум-насосом и инициатором в виде ...

Подробнее
27-06-2012 дата публикации

УСТАНОВКА ДЛЯ ПОЛУЧЕНИЯ ФОТОКАТАЛИЗАТОРА

Номер: RU0000117318U1

Установка для получения фотокатализатора, содержащая устройство для внедрения в соединения титана химических элементов, отличающаяся тем, что устройство для внедрения в соединения титана химических элементов выполнено в виде двух ионных имплантеров, один - на основе тлеющего разряда низкого давления в магнитном поле для имплантации газовых ионов, второй - на основе дуги с катодным пятном для имплантации ионов металлов, а установка дополнительно содержит вакуумную имплантационную камеру и связанный с ней турбомолекулярный насос. РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 117 318 U1 (51) МПК B01J 37/34 (2006.01) B01J 21/06 (2006.01) B01J 19/12 (2006.01) C23C 14/02 (2006.01) C01G 23/047 (2006.01) B82B 3/00 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ (21)(22) Заявка: ПОЛЕЗНОЙ МОДЕЛИ К ПАТЕНТУ 2011151358/04, 15.12.2011 (24) Дата начала отсчета срока действия патента: 15.12.2011 (45) Опубликовано: 27.06.2012 Бюл. № 18 R U 1 1 7 3 1 8 Формула полезной модели Установка для получения фотокатализатора, содержащая устройство для внедрения в соединения титана химических элементов, отличающаяся тем, что устройство для внедрения в соединения титана химических элементов выполнено в виде двух ионных имплантеров, один - на основе тлеющего разряда низкого давления в магнитном поле для имплантации газовых ионов, второй - на основе дуги с катодным пятном для имплантации ионов металлов, а установка дополнительно содержит вакуумную имплантационную камеру и связанный с ней турбомолекулярный насос. Стр.: 1 U 1 U 1 (54) УСТАНОВКА ДЛЯ ПОЛУЧЕНИЯ ФОТОКАТАЛИЗАТОРА 1 1 7 3 1 8 Адрес для переписки: 620078, г.Екатеринбург, ул. Комсомольская, 61, оф.202, А.Н. Черепанову (73) Патентообладатель(и): Общество с ограниченной ответственностью "Центр детекторных технологий" (RU) R U Приоритет(ы): (22) Дата подачи заявки: 15.12.2011 (72) Автор(ы): Гаврилов Николай Васильевич (RU), Чолох Сеиф Османович (RU), Черепанов Александр Николаевич (RU), Пиличев Валерий Валерьевич (RU), ...

Подробнее
10-08-2014 дата публикации

ТЕХНОЛОГИЧЕСКАЯ ЛИНИЯ ПОЛУЧЕНИЯ КАТАЛИЗАТОРА ДЛЯ ГЛУБОКОГО ОКИСЛЕНИЯ УГЛЕВОДОРОДОВ ДЛЯ ИК ИЗЛУЧАТЕЛЯ

Номер: RU0000143836U1

1. Технологическая линия получения катализатора для глубокого окисления углеводородов для ИК излучателя, включающая последовательно соединенные и технологически связанные между собой участки пропитки носителя - кремнеземного волокна - солями металлов, путем погружения носителя в раствор, участок сушки и участок прокаливания катализатора, отличающаяся тем, что перед участком пропитки носителя, выполненным в виде ванны с сетчатым поддоном, расположен участок приготовления реагента и участок предварительного прокаливания носителя, а участок прокаливания катализатора снабжен воздуховодом подачи воздуха и воздуховодом для удаления продуктов разложения. 2. Технологическая линия по п.1, отличающаяся тем, что участок приготовления реагентов включает последовательно связанные между собой и с участком приготовления реагентов дистиллятор, емкость для хранения воды и дозатор воды, а также дозатор реагентов. 3. Технологическая линия по п.1, отличающаяся тем, что участок приготовления реагентов оборудован мешалкой. 4. Технологическая линия по п.1, отличающаяся тем, что перед участком прокаливания носителя расположен участок предварительного раскроя носителя в виде раскройного стола. 5. Технологическая линия по п.1, отличающаяся тем, что за участком сушки и перед участком прокаливания катализатора расположен участок раскроя катализатора в виде гильотины. 6. Технологическая линия по п.1, отличающаяся чем, что участок сушки выполнен в виде этажерной сушилки. 7. Технологическая линия по п.1, отличающаяся тем, что за участком прокаливания катализатора расположены участок упаковки и участок хранения катализатора. И 1 143836 ко РОССИЙСКАЯ ФЕДЕРАЦИЯ ВУ” 143 836” 44 ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ИЗВЕЩЕНИЯ К ПАТЕНТУ НА ПОЛЕЗНУЮ МОДЕЛЬ ММ9К Досрочное прекращение действия патента из-за неуплаты в установленный срок пошлины за поддержание патента в силе Дата прекращения действия патента: 06.03.2021 Дата внесения записи в Государственный реестр: 11.11.2021 Дата ...

Подробнее
27-07-2015 дата публикации

УСТАНОВКА ДЛЯ ПОЛУЧЕНИЯ НАГРУЖЕННЫХ ВЕЩЕСТВАМИ ИЗ НАНОДИСПЕРСИЙ ТЕЛ НОСИТЕЛЕЙ

Номер: RU0000153579U1

1. Установка для получения нагруженных из нанодисперсий тел носителей, включающая вентили, корпус, крышку и донную часть, при этом в корпусе расположена пористая перегородка, выполненная с возможностью размещения на ней сформованных тел носителей и обеспечивающая возможность нагнетания жидкой среды с наночастицами, содержащими металл, кроме того, установка имеет пористую перегородку, расположенную между корпусом и крышкой и обеспечивающую возможность нагнетания жидкой среды с наночастицами, содержащими металл, отличающаяся тем, что корпус с внешней стороны имеет два вала, перпендикулярных продольной оси установки и обеспечивающих возможность поворота установки на угол не менее 180° с помощью привода, также установка имеет смотровые окна, выполненные по меньшей мере части ее высоты. 2. Установка по п.1, отличающаяся тем, что в виде наночастиц, содержащих металл, используют наночастицы металла и металлооксида. 3. Установка по п.1, отличающаяся тем, что в виде наночастиц, содержащих металл, используют наночастицы металлооксида. 4. Установка по п.1, отличающаяся тем, что корпус содержит цилиндрическую часть и фланцы, обеспечивающие возможность фиксации к нему крышки и донной части. 5. Установка по п.4, отличающаяся тем, что она дополнительно имеет фиксатор, обеспечивающий возможность ее удержания при повороте на угол не менее 180°. 6. Установка по п.5, отличающаяся тем, что она имеет станину. 7. Установка по любому из пп.1-6, отличающаяся тем, что в качестве привода она имеет электрический привод. 8. Установка по любому из пп.1-6, отличающаяся тем, что в качестве привода она имеет мускульный привод. И 1 153579 ко РОССИЙСКАЯ ФЕДЕРАЦИЯ 7 ВУ‘’” 153 579? Ц1 ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ИЗВЕЩЕНИЯ К ПАТЕНТУ НА ПОЛЕЗНУЮ МОДЕЛЬ МЕЭК Восстановление действия патента Дата, с которой действие патента восстановлено: 10.10.2019 Дата внесения записи в Государственный реестр: 10.10.2019 Дата публикации и номер бюллетеня: 10.10.2019 Бюл. №28 Стр.: 1 па 619$ ...

Подробнее
27-11-2019 дата публикации

АППАРАТ ДЛЯ ПРОВЕДЕНИЯ ПРОКАЛКИ НОСИТЕЛЯ КАТАЛИЗАТОРА ИЗОМЕРИЗАЦИИ

Номер: RU0000194072U1

Аппарат для проведения прокалки носителей катализаторов изомеризации С-фракции и носителей других катализаторов изомеризации имеет по меньшей мере пять обособленных тепловых зон - предварительного нагрева, сушки, разогрева, прокалки, охлаждения, разделенных внутренними устройствами, причем внутренние устройства представляют собой комплекс переточных труб, обеспечивающих движение носителя между зонами под действием силы тяжести и препятствующих предпочтительному перетоку газа-теплоносителя из одной зоны в другую, и каждая зона тепловой обработки гранулированного материала имеет индивидуальный ввод и вывод теплоносителя. Точная регулировка температуры в тепловых зонах осуществляется за счет смешения газа-теплоносителя и газа-разбавителя, поступающих на вход каждой зоны. Перепад температуры в зонах термообработки обеспечивается на уровне не более 5°С. Распределение газообразного теплоносителя в объеме носителя катализатора изомеризации осуществляется за счет газораспределительного устройства, представляющего собой горизонтально расположенную систему конусообразных полых каналов, пронизывающих слой носителя. Аппарат содержит внутренние устройства, разделяющие зоны тепловой обработки гранулированного носителя катализатора изомеризации, и состоящие из распределительной тарелки, образованной газонепроницаемыми воронкообразными сегментами, перекрывающими полость цилиндрического кожуха в поперечном сечении. 5 з.п. ф-лы, 1 табл., 2 пр., 4 ил. И 1 194072 ко РОССИЙСКАЯ ФЕДЕРАЦИЯ ВУ” 194 072” 44 ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ИЗВЕЩЕНИЯ К ПАТЕНТУ НА ПОЛЕЗНУЮ МОДЕЛЬ ММ9К Досрочное прекращение действия патента из-за неуплаты в установленный срок пошлины за поддержание патента в силе Дата прекращения действия патента: 13.08.2021 Дата внесения записи в Государственный реестр: 15.07.2022 Дата публикации и номер бюллетеня: 15.07.2022 Бюл. №20 Стр.: 1 па СЛОУб6 | ЕП

Подробнее
12-02-2020 дата публикации

АВТОКЛАВ ДЛЯ ОБРАБОТКИ ЦЕОЛИТА ПУТЕМ ИОННОГО ОБМЕНА

Номер: RU0000195954U1

Полезная модель относится к области получения цеолитных катализаторов и может быть использована в катализе, в частности в катализе процессов алкилирования изобутана бутиленом. Автоклав для обработки цеолита путем ионного обмена, выполненный в виде цилиндрического корпуса, снабженного герметичной крышкой и нагревательным элементом, выполнен так, что корпус закреплен в стационарной стойке с возможностью регулирования угла наклона корпуса в пределах 30-60°. У основания стойки, выполненной в виде усеченной трапеции, расположен двигатель, соединенный с одной стороны с задатчиком частоты вращения корпуса, а с другой - с вращательным механизмом, обеспечивающим вращение корпуса. Технический результат: эффективное перемешивание гранул цеолита без нарушения их целостности при разной степени загрузки цеолита. 1 фиг., 7 пр. РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 195 954 U1 ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ИЗВЕЩЕНИЯ К ПАТЕНТУ НА ПОЛЕЗНУЮ МОДЕЛЬ QZ9K Государственная регистрация изменений, касающихся предоставления права использования по договору Вид договора: лицензионный Лицо(а), которому(ым) предоставлено право использования: Акционерное общество "Электрогорский институт нефтепереработки имени академика Хаджиева Салмбека Наибовича" (RU) Изменения: предоставляемая лицензия изменена на неисключительную 1 9 5 9 5 4 Лицо(а), предоставляющее(ие) право использования: Федеральное государственное бюджетное учреждение науки Ордена Трудового Красного Знамени Институт нефтехимического синтеза им. А.В. Топчиева Российской академии наук (RU) R U Дата и номер государственной регистрации предоставления права использования по договору, в которое внесены изменения: 31.08.2020 РД0339602 Дата и номер государственной регистрации изменений, касающихся предоставления права использования: 11.01.2021 РД0351078 U 1 R U 1 9 5 9 5 4 Дата публикации и номер бюллетеня: 11.01.2021 Бюл. №2 Стр.: 1 U 1 Дата внесения записи в Государственный реестр: 11.01.2021

Подробнее
26-01-2012 дата публикации

Vanadium-free diesel oxidation catalyst and method for its production

Номер: US20120020843A1
Принадлежит: Sued Chemie AG

The invention relates to a method for producing a catalytic composition, wherein the catalytic composition has a high activity and selectivity with regard to the oxidation of CO and a reduced activity with regard to the oxidation of NO. The invention also relates to the catalyst produced using the method according to the invention. Finally, the invention is directed towards an exhaust-gas cleaning system which comprises the catalyst according to the invention.

Подробнее
26-01-2012 дата публикации

Fischer-tropsch synthesis catalyst, preparation and application thereof

Номер: US20120022174A1
Принадлежит: Synfuels China Technology Co Ltd

A micro-spherical Fe-based catalyst for a slurry bed Fischer-Tropsch synthesis (FTS) comprises Fe as its active component, a transitional metal promoter M, a structure promoter S and a K promoter. The transitional metal promoter M is one or more selected from the group consisting of Mn, Cr and Zn, and the structure promoter S is SiO 2 and/or Al 2 O 3 . The weight ratio of the catalyst components is Fe: transitional metal promoter: structure promoter: K=100:1-50:1-50:0.5-10. Preparation method of the catalyst comprises: adding the structure promoter S into a mixed solution of Fe/M nitrates, then co-precipitating with ammonia water to produce a slurry, filtering and washing the slurry to produce a filter cake, adding the required amount of the K promoter and water to the filter cake, pulping and spray drying, and roasting to produce the micro-spherical Fe-based catalyst for the slurry bed Fischer-Tropsch synthesis. The catalyst has good abrasion resistance and narrow particle size distribution, furthermore, it has high conversion capability of synthesis gas, good product selectivity and high space time yield, and the catalyst also can be used for the slurry bed Fischer-Tropsch synthesis in a wide temperature range.

Подробнее
09-02-2012 дата публикации

Exhaust gas purifying catalyst

Номер: US20120031085A1
Принадлежит: JOHNSON MATTHEY PLC

An exhaust gas purifying catalyst includes two catalyst layers containing a fire resistant inorganic compound carrying a catalyst component in an exhaust gas passage of a base material provided with the exhaust gas passage penetrating through the base material from the exhaust gas introduction port side to discharge port side, wherein each catalyst layer is formed by supporting the catalyst component on a different fire resistant inorganic compound, a catalyst layer extended from the exhaust gas introduction port side to the exhaust gas discharge port side and a catalyst layer extended from the exhaust gas discharge port side to the exhaust gas introduction port side are formed such that the catalyst layers are overlapped on each other and the exhaust gas introduction port side is coated only with one of the catalyst layers and the exhaust gas discharge port side is coated only with the other.

Подробнее
16-02-2012 дата публикации

Method of producing photocatalyst layer

Номер: US20120040819A1
Автор: Norio Matsuda
Принадлежит: Pioneer Corp

A method of producing a photocatalyst layer can increase a photocatalyst effect without increasing light irradiation energy for activation. The method includes: an irradiation process of irradiating an ultraviolet ray on a titanium oxide layer formed on a substrate, an aqueous photocatalyst solution application process of applying an aqueous photocatalyst solution containing fine particles on the titanium oxide layer to form a photocatalyst layer, and a drying process of drying the photocatalyst layer, wherein the aqueous photocatalyst solution application process is a process of applying the aqueous photocatalyst solution on the titanium oxide layer in such a way that a thickness of the aqueous photocatalyst solution is ununiform.

Подробнее
08-03-2012 дата публикации

Zeolite-palladium complex, method for producing the same, catalyst containing the complex, and method for producing a coupling compound by using the catalyst

Номер: US20120059191A1
Принадлежит: Individual

There is provided a substance having much higher catalytic activity for a Suzuki-Miyaura coupling reaction than conventional heterogenous catalysts. The present invention provides a zeolite-palladium complex including USY-zeolite and Pd supported on the USY-zeolite, the Pd having a Pd—Pd coordination number of 4 or less and an oxidation number of 0.5 or less.

Подробнее
15-03-2012 дата публикации

Exhaust gas-purifying catalyst

Номер: US20120065058A1
Принадлежит: Cataler Corp

An exhaust gas-purifying catalyst according to the present invention includes a substrate, a first catalytic layer facing the substrate and includes at least one precious metal selected from the group consisting of palladium and platinum, and alumina doped with an alkaline-earth metal element, and a second catalytic layer facing the substrate with the first catalytic layer interposed therebetween or intervening between the substrate and the first catalytic layer, the second catalytic layer includes rhodium and alumina doped with the alkaline-earth metal element.

Подробнее
17-05-2012 дата публикации

Hydroconversion multi-metallic catalyst and method for making thereof

Номер: US20120122655A1
Принадлежит: Chevron USA Inc

In a process for forming a bulk hydroprocessing catalyst by sulfiding a catalyst precursor made in a co-precipitation reaction, up to 60% of the metal precursor feeds do not react to form catalyst precursor and end up in the supernatant. In the present disclosure, the metals can be recovered via any of chemical precipitation, ion exchange, electro-coagulation, and combinations thereof to generate an effluent stream containing less than 50 mole % of metal ions in at least one of the metal residuals, and for at least one of the metal residuals is recovered as a metal precursor feed, which can be recycled for use in the co-precipitation reaction. An effluent stream from the process to waste treatment contains less than 50 ppm metal ions.

Подробнее
17-05-2012 дата публикации

Hydroconversion multi-metallic catalyst and method for making thereof

Номер: US20120122659A1
Принадлежит: Chevron USA Inc

In a process for forming a bulk hydroprocessing catalyst by sulfiding a catalyst precursor made in a co-precipitation reaction, up to 60% of the metal precursor feeds end up in the supernatant. The metals can be recovered via any of chemical precipitation, ion exchange, electro-coagulation, and combinations thereof to generate an effluent stream containing less than 50 mole % of metal ions in at least one of the metal residuals, and for at least one of the metal residuals recovered as a metal precursor feed for use in the co-precipitation reaction. In one embodiment, the resin functions as an anion exchange resin with an acidic supernatant to recover Group VIB metal residuals, and a cation exchange resin with a basic supernatant to recover Promoter metal residuals. An effluent stream from the process to waste treatment contains less than 50 ppm metals.

Подробнее
17-05-2012 дата публикации

Exhaust gas-purifying catalyst

Номер: US20120122672A1
Принадлежит: Cataler Corp

An exhaust gas-purifying catalyst includes first particles of oxygen storage material, second particles of one or more rare-earth elements other than cerium and/or compounds thereof interposed between the first particles, and third particles of one or more precious metal elements interposed between the first particles, wherein a spectrum of a characteristic X-ray intensity for one of the rare-earth element(s) and a spectrum of a characteristic X-ray intensity for one of the precious metal element(s) that are obtained by performing a line analysis using energy-dispersive X-ray spectrometry along a length of 500 nm have a correlation coefficient of 0.68 or more.

Подробнее
07-06-2012 дата публикации

Metal oxide particle production method and production device

Номер: US20120141362A1
Принадлежит: Hokkaido University NUC

An object of the present invention is to provide a method for producing metal oxide particles, in which metal oxide particles with high photocatalytic activity is produced, and a production apparatus therefor. The above object can be achieved by using a method for producing metal oxide particles, which includes subjecting a reaction gas containing metal chloride and an oxidizing gas containing no metal chloride in a reaction tube ( 11 ) to preheating, and then subjecting a combined gas composed of the reaction gas and the oxidizing gas to main heating in a main heating region (A) apart from the downstream side of the junction ( 5 b ), wherein the time until the combined gas from the junction ( 5 b ) arrives at the upstream end (A 1 ) of the main heating region (A) is adjusted to be less than 25 milliseconds.

Подробнее
07-06-2012 дата публикации

Obtaining catalysts of mmos2 and m/mos2 with nanometric additive of sio2, synthesized in aqueous solution assisted by ultrasound

Номер: US20120142519A1

A method for obtaining a promoted molybdenum sulfide catalyst and a promoted molybdenum sulfide added with a nanometric additive. The obtained catalyst exhibits an improved catalytic activity in hydrotreatment reactions, such as hydrodesulfurization, hydrodenitrogenation, and hydrogenation. The invention presents as an advantage, in addition to a low cost composition by their transition metals content, the activation of thiosalts precursor using an environmentally friendly atmosphere.

Подробнее
07-06-2012 дата публикации

Photocatalyst-coated body and photocatalytic coating liquid therefor

Номер: US20120142521A1
Принадлежит: TOTO LTD

A photocatalyst-coated body comprises a substrate and a photocatalyst layer provided on the substrate, the photocatalyst layer comprising photocatalyst particles of 1 part or more by mass and less than 20 parts by mass, inorganic oxide particles of 70 parts or more by mass and less than 99 parts by mass, and the dried substance of a hydrolyzable silicone of zero parts or more by mass and less than 10 parts by mass, provided that a total amount of the photocatalyst particles, the dried substance of the inorganic oxide particles and the hydrolyzable silicone is 100 parts by mass in terms of silica. The inorganic oxide particles have a number average particle diameter ranging from 10 nm or more to less than 40 nm calculated by measuring lengths of 100 particles randomly selected from particles located within a visible field magnified 200,000 times by a scanning electron microscope.

Подробнее
07-06-2012 дата публикации

Process for producing hydrogenolysis products of polyhydric alcohols

Номер: US20120142976A1
Принадлежит: Kao Corp

The present invention relates to a process for producing hydrogenolysis products of polyhydric alcohols with a good selectivity and a high yield, as well as hydrogenolysis catalysts used in the production process. The present invention provides (1) a process for producing a hydrogenolysis product of a polyhydric alcohol which includes the step of reacting the polyhydric alcohol with hydrogen in the presence of a catalyst containing a copper component, wherein the catalyst is a catalyst (A) containing the copper component, an iron component and an aluminum component, or a catalyst (B) containing the copper component and a silicon component; and (2) a hydrogenolysis catalyst for polyhydric alcohols which includes a copper component, an iron component and an aluminum component, and (3) a hydrogenolysis catalyst for polyhydric alcohols which includes a copper component and a silicon component.

Подробнее
07-06-2012 дата публикации

Process for producing aromatic hydrocarbon and transition-metal-containing crystalline metallosilicate catalyst for use in the production process

Номер: US20120142986A1

Provided is a process for producing an aromatic hydrocarbon efficiently at high yield from a lower hydrocarbon containing methane as a major component, and such a process for producing an aromatic hydrocarbon includes the step of reacting a lower hydrocarbon containing methane as a major component in the presence of a transition-metal-containing crystalline metallosilicate catalyst which is obtainable by supporting 5 to 25 parts by weight of a transition metal (X) on 100 parts by weight of a modified crystalline metallosilicate obtainable by subjecting a crystalline metallosilicate to a series of treatment (A) including a step (i) of eliminating part of a metal from the crystalline metallosilicate and a silylation step (ii).

Подробнее
05-07-2012 дата публикации

Catalyst for treating exhaust gases, method for producing the same, and method for treating exhaust gases

Номер: US20120171097A1
Принадлежит: Mitsubishi Heavy Industries Ltd

A catalyst for treating exhaust gases containing nitrogen monoxide, carbon monoxide and volatile organic compounds includes a plurality of layers, an upper layer of which has an active component contained uniformly therein and a lower layer of which has no active component contained therein. The catalyst is obtained through the steps of: forming the lower layer by coating the surface of substrate with a slurry of a porous inorganic compound, followed by drying; and forming the upper layer, which is to be the top surface of the catalyst, by coating the surface of the lower layer with a slurry of a porous inorganic compound that has the active component composed of one or more precious metals supported thereon, followed by drying. The oxidation power of the resulting catalyst is enhanced without increasing the amount of precious metal supported thereon.

Подробнее
05-07-2012 дата публикации

Hydroprocessing catalysts and methods for making thereof

Номер: US20120172199A1
Принадлежит: Chevron USA Inc

An improved process to make a slurry catalyst for the upgrade of heavy oil feedstock is provided. In the process, at least a metal precursor feedstock is portioned and fed in any of the stages: the promotion stage; the sulfidation stage; or the transformation stage of a water-based catalyst precursor to a slurry catalyst. In one embodiment, the promoter metal precursor feedstock is split into portions, the first portion is for the sulfiding step, the second portion is for the promotion step; and optionally the third portion is to be added to the transformation step in the mixing of the sulfided promoted catalyst precursor with a hydrocarbon diluent to form the slurry catalyst. In another embodiment, the Primary metal precursor feedstock is split into portions.

Подробнее
12-07-2012 дата публикации

Method for preparing a multi-metal catalyst having an optimized site proximity

Номер: US20120178979A1
Принадлежит: IFP Energies Nouvelles IFPEN

The invention concerns a process for preparing a catalyst comprising at least one metal M from the platinum group, tin, a phosphorus promoter, a halogenated compound, a porous support and at least one promoter X1 selected from the group constituted by gallium, indium, thallium, arsenic, antimony and bismuth. The promoter or promoters X1 and the phosphorus are introduced during one or more sub-steps a1) or a2), the sub-step a1) corresponding to synthesis of the precursor of the main oxide and sub-step a2) corresponding to shaping the support. The tin is introduced during at least one of sub-steps a1) and a2). The product is dried and calcined before depositing at least one metal M from the platinum group. The ensemble is then dried in a stream of neutral gas or a stream of gas containing oxygen, and then is dried. The invention also concerns the use of a catalyst obtained by said process in catalytic reforming or aromatics production reactions.

Подробнее
19-07-2012 дата публикации

Three Way Conversion Catalyst With Alumina-Free Rhodium Layer

Номер: US20120180464A1
Принадлежит: BASF Corp

Provided are exhaust systems and components suitable for use in conjunction with gasoline engines to treat gaseous emissions such as hydrocarbons, nitrogen oxides, and carbon monoxides. Layered three-way conversion (TWC) catalysts comprise an outer layer whose rhodium is supported by an oxygen storage component, such as a ceria-zirconia composite, and the outer layer is substantially free from alumina as a support. The rhodium-containing layer can be free of all other precious metals, such as platinum and palladium. A lower palladium layer is provided where the palladium is supported by a refractory metal oxide. The lower palladium layer can be free of rhodium and platinum and can contain an oxygen storage component that is the same or different from that in the rhodium-containing layer. Methods of making and using these catalysts are also provided.

Подробнее
26-07-2012 дата публикации

Method for forming thermally stable nanoparticles on supports

Номер: US20120190540A1

An inverse micelle-based method for forming nanoparticles on supports includes dissolving a polymeric material in a solvent to provide a micelle solution. A nanoparticle source is dissolved in the micelle solution. A plurality of micelles having a nanoparticle in their core and an outer polymeric coating layer are formed in the micelle solution. The micelles are applied to a support. The polymeric coating layer is then removed from the micelles to expose the nanoparticles. A supported catalyst includes a nanocrystalline powder, thin film, or single crystal support. Metal nanoparticles having a median size from 0.5 nm to 25 nm, a size distribution having a standard deviation ≦0.1 of their median size are on or embedded in the support. The plurality of metal nanoparticles are dispersed and in a periodic arrangement. The metal nanoparticles maintain their periodic arrangement and size distribution following heat treatments of at least 1,000° C.

Подробнее
26-07-2012 дата публикации

Reactive systems

Номер: US20120190787A1
Принадлежит: Elantas GmbH

Reactive system comprising at least one component (I) composed of particles in very finely divided form present in a liquid phase of at least one further component (II) with which component (I) is capable of reacting following activation through energy supply, wherein component (I) is not soluble in component (II), process for preparation and use.

Подробнее
26-07-2012 дата публикации

Process for producing diphenyl carbonate

Номер: US20120190878A1
Автор: J. Yong Ryu
Принадлежит: Shell Oil Co

Processes for producing diaryl carbonates are disclosed, where such processes may provide for the production of diaryl carbonates from green house gases, such as carbon dioxide. The processes disclosed advantageously integrate diethyl carbonate and diaryl carbonate production, eliminating the need for solvent-based extractive distillation, as is commonly required when producing diaryl carbonates from dimethyl carbonate, providing for the integration of separation equipment and raw material usage, and reducing the operating and capital requirements for such processes. In some embodiments, processes disclosed herein may be operated essentially closed-loop with respect to ethanol usage, for example.

Подробнее
09-08-2012 дата публикации

Production of hydrocarbons

Номер: US20120202899A1
Принадлежит: Sasol Technology Pty Ltd

A process for producing hydrocarbons and, optionally, oxygenates of hydrocarbons is provided. A synthesis gas comprises hydrogen, carbon monoxide and N-containing contaminants selected from the group consisting of HCN, NH 3 , NO, R X NH 3-X , R 1 —CN and heterocyclic compounds containing at least one nitrogen atom as a ring member of a heterocyclic ring of the heterocyclic compound. The N-containing contaminants constitute, in total, at least 100 vppb but less than 1 000 000 vppb of the synthesis gas. The synthesis gas is contacted at an elevated temperature and an elevated pressure, with a particulate supported Fischer-Tropsch synthesis catalyst. The catalyst comprises a catalyst support, Co in catalytically active form supported on the catalyst support, and a dopant selected from the group consisting of platinum (Pt), palladium (Pd), ruthenium (Ru) and/or rhenium (Re). The dopant level is expressed by a formula. Hydrocarbons and, optionally, oxygenates of hydrocarbons are obtained.

Подробнее
30-08-2012 дата публикации

Photocatalytic structural member and deodorizing device

Номер: US20120219459A1
Автор: Morio Nakatani
Принадлежит: Sanyo Electric Co Ltd

A photocatalytic structural member is provided with a substrate having a concave-convex structure formed on a surface thereof, and a photocatalyst film which is disposed on a side of the concave-convex structure of the substrate and reflects a shape of the concave-convex structure. The concave-convex structure is formed with a pitch smaller than a wavelength of light which causes a photocatalytic reaction on the photocatalyst film. A deodorizing device is provided with the photocatalytic structural member, a light source which emits the light from a side of the substrate to the photocatalytic structural member, and a fan which causes an air to flow to the photocatalytic structural member.

Подробнее
20-09-2012 дата публикации

Methanation Reaction Methods Utilizing Enhanced Catalyst Formulations and Methods of Preparing Enhanced Methanation Catalysts

Номер: US20120238647A1
Принадлежит: ConocoPhillips Co

Enhanced mixed metal catalysts are provided which allow high conversions of carbon dioxide to methane, in some cases up to about 100% conversion. Methods of preparing enhanced mixed metal catalysts comprise a series of steps involving combining nickel and chromium salts with a nucleation promoter in a base environment to form a gel, allowing the gel to digest to form a solid and a mother liquor, isolating the solid, washing the solid, drying the solid, and thermally treating the solid to form a nickel-chromium catalyst. Methanation processes using the catalysts are also provided. The enhanced mixed metal catalysts provide more efficient conversion and lower operating temperatures for carbon dioxide methanation when compared to conventional methanation catalysts. Additionally, these enhanced catalyst formulations allow realization of higher value product from captured carbon dioxide.

Подробнее
04-10-2012 дата публикации

Conditioning of double metal cyanide catalysts

Номер: US20120253005A1
Принадлежит: BASF SE

The invention relates to a method for conditioning double metal catalysts which are used in the production of polyether polyols. The conditioning enhances the performance of the catalyst, so that lower concentrations of the DMC catalyst can be used in polyether polyol production.

Подробнее
25-10-2012 дата публикации

Process for the dehydration of aqueous bio-derived terminal alcohols to terminal alkenes

Номер: US20120271089A1
Автор: Michael E. Wright
Принадлежит: US Department of Navy

A method and apparatus for dehydrating bio-1-alcohols to bio-l-alkenes with high selectivity. The bio-1-alkenes are useful in preparing high flashpoint diesel and jet biofuels which are useful to civilian and military applications. Furthermore, the bio-1-alkenes may be converted to biolubricants useful in the transporation sector and other areas requiring high purity/thermally stable lubricants.

Подробнее
01-11-2012 дата публикации

Double-component modified molecular sieve with improved hydrothermal stability and production method thereof

Номер: US20120275994A1
Принадлежит: Petrochina Co Ltd

A method for producing double-component modified molecular sieve comprises adding molecular sieve to an aqueous solution containing phosphorus to form a mixture, allowing the mixture to react at pH of 1-10, temperature of 70-200° C. and pressure of 0.2-1.2 MPa for 10-200 min, and then filtering, drying and baking the resultant to obtain phosphorus-modified molecular sieve, and then adding the phosphorus-modified molecular sieve to an aqueous solution containing silver ions, allowing the phosphorus-modified molecular sieve to react with silver ions at 0-100° C. in dark condition for 30-150 min, and then filtering, drying and baking. The obtained double-component modified molecular sieve contains 88-99 wt % molecular sieve with a ratio of silica to alumina between 15 and 60, 0.5-10 wt % phosphorus (based on oxides) and 0.01-2 wt % silver (based on oxides), all based on dry matter. A catalyst produced from the double-component modified molecular sieve has improved hydrothermal stability and microactivity.

Подробнее
01-11-2012 дата публикации

Process for the regeneration of hydrocarbon conversion catalysts

Номер: US20120277089A1
Принадлежит: Individual

The present invention provides a process for hydrocarbon conversion, especially for producing aromatic hydrocarbons, which comprises: (a) alternately contacting a hydrocarbon feed, especially a lower alkane feed, with a hydrocarbon conversion catalyst, especially an aromatization catalyst, under hydrocarbon conversion, especially aromatization reaction conditions, in a reactor for a short period of time, preferably 30 minutes or less, to produce reaction products and then contacting the catalyst with hydrogen-containing gas at elevated temperature for a short period of time, preferably 10 minutes or less, (b) repeating the cycle of step (a) at least one time, (c) regenerating the catalyst by contacting it with an oxygen-containing gas at elevated temperature and (d) repeating steps (a) through (c) at least one time.

Подробнее
01-11-2012 дата публикации

Processes for Transalkylating Aromatic Hydrocarbons

Номер: US20120277512A1
Автор: Edwin P. Boldingh
Принадлежит: UOP LLC

A process for transalkylating aromatic hydrocarbon compounds, the process comprising introducing an aromatic hydrocarbon feed stream and a sulfur source to a transalkylation zone. The feed stream contacts a catalyst in the transalkylation zone in the presence of sulfur, and produces a reaction product stream comprising benzene and xylene. The invention includes methods to control the transalkylation process.

Подробнее
29-11-2012 дата публикации

Engine exhaust catalysts doped with bismuth or manganese

Номер: US20120302439A1
Принадлежит: Nanostellar Inc

An emission control catalyst is doped with bismuth, manganese, or bismuth and manganese. The doped catalyst may be a palladium-gold catalyst or a platinum-based catalyst, or both. The doped palladium-gold catalyst and the doped platinum-based catalyst may be contained in a single washcoat layer or in different washcoat layers of a multi-brick, multi-zoned, or multi-layered emission control system. In all embodiments, zeolite may be added as a hydrocarbon absorbing component.

Подробнее
20-12-2012 дата публикации

Hydrothermal hydrocatalytic treatment of biomass

Номер: US20120317873A1
Принадлежит: Shell Oil Co

A method of hydrothermal hydrocatalytic treating biomass is provided. Lignocellulosic biomass is treated with a digestive solvent to form a pretreated biomass containing soluble carbohydrates. The pretreated biomass is contacted, with hydrogen at a temperature in the range of 150° C. to less than 300° C. in the presence of a pH buffering agent and a supported hydrogenolysis catalyst containing (a) sulfur, (b) Mo or W, and (c) Co, Ni or mixture thereof, incorporated into a suitable support, to form a plurality of oxygenated hydrocarbons.

Подробнее
03-01-2013 дата публикации

Spinel structured catalyst for aldehyde production

Номер: US20130006019A1
Принадлежит: Individual

The present invention refers to a catalyst for aldehyde production, in particular formaldehyde or acetaldehyde production, through selective oxidation of alkanol, especially methanol or ethanol, with oxygen, said catalyst having a spinel structure. The catalyst typically comprises a Fe a q +V b+ Mo c+ y +Δ z O 4 spinel structure wherein Δ is an optional cation vacancy and wherein wherein z=3−q−x−y and q×a+x×b+y×c=8 in concentrations corresponding to 0.6<q<3, 0<x<1.5, 0<y<1 and 0<z<1.3 and 2<a<3, 3<b<5 and 3<c<6. The present invention further refers to a process for producing said catalyst and to the use of said catalyst for selective oxidation of alkanol, preferably methanol or ethanol, with oxygen to aldehyde, preferably formaldehyde or acetaldehyde.

Подробнее
17-01-2013 дата публикации

Catalyst for glycerin dehydration, and process for producing acrolein, process for producing acrylic acid, and process for producing hydrophilic resin each using the catalyst

Номер: US20130018161A1
Принадлежит: NIPPON SHOKUBAI CO LTD

A catalyst for glycerin dehydration of the present invention comprises boron phosphate or a rare-earth metal phosphate, wherein a molar ratio P/B of phosphorus (P) to boron (B) or a molar ratio P/R of phosphorus (P) to a rare-earth metal (R) is more than 1.0 and 2.0 or less. An another catalyst for glycerin dehydration of the present invention comprises a combination of boron phosphate and a metal element or a combination of a rare-earth metal phosphate and a metal element other than a rare-earth metal, wherein a molar ratio M/(P+B) of a metal element (M) to phosphorus (P) and boron (B) or a molar ratio M/(P+R) of a metal element (M) to phosphorus (P) and a rare-earth metal (R) is more than 0.00005 and 0.5 or less.

Подробнее
24-01-2013 дата публикации

Catalysts supports

Номер: US20130023593A1
Принадлежит: JOHNSON MATTHEY PLC

A method for preparing a silica-modified catalyst support is described including: (I) applying an alkyl silicate to the surface of a porous support material in an amount to produce a silica content of the silica-modified catalyst support, expressed as Si, in the range 0.25 to 15% by weight, (ii) optionally drying the resulting silicate-modified support, (iii) treating the support with water, (iv) drying the resulting water-treated support, and (v) calcining the dried material to form the silica-modified catalyst support.

Подробнее
07-02-2013 дата публикации

Method for producing catalyst

Номер: US20130035226A1
Автор: Nobuaki Mizutani
Принадлежит: Toyota Motor Corp

This invention is intended to improve the coverage of a platinum or platinum alloy surface with gold when producing a catalyst comprising carrier particles that support gold-modified platinum or platinum alloys. The invention provides a method for producing a catalyst comprising carrier particles that support gold-modified platinum or platinum alloys comprising a step of gold reduction comprising adding carrier particles that support platinum or platinum alloys, a reducing agent, and a gold precursor to a liquid medium and mixing the same, wherein the reducing agent is added to adjust the ORP value (i.e., an oxidation-reduction potential with reference to the silver-silver chloride electrode) of the liquid medium to −630 to +230 mV upon completion of addition.

Подробнее
07-03-2013 дата публикации

Dehydrofluorination of pentafluoroalkanes to form tetrafluoroolefins

Номер: US20130060069A1
Принадлежит: Arkema Inc

A method for producing a tetrafluoroolefin, such as 2,3,3,3-tetrafluoropropene (HFO-123434), comprises dehydrofluorinating a pentafluoroalkane in a gas phase in the presence of a catalyst comprising chromium oxyfluoride. In a preferred embodiment, 2,3,3,3-tetrafluoropropene (HFO-1234yf) is produced by forming a catalyst comprising chromium oxyfluoride by calcining CrF3?xH2O, where x is 1-10, in the presence of a flowing gas comprising nitrogen to form a calcined chromium oxyfluoride, and dehydrofluorinating 1,1,1,2,2-pentafluoropropane (HFC-245cb) in a gas phase in the presence of the catalyst to form the 2,3,3,3-tetrafluoropropene (HFO-1234yf).

Подробнее
14-03-2013 дата публикации

METHOD OF SUPPRESSING INCREASE IN SO2 OXIDATION RATE OF NOx REMOVAL CATALYST

Номер: US20130065750A1
Принадлежит: Mitsubishi Heavy Industries Ltd

In a NO x removal catalyst used for removing nitrogen oxide in flue gas, when a silica (Si) component as an inhibitor that causes an increase in an SO 2 oxidation rate accumulates on a surface of the NO x removal catalyst, the silica component accumulating on the surface of the NO x removal catalyst is dissolved, thereby regenerating the catalyst. Accordingly, the inhibitor such as the silica component covering the surface of the NO x removal catalyst can be removed, thereby enabling to provide a catalyst without having an increase in the SO 2 oxidation rate of the regenerated NO x removal catalyst.

Подробнее
21-03-2013 дата публикации

AMORPHOUS TRANSITION METAL SULPHIDE FILMS OR SOLIDS AS EFFICIENT ELECTROCATALYSTS FOR HYDROGEN PRODUCTION FROM WATER OR AQUEOUS SOLUTIONS

Номер: US20130068613A1

The present invention relates to amorphous transition metal sulphides as electrocatalysts for hydrogen production from water or aqueous solutions and use thereof in electrodes and electrolysers. 1. Use of amorphous transition metal sulphide films or solids as electrocatalysts for the reduction of proton to form H.2. The use of amorphous transition metal sulphide films or solids of claim 1 , wherein the transition metal sulphide is of formula MS claim 1 , where M is the transition metal and x is in the range 1.5 to 3.5.3. The use of amorphous transition metal sulphide films or solids of claim 1 , wherein the transition metal is selected from the group comprising Mo claim 1 , W claim 1 , Fe claim 1 , Cr claim 1 , Cu claim 1 , Ni.4. The use of amorphous transition metal sulphide films or solids of claim 1 , wherein the transition metal sulphide is MoS claim 1 , MoS claim 1 , WSor WS.5. The use of amorphous transition metal sulphide films or solids of claim 1 , wherein the amorphous transition metal sulphide films or solids are further doped with at least one metal selected from the group comprising Ni claim 1 , Co claim 1 , Mn claim 1 , Cu claim 1 , Fe.6. The use of amorphous transition metal sulphide films or solids of claim 5 , wherein the amorphous transition metal sulphide films or solids are further doped with Ni.7. The use of amorphous transition metal sulphide films or solids of claim 1 , wherein His originated from water or aqueous solutions.8. An electrode for use in the production of hydrogen gas from water or aqueous solutions comprising an electrode substrate claim 1 , wherein the amorphous transition metal sulphide films or solids of are deposited on said electrode substrate.9. The electrode of claim 8 , wherein the amorphous transition metal sulphide films or solids are selected from the group comprising amorphous MoSfilm or solid claim 8 , amorphous MoSfilm or solid claim 8 , amorphous WSfilm or solid claim 8 , and amorphous WSfilm or solid.10. The ...

Подробнее
25-04-2013 дата публикации

Nano Mixed Metal Oxide Thin Film Photocatalyst Consisting Of Titanium, Indium and Tin

Номер: US20130102953A1
Принадлежит: HCL TECHNOLOGIES LTD.

The present invention relates to a novel photocatalyst comprising Nano mixed metal oxides of titanium, Indium and tin as a thin film with nano sized grains, method of its preparation and applications. The photocatalyst disclosed herein can be used in oxygenation of human/mammalian blood along with all other applications of photocatalysts. A photocatalytic oxygenator for the oxygenation derives oxygen from the water content of mammalian blood. The photocatalyst disclosed herein can also be used for effluent treatments along with all other applications associated with photocatalysts. 1. A photocatalyst comprising mixed metal oxides of titanium , Indium and tin as a thin film with nano sized grains.214-. (canceled)15. The photocatalyst as claimed in claim 1 , wherein the atomic percentage of constituents are about 3.58-4.80 Indium claim 1 , about 0.29-0.32 Tin claim 1 , and about 0.62-0.72 Titanium claim 1 , as measured by EDX measurements on the thin films claim 1 , along with oxygen.16. The photocatalyst as claimed in claim 1 , wherein the photocatalyst consists of tin doped indium oxide (ITO) and titanium dioxide (TiO)17. The photocatalyst as claimed in claim 1 , wherein the photo energy required is any single or a range of wavelengths in the spectrum of 255 nm-1100 nm.18. A method making a photocatalyst consisting of a Titanium claim 1 , Indium and Tin mixed metal oxide thin film with nano sized grains comprising depositing the metal oxides by DC magnetron sputtering on a substrate followed by annealing.19. The method as claimed in claim 18 , wherein the substrate is quartz claim 18 , synthetic silicon dioxide claim 18 , soda lime glass claim 18 , poly-carbonates claim 18 , poly imides or a polymer.20. The method as claimed in claim 19 , wherein the substrate is quartz or synthetic silicon dioxide.21. The method as claimed in claim 18 , wherein the depositing of the metal oxides is performed at a temperature in the range of 300K to 400 K.22. The method as claimed ...

Подробнее
02-05-2013 дата публикации

Continuous Catalyst Activator

Номер: US20130109818A1
Принадлежит: CHEVRON PHILLIPS CHEMICAL COMPANY LP

Methods and systems for preparing catalyst, such as chromium catalysts, are provided. The valence of at least a portion of the catalyst sent to an activator is changed from Cr(III) to Cr(VI). The catalyst is prepared or activated continuously using a fluidization bed catalyst activator. 1. A polymerization system comprising:(a) a polymerization reactor,(b) a continuous catalyst activator comprising a fluidized bed, and(c) a controller programmed with an algorithm to control a polymerization reactor process variable by adjusting a continuous catalyst activator process variable.2. The polymerization system of claim 1 , wherein the continuous catalyst activator comprises:(a) a substantially horizontal fluidized bed vessel;(b) a gas distributor plate extending substantially horizontal within the fluidized bed vessel being arranged to allow passage of a fluidizing gas throughout the fluidized bed vessel;(c) an inlet for introducing a catalyst into the fluidized bed vessel;(d) at least one zone dividing wall for dividing the fluidized bed vessel into a plurality of zones, at least one of the zone dividing walls comprising a zone opening that allows the catalyst to be introduced into a next downstream zone, the plurality of zones being located substantially horizontal in relation to one another; and(e) each zone comprising at least one baffle, each baffle defining a stage, each zone comprising a lower boundary that comprises at least a portion of the gas distributor plate.3. The polymerization system of claim 2 , wherein the continuous catalyst activator comprises sufficient baffles to cause an essentially plug flow profile through the fluidized bed vessel.4. The polymerization system of claim 2 , wherein the continuous catalyst activator further comprises a filter apparatus adapted to remove any catalyst particles entrained in the fluidizing gas.5. The polymerization system claim 2 , wherein the continuous catalyst activator further comprises a cooling system wherein an ...

Подробнее
16-05-2013 дата публикации

Silver vanadium phosphates

Номер: US20130123517A1
Принадлежит: BASF SE

The invention relates to novel silver vanadium phosphates, catalysts based on these silver vanadium phosphates and the use of these catalysts for carrying out organic reactions in the gas phase.

Подробнее
23-05-2013 дата публикации

ACTIVATION OF DUAL CATALYST SYSTEMS

Номер: US20130130893A1

Methods are provided for liquid phase activation of dewaxing and/or hydrofinishing catalysts that include a molecular sieve or other acidic crystalline support. The methods are compatible with activating the catalysts as part of a catalyst system that also includes a hydrotreating catalyst. 1. A method for activating a catalyst system , comprising:exposing a catalyst system to a first liquid activation feed under effective reducing conditions for at least about 24 hours, the catalyst system including at least one catalyst that comprises a Group VIII non-noble metal on an amorphous support and at least one catalyst that comprises a Group VIII noble metal on an acidic support, the effective reducing conditions including a hydrogen partial pressure of at least about 500 psig (145 MPag) and a temperature of at least about 200° C.; andexposing the catalyst system to a second liquid activation feed under effective sulfiding conditions.2. The method of claim 1 , wherein the catalyst with an amorphous support is a hydrotreating catalyst.3. The method of claim 1 , wherein the catalyst comprising a Group VIII noble metal on an acidic support comprises a dewaxing catalyst with Pt claim 1 , Pd claim 1 , or a combination thereof on a support including a molecular sieve.4. The method of claim 1 , wherein the catalyst comprising a Group VIII noble metal on an acidic support comprises a hydrofinishing catalyst with Pt claim 1 , Pd claim 1 , or a combination thereof on a support comprising an M41S family support.5. The method of claim 1 , wherein the catalyst system is provided in a single reactor.6. The method of claim 1 , wherein first liquid activation feed comprises a distillate boiling range feed with a sulfur content of less than about 100 wppm and a water content of less than about 100 wppm.7. The method of claim 6 , wherein first liquid activation feed has a nitrogen content of less than about 250 wppm.8. The method of claim 1 , wherein the second liquid activation feed ...

Подробнее
30-05-2013 дата публикации

Method for Preparing Catalyst Coating on Metal Base Plate

Номер: US20130137569A1
Принадлежит:

A method for preparing catalyst coating on a metal base plate comprising: thermal-spraying a layer of a-aluminum oxide nano-particles on a metal base plate using a high temperature flame powder spray gun, at a temperature of 2500-3500° C. and a pressure of 0.2-1.2 MPa; coating an aluminum sol, the weight concentration of the aluminum sol aqueous solution being 2-30%, at a pH of 0.5-4, the drying temperature being 50-150° C., the drying time being 0.5-24 hours, the calcination temperature being 200-1200° C., and the calcination time being 0.5-24 hours; immersing in an active component, the immersing temperature being 20-120° C., the duration being 0.5-24 hours, the drying temperature being 50-150° C., the drying time being 0.5-24 hours, the calcination temperature being 200-1200° C., and the calcination time being 0.5-24 hours. The method is suitable for the preparation of various catalyst coatings with active components. 1. A method for preparing a catalyst coating on a metal substrate , comprising:a) pre-heating the metal substrate to about its melting point;b) thermally spraying a layer of α-alumina nanoparticles onto the pre-heated metal substrate to produce a composite substrate;c) coating the composite substrate with an alumina sol;d)drying and calcinating the alumina sol-coated composite substrate to form an α-alumina coated composite substrate;e) immersing the α-alumina coated composite substrate into a solution of active components to form a coating of the active components thereon; andf) drying and calcinating the active components onto the α-alumina coated composite substrate to obtain the catalyst coating.2. The method for preparing a catalyst coating on a metal substrate according to claim 1 , wherein a flame temperature is 2500° C. to 3500° C. claim 1 , and a pressure is 0.2 MPa to 1.2 MPa.3. The method for preparing a catalyst coating on a metal substrate according to claim 1 , wherein the alumina sol is prepared by heating an aqueous solution of ...

Подробнее
06-06-2013 дата публикации

Process for hydrocracking a hydrocarbon feed in the presence of a sulphide catalyst prepared using a cyclic oligosaccharide

Номер: US20130140215A1
Принадлежит: IFP Energies Nouvelles IFPEN

Hydrocracking a hydrocarbon feed in the presence of a catalyst comprising an acidic support and an active phase formed from at least one metal from group VIII and at least one metal from group VIB, said catalyst being prepared using a process comprising, in succession: contacting a pre-catalyst comprising said metal from group VIII, said metal from group VIB and said acidic support with a cyclic oligosaccharide of at least 6α-(1,4)-bonded glucopyranose subunits; contacting the acidic support with a solution containing a precursor of metal from group VIII, a precursor of said metal from group VIB and a cyclic oligosaccharide of at least 6α-(1,4)-bonded glucopyranose subunits; and contacting acidic support with a cyclic oligosaccharide of at least 6α-(1,4)-bonded glucopyranose subunits followed by a second contacting acidic solid with a precursor of metal from group VIII and a precursor of metal from group VIB; drying; heat treatment; sulphurization.

Подробнее
06-06-2013 дата публикации

The method of preparation of cerium oxide supported gold-palladium catalysts and its application in destruction of volatile organic compounds

Номер: US20130142720A1

This invention declares the method of preparation of cerium oxide supported palladium-gold catalysts and the process of destruction of volatile organic compounds in air to remove volatile organic compounds using the above catalysts. Destruction of volatile organic compounds in air stream over these catalysts is carried out in a fixed bed reactor to remove volatile organic compounds in air.

Подробнее
06-06-2013 дата публикации

SYNTHESIS OF HIGH ACTIVITY LARGE CRYSTAL ZSM-5

Номер: US20130144100A1

In a process for preparing a high activity, large crystal ZSM-5 type zeolite in the absence of a template, a reaction mixture can be prepared comprising water, a silica source having a surface area less than 150 m/g, an alumina source, seeds, a source of an oxide of an alkali metal, M, and a source of gluconic acid or salt thereof, Q, wherein the mixture has a SiO/AlOmolar ratio≦40. The reaction mixture can be heated to a crystallization temperature from about 100° C. to 200° C. for a time sufficient for crystals of ZSM-5 to form Crystals of ZSM-5 can then be recovered from the reaction mixture which crystals can have a SiO/AlOmolar ratio≦40 and a majority of which crystals can have at least one crystalline dimension of at least about 2 μm. 1. A process for preparing a high activity , large crystal ZSM-5 type zeolite in the absence of a template , the process comprising:{'sup': '2', 'sub': 2', '2', '3, '(a) preparing a reaction mixture comprising water, a silica source having a surface area less than 150 m/g, an alumina source, seeds, a source of an oxide of an alkali metal, M, and a source of gluconic acid or salt thereof, Q, wherein said mixture has a SiO/AlOmolar ratio less than or equal to 40;'}(b) heating the reaction mixture at a crystallization temperature from about 100° C. to 200° C. for a time sufficient for crystals of ZSM-5 to form; and{'sub': 2', '2', '3, '(c) recovering from the reaction mixture crystals of ZSM-5 having a SiO/AlOmolar ratio less than or equal to 40, wherein a majority of the crystals have at least one crystalline dimension of at least about 2 μm.'}2. The process of claim 1 , wherein the silica source has a specific surface area less than 125 m/g.3. The process of claim 1 , wherein the reaction mixture has a molar composition in the following amounts:{'sub': 2', '2', '3, 'SiO/AlO: up to about 40/1;'}{'sub': 2', '2, 'HO/SiO: about 5 to about 50;'}{'sup': '−', 'sub': '2', 'OH/SiO: about 0.05 to about 0.5'}{'sub': '2', 'M/SiO; about 0.05 ...

Подробнее
13-06-2013 дата публикации

CATALYST FUNCTIONALIZED BUFFER SORBENT PEBBLES FOR RAPID SEPARATION OF CARBON DIOXIDE FROM GAS MIXTURES

Номер: US20130149768A1
Автор: Aines Roger D.

A method for separating COfrom gas mixtures uses a slurried media impregnated with buffer compounds and coating the solid media with a catalyst or enzyme that promotes the transformation of COto carbonic acid. Buffer sorbent pebbles with a catalyst or enzyme coating are provided for rapid separation of COfrom gas mixtures. 1. A catalyst functionalized buffer sorbent pebble for separation of carbon dioxide from a gas mixture , comprising:a sorbent pebble, said sorbent pebbles includinga sorbent pebble body anda surface layer with an attached or embedded catalyst or enzyme, wherein said sorbent pebble provides separation of carbon dioxide from the gas mixture.2. The catalyst functionalized buffer sorbent pebble for separation of carbon dioxide from a gas mixture of wherein said sorbent pebble body is a material that absorbs carbon dioxide.3. The catalyst functionalized buffer sorbent pebble for separation of carbon dioxide from a gas mixture of wherein said surface layer with an attached catalyst or enzyme is an attached catalyst.4. The catalyst functionalized buffer sorbent pebble for separation of carbon dioxide from a gas mixture of wherein said surface layer with an attached catalyst or enzyme is an embedded catalyst.5. The catalyst functionalized buffer sorbent pebble for separation of carbon dioxide from a gas mixture of wherein said surface layer with an attached catalyst or enzyme is an attached enzyme.6. The catalyst functionalized buffer sorbent pebble for separation of carbon dioxide from a gas mixture of wherein said surface layer with an attached catalyst or enzyme is an embedded enzyme.7. The catalyst functionalized buffer sorbent pebble for separation of carbon dioxide from a gas mixture of wherein said surface layer with an attached catalyst or enzyme is a material that promotes the transformation of carbon dioxide to carbonic acid.8. The catalyst functionalized buffer sorbent pebble for separation of carbon dioxide from a gas mixture of wherein said ...

Подробнее
13-06-2013 дата публикации

Mixed oxide based catalyst for the conversion of carbon dioxide to syngas and method of preparation and use

Номер: US20130150466A1
Принадлежит: Saudi Basic Industries Corp

The invention relates to a catalyst and process for making syngas mixtures including hydrogen, carbon monoxide and carbon dioxide. The process comprises contacting a gaseous feed mixture containing carbon dioxide and hydrogen with the catalyst, where the catalyst comprises Mn oxide and an auxiliary metal oxide selected from the group consisting of La, Ca, K, W, Cu, Al and mixtures or combinations thereof. The process enables hydrogenation of carbon dioxide into carbon monoxide with high selectivity, and good catalyst stability over time and under variations in processing conditions. The process can be applied separately, but can also be integrated with other processes, both up-stream and/or down-stream including methane reforming or other synthesis processes for making products like alkanes, aldehydes, or alcohols.

Подробнее
20-06-2013 дата публикации

Hydrodesulfurization catalyst for hydrocarbon oil, process of producing same and method for hydrorefining

Номер: US20130153467A1

A hydrodesulfurization catalyst is produced by pre-sulfurizing a hydrodesulfurization catalyst Y including a support containing silica, alumina and titania and at least one metal component supported thereon and selected from VIA and VIII groups of the periodic table (comprising at least Mo), in which the total area of the diffraction peak area indicating the crystal structure of anatase titania (101) planes and the diffraction peak area indicating the crystal structure of rutile titania (110) planes in the support, measured by X-ray diffraction analysis being ¼ or less of the alumina diffraction peak area assigned to γ-alumina (400) planes. The molybdenum is formed into molybdenum disulfide crystal disposed in layers on the support by the pre-sulfurization, and having an average length of longer than 3.5 nm and 7 nm or shorter in the plane direction and an average number of laminated layers of more than 1.0 and 1.9 or fewer.

Подробнее
20-06-2013 дата публикации

Process of Producing Zeolite-Based Catalysts for Converting Oxygenates to Lower Olefins

Номер: US20130156688A1
Принадлежит: SUD-CHEMIE IP GMBH & CO. KG

A process of producing a catalyst based on pentasil-type crystalline aluminosilicate is described, including the steps of (a) treating hydrous aluminium oxide with an aqueous, acid-containing medium, (b) mixing the hydrous aluminium oxide treated with aqueous, acid-containing medium from step (a) with an H-zeolite and (c) calcining the mixture obtained in step (b). In addition, a catalyst is disclosed which is obtained by such a process, as well as its use in CMO and OTO processes. 1. A process for producing a catalyst based on pentasil-type crystalline aluminosilicate , comprising the steps of:(a) treating hydrous aluminium oxide with an aqueous, acid-containing medium,(b) mixing the hydrous aluminium oxide treated with aqueous, acid-containing medium from step (a) with an H-zeolite with an average diameter of its primary crystallites between 0.01 μm and 0.1 μm to form a mixture, and(c) calcining the mixture obtained in step (b),wherein at least 95 vol.-% of particles of the hydrous aluminium oxide (relative to an average diameter) are smaller than or equal to 100 μm.2. The process according to claim 1 , wherein the aqueous claim 1 , acid-containing medium comprises an aqueous inorganic acid.3. The process according to claim 1 , wherein the acid-containing medium comprises an aqueous organic acid.4. The process according to claim 1 , wherein in step (a) the aqueous claim 1 , acid-containing medium is added to the hydrous aluminium oxide in a quantity such that an acid concentration of from 0.005 to 2.5 mol H/mol AlO. results.5. The process according to claim 1 , wherein at least 97 vol.-% of the particles of the hydrous aluminium oxide (relative to the average diameter) are smaller than or equal to 100 μm.7. The process according to claim 1 , wherein the hydrous aluminium oxide is present in a quantity of from 10 wt.-% to 40 wt.-% aluminium oxide claim 1 , relative to the total weight of the end-product.8. The process according to claim 1 , wherein the calcining ...

Подробнее
04-07-2013 дата публикации

EXHAUST GAS PURIFICATION FILTER, AND METHOD FOR PRODUCING SAME

Номер: US20130171036A1
Принадлежит: OTSUKA CHEMICAL CO., LTD.

Provided are an exhaust gas purification filter having a high particulate matter (PM) combustion efficiency, a low coefficient of thermal expansion, and superior thermal resistance and a method for producing the same. An exhaust gas purification filter is formed by sintering columnar aluminum titanate particles whose surfaces have a catalyst material deposited thereon and which have an average aspect ratio (=number average major-axis length/number average minor-axis length) of 1.3 or more, wherein a catalyst made from the catalyst material by thermal treatment during the sintering is supported on the surface of the aluminum titanate. 1. An exhaust gas purification filter formed by sintering columnar aluminum titanate particles whose surfaces have a catalyst material deposited thereon and which have an average aspect ratio (=number average major-axis length/number average minor-axis length) of 1.3 or more ,wherein a catalyst made from the catalyst material by thermal treatment during the sintering is supported on the surface of the aluminum titanate.2. The exhaust gas purification filter according to claim 1 , wherein the catalyst contains a composite oxide containing: at least one metal of alkali metals and alkaline earth metals; and at least one of Al claim 1 , Si claim 1 , Ti claim 1 , and Zr.3. The exhaust gas purification filter according to claim 1 , wherein the exhaust gas purification filter is made by sintering a filter green body formed by extrusion and the coefficient of thermal expansion of the exhaust gas purification filter in a direction of the extrusion between 30° C. and 800° C. is 1.0×10/° C. or less.4. The exhaust gas purification filter according to claim 1 , wherein the exhaust gas purification filter is made by sintering a filter green body formed by extrusion and the c-axis crystal orientation ratio of the exhaust gas purification filter in the direction of the extrusion is 0.7 or more.5. The exhaust gas purification filter according to claim 1 ...

Подробнее
11-07-2013 дата публикации

Method for producing hydrocarbons with continuous charging of the catalyst

Номер: US20130178545A1
Принадлежит: IFP Energies Nouvelles IFPEN

The present invention relates to a method for the continuous production of hydrocarbons from synthesis gas in the presence of a catalyst comprising a synthesis step in which a synthesis gas is reacted in the presence of a catalyst in a Fischer-Tropsch synthesis reactor ( 4 ), characterised in that, at the same time as the synthesis step, the following successive steps are carried out: a) charging a catalyst precursor comprising cobalt oxide in a reduction reactor ( 2 ); b) reducing the catalyst precursor charged in step a) by placing it in contact with a reduction gas comprising hydrogen (H 2 ) and/or carbon monoxide (CO); and c) introducing the catalyst reduced in step b) into the synthesis reactor ( 4 ).

Подробнее
18-07-2013 дата публикации

METHOD FOR TUNING SURFACE STRUCTURE OF METALLIC NANO-CATALYST AND PREPARATION METHOD THEREOF

Номер: US20130184146A1
Принадлежит: XIAMEN UNIVERSITY

The present disclosure relates to a surface structure control and preparation process for a metal nanocatalyst involving a metal nanocatalyst. The present disclosure provides a surface structure control and continuous preparation system for a metal nanocatalyst, a metal nanocatalyst having an open surface structure and high surface energy, and a surface structure control and a preparation process thereof. The system is provided with a nucleation electrolytic cell, a distribution valve, at least two growth electrolytic cells, with two ends of the distribution valve being connected to an output port of the nucleation electrolytic cell and to input port of all the growth electrolytic cells, respectively. The metal nanocatalyst having an open surface structure is a single metal nanoscale crystal and has a high density of terrace atoms or active sites on the surface thereof. The precursor reaction solution is injected into the nucleation electrolytic cell, and a nucleation programmed potential is applied to one pair of electrodes in the nucleation electrolytic cell to obtain a nucleation reaction solution having the metal crystal nucleus formed, which is conveyed to the growth electrolytic cell through the distribution valve, a growth programmed potential is applied to one pair of electrodes in the growth electrolytic cell to obtain a metal nanoscale crystal having an open surface structure; controlling the growth time to obtain a reaction solution, and collecting a product by centrifugation. 1. A surface structure control and preparation system for a metal nanocatalyst , characterized in having a nucleation electrolytic cell , a distribution valve , at least two growth electrolytic cells , with one end of the distribution valve being connected to an output port of the nucleation electrolytic cell and the other end of the distribution valve being connected to input ports of all the growth electrolytic cells; the nucleation electrolytic cell has a cell body of the ...

Подробнее
18-07-2013 дата публикации

Catalyst treatment

Номер: US20130184360A1
Принадлежит: GTL F1 AG

A method of preparing a Fischer-Tropsch catalyst for handling, storage, transport and deployment, including the steps of impregnating a porous support material with a source of cobalt, calcining the impregnated support material activating the catalyst, and passivating the activated catalyst.

Подробнее
18-07-2013 дата публикации

Preparation of catalyst for selective hydrogenation of hydrogenatable precursors

Номер: US20130184499A1
Принадлежит: Bioamber International SARL

A reduced metallic catalyst or pre-activated catalyst is formed by contacting a precursor catalyst or a reduced metallic catalyst with a modifier solution in the presence of a source of hydrogen and heat treating the precursor catalyst or the reduced metallic catalyst at super-atmospheric pressure to obtain the reduced metallic catalyst from the precursor catalyst or the pre-activated catalyst from the reduced metallic catalyst. A method of hydrogenating a hydrogenatable precursor includes providing a reduced metallic catalyst or the pre-activated catalyst prepared with modifier buffer and contacting the reduced metallic catalyst or pre-activated catalyst with the hydrogenatable precursor in the presence of hydrogen and, optionally, in the presence of a modifier solution.

Подробнее
15-08-2013 дата публикации

CATALYTICALLY ACTIVE BODY FOR THE SYNTHESIS OF DIMETHYL ETHER FROM SYNTHESIS GAS

Номер: US20130210612A1
Принадлежит: BASF SE

The invention relates to a catalytically active body for the synthesis of dimethyl ether from synthesis gas. In particular, the invention relates to an improved catalytically active body for the synthesis of dimethyl ether, whereby the components of the active body comprise a defined particle size distribution. Furthermore, the present invention concerns a method for the preparation of a catalytically active body, the use of the catalytically active body and a method for preparation of dimethyl ether from synthesis gas. 119-. (canceled)20. Catalytically active body for the synthesis of dimethyl ether from synthesis gas , comprising a mixture of:(A) 70-90% by weight of a methanol-active component, selected from the group consisting of copper oxide, aluminium oxide, zinc oxide, amorphous aluminium oxide, ternary oxide or mixtures thereof,(B) 10-30% by weight of an acid component, selected from the group consisting of alumosilicate, γ-alumina and zeolite or mixtures thereof,(C) 0-10 Gew.-% by weight of at least one additive, whereby the sum of the components (A), (B) and (C) is in total 100% by weight.21. Catalytically active body according to claim 20 , whereby the component (A) has a particle size distribution characterized by a D-10 value of 5-140 μm claim 20 , a D-50 value of 40-300 μm claim 20 , and a D-90 value of 180-800 μm claim 20 , whereby the component (B) has a particle size distribution characterized by a D-10 value of 5-140 μm claim 20 , a D-50 value of 40-300 μm claim 20 , and a D-90 value of 180-800 μm and the particle size distribution of components (A) and (B) is maintained in the catalytically active body.22. Catalytically active body according to claim 20 , characterized in that component (A) comprises 50-80% by weight of copper oxide claim 20 , 15-35% by weight of ternary oxide and 15-35% by weight of zinc oxide and the sum of which is in total 100% by weight.23. Catalytically active body according to claim 20 , characterized in that component (A) ...

Подробнее
15-08-2013 дата публикации

Catalyst And Method For The Direct Synthesis Of Dimethyl Ether From Synthesis Gas

Номер: US20130211148A1
Принадлежит: BASF Corp

Catalysts and methods for their manufacture and use for the synthesis of dimethyl ether from syngas are disclosed. The catalysts comprise ZnO, CuO, ZrO 2 , alumina and one or more of boron oxide, tantalum oxide, phosphorus oxide and niobium oxide. The catalysts may also comprise ceria. The catalysts described herein are able to synthesize dimethyl ether directly from synthesis gas, including synthesis gas that is rich in carbon monoxide.

Подробнее
05-09-2013 дата публикации

Method for producing catalysts and catalysts thereof

Номер: US20130231241A1
Принадлежит: Yara International ASA

The invention relates to a process to produce catalysts by powder injection moulding and the catalysts thereof, wherein the catalysts are made by preparing a ceramic formulation with temperature controlled rheological properties comprising catalytic components, heating the powder formulation up to at least the fluid state transition temperature, shaping a sample by injecting the fluid powder formulation into an injection mould followed by cooling the injected powder formulation below the fluid state transition temperature, de-binding the shaped sample, and sintering the shaped sample to form a ceramic catalyst. Alternatively the ceramic structure may be formed initially followed by a coating of the ceramic structure by one or more catalytic compounds.

Подробнее
05-09-2013 дата публикации

Silica composite, method for producing the same, and method for producing propylene using the silica composite

Номер: US20130231515A1
Принадлежит: Asahi Kasei Chemicals Corp

The present invention provides a method for producing a silica composite by the steps of: preparing a raw material mixture containing silica and zeolite; drying the raw material mixture to obtain a dried product; and calcining the dried product, wherein the method comprising the step of allowing the raw material mixture to contain phosphoric acid and/or phosphate or bringing a solution of phosphoric acid and/or phosphate into contact with the zeolite and/or the dried product, or a combination thereof to thereby adjust a phosphorus content in the silica composite to 0.01 to 1.0% by mass based on the total mass of the silica composite.

Подробнее
12-09-2013 дата публикации

Spin formed catalyst

Номер: US20130233465A1
Принадлежит: Cummins Filtration IP Inc

A catalytic device and method for forming a catalytic device are described. The devices and methods described can be used for emissions systems in heavy duty diesel engines. In particular, a method of spin forming a catalytic device generally includes disposing a mat about an outer surface of a catalyst substrate and inserting the catalyst substrate and mat inside a shell. The mat is between the shell and the catalyst substrate. The shell, catalyst substrate, and mat can be spin formed into at least a generally elliptical shape but generally other than a circle shape.

Подробнее
10-10-2013 дата публикации

MECHANOCHEMICAL PRODUCTION OF ZEOLITES

Номер: US20130266507A1
Принадлежит: SUD-CHEMIE IP GMBH & CO. KG

The subject of the invention is a method for the synthesis of zeolites, comprising the following steps: a) providing a silicon source; b) providing an aluminium source; c) optionally providing at least one template; d) mixing the silicon source, aluminium source and optional template in order to produce a synthesis gel; e) grinding the synthesis gel; f) treating the ground synthesis gel under hydrothermal conditions in order to produce crystalline zeolite, as well as zeolites that can be obtained according to this method. The products obtained according to the method can be used as catalysts or catalyst supports. 1. Method for synthesis of zeolites , comprising the following steps:a) providing a silicon source;b) providing an aluminium source;c) mixing the silicon source and the aluminium source in order to produce a synthesis gel;d) grinding the synthesis gel;e) treating the ground synthesis gel under hydrothermal conditions in order to produce a crystalline zeolite.2. Method according to claim 1 , characterized in that the silicon source claim 1 , the aluminium source claim 1 , and the synthesis gel are present in an aqueous medium.3. Method according to claim 1 , characterized in that the silicon source comprises precipitated silicic acid.4. Method according to claim 1 , characterized in that the silicon source and the aluminium source are subjected to grinding.5. Method according to claim 1 , characterized in that the grinding is carried out with at least one grinding device claim 1 , wherein the at least one grinding device is selected from the group consisting of a ball mill claim 1 , an annular gap mill claim 1 , a bead mill claim 1 , a Manton-Gaulin mill claim 1 , and combinations thereof.6. Method according to claim 1 , characterized in that the grinding is carried out at a pH in the range from approximately 9 to 14.7. (canceled)8. Method according to claim 1 , characterized in that after treatment under hydrothermal conditions claim 1 , the obtained ...

Подробнее
17-10-2013 дата публикации

Electrocatalyst for oxygen reduction including silver/silver halide composite, fuel cell including the same, and preparing method of the same

Номер: US20130273458A1

The present disclosure relates to an electrocatalyst for oxygen reduction including a silver/silver halide composite, a fuel cell including the electrocatalyst for oxygen reduction, and a method for preparing the electrocatalyst for oxygen reduction.

Подробнее
17-10-2013 дата публикации

Method for Producing a Platinum Catalyst Precursor

Номер: US20130274089A1
Принадлежит: Sued Chemie IP GmbH and Co KG

The present invention relates to a method for producing a precursor of a supported platinum catalyst. To provide a method for producing a platinum catalyst precursor, by means of which supported platinum catalysts can be produced which have a relatively high activity, a method is proposed, comprising the steps of: a) impregnating an open-pored support material with platinum sulphite acid; b) calcining the impregnated zeolite material under a protective gas.

Подробнее
17-10-2013 дата публикации

IRON AND COBALT BASED FISCHER-TROPSCH PRE-CATALYSTS AND CATALYSTS

Номер: US20130274093A1
Принадлежит:

A method of making iron and cobalt pre-catalysts and catalysts in activated, finished form suitable for use in Fischer-Tropsch synthesis. The pre-catalysts are prepared by mixing an iron or cobalt salt, a base, and a metal oxide textural promoter or support. The reaction is carried out in a solvent deficient environment. The resulting product is then calcined at temperatures of about 300-500° C. to produce a metal oxide. The catalysts are prepared by reducing the metal oxide in the presence of hydrogen at temperatures of about 300-500° C. and carbiding the reduced metal in the case of iron. 1. A process for preparing an iron or cobalt based pre-catalyst comprising(a) reacting a metal salt selected from the group consisting of an iron salt and a cobalt salt with a base in the presence of a textural promoter, with no solvent added to produce a cobalt or iron oxide: and(b) calcining the product of step (a) at a temperature of about 150-500° C.2. The process of wherein the metal salt is an iron salt.3. The process of wherein a copper salt claim 2 , a potassium salt and the textural promoter are provided in step (a) and mixed together in one step prior to heating.4. The process of wherein the iron salt is selected from the group consisting of iron nitrate claim 2 , iron oxalate claim 2 , iron acetate claim 2 , iron chloride and mixtures thereof5. The process of wherein the base is selected from the group consisting of ammonium carbonate claim 2 , ammonium bicarbonate claim 2 , ammonium sesquicarbonate claim 2 , ammonium chloride claim 2 , ammonium oxalate claim 2 , ammonium sulfate claim 2 , ammonium hydroxide claim 2 , ammonium nitrate claim 2 , potassium carbonate claim 2 , lithium hydroxide claim 2 , sodium hydroxide claim 2 , potassium hydroxide claim 2 , magnesium hydroxide claim 2 , calcium hydroxide claim 2 , and mixtures thereof6. The process of wherein the base is ammonium bicarbonate or ammonium carbonate.7. The process of wherein the iron salt is iron nitrate ...

Подробнее
17-10-2013 дата публикации

Catalyst support materials with oxygen storage capacity (osc) and method of making thereof

Номер: US20130274096A1
Принадлежит: Pacific Industrial Development Corp

A new type of catalyst support with oxygen storage capacity (OSC) and methods of making the same are disclosed. The composition ratio is x(Ce 1-w Zr w 0 2 ):yM:zL:(1-x-y-z)AI 2 0 3 , where Ce 1-w Zr w 0 2 is the oxygen storage composition with stabilizer Zr0 2 , molar ratio (w) in the range of 0 to about 0.8, and a weight ratio (x) of about 0.05 to about 0.8; M is an interactive promoter for oxygen storage capacity with a weight ratio (y) of 0 to about 0.10; and L is a stabilizer for the support Al 2 0 3 with weight ratio (z) of from 0 to about 0.10. In some cases, M or L can act as both OSC promoter and thermal stabilizer. The weight percentage range of ceria-zirconia and other metal and rare earth oxides (x+y+z) is from about 5 to about 80% relative to total oxides. Combining platinum group metals (PGM) and adhesive with the catalyst supports, a new wash coat made therefrom is provided that comprises a mixture of catalyst support materials according to the relationship (a)RE-Ce—Zr0 2 +(3)CZMLA+(1-a-β)RE-AI 2 0 3 , where RE-Ce—Zr0 2 is a commercial OSC material of rare earth elements stabilized ceria zirconia having a weight ratio (a) ranging from 0 to about 0.7; CZMLA is the catalyst support material of the present disclosure having a weight ratio (β) ranging from about 0.2 to about 1 such that (α+β)<1; and RE-AI 2 0 3 is rare earth element stabilized alumina having a weight ratio equal to (1-α-β). The new wash coat made therefrom exhibits a lower activation temperature compared with traditional formulation of wash coat by at least 50° C. The new wash coat made therefrom also requires less RE-Ce—Zr0 2 oxide and/or less PGM in the formulation of emission control catalyst for gasoline and diesel engines.

Подробнее
31-10-2013 дата публикации

CARRIER FOR NOx REDUCTION CATALYST

Номер: US20130287665A1
Принадлежит: Mitsubishi Heavy Industries Ltd

A NOx reduction catalyst carrier yields a NOx reduction catalyst with an improved permissible dose of poisoning substances such as arsenic. More specifically, the present invention relates to a NOx reduction catalyst carrier comprising TiO 2 , having a honeycomb structure and having a specific surface area greater than 100 m 2 /g.

Подробнее
31-10-2013 дата публикации

Catalysts and process for producing same

Номер: US20130288891A1
Принадлежит: Santoku Corp

A catalyst, a hydrocarbon steam reforming catalyst, and a method for producing the same are provided. A catalytic metal containing at least Ni is supported on a composite oxide containing R, Zr, and oxygen, at a composition of not less than 10 mol % and not more than 90 mol % of R, not less than 10 mol % and not more than 90 mol % of Zr, and not less than 0 mol % and not more than 20 mol % of M (M: elements other than oxygen, R, and Zr), with respect to the total of the elements other than oxygen being 100 mol %, wherein the composite oxide has a specific surface area of 11 to 90 m 2 /g, and the largest peak in the wavelength range of 200 to 800 cm −1 of Raman spectrum with a full width at half maximum of 20 to 72 cm −1 .

Подробнее
31-10-2013 дата публикации

One-Step Synthesis of Monodisperse Transition Metal Core-Shell Nanoparticles with Solid Solution Shells

Номер: US20130288892A1
Принадлежит:

Methods of forming monodispersed core-shell nanoparticles are provided. A cobalt(II)-ligand component, a metal(II)-ligand component, an organic reducing agent, and a capping agent can be added to an organic solvent to form a reaction mixture. The reaction mixture is then heated to a dissolving temperature while under a gas (e.g., including methane) such that the reaction mixture becomes a reaction solution while stirring at the dissolving temperature. The reaction solution is then be heated to a reaction temperature (e.g., about 200° C. or more) while under the gas to form the core-shell nanoparticles, and the core-shell nanoparticles can be collected from the reaction solution. 1. A method of forming monodispersed core-shell nanoparticles , the method comprising:adding a cobalt(II)-ligand component, a metal(II)-ligand component, an organic reducing agent, and a capping agent to an organic solvent to form a reaction mixture, wherein the metal(II)-ligand comprises a metal(II) selected from the group consisting of copper(II), iron(II), chromium(II), scandium(II), nickel (II), zirconium (IV), and mixtures thereof;heating the reaction mixture to a dissolving temperature while under a gas, wherein the reaction mixture becomes a reaction solution while stirring at the dissolving temperature, and wherein the gas comprises methane;heating the reaction solution to a reaction temperature while under the gas to form the core-shell nanoparticles, wherein the reaction temperature is about 200° C. or more; andcollecting the core-shell nanoparticles from the reaction solution.2. The method as in claim 1 , further comprising:after collecting the core-shell nanoparticles, dispersing the core-shell nanoparticles in a solvent.3. The method as in claim 1 , wherein the metal(II)-ligand component comprises a copper(II)-ligand.4. The method as in claim 3 , wherein the copper(II)-ligand comprises copper(II)-acetylacetonate.5. The method as in claim 3 , wherein the core-shell nanoparticles ...

Подробнее
07-11-2013 дата публикации

Catalyst for the epoxidation of alkenes

Номер: US20130296587A1
Принадлежит: BASF SE

The present invention relates to a catalyst for preparing alkylene oxides, which is a supported silver catalyst having a novel promoter combination. The present invention further relates to a process for producing the catalyst and the use of the catalyst for the oxidation of alkylenes to alkylene oxides. In addition, the present invention relates to a process for preparing ethylene oxide from ethylene, which comprises the oxidation of ethylene in the presence of the stated catalyst.

Подробнее
14-11-2013 дата публикации

Catalyst for the hydrogenation of unsaturated hydrocarbons and process for its preparation

Номер: US20130303812A1
Принадлежит: Shell Oil Co

The present invention relates to a catalyst for the hydrogenation of unsaturated hydrocarbons, in particular aromatics with a broad molecular weight range, a process for the production thereof and a process for hydrogenating unsaturated hydrocarbons.

Подробнее
21-11-2013 дата публикации

METHOD FOR REGULATING THE DISTRIBUTION OF METALLIC NANOPARTICLES WITHIN THE RESIN SUPPORT

Номер: US20130310243A1
Принадлежит: NANJING UNIVERSITY

A method for regulating the distribution of metallic nanoparticles within the resin support is provided. This method uses the ion exchange or absorption resin bearing basic functional groups as the support; firstly introducing the metal in the form of anionic complexes onto the resin support through the ion exchange process, then realizing the purpose of regulating the distribution of the metal and its compound within the resin support by means of changing the concentration of the reductive or deposition agent in water solution and the reaction time. The regulated distribution of metallic nanoparticles within the resin support is in the form of rings with different depths and densities. The different distribution patterns result in improvements upon properties of the inorganic-organic composite material, such as reaction activity, reaction selectivity and metallic stability, and has significant referential value for preparation and structural regulation of other inorganic-organic composite materials of the same kind. 1. A method for regulating a distribution of metallic nanoparticles within a resin support , consisting of the following steps:{'sub': 4', '4', '4, 'sup': −', '2−', '2−, '(A) using a styrenic or acrylic ion exchange resin bearing basic functional groups as the support, introducing anionic complexes such as FeCl, CdCland PdClin a water solution onto the resin through an ion exchange process;'}(B) adopting a reductive or deposition agent to fixate the metal within the resin support through reduction or deposition process, and as a concentration of the reductive or deposition agent increases and the reaction time extends, the distribution ring of metallic nanoparticles within the resin support increases inwardly both in depth and in density.2. A method for regulating the distribution of metallic nanoparticles within the resin support as defined in claim 1 , wherein in step (A) the matrix of the support resin contains tertiary ammonium groups claim 1 , ...

Подробнее
21-11-2013 дата публикации

Processes for preparing amines and catalysts for use therein

Номер: US20130310560A1
Принадлежит: BASF SE

Processes for preparing an amine are described which comprise reacting a primary or secondary alcohol, aldehyde and/or ketone with hydrogen and a nitrogen compound selected from the group of ammonia, primary and secondary amines, in the presence of a zirconium dioxide-, copper- and nickel-containing catalyst. The catalytically active composition of the catalyst, before its reduction with hydrogen, comprises oxygen compounds of zirconium, of copper, of nickel, in the range from 1.0 to 5.0% by weight of oxygen compounds of cobalt, calculated as CoO, and in the range from 0.2 to 5.0% by weight of oxygen compounds of sulfur, of phosphorus, of gallium, of lead and/or of antimony, calculated in each case as H2SO4, H3PO4, Ga203, PbO and Sb203 respectively.

Подробнее
28-11-2013 дата публикации

Method of Simultaneously Removing Sulfur and Mercury from Hydrocarbon Material Using Catalyst by Means of Hydrotreating Reaction

Номер: US20130313165A1
Принадлежит: SK Innovation Co Ltd

Disclosed herein is a method of simultaneously removing sulfur and mercury from a hydrocarbon material, including: hydrotreating the hydrocarbon material containing sulfur and mercury in the presence of a catalyst including a metal supported with a carrier to convert sulfur into hydrogen sulfide, and adsorb mercury on a metal active site or a carrier of the catalyst in the form of mercury sulfide.

Подробнее
28-11-2013 дата публикации

Catalyst with an Ion-Modified Binder

Номер: US20130316899A1
Принадлежит: FINA TECHNOLOGY, INC.

A solid catalyst, such as a molecular sieve catalyst or solid acid catalyst, is supported by a binder, such as amorphous silica or alumina, wherein the binder is charged with metal ions to form an ion-modified binder. The ion-modified binder is capable of attachment to polar contaminants and inhibit their contact with the catalyst. The catalyst can be a zeolite and can be the catalyst for an alkylation reaction, such as the alkylation of benzene with ethylene. 122-. (canceled)23. A binder for providing mechanical support for a molecular sieve catalyst comprising:an ion-modified binder having at least one active metal species;wherein the ion-modified binder is adapted to attach to polar contaminants and thereby inhibit the contact of polar contaminants with the catalyst component;wherein metal ions make up 0.1% to 50% by weight of the ion-modified binder; andwherein the metal ions are chosen from the group consisting of Cu, Zn, Sn, Pb, Bi, Ba, Mn, and combinations thereof.24. The binder according to claim 23 , wherein the binder is composed primarily of amorphous silica or alumina.25. The binder according to claim 23 , wherein the metal ions make up 0.1% to 20% by weight of the ion-modified binder.26. The binder according to claim 23 , wherein the binder comprises silica claim 23 , alumina claim 23 , titania claim 23 , zirconia claim 23 , zinc oxide claim 23 , magnesia claim 23 , boria claim 23 , silica-alumina claim 23 , silica-magnesia claim 23 , chromia-alumina claim 23 , alumina-boria claim 23 , silica-zirconia claim 23 , silica gel claim 23 , clays claim 23 , or combinations thereof.27. The binder according to claim 26 , wherein the binder is amorphous silica or alumina.28. The binder according to claim 27 , wherein the binder is gamma- claim 27 , eta- claim 27 , or theta-alumina.29. A method for forming an ion-modified binder comprising:providing a binder;adding a metal ion precursor to an aqueous solution to form a metal ion solution;pouring the metal ion ...

Подробнее
05-12-2013 дата публикации

Desulfurization system, hydrogen-manufacturing system, fuel-cell system, fuel-desulfurization method, and method for manufacturing hydrogen

Номер: US20130323612A1
Принадлежит: JX Nippon Oil and Energy Corp

A desulfurization system includes: a fuel supply part for supplying a hydrocarbon-based fuel containing water and a sulfur compound to a subsequent stage; and a desulfurization part for desulfurizing the above hydrocarbon-based fuel supplied from the above fuel supply part, wherein, in the above desulfurization part, the above hydrocarbon-based fuel is brought into contact at a temperature of 65 to 105° C. with a catalyst prepared by loading silver on an X-type zeolite.

Подробнее
19-12-2013 дата публикации

Glass having a photocatalytic function

Номер: US20130336846A1

Provided is an inexpensive material having a photocatalytic action. A photocatalyst is obtained by halogenation-treating glass fibers containing silicon dioxide in its components. Fused quartz, soda-lime glass, non-alkali glass, and borosilicate glass may be used for the glass. Hydrofluoric acid, hydrochloric acid and hydrobromic acid may be used for the halogen acid, and hydrofluoric acid is most desirable. The glass can be particulate, fibrous or sheet form material. The glass exhibits a photocatalytic action even with visible light other than ultraviolet light, and also water repellent effect. The glass according to the invention is capable of decomposing organic substances, and therefore, it is used for window glass in buildings or in transportation such as automobiles, when formed in a plate shape, and for a filter in an air intake/exhaust apparatus, when formed in fibrous shape.

Подробнее
26-12-2013 дата публикации

Oxidation catalyst for a lean burn internal combustion engine

Номер: US20130340414A1
Принадлежит: JOHNSON MATTHEY PLC

An apparatus is disclosed. The apparatus comprises a lean-burn internal combustion engine, engine management means and an exhaust system for treating exhaust gas of the engine. The exhaust system comprises a first oxidation catalyst disposed on a first honeycomb monolith substrate. The first oxidation catalyst comprises platinum supported on a first metal oxide support comprising at least one reducible oxide, and is substantially free of alkali metals and alkaline earth metals. The engine management means is arranged, when in use, intermittently to modulate the lambda composition of the exhaust gas entering the first oxidation catalyst to a rich lambda composition.

Подробнее
26-12-2013 дата публикации

Exhaust gas purification catalyst

Номер: US20130345049A1
Автор: Isao Chinzei
Принадлежит: Toyota Motor Corp

An exhaust gas purification catalyst is provided with a catalyst coating layer ( 40 ) formed on the surface of a substrate ( 32 ). This catalyst coating layer ( 40 ) is formed of an upper catalyst coating layer ( 36 ) in which Rh particles are supported on a porous support, and a lower catalyst coating layer ( 34 ) in which Pd particles are supported on a support that contains an ACZ composite oxide made of alumina (Al 2 O 3 ), ceria (CeO 2 ), and zirconia (ZrO 2 ).

Подробнее
02-01-2014 дата публикации

MESOPOROUS CATALYSTS OF MAGNETIC NANOPARTICLES AND FREE-RADICAL-PRODUCING ENZYMES, AND METHODS OF USE

Номер: US20140004583A1
Принадлежит: CORNELL UNIVERSITY

A composition comprising mesoporous aggregates of magnetic nanoparticles and free-radical producing enzyme (i.e., enzyme-bound mesoporous aggregates), wherein the mesoporous aggregates of magnetic nanoparticles have mesopores in which the free-radical-producing enzyme is embedded. Methods for synthesizing the enzyme-bound mesoporous aggregates are also described. Processes that use said enzyme-bound mesoporous aggregates for depolymerizing lignin, removing aromatic contaminants from water, and polymerizing monomers polymerizable by a free-radical reaction are also described. 1. A composition comprising mesoporous aggregates of magnetic nanoparticles and free-radical producing enzyme , wherein said mesoporous aggregates of magnetic nanoparticles have mesopores in which said free-radical-producing enzyme is embedded.2. The composition of claim 1 , wherein said mesoporous aggregates of magnetic nanoparticles have an iron oxide composition.3. The composition of claim 1 , wherein said mesoporous aggregates of magnetic nanoparticles have a magnetic nanoparticle size distribution in which at least 90% of magnetic nanoparticles have a size of at least 3 nm and up to 30 nm claim 1 , and an aggregated particle size distribution in which at least 90% of said mesoporous aggregates of magnetic nanoparticles have a size of at least 10 nm and up to 500 nm.4. The composition of claim 1 , wherein said mesoporous aggregates of magnetic nanoparticles possess a saturated magnetization of at least 10 emu/g.5. The composition of claim 1 , wherein said mesoporous aggregates of magnetic nanoparticles possess a remanent magnetization up to 5 emu/g.6. The composition of claim 1 , wherein said free-radical-producing enzyme is contained in said mesoporous aggregates of magnetic nanoparticles in up to 100% of saturation capacity.7. The composition of claim 1 , wherein said free-radical-producing enzyme is selected from EC 1.11 oxidoreductases acting with peroxide as an acceptor and EC 1.10 ...

Подробнее
02-01-2014 дата публикации

Catalyst containing a modified y-type zeolite and a preparaton process thereof

Номер: US20140005032A1

The present invention discloses a catalytic cracking catalyst and a preparation process therefor. The catalytic cracking catalyst comprises a cracking active component, 10 wt %-70 wt % of a clay on the dry basis, and 10 wt %-40 wt % of an inorganic oxide binder (as oxide), relative to the weight of the catalytic cracking catalyst, wherein said cracking active component contains, relative to the weight of the catalytic cracking catalyst, 10 wt %-50 wt % of a modified Y-type zeolite on the dry basis and 0-40 wt % of other zeolite on the dry basis, wherein said modified Y-type zeolite is characterized by having a unit cell size of 2.420-2.440 nm; as percent by weight of the modified Y-type zeolite, a phosphorus content of 0.05-6%, a RE 2 O 3 content of 0.03-10%, and an alumina content of less than 22%; and a specific hydroxy nest concentration of less than 0.35 mmol/g and more than 0.05 mmol/g.

Подробнее
02-01-2014 дата публикации

PROCESS FOR PREPARING CATALYST

Номер: US20140005039A1
Принадлежит: Sumitomo Chemical Company, Limited

A process for preparing a catalyst for production of an olefin oxide containing (a) a copper oxide and (b) a ruthenium oxide, which comprises the step of drying a mixture containing a copper component, a ruthenium component, water, and at least one ion selected from the group consisting of a nitrate ion having a molar ratio to the copper of 3 or more and a halide ion having a molar ratio to the ruthenium of 9 or more, and calcining. 1. A process for preparing a catalyst for production of an olefin oxide comprising (a) a copper oxide and (b) a ruthenium oxide , which comprises the step ofdrying a mixture containing a copper component, a ruthenium component, water, and at least one ion selected from the group consisting of a nitrate ion having a molar ratio to the copper of 3 or more and a halide ion having a molar ratio to the ruthenium of 9 or more, and calcining.2. A process for preparing a catalyst for production of an olefin oxide comprising (a) a copper oxide , (b) a ruthenium oxide and (c) an alkaline metal component or alkaline earth metal component , which comprises the step ofdrying a mixture containing a copper component, a ruthenium component, an alkaline metal component or alkaline earth metal component, water, and at least one ion selected from the group consisting of a nitrate ion having a molar ratio to the copper of 3 or more and a halide ion having a molar ratio to the ruthenium of 9 or more, and calcining.3. A process for preparing a catalyst for production of an olefin oxide comprising (a) a copper oxide , (b) a ruthenium oxide , (c) an alkaline metal component or alkaline earth metal component and (d) a tellurium oxide , which comprises the step ofdrying a mixture containing a copper component, a ruthenium component, an alkaline metal component or alkaline earth metal component, a tellurium component, water, and at least one ion selected from the group consisting of a nitrate ion having a molar ratio to the copper of 3 or more and a halide ion ...

Подробнее
02-01-2014 дата публикации

Metal nanoparticle deposited inorganic nanostructure hybrids, uses thereof and processes for their preparation

Номер: US20140005040A1

This invention relates to a hybrid component comprising at least one nanoparticle of inorganic layered compound (in the form of fullerene-like structure or nanotube), and at least one metal nanoparticle, uses thereof as a catalyst, (e.g. photocatalysis) and processes for its preparation.

Подробнее
02-01-2014 дата публикации

Selective Hydrogenation Catalyst and Methods of Making and Using Same

Номер: US20140005449A1
Принадлежит: BASF Corp, Chevron Phillips Chemical Co LP

A composition comprising a support formed from a high surface area alumina and having a low angularity particle shape; and at least one catalytically active metal, wherein the support has pores, a total pore volume, and a pore size distribution; wherein the pore size distribution displays at least two peaks of pore diameters, each peak having a maximum; wherein a first peak has a first maximum of pore diameters of equal to or greater than about 200 nm and a second peak has a second maximum of pore diameters of less than about 200 nm; and wherein greater than or equal to about 5% of a total pore volume of the support is contained within the first peak of pore diameters.

Подробнее
02-01-2014 дата публикации

CATALYST AND PROCESS FOR THE CONVERSION OF OXYGENATES TO OLEFINS

Номер: US20140005457A1
Принадлежит:

The present invention relates to a catalyst for the conversion of oxygenates to olefins, wherein the catalyst comprises one or more zeolites of the MFI, MEL and/or MWW structure type and particles of one or more metal oxides, the one or more zeolites of the MFI, MEL and/or MWW structure type comprising one or more alkaline earth metals, and the particles of the one or more metal oxides comprising phosphorus, the phosphorus being present at least partly in oxidic form, and the one or more alkaline earth metals being selected from the group consisting of Mg, Ca, Sr, Ba and combinations of two or more thereof, to the preparation and use thereof, and to a process for converting oxygenates to olefins using the catalyst. 126-. (canceled)27. A catalyst for the conversion of oxygenates to olefins , wherein the catalyst comprises one or more zeolites of the MFI , MEL and/or MWW structure type and particles of one or more metal oxides , the one or more zeolites of the MFI , MEL and/or MWW structure type comprising one or more alkaline earth metals , and the particles of the one or more metal oxides comprising phosphorus , the phosphorus being present at least partly in oxidic form , andthe one or more alkaline earth metals being selected from the group consisting of Mg, Ca, Sr, Ba and combinations of two or more thereof.28. The catalyst according to claim 27 , wherein the one or more zeolites of the MFI claim 27 , MEL and/or MWW structure type comprise phosphorus claim 27 , the phosphorus being present at least partly in oxidic form.29. The catalyst according to claim 27 , wherein the one or more zeolites are of the MFI structure type.30. The catalyst according to claim 27 , wherein the alkaline earth metal is Mg.31. The catalyst according to claim 27 , wherein the one or more zeolites of the MFI claim 27 , MEL and/or MWW structure type comprise the one or more alkaline earth metals in a total amount in the range from 0.1 to 20% by weight claim 27 , based on the total amount ...

Подробнее
09-01-2014 дата публикации

HYBRID SILICA AND ALUMINA AS CATALYST MATRIX AND/OR BINDER IN BIOMASS CONVERSION CATALYSTS AND BIO-OIL UPGRADING

Номер: US20140007493A1
Принадлежит: KiOR, Inc.

The invention relates to catalyst compositions and components thereof for use in a catalytic process, and more particularly in a catalytic pyrolysis process or gasification of solid biomass material. In one aspect, a catalyst component is provided. The catalyst component includes a hybrid silica-alumina having a controlled Lewis acidity, and having a controlled porosity providing optimized accessibility for reactants. 1. A catalyst component , comprising hybrid silica-alumina having a controlled Lewis acidity , and having a controlled porosity providing optimized accessibility for reactants.2. The catalyst component of claim 1 , wherein the catalyst component is a catalyst matrix material.3. The catalyst component of claim 1 , wherein the catalyst component is a catalyst binder providing structural strength and attrition resistance to a catalyst composition.4. The catalyst component of claim 1 , wherein the hybrid silica-alumina is one or more of silica doped alumina claim 1 , alumina doped silica claim 1 , silicoaluminate claim 1 , and any mixture thereof.5. The catalyst component of claim 4 , wherein the silica doped alumina includes alumina particles and silica claim 4 , wherein at least a portion of the silica is distributed in pores in the alumina particles.6. The catalyst component of claim 4 , wherein the silica doped alumina includes alumina particles and silica claim 4 , wherein at least a portion of the silica is doped on a surface of the alumina particles.7. The catalyst component of claim 4 , wherein the alumina doped silica includes alumina and silica claim 4 , wherein the alumina is dispersed and doped on a surface of the silica.8. The catalyst component of claim 4 , wherein the silicoaluminate includes alumina and silica claim 4 , wherein the alumina is atomically dispersed in matrices in the silica.9. The catalyst component of claim 1 , wherein the controlled Lewis acidity includes suppressed density of Lewis acid sites in the hybrid silica-alumina. ...

Подробнее
09-01-2014 дата публикации

Exhaust gas purifying catalyst device

Номер: US20140010723A1
Принадлежит: FCC Co Ltd

An exhaust gas purifying catalyst device, which can have high durability against vibration and high temperatures, can be configured to suppress the peeling of the catalyst layer from the catalyst carrier member during use. Additionally, the metallic catalyst can be easily recovered after use. According to the present disclosure, an exhaust gas purifying catalyst device can comprise a catalyst carrier member on which metallic catalyst for exhaust gas purification can be carried characterized in that the catalyst carrier member can be formed of a sheet-like catalyst carrier made by a wet paper-making method, and that the metallic catalyst can be carried as a catalyst layer on surfaces of the sheet-like catalyst carrier after the sheet-like catalyst carrier has been baked.

Подробнее
09-01-2014 дата публикации

METHOD OF PRODUCING A CATALYST BODY CONTAINING URANIUM OXIDE AS ACTIVE COMPONENT

Номер: US20140011668A1
Принадлежит: AREVA GMBH

A method for producing a uranium oxide catalyst body includes the following steps: UOpowder, with x≦0.7, having a purity of at least 50% is sintered in a first sintering process to obtain a UOintermediate, where y≦0.25. Then the UOintermediate is oxidized with oxygen and converted in the process into a UOpowder, with z≦1. The UOpowder is pressed to form a blank having a shape that corresponds with the catalyst body to be produced. The blank is sintered in a second sintering process at a temperature of at least 900° C. in an oxygen-containing sintering atmosphere. 1. A method of producing a uranium oxide catalyst body , the method comprising the following steps:{'sub': 2+x', '2+y, 'a) sintering a UOpowder having a purity of at least 50% in a first sintering stage to obtain a UOintermediate;'}{'sub': 2+y', '2+y', '3', '8−z, 'b) oxidizing the UOintermediate with oxygen and thus converting the UOintermediate into a UOpowder;'}{'sub': 3', '8−z, 'c) pressing the UOpowder to obtain a blank having a shape substantially corresponding with the catalyst body to be produced; and'}d) sintering the blank at a temperature of at least 900° C. in an oxygen-containing sintering atmosphere in a second sintering stage.2. The method according to claim 1 , wherein in step a) claim 1 , the powder to be sintered is a UOpowder with x≦0.7 and the intermediate is a UOintermediate with y≦0.25 claim 1 , and wherein in step b) claim 1 , the intermediate is converted to UOpowder with z≦1.3. The method according to claim 1 , which comprises claim 1 , prior to step a) claim 1 , obtaining the UOpowder by a conversion of UF claim 1 , UO claim 1 , UNH claim 1 , UOor UF.4. The method according to claim 1 , wherein the UOpowder in step a) has powder particles with an average particle size of from 5 μm to 500 μm.5. The method according to claim 4 , which comprises using a UOpowder having an average particle size of from 10 μm to 150 μm.6. The method according to claim 1 , which comprises using a UOpowder ...

Подробнее
23-01-2014 дата публикации

Process for Producing Molecular Sieve Materials

Номер: US20140024523A1

In a process for producing a molecular sieve material, water, at least one source of an oxide of a tetravalent and/or a trivalent element and at least one structure directing agent is mixed in a reactor equipped with a mixer having a Froude number of at least 1, to produce a molecular sieve synthesis mixture having a solids content of at least about 20 wt %. The molecular sieve synthesis mixture is heated in the reactor while agitating the mixture with said mixer to form crystals of said molecular sieve material and the molecular sieve crystals are subsequently recovered from the reactor. 1. A process for producing a molecular sieve material , said process comprising the steps of:(a) mixing water, at least one source of an oxide of a tetravalent element, and optionally a trivalent element, and at least one structure directing agent in a reactor equipped with a mixer having a Froude number of at least 1, to produce a molecular sieve synthesis mixture having a solids content of at least 20 wt %;(b) heating the molecular sieve synthesis mixture in the reactor while agitating the mixture with said mixer to form crystals of said molecular sieve material; and then(c) recovering the molecular sieve crystals from the reactor.2. The process of and further comprising the step of:(d) prior to step (c), removing water from the mixture in the reactor while agitating the mixture with the mixer so as to decrease the water content of the mixture inside the reactor by at least 5 wt % and produce a partially dried mixture.3. The process of claim 2 , wherein said removing step (d) is conducted after formation of the crystals of said molecular sieve material.4. The process of claim 2 , wherein said removing step (d) is conducted by applying heat to said molecular sieve synthesis mixture.5. The process of claim 2 , wherein said removing step (d) is conducted by reducing the pressure in said reactor.6. The process of and further comprising the step of:(e) mixing said partially dried ...

Подробнее
06-02-2014 дата публикации

POROUS ALUMINUM OXIDE

Номер: US20140038819A1
Принадлежит: Ceram Tec GmbH

The invention relates to a substrate material, which is highly porous and which is provided with a mechanically stable, component-penetrating framework structure made of alpha-AlO, to methods for producing the substrate material, and to the use of the substrate material. 119-. (canceled)20. A substrate material comprising a mechanically stable , component-penetrating framework structure composed of alpha-AlO , wherein the substrate material is highly porous.21. The substrate material according to claim 20 , wherein the alpha-AlOcomprises up to 30 to 90% by weight based on the sum of all inorganic components of a first alpha-AlOcomponent having a primary crystal grain size of 1 to 3 μm and an agglomerate size of 3 to 5 μm claim 20 , and up to 10 to 70% by weight based on the sum of all inorganic components of a second alpha-AlOcomponent having a primary crystal grain size of 0.3 to 1 μm and an agglomerate size of 0.5 to 1 μm.22. The substrate material according to claim 20 , wherein the alpha-AlOcomprises up to 50% by weight based on the sum of all inorganic components of an AlOcomponent which has been formed in situ from an AlOprecursor material during the production.23. The substrate material according to claim 22 , wherein the AlOprecursor is selected from the group consisting of Al(OH) claim 22 , AlOOH and a transition alumina.24. The substrate material according to claim 23 , wherein the AlOprecursor is Al(OH)having a grain size of 1.3 μm.25. The substrate material according to claim 20 , wherein the substrate material has a multimodal pore structure with high porosity claim 20 , and at the same time has high mechanical strength.26. The substrate material according to claim 20 , wherein the substrate material has a specific surface measured according to the BET method of from 0.5 to 1.3 m/g.27. The substrate material according to claim 26 , wherein the specific surface is from 0.5 to 0.95 m/g.28. The substrate material according to claim 20 , wherein the weight ...

Подробнее
06-02-2014 дата публикации

POROUS ALUMINUM OXIDE

Номер: US20140038820A1
Принадлежит: Ceram Tec GmbH

The invention relates to a substrate material, which is highly porous and which is provided with a mechanically stable, component-penetrating framework structure made of alpha-AlO, to methods for producing the substrate material, and to the use of the substrate material. 118.-. (canceled)19. A substrate material comprising alpha-AlO , wherein the alpha-AlOcomprises a first alpha-AlOcomponent having a primary crystal grain size of 1 to 3 μm , wherein the substrate material is highly porous and is provided with a mechanically stable , component-penetrating framework structure comprising the alpha-AlO.20. A substrate according to claim 19 , wherein the first alpha-AlOis present in an amount of up to to 30 to 90% by weight based on the sum of all inorganic components.21. A substrate material according to claim 19 , wherein first alpha-AlOcomponent has an agglomerate size of 3 to 5 μm claim 19 , and further comprises up to 10 to 70% by weight based on the sum of all inorganic components of a second alpha-AlOcomponent having a primary crystal grain size of 0.3 to 1 μm and an agglomerate size of 0.5 to 1 μm.22. A substrate material according to claim 19 , wherein the substrate material contains claim 19 , in addition to the first and second alpha-AlOcomponent claim 19 , up to 50% by weight based on the sum of all inorganic components of an AlOcomponent which has been formed in situ from an AlOprecursor material during the production.23. A substrate material according to claim 19 , wherein the AlOprecursor is selected from the group consisting of Al(OH) claim 19 , AlOOH and a transition alumina.24. A substrate material according to claim 19 , wherein the AlOprecursor is Al(OH)having a grain size of 1.3 μm.25. A substrate material according to claim 19 , wherein the substrate material has a multimodal pore structure with high porosity claim 19 , and at the same time has high mechanical strength.26. A substrate material according to claim 19 , wherein the substrate material ...

Подробнее
13-02-2014 дата публикации

Process for passivation by a nitrogen-containing compound of a zeolitic catalyst, in particular a hydrocracking catalyst

Номер: US20140042057A1

The invention relates to a process for ex-situ treatment of a catalyst that contains at least one hydrogenating phase, and at least one amorphous silica-alumina or a zeolite that contains acid sites, whereby said process comprises: A stage for introducing nitrogen by contact at a temperature that is less than 100° C., with at least one basic nitrogen-containing compound that is ammonia or a compound that can be decomposed into ammonia, with said compound being introduced at a rate of 0.5-10% by weight (expressed in terms of N), and A sulfurization/activation stage with a gas that contains hydrogen and hydrogen sulfide at a temperature of at least 250° C., with this stage being carried out before or after the stage for introducing said nitrogen-containing compound, and the catalyst that is obtained is optionally dried. This treatment allows a rapid, effective start-up on the hydrocracking unit.

Подробнее