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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

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

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16-09-1996 дата публикации

УСТАНОВКА ДЛЯ ТЕСТИРОВАНИЯ КАТАЛИЗАТОРОВ ГИДРООБЛАГОРАЖИВАНИЯ НЕФТЯНЫХ ДИСТИЛЛЯТОВ

Номер: RU0000002814U1

Установка для тестирования катализаторов гидрооблагораживания нефтяных дистиллятов, содержащая блок подготовки сырья с нагревателем, реакторный блок с нагревателем и блок разделения продуктов, отличающаяся тем, что реакторный блок выполнен из четырех реакторов одинаковой высоты, при этом блок подготовки сырья и реакторный блок размещены в одном нагревателе, а нагреватель выполнен индукционным. (19) RU (11) (13) 2 814 U1 (51) МПК C10G 45/08 (1995.01) РОССИЙСКОЕ АГЕНТСТВО ПО ПАТЕНТАМ И ТОВАРНЫМ ЗНАКАМ (12) ОПИСАНИЕ ПОЛЕЗНОЙ МОДЕЛИ К СВИДЕТЕЛЬСТВУ (21), (22) Заявка: 94039208/20, 19.10.1994 (46) Опубликовано: 16.09.1996 (57) Формула полезной модели Установка для тестирования катализаторов гидрооблагораживания нефтяных дистиллятов, содержащая блок подготовки сырья с нагревателем, реакторный блок с нагревателем и блок разделения продуктов, отличающаяся тем, что реакторный блок выполнен из четырех реакторов одинаковой высоты, при этом блок подготовки сырья и реакторный блок размещены в одном нагревателе, а нагреватель выполнен индукционным. R U 2 8 1 4 (54) УСТАНОВКА ДЛЯ ТЕСТИРОВАНИЯ КАТАЛИЗАТОРОВ ГИДРООБЛАГОРАЖИВАНИЯ НЕФТЯНЫХ ДИСТИЛЛЯТОВ Ñòðàíèöà: 1 U 1 U 1 (73) Патентообладатель(и): Насиров Рашид Кулам оглы 2 8 1 4 (72) Автор(ы): Насиров Р.К., Дианова С.А., Сурков В.В., Воронин А.И., Талисман Е.Л., Ковальчук Н.А. R U (71) Заявитель(и): Насиров Р.К., Дианова С.А., Сурков В.В., Воронин А.И., Талисман Е.Л., Ковальчук Н.А. RU 2 814 U1 RU 2 814 U1 RU 2 814 U1 RU 2 814 U1

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05-01-2012 дата публикации

Production of Low Color Middle Distillate Fuels

Номер: US20120000817A1
Автор: Stuart S. Shih
Принадлежит: ExxonMobil Research and Engineering Co

In a process for producing a low color diesel and/or kerosene fuel, a middle distillate feed can be supplied to a reactor having at least one first catalyst bed containing a first desulfurization and/or isomerization catalyst and at least one second catalyst bed containing a decolorization catalyst downstream from the first catalyst bed(s). The feed can be reacted with the hydrogen in the presence of the first catalyst at a temperature from about 290° C. to about 430° C. to produce a first liquid effluent, which can be cooled by about 10° C. to about 40° C. with a quench medium and cascaded to the at least one second catalyst bed. The cooled first liquid effluent can then be reacted with hydrogen in the presence of the decolorization catalyst at a temperature from about 280° C. to about 415° C. to produce a second effluent having an ASTM color less than 2.5.

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27-01-2005 дата публикации

УСТАНОВКА ТЕРМОМЕХАНИЧЕСКОГО КРЕКИНГА И ГИДРОГЕНИЗАЦИИ УГЛЕВОДОРОДОВ

Номер: RU0000043545U1

Установка термомеханического крекинга и гидрогенизации углеводородов, включающая бункер исходного материала и реактор, соединенные питающим устройством, отличающаяся тем, что реактор снабжен по меньшей мере одним излучателем акустических колебаний, связанным с генератором указанных колебаний. РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) 43 545 (13) U1 (51) МПК C10G 47/30 (2000.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ, ПАТЕНТАМ И ТОВАРНЫМ ЗНАКАМ (12) ОПИСАНИЕ ПОЛЕЗНОЙ МОДЕЛИ К ПАТЕНТУ (21), (22) Заявка: 2004127084/22 , 13.09.2004 (24) Дата начала отсчета срока действия патента: 13.09.2004 (45) Опубликовано: 27.01.2005 (73) Патентообладатель(и): Общество с ограниченной ответственностью "НОВЫЕ ТЕХНОЛОГИИ БИЗНЕСА" (RU) U 1 4 3 5 4 5 R U Ñòðàíèöà: 1 U 1 Формула полезной модели Установка термомеханического крекинга и гидрогенизации углеводородов, включающая бункер исходного материала и реактор, соединенные питающим устройством, отличающаяся тем, что реактор снабжен по меньшей мере одним излучателем акустических колебаний, связанным с генератором указанных колебаний. 4 3 5 4 5 (54) УСТАНОВКА ТЕРМОМЕХАНИЧЕСКОГО КРЕКИНГА И ГИДРОГЕНИЗАЦИИ УГЛЕВОДОРОДОВ R U Адрес для переписки: 197136, Санкт-Петербург, а/я 55, пат.пов. Ю.В. Рыбакову, рег.№ 244 (72) Автор(ы): Ольховский Э.В. (RU) U 1 U 1 4 3 5 4 5 4 3 5 4 5 R U R U Ñòðàíèöà: 2 RU 5 10 15 20 25 30 35 40 45 50 43 545 U1 Полезная модель относится к термомеханическому крекингу и гидрогенизации химических веществ. Известны установки термомеханического крекинга и гидрогенизации углеводородов в жидкой или твердой форме, карбонатов, извести, нефтеносных сланцев и песков, маслянистых остатков нефтеперерабатывающих заводов и т.п. Наиболее близким по технической сущности к заявляемой полезной модели является устройство, описанное в патенте РФ, включающее бункер исходного материала и реактор, соединенные питающим устройством (1). Однако, КПД указанного устройства недостаточен. Задачей полезной модели является обработка углеродистого ...

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10-07-2013 дата публикации

УСТРОЙСТВО РИФОРМИНГА СМЕСИ ТЯЖЕЛЫХ ПИРОЛИЗНЫХ СМОЛ И КИСЛОЙ ВОДЫ

Номер: RU0000129924U1

Устройство для риформинга смеси тяжелых пиролизных смол характеризуется тем, что оно содержит емкость перемешивания (гомогенизации) смеси тяжелых пиролизных смол и кислой воды с размещенными в нижней ее части барботажным коллектором, связанным с источником кислой воды, и барботажным коллектором, связанным с источником тяжелых углеводородов, в емкости перемешивания размещен в верхней части патрубок вывода гомогенизированной смеси, соединенный с огнепреградителем, который связан с емкостью реактора риформинга, реактор риформинга с расположенными в верхней части патрубком отвода углеводородов (их гомологов) и водородосодержащего синтез-газа, и в нижней части - системой выгрузки кокса, при этом внутри реактора расположен ориентированный вдоль его осевой линии змеевик, соединенный с огнепреградителем, а на корпусе реактора установлены индукционные петли генератора тока высокой частоты. РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 129 924 U1 (51) МПК C10G 35/16 (2006.01) C10G 49/00 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ (21)(22) Заявка: ПОЛЕЗНОЙ МОДЕЛИ К ПАТЕНТУ 2013104149/04, 01.02.2013 (24) Дата начала отсчета срока действия патента: 01.02.2013 (72) Автор(ы): Шимченко Сергей Петрович (RU) (73) Патентообладатель(и): Шимченко Сергей Петрович (RU) R U Приоритет(ы): (22) Дата подачи заявки: 01.02.2013 (45) Опубликовано: 10.07.2013 Бюл. № 19 1 2 9 9 2 4 R U Формула полезной модели Устройство для риформинга смеси тяжелых пиролизных смол характеризуется тем, что оно содержит емкость перемешивания (гомогенизации) смеси тяжелых пиролизных смол и кислой воды с размещенными в нижней ее части барботажным коллектором, связанным с источником кислой воды, и барботажным коллектором, связанным с источником тяжелых углеводородов, в емкости перемешивания размещен в верхней части патрубок вывода гомогенизированной смеси, соединенный с огнепреградителем, который связан с емкостью реактора риформинга, реактор риформинга с расположенными в верхней части ...

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20-07-2013 дата публикации

УСТАНОВКА ДЛЯ ПОЛУЧЕНИЯ ДИЗЕЛЬНЫХ ТОПЛИВ

Номер: RU0000130311U1

Установка для получения дизельного топлива, включающая в себя ректификационную колонну, блок подготовки сырья, реакторный блок, состоящий из печи, реактора гидроочистки, теплообменников и холодильников, отличающаяся тем, что она дополнительно содержит перед блоком подготовки сырья блок экстракции серосодержащих соединений, состоящий из связанных между собой экстрактора, ректификационной колонны для отделения экстрагента, нагревателей и холодильников, а также блок стабилизации гидроочищенного продукта, включающий в себя сепаратор, теплообменник, колонну стабилизации и холодильник. РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 130 311 U1 (51) МПК C10G 21/06 (2006.01) C10G 45/02 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ (21)(22) Заявка: ПОЛЕЗНОЙ МОДЕЛИ К ПАТЕНТУ 2012143774/04, 04.10.2012 (24) Дата начала отсчета срока действия патента: 04.10.2012 (45) Опубликовано: 20.07.2013 Бюл. № 20 (73) Патентообладатель(и): Общество с ограниченной ответственностью "Институт по проектированию предприятий нефтедобывающей и нефтехимической промышленности", ООО "ЛЕНГИПРОНЕФТЕХИМ" (RU) 1 3 0 3 1 1 Адрес для переписки: 193313, Санкт-Петербург, ул. Подвойского, 14, корп.1, кв.741, В.А. Кузнецову R U Приоритет(ы): (22) Дата подачи заявки: 04.10.2012 (72) Автор(ы): Фомин Александр Степанович (RU), Кашин Олег Николаевич (RU), Сомов Вадим Евсеевич (RU), Лисицын Николай Васильевич (RU), Ермоленко Алла Дмитриевна (RU), Журавлев Артем Николаевич (RU), Гайле Александр Александрович (RU), Кузичкин Николай Васильевич (RU) 1 3 0 3 1 1 R U Формула полезной модели Установка для получения дизельного топлива, включающая в себя ректификационную колонну, блок подготовки сырья, реакторный блок, состоящий из печи, реактора гидроочистки, теплообменников и холодильников, отличающаяся тем, что она дополнительно содержит перед блоком подготовки сырья блок экстракции серосодержащих соединений, состоящий из связанных между собой экстрактора, ректификационной колонны для отделения ...

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20-03-2014 дата публикации

УСТАНОВКА ДЛЯ ПЕРЕРАБОТКИ НЕФТЕШЛАМОВ

Номер: RU0000138715U1

Установка для переработки нефтешламов, включающая сообщенные между собой устройство для обработки исходного сырья, устройство выделения конечных продуктов, соединенного с устройством для охлаждения и конденсации конечного продукта, отличающаяся тем, что устройство для обработки исходного сырья выполнено из трех, соединенных между собой диафрагм с разным диаметром сечений, на выходе которых установлен полый шар, в котором закреплен металлический шар, а устройство для выделения конечных продуктов состоит из блока подготовки, фильтров-адсорберов, каталитического реактора, источника водяного пара, причем блок подготовки выполнен в виде горизонтального расположенного тора, внутри которого установлены ребра, параллельно боковым стенкам, по всей длине корпуса, вход которого соединен с устройством для обработки исходного сырья и источником водяного пара, а выход с фильтрами-адсорберами, состоящими из корпуса, чугунного и керамического наполнителя, расположенного слоями друг за другом, под днищем которых расположены термостатические рубашки, выходы фильтров-адсорберов соединены с противоположно направленными входами каталитического реактора, который соединен с источником водяного пара. РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 138 715 U1 (51) МПК C10G 47/32 (2006.01) C10G 47/02 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ (21)(22) Заявка: ПОЛЕЗНОЙ МОДЕЛИ К ПАТЕНТУ 2013147315/04, 22.10.2013 (24) Дата начала отсчета срока действия патента: 22.10.2013 (72) Автор(ы): Зайченко Владимир Николаевич (RU) (73) Патентообладатель(и): Зайченко Владимир Николаевич (RU) R U Приоритет(ы): (22) Дата подачи заявки: 22.10.2013 (45) Опубликовано: 20.03.2014 Бюл. № 8 1 3 8 7 1 5 R U Формула полезной модели Установка для переработки нефтешламов, включающая сообщенные между собой устройство для обработки исходного сырья, устройство выделения конечных продуктов, соединенного с устройством для охлаждения и конденсации конечного продукта, отличающаяся тем, что устройство ...

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12-03-2018 дата публикации

ТРУБЧАТАЯ ПЕЧЬ КОНВЕКЦИОННОГО НАГРЕВА ТЕПЛОНОСИТЕЛЯ С ПРИНУДИТЕЛЬНОЙ РЕЦИРКУЛЯЦИЕЙ ДЫМОВЫХ ГАЗОВ

Номер: RU0000177784U1

Полезная модель относится к устройствам для нагрева теплоносителей (жидкостей, газов и других), конкретно к трубчатым печам и может быть использована в нефтяной, газовой, нефтеперерабатывающей и нефтехимической отраслях промышленности. Технический результат заявляемой полезной модели заключается в увеличении срока службы устройства за счет устранения воздействия пламени горелочного узла на стенки камеры сгорания, устранения перегрева стенок теплообменной камеры за счет введения камеры смешения и устранения перегрева трубного змеевика благодаря улучшению теплопередачи от горелочного узла к содержимому трубного змеевика за счет использования оребренных труб с внутренними турбулизирующими вставками, при снижении теплопотерь. Указанный технический результат достигается тем, что трубчатая печь содержит корпус с размещенной внутри камерой сгорания, снабженной горелочным узлом, и теплообменной камерой, снабженной по крайней мере одним трубным змеевиком; рециркуляционный вентилятор, вход которого соединен с выходом теплообменной камеры, согласно решению печь содержит камеру смешения, вход которой соединен с выходом камеры сгорания и выходом рециркуляционного вентилятора, а выход соединен с входом теплообменной камеры, камера смешения выполнена из двух концентрических обечаек, между которыми расположено спиральное ребро жесткости, образующее воздушный канал от выхода камеры смешения к входу камеры смешения; печь содержит дутьевой вентилятор, выход которого соединен с воздушным каналом у выхода камеры смешения; горелочный узел снабжен входом для воздуха, соединенным с воздушным каналом у входа камеры смешения; камера сгорания, камера смешения и теплообменная камера расположены в корпусе так, чтобы обеспечить направление потока газа в теплообменной камере под углом 90° относительно направления потока газа в камерах сгорания и смешения. Трубный змеевик выполнен из гладких или оребренных труб и снабжен внутренними турбулизирующими вставками в наиболее теплонапряженных зонах ...

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26-03-2018 дата публикации

УСТРОЙСТВО ДЛЯ ПОЛУЧЕНИЯ МИКРОКРИСТАЛЛОВ МАГГЕМИТА

Номер: RU0000178133U1

Полезная модель относится к устройствам, предназначенным для получения микрокристаллов высокодисперсного оксида железа в форме маггемита (γ-FeO) электрохимическим способом при комнатной температуре и атмосферном давлении, которые могут быть использованы в качестве основы для композиционных материалов, в частности, обладающих значительной удельной поверхностью и ярко выраженными ферромагнитными свойствами порошкообразных сорбентов, отделяемых под действием магнитного поля. Устройство содержит ванну с электролитом (40%-ным водным раствором гидроксида натрия), снабженную пластинчатыми железными электродами, подключенными к источнику постоянного тока. Устройство дополнительно оснащено постоянным магнитом, монтируемым на железном пластинчатом катоде, датчиком температуры и охладительным узлом, размещаемыми в объеме электролита, поддерживающими его температуру на уровне, не превышающем t=45°C. Технический результат, получаемый при реализации изобретения, состоит в значительном упрощении процесса получения микрокристаллов маггемита, повышении его эффективности и экономичности. РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 178 133 U1 (51) МПК C25B 9/00 (2006.01) C25B 1/00 (2006.01) C10G 49/06 (2006.01) C25B 1/06 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ПОЛЕЗНОЙ МОДЕЛИ К ПАТЕНТУ (52) СПК C25B 9/00 (2017.08); C25B 1/00 (2017.08); C25B 1/06 (2017.08) (21)(22) Заявка: 2017135699, 05.10.2017 (24) Дата начала отсчета срока действия патента: 26.03.2018 Приоритет(ы): (22) Дата подачи заявки: 05.10.2017 (45) Опубликовано: 26.03.2018 Бюл. № 9 2000336495 A, 05.12.2000. RU 93007681 A, 30.04.1995. (54) УСТРОЙСТВО ДЛЯ ПОЛУЧЕНИЯ МИКРОКРИСТАЛЛОВ МАГГЕМИТА (57) Реферат: Полезная модель относится к устройствам, (40%-ным водным раствором гидроксида натрия), предназначенным для получения снабженную пластинчатыми железными микрокристаллов высокодисперсного оксида электродами, подключенными к источнику железа в форме маггемита (γ-Fe2O3) постоянного тока. Устройство ...

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29-06-2021 дата публикации

Устройство усовершенствованной микроповерхностной реакции гидрирования с нисходящим потоком и фиксированным слоем для производства нефтепродуктов

Номер: RU0000205181U1

Полезная модель относится к устройству усовершенствованной микроповерхностной реакции гидрирования с нисходящим потоком и фиксированным слоем для производства нефтепродуктов. Устройство включает в себя реактор с фиксированным слоем и генератор микроповерхностей, при этом генератор микроповерхностей расположен над реактором с фиксированным слоем для преобразования энергии давления водорода и/или кинетической энергии нефтепродукта во время реакции в поверхностную энергию пузырька и передачи поверхностной энергии пузырьку водорода, так что пузырек водорода дробится на микропузырьки и микропузырьки смешиваются с нефтепродуктом в процессе реакции для образования газожидкостной эмульсии; реактор с фиксированным слоем используется в качестве места протекания реакции гидрирования для образования стабильной усовершенствованной газожидкостной системы для реакции с фиксированным слоем, когда газожидкостная эмульсия поступает в реактор с фиксированным слоем; резервуар для разделения газа и жидкости соединен с реактором с фиксированным слоем для отделения газа от жидкости в смеси, являющейся результатом реакции в реакторе с фиксированным слоем. Устройство микроповерхностной реакции гидрирования с фиксированным слоем имеет преимущества низкого потребления энергии, низкого рабочего давления, большой площади межфазной границы массопереноса газ-жидкость, высокой видимой скорости реакции и высокой эффективности использования газа. РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 205 181 U1 (51) МПК B01J 8/02 (2006.01) C10G 45/08 (2006.01) C10G 45/22 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ПОЛЕЗНОЙ МОДЕЛИ К ПАТЕНТУ (52) СПК B01J 8/02 (2021.02); C10G 45/08 (2021.02); C10G 45/22 (2021.02) (21)(22) Заявка: 2020129865, 06.06.2019 (24) Дата начала отсчета срока действия патента: Дата регистрации: 29.06.2021 15.03.2019 CN 201910196596.X (45) Опубликовано: 29.06.2021 Бюл. № 19 (85) Дата начала рассмотрения заявки PCT на национальной фазе: 10.09.2020 (73) ...

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15-10-2021 дата публикации

УСТРОЙСТВО УСОВЕРШЕНСТВОВАННОЙ МИКРОПОВЕРХНОСТНОЙ РЕАКЦИИ ГИДРИРОВАНИЯ

Номер: RU0000207190U1

Полезная модель представляет собой устройство усовершенствованной микроповерхностной реакции гидрирования, которое включает корпус реактора, используемый в качестве реакционной камеры в процессе реакции гидрирования, обеспечивающий полноценное протекание реакции гидрирования, генератор микроповерхностей, соединенный с корпусом реактора для дробления водородного и/или жидкого реагента в генераторе микроповерхностей на микропузырьки и/или микрокапли с диаметром микронного уровня посредством механической и/или турбулентной микроструктуры в заданном режиме функционирования до того, как водород и жидкость и/или смесь твердых и жидких материалов в процессе реакции гидрирования войдут в корпус реактора, для увеличения площади межфазного переноса между водородом и жидкостью и/или смесью твердых и жидких материалов в процессе реакции гидрирования, повышения эффективности массопереноса между фазами реакции и улучшения реакции гидрирования при заданных условиях температуры и давления. Полезная модель эффективно решает проблему низкой скорости массопереноса из-за малой площади контакта границы раздела фаз реагентов при протекании реакции. РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 207 190 U1 (51) МПК B01J 8/02 (2006.01) C10G 45/08 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ПОЛЕЗНОЙ МОДЕЛИ К ПАТЕНТУ (52) СПК B01J 8/02 (2021.08); C10G 45/08 (2021.08) (21)(22) Заявка: 2020129854, 06.06.2019 (24) Дата начала отсчета срока действия патента: Дата регистрации: 15.10.2021 15.03.2019 CN 201910196624.8 (45) Опубликовано: 15.10.2021 Бюл. № 29 (73) Патентообладатель(и): НАНКИН ЙАНЧАНГ РИЭКШН ТЕКНОЛОДЖИ РИСЁРЧ ИНСТИТЬЮТ КО. ЛТД (CN) (85) Дата начала рассмотрения заявки PCT на национальной фазе: 10.09.2020 (86) Заявка PCT: 2 0 7 1 9 0 Приоритет(ы): (30) Конвенционный приоритет: R U 06.06.2019 (72) Автор(ы): ЖАНГ Жибинг (CN), ЖОУ Женг (CN), ЖАНГ Фенг (CN), ЛИ Леи (CN), МЕНГ Веимин (CN), ВАНГ Баоронг (CN), ЙАНГ Гаодонг (CN), ЛУО Хуаксун (CN), ЙАНГ Гуокианг (CN), ...

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12-01-2012 дата публикации

Systems for increasing catalyst concentration in heavy oil and/or coal resid hydrocracker

Номер: US20120009094A1
Принадлежит: Individual

Systems for hydrocracking a heavy oil feedstock employ a colloidally or molecularly dispersed catalyst (e.g., molybdenum sulfide) which provide for concentration of the colloidally dispersed catalyst within the lower quality materials requiring additional hydrocracking. In addition to increased catalyst concentration, the inventive systems and methods provide increased reactor throughput, increased reaction rate, and of course higher conversion of asphaltenes and lower quality materials. Increased conversion levels of asphaltenes and lower quality materials also reduces equipment fouling, enables the reactor to process a wider range of lower quality feedstocks, and can lead to more efficient use of a supported catalyst if used in combination with the colloidal or molecular catalyst.

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12-01-2012 дата публикации

Method and System for Synthesizing Liquid Hydrocarbon Compounds

Номер: US20120010304A1
Автор: Kazuhiko Tasaka

Provided is a method for synthesizing liquid hydrocarbon compounds wherein synthesizing liquid hydrocarbon compounds from a synthesis gas by a Fisher-Tropsch synthesis reaction. The method includes a first absorption step of absorbing a carbon dioxide gas, which is contained in gaseous by-products generated in the Fisher-Tropsch synthesis reaction, with an absorbent, and a second absorption step of absorbing a carbon dioxide gas, which is contained in the synthesis gas, with the absorbent which is passed through the first absorption step.

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19-01-2012 дата публикации

Multiphase contact and distribution apparatus for hydroprocessing

Номер: US20120014847A1
Принадлежит: Chevron USA Inc

Systems and apparatus for mixing, cooling, and distributing multiphase fluid mixtures within a reactor, wherein reactor internal apparatus of the present invention provides not only improved fluid mixing and distribution to each underlying catalyst bed surface, but also offers other advantages including: decreased mixing tray height; easier maintenance, assembly and disassembly; and decreased amounts of fabrication material. In an embodiment, fluid may be evenly distributed to a catalyst bed from a fluid distribution unit comprising a nozzle tray including a plurality of nozzles, wherein the nozzles include at least one liquid inlet disposed tangentially to an inner surface of the nozzle.

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02-02-2012 дата публикации

Catalyst- and lignin-comprising composition and its use for preparing an aromatics composition

Номер: US20120029243A1
Принадлежит: BASF SE

The present invention relates to a composition (“composite”) comprising lignin and at least one catalyst dispersed in the composition. The invention further provides a process for producing such a catalyst- and lignin-comprising composition and its use for preparing an aromatics composition.

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19-04-2012 дата публикации

Process for producing middle distillates by hydroisomerization and hydrocracking of a heavy fraction derived from a fischer-tropsch effluent

Номер: US20120091034A1
Принадлежит: Eni Spa, IFP Energies Nouvelles IFPEN

The present invention describes a process for producing middle distillates from a C5+ liquid paraffinic fraction, termed a heavy fraction, with an initial boiling point in the range 15° C. to 40° C. produced by Fischer-Tropsch synthesis, comprising the following steps in succession: passing said C5+ liquid paraffinic fraction, termed a heavy fraction, over at least one ion exchange resin at a temperature in the range 80° C. to 150° C., at a total pressure in the range 0.7 to 2.5 MPa, at an hourly space velocity in the range 0.2 to 2.5 h −1 ; eliminating at least a portion of the water formed in step a); hydrogenating the unsaturated olefinic type compounds of at least a portion of the effluent derived from step b) in the presence of hydrogen and a hydrogenation catalyst; and hydroisomerization/hydrocracking of at least a portion of the hydrotreated effluent derived from step c) in the presence of hydrogen and a hydroisomerization/hydrocracking catalyst.

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03-05-2012 дата публикации

Fuel and base oil blendstocks from a single feedstock

Номер: US20120108869A1
Принадлежит: Chevron USA Inc

A method comprising the steps of providing a quantity of biologically-derived oil comprising triglycerides; processing the biologically derived oil so as to transesterify at least some of the triglycerides contained therein to yield a quantity of saturated monoesters and unsaturated monoesters; oligomerizing at least some of the unsaturated monoesters to yield a quantity of fatty acid ester oligomers; separating at least some of the saturated monoesters from the fatty acid ester oligomers; and hydrotreating at least some of the fatty acid ester oligomers to yield a quantity of alkanes.

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03-05-2012 дата публикации

Fuel and base oil blendstocks from a single feedstock

Номер: US20120108871A1
Автор: Stephen J. Miller
Принадлежит: Chevron USA Inc

A method comprising providing a fatty acyl mixture comprising: (i) a C 10 -C 16 acyl carbon atom chain content of at least 30 wt. % wherein at least 80% of the C 10 -C 16 acyl carbon atom chains are saturated; and (ii) a C 18 -C 22 acyl carbon atom chain content of at least 20 wt. % wherein at least 50% of the acyl C 18 -C 22 carbon atom chains contain at least one double bond; hydrolyzing the mixture to yield a quantity of C 10 -C 16 saturated fatty acids and C 18 -C 22 unsaturated fatty acids; oligomerizing at least some of the C 18 -C 22 unsaturated fatty acids to yield a quantity of C 36+ fatty acid oligomers; hydrotreating at least some of the C 10 -C 16 saturated fatty acids and at least some of the C 36+ fatty acid oligomers to yield a quantity of diesel fuel blendstock and C 36+ alkanes; and separating at least some of the diesel fuel blendstock from the C 36+ alkanes.

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17-05-2012 дата публикации

Device and method for controlling the conversion of biomass to biofuel

Номер: US20120117815A1
Принадлежит: RENEWABLE FUEL TECHNOLOGIES Inc

Embodiments presented herein describe an apparatus and method to control the conversion of carbonaceous materials, particularly biomass and those biomass resources, into a high performance solid fuel. This method, and the apparatus described as the means to accomplish this method, provides a process having a control system that enables the system to produce a fuel of uniform quality, even with a change in biomass supply.

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17-05-2012 дата публикации

Metallic Composite Comprising a Load-Bearing Member and a Corrosion Resistant Lager

Номер: US20120121930A1
Принадлежит: Sandvik Intellectual Property AB

A composite material intended for components used in corrosive environments, wherein said material comprises a corrosion-resistant part and a load-bearing part, wherein said parts are disposed adjacent one another, wherein the corrosion-resistant part is a copper-aluminium alloy (Cu/Al) and wherein the load-bearing part is comprised of an iron-based (Fe), a nickel-based (Ni) or a cobalt-based (Co) alloy. The invention is characterized in that the diffusion barrier is disposed between the corrosion-resistant part and the load-bearing part, and in that the diffusion barrier contains one of the substances chromium (Cr) or iron (Fe) or iron (Fe) that contains one of the alloying substances chromium (Cr) or carbon (C).

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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.

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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.

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24-05-2012 дата публикации

Process for Cracking Heavy Hydrocarbon Feed

Номер: US20120125812A1
Принадлежит: EQUISTAR CHEMICALS LP

A process for cracking a heavy hydrocarbon feed comprising a vaporization step, a hydroprocessing step, and a steam cracking step is disclosed. The heavy hydrocarbon feed is passed to a first zone of a vaporization unit to separate a first vapor stream and a first liquid stream. The first liquid stream is passed to a second zone of the vaporization unit and contacted intimately with a counter-current steam produce a second vapor stream and a second liquid stream. The first vapor stream and the second vapor stream are cracked in the radiant section of the steam cracker to produce a cracked effluent. The second liquid stream reacted with hydrogen in the presence of a catalyst to produce a hydroprocessed product. A liquid hydroprocessed product is fed to the vaporization unit.

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21-06-2012 дата публикации

Increasing fuel smoke point

Номер: US20120152803A1
Автор: Stuart S. Shih
Принадлежит: ExxonMobil Research and Engineering Co

The present invention relates to processes for increasing smoke point of a fuel. The process can be carried out using an upgrading catalyst that contains at least one noble metal supported on an inorganic, porous crystalline phase material. The catalyst is particularly effective in increasing smoke point, while minimizing reduction in total aromatics content, particularly naphthalene content.

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21-06-2012 дата публикации

Method of making a catalyst

Номер: US20120157299A1
Принадлежит: ENERGIA TECHNOLOGIES Inc

Presented are one or more aspects and/or one or more embodiments of catalysts, methods of preparation of catalyst, methods of deoxygenation, and methods of fuel production.

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21-06-2012 дата публикации

Methods of deoxygenation and systems for fuel production

Номер: US20120157727A1
Принадлежит: ENERGIA TECHNOLOGIES Inc

Presented are one or more aspects and/or one or more embodiments of catalysts, methods of preparation of catalyst, methods of deoxygenation, and methods of fuel production.

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21-06-2012 дата публикации

Production of renewable fuels

Номер: US20120157742A1
Принадлежит: ConocoPhillips Co

The present disclosure relates to a process for the conversion of oxygen-containing hydrocarbons into long-chain hydrocarbons suitable for use as a fuel. These hydrocarbons may be derived from biomass, and may optionally be mixed with petroleum-derived hydrocarbons prior to conversion. The process utilizes a catalyst comprising Ni and Mo to convert a mixture comprising oxygenated hydrocarbons into product hydrocarbons containing from ten to thirty carbons. Hydro-conversion can be performed at a significantly lower temperature than is required for when utilizing a hydrotreating catalyst comprising Co and Mo (CoMo), while still effectively removing sulfur compounds (via hydrodesulfurization) to a level of 10 ppm (by weight) or less.

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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.

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19-07-2012 дата публикации

Method for upgrading heavy hydrocarbon oil

Номер: US20120181216A1
Принадлежит: Arisdyne Systems Inc

A process for upgrading hydrocarbon oil including mixing hydrocarbon oil with hydrogen gas and heating the hydrogen-enriched hydrocarbon oil before passing the oil through a cavitation apparatus to induce hydrotreating. Hydrotreating is achieved by hydrodynamically generating hydrogen-filled cavitation bubbles and collapsing the bubbles in the hydrocarbon oil under static pressure. The hydrotreating process can increase the API gravity of the hydrocarbon oil and reduce the viscosity of the hydrocarbon oil.

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19-07-2012 дата публикации

Process for making high viscosity index lubricating base oils

Номер: US20120184787A1
Автор: Stephen J. Miller
Принадлежит: Chevron USA Inc

A process for making a lubricating base oil having a viscosity index of at least 110, comprising the steps of: combining a waxy light neutral base oil and a wax derived from pyrolyzing a plastics feed comprising polyethylene to form a blend; hydroisomerization dewaxing the blend; and recovering the lubricating base oil from an effluent from the hydroisomerization dewaxing step.

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19-07-2012 дата публикации

Method and arrangement for feeding heat-sensitive materials to fixed-bed reactors

Номер: US20120184792A1
Принадлежит: Neste Oyj

The invention relates to an arrangement for feeding heat-sensitive feedstock to a fixed-bed reactor system comprising means for product recycle and a fixed-bed reactor system comprising a fixed-bed reactor comprising at least one reaction zone having at least one catalyst bed and said reaction zone comprising a cold feed distributor arranged on top of each catalyst bed and a conventional distributor arranged above each cold feed distributor. Also a method is provided for feeding heat-sensitive feedstock to a fixed-bed reactor system wherein said fixed-bed reactor system comprises means for product recycle and a fixed-bed reactor comprising at least one reaction zone having at least one catalyst bed and said reaction zone comprising a cold feed distributor arranged on top of each catalyst bed and a conventional distributor arranged above each cold feed distributor.

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19-07-2012 дата публикации

Process for isomerizing a feed stream including one or more c4-c6 hydrocarbons

Номер: US20120184793A1
Автор: David J. Shecterle
Принадлежит: UOP LLC

One exemplary embodiment can be a process for isomerizing a feed stream including one or more C4-C6 hydrocarbons. The process may include contacting the feed stream in an isomerization reaction zone with an isomerization catalyst at isomerization conditions to produce an isomerization zone effluent; passing at least a portion of the isomerization zone effluent to a stabilizer zone and recovering a stabilizer overhead stream, a bottom stream, and a stripper feed stream; passing the stripper feed stream to a stripping zone and separating the stripper feed stream into a stripper overhead stream and a stripper bottom stream; and recycling at least a portion of the stripper bottom stream to a deisopentanizer zone and passing a stream from the deisopentanizer zone to the isomerization reaction zone. Usually, the stabilizer overhead stream includes one or more C5 − hydrocarbons, the bottom stream includes at least about 85%, by weight, one or more C6 + hydrocarbons, and a stripper feed stream including at least about 10%, by weight, one or more C5 + hydrocarbons. Often, a stripper overhead stream includes at least about 5%, by weight, one or more C4 − hydrocarbons and a stripper bottom stream includes at least about 90%, by weight, one or more C5 + hydrocarbons.

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26-07-2012 дата публикации

Molecular Sieve Of MFS Framework Type With Controllable Average Size, Its Method of Making And Use

Номер: US20120190896A1
Принадлежит: ExxonMobil Chemical Patents Inc

A method of making a crystalline molecular sieve of MFS framework type, preferably ZSM-57, from a synthesis mixture comprising at least one source of tetravalent element (Y), at least one source of trivalent element (X), at least one source of alkali metal hydroxide (MOH), at least one structure-directing-agent (R) and water, said alkali metal (M) comprising potassium, and having the following mole composition (expressed in terms of oxide): YO 2 :( p )X 2 O 3 :( q )OH − :( r )R:( s )H 2 O, wherein (p) is in the range from 0.005 to 0.05, (q) is in the range from 0.01 to 3, (r) is in the range from 0.03 to 2 and (s) is in the range from 10 to 75 (based on total weight of said synthesis mixture); wherein the crystals of molecular sieve formed having an average diameter (D) of less than or equal to 1.5 micron and an average thickness (T) of less than or equal to 300 nanometers.

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09-08-2012 дата публикации

Systems and processes for catalytic pyrolysis of biomass and hydrocarbonaceous materials for production of aromatics with optional olefin recycle, and catalysts having selected particle size for catalytic pyrolysis

Номер: US20120203042A1

This invention relates to compositions and methods for fluid hydrocarbon product, and more specifically, to compositions and methods for fluid hydrocarbon product via catalytic pyrolysis. Some embodiments relate to methods for the production of specific aromatic products (e.g., benzene, toluene, naphthalene, xylene, etc.) via catalytic pyrolysis. Some such methods may involve the use of a composition comprising a mixture of a solid hydrocarbonaceous material and a heterogeneous pyrolytic catalyst component. In some embodiments, an olefin compound may be co-fed to the reactor and/or separated from a product stream and recycled to the reactor to improve yield and/or selectivity of certain products. The methods described herein may also involve the use of specialized catalysts. For example, in some cases, zeolite catalysts may be used. In some instances, the catalysts are characterized by particle sizes in certain identified ranges that can lead to improve yield and/or selectivity of certain products.

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16-08-2012 дата публикации

Hydroprocessing Catalyst Prepared with Waste Catalyst Fines and Its Use

Номер: US20120205290A1
Принадлежит: Shell Oil Co

A hydroprocessing catalyst composition that comprises a shaped support that is formed from a mixture of inorganic oxide powder and catalyst fines and wherein the shaped support has incorporated therein at least one metal component, a chelating agent and a polar additive. The hydroprocessing catalyst composition is prepared by incorporating into the shaped support a metal component, a chelating agent and a polar additive. The hydroprocessing catalyst composition has particular application in the catalytic hydroprocessing of petroleum derived feedstocks.

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16-08-2012 дата публикации

Selective isomerization and oligomerization of olefin feedstocks for the production of turbine and diesel fuels

Номер: US20120209046A1
Принадлежит: US Department of Navy

A process from converting alcohol feedstock to diesel/turbine fuels.

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23-08-2012 дата публикации

Process for hydrotreating naphtha fraction and process for producing hydrocarbon oil

Номер: US20120211401A1
Принадлежит: Individual

A process for hydrotreating a naphtha fraction that includes a step of estimating the difference between the naphtha fraction hydrotreating reactor outlet temperature and inlet temperature, based on the reaction temperature of the Fischer-Tropsch synthesis reaction and the ratio of the flow rate of the treated naphtha fraction returned to the naphtha fraction hydrotreating step relative to the flow rate of the treated naphtha fraction discharged from the naphtha fraction hydrotreating step, a step of measuring the difference between the naphtha fraction hydrotreating reactor outlet temperature and inlet temperature, and a step of adjusting the reaction temperature of the naphtha fraction hydrotreating step so that the measured difference between the naphtha fraction hydrotreating reactor outlet temperature and inlet temperature becomes substantially equal to the estimated difference between the naphtha fraction hydrotreating reactor outlet temperature and inlet temperature.

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30-08-2012 дата публикации

Method for producing aviation fuel oil base and aviation fuel oil composition

Номер: US20120216449A1
Принадлежит: JX Nippon Oil and Energy Corp

A method for producing an aviation fuel oil base includes obtaining a first generated oil by hydrotreating a feedstock by bringing a feedstock which includes an oxygen-containing hydrocarbon compound derived from an animal or vegetable oils and fat into contact with a first dual functional catalyst which has dehydrogenation and hydrogenation functions and which includes a metal of group 6A of the periodic table, a metal of group 8, and an amorphous solid acidic substance, in the presence of hydrogen; and obtaining a second generated oil including an aviation fuel oil base by hydroisomerizing the first generated oil by bringing the first generated oil into contact with a second dual functional catalyst which has dehydrogenation and hydrogenation functions and which includes a metal of the group 8 of the periodic table and a crystalline solid acidic substance, in the presence of hydrogen.

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06-09-2012 дата публикации

Molecular Sieve Composition (EMM-10), Its Method of Making, and Use for Hydrocarbon Conversions

Номер: US20120226084A1
Принадлежит: ExxonMobil Chemical Patents Inc

This invention relates to a process for hydrocarbon conversion comprising contacting a hydrocarbon feedstock with a crystalline molecular sieve, in its ammonium exchanged form or in its calcined form, under conversion conditions to form a conversion product, said crystalline molecular sieve comprising unit cells with MWW topology and is characterized by diffraction streaking from the unit cell arrangement in the c direction as evidenced by the arced hk0 patterns of electron diffraction pattern.

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04-10-2012 дата публикации

Fuels hydrocracking with dewaxing of fuel products

Номер: US20120248008A1
Принадлежит: ExxonMobil Research and Engineering Co

This invention relates to a process involving hydrocracking and dewaxing of a feedstream in which a converted fraction can correspond to a majority of the product from the reaction system, while an unconverted fraction can exhibit improved properties. In this hydrocracking process, it can be advantageous for the yield of unconverted fraction for gasoline fuel application to be controlled to maintain desirable cold flow properties for the unconverted fraction. Catalysts and conditions can be chosen to assist in attaining, or to optimize, desirable product yields and/or properties.

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04-10-2012 дата публикации

Apparatus for producing diesel

Номер: US20120251403A1
Принадлежит: UOP LLC

An apparatus is disclosed for hydrocracking hydrocarbon feed in a hydrocracking unit and hydrotreating a diesel product from the hydrocracking unit in a hydrotreating unit. The hydrocracking unit and the hydrotreating unit shares the same recycle gas compressor. A warm separator separates recycle gas and hydrocarbons from diesel in the hydrotreating effluent, so fraction of the diesel is relatively simple. The warm separator also keeps the diesel product separate from the more sulfurous diesel in the hydrocracking effluent, and still retains heat needed for fractionation of lighter components from the low sulfur diesel product.

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04-10-2012 дата публикации

Dispersed metal sulfide-based catalysts

Номер: US20120252660A1
Принадлежит: Intevep SA

The invention provides a catalyst composition, which includes an emulsion of an aqueous phase in an oil phase, wherein the aqueous phase comprises an aqueous solution containing a group 6 metal and a group 8, 9 or 10 metal. The metals can be provided in two separate emulsions, and these emulsions are well suited for treating hydrocarbon feedstocks.

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25-10-2012 дата публикации

In situ radio frequency catalytic upgrading

Номер: US20120267095A1
Принадлежит: ConocoPhillips Co, HARRIS CORP

The present invention relates to a method and system for enhancing in situ upgrading of hydrocarbon by implementing an array of radio frequency antennas that can uniformly heat the hydrocarbons within a producer well pipe, so that the optimal temperatures for different hydroprocessing reactions can be achieved.

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22-11-2012 дата публикации

Oil and polar additive impregnated composition useful in the catalytic hydroprocessing of hydrocarbons, a method of making such catalyst, and a process of using such catalyst

Номер: US20120295786A1
Принадлежит: Shell Oil Co

A composition that comprises a support material having incorporated therein a metal component and impregnated with both hydrocarbon oil and a polar additive. The composition that is impregnated with both hydrocarbon oil and polar additive is useful in the hydrotreating of hydrocarbon feedstocks, and it is especially useful in applications involving delayed feed introduction whereby the composition is first treated with hot hydrogen, and, optionally, with a sulfur compound, prior to contacting it with a hydrocarbon feedstock under hydrodesulfurization process conditions.

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29-11-2012 дата публикации

Regenerated hydrotreatment catalyst

Номер: US20120298557A1

The present invention relates to a regenerated hydrotreatment catalyst regenerated from a hydrotreatment catalyst for treating a petroleum fraction, the hydrotreatment catalyst being prepared by supporting molybdenum and at least one species selected from metals of Groups 8 to 10 of the Periodic Table on an inorganic carrier containing an aluminum oxide, wherein a residual carbon content is in the range of 0.15 mass % to 3.0 mass %, a peak intensity of a molybdenum composite metal oxide with respect to an intensity of a base peak is in the range of 0.60 to 1.10 in an X-Ray diffraction spectrum, and a peak intensity of a Mo—S bond derived from a residual sulfur peak with respect to an intensity of a base peak is in the range of 0.10 to 0.60 in a radial distribution curve obtained from an extended X-ray absorption fine structure spectrum of an X-ray absorption fine structure analysis.

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13-12-2012 дата публикации

Apparatus and method for hydroconversion

Номер: US20120315202A1
Принадлежит: Chevron Corp

An apparatus is disclosed for the hydroconversion of hydrocarbon feedstock with a hydrogen gas at elevated temperature and pressure with the use of a catalyst. The apparatus is a reactor vessel with a grid plate distributor for improved gas liquid distribution. The distributor comprises a grid plate and a bubble cap assembly with a plurality of tubular risers extending through the grid plate. Each tubular riser has an upper section above the grid plate and a lower section below the grid plate, the lower section terminated with an open bottom end for ingress of the hydrogen gas and hydrocarbon feedstock, the upper section having a closed top terminated with a housing cap. Each tubular riser has at least a vertical slot and a least a side hole sufficiently sized such that in operation, the liquid level in the zone below the grid plate is above the vertical slot and below the side hole opening.

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03-01-2013 дата публикации

Method for producing monocyclic aromatic hydrocarbons

Номер: US20130006027A1
Принадлежит: Individual

A method for producing monocyclic aromatic hydrocarbons of 6 to 8 carbon number from a feedstock oil having a 10 volume % distillation temperature of at least 140° C. and a 90 volume % distillation temperature of not more than 380° C., the method including: a cracking and reforming reaction step of obtaining a product containing monocyclic aromatic hydrocarbons of 6 to 8 carbon number from the feedstock oil, a refining and collection step of refining and collecting monocyclic aromatic hydrocarbons of 6 to 8 carbon number that have been separated from the product, a hydrogenation reaction step of hydrogenating a heavy fraction of 9 or more carbon number separated from the product, and a recycling step of returning the heavy fraction hydrogenation reaction product obtained in the hydrogenation reaction step to the cracking and reforming reaction step.

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07-03-2013 дата публикации

Catalytical hydrodesulfurization of kerosene in two steps on cobalt-molybdenum catalyst and intermediate stripping

Номер: US20130056391A1
Принадлежит: Indian Oil Corp Ltd

A process for selective removal of mercaptan from aviation turbine fuel feed includes mixing aviation turbine fuel feed with hydrogen, at a pressure in a range from 3 bar to 20 bar to obtain a reaction mixture. The reaction mixture is heated at a temperature range of 150° C. to 350° C. to obtain a heated mixture. The heated mixture is reacted with a hydrotreating catalyst in a rector to obtain a reactor effluent, and H 2 S gas is stripped from the reactor effluent to obtain a stripper bottom product. Moisture is removed from the stripper bottom product to obtain aviation turbine fuel product having less than 10 ppm mercaptan. The aviation fuel product has improved properties such as color and acidity. Embodiments also relate to an aviation turbine fuel product having less than 10 ppm mercaptan prepared by the described process of the present invention.

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14-03-2013 дата публикации

Hydrotreating of Aromatic-Extracted Hydrocarbon Streams

Номер: US20130062255A1
Автор: Omer Refa Koseoglu
Принадлежит: Saudi Arabian Oil Co

Deep desulfurization of hydrocarbon feeds containing undesired organosulfur compounds to produce a hydrocarbon product having low levels of sulfur, i.e., 15 ppmw or less of sulfur, is achieved by first subjecting the entire feed to an extraction zone to separate an aromatic-rich fraction containing a substantial amount of the aromatic refractory and sterically hindered sulfur-containing compounds and an aromatic-lean fraction containing a substantial amount of the labile sulfur-containing compounds. The aromatic-rich fraction is contacted with isomerization catalyst, and the isomerized aromatic-rich fraction and the aromatic-lean fraction are combined and contacted with a hydrotreating catalyst in a hydrodesulfurization reaction zone operating under mild conditions to reduce the quantity of organosulfur compounds to an ultra-low level.

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14-03-2013 дата публикации

Integrated Isomerization and Hydrotreating Process

Номер: US20130062257A1
Автор: Omer Refa Koseoglu
Принадлежит: Saudi Arabian Oil Co

Deep desulfurization of hydrocarbon feeds containing undesired organosulfur compounds to produce a hydrocarbon product having low levels of sulfur, i.e., 15 ppmw or less of sulfur, is achieved by flashing the feed at a target cut point temperature to obtain two fractions. A low boiling temperature fraction contains refractory, sterically hindered sulfur-containing compounds, which have a boiling point at or above the target cut point temperature. A high boiling temperature fraction, having a boiling point below the target cut point temperature, is substantially free of refractory sulfur-containing compounds. The high boiling temperature fraction is contacted with isomerization catalyst, and the isomerized effluent and the low boiling temperature fraction are combined and contacted with a hydrotreating catalyst in a hydrodesulfurization reaction zone operating under mild conditions to reduce the quantity of organosulfur compounds to an ultra-low level.

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21-03-2013 дата публикации

HYDROCONVERSION MULTI-METALLIC CATALYST AND METHOD FOR MAKING THEREOF

Номер: US20130068662A1
Принадлежит:

A method for hydroprocessing a hydrocarbon feedstock is provided. The method comprises contacting the feedstock with a catalyst under hydroprocessing conditions, wherein the catalyst is formed by sulfiding an unsupported catalyst precursor of the general formula A[(M)(OH)(L)](MO), wherein Mis selected from Group VIII, Group IIB, Group IIA, Group IVA and combinations thereof; L is one or more oxygen-containing ligands, and L has a neutral or negative charge n<=0, Mis at least a Group VIB metal having an oxidation state of +6; M: Mhas an atomic ratio between 100:1 and 1:100; v−2+P*z−x*z+n*y*z=0; and 0≦y≦−P/n; 0≦x≦P; 0≦v≦2; 0≦z. In one embodiment, the catalyst precursor further comprises a cellulose-containing material. In another embodiment, the catalyst precursor further comprises at least a diluent (binder). In one embodiment, the diluent is a magnesium aluminosilicate clay. 1. A process for hydroprocessing a hydrocarbon feedstock which comprises contacting the hydrocarbon feedstock with a catalyst under hydroprocessing conditions ,{'sub': v', 'x', 'y', 'Z', '4, 'sup': P', 'n', 'VIB, 'wherein the catalyst is formed by sulfiding an unsupported catalyst precursor composition having a formula A[(M) (OH)(L)](MO),'}whereinA is at least one of an alkali metal cation, an ammonium, an organic ammonium and a phosphonium cation,{'sup': P', 'P', 'P, 'Mis selected from Group VIII, Group IIB, Group IIA, Group IVA and combinations thereof, P is oxidation state with Mhaving an oxidation state of either +2 or +4 depending on the selection of M,'}L is at least one organic oxygen-containing ligand,{'sup': 'VIB', 'Mis at least a Group VIB metal, having an oxidation state of +6,'}{'sup': P', 'VIB, 'M: Mhas an atomic ratio of 100:1 to 1:100,'}v−2+P*z−x*z+n*y*z=0; and0 Подробнее

28-03-2013 дата публикации

PROCESS FOR HYDROCONVERSION OF PETROLEUM FEEDSTOCKS VIA A SLURRY TECHNOLOGY ALLOWING THE RECOVERY OF METALS FROM THE CATALYST AND FROM THE FEEDSTOCK USING A COKING STEP

Номер: US20130075303A1
Принадлежит: IFP ENERGIES NOUVELLES

A process for hydroconversion of heavy petroleum feedstocks comprising a hydroconversion step of the feedstock in at least one reactor containing a slurry catalyst and allowing the recovery of metals in the unconverted residual fraction, in particular those used as catalysts, The process comprises a hydroconversion step, a gas/liquid separation step, a coking step, a combustion step, a metals extraction step and a step of preparing catalytic solutions which are recycled to the hydroconversion step. 1. Process for hydroconversion of heavy petroleum feedstocks containing metals comprising:a) a step of hydroconversion of the feedstock in at least one reactor containing a slurry catalyst containing at least one metal, and optionally a solid additive,b) a step of separation of the hydroconversion effluent without decompression into a so-called light fraction containing the compounds boiling at a maximum temperature of 500° C. and a residual fraction,b′) optionally a fractionation step comprising a separation under vacuum of said residual fraction as obtained in step b), and a vacuum residue with a high concentration of metals is obtained,c) a step of coking of said residual fraction as obtained in step b) and/or of said vacuum residue as obtained in step b′) making it possible to obtain a solid effluent containing coke,d) a step of combustion of said solid effluent containing coke at a temperature comprised between 200 and 700° C. making it possible to obtain ashes with a high concentration of metals,e) a step of extraction of the metals from the ashes obtained in the combustion step,f) a step of preparation of metallic solution(s) containing at least the metal of the catalyst which is/are recycled(s) as catalyst in the hydroconversion step.2. Process according to in which said so-called light fraction originating from the separation step without decompression is subjected to at least one hydrotreatment and/or hydrocracking step.3. Process according to claim 1 , in which ...

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28-03-2013 дата публикации

Methods for increasing catalyst concentration in heavy oil and/or coal resid hydrocracker

Номер: US20130075304A1
Автор: Yu-Hwa Chang
Принадлежит: Individual

Methods and systems for hydrocracking a heavy oil feedstock include using a colloidal or molecular catalyst (e.g., molybdenum sulfide) and provide for concentration of the colloidal or molecular catalyst within the lower quality materials requiring additional hydrocracking in one or more downstream reactors. In addition to increased catalyst concentration, the inventive systems and methods provide increased reactor throughput, increased reaction rate, and of course higher conversion of asphaltenes and lower quality materials. Increased conversion levels of asphaltenes and lower quality materials also reduces equipment fouling, enables the reactor to process a wider range of lower quality feedstocks, and can lead to more efficient use of a supported catalyst if used in combination with the colloidal or molecular catalyst.

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04-04-2013 дата публикации

Method for the hydroconversion of oil feedstocks using slurry technology, allowing the recovery of metals from the catalyst and the feedstock, comprising an extraction step

Номер: US20130081976A1
Принадлежит: IFP Energies Nouvelles IFPEN

A process for the hydroconversion of heavy oil feedstocks comprises a step for hydroconversion of the feedstock in at least one reactor containing a catalyst in slurry mode used to recover metals from the residual unconverted fraction, especially those used as catalysts. The process comprises a hydroconversion step, a gas/liquid separation step, at least one liquid/liquid extraction step, a combustion step, a metals extraction step and a step for the preparation of catalytic solutions which are recycled to the hydroconversion step.

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04-04-2013 дата публикации

HYDROPROCESSING OF HEAVY HYDROCARBON FEEDS USING SMALL PORE CATALYSTS

Номер: US20130081977A1

Heavy oil feeds are hydroprocessed in the presence of a solvent and in the presence of a catalyst with a median pore size of about 85 Å to about 120 Å under conditions that provide a variety of benefits. The solvent can be an added solvent or a portion of the liquid effluent from hydroprocessing. The processes allow for lower pressure processing of heavy oil feeds for extended processing times or extended catalyst lifetimes be reducing or mitigating the amount of coke formation on the hydroprocessing catalyst. 1. A process for producing a hydroprocessed product , comprising:{'sup': '−1', 'exposing a combined feedstock comprising a heavy oil feed component and a solvent component to a hydroprocessing catalyst comprising a Group VIII non-noble metal and a Group VI metal and having a median pore size of about 85 Å to about 120 Å, under effective hydroprocessing conditions to form a hydroprocessed effluent, the effective hydroprocessing conditions including a total pressure of about 1500 psig (10.3 MPag) or less, a temperature of at least about 360° C., and a liquid hourly space velocity of the fraction of the combined feedstock boiling above 1050° F. (566° C.) of at least about 0.10 hr;'}separating the hydroprocessing effluent to form at least a liquid effluent; andfractionating a first portion of the liquid effluent to form at least a distillate product and a bottoms product, the bottoms product having an ASTM D86 distillation point of at least about 600° F. (316° C.)2. The process of claim 1 , wherein the hydroprocessing catalyst is a bulk catalyst claim 1 , the hydroprocessing catalyst having a median pore size of about 85 Å to about 100 Å.3. The process of claim 1 , wherein the solvent component comprises a recycle component claim 1 , the process further comprising recycling a second portion of the liquid effluent to form the recycle component.4. The process of claim 3 , wherein the ratio of the recycle component to the heavy oil feed component on a weight basis is ...

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04-04-2013 дата публикации

USE OF LOW BOILING POINT AROMATIC SOLVENT IN HYDROPROCESSING HEAVY HYDROCARBONS

Номер: US20130081978A1

This invention is directed to a process for producing a hydroprocessed product. The invention is particularly advantageous in that substantially less hydrogen is absorbed during the process relative to conventional hydroprocessing methods. This benefit is achieved by using a particular solvent as a co-feed component. In particular, the solvent component contains at least one single ring aromatic compound and has a relatively low boiling point range compared to the heavy hydrocarbon oil component used as another co-feed component. 1. A process for producing a hydroprocessed product , comprising:sending to a hydroprocessing zone a combined feed comprised of a heavy hydrocarbon oil component, wherein the heavy hydrocarbon oil component has a ASTM D86 10% distillation point of at least 650° F. (343° C.), and a solvent component containing at least one single ring aromatic compound in which the solvent has an ASTM D86 10% distillation point of at least 120° C. (248° F.) and a 90% distillation point of not greater than 300° C. (572° F.); andcontacting the combined feed with a hydroprocessing catalyst in the presence of hydrogen in the hydroprocessing zone to form a hydroprocessed product.2. The process of claim 1 , wherein the heavy hydrocarbon oil component has an initial ASTM D86 boiling point of at least 650° F. (343° C.).3. The process of claim 1 , wherein the heavy hydrocarbon oil component has an ASTM D86 10% distillation point of at least 750° F. (399° C.).4. The process of claim 1 , wherein the heavy hydrocarbon oil component contains at least 0.0001 grams of Ni/V/Fe claim 1 , on a total elemental basis of nickel claim 1 , vanadium and iron.5. The process of claim 1 , wherein the heavy hydrocarbon oil component contains at least 50 wppm elemental nitrogen claim 1 , based on total weight of the heavy hydrocarbon oil component.6. The process of claim 5 , wherein the heavy hydrocarbon oil component contains at least 500 wppm elemental sulfur claim 5 , based on total ...

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04-04-2013 дата публикации

USE OF SUPERCRITICAL FLUID IN HYDROPROCESSING HEAVY HYDROCARBONS

Номер: US20130081979A1

This invention is directed to a process for producing a hydroprocessed product. The invention is particularly advantageous in that substantially longer run length can be attained relative to conventional hydroprocessing methods. This benefit is achieved by using a particular solvent as a co-feed component. In particular, the solvent component is comprised of at least one or more supercritical solvent compounds. 1. A process for producing a hydroprocessed product , comprising:sending to a hydroprocessing zone a combined feed comprised of a heavy hydrocarbon oil component, wherein the heavy hydrocarbon oil component has a ASTM D86 10% distillation point of at least 650° F. (343° C.), and a solvent component in which a majority of the solvent is comprised of at least one supercritical hydrocarbon compound having a critical temperature and pressure; andcontacting the combined feed with a hydroprocessing catalyst in the presence of hydrogen at a temperature and pressure above the critical temperature and pressure of the at least one supercritical hydrocarbon compound to form the hydroprocessed product.2. The process of claim 1 , wherein the heavy hydrocarbon oil component has an initial ASTM D86 boiling point of 650° F. (343° C.) or greater.3. The process of claim 1 , wherein the heavy hydrocarbon oil component contains at least 0.0001 grams of Ni/V/Fe claim 1 , on a total elemental basis of nickel claim 1 , vanadium and iron.4. The process of claim 1 , wherein the combined feed is comprised of from 30 wt % to 90 wt % of the heavy hydrocarbon oil component and from 10 wt % to 70 wt % of the solvent component claim 1 , based on total weight of the combined feed.5. The process of claim 1 , wherein the contacting of the combined feed with the hydroprocessing catalyst in the presence of hydrogen is carried out at a hydrogen partial pressure from 550 psig (3792 kPa-g) to 3000 psig (20684 kPa-g).6. The process of claim 1 , wherein the solvent component is comprised of more ...

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11-04-2013 дата публикации

PROCESS FOR THE HYDROCONVERSION OF PETROLEUM FEEDSTOCKS VIA SLURRY TECHNOLOGY ALLOWING THE RECOVERY OF METALS FROM THE CATALYST AND FEEDSTOCK USING A LEACHING STEP

Номер: US20130087481A1
Принадлежит: IFP ENERGIES NOUVELLES

A process for the hydroconversion of heavy oil feedstocks comprises a step for hydroconversion of the feedstock in at least one reactor containing a catalyst in slurry mode used to recover metals from the residual unconverted fraction, especially those used as catalysts. The process comprises a hydroconversion step, a gas/liquid separation step, a liquid/liquid extraction step, a grinding step, a leaching step, a combustion step, a metals extraction step and a step for the preparation of catalytic solutions which are recycled to the hydroconversion step. 1. A process for the hydroconversion of heavy oil feedstocks containing metals , comprising:a. a step for hydroconversion of the feedstock in at least one reactor containing a catalyst in the form of a slurry containing at least one metal, and optionally a solid additive;b. a step for separation of the hydroconversion effluent without decompression into a fraction termed the light fraction containing compounds boiling at 500° C. at most and into a residual fraction;b′. an optional step for fractionation, comprising vacuum separation of said residual fraction as obtained in step b) to obtain a vacuum residue which is concentrated in metals;c. a step for liquid/liquid extraction of said residual fraction as obtained in step b) and/or said vacuum residue as obtained in step b′) using a solvent with a saturated nature in order to obtain a solid extract which is concentrated in metals and a raffinate;d. a step for grinding the solid extract which is concentrated in metals obtained from the liquid/liquid extraction step;e. a step for leaching the ground extract in the presence of water, a solvent with a saturated nature and a surfactant in order to obtain a solid extract and a leachate;f. a step for combustion of said solid extract obtained from the leaching step in the presence of oxygen in order to obtain ash which is concentrated in metals;g. a step for extraction of metals from the ash obtained in the combustion step; ...

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11-04-2013 дата публикации

Reforming process with integrated fluid catalytic cracker gasoline and hydroprocessed cycle oil

Номер: US20130087482A1
Принадлежит: UOP LLC

A reforming process includes integrating catalytic cracking product naphtha dehydrogenation and naphtha from a hydrocracking zone and feeding them to a dehydrogenation zone. The dehydrogenation zone includes a first portion of reforming catalyst from a catalyst regenerator that moves downward through the dehydrogenation zone. A product stream from the dehydrogenation zone flows to an aromatics unit and is separated into an aromatic-rich extract and a raffinate. Straight run naphtha and the raffinate are introduced to a first reforming zone that includes a second portion of reforming catalyst. The reforming catalyst moves through the first reforming zone then is removed from the bottom of each of the first reforming zone and the dehydrogenation zone and is fed to a second reforming zone. An effluent from the first reforming zone is fed to a plurality of reforming zones. The reforming catalyst moves downward through the multiple refoiniing zones then to a regenerator.

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02-05-2013 дата публикации

Diesel fuel production process employing direct and indirect coal liquefaction

Номер: US20130104611A1
Принадлежит: Accelergy Corp

A combined Direct Coal Liquefaction (DCL)/Fischer Tropsch (F-T) process and system for producing high Cetane diesel fuel by converting at least 70% of the feed coal by DCL operating at 50 to 70% conversion and gasifying the bottoms and between 0 and 30% of the feed coal to produce H2 for supply to the DCL and to upgrading and syngas for being converted to diesel by F-T. Diesel blendstocks produced by the DCL and the F-T in a ratio of 3 to 1 to 14 to 1 are blended to produce diesel fuel having a Cetane Number of at least 50.

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02-05-2013 дата публикации

Self-activating hydroprocessing catalyst and process for treating heavy hydrocarbon feedstocks

Номер: US20130105357A1
Автор: Opinder K. BHAN
Принадлежит: Shell Oil Co

A self activating catalyst for treating heavy hydrocarbon feedstocks that comprises a calcined particle comprising a co-mulled mixture made by co-mulling inorganic oxide powder, molybdenum trioxide powder, and a nickel compound and then forming the co-mulled mixture into a particle that is calcined to thereby provide the calcined particle. The self activating catalyst may be activated when it is contacted under suitable process conditions with a heavy residue feedstock having high nickel, vanadium and sulfur concentrations.

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02-05-2013 дата публикации

Nozzle Reactor Systems and Methods of Use

Номер: US20130105361A1
Принадлежит: MARATHON OIL CANADA CORPORATION

A nozzle reactor system for increasing the conversion rate of material feed injected into the nozzle reactor system. The system includes two or more nozzle reactors aligned in parallel. A main stream of material to be upgraded is divided such that one stream is produced for each nozzle reactor in the system. Each nozzle reactor includes an interior reactor chamber and an injection passage and material feed passage that are each in material injecting communication with the interior reactor chamber. Furthermore, the injection passage is aligned transversely to the injection passage. The injection passage is configured to accelerate cracking material passed therethrough to a supersonic speed. The product produced from each of the nozzle reactors is combined into one product stream. 1. A nozzle reactor system comprising:a stream dividing apparatus comprising a first output port and a second output port;a first nozzle reactor having a feed material injection port in fluid communication with the first output port of the stream dividing apparatus, and an ejection end;a second nozzle reactor having a feed material injection port in fluid communication with the second output port of the stream dividing apparatus, and an ejection end; anda mixing apparatus having a first input port in fluid communication with the ejection end of the first nozzle reactor, and a second input port in fluid communication with the ejection end of the second nozzle reactor.2. The nozzle reactor system as recited in claim 1 , wherein: a reactor body having an interior reactor chamber with an injection end and an ejection end;', 'an injection passage mounted in the nozzle reactor in material injecting communication with the interior reactor chamber, the injection passage having (a) an enlarged volume injection section, an enlarged volume ejection section, and a reduced volume mid-section intermediate the enlarged volume injection section and enlarged volume ejection section, (b) a material injection ...

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02-05-2013 дата публикации

Fuel compositions containing an isomerized component of a single carbon number and methods of preparing the fuel compositions

Номер: US20130109893A1
Принадлежит: University of Dayton

Fuel compositions containing an isomerized component of a single carbon number may contain at least 97 wt. %, based on the total weight of the fuel composition, of an isomerized component consisting of aliphatic paraffin isomers all having the formula C n H 2n+2 , where 10≦n≦22 and n has the same value for each aliphatic paraffin isomer in the isomerized component. The fuel compositions have a normal alkane content of less than 10 wt. %, based on the total weight of the fuel composition. Methods for preparing the fuel compositions include hydroisomerizing a normal alkane starting material to form an isomerized mixture and subsequently removing remnant normal alkanes from the isomerized mixture by solvent dewaxing and/or distillation. Some of the fuel compositions may have freezing points at or below −47° C., making them amenable for use a surrogate fuels in the place of JP-8.

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09-05-2013 дата публикации

Production of low cloud point distillates

Номер: US20130112594A1
Принадлежит: ExxonMobil Research and Engineering Co

Systems and methods are provided for producing at least one low sulfur distillate fuel product with improved low temperature properties. A potential distillate fuel feed is initially hydrotreated to reduce sulfur and nitrogen levels in the feed to desired amounts. The hydrotreated effluent is then fractionated to form several fractions, including a light diesel/distillate fraction and a heavy diesel fraction. The heavy diesel fraction is then dewaxed to improve the cold flow properties of the heavy diesel fraction. The dewaxed heavy diesel fraction can be combined with the light diesel fraction, or the dewaxed heavy diesel fraction can be fractionated as well. Optionally, the heavy diesel fraction is dewaxed under conditions effective for producing a dewaxed fraction with a cloud point that is less than or equal to the cloud point of the light diesel/distillate fraction.

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16-05-2013 дата публикации

Mesoporous y hydrocracking catalyst and associated hydrocracking processes

Номер: US20130118954A1
Принадлежит: ExxonMobil Research and Engineering Co

This invention relates to the composition, method of making and use of a hydrocracking catalyst that is comprised of a new Y zeolite which exhibits an exceptionally low small mesoporous peak around the 40 Å (angstrom) range as determined by nitrogen adsorption measurements. The hydrocracking catalysts of invention exhibit improved distillate yield and selectivity as well as improved conversions at lower temperatures than conventional hydrocracking catalysts containing Y zeolites. The hydrocracking catalysts herein are particularly useful in the hydrocracking processes as disclosed herein, particularly for conversion of heavy hydrocarbon feedstocks such as gas oils and vacuum tower bottoms and an associated maximization and/or improved selectivity of the distillate yield obtained from such hydrocracking processes.

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23-05-2013 дата публикации

SLURRY BED HYDROPROCESSING AND SYSTEM USING FEEDSTOCK CONTAINING DISSOLVED HYDROGEN

Номер: US20130126392A1
Автор: KOSEOGLU Omer Refa
Принадлежит: Saudi Arabian Oil Company

A system and process for conversion of heavy feedstocks in a slurry bed hydroprocessing reactor is provided in which (a) hydrogen gas is dissolved in the liquid feedstock by mixing and/or diffusion, (b) the mixture is flashed to remove and recover any light components and hydrogen, leaving a hydrogen-enriched feedstock. A homogenous and/or heterogeneous catalyst is added to the feedstock upstream of the inlet of the slurry bed hydroprocessing reactor. 1. A process for converting a liquid hydrocarbon feedstock into lower molecular weight hydrocarbon compounds in a slurry bed reactor , the process comprising:a. mixing the liquid hydrocarbon feedstock and an excess of hydrogen gas in a mixing zone under predetermined conditions of temperature and hydrogen partial pressure to dissolve a portion of the hydrogen gas in the liquid hydrocarbon feedstock to produce a mixture of hydrogen-enriched liquid hydrocarbon feedstock and undissolved hydrogen gas;b. introducing the mixture produced in step (a) into a flashing zone under predetermined conditions to separate undissolved hydrogen gas and light hydrocarbon components and recovering a hydrogen-enriched liquid hydrocarbon feedstock;c. introducing the hydrogen-enriched liquid hydrocarbon feedstock into a reaction zone containing at least one slurry bed reactor with at least one catalyst or catalyst precursor and reacting the feedstock to convert at least a portion of the feedstock into lower boiling point hydrocarbons; andd. recovering converted hydrocarbon products from the slurry bed reactor.2. The process of in which at least a portion of unconverted liquid feedstock is recovered from the slurry bed reactor and is recycled to form a portion of the liquid hydrocarbon feedstock.3. The process of in which the at least one catalyst is selected from a liquid homogeneous catalyst precursor and a small particulate heterogeneous catalyst4. The process of in which fresh catalyst is added to the unconverted feedstock upstream of one ...

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23-05-2013 дата публикации

HIGH SURFACE AREA COMPOSITION FOR USE IN THE CATALYTIC HYDROCONVERSION OF A HEAVY HYDROCARBON FEEDSTOCK, A METHOD MAKING SUCH COMPOSITION AND ITS USE

Номер: US20130126393A1
Принадлежит: SHELL OIL COMPANY

A catalyst composition that is especially useful in the hydroconversion of pitch, micro carbon residue and sulfur contents of a heavy hydrocarbon feedstock without the excessive formation of sediment. The catalyst composition is a reasonably high surface area composition containing alumina and a low molybdenum content with a high ratio of nickel-to-molybdenum. The catalyst composition further has a unique pore distribution that in combination with the special metals loading provide for good conversion of pitch and micro carbon residue without an excessive yield of sediment. 1. A catalyst composition comprising a molybdenum component in an amount of greater than or equal to 5 wt. % and less than 11 wt. % , with the wt. % being based on the total weight of said catalyst composition and assuming said molybdenum component is in the oxide form (MoO) regardless of its actual form , and a nickel component present in an amount such that said catalyst composition has a weight ratio of said nickel component-to-said molybdenum component exceeding 0.25 , with said weight ratio being computed assuming said nickel component and said molybdenum component are each in the oxide form regardless of their actual forms , and wherein said catalyst composition has a total surface area in the range of from 240 m/g to 360 m/g , a total pore volume in the range of from 0.65 cc/g to 1.1 cc/g and a pore size distribution such that from 11% to 30.5% of the total pore volume is present in macropores of diameter greater than or equal to 250 Å.2. A catalyst composition as recited in claim 1 , having a pore size distribution such that from 50% to 80% of the total pore volume of said catalyst composition is present as pores having diameters in the range of from 55 Å to 115 Å claim 1 , and from 16% to 30% of the total pore volume of said catalyst composition is present in macropores of diameter greater than 500 Å.3. A catalyst composition as recited in claim 2 , wherein more than 20% of the total ...

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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.

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06-06-2013 дата публикации

Process for producing hydrocarbon oil and system for producing hydrocarbon oil

Номер: US20130143971A1

Hydrocarbon oil obtained by Fischer-Tropsch synthesis reaction using a slurry bed reactor holding a slurry of a liquid hydrocarbon in which a catalyst is suspended; the hydrocarbon oil is fractionated into a distilled oil and a column bottom oil containing the catalyst fine powder by a rectifying column; at least part of the column bottom oil is transferred to a storage tank, and the catalyst fine powder is sedimented to the bottom of the storage tank to capture the catalyst fine powder; a residue of the column bottom oil is transferred from the rectifying column to a hydrocracker, and/or the supernatant of the column bottom oil from which the catalyst fine powder is captured by the storage tank is transferred from the storage tank to the hydrocracker; and using the hydrocracker, the residue of the column bottom oil and/or the supernatant of the column bottom oil is hydrocracked.

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06-06-2013 дата публикации

Method for producing hydrocarbon oil and system for producing hydrocarbon oil

Номер: US20130144099A1

Hydrocarbon oil obtained by Fischer-Tropsch (FT) synthesis reaction using a catalyst within a slurry bed reactor is fractionated into a distilled oil and a column bottom oil in a rectifying column, part of the column bottom oil is flowed into a first transfer line that connects a column bottom of the rectifying column to a hydrocracker, at least part of the column bottom oil is flowed into a second transfer line branched from the first transfer line and connected to the first transfer line downstream of the branching point, the amount of the catalyst fine powder to be captured is monitored while the catalyst fine powder in the column bottom oil that flows in the second transfer line are captured by a detachable filter provided in the second transfer line, and the column bottom oil is hydrocracked within the hydrocracker.

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13-06-2013 дата публикации

METHODS AND UNITS FOR MITIGATION OF CARBON OXIDES DURING HYDROTREATING

Номер: US20130149210A1
Принадлежит: BP CORPORATION NORTH AMERICA INC.

This invention relates to methods and units for mitigation of carbon oxides during hydrotreating hydrocarbons including mineral oil based streams and biological oil based streams. A hydrotreating unit includes a first hydrotreating reactor for receiving a mineral oil based hydrocarbon stream and forming a first hydrotreated product stream, and a second hydrotreating reactor for receiving a biological oil based hydrocarbon stream and forming a second hydrotreated product stream. 1. (canceled)2. (canceled)3. (canceled)4. (canceled)5. (canceled)6. (canceled)7. (canceled)8. (canceled)9. A hydrotreating unit for processing mineral oil based hydrocarbon streams , biological oil based hydrocarbon streams , and combinations thereof , the unit comprising:a first hydrotreating reactor for receiving a mineral oil based hydrocarbon stream and forming a first hydrotreated product stream; anda second hydrotreating reactor for receiving a biological oil based hydrocarbon stream and forming a second hydrotreated product stream.10. The unit of claim 9 , wherein a common hydrogen stream supplies both the first hydrotreating reactor and the second hydrotreating reactor claim 9 , and the hydrogen stream comprises make-up hydrogen and recycle hydrogen.11. The unit of claim 9 , wherein a make-up hydrogen stream connects to the second hydrotreating reactor and a recycle hydrogen stream connects to the first hydrotreating reactor.12. The unit of claim 9 , wherein a make-up hydrogen stream connects to the first hydrotreating reactor and a recycle hydrogen stream connects to the second hydrotreating reactor.13. The unit of claim 9 , wherein the first hydrotreating reactor comprises a cobalt and molybdenum catalyst claim 9 , and the second hydrotreating reactor comprises a nickel and molybdenum catalyst.14. The unit of claim 9 , further comprising a carbon dioxide removal system on a hydrogen recycle stream.15. A hydrotreating unit for processing mineral oil based hydrocarbon streams claim 9 ...

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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.

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27-06-2013 дата публикации

Uzm-39 aluminosilicate zeolite

Номер: US20130164213A1
Принадлежит: UOP LLC

A new family of coherently grown composites of TUN and IMF zeotypes have been synthesized. These zeolites are represented by the empirical formula. Na n M m k+ T t Al 1−x E x Si y O z where “n” is the mole ratio of Na to (Al+E), M represents a metal or metals from zinc, Group 1, Group 2, Group 3 and or the lanthanide series of the periodic table, “m” is the mole ratio of M to (Al+E), “k” is the average charge of the metal or metals M, T is the organic structure directing agent or agents, and E is a framework element such as gallium. These zeolites are similar to TNU-9 and IM-5 but are characterized by unique compositions and synthesis procedures and have catalytic properties for carrying out various hydrocarbon conversion processes and separation properties for carrying out various separations.

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27-06-2013 дата публикации

PROCESS FOR THE PREPARATION OF A CATALYST WHICH CAN BE USED IN HYDROTREATMENT AND HYDROCONVERSION

Номер: US20130165316A1
Принадлежит:

A process for the preparation of a catalyst from a catalytic precursor comprising a support based on alumina and/or silica-alumina and/or zeolite and comprising at least one element of group VIB and optionally at least one element of group VIII, by impregnation of said precursor with a solution of a C1-C4 dialkyl succinate. An impregnation step for impregnation of said precursor which is dried, calcined or regenerated, with at least one solution containing at least one carboxylic acid other than acetic acid, then maturing and drying at a temperature less than or equal to 200° C., optionally a heat treatment at a temperature lower than 350° C., followed by an impregnation step with a solution containing at least one C1-C4 dialkyl succinate followed by maturing and drying at a temperature less than 200° C. without subsequent calcination step. The catalyst is used in hydrotreatment and/or hydroconversion. 2. A process according to characterised in that the catalytic precursor is a catalyst which has been regenerated.3. A process according to characterised in that that the catalytic precursor contains all of the elements of groups GVIB and if they are present all of the elements of group V111.4. A process according to characterised in that the dialkyl succinate is dimethyl succinate.5. A process according to characterised in that the carboxylic acid is citric acid.6. A process according to characterised in that steps 1) and/or 2) are performed in the presence of water and/or ethanol.7. A process according to characterised in that the maturing steps are performed at a temperature between 17 and 60° C.8. A process according to characterised in that the drying operation in step 1) is performed at a temperature between 100 and 180° C.9. A process according to characterised in that the drying operation in step 2) is performed at a temperature between 50 and 160° C.10. A process according to characterised in that the solution of step 1) and/or step 2) contains at least one ...

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27-06-2013 дата публикации

Process for conversion of paraffinic feedstocks obtained from the biomass of middle distillate bases employing at least one izm-2 zeolite-based catalyst

Номер: US20130165730A1
Принадлежит: IFP Energies Nouvelles IFPEN

The invention relates to a process for conversion of a paraffinic feedstock that has a number of carbon atoms of between 9 and 25, whereby said paraffinic feedstock is produced starting from renewable resources, employing a catalyst that comprises at least one hydrogenating-dehydrogenating metal that is selected from the group that is formed by the metals of group VIB and group VIII of the periodic table, taken by themselves or in a mixture, and a substrate that comprises at least one IZM-2 zeolite and at least one binder, with said process being carried out at a temperature of between 150 and 500° C., at a pressure of between 0.1 MPa and 15 MPa, at an hourly volumetric flow rate of between 0.1 and 10 h −1 , and in the presence of a total quantity of hydrogen mixed with the feedstock such that the hydrogen/feedstock ratio is between 70 and 2,000 Nm 3 /m 3 of feedstock.

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04-07-2013 дата публикации

PROCESS FOR THE HYDRODESULPHURIZATION OF A GASOLINE CUT IN THE PRESENCE OF A SUPPORTED SULPHIDE CATALYST PREPARED USING AT LEAST ONE CYCLIC OLIGOSACCHARIDE

Номер: US20130168292A1
Принадлежит: IFP ENERGIES NOUVELLES

Hydrodesulphurization of a gasoline cut containing hydrocarbons containing at least 2 carbon atoms per molecule and having an end point of 250° C. or less, by contacting the gasoline cut with at least one catalyst having an active phase of at least one metal from group VIII and at least one metal from group VIB deposited on a support, said catalyst being prepared using a process of: 1. A process for the hydrodesulphurization of a gasoline cut containing hydrocarbons containing at least 2 carbon atoms per molecule and having an end point of 250° C. or less , said process consisting of bringing said gasoline cut into contact with at least one catalyst the active phase of which comprises at least one metal from group VIII and at least one metal from group VIB deposited on a support formed from at least one oxide , said catalyst being prepared using a process comprising at least:i) at least one step for bringing at least said support into contact with at least one solution containing at least one precursor of at least said metal from group VIII and at least one precursor of at least said metal from group VIB;ii) at least one step for bringing at least said support into contact with at least one organic compound formed from at least one cyclic oligosaccharide composed of at least 6 α-(1,4)-bonded glucopyranose subunits;iii) at least one drying step to obtain at least said metal from group VIII and at least said metal from group VIB in the oxide form; then 'the steps i) and ii) possibly being carried out separately, in any order, or simultaneously.', 'iv) at least one sulphurization step such that said active phase is in the sulphide form;'}2. A hydrodesulphurization process according to claim 1 , in which said gasoline cut originates from a fluid catalytic cracking unit.3. A hydrodesulphurization process according to claim 1 , in which said gasoline cut has a sulphur content in the range 200 to 5000 ppm by weight.4. A hydrodesulphurization process according to claim 1 , ...

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11-07-2013 дата публикации

FLAKES MANAGEMENT IN HYDROCARBON PROCESSING UNITS

Номер: US20130175157A1
Принадлежит: TOTAL RAFFINAGE MARKETING

The instant invention discloses a method for the improvement of flakes recovery from hydrocarbon processing units and in particular slurry reactors as well as slurry flakes obtained thereof. 1. A method for the separation of solids contained in a solid containing treated hydrocarbon feedstock issued from an industrial unit , wherein an ultimate reactor is fed with an ultimate catalyst , an ultimate hydrocarbon feedstock and an ultimate hydrogen containing gas , and wherein after reaction , the resulting ultimate treated hydrocarbon feedstock undergoes a liquid-solid filtration before a final fractionation is performed.2. A method according claim 1 , wherein claim 1 , before reaction and before filtration claim 1 , a penultimate hydrocarbon feedstock undergoes a penultimate treatment in a penultimate reactor fed with a penultimate catalyst and/or the ultimate catalyst claim 1 , and a penultimate hydrogen containing gas claim 1 , to obtain the ultimate hydrocarbon feedstock.3. A method according to claim 1 , wherein the final fractionation is a vacuum fractionation.4. A method according to claim 1 , wherein the final fractionation is a combination of an atmospheric fractionation followed by a vacuum fractionation.5. A method according to claim 1 , wherein the resulting ultimate treated hydrocarbon feedstock undergoes flash separation to remove gaseous species before liquid-solid filtration.6. A method according to claim 1 , wherein the industrial unit is a slurry plant.7. A method according to claim 1 , wherein filtration allows separating the catalyst from the remaining solid residues contained in the ultimate treated hydrocarbon feedstock.8. A method according to claim 7 , wherein filtration is performed with at least two filters having different porosities so as to discriminate the catalyst from the remaining solid residues.9. A method according to claim 7 , wherein the catalyst is recycled.10. A method according to claim 7 , wherein the catalyst is reused.11. A ...

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11-07-2013 дата публикации

HYDROCRACKING CATALYST FOR HYDROCARBON OIL, METHOD FOR PRODUCING HYDROCRACKING CATALYST, AND METHOD FOR HYDROCRACKING HYDROCARBON OIL WITH HYDROCRACKING CATALYST

Номер: US20130175202A1
Принадлежит:

The present invention relates to a hydrocracking catalyst for hydrocarbon oil comprising a support containing a framework-substituted zeolite-1 in which zirconium atoms and/or hafnium atoms form a part of a framework of an ultrastable y-type zeolite and a hydrogenative metal component carried thereon and a method for producing the same. The hydrocracking catalyst of the present invention makes it easy to diffuse heavy hydrocarbon oils such as VGO, DAO and the like into mesopores, is improved in a cracking activity and makes it possible to obtain a middle distillate at a high yield as compared with catalysts prepared by using zeolite comprising titanium and/or zirconium carried thereon. 1. A hydrocracking catalyst for hydrocarbon oil comprising a hydrogenative metal component carried on a support containing an ultra-stable Y-type zeolite , wherein the above ultra-stable Y-type zeolite is a framework-substituted zeolite (hereinafter referred to as a framework-substituted zeolite-1) in which a part of aluminum atoms constituting a zeolite framework thereof is substituted with zirconium atoms and/or hafnium atoms.2. A hydrocracking catalyst for hydrocarbon oil according to claim 1 , wherein said zeolite-1 contains from 0.1 to 5 mass % zirconium atoms and/or hafnium atoms as calculated as the oxide basis.3. The hydrocracking catalyst for hydrocarbon oil according to or claim 1 , wherein said zeolite-1 further contains titanium atoms.4. The hydrocracking catalyst for hydrocarbon oil according to claim 3 , wherein in the zeolite-1 claim 3 , a part of the aluminum atoms forming the zeolite framework is further substituted with titanium atoms.5. The hydrocracking catalyst for hydrocarbon oil according to or claim 3 , wherein said zeolite-1 contains from 0.1 to 5 mass % titanium atoms as calculated as the oxide basis.6. The hydrocracking catalyst for hydrocarbon oil according to any of to claim 3 , wherein the support contains the zeolite-1 and inorganic oxide excluding the ...

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18-07-2013 дата публикации

Hydrocarbon feedstock average molecular weight increase

Номер: US20130180884A1
Принадлежит: Total Raffinage Marketing SA

The invention deals with hydrocarbon feedstock molecular weight increase via olefin oligomerization and/or olefin alkylation onto aromatic rings. Addition of a purification section allows improved unit working time and lower maintenance.

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18-07-2013 дата публикации

CATALYST FOR USE IN HYDROCONVERSION, COMPRISING AT LEAST ONE ZEOLITE AND METALS FROM GROUPS VIII AND VIB, AND PREPARATION OF THE CATALYST

Номер: US20130180886A1
Принадлежит:

The invention concerns a catalyst containing a support comprising at least one binder and at least one zeolite having at least one series of channels the opening of which is defined by a ring containing 12 oxygen atoms, said catalyst comprising phosphorus, at least one C1-C4 dialkyl succinate, acetic acid and a hydrodehydrogenating function comprising at least one element from group VIB and at least one element from group VIII, the Raman spectrum of the catalyst comprising bands at 990 and/or 974 cm, characteristic of at least one Keggin heteropolyanion, the characteristic bands of said succinate and the characteristic principal band of acetic acid at 896 cm. 1. A catalyst containing a support comprising at least one binder and at least one zeolite having at least one series of channels the opening of which is defined by a ring containing 12 oxygen atoms , said catalyst comprising phosphorus , at least one C1-C4 dialkyl succinate , acetic acid and a hydrodehydrogenating function comprising at least one element from group VIB and at least one element from group VIII , the Raman spectrum of the catalyst comprising bands at 990 and/or 974 cm , characteristic of at least one Keggin heteropolyanion , the characteristic bands of said succinate and the characteristic principal band of acetic acid at 896 cm.2. A catalyst according to claim 1 , in which the dialkyl succinate is dimethyl succinate and in which the Raman spectrum of the catalyst has principal bands at 990 and/or 974 cmwhich are characteristic of Keggin heteropolyanions claim 1 , and at 853 cm claim 1 , which is characteristic of dimethyl succinate and at 896 cm claim 1 , which is characteristic of acetic acid.3. A catalyst according to claim 1 , in which the dialkyl succinate is diethyl succinate claim 1 , dibutyl succinate or diisopropyl succinate.4. A catalyst according to claim 1 , comprising a support constituted by alumina and zeolite.5. A catalyst according to claim 1 , comprising a support constituted ...

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25-07-2013 дата публикации

Process for hydrotreating a hydrocarbon cut with a boiling point of more than 250°c in the presence of a sulphide catalyst prepared using a cyclic oligosaccharide

Номер: US20130186806A1
Принадлежит: IFP Energies Nouvelles IFPEN

Preparation of a catalyst having at least one metal from group VIII, at least one metal from group VIB and at least one support; in succession: i) one of i1) contacting a pre-catalyst with metal from group VIII, metal from group VIB and support with a cyclic oligosaccharide naming at least 6 α-(1,4)-bonded glucopyranose subunits; i2) contacting support with a solution containing a precursor of metal from group VIII, a precursor of said metal from group VIB and a cyclic oligosaccharide composed of at least 6 α-(1,4)-bonded glucopyranose subunits; or i3) contacting support with a cyclic oligosaccharide composed of at least 6 α-(1,4)-bonded glucopyranose subunits followed by contacting solid derived therefrom with a precursor of metal from group VIII and a precursor of metal from group VIB.

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01-08-2013 дата публикации

Processing biomass

Номер: US20130196386A1
Автор: Marshall Medoff
Принадлежит: Xyleco Inc

Biomass (e.g., plant biomass, animal biomass, and municipal waste biomass) is processed to produce useful products, such as fuels. For example, systems are described that can use feedstock materials, such as cellulosic and/or lignocellulosic materials, to produce ethanol and/or butanol, e.g., by fermentation.

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15-08-2013 дата публикации

Using supercritical fluids to refine hydrocarbons

Номер: US20130206645A1
Автор: Stephen Lee Yarbro
Принадлежит: Stephen Lee Yarbro

A system and method for reactively refining hydrocarbons, such as heavy oils with API gravities of less than 20 degrees and bitumen-like hydrocarbons with viscosities greater than 1000 cp at standard temperature and pressure, using a selected fluid at supercritical conditions. A reaction portion of the system and method delivers lightweight, volatile hydrocarbons to an associated contacting unit which operates in mixed subcritical/supercritical or supercritical modes. Using thermal diffusion, multiphase contact, or a momentum generating pressure gradient, the contacting unit separates the reaction products into portions that are viable for use or sale without further conventional refining and hydro-processing techniques.

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29-08-2013 дата публикации

PROCESS FOR HYDROCRACKING A HYDROCARBON FEEDSTOCK

Номер: US20130220885A1
Принадлежит: Haldor Topsoe A/S

A hydrocracking process comprising the steps of: (a) combining a hydrocarbonaceous feedstock and a heavy bottom fraction recycle stream with a hydrogen-rich gas to obtain a mixture comprising hydrocarbonaceous feedstock and hydrogen; (b) catalytically hydrocracking the mixture comprising hydrocarbonaceous feedstock and hydrogen in a hydrocracking zone to obtain a hydrocracked effluent; (c) separating the hydrocracked effluent into a first vapour portion and a first liquid portion in a separation zone; (d) heating the first liquid portion to form a vapourised first liquid portion; (e) feeding the vapourised first liquid portion to a fractionation section producing individual product fractions including a heavy bottom fraction comprising unconverted oil at the bottom zone of the fractionation section; (f) withdrawing from the fractionation section the heavy bottom fraction; (g) splitting the heavy bottom fraction in a stream for stripping and a heavy bottom fraction recycle stream; (h) stripping the stream for stripping, with a stripping medium, in a counter current stripping column to form an overhead vapour and a stripped liquid; (i) feeding the overhead vapour to the fractionation section, to a recycle stream or to a position upstream the fractionation section; and (j) removing at least a part of the stripped liquid from the counter current stripping column as a net purge of unconverted oil. 1. A hydrocracking process comprising the steps of:(a) combining a hydrocarbonaceous feedstock and a heavy bottom fraction recycle stream with a hydrogen-rich gas to obtain a mixture comprising hydrocarbonaceous feedstock and hydrogen;(b) catalytically hydrocracking the mixture comprising hydrocarbonaceous feedstock and hydrogen in a hydrocracking zone to obtain a hydrocracked effluent;(c) separating the hydrocracked effluent into a first vapour portion and a first liquid portion in a separation zone;(d) heating the first liquid portion to form a vapourised first liquid portion ...

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29-08-2013 дата публикации

Low viscosity oligomer oil product, process and composition

Номер: US20130225459A1
Принадлежит: INEOS USA LLC

The present invention relates to a low viscosity lubricant process, product, and composition characterized by low Noack volatility, low pour point, useful low temperature viscometrics, and high viscosity index and more particularly concerns a PAO composition having a kinetic viscosity at 100° C. in the range of about 4 cSt.

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05-09-2013 дата публикации

Method for efficiently operating an ebbulated bed reactor and an efficient ebbulated bed reactor

Номер: US20130228494A1
Принадлежит: Headwaters Heavy Oil LLC

A hydroprocessing method and system involves introducing heavy oil and well-dispersed metal sulfide catalyst particles, or a catalyst precursor capable of forming the well-dispersed metal sulfide catalyst particles in situ within the heavy oil, into a hydroprocessing reactor. The well-dispersed or in situ metal sulfide catalyst particles are formed by 1) premixing a catalyst precursor with a hydrocarbon diluent to form a precursor mixture, 2) mixing the precursor mixture with heavy oil to form a conditioned feedstock, and 3) heating the conditioned feedstock to decompose the catalyst precursor and cause or allow metal from the precursor to react with sulfur in the heavy oil to form the well-dispersed or in situ metal sulfide catalyst particles. The well-dispersed or in situ metal sulfide catalyst particles catalyze beneficial upgrading reactions between the heavy oil and hydrogen and eliminates or reduces formation of coke precursors and sediment.

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05-09-2013 дата публикации

Integrated hydrotreating and steam pyrolysis process including hydrogen redistribution for direct processing of a crude oil

Номер: US20130228495A1
Принадлежит: Saudi Arabian Oil Co

Steam pyrolysis and hydroprocessing are integrated including hydrogen redistribution to permit direct processing of crude oil feedstocks to produce petrochemicals including olefins and aromatics. A feed is initially split into a light portion and a heavy portion, and the heavy portion is hydroprocessed. A hydroprocessed effluent is charged, along with steam, to a convection section of a steam pyrolysis zone. The mixture is heated and passed to a vapor-liquid separation section. A residual portion is removed and light components are charged to a pyrolysis section of the steam pyrolysis zone. A mixed product stream is recovered from the steam pyrolysis zone and it is separated into product including olefins and aromatics.

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12-09-2013 дата публикации

Upgrading Hydrocarbon Pyrolysis Products

Номер: US20130233764A1
Принадлежит: ExxonMobil Chemical Patents Inc

The invention relates to upgraded pyrolysis products, processes for upgrading products obtained from hydrocarbon pyrolysis, equipment useful for such processes, and the use of upgraded pyrolysis products.

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12-09-2013 дата публикации

METHOD OF PRODUCING REGENERATED HYDROTREATING CATALYST AND METHOD OF PRODUCING PETROLEUM PRODUCTS

Номер: US20130233769A1
Принадлежит: JX NIPPON OIL & ENERGY CORPORATION

A method of producing a regenerated hydrotreating catalyst, including a first step of preparing a hydrotreating catalyst that has been used for hydrotreatment of a petroleum fraction and has a metal element selected from Group 6 elements of the periodic table; a second step of performing regeneration treatment for part of the catalyst prepared in the first step, then performing X-ray absorption fine structure analysis for the catalyst after the regeneration treatment, and obtaining regeneration treatment conditions in which a ratio IS/IO of a peak intensity IS of a peak attributed to a bond between the metal element and a sulfur atom to a peak intensity IO of a peak attributed to a bond between the metal element and an oxygen atom is in the range of 0.1 to 0.3 in a radial distribution curve obtained from an extended X-ray absorption fine structure spectrum. 1. A method of producing a regenerated hydrotreating catalyst , comprising:a first step of preparing a hydrotreating catalyst that has been used for hydrotreatment of a petroleum fraction and has a metal element selected from Group 6 elements of the periodic table;{'sub': S', 'O', 'S', 'O, 'a second step of performing regeneration treatment for part of the catalyst prepared in the first step, then performing X-ray absorption fine structure analysis for the catalyst after the regeneration treatment, and obtaining regeneration treatment conditions in which a ratio I/Iof a peak intensity Iof a peak attributed to a bond between the metal element and a sulfur atom to a peak intensity Iof a peak attributed to a bond between the metal element and an oxygen atom is in the range of 0.1 to 0.3 in a radial distribution curve obtained from an extended X-ray absorption fine structure spectrum; and'}a third step of performing regeneration treatment under regeneration treatment conditions determined based on the second step, for the other part of the catalyst prepared in the first step.2. The method of producing a regenerated ...

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19-09-2013 дата публикации

Process unit for flexible production of alkylate gasoline and distillate

Номер: US20130243672A1
Принадлежит: Chevron USA Inc

A process unit, comprising: a) an alkylation reactor; and b) a control system that enables the alkylation reactor to be operated in an alkylate mode and in a distillate mode; wherein the alkylation reactor can switch back and forth from operating in the alkylate mode to the distillate mode.

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26-09-2013 дата публикации

PLATINUM-FREE MONOMETALLIC AND BIMETALLIC NANOPARTICLES AS RING-OPENING CATALYSTS

Номер: US20130248414A1
Принадлежит: GOVERNORS OF THE UNIVERSITY OF ALBERTA

Nanoparticle catalyst compositions and methods for preparation of same are described. The nanoparticle catalysts are platinum-free and are useful in effecting selective ring-opening reactions, for example in upgrading heavy oil. The catalyst may be of monometallic composition, or may comprise an alloyed or core-shell bimetallic composition. The nanoparticles are of controlled size and shape. 1. A ring-opening catalyst composition comprising: a primary non-platinum transition metal having ring-opening catalytic activity; and', 'a secondary transition metal;, 'a plurality of monodispersed nanoparticles, each of the monodispersed nanoparticles having a size between 1-5 nm in diameter, and each of the monodispersed nanoparticles comprising2. The ring-opening catalyst composition as in claim 1 , further comprising a capping agent.3. The bimetallic nanoparticle ring-opening catalyst as in claim 1 , wherein the primary transition metal has suitable activity and selectivity in catalyzing single-cleavage ring-opening reactions.4. The bimetallic nanoparticle ring-opening catalyst as in claim 1 , wherein the primary transition metal is a metal selected from the group consisting of: palladium claim 1 , ruthenium claim 1 , rhodium claim 1 , iridium claim 1 , and rhenium.5. The bimetallic nanoparticle ring-opening catalyst as in claim 1 , wherein the primary transition metal is iridium.6. The bimetallic nanoparticle ring-opening catalyst as in claim 1 , wherein the secondary transition metal is a catalytically active transition metal.7. The bimetallic nanoparticle ring-opening catalyst as in claim 6 , wherein the secondary transition metal has ring-opening catalytic activity.8. The bimetallic nanoparticle ring-opening catalyst as in claim 6 , wherein the secondary transition metal is a hydrodesulfurization catalyst.9. The bimetallic nanoparticle ring-opening catalyst as in claim 6 , wherein the secondary transition metal is a hydrogenation catalyst.10. The bimetallic nanoparticle ...

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03-10-2013 дата публикации

Hydrocarbon conversion process

Номер: US20130256190A1
Принадлежит: UOP LLC

One exemplary embodiment can be a process for hydrocarbon conversion. The process can include providing a feed to a slurry hydrocracking zone, obtaining a hydrocarbon stream including one or more C16-C45 hydrocarbons from the at least one separator, providing another feed to a hydrocracking zone, and providing hydrogen from a three-stage compressor to the slurry hydrocracking zone and the hydrocracking zone. Moreover, the slurry hydrocracking zone may include a slurry hydrocracking reactor and at least one separator.

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10-10-2013 дата публикации

SYNTHESIS OF ACIDIC SILICA TO UPGRADE HEAVY FEEDS

Номер: US20130264245A1
Принадлежит:

A method and a product made by treating a sulfur-containing hydrocarbon heavy feed, e.g., heavy crude asphaltene reduction is disclosed herein. The method comprises the steps of: mixing the sulfur-containing hydrocarbon heavy feed with a hydrogen donor solvent and an acidified silica to form a mixture and oxidizing the sulfur in the mixture at a temperature between 50° C. and 210° C., wherein the oxidation lowers the amount sulfur in the sulfur-containing hydrocarbon heavy feed by at least 90%. 1. A method of extracting sulfur from an oxidized hydrocarbon feed comprising the steps of:mixing a solution comprising a sulfur containing oxidized hydrocarbon feed, an acidified silica, a hydrogen donor solvent, any unreacted materials and reaction by-products with one or more polar organic solvents;allowing the sulfur containing oxidized hydrocarbon feed to migrate to the polar organic solvent phase; andremoving the one or more polar organic solvents by evaporation to recover the sulfur.2. The method of claim 1 , wherein the oxidized hydrocarbon feed comprises asphaltenes claim 1 , tar sands claim 1 , bitumens claim 1 , heavy petroleum or mixtures thereof.3. The method of claim 1 , wherein the hydrogen donor solvent is selected from the group consisting of hydrogen claim 1 , natural petroleum claim 1 , bases claim 1 , alcohols claim 1 , decahydronaphthalene claim 1 , and tetrahydronaphthalene.4. The method of claim 1 , wherein acidified silica has a pH range from 0 to 2.5. The method of claim 1 , wherein the acidified silica comprises an amorphous silica or a silica gel.6. The method of claim 1 , wherein the polar organic solvent is selected from the group consisting of ethanol claim 1 , methanol claim 1 , n-propanol claim 1 , isopropanol claim 1 , n-butanol claim 1 , formic acid claim 1 , acetic acid claim 1 , 1 claim 1 ,4-dioxane claim 1 , THF claim 1 , dichloromethane claim 1 , acetone claim 1 , acetonitrile claim 1 , DMF claim 1 , DMSO claim 1 , and any combinations ...

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10-10-2013 дата публикации

Catalyst for producing monocyclic aromatic hydrocarbons and production method of monocyclic aromatic hydrocarbons

Номер: US20130267749A1
Принадлежит: JX Nippon Oil and Energy Corp

The catalyst for producing monocyclic aromatic hydrocarbons is for producing monocyclic aromatic hydrocarbons having 6 to 8 carbon number from oil feedstock having a 10 volume % distillation temperature of 140° C. or higher and a 90 volume % distillation temperature of 380° C. or lower. The catalyst includes crystalline aluminosilicate, phosphorus, and a binder, and the amount of phosphorus is 0.1 to 10 mass % based on the total mass of the catalyst.

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17-10-2013 дата публикации

Processing biomass and petroleum containing materials

Номер: US20130273612A1
Автор: Marshall Medoff
Принадлежит: Xyleco Inc

Biomass (e.g., plant biomass, animal biomass, and municipal waste biomass) is processed to produce useful products, such as fuels. For example, systems can use feedstock materials, such as cellulosic and/or lignocellulosic materials and/or starchy materials, to produce ethanol and/or butanol, e.g., by fermentation.

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24-10-2013 дата публикации

Treatment process for an isomerization unit

Номер: US20130276825A1
Принадлежит: UOP LLC

One exemplary embodiment can be a process for treating an interior of equipment for an isomerization unit. Generally, the isomerization unit includes at least one of a drying zone, an isomerization reaction zone, and a stabilizer zone, for receiving a feed stream. Usually, the feed stream includes one or more C4-C8 hydrocarbons. The process can include combining an anhydrous hydrogen stream and anhydrous organic chloride stream to form a hydrogen chloride feedstock, and passing the hydrogen chloride feedstock to a reaction zone containing a catalyst including at least one of nickel, palladium, and platinum on an alumina support to form a hydrogen chloride stream, and passing the hydrogen chloride stream upstream of the isomerization reaction zone.

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24-10-2013 дата публикации

IN-SITU HYDROGENATION OF AROMATIC COMPOUNDS FOR HEAVY OIL UPGRADING

Номер: US20130277273A1
Автор: Mazyar Oleg A.
Принадлежит: BAKER HUGHES INCORPORATED

A method for upgrading a heavy oil includes: disposing a catalyst comprising rhodium and a support in a heavy oil environment, the heavy oil environment including a heavy oil comprising an aromatic compound; introducing hydrogen; and hydrogenating the aromatic compound with the catalyst and hydrogen to upgrade the heavy oil to upgraded oil. A method for converting an asphaltene includes: disposing a supported catalyst in a composition comprising an asphaltene, the supported catalyst being a low temperature catalyst; introducing hydrogen; and hydrogenating the asphaltene to convert the asphaltene into a hydrogenated asphaltene. 1. A method for upgrading a heavy oil , the method comprising:disposing a catalyst comprising rhodium and a support in a heavy oil environment, the heavy oil environment including a heavy oil comprising an aromatic compound;introducing hydrogen; andhydrogenating the aromatic compound with the catalyst and hydrogen to upgrade the heavy oil to upgraded oil.2. The method of claim 1 , wherein the rhodium comprises rhodium nanoparticles supported on the support.3. The method of claim 2 , wherein the support comprises hydroxyapatite claim 2 , fluoroapatite claim 2 , chloroapatite claim 2 , bromoapatite claim 2 , zeolite claim 2 , or a combination comprising at least one of the foregoing.4. The method of claim 3 , wherein the catalyst is rhodium nanoparticles supported on nanocrystalline hydroxyapatite.5. The method claim 1 , wherein the catalyst is dispersed in a fluid prior to disposing the catalyst in the heavy oil environment.6. The method of claim 5 , wherein the fluid comprises propane claim 5 , butane claim 5 , pentane claim 5 , dimethyl sulfoxide claim 5 , tetrahydrofuran claim 5 , o-dioxane claim 5 , m-dioxane claim 5 , p-dioxane claim 5 , dimethoxyethane claim 5 , n-methyl-pyrrolidone claim 5 , n claim 5 ,n-dimethylacetamide claim 5 , γ-butyrolactone claim 5 , 1 claim 5 ,3-dimethyl-2-imidazolidinone claim 5 , dimethylformamide claim 5 , ...

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31-10-2013 дата публикации

HYDROCRACKING PROCESS OF HEAVY HYDROCARBON DISTILLATES USING SUPERCRITICAL SOLVENT

Номер: US20130284639A1
Принадлежит:

Specific embodiments of the present invention provide a hydrocracking process for converting low value-added heavy hydrocarbon distillates into high value-added hydrocarbon distillates using a supercritical solvent as a medium. 1. A method of converting a heavy hydrocarbon distillate into a low-boiling hydrocarbon , the method comprising the step of:contacting a heavy hydrocarbon distillate with a supercritical xylene-containing solvent in the presence of a hydrogenation catalyst to hydrogenate the heavy hydrocarbon distillate for converting the heavy hydrocarbon distillate into the low-boiling hydrocarbon.2. The method of claim 1 , wherein the hydrogenation of the heavy hydrocarbon distillate is performed at a hydrogen pressure of 30 to 150 bars.3. The method of claim 1 , wherein the supercritical xylene-containing solvent is an aromatic solvent comprising at least 25 wt % of m-xylene.4. The method of claim 3 , wherein the supercritical xylene-containing solvent comprises (i) 70 to 85 wt % of xylene claim 3 , (ii) 15 to 25 wt % of ethylbenzene claim 3 , and (iii) 5 wt % of toluene or a C+ aromatic.5. The method of claim 1 , wherein the heavy hydrocarbon distillate is a vacuum residue.6. The method of claim 1 , wherein a weight ratio of the supercritical xylene-containing solvent to the heavy hydrocarbon distillate (xylene-containing solvent/heavy hydrocarbon distillate) is 3 to 10.7. The method of claim 1 , wherein the hydrogenation of the heavy hydrocarbon distillate is performed at a temperature of 350° C. to 420° C. and a hydrogen pressure of 30 to 100 bars.8. The method of claim 1 , wherein the hydrogenation catalyst comprises one of a metal-based catalyst and an active carbon catalyst.9. The method of claim 8 , wherein the metal-base catalyst comprises Mo claim 8 , W claim 8 , Co claim 8 , Ni or a combination thereof.10. The method of claim 8 , wherein the active carbon catalyst is an acid-treated active carbon catalyst.11. The method of claim 10 , wherein the ...

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31-10-2013 дата публикации

HYDROPROCESSING CATALYST AND PROCESS FOR TREATING HEAVY HYDROCARBON FEEDSTOCKS

Номер: US20130284640A1
Автор: BHAN Opinder Kishan
Принадлежит: SHELL OIL COMPANY

A catalyst for treating heavy hydrocarbon feedstocks. The catalyst comprises a calcined particle comprising a co-mulled mixture made by co-mulling inorganic oxide powder, molybdenum trioxide powder, and a nickel compound or cobalt compound, or both compounds, and then forming the co-mulled mixture into a particle that is calcined to provide the calcined particle. The calcination is conducted at a temperature such that at least 20% of the pore volume of the calcined particle is in pores of greater than 5,000 Å and less than 70% of the pore volume of the calcined particle is in the pores having a pore size in the range of from 70 to 250 Å. 1. A hydroprocessing catalyst for treating a heavy hydrocarbon feedstock , wherein said hydroprocessing catalyst comprises: a calcined particle comprising a co-mulled mixture made by co-mulling inorganic oxide powder , molybdenum trioxide powder , and Group VIII metal particles and then forming said co-mulled mixture into a particle that is calcined to thereby provide said calcined particle , wherein said calcined particle has a pore structure such that at least 20% of the total pore volume of said calcined particle is in the pores of said calcined particle having pore diameters greater than 5 ,000 Å and less than 70% of the total pore volume of said calcined particle is in the pores of said calcined particle having pore diameters in the range of from 70 Å to 250 Å , as measured by mercury penetration.2. A hydroprocessing catalyst as recited in claim 1 , wherein the calcining of said particle is conducted under a controlled temperature condition at a calcination temperature in the range of from 482° C. (900° F.) to 787.7° C. (1450° F.) for a calcination time period so as to provide said calcined particle having said pore structure.3. A hydroprocessing catalyst as recited in claim 2 , wherein said molybdenum trioxide powder of said co-mulled mixture is in a finely divided state of particulate molybdenum trioxide either as a finely ...

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31-10-2013 дата публикации

Processing Biomass Containing Materials

Номер: US20130288307A1
Автор: Marshall Medoff
Принадлежит: Xyleco Inc

Biomass (e.g., plant biomass, animal biomass, and municipal waste biomass) is processed to produce useful products, such as fuels. For example, systems can use feedstock materials, such as cellulosic and/or lignocellulosic materials and/or starchy materials, to produce ethanol and/or butanol, e.g., by fermentation.

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31-10-2013 дата публикации

Conversion of Natural Gas

Номер: US20130289144A1
Автор: Rian Steyn
Принадлежит: Asa Energy Conversions Ltd

A process and apparatus for converting a mixture of hydrogen and carbon monoxide to hydrocarbons comprising reacting the hydrogen and carbon monoxide at elevated temperature and pressure in contact with a suitable catalyst in a reactive distillation column is disclosed.

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