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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

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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Форма поиска

Поддерживает ввод нескольких поисковых фраз (по одной на строку). При поиске обеспечивает поддержку морфологии русского и английского языка
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Применить Всего найдено 18711. Отображено 100.
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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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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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

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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19-04-2012 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

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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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

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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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

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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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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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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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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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

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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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

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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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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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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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

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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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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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

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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31-10-2013 дата публикации

Method for Reducing the Amount of Organic Acids in a Hydrocarbon Oil Fraction

Номер: US20130289328A1
Принадлежит:

Provided is a method for reducing the amount of organic acids in a hydrocarbon oil fraction by hydrogenating the organic acids in the hydrocarbon oil fraction under mild conditions. Provided is a new method able to overcome the problem of organic-acid-induced corrosion during the process of distillation, by using hydrogen or a hydrogen-containing mixed gas and a hydrogenation catalyst to subject the organic acids in the hydrocarbon oil fraction to hydrogenation at an appropriate temperature and pressure, thereby converting the same to hydrocarbons and so reducing the amount of organic acids in the hydrocarbon oil fraction. 1. A method of reducing an amount of an organic acid in a hydrocarbon oil fraction , comprising the step of:{'sub': '2', 'sup': '2', 'hydrogenating the hydrocarbon oil fraction using a hydrogen gas supplied at a H/oil ratio of about 1-100 (NL/L) in the presence of a hydrogenation catalyst under conditions of a temperature of about 300-400° C. and a pressure of about 3-15 kg·f/cm.'}2. The method of claim 1 , wherein the hydrocarbon oil fraction is crude oil or biofuel.3. The method of claim 1 , wherein the hydrocarbon oil fraction is atmospheric residual oil or an upgraded oil fraction.4. The method of claim 2 , wherein the crude oil or the biofuel is desalinated claim 2 , and then hydrogenated in the presence of the hydrogenation catalyst under conditions of the temperature of about 300-400° C. and the pressure of about 3-10 kg·f/cm.5. The method of claim 3 , wherein the atmospheric residual oil or the upgraded oil fraction is hydrogenated in the presence of the hydrogenation catalyst under conditions of the temperature of about 300-400° C. and the pressure of about 10-15 kg·f/cm.6. The method of claim 1 , wherein the hydrogenation catalyst is selected from the group consisting of a gas oil hydrodesulfurization catalyst claim 1 , a heavy metal adsorption catalyst for use in desulfurization of atmospheric residual oil or vacuum residual oil claim 1 ...

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07-11-2013 дата публикации

Titania-Supported Hydrotreating Catalysts

Номер: US20130294985A1
Принадлежит: SACHTLEBEN CHEMIE GMBH

TiO-supported catalysts include at least molybdenum or tungsten as active components for hydrotreating processes, in particular for the removal of sulfur and nitrogen compounds as well as metals out of crude oil fractions and for the hydrogenation of sulfur oxides. 1. Supported catalyst composition for hydrotreating , comprising shaped titania support bodies having at least one oxide of molybdenum and/or tungsten on the surface thereof and having a surface area of at least 80 mper gram , a pore volume measured by mercury porosimetry of at least 0.25 cm/g , a side-crush strength greater than 7 N/mm , and a tapped bulk density in the range of 600-1200 kg/m.2. Catalyst composition according to claim 1 , having a titanium dioxide content of the support bodies in the range of 80 to 100 wt. % as calculated on the total weight of the supported catalyst composition.3. Catalyst composition according to claim 1 , having a content of molybdenum and/or tungsten in the range of 9.0 to 16.0 wt. % claim 1 , expressed as trioxides claim 1 , calculated on the total weight of the supported catalyst composition.4. Catalyst composition according to claim 1 , further comprising a total content of at least one of cobalt and nickel in the range of 0 to 6.5 wt. % claim 1 , expressed as CoOor NiO claim 1 , calculated on the total weight of the supported catalyst composition.5. Catalyst composition according to claim 1 , wherein at least 20 weight percent of the supported precursor particles of the catalytically active oxides being present after calcination are smaller than 50 nm.6. Catalyst composition for hydrotreating according to claim 1 , obtainable by applying an aqueous solution of at least one salt of molybdenum and/or tungsten on shaped titania support bodies followed by drying and calcining the obtained bodies.7. Process for the preparation of a catalyst composition as claimed in claim 1 , wherein a solution of at least one salt of molybdenum and/or tungsten is applied on titania ...

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07-11-2013 дата публикации

A CATALYST AND PROCESS FOR THE MANUFACTURE OF ULTRA-LOW SULFUR DISTILLATE PRODUCT

Номер: US20130296163A1
Автор: BHAN Opinder Kishan
Принадлежит:

Described is a catalyst and process useful in the hydrodesulfurization of a distillate feedstock to manufacture a low-sulfur distillate product. The catalyst comprises a calcined mixture of inorganic oxide material, a high concentration of a molybdenum component, and a high concentration of a Group VIII metal component. The mixture that is calcined to form the calcined mixture comprises molybdenum trioxide in the form of finely divided particles, a Group VIII metal compound, and an inorganic oxide material. The catalyst is made by mixing the aforementioned starting materials and forming therefrom an agglomerate that is calcined to yield the calcined mixture that may be used as the catalyst or catalyst precursor. 1. A composition for use as a distillate hydrodesulfurization catalyst in the manufacture of an ultra-low sulfur distillate product , wherein said composition comprises:a calcined mixture made by calcining a co-mulled mixture comprising an inorganic oxide material, molybdenum trioxide in the form of finely divided particles having a maximum dimension of less than 150 μm, and a Group VIII metal compound selected from the group consisting of a nickel compound, a cobalt compound and a combination thereof, wherein said calcined mixture has a molybdenum content in the range of from 10 weight percent to 22 weight percent with the weight percent being based upon the molybdenum as metal and the total weight of said calcined mixture, and a Group VIII metal content in the range of from 3 weight percent to 12 weight percent with the weight percent being based upon the Group VIII metal in its elemental form and the total weight of said calcined mixture, wherein said calcined mixture has a mean pore diameter in the range of from 50 angstroms to 100 angstroms, and wherein said calcined mixture has less than 1 percent of the total pore volume in macropores having a diameter greater than 1000 angstroms.2. A composition as recited in claim 1 , wherein said pore structure is ...

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14-11-2013 дата публикации

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

Номер: US20130303812A1
Принадлежит: Shell Oil Co

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

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21-11-2013 дата публикации

Hydrocarbon Conversion Process

Номер: US20130310601A1
Принадлежит: ExxonMobil Chemical Patents Inc

The invention relates to processes for converting hydrocarbons to phthalic acids such as terephthalic acid. The invention also relates to polymerizing phthalic acid derivatives to produce, e.g., synthetic fibers.

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21-11-2013 дата публикации

Process for separation of water from pyrolysis gasoline

Номер: US20130310616A1
Принадлежит: BASF SE

A process for separating water from pyrolysis gasoline obtained from a steam cracking step uses a coalescer for the water separation. And a device comprises a coalescer for water separation from pyrolysis gasoline.

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21-11-2013 дата публикации

Coprocessing of biofeeds with group vi metal catalysts

Номер: US20130310618A1
Принадлежит: ExxonMobil Research and Engineering Co

Feedstocks containing biocomponent materials are coprocessed with mineral feeds using a Group VI metal catalyst prior to hydrodesulfurization of the feedstocks. The Group VI metal catalyst is optionally a physically promoted Group VI metal catalyst.

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21-11-2013 дата публикации

Catalytically Active Material for the Hydrogenation Treatment of Hydrocarbons

Номер: US20130310622A1
Принадлежит: Euro Support Catalyst Group Bv

A catalytically active material having adsorption properties is used for the hydrogenation treatment of hydrocarbons severely contaminated with inorganic constituents.

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28-11-2013 дата публикации

Process for direct hydrogen injection in liquid full hydroprocessing reactors

Номер: US20130313161A1
Автор: Hasan Dindi
Принадлежит: EI Du Pont de Nemours and Co

A process of hydroprocessing a hydrocarbon in a down flow reactor comprising one or more hydroprocessing-catalyst beds. The hydrocarbon feed is mixed with hydrogen and optionally diluent to form a liquid feed mixture wherein hydrogen is dissolved in the mixture, and the liquid feed mixture is introduced into the down flow reactor under hydroprocessing conditions. The hydroprocessing-catalyst bed(s) are liquid-full and the feed reacts by contact with the catalyst. Hydrogen gas is injected into at least one of the hydroprocessing-catalyst beds such that at least part of the hydrogen consumed in that bed is replenished and the liquid-full condition is maintained. In a multi-bed reactor, hydrogen gas may be injected into more than one or all of the hydroprocessing-catalyst beds.

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28-11-2013 дата публикации

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

Номер: US20130313165A1
Принадлежит: SK Innovation Co Ltd

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

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28-11-2013 дата публикации

Distillate oil hydrogenation deacidification catalyst containing molecular sieve, preparation and use thereof

Номер: US20130316894A1
Принадлежит: Petrochina Co Ltd

Provided are a distillate oil hydrogenation deacidification catalyst containing a molecular sieve, preparation and use thereof. In this catalyst, the weight of the catalyst, on the basis of 100%, is 1-5% magnesium calculated as an oxide, 1-20% alumino-phosphate molecular sieve and/or aluminosilicate molecular sieve; 1-10% Co and/or Ni; 5-30% Mo and/or W, and the balance is aluminium oxide. The catalyst is prepared through forming, dipping and baking. The catalyst is very active in hydrogenation deacidification, and also in hydrodesulfurization and hydrodenitrogenation.

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05-12-2013 дата публикации

Hydrocarbon Conversion Process Using a High Throughpout Process for Manufacturing Molecular Sieves

Номер: US20130324760A1
Принадлежит: ExxonMobil Chemical Patents Inc

A method of crystallizing a crystalline molecular sieve having a pore size in the range of from about 2 to about 19 Å, said method comprising the steps of (a) providing a mixture comprising at least one source of ions of tetravalent element (Y), at least one hydroxide source (OH − ), and water, said mixture having a solid-content in the range of from about 15 wt. % to about 50 wt. %; and (b) treating said mixture to form the desired crystalline molecular sieve with stirring at crystallization conditions sufficient to obtain a weight hourly throughput from about 0.005 to about 1 hr −1 , wherein said crystallization conditions comprise a temperature in the range of from about 200° C. to about 500° C. and a crystallization time less than 100 hr.

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26-12-2013 дата публикации

Novel fuel compositions and methods for making same

Номер: US20130340323A1
Принадлежит: ExxonMobil Research and Engineering Co

This invention relates to low sulfur marine/bunker fuel compositions and methods of making same. Contrary to conventional marine/bunker fuel compositions/methods, the inventive lower sulfur compositions/methods focus on use of mostly uncracked components, such as (cat feed) hydrotreated gasoils, and/or can also have reduced contents of residual components.

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26-12-2013 дата публикации

MICROWAVE-PROMOTED DESULFURIZATION OF CRUDE OIL

Номер: US20130341247A1
Принадлежит: Saudi Arabian Oil Company

Heavy crude oils having high sulfur content and viscosities are upgraded by a hydrodesulfurization (HDS) process that includes microwave irradiation of a mixture of the sour heavy crude oil with at least one catalyst and optionally, one or more sensitizers, and irradiation in the presence of hydrogen. The process is also adapted to microwave treatment of hard to break emulsions, either above ground or below ground where water-in-oil emulsions are initially formed, followed by the catalytic hydrodesulfurization promoted by application of further microwave energy to the demulsified crude oil stream. 1. A process for upgrading a sulfur-containing crude oil feedstream to improve the API gravity and reduce the sulfur content , the process comprising:a. mixing the crude oil with one or more hydrotreating catalysts having a reaction surface to provide a catalyst-crude oil reaction mixture;b. irradiating the mixture of the crude oil and one or more hydrotreating catalysts with microwave energy in the presence of hydrogen at a pressure level of from one atmosphere to 400 psig to raise the temperature of the reaction mixture to a temperature in the range from 70° C. to about 400° C.;c. maintaining the temperature of the reaction mixture by varying the microwave energy, for a period of time that is sufficient to form soluble sulfur compounds and thereby reduce the sulfur content of the crude oil;d. separating the irradiated mixture into a catalyst-containing solid phase and an upgraded oil phase; ande. recovering the upgraded oil phase.2. The process of claim 1 , wherein the one or more catalysts comprise powdered iron claim 1 , palladium oxide claim 1 , calcium oxide claim 1 , an alkali metal oxide catalyst claim 1 , traditional hydrotreating catalysts claim 1 , and combinations thereof.3. The process of claim 1 , wherein the hydrotreating catalyst comprises at least one metal selected from Group VIB or VIIIB of the Periodic Table.4. The process of in which the at least one ...

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26-12-2013 дата публикации

Methods and apparatuses for deoxygenating biomass-derived pyrolysis oil

Номер: US20130345487A1
Принадлежит: UOP LLC

Embodiments of methods and apparatuses for deoxygenating a biomass-derived pyrolysis oil are provided. In one example, a method comprises the steps of separating a low-oxygen biomass-derived pyrolysis oil effluent into a low-oxygen-pyoil organic phase stream and an aqueous phase stream. Phenolic compounds are removed from the aqueous phase stream to form a phenolic-rich diluent recycle stream. A biomass-derived pyrolysis oil stream is diluted and heated with the phenolic-rich diluent recycle stream to form a heated diluted pyoil feed stream. The heated diluted pyoil feed stream is contacted with a deoxygenating catalyst in the presence of hydrogen to deoxygenate the heated diluted pyoil feed stream.

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02-01-2014 дата публикации

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

Номер: US20140005040A1

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

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02-01-2014 дата публикации

Selective Hydrogenation Catalyst and Methods of Making and Using Same

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

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

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09-01-2014 дата публикации

Method for producing monocyclic aromatic hydrocarbons

Номер: US20140012055A1
Принадлежит: JX Nippon Oil and Energy Corp

A method of producing monocyclic aromatic hydrocarbons includes bringing a light feedstock oil having a 10 vol % distillation temperature of 140° C. to 205° C. and a 90 vol % distillation temperature of 300° C. or lower, which has been prepared from a feedstock oil having a 10 vol % distillation temperature of 140° C. or higher and a 90 vol % distillation temperature of 380° C. or lower, into contact with a catalyst for monocyclic aromatic hydrocarbon production containing a crystalline aluminosilicate, in which a content ratio of monocyclic naphthenobenzenes in the light feedstock oil is adjusted by distillation of the feedstock oil such that the content ratio of monocyclic naphthenobenzenes in the light feedstock oil is higher than a content ratio of monocyclic naphthenobenzenes in the feedstock oil.

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16-01-2014 дата публикации

PROCESS FOR REDUCING ULTRA LOW SULFUR DIESEL COLOR

Номер: US20140014556A1
Автор: Fadakar Farhad
Принадлежит:

The present invention is a process for preparing ultra low sulfur diesel. The steps include reacting a feedstock of petroleum crude oil with hydrogen in the presence of a hydrodesulfurization catalyst under hydrodesulfurization conditions, fractionating the reaction products, flash distilling the bottoms fraction, condensing the volatile distillate fraction as ultra low sulfur diesel, and recycling the distillation bottoms fraction for further reacting with hydrogen. 1. A process for preparing ultra low sulfur diesel comprising the steps of:(a) reacting a feedstock of petroleum crude oil with hydrogen in the presence of a hydrodesulfurization catalyst under hydrodesulfurization conditions;(b) fractionating the reaction products into a naphtha fraction, a kerosene fraction, and a first bottoms fraction; (i) a volatile distillate fraction having an ASTM Color of less than or equal to 2.5 and a sulfur content less than 15 ppm and', '(ii) a second bottoms fraction;, '(c) flash distilling the first bottoms fraction in a distillation column having at least one stage and a total stage efficiency of less than about 99%, thereby yielding'}(d) condensing the volatile distillate fraction as ultra low sulfur diesel; and(e) recycling the second bottoms fraction into the feedstock of petroleum crude oil for further reacting of the second bottoms fraction with hydrogen in the presence of the hydrodesulfurization catalyst.2. The process of wherein the reacting step occurs in a hydrotreater.3. The process of wherein the distillation column for the flash distilling step has a stage efficiency of at least about 80%.4. The process of wherein the distillation column for the flash distilling step has a stage efficiency in the range of about 80% to about 99%.5. The process of wherein the distillation column for the flash distilling step has a stage efficiency of about 95%.6. The process of wherein the hydrodesulfurization catalyst is a zeolite catalyst.7. The process of wherein the ...

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16-01-2014 дата публикации

More energy efficient c5 hydrogenation process

Номер: US20140018584A1
Принадлежит: Lummus Technology Inc

A process for the conversion of linear pentenes to propylene is disclosed. The process may include feeding hydrogen and a C5-olefin containing stream comprising linear pentenes, dienes, acetylenes, and cyclopentene to a catalytic distillation reactor system. Concurrently in the catalytic distillation reactor system, the acetylenes and dienes may be hydrogenated and the C5-olefin containing stream may be fractionated, thereby recovering an overheads fraction comprising the linear pentenes, a side draw fraction comprising the cyclopentene, and a bottoms fraction. In some embodiments, at least a portion of the overheads fraction may then be fed to a metathesis reactor for converting the linear pentenes to propylene.

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23-01-2014 дата публикации

Method of producing monocyclic aromatic hydrocarbons

Номер: US20140024871A1
Принадлежит: JX Nippon Oil and Energy Corp

A method of producing monocyclic aromatic hydrocarbons includes bringing a feedstock oil having a 10 vol % distillation temperature of 140° C. or higher and a 90 vol % distillation temperature of 380° C. or lower, into contact with a catalyst for monocyclic aromatic hydrocarbon production containing a crystalline aluminosilicate, in which a content ratio of monocyclic naphthenobenzenes in the feedstock oil is adjusted to 10 mass % to 90 mass %, by mixing a hydrocarbon oil A having a 10 vol % distillation temperature of 140° C. or higher and a 90 vol % distillation temperature of 380° C. or lower with a hydrocarbon oil B containing more monocyclic naphthenobenzenes than the hydrocarbon oil A.

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30-01-2014 дата публикации

Dual stripper column apparatus and methods of operation

Номер: US20140027347A1
Принадлежит: UOP LLC

Dual stripper column arrangements are described in which hot flash drum liquid is sent to one column and cold flash drum liquid is sent to a second column. Methods of operating the dual stripper column apparatus are also described.

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30-01-2014 дата публикации

Hydrocarbon hydroprocessing using bulk catalyst composition

Номер: US20140027350A1
Принадлежит:

The invention relates to a method for hydroprocessing hydrocarbon feedstocks, said process comprising contacting a hydrocarbon feedstock under hydroprocessing conditions with a bulk catalyst composition comprising bulk metal particles that comprise at least one Group VIII non-noble metal, at least one Group VIB metal and nanoparticles. The bulk metal catalyst composition comprises bulk metal particles that may be prepared by a manufacturing process comprising the steps of combining in a reaction mixture (i) dispersible nanoparticles having a dimension of less than about 1 μm upon being dispersed in a liquid, (ii) at least one Group VIII non-noble metal compound, (iii) at least one Group VIB metal compound, and (iv) a protic liquid; and reacting the at least one Group VIII non-noble metal compound and the at least one Group VIB metal in the presence of the nanoparticles. 1. A method for hydroprocessing hydrocarbon feedstocks , said method comprising contacting a hydrocarbon feedstock under hydroprocessing conditions with a bulk catalyst composition comprising bulk metal particles , wherein said bulk metal particles compriseat least one Group VIII non-noble metal and at least one Group VIB metal, said metals being in the form of oxides, sulfides, or a combination of oxides and sulfides, andnanoparticles having a dimension of less than 1 μm, said nanoparticles being different in composition from said Group VIII non-noble metal and Group VIB metal oxides, sulfides, or combination of oxides and sulfides.2. The method of claim 1 , whereinthe combined weight of Group VIII non-noble metal and Group VIB metal in said bulk metal particles, calculated as weight of metal oxides relative to the total weight of bulk metal particles, represents from 50 wt. % to 99.5 wt. % of the total weight of the bulk metal particles; and,the weight of nanoparticles in said bulk metal particles represents from 0.5 wt. % to 15 wt. % relative to the total weight of the bulk metal particles.3. The ...

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30-01-2014 дата публикации

PROCESS FOR HYDROTREATING HEAVY HYDROCARBON FEEDS WITH SWITCHABLE REACTORS INCLUDING AT LEAST ONE STEP OF PROGRESSIVE SWITCHING

Номер: US20140027351A1
Принадлежит: IFP ENERGIES NOUVELLES

Process for hydrotreating a heavy hydrocarbon fraction using a system of switchable fixed bed guard zones each containing at least one catalyst bed including at least one step during which the flow of feed supplied to the first guard zone brought into contact with the feed is partly displaced to the next guard zone downstream, preferably progressively. 1. Process for hydrotreating a heavy hydrocarbon fraction containing asphaltenes , sediments , sulphur-containing , nitrogen-containing and metallic impurities , in which the feed of hydrocarbons and hydrogen is passed , under hydrotreating conditions , over a hydrotreating catalyst , in at least two fixed bed hydrotreating guard zones each containing at least one catalyst bed , the guard zones being arranged in series to be used cyclically , consisting of successive repetition of steps b) , c) and c′) defined below:a step a) during which the feed passes through all the guard zones during a fraction of the deactivation time and/or clogging time of the first guard zone brought into contact with the feed,a step a′) during which a portion of the feed continues to pass through the first guard zone brought into contact with the feed and another portion of the feed is introduced into the next guard zone downstream for a period at most equal to the deactivation time and/or clogging time of the first guard zone brought into contact with the feed,a step b) during which the deactivated and/or clogged guard zone is by-passed and the catalyst that it contains is regenerated and/or replaced with fresh catalyst and during which the other guard zone(s) are used,a step c) during which the feed passes through all the guard zones, the guard zone of which the catalyst was regenerated during the preceding step being reconnected so as to be downstream of all the other guard zones and said step being continued for a fraction of the deactivation time and/or clogging time of the first guard zone brought into contact with the feed,a step c′) ...

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06-02-2014 дата публикации

Extracted conjunct polymer naphtha

Номер: US20140039230A1
Принадлежит: Chevron USA Inc

We provide an extracted conjunct polymer naphtha ( 45 ), comprising a hydrogenated conjunct polymer naphtha, from a used ionic liquid catalyst, having a final boiling point less than 246° C. (475° F.), a Bromine Number of 5 or less, and at least 30 wt % naphthenes. We also provide a blended alkylate gasoline ( 97 ) comprising the extracted conjunct polymer naphtha ( 45 ), and integrated alkylation processes to make the extracted conjunct polymer naphtha ( 45 ) and the blended alkylate gasoline ( 97 ). We also provide a method to analyze alkylate products, by determining an amount of methylcyclohexane in the alkylate products ( 80 ).

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13-02-2014 дата публикации

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

Номер: US20140042057A1

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

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13-02-2014 дата публикации

Process for the Production of Hydrocarbons for Fuels, Solvents, and Other Hydrocarbon Products

Номер: US20140046101A1

Catalytic processes for converting carboxylic acids obtained from biomass and other natural or industrial sources into paraffinic or olefinic hydrocarbons through decarboxylation, along with products formed from such hydrocarbons, in which the carbon chain length, the ratio of carbon-14 to carbon-12, and the ratio of odd number to even number of carbons in the chain are among factors which are indicative or otherwise useful for the detection of hydrocarbons formed by undergoing the claimed processes.

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06-03-2014 дата публикации

Hydroconversion Multi-Metallic Catalyst and Method For Making Thereof

Номер: US20140066293A1
Принадлежит: Chevron USA Inc

The invention relates to a self-supported mixed metal sulfide (MMS) catalyst for hydrotreating hydrocarbon feedstock and to a method for preparing the catalyst. The self-supported MMS catalyst contains Ni:W in a mole ratio of 1:3 to 4:1, on a transition metal basis. The self supported MMS catalyst is characterized as having an HYD reaction rate constant of at least 15% higher than that of a catalyst comprising nickel sulfide alone or a catalyst comprising tungsten sulfide alone, when compared on same metal molar basis in hydrotreating of benzene as a feedstock at identical process conditions.

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20-03-2014 дата публикации

CHARACTERIZATION OF PRE-REFINED CRUDE DISTILLATE FRACTIONS

Номер: US20140076776A1

Methods are provided for qualifying jet fuel fractions that are derived at least in part from pre-refined crude oil sources. The methods allow for determination of the stability of a jet fuel product over time by using an accelerated aging test. The methods are beneficial for verifying the stability of a jet fuel fraction that includes a portion derived from a pre-refined crude oil. 1. A method for preparing a jet fuel or kerosene product , comprising:determining a breakpoint for a first sample of a distillate fraction, the distillate fraction having an initial boiling point of at least about 284° F. (140° C.) and a final boiling point of about 572° F. (300° C.) or less, at least a portion of the distillate fraction being derived from a first pre-refined crude oil;maintaining a second sample of the distillate fraction at a temperature of at least about 40° C. for an aging period;determining a breakpoint for the aged second sample of the distillate fraction, the breakpoint for the aged second sample being at least about 265° C.; andpreparing a jet fuel product comprising a kerosene portion derived from a second pre-refined crude oil, the second pre-refined crude oil being derived from the same source as the first pre-refined crude oil, a volume percentage of the kerosene portion derived from the second pre-refined crude in the jet fuel product being about 110% or less of a volume percentage corresponding to the portion of the distillate fraction derived from the first pre-refined crude oil, the initial boiling point of the jet fuel product being at least about the initial boiling point of the distillate fraction, and the final boiling point of the jet fuel product being less than or equal to the final boiling point of the distillate fraction.2. The method of claim 1 , further comprising:obtaining a portion of the distillate fraction; andsplitting the portion of the distillate fraction to form at least the first sample and the second sample.3. The method of claim 1 , ...

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20-03-2014 дата публикации

CATALYST FOR USE IN HYDROTREATMENT, COMPRISING METALS FROM GROUPS VIII AND VIB, AND PREPARATION WITH CITRIC ACID AND C1-C4 DIALKYL SUCCINATE

Номер: US20140076780A1
Принадлежит:

A catalyst which comprises an amorphous support based on alumina, a C1-C4 dialkyl succinate, citric acid and optionally acetic acid, phosphorus and a hydrodehydrogenating function comprising at least one element from group VIII and at least one element from group VIB; the most intense bands comprised in the Raman spectrum of the catalyst are characteristic of Keggin heteropolyanions (974 and/or 990 cm), C1-C4 dialkyl succinate and citric acid (in particular 785 and 956 cm). Also a process for preparing said catalyst in which a catalytic precursor in the dried, calcined or regenerated state containing the elements of the hydrodehydrogenating function, and optionally phosphorus, is impregnated with an impregnation solution comprising at least one C1-C4 dialkyl succinate, citric acid and optionally at least one compound of phosphorus and optionally acetic acid, and is then dried. Further, the use of said catalyst in any hydrotreatment process. 1. A catalyst comprising an amorphous support based on alumina , at least one C1-C4 dialkyl succinate , citric acid , phosphorus and a hydrodehydrogenating function comprising at least one element from group VIB and at least one element from group VIII , with 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 principal characteristic bands of citric acid.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 cmcharacteristic of Keggin heteropolyanions claim 1 , and at 853 cm claim 1 , characteristic of dimethyl succinate and at 785 and 956 cm claim 1 , characteristic of citric acid.3. A catalyst according to claim 1 , also comprising acetic acid the Raman spectrum of which includes a line at 896 cm claim 1 , characteristic of acetic acid.4. A catalyst according to claim 1 , in which ...

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20-03-2014 дата публикации

Regeneration or remanufacturing catalyst for hydrogenation processing heavy oil, and method for manufacturing same

Номер: US20140076781A1
Автор: Hea Kyung Park

Provided are a regenerated or remanufactured catalyst for hydrogenating heavy oil or residual oil obtained by effectively removing a sulfur component, a carbonaceous component and a vanadium component, which are present in a spent catalyst for hydrogenating the heavy oil or residual oil and thus degrade an activity thereof, a method of manufacturing the same, and a method of hydrogenating heavy oil or residual oil using the same.

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20-03-2014 дата публикации

HIGH ACTIVITY HYDRODESULFURIZATION CATALYST, A METHOD OF MAKING A HIGH ACTIVITY HYDRODESULFURIZATION CATALYST, AND A PROCESS FOR MANUFACTURING AN ULTRA-LOW SULFUR DISTILLATE PRODUCT

Номер: US20140076783A1
Автор: BHAN Opinder Kishan
Принадлежит: SHELL OIL COMPANY

A method of making a high activity catalyst composition suitable for use in the hydrodesulfurization of a middle distillate feed, such as diesel fuel, having a high concentration of sulfur, to thereby provide a low sulfur middle distillate product. The method comprises heat treating aluminum hydroxide under controlled temperature conditions thereby converting the aluminum hydroxide to gamma-alumina to give a converted aluminum hydroxide, and controlling the fraction of converted aluminum hydroxide that is gamma-alumina. A catalytic component is incorporated into the converted aluminum hydroxide to provide an intermediate, which is heat treated to provide the high activity catalyst composition. The high activity catalyst composition can suitably be used in the hydrodesulfurization of a middle distillate feed containing a high sulfur concentration. 2. A method as recited in claim 1 , wherein said calcined shaped particle has a material absence of both boehmite and a crystalline transitional phase of alumina other than gamma-alumina.3. A method as recited in claim 2 , wherein said calcined shaped particle contains less than 5 weight percent boehmite with the weight percent being based on the total weight of said calcined shaped particle.4. A method as recited in claim 3 , wherein less than 5 weight percent of said alumina of said calcined shaped particle is said transitional crystalline phase of alumina other than gamma alumina.5. A method as recited in claim 4 , wherein the median pore diameter of said calcined shaped particle is in the range of from about 80 angstroms to about 110 angstroms claim 4 , wherein the total pore volume of said calcined shaped particle is in the range of from about 0.6 cc/gram to about 1.1 cc/gram claim 4 , and wherein more than 70 percent of the total pore volume of said calcined shaped particle is contained in the pores having a pore diameter of from 80 angstroms to 350 angstroms.6. A method as recited in claim 5 , wherein said ...

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20-03-2014 дата публикации

INTERSTITIAL METAL HYDRIDE CATALYST SYSTEMS AND ASSOCIATED PROCESSES

Номер: US20140081060A1

Exemplary embodiments of the present invention relate to the processing of hydrocarbon-containing feedstreams in the presence of an interstitial metal hydride containing catalyst comprising a surface, and a Group VI/Group VIII metal sulfide coated onto the surface of the interstitial metal hydride. The catalysts and processes of the present invention can improve overall hydrogenation, product conversion, as well as sulfur reduction in hydrocarbon feedstreams. 1. A process for upgrading a hydrocarbon feedstream , comprising contacting a hydrocarbon feedstream with a catalyst comprising an interstitial metal hydride having a surface and a Group VI/Group VIII metal sulfide coated on the surface of the interstitial metal hydride , in the presence of hydrogen to yield an upgraded hydrocarbon product stream.2. The process of claim 1 , wherein process is performed in the presence of a hydrogen-rich gas containing at least 50 mol % hydrogen.3. The process of claim 1 , wherein the hydrocarbon feedstream is a heavy hydrocarbon feedstream with an API gravity of less than 20 and a sulfur content of at least 1 wt % sulfur.4. The process of claim 1 , wherein the hydrocarbon feedstream comprises a biofuel.5. The process of claim 1 , wherein the process is a hydroprocessing process selected from hydrogenation claim 1 , hydrocracking claim 1 , hydrodesulfurization claim 1 , hydrodenitrogenation claim 1 , hydrodemetalization claim 1 , and catalytic hydrodewaxing processes.6. The process of claim 1 , wherein the Group VI metal is selected from Mo and W; the Group VIII metal is selected from Fe claim 1 , Co claim 1 , Ni claim 1 , Pd claim 1 , and Pt; and wherein the interstitial metal hydride and the Group VI/Group VIII metal sulfide are present in a ratio of about 20:80 by weight to about 80:20 by weight. This application is a divisional application of U.S. patent application Ser. No. 12/942,271, filed on Nov. 9, 2010.The present invention relates to catalysts for the processing of ...

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03-04-2014 дата публикации

Transition-metal free reductive cleavage of aromatic c-o, c-n, and c-s bonds by activated silanes

Номер: US20140091256A1

The present invention describes chemical systems and methods for reducing C—O, C—N, and C—S bonds, said system comprising a mixture of (a) at least one organosilane and (b) at least one strong base, said system being substantially free of a transition-metal compound, and said system optionally comprising at least one molecular hydrogen donor compound, molecular hydrogen, or both.

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01-01-2015 дата публикации

Generating cellulosic-renewable identification numbers in a refinery

Номер: US20150000186A1
Принадлежит: Ensyn Renewables Inc

The present application generally relates to methods of generating cellulosic-renewable identification numbers by thermally processing a cellulosic biomass to form a renewable fuel oil, and then co-processing the renewable fuel oil with a petroleum fraction in a refinery to form a cellulosic-renewable identification number-compliant fuel.

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07-01-2016 дата публикации

HYDROTREATMENT CATALYST WITH A HIGH DENSITY OF MOLYBDENUM, AND PROCESS FOR ITS PREPARATION

Номер: US20160001272A1
Автор: Daudin Antoine
Принадлежит: IFP ENERGIES NOUVELLES

The present invention concerns a hydrotreatment catalyst comprising an alumina-based support, at least one metal from group VIB, at least one metal from group VIII and phosphorus, in which: 2. The catalyst according to claim 1 , in which:the content of the metal from group VIB is in the range 3% to 35% by weight of oxide of said metal from group VIB with respect to the total catalyst weight;the content of the metal from group VIII is in the range 0.1% to 10% by weight of oxide of said metal from group VIII with respect to the total catalyst weight;{'sub': 2', '5, 'the phosphorus content is in the range 0.3% to 10% by weight of POwith respect to the total catalyst weight.'}3. The catalyst according to claim 1 , in which the (metal from group VIII)/(metal from group VIB) molar ratio is in the range 0.1 to 0.8 and the phosphorus/(metal from group VIB) molar ratio is in the range 0.1 to 0.7.4. The catalyst according to claim 1 , in which the specific surface area of the catalyst is in the range 30 to 150 m/g claim 1 , preferably in the range 40 to 95 m/g and highly preferably in the range 50 to 90 m/g.5. The catalyst according to claim 1 , in which the density of the metal from group VIB is in the range 7 to 25 atoms of metal from group VIB per nmof catalyst claim 1 , preferably in the range 7 to 20 atoms of metal from group VIB per nmof catalyst claim 1 , more preferably in the range 7 to 15 atoms of metal from group VIB per nmof catalyst.6. The catalyst according to claim 1 , in which the metal from group VIB is selected from tungsten and molybdenum and the metal from group VIII is selected from nickel and cobalt.7. The catalyst according to claim 6 , in which the metal from group VIB is molybdenum and the metal from group VIII is cobalt.8. The catalyst according to claim 1 , in which the alumina-based support is obtained from an alumina gel which has been kneaded claim 1 , shaped and calcined.9. The catalyst according to claim 1 , further comprising at least one ...

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04-01-2018 дата публикации

STABLE FACILITATED TRANSPORT MEMBRANES FOR OLEFIN/PARAFFIN SEPARATIONS

Номер: US20180001268A1
Принадлежит:

A stable high performance facilitated transport membrane comprising an asymmetric integrally-skinned polymeric membrane wherein the pores on the relatively porous, thin, dense skin layer of the membrane comprises a hydrophilic polymer such as chitosan or sodium alginate, a metal salt such as silver nitrate, or a mixture of a metal salt such as silver nitrate and hydrogen peroxide and the asymmetric integrally-skinned polymeric membrane comprises a relatively porous, thin, dense skin layer as characterized by a COpermeance of at least 200 GPU and a COover CHselectivity between 1.1 and 10 at 50° C. under 50-1000 psig, 10% CO/90% CHmixed gas feed pressure. The present invention further includes a method of making these membranes and their use for olefin/paraffin separations, particularly for propylene/propane and ethylene/ethane separations. 1. A stable high performance facilitated transport membrane comprising an asymmetric integrally-skinned polymeric membrane wherein the pores on a relatively porous , thin , dense skin layer of the membrane comprises a hydrophilic polymer , a metal salt or a mixture of a metal salt and hydrogen peroxide , wherein said asymmetric integrally-skinned polymeric membrane comprises a relatively porous , thin , dense skin layer as characterized by a COpermeance of at least 200 GPU and a COover CHselectivity between 1.1 and 10 at 50° C. under 50-1000 psig , 10% CO/90% CHmixed gas feed pressure.2. The stable high performance facilitated transport membrane of wherein said metal salt comprises silver nitrate.3. The stable high performance facilitated transport membrane of comprising a polymer selected from a group consisting of a polyimide claim 1 , a blend of two or more different polyimides claim 1 , and a blend of a polyimide and a polyethersulfone.4. The stable high performance facilitated transport membrane of wherein the polyimide is selected from the group consisting of poly(2 claim 3 ,2′-bis-(3 claim 3 ,4-dicarboxyphenyl) ...

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02-01-2020 дата публикации

POORLY CRYSTALLINE TRANSITION METAL TUNGSTATE

Номер: US20200001281A1
Принадлежит:

A hydroprocessing catalyst has been developed. The catalyst is a poorly crystalline transition metal tungstate material or a metal sulfide decomposition product thereof. The hydroprocessing using the crystalline ammonia transition metal tungstate material may include hydrodenitrification, hydrodesulfurization, hydrodemetallation, hydrodesilication, hydrodearomatization, hydroisomerization, hydrotreating, hydrofining, and hydrocracking. 2. The poorly crystalline transition metal tungstate material of wherein the poorly crystalline transition metal tungstate material is present in a mixture with at least one binder and wherein the mixture comprises up to 25 wt-% binder.3. The poorly crystalline transition metal tungstate material of wherein the binder is selected from the group consisting of silicas claim 2 , aluminas claim 2 , and silica-aluminas.4. The poorly crystalline transition metal tungstate material of wherein M is nickel or zinc.5. The poorly crystalline transition metal tungstate material of wherein M is nickel.7. The method of further comprising removing at least some of the NH claim 6 , HO or combination thereof to form an intermediate before reacting the mixture at a temperature from about 90° C. to about 350° C. in an autogenous environment.8. The method of wherein the reacting is conducted from about 30 minutes to 14 days.9. The method of wherein the recovering is by filtration or centrifugation.10. The method of further comprising adding a binder to the poorly crystalline transition metal tungstate material.11. The method of wherein the binder is selected from the group consisting of aluminas claim 10 , silicas claim 10 , and alumina-silicas.12. The method of further comprising decomposing the poorly crystalline transition metal tungstate material by sulfidation to form metal sulfides.14. The process of wherein the conversion process is hydroprocessing.15. The process of wherein the conversion process is selected from the group consisting of ...

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02-01-2020 дата публикации

POORLY CRYSTALLINE TRANSITION METAL MOLYBDOTUNGSTATE

Номер: US20200001282A1
Принадлежит:

A hydroprocessing catalyst or catalyst precursor has been developed. The catalyst is a poorly crystalline transition metal molybdotungstate material or a metal sulfide decomposition product thereof. The hydroprocessing using the crystalline ammonia transition metal molybdotungstate material may include hydrodenitrification, hydrodesulfurization, hydrodemetallation, hydrodesilication, hydrodearomatization, hydroisomerization, hydrotreating, hydrofining, and hydrocracking. 2. The poorly crystalline transition metal molybdotungstate material of wherein the poorly crystalline transition metal molybdotungstate material is present in a mixture with at least one binder and wherein the mixture comprises up to 25 wt-% binder.3. The poorly crystalline transition metal molybdotungstate material of wherein the binder is selected from the group consisting of silicas claim 2 , aluminas claim 2 , and silica-aluminas.4. The poorly crystalline transition metal molybdotungstate material of wherein M is nickel or zinc.5. The poorly crystalline transition metal molybdotungstate material of wherein M is nickel.7. The method of further comprising removing at least some of the NH claim 6 , HO claim 6 , or a combination thereof to form an intermediate before reacting the mixture at a temperature from about 90° C. to about 350° C. in an autogenous environment8. The method of wherein the reacting is conducted for a period from about 30 minutes to 14 days.9. The method of wherein the recovering is by filtration or centrifugation.10. The method of further comprising adding a binder to the poorly crystalline transition metal molybdotungstate material.11. The method of wherein the binder is selected from the group consisting of aluminas claim 10 , silicas claim 10 , and alumina-silicas.12. The method of further comprising decomposing the transition metal molybdotungstate material by sulfidation to form metal sulfides.14. The process of wherein the conversion process is hydroprocessing.15. The ...

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02-01-2020 дата публикации

ACCELERATED METHOD FOR PREPARING HYDROCARBON-SOLUBLE MOLYBDENUM CATALYST PRECURSORS UNDER PRESSURE

Номер: US20200001284A1
Автор: Jinhai Xie
Принадлежит:

This present invention relates to the preparation of hydrocarbon-soluble molybdenum catalyst precursors by reacting molybdenum compounds with carboxylic acids. During the reaction, vacuum was applied to accelerate removal of the water produced and to improve the conversion of reactants when reaction was carried out at low temperatures, in the range of 100-200° C. A high controlled heating temperature was employed to increase the conversion of the reactants. Vacuum was also used after the reaction process to accelerate the removal of non-reacted carboxylic acid so as to increase the concentration of produced catalyst precursors. The catalyst precursors can generate, in situ, a hydroprocessing molybdenum sulphide catalyst during heavy oil or residue upgrading. 1. A method of making a molybdenum catalyst precursor for the hydroprocessing of heavy oil/residue , comprising:Providing a molybdenum sources;Providing carboxylic acids having at least one carboxylic group that is reactive with molybdenum atoms; and the molar ratio of molybdenum atoms to carboxylic acid molecules in the range of 1:4 to 1:10;2. A method as in claim 1 , wherein a vacuum is employed to help remove water generated during the synthesis of catalyst precursors.3. A method as in claim 2 , wherein a low vacuum in the range of −4 mmHg˜−8 mmHg is employed.4. A method as in claim 3 , wherein a low vacuum is employed when controlled heating temperature is below 200° C.5. A method as in claim 3 , wherein the vacuum is employed intermittently or continuously.6. A method as in claim 3 , wherein a low vacuum is not necessary to be employed when the synthesis temperature is higher than 200° C.7. A method as in claim 1 , wherein the carboxylic acid has a range of 7 and 18 carbon atoms.8. A method as in claim 1 , wherein the heating element claim 1 , such as a furnace claim 1 , a heating mantle or a sand bath claim 1 , is claim 1 , at least claim 1 , regulated to the temperature at which the mixture temperature in ...

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