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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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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 533. Отображено 188.
10-06-2010 дата публикации

РЕАКТОР С ПСЕВДООЖИЖЕННЫМ СЛОЕМ, ТРЕХФАЗНЫЙ ШЛАМОВЫЙ РЕАКТОР И СПОСОБЫ ОБЕСПЕЧЕНИЯ ИХ ФУНКЦИОНИРОВАНИЯ (ВАРИАНТЫ)

Номер: RU2391132C2

FIELD: power industry. ^ SUBSTANCE: invention refers to reactors with air-fluidised bed. One of the versions discloses the procedure facilitating operation of a two-phase reactor with fluidised bed, which consists in low-level supply of at least one gaseous reagent into vertical directed air-fluidised mass of solid particles. Also air-fluidised mass is present in at least two vertically arranged neighbour columns located inside a common shell of the reactor. Each column is divided into a multitude of vertically running channels. At least part of the channels is inter-communicated with flow of air-fluidised mass. Notably, air fluidised mass is present in at least some of the channels. At least some of the columns and/or channels are limited with surfaces of heat exchange. Further, the procedure consists in creating conditions for reaction of the gaseous reagent, when it rises through air-fluidised mass present in at least some of the channels of the columns. Thus, there is produced a gaseous product. Successively, the procedure consists in creating conditions for extracting the gaseous product and/or not-reacted gaseous reagent from air-fluidised mass in head free space above air-fluidised mass, and in removing the gaseous product and not-reacted gaseous reagent, if present, from head free space. The disclosed designs of the reactors have large areas of heat transfer surfaces and limit degree of undesirable reverse mixing, owing to which there is potentially possible to obtain optimal combination of desired characteristics of plug flow (facilitating high efficiency and good selectivity) and characteristics of good mixing (required for wanted distribution of solid particles and for uniform temperature profiles). ^ EFFECT: invention essentially reduces risk of zooming at conversion of prototype to industrial installation. ^ 25 cl, 4 dwg РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) 2 391 132 (13) C2 (51) МПК B01J 8/22 (2006.01) B01J 19/24 (2006.01) C10G 2/00 (2006.01) ФЕДЕРАЛЬНАЯ ...

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31-10-2013 дата публикации

Method for estimating content of fine particles inslurry and process for producing hydrocarbon oil

Номер: AP0201307201D0
Автор: HAYASAKA KAZUAKI
Принадлежит:

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31-05-2015 дата публикации

Start-up method for hydrocarbon synthesis reactionapparatus

Номер: AP0201508412D0
Принадлежит:

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30-06-2016 дата публикации

A METHOD OF SHUTTING DOWN AN OPERATING THREE-PHASE SLURRY BUBBLE COLUMN REACTOR

Номер: AP2016009249A0
Принадлежит:

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31-07-2015 дата публикации

Hydrocarbon synthesis reaction apparatus

Номер: AP2015008610A0
Принадлежит:

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29-02-2016 дата публикации

REACTOR FOR HYDROCARBON SYNTHESIS

Номер: AP2016009024A0
Принадлежит:

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31-10-2016 дата публикации

The operation of processes which employ a catalystthat deactivates over time

Номер: AP0000003869A
Автор: NEL HERMAN GERHARDUS
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31-07-2016 дата публикации

Method of producing hydrocarbons

Номер: AP0000003748A
Автор: SHINGU MASAKI
Принадлежит:

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23-12-2016 дата публикации

Slurry phase apparatus

Номер: AP0000003958A
Принадлежит:

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31-05-2015 дата публикации

Start-up method for hydrocarbon synthesis reactionapparatus

Номер: AP2015008412A0
Принадлежит:

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30-09-2016 дата публикации

CATALYST

Номер: AP2016009428A0
Принадлежит: Shell Int Research

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30-11-2013 дата публикации

Process for producing at least one product from atleast one gaseous reactant in a slurry bed

Номер: AP2013007262A0
Принадлежит:

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30-04-2013 дата публикации

The operation of processes which employ a catalystthat deactivates over time

Номер: AP2013006789A0
Автор: NEL HERMAN GERHARDUS
Принадлежит:

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31-07-2013 дата публикации

Slurry phase apparatus

Номер: AP2013006960A0
Принадлежит:

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31-10-2013 дата публикации

Method of producing hydrocarbons

Номер: AP2013007187A0
Автор: SHINGU MASAKI
Принадлежит:

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31-07-2013 дата публикации

Slurry phase apparatus

Номер: AP0201306960A0
Принадлежит:

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31-10-2013 дата публикации

Method for estimating content of fine particles inslurry and process for producing hydrocarbon oil

Номер: AP2013007201A0
Автор: HAYASAKA KAZUAKI
Принадлежит:

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31-10-2013 дата публикации

Method of producing hydrocarbons

Номер: AP0201307187A0
Автор: SHINGU MASAKI
Принадлежит:

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31-07-2013 дата публикации

Slurry phase apparatus

Номер: AP0201306960D0
Принадлежит:

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30-09-2016 дата публикации

CATALYST

Номер: AP0201609428A0
Принадлежит:

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30-04-2013 дата публикации

The operation of processes which employ a catalystthat deactivates over time

Номер: AP0201306789A0
Автор: NEL HERMAN GERHARDUS
Принадлежит:

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30-06-2016 дата публикации

A METHOD OF SHUTTING DOWN AN OPERATING THREE-PHASE SLURRY BUBBLE COLUMN REACTOR

Номер: AP0201609249D0
Принадлежит:

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31-07-2015 дата публикации

Hydrocarbon synthesis reaction apparatus

Номер: AP0201508610D0
Принадлежит:

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30-04-2013 дата публикации

The operation of processes which employ a catalystthat deactivates over time

Номер: AP0201306789D0
Автор: NEL HERMAN GERHARDUS
Принадлежит:

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31-10-2013 дата публикации

Method of producing hydrocarbons

Номер: AP0201307187D0
Автор: SHINGU MASAKI
Принадлежит:

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29-02-2016 дата публикации

REACTOR FOR HYDROCARBON SYNTHESIS

Номер: AP0201609024D0
Принадлежит:

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30-11-2013 дата публикации

Process for producing at least one product from atleast one gaseous reactant in a slurry bed

Номер: AP0201307262A0
Принадлежит:

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31-05-2015 дата публикации

Start-up method for hydrocarbon synthesis reactionapparatus

Номер: AP0201508412A0
Принадлежит:

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29-02-2016 дата публикации

REACTOR FOR HYDROCARBON SYNTHESIS

Номер: AP0201609024A0
Принадлежит:

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31-10-2013 дата публикации

Method for estimating content of fine particles inslurry and process for producing hydrocarbon oil

Номер: AP0201307201A0
Автор: HAYASAKA KAZUAKI
Принадлежит:

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30-11-2013 дата публикации

Process for producing at least one product from atleast one gaseous reactant in a slurry bed

Номер: AP0201307262D0
Принадлежит:

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31-07-2015 дата публикации

Hydrocarbon synthesis reaction apparatus

Номер: AP0201508610A0
Принадлежит:

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30-06-2016 дата публикации

A METHOD OF SHUTTING DOWN AN OPERATING THREE-PHASE SLURRY BUBBLE COLUMN REACTOR

Номер: AP0201609249A0
Принадлежит:

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27-10-1986 дата публикации

PROCEDURE FOR THE PRODUCTION OF HYDROCARBONS

Номер: AT0000381488B
Автор:
Принадлежит:

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07-07-2016 дата публикации

A method of shutting down an operating three-phase slurry bubble column reactor

Номер: AU2014363104A1
Принадлежит:

A method is provided of shutting down an operating three-phase slurry bubble column reactor (10) having downwardly directed gas distribution nozzles (30) submerged in a slurry body (19) of solid particulate material suspended in a suspension liquid contained inside a reactor vessel (12), with the gas distribution nozzles (30) being in flow communication with a gas feed line (26) through which gas is being fed to the gas distribution nozzles (30) by means of which the gas is injected downwardly into the slurry body (19). The method includes abruptly stopping flow of gas from the gas feed line (26) to the gas distribution nozzles (30) to trap gas in the gas distribution nozzles (30) thereby to inhibit slurry ingress upwardly into the gas distribution nozzles (30).

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18-11-2014 дата публикации

HYDROCARBON SYNTHESIS REACTION APPARATUS, HYDROCARBON SYNTHESIS REACTION SYSTEM, AND LIQUID HYDROCARBON RECOVERY METHOD

Номер: CA0002772031C

A hydrocarbon synthesis reaction apparatus synthesizes hydrocarbons by a Fischer-Tropsch synthesis reaction. The apparatus includes a reactor; a flowing line; a first cooling unit; a second cooling unit; a first separating unit which separates the liquid hydrocarbons condensed by the first cooling unit from the gaseous hydrocarbons; and a second separating unit which separates the liquid hydrocarbons condensed by the second cooling unit from the gaseous hydrocarbons. The first cooling unit cools the hydrocarbons which flow through the flowing line to a temperature range equal to or lower than a condensing point at which a wax fraction condenses, and higher than a freezing point at which the wax fraction solidifies. The second cooling unit cools the hydrocarbons which flow through the flowing line to a temperature range lower than the temperature to which the gaseous hydrocarbons are cooled by the first cooling unit, and higher than a freezing point at which a middle distillate solidifies ...

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17-07-2018 дата публикации

REACTOR FOR HYDROCARBON SYNTHESIS

Номер: CA0002918676C

The present invention includes a reactor main body (4) that is formed into a tubular shape having an axis (O) as the center and accumulates a slurry (S); a gas supply line (10) for incorporating a synthesis gas (G) into the reactor main body (4), and a sparger part (5) that is disposed in a lower portion within the reactor main body (4), communicates with the gas supply line (10), and sprays the synthesis gas (G). The sparger part (5) includes a header tube (15) in which a plurality of openings are formed so as to be separated from each other in a first direction and which sprays the synthesis gas (G) from the openings, and a pair of wall surface parts that protrude from the header tube (15), on opposing sides of the plurality of openings and in a direction orthogonal to the first direction.

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31-07-2018 дата публикации

METHOD OF OPERATION SUSPENSION BUBBLING COLUMN REACTOR

Номер: EA0201890496A1
Автор:
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10-10-2016 дата публикации

Номер: UA0000112649C2
Автор:
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29-03-2013 дата публикации

РЕАКТОР СИНТЕЗА УГЛЕВОДОРОДОВ ТИПА БАРБОТАЖНОЙ КОЛОННЫ И СОДЕРЖАЩАЯ ЕГО РЕАКЦИОННАЯ СИСТЕМА СИНТЕЗА УГЛЕВОДОРОДОВ

Номер: EA0000017888B1

Предлагается реактор синтеза углеводородов типа барботажной колонны, который синтезирует углеводородное соединение путем химической реакции синтез-газа, содержащего водород и моноксид углерода в качестве основных компонентов, и суспензии, содержащей суспензированные в ней частицы твердого катализатора. Реактор синтеза углеводородов включает в себя основное тело реактора, которое вмещает суспензию, секцию подачи синтез-газа, которая подает синтез-газ в суспензию, и вводную часть, которая вводит охлаждающую текучую среду, имеющую более низкую температуру, чем температура суспензии, в основное тело реактора.

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30-06-2016 дата публикации

REACTOR FOR SYNTHESIS OF HYDROCARBONS

Номер: EA0201690266A1
Автор:
Принадлежит:

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29-06-2007 дата публикации

РЕАКТОР С НЕСКОЛЬКИМИ ВЕРТИКАЛЬНЫМИ ТРУБАМИ И ОБЪЕДИНЕННОЙ ТРАНСПОРТИРОВКОЙ

Номер: EA0000008696B1

В изобретении описан аппарат для превращения углеводородов. Этот аппарат включает следующее: несколько вертикальных трубных реакторов, причем у каждого из вертикальных трубных реакторов имеются первый конец, в который можно направлять катализатор, и второй конец, через который из вертикального трубного реактора может выходить катализатор; разделительную зону, обеспечивающую отделение катализатора от продуктов реакции, проводимой в аппарате для превращения углеводородов; по меньшей мере один транспортировочный патрубок, у которого имеются первый конец, сообщающийся с возможностью перетекания текучей среды по меньшей мере с двумя вторыми концами вертикальных трубных реакторов, и второй конец, проходящий в разделительную зону; и по меньшей мере одно средство возврата катализатора, сообщающееся с возможностью перетекания текучей среды с разделительной зоной и первыми концами вертикальных трубных реакторов, причем это средство возврата катализатора предусмотрено для переноса катализатора из ...

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31-05-2016 дата публикации

DEVICE FOR REACTION OF SYNTHESIS OF HYDROCARBONS

Номер: EA0201591248A1
Автор:
Принадлежит:

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30-04-2014 дата публикации

СПОСОБ И СИСТЕМА ДЛЯ СИНТЕЗА ЖИДКИХ УГЛЕВОДОРОДНЫХ СОЕДИНЕНИЙ

Номер: EA0000019593B1

Обеспечен способ для синтеза жидких углеводородных соединений, в котором синтез жидких углеводородных соединений из синтез-газа осуществляется путем реакции синтеза Фишера-Тропша. Способ включает в себя первую стадию абсорбции, состоящую из абсорбции газообразного диоксида углерода, который содержится в газообразных побочных продуктах, генерированных в ходе реакции синтеза Фишера-Тропша, с помощью абсорбента, и вторую стадию абсорбции, состоящую из абсорбции газообразного диоксида углерода, который содержится в синтез-газе, с помощью абсорбента, который прошел через первую стадию абсорбции.

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28-02-2014 дата публикации

METHOD FOR ESTIMATION OF CONTENT OF FINELY DISPERSED PARTICLES IN SUSPENSION AND METHOD OF PRODUCING HYDROCARBON OIL

Номер: EA0201391433A1
Автор:
Принадлежит:

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31-08-2015 дата публикации

METHOD OF STARTING REACTOR PLANT SYNTHESIS OF HYDROCARBONS

Номер: EA0201590702A1
Автор:
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09-04-2012 дата публикации

COMPLEX REACTABLE FISCHER-TROPSCH BUBBLE COLUMN REACTOR CAPABLE OF FORMING TWO COMPLEX REACTION REGIONS BY APPLYING DIFFERENT REACTION CONDITIONS TO A SINGLE BUBBLE COLUMN REACTOR

Номер: KR1020120033623A
Принадлежит:

PURPOSE: A complex reactable Fischer-Tropsch(F-T) bubble column reactor is provided to simplify manufacturing facilities and to improve the yield of synthetic fuel by improving energy efficiency of the reactor. CONSTITUTION: A complex reactable F-T bubble column reactor includes a first dispersing unit(20a) and a second dispersing unit(20b). The first dispersing unit and the second dispersing unit define the inside of a bubble column reactor main body(10) such that two complex reaction regions are formed in the main body. A first reaction region(20a-1) is formed at the upper side of the first dispersing unit and implements a F-T reaction with Fe-catalyst. A second reaction region(20b-1) is formed at the upper side of the second dispersing unit and implements a F-T reaction with Fe/Co catalyst or Co catalyst. The F-T bubble column reactor reacts coal synthetic gas with catalyst contained in slurry to generate synthetic fuel. COPYRIGHT KIPO 2012 ...

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02-04-2009 дата публикации

BUBBLE-COLUMN-TYPE HYDROCARBON SYNTHESIS REACTOR, AND HYDROCARBON SYNTHESIS REACTION SYSTEM HAVING THE REACTOR

Номер: WO000002009041604A1
Принадлежит:

Disclosed is a bubble-column-type hydrocarbon synthesis reactor for synthesizing a hydrocarbon compound through the chemical reaction between a synthetic gas mainly composed of hydrogen and carbon monoxide with a slurry comprising a solid catalyst particle suspended in a liquid. The bubble-column-type hydrocarbon synthesis reactor comprises: a reactor main body for containing the slurry therein; a synthetic gas supply unit for supplying the synthetic gas to the slurry; and an introduction unit for introducing a cooling fluid having a temperature lower than that of the slurry into the interior of the reactor main body.

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13-10-2005 дата публикации

PREVENTION OF AND RECOVERING FROM A CATALYST BED SLUMPING IN A GAS-AGITATED MULTIPHASE REACTOR

Номер: WO2005095312A1
Принадлежит: ConocoPhillips Company

Methods are disclosed for prevention of and recovery from a catalyst bed slumping in a gas-agitated multiphase hydrocarbon synthesis reactor, while the reactor is either under non-reactive conditions or under reaction promoting conditions when syngas is converted to products. The reactor contains a catalyst bed comprising catalyst particles and a gas injection zone suitable for injecting a reactor gas feed. A method for preventing bed slumping comprises supplying supplemental gas to the gas-agitated multiphase reactor to prevent the catalyst bed from slumping due to insufficient reactor gas feed flow. The method may include recycling some or all of the supplemental gas to the reactor. The method may further comprise separating the gas injection zone from the catalyst bed with a porous plate so as to prevent migration of catalyst particles into the gas injection zone and to minimize plugging of gas distributor(s) present in said zone.

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11-06-2014 дата публикации

Additive injection into a hydrocarbon synthesis unit from synthesis gas for monitoring and maintaining a homogenous concentration of catalyst

Номер: EP2740530A1
Принадлежит:

La présente invention a pour objet un procédé de synthèse d'hydrocarbures à partir d'une charge comprenant du gaz de synthèse, dans lequel on met en oeuvre un catalyseur Fischer-Tropsch solide dans une section réactionnelle tri-phasique opérée telle que ledit catalyseur est maintenu en suspension dans une phase liquide par la circulation d'une phase gaz du bas vers le haut de ladite section réactionnelle, caractérisé en ce que l'on effectue les étapes suivantes de manière à contrôler et de maintenir l'homogénéité de la concentration en particules de catalyseur dans la section réactionnelle : (a) pour tout i compris entre 1 et n-1, n représentant le nombre de points de mesure de pression disposés le long de l'axe longitudinal du réacteur et étant au moins égal à 3, on mesure les pressions différentielles ΔPi entre deux points de mesure consécutifs de pression distants de Δhi et on calcule les pertes de charge au mètre ΔGi =ΔPi/Δhi, (b) pour chaque perte de charge au mètre dans ladite suspension ...

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27-09-2011 дата публикации

СИСТЕМА СИНТЕЗА ЖИДКОГО ТОПЛИВА

Номер: RU2430141C2

FIELD: chemistry. ^ SUBSTANCE: invention relates to versions of a liquid fuel synthesis system comprising: reformer for reforming a hydrocarbon raw material to produce a synthetic gas containing carbon monoxide gas and hydrogen gas as main components; apparatus for recycling waste heat from the synthetic gas coming from the reformer; a reactor for synthesising liquid hydrocarbons from the carbon monoxide gas and hydrogen gas contained in the synthetic gas; apparatus for removing CO2, having an absorption column which separates carbon dioxide gas from the synthetic gas from the apparatus for recycling waste heat using an absorbent, and a regenerating column which heats the absorbent, which contains carbon dioxide gas separated in the absorption column in order to separate carbon dioxide gas, and a fractionation column which heats liquid hydrocarbons synthesised in the reactor for fractional distillation of liquid hydrocarbons into two or more types of liquid fuel, the boiling points of which differ from each other, in which the regenerating column heats the absorbent using medium-pressure vapour at pressure ranging from 1.2 to 2.5 MPa (excess), obtained by lowering pressure of the high-pressure vapour having pressure ranging from 3.4 to 10 MPa (excess), regenerated in the apparatus for recycling waste heat. ^ EFFECT: use of the present invention enables to efficiently recycle reaction heat from a reformer or reactor. ^ 6 cl, 2 dwg РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) 2 430 141 (13) C2 (51) МПК C10G 2/00 (2006.01) C10L 1/00 (2006.01) C01B 3/38 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ, ПАТЕНТАМ И ТОВАРНЫМ ЗНАКАМ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ Приоритет(ы): (30) Конвенционный приоритет: 30.03.2006 JP 2006-095534 (73) Патентообладатель(и): НИППОН СТИЛ ИНДЖИНИРИНГ КО., ЛТД. (JP) R U (24) Дата начала отсчета срока действия патента: 29.03.2007 (72) Автор(ы): ОНИСИ Ясухиро (JP), ВАКАМУРА Осаму (JP), ФУДЗИМОТО Кенитиро (JP) (21)(22) Заявка: 2008141152/ ...

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20-06-2009 дата публикации

СПОСОБ ПОЛУЧЕНИЯ ЖИДКИХ И ГАЗООБРАЗНЫХ ПРОДУКТОВ ИЗ ГАЗООБРАЗНЫХ РЕАГЕНТОВ

Номер: RU2358798C2

FIELD: chemistry. SUBSTANCE: gaseous reagents 18 are input to the pulp layer 14 consisting of the firm catalyst particles suspended in the air. Reagents react during passing up the layer form the liquid and gaseous products. On the first stage of filtration 30 the liquid product passes through filtration media having the weep holes with control size x micron (for removal of big particles - x micron). The primary effluent containing the particles close to this size and the small catalyst particles undergo the secondary filtration 64. The precipitate of the catalyst particles is formed on the filtration media and primary effluent elements are back-flushed with secondary filtrate. EFFECT: exclusion of the irreversible primary filter blinding during the filter back-flushing. 26 cl, 4 dwg РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) 2 358 798 (13) C2 (51) МПК B01J 8/22 (2006.01) C07C 1/04 (2006.01) C10G 2/00 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ, ПАТЕНТАМ И ТОВАРНЫМ ЗНАКАМ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ (21), (22) Заявка: 2006104329/15, 09.07.2004 (24) Дата начала отсчета срока действия патента: 09.07.2004 (73) Патентообладатель(и): СЭСОЛ ТЕКНОЛОДЖИ (ПРОПРИЕТЕРИ) ЛИМИТЕД (ZA) (43) Дата публикации заявки: 10.06.2006 2 3 5 8 7 9 8 (45) Опубликовано: 20.06.2009 Бюл. № 17 (56) Список документов, цитированных в отчете о поиске: US 5527473 А, 18.06.1996. RU 2201800 С2, 10.04.2003. RU 2108146 C1, 10.04.1998. SU 969290 A, 30.10.1982. SU 1463331 A1, 07.03.1989. ЖУЖИКОВ В.А. Фильтрование. М.: Химия, 1971, с.279-289. 2 3 5 8 7 9 8 R U (86) Заявка PCT: IB 2004/002243 (09.07.2004) C 2 C 2 (85) Дата перевода заявки PCT на национальную фазу: 15.02.2006 (87) Публикация PCT: WO 2005/005038 (20.01.2005) Адрес для переписки: 119034, Москва, Пречистенский пер., 14, стр. 1, 4-й этаж, Гоулингз Интернэшнл Инк., Ю.В.Дементьевой (54) СПОСОБ ПОЛУЧЕНИЯ ЖИДКИХ И ГАЗООБРАЗНЫХ ПРОДУКТОВ ИЗ ГАЗООБРАЗНЫХ РЕАГЕНТОВ (57) Реферат: Изобретение может быть использовано в химической ...

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27-04-2010 дата публикации

СИСТЕМА СИНТЕЗА ЖИДКОГО ТОПЛИВА

Номер: RU2008141152A
Принадлежит:

... 1. Система синтеза жидкого топлива, содержащая: ! реформинг-установку, в которой производится преобразование углеводородного сырья для получения синтез-газа, включающего газообразный монооксид углерода и газообразный водород в качестве основных компонентов; ! установку для утилизации отходящего тепла, которая утилизирует отходящее тепло из синтез-газа, выводимого из реформинг-установки; ! реактор, в котором синтезируются жидкие углеводороды из газообразного монооксида углерода и газообразного водорода, содержащихся в синтез-газе; и ! установку для тепловой обработки, которая выполняет заданную тепловую обработку с использованием пара, генерированного в установке для утилизации отходящего тепла. ! 2. Система синтеза жидкого топлива по п.1, дополнительно содержащая установку для удаления СО2, имеющую поглотительную колонну, которая отделяет газообразный диоксид углерода от синтез-газа, подаваемого из установки для утилизации отходящего тепла, с использованием поглотителя, и регенерационную ...

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20-07-2015 дата публикации

СПОСОБ ПОЛУЧЕНИЯ ПО МЕНЬШЕЙ МЕРЕ ОДНОГО ПРОДУКТА ИЗ ПО МЕНЬШЕЙ МЕРЕ ОДНОГО ГАЗООБРАЗНОГО РЕАГЕНТА В СУСПЕНЗИОННОМ СЛОЕ

Номер: RU2013154045A

1. Способ получения по меньшей мере одного продукта из по меньшей мере одного газообразного реагента, включающийподачу указанного по меньшей мере одного газообразного реагента в качестве газообразного сырья или части газообразного сырья при приведенной скорости газа на входе по меньшей мере 0.5 м/с в сосуд, содержащий расширенный суспензионный слой твердых частиц катализатора, суспендированных в суспензионной жидкости, так что газообразный реагент может барботировать наверх через суспензионный слой, причем суспензионный слой содержит загрузку катализатора, составляющую менее 14 об.% от дегазированной суспензии;проведение каталитической реакции по меньшей мере одного указанного газообразного реагента при давлении выше атмосферного по мере того, как пузырьки газообразного реагента барботируют наверх через суспензионный слой с образованием по меньшей мере одного продукта; иотвод из сосуда по меньшей мере одного указанного продукта и любого непрореагировавшего газообразного реагента.2. Способ по п. 1, в котором газообразное сырье включает по меньшей мере СО и Нв качестве газообразных реагентов и в котором газообразное сырье подают в суспензионный слой с получением жидких и газообразных углеводородов, причем катализатор является катализатором синтеза углеводородов.3. Способ по п. 1, в котором приведенная скорость газа на входе составляет по меньшей мере 0.6 м/с.4. Способ по п. 3, в котором приведенная скорость газа на входе составляет по меньшей мере 0.7 м/с.5. Способ по п. 1, в котором приведенная скорость газа на входе составляет по меньшей мере 0.85 м/с.6. Способ по п. 1, в котором конверсия сингаза за один проход сост РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (51) МПК B01J 8/22 (11) (13) 2013 154 045 A (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ЗАЯВКА НА ИЗОБРЕТЕНИЕ (21)(22) Заявка: 2013154045/05, 30.05.2012 (71) Заявитель(и): СЭСОЛ ТЕКНОЛОДЖИ (ПРОПРИЕТЕРИ) ЛИМИТЕД (ZA) Приоритет(ы): (30) Конвенционный приоритет: 07.06.2011 ZA 2011/04229; 07.06.2011 US 61 ...

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07-01-2009 дата публикации

Production of liquid and, optionally gaseous products form gaseous reactants

Номер: GB0002438814B
Принадлежит: SASOL TECHNOLOGY

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05-12-2007 дата публикации

Plate-type fluid bed reactor

Номер: GB0002438815A
Принадлежит:

A method of operating a three-phase slurry reactor includes feeding at a low level at least one gaseous reactant into a vertically extending slurry body of solid particles suspended in a suspension liquid, the slurry body being contained in at least two vertically extending shafts housed within a common reactor shell, each shaft being divided into a plurality of vertically extending channels at least some of which are in slurry flow communication and the slurry body being present in at least some of the channels. The gaseous reactant is allowed to react as it passes upwardly through the slurry body present in at least some of the channels of the shafts, thereby to form a non-gaseous and/or a gaseous product. Gaseous product, if present, and/or unreacted gaseous reactant is allowed to disengage from the slurry body in a head space above the slurry body.

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15-05-2008 дата публикации

REACTOR WITH SEVERAL TUBING AND WITH CONSOLIDATED TRANSPORT

Номер: AT0000395395T
Принадлежит:

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15-03-1986 дата публикации

VERFAHREN ZUR HERSTELLUNG VON KOHLENWASSERSTOFFEN

Номер: ATA275682A
Автор:
Принадлежит:

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27-06-2013 дата публикации

Slurry phase apparatus

Номер: AU2011342806A1
Принадлежит:

A method of operating a slurry phase apparatus (10) includes feeding one or more gaseous reactants into a slurry body (37) of solid particulate material suspended in a suspension liquid contained inside a vessel (12). The one or more gaseous reactants are fed into the slurry body (37) through a gas distributor (14) having downward facing gas outlets (32) and are fed towards a fluid impermeable partition (18) spanning across the vessel (12) below the gas distributor (14). The partition (18) divides the vessel (12) into a slurry volume (19) above the partition (18) and a bottom volume (36) below the partition (18). A differential pressure is maintained over the partition (18) between predefined limits by manipulating or allowing changes in the pressure in the bottom volume (36) by employing a pressure transfer passage (34) establishing flow or pressure communication between the bottom volume (36) and a head space (40) above the slurry body (37).

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26-05-2016 дата публикации

Slurry phase apparatus

Номер: AU2011342806B2
Принадлежит:

A method of operating a slurry phase apparatus (10) includes feeding one or more gaseous reactants into a slurry body (37) of solid particulate material suspended in a suspension liquid contained inside a vessel (12). The one or more gaseous reactants are fed into the slurry body (37) through a gas distributor (14) having downward facing gas outlets (32) and are fed towards a fluid impermeable partition (18) spanning across the vessel (12) below the gas distributor (14). The partition (18) divides the vessel (12) into a slurry volume (19) above the partition (18) and a bottom volume (36) below the partition (18). A differential pressure is maintained over the partition (18) between predefined limits by manipulating or allowing changes in the pressure in the bottom volume (36) by employing a pressure transfer passage (34) establishing flow or pressure communication between the bottom volume (36) and a head space (40) above the slurry body (37).

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12-07-2018 дата публикации

Loading a catalyst into a bubble column for Fischer-Tropsch synthesis

Номер: AU2016368402A1
Принадлежит: Griffith Hack

Process for loading a catalyst into a reactor (40) comprising a separation loop (21) comprising the following steps: a) filling the reactor (40) with a solvent S1; b) filling the separation loop (21) with said solvent S1; c) circulating said solvent S1 in the synthesis reactor (40) and the separation loop (21); d) heating the reactor (40) at a temperature less than or equal to 100°C; e) injecting an inert gas at the bottom of the reactor (40); f) mixing said catalyst with a solvent S2 in a tank (30) in order to obtain a liquid/solid mixture; g) increasing the pressure in the tank (30) then sending the liquid/solid mixture to the reactor (40); h) drawing off said solvent S1 and/or S2.

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10-10-2013 дата публикации

Method for producing hydrocarbon

Номер: AU2012234832A1
Принадлежит:

This method for producing hydrocarbon comprises: a synthesis step for using a bubble column-type slurry bed reactor to synthesize hydrocarbon by a Fischer-Tropsch synthesis reaction, the reactor having a gas phase part at the top and holding a slurry including catalyst particles and liquid hydrocarbon; an extraction step for causing the slurry to flow through a filter disposed on the interior and/or exterior of the reactor to separate out the heavy liquid hydrocarbon, and extracting the heavy liquid hydrocarbon; a backwashing step for causing the liquid hydrocarbon to flow through the filter in a direction inverse to the direction of flow of the slurry and returning the catalyst particles to the reactor; and a cooling and gas-liquid separation step for cooling the hydrocarbon expelled from the gas phase part and separating out and collecting the condensed light liquid hydrocarbon. The liquid hydrocarbon made to flow in the backwashing step includes the light liquid hydrocarbon obtained ...

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30-07-2015 дата публикации

Hydrocarbon synthesis reaction apparatus

Номер: AU2014206260A1
Принадлежит:

A hydrocarbon synthesis reaction apparatus according to the present invention is provided with: a reactor for bringing a synthetic gas into contact with a slurry that is produced by suspending a solid catalyst in a liquid hydrocarbon, thereby synthesizing a hydrocarbon through a Fischer-Tropsch synthesis reaction; a cylindrical inner tube which is arranged in the reactor in such a manner that there is a space between the lower end of the inner tube and the bottom of the reactor; and a sparger which is arranged on the inner lower side of the inner tube and can blow the synthetic gas into the inside of the inner tube. When the slurry is introduced into the reactor until the position of the upper end of the inner tube becomes lower than the liquid level of the slurry, a Fischer-Tropsch synthesis reaction zone is formed in a space between an extended part from the upper end of the inner tube and the inner surface of the reactor, wherein the slurry containing bubbles flows into the Fischer-Tropsch ...

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15-06-2006 дата публикации

METHOD FOR TEMPORARILY INTERRUPTING A FISCHER-TROPSCH REACTION IN A THREE-PHASE BED REACTOR

Номер: CA0002587197A1
Принадлежит:

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30-09-2019 дата публикации

METHOD OF PRODUCING HYDROCARBONS

Номер: EA0201991052A1
Автор:
Принадлежит:

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30-04-2012 дата публикации

СПОСОБ И СИСТЕМА ДЛЯ СИНТЕЗА ЖИДКИХ УГЛЕВОДОРОДНЫХ СОЕДИНЕНИЙ

Номер: EA0201171146A1
Принадлежит:

Обеспечен способ для синтеза жидких углеводородных соединений, в котором синтез жидких углеводородных соединений из синтез-газа осуществляется путем реакции синтеза Фишера-Тропша. Способ включает в себя первую стадию абсорбции, состоящую из абсорбции газообразного диоксида углерода, который содержится в газообразных побочных продуктах, генерированных в ходе реакции синтеза Фишера-Тропша, с помощью абсорбента, и вторую стадию абсорбции, состоящую из абсорбции газообразного диоксида углерода, который содержится в синтез-газе, с помощью абсорбента, который прошел через первую стадию абсорбции.

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26-11-2007 дата публикации

ПРОЦЕС СИНТЕЗУ ВУГЛЕВОДНІВ

Номер: UA0000081065C2

Процес синтезу вуглеводнів включає подавання газоподібного матеріалу, який містить водень і монооксид вуглецю, в першу стадію реакції Фішера-Тропша, яка є трифазною низькотемпературною стадією каталітичної реакції Фішера-Тропша, причому надають можливість водню і монооксиду вуглецю частково каталітично реагувати на першій стадії реакції для утворення вуглеводнів. Щонайменше частину хвостового газу, яка включає водень і монооксид вуглецю, які не прореагували та які надходять з першої стадії реакції, подають в другу стадію реакції Фішера-Тропша, яка є двофазною високотемпературною стадією каталітичної реакції Фішера-Тропша. Надають можливість водню і монооксиду вуглецю щонайменше частково каталітично реагувати в другій стадії реакції для формування газоподібних вуглеводнів.

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28-02-2014 дата публикации

METHOD OF PRODUCING HYDROCARBONS

Номер: EA0201391219A1
Автор:
Принадлежит:

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02-05-2013 дата публикации

APPARATUS FOR MILKING PHASE OF

Номер: AR0000084260A1
Автор:
Принадлежит:

Un método para la operación de un aparato para fase de lechada (10) incluye alimentar uno o más reactivos gaseosos a un cuerpo de lechada (37) de material sólido en partículas suspendido en un líquido de suspensión contenido en el interior de un recipiente (12). Dichos uno o más reactivos gaseosos son alimentados al cuerpo de la lechada (37) a través de un distribuidor de gases (14) que presenta bocas de salida de gas dirigidas en dirección descendente (32) y son alimentados hacia una partición impermeable a los fluidos (18) que cruza de lado a lado el recipiente (12) por debajo del distribuidor de gases (14). La partición (18) divide el recipiente (12) en un volumen de lechada (19) por encima de la partición (18) y un volumen de fondo (36) por debajo de la partición (18). Se mantiene una presión diferencial sobre la partición (18) entre límites predefinidos mediante la manipulación o la habilitación de cambios de presión en el volumen de fondo (36) merced al empleo de un conducto de transferencia ...

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11-10-2007 дата публикации

BUBBLE TOWER TYPE HYDROCARBON SYNTHESIS REACTOR

Номер: WO000002007114271A1
Принадлежит:

Bubble tower type hydrocarbon synthesis reactor (100) comprising reactor main frame (110) accommodating slurry (120) having solid catalyst particles (124) suspended in liquid hydrocarbon (122), and distributor (140) disposed at an inferior portion of the reactor main frame (110) and used to feed a synthetic gas composed mainly of hydrogen and carbon monoxide into the slurry (120), wherein the reactor main frame (110) in its interior is provided with baffle plate (150) so as to block the side-wall side of the reactor main frame (110) and open the center part thereof.

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03-03-2005 дата публикации

PROCESS FOR SYNTHESISING HYDROCARBONS

Номер: WO2005019384A1
Принадлежит:

A process (10) for synthesising hydrocarbons includes feeding a gaseous feedstock (18) comprising hydrogen and carbon monoxide, into a first Fischer-Tropsch reaction stage (12) which is a three-phase low temperature catalytic Fischer-Tropsch reaction stage, and allowing the hydrogen and carbon monoxide partially to react catalytically in the first reaction stage (12) to form hydrocarbons. At least a portion of a tail gas (32) which includes unreacted hydrogen and carbon monoxide obtained from the first reaction stage, is fed into a second Fischer-Tropsch reaction stage (42) which is a two-phase high temperature catalytic Fischer-Tropsch reaction stage. The hydrogen and carbon monoxide are allowed at least partially to react catalytically in the second reaction stage (42) to form gaseous hydrocarbons.

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12-07-2007 дата публикации

Filtration system for slurry hydrocarbon synthesis process using both small and large pore filter elements

Номер: US2007161715A1
Принадлежит:

A method for separating and filtering solid particles from a hydrocarbon slurry liquid includes two or more filter sections in fluid communication with the hydrocarbon slurry. At least one filter section is comprised of one or more filter elements having a mean pore size of less than 10 microns, and at least one other section is comprised of one or more filter elements having a mean pore size of 10 microns or greater. The small pore filter (less than 10 microns) will exclude all or substantially all of the smaller catalyst fines produced by catalyst particle attrition. The liquid product removed from the small pore filters will be substantially free of particulates. The large pore filters (10 microns or greater) will exclude larger catalyst particles, but will allow the smaller fines to pass. The liquid product removed from the large pore filters will contain the fines generated from catalyst particle attrition.

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09-07-2020 дата публикации

ЗАГРУЗКА КАТАЛИЗАТОРА В БАРБОТАЖНУЮ КОЛОННУ ДЛЯ СИНТЕЗА ФИШЕРА-ТРОПША

Номер: RU2726117C2
Принадлежит: ИФП ЭНЕРЖИ НУВЕЛЛЬ (FR)

FIELD: separation; mixing.SUBSTANCE: invention relates to a method of loading a catalyst into synthesis reactor (40) such as a bubble column comprising separation circuit (21). Method includes the following steps: a) filling at least part of synthesis reactor (40) with solvent S1; b) filling at least part of separation circuit (21) of said synthesis reactor (40) with said solvent S1; c) said solvent S1 is subjected to circulation from synthesis reactor (40) to separation circuit (21) and from separation circuit to synthesis reactor (40); d) heating reactor (40) to temperature less than or equal to 100 °C; e) introducing inert gas into the lower portion of synthesis reactor (40) and increasing the pressure in synthesis reactor (40) until an absolute pressure in range of 0.1 to 0.6 MPa is achieved; f) mixing said catalyst with solvent S2 in reservoir (30) to produce solid/liquid mixture; g) increasing pressure in tank (30) to pressure of at least 0.2 MPa above pressure in synthesis reactor (40), then sending solid/liquid mixture obtained at step f) into synthesis reactor (40); h) removing at least a portion of said solvent S1 and/or S2 contained in synthesis reactor (40) and/or separation circuit (21).EFFECT: use of disclosed invention allows loading catalyst without using pump, which reduces the formation of fine catalyst particles, and also, the catalyst is loaded at a lower temperature.14 cl, 1 dwg РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 726 117 C2 (51) МПК C10G 2/00 (2006.01) B01J 8/18 (2006.01) B01J 8/22 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ (52) СПК C10G 2/344 (2020.01); C10G 2/30 (2020.01); C10G 2/32 (2020.01); B01J 8/0015 (2020.01); B01J 8/007 (2020.01); B01J 8/1836 (2020.01); B01J 8/22 (2020.01) (21)(22) Заявка: 2018122962, 08.11.2016 08.11.2016 Дата регистрации: 09.07.2020 (73) Патентообладатель(и): ИФП ЭНЕРЖИ НУВЕЛЛЬ (FR) 08.12.2015 FR 1562031 (43) Дата публикации заявки: 10.01.2020 Бюл. № 1 (45) ...

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27-04-2010 дата публикации

СИСТЕМА СИНТЕЗА ЖИДКОГО ТОПЛИВА

Номер: RU2008141283A
Принадлежит:

... 1. Система синтеза жидкого топлива, включающая: ! реформинг-аппарат, который преобразует углеводородный сырьевой материал для получения синтез-газа, содержащего газообразный монооксид углерода и газообразный водород в качестве основных компонентов; ! реактор, который синтезирует жидкие углеводороды из газообразного монооксида углерода и газообразного водорода, содержащихся в синтез-газе; ! устройство для повышающей качество обработки, которое осуществляет заданную повышающую качество обработку жидких углеводородов, синтезированных в реакторе; и ! нагревательное устройство, которое нагревает жидкие углеводороды, вводимые в устройство для повышающей качество обработки, с использованием газа, выводимого из реформинг-аппарата, в качестве источника тепла. ! 2. Система синтеза жидкого топлива по п.1, в которой ! устройство для повышающей качество обработки представляет собой ректификационную колонну, которая производит фракционную разгонку жидких углеводородов на множество видов жидких топлив ...

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27-04-2009 дата публикации

СПОСОБЫ ОБЕСПЕЧЕНИЯ ФУНКЦИОНИРОВАНИЯ РЕАКТОРА С ПСЕВДООЖИЖЕННЫМ СЛОЕМ И ТРЕХФАЗНОГО ШЛАМОВОГО РЕАКТОРА

Номер: RU2007138256A
Принадлежит:

... 1. Способ обеспечения функционирования двухфазного реактора с псевдоожиженным слоем, включающий в себя следующие операции: ! подача на низком уровне по меньшей мере одного газообразного реагента в вертикально расположенную псевдоожиженную массу твердых частиц, причем псевдоожиженная масса находится по меньшей мере в двух вертикально идущих стволах, расположенных рядом друг с другом внутри общей оболочки реактора, при этом каждый ствол разделен на множество вертикально идущих каналов, по меньшей мере некоторые из которых имеют связь по потоку, причем псевдоожиженная масса присутствует по меньшей мере в некоторых из каналов, при этом по меньшей мере некоторые из стволов и/или каналов по меньшей мере частично ограничены поверхностями теплообмена; ! создание условий для реакции газообразного реагента, когда он проходит вверх через псевдоожиженную массу, присутствующую по меньшей мере в некоторых из каналов стволов, в результате чего образуется газообразный продукт; ! создание условий для отделения ...

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10-06-2015 дата публикации

ВПРЫСК ДОБАВКИ В УСТАНОВКУ СИНТЕЗА УГЛЕВОДОРОДОВ ИЗ СИНТЕЗ-ГАЗА, ПОЗВОЛЯЮЩИЙ КОНТРОЛИРОВАТЬ И ПОДДЕРЖИВАТЬ РАВНОМЕРНУЮ КОНЦЕНТРАЦИЮ КАТАЛИЗАТОРА

Номер: RU2013153933A
Принадлежит:

... 1. Способ синтеза углеводородов из сырья, содержащего синтез-газ, в котором применяют твердый катализатор Фишера-Тропша в трехфазной реакционной секции, выполненной таким образом, что упомянутый катализатор поддерживается в суспензии в жидкой фазе за счет циркуляции газовой фазы снизу вверх в упомянутой реакционной секции, отличающийся тем, что для контроля и поддержания равномерной концентрации частиц катализатора в реакционной секции осуществляют следующие этапы:(а) для любого i, находящегося в пределах от 1 до n-1, где n обозначает число точек измерения давления, расположенных вдоль продольной оси реактора, и, по меньшей мере, равно 3, измеряют дифференциальные давления ΔРмежду двумя последовательными точками измерения давления, отстоящими друг от друга на Δh, и вычисляют потери напора на метр ΔG=ΔР/Δh,(b) для каждой потери напора на метр в упомянутой суспензии катализатора в жидкой фазе ΔGвычисляют значение, соответствующее разности между двумя последовательными потерями напора на метр ...

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14-03-2007 дата публикации

Process for separating a catalyst from a liquid

Номер: GB0002418626B
Принадлежит: SASOL TECH PTY LTD, SASOL TECHNOLOGY

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15-03-1986 дата публикации

PROCEDURE FOR THE PRODUCTION OF HYDROCARBONS

Номер: AT0000275682A
Автор:
Принадлежит:

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11-10-2007 дата публикации

Liquid fuel synthesis system

Номер: AU2007232922A1
Принадлежит:

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15-03-2012 дата публикации

Hydrocarbon synthesis reaction apparatus, hydrocarbon synthesis reaction system, and method for collection of liquid hydrocarbon

Номер: AU2010287744A1
Принадлежит:

Disclosed is a hydrocarbon synthesis reaction apparatus for synthesizing a hydrocarbon through a Fischer-Tropsch synthesis reaction. The apparatus comprises a reaction vessel, a flow path, a first cooling unit, a second cooling unit, a first separation unit for separating a liquid hydrocarbon that has been concentrated by means of the first cooling unit from a gaseous hydrocarbon, and a second separation unit for separating a liquid hydrocarbon that has been concentrated by means of the second cooling unit from a gaseous hydrocarbon, wherein the first cooling unit cools a gaseous hydrocarbon passing through the flow path to a temperature equal to or lower than a condensation temperature at which a wax fraction is condensed and higher than a congeal point at which the wax fraction congeals, and the second cooling unit cools a gaseous hydrocarbon passing through the flow path to a temperature lower than a temperature to which the gaseous hydrocarbon is cooled by means of the first cooling ...

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23-02-2017 дата публикации

A METHOD OF OPERATING A SLURRY BUBBLE COLUMN REACTOR

Номер: CA0002995432A1
Принадлежит:

A method for starting a slurry bubble column reactor that includes a reactor vessel holding a settled or slumped bed of particles and a liquid phase from which the particles have settled includes introducing a flow of a re-suspension liquid into the settled or slumped bed to loosen the settled or slumped bed. The introduction of the re-suspension liquid takes place before the introduction of any gas into the settled or slumped bed, or together with feeding of gas into the settled or slumped bed, provided that, if gas is fed together with the re-suspension liquid into the settled or slumped bed before the settled or slumped bed has been loosened, the gas has a superficial gas velocity in the reactor below 10 cm/s. Once the settled or slumped bed has been loosened by at least the re-suspension liquid, gas is passed at a superficial gas velocity above 10 cm/s through the liquid phase.

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15-06-2017 дата публикации

LOADING A CATALYST INTO A BUBBLE COLUMN FOR FISCHER-TROPSCH SYNTHESIS

Номер: CA0003004932A1
Принадлежит:

Procédé de chargement d'un catalyseur dans un réacteur (40) comprenant une boucle de séparation (21) comprenant les étapes suivantes : a) on remplit le réacteur (40) avec un solvant S1; b) on remplit la boucle de séparation (21) avec ledit solvant S1; c) on fait circuler ledit solvant S1 dans le réacteur de synthèse (40) et la boucle de séparation (21); d) on chauffe le réacteur (40) à une température inférieure ou égale à 100°C; e) on injecte en fond du réacteur (40) un gaz inerte; f) on mélange ledit catalyseur avec un solvant S2 dans une capacité (30) pour obtenir un mélange liquide/solide; g) on augmente la pression dans la capacité (30) puis on envoie le mélange liquide/solide vers le réacteur (40); h) on soutire ledit solvant S1 et/ou S2.

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05-03-2004 дата публикации

Hydrocarbon synthesis by Fischer-Tropsch reaction comprises use of coolant fluid fed into heat exchange zone at close to boiling point

Номер: FR0002843961A1
Принадлежит:

Procédé de synthèse d'hydrocarbures par réaction de Fischer-Tropsch à partir de gaz de synthèse, travaillant en fluidisation triphasique, le réacteur possédant un échangeur immergé au sein du lit fluidisé et utilisant comme fluide de réfrigération un fluide mis en oeuvre à sa température d'ébullition à une pression légèrement supérieure à la pression du procédé, cette température d'ébullition étant situé de 10 à 70°C au dessous de la température du procédé.

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11-02-2010 дата публикации

INCREASED HEAT EXCHANGE IN TWO OR THREE PHASE MEDIUM

Номер: KR0100941822B1

리브의 종횡비가 5 미만인 리브식 열교환 튜브는, 유동하는 가스 기포 또는 미립자 고체, 및 유동하는 가스 기포가 분산된 액체상을 포함하는 매체 내에서 사용되는 경우, 핀을 갖거나 또는 갖지 않는 종래의 열교환 튜브보다 큰 간접 열교환을 제공한다. 리브, 및 전형적으로 또한 열교환 튜브의 종축은 가스 기포 유동 방향에 평행한 방향으로 또는 그 종축을 따라 나선형으로 정렬된다. 이것은 ① 반응기 내의 온도의 증가 없이 슬러리 피셔-트롭시 탄화수소 합성 반응기의 생산성을 증가시키거나, 또는 ② 소정의 공급물 전환에서 반응 온도를 낮춤으로써 더 큰 분자량 탄화수소의 생산을 증대하는데 유용하다. Ribbed heat exchange tubes having an aspect ratio of ribs of less than 5 are conventional heat exchange tubes with or without fins when used in a medium comprising a flowing gas bubble or particulate solid and a liquid phase in which the flowing gas bubble is dispersed. Provide greater indirect heat exchange. The ribs, and typically also the longitudinal axis of the heat exchange tube, are helically aligned in a direction parallel to or along the longitudinal direction of the gas bubble flow. This is useful for increasing the production of a larger molecular weight hydrocarbon by increasing the productivity of the slurry Fischer-Tropsch hydrocarbon synthesis reactor without increasing the temperature in the reactor, or lowering the reaction temperature at a given feed conversion.

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12-07-2007 дата публикации

FILTRATION SYSTEM FOR SLURRY HYDROCARBON SYNTHESIS PROCESS USING BOTH SMALL AND LARGE PORE FILTER ELEMENTS

Номер: WO000002007079031A1
Принадлежит:

A method for separating and filtering solid particles from a hydrocarbon slurry liquid includes two or more filter sections in fluid communication with the hydrocarbon slurry. At least one filter section is comprised of one or more filter elements having a mean pore size of less than 10 microns, and at least one other section is comprised of one or more filter elements having a mean pore size of 10 microns or greater. The small pore filter (less than 10 microns) will exclude all or substantially all of the smaller catalyst fines produced by catalyst particle attrition. The liquid product removed from the small pore filters will be substantially free of particulates. The large pore filters (10 microns or greater) will exclude larger catalyst particles, but will allow the smaller fines to pass. The liquid product removed from the large pore filters will contain the fines generated from catalyst particle attrition.

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26-10-2011 дата публикации

METHOD AND SYSTEM FOR FINES MANAGEMENT IN SLURRY PROCESSES

Номер: EP2379215A1
Автор: SOTO, Jorge L.
Принадлежит:

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25-09-2013 дата публикации

Номер: JP0005301330B2
Автор:
Принадлежит:

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10-05-2016 дата публикации

СПОСОБ ПОЛУЧЕНИЯ ПО МЕНЬШЕЙ МЕРЕ ОДНОГО ПРОДУКТА ИЗ ПО МЕНЬШЕЙ МЕРЕ ОДНОГО ГАЗООБРАЗНОГО РЕАГЕНТА В СУСПЕНЗИОННОМ СЛОЕ

Номер: RU2583457C2

FIELD: technological processes. SUBSTANCE: method of producing at least one product of at least one gaseous reagent involves supply of gaseous reagent as gaseous material (59) or part of the gaseous material (59) at specified speed of gas at inlet of at least 0.5 m/s to vessel (12), containing the expanded suspension layer (70) of solid catalyst particles suspended in suspension, so that gaseous reagent can bubble through upwards through suspension layer (70). Suspension layer (70) has loading catalyst less than 14 vol.% of pumped out suspension. Gaseous reagent comes in catalytic reaction at pressure above atmospheric as gaseous reagent bubble through upwards through suspension layer (70) to obtain at least one product. Products and any unreacted gaseous reagent is removed from container (12). EFFECT: method of obtaining at least one product of at least one gaseous reagent. 9 cl, 10 dwg, 1 tbl РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (51) МПК B01J 8/22 (11) (13) 2 583 457 C2 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ (21)(22) Заявка: ИЗОБРЕТЕНИЯ К ПАТЕНТУ 2013154045/05, 30.05.2012 (24) Дата начала отсчета срока действия патента: 30.05.2012 (72) Автор(ы): БРЕМАН Бертхольд Беренд (NL) (73) Патентообладатель(и): СЭСОЛ ТЕКНОЛОДЖИ (ПРОПРИЕТЕРИ) ЛИМИТЕД (ZA) Приоритет(ы): (30) Конвенционный приоритет: R U 07.06.2011 ZA 2011/04229; 07.06.2011 US 61/493,988 (43) Дата публикации заявки: 20.07.2015 Бюл. № 20 (56) Список документов, цитированных в отчете о поиске: RU 2342355 C2, 27.12.2008. US 6800664 B1, 05.10.2004. RU 2108146 C1, 10.04.1998. RU 2190588 C2, 10.10.2002.. (85) Дата начала рассмотрения заявки PCT на национальной фазе: 09.01.2014 2 5 8 3 4 5 7 (45) Опубликовано: 10.05.2016 Бюл. № 13 (86) Заявка PCT: 2 5 8 3 4 5 7 R U C 2 C 2 IB 2012/052693 (30.05.2012) (87) Публикация заявки PCT: WO 2012/168830 (13.12.2012) Адрес для переписки: 119019, Москва, Гоголевский бульвар, 11, этаж 3, "Гоулингз Интернэшнл Инк.", Соболеву А.Ю. (54) СПОСОБ ПОЛУЧЕНИЯ ...

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20-12-2015 дата публикации

РЕАЛИЗАЦИЯ СПОСОБОВ С ПРИМЕНЕНИЕМ КАТАЛИЗАТОРА, КОТОРЫЙ ИНАКТИВИРУЕТСЯ ВО ВРЕМЕНИ

Номер: RU2571121C2

FIELD: chemistry. SUBSTANCE: invention relates to method for conversion of one or more reagents into one or several products in reactor with fluidised catalyst bed, which is inactivated in time. Method includes, in the course of catalytic cycle at stage A, gradual increase of working temperature in reactor to counteract negative impact of catalyst inactivation on rate of reagent conversion, with working temperature not exceeding specified maximal working temperature, and at stage B addition of catalyst, possessing property to increase rate of reagent conversion, into reactor and reduction of working temperature for partial counteraction of impact of added catalyst on rate of reagent conversion, with working temperature remaining higher than specified minimal working temperature, and repetition of A and B stages. EFFECT: invention provides long-term working procedure for methods, in which catalyst inactivation takes place in the course of time. 14 cl, 7 dwg, 3 ex РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 571 121 C2 (51) МПК B01J 8/22 (2006.01) C10G 2/00 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ (21)(22) Заявка: ИЗОБРЕТЕНИЯ К ПАТЕНТУ 2013119829/05, 10.10.2011 (24) Дата начала отсчета срока действия патента: 10.10.2011 (72) Автор(ы): НЕЛ Херман Герхардус (ZA) (73) Патентообладатель(и): СЭСОЛ ТЕКНОЛОДЖИ (ПРОПРИЕТЕРИ) ЛИМИТЕД (ZA) Приоритет(ы): (30) Конвенционный приоритет: R U 27.10.2010 US 61/407,067; 27.10.2010 ZA 2010/07687 (43) Дата публикации заявки: 10.12.2014 Бюл. № 34 (56) Список документов, цитированных в отчете о поиске: US 6458857 B1, 01.10.2002. US 4927523 A, 22.05.1990. US 2003/0087971 A1, 08.05.2003. RU 2340394 С2, 10.12.2008. (85) Дата начала рассмотрения заявки PCT на национальной фазе: 27.05.2013 2 5 7 1 1 2 1 (45) Опубликовано: 20.12.2015 Бюл. № 35 (86) Заявка PCT: 2 5 7 1 1 2 1 R U C 2 C 2 IB 2011/054450 (10.10.2011) (87) Публикация заявки PCT: WO 2012/056346 (03.05.2012) Адрес для переписки: 119019, Москва, ...

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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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21-03-2013 дата публикации

Method Of Operating A Fluid Bed Reactor

Номер: US20130071293A1
Принадлежит: Individual

Method of operating a three-phase slurry reactor includes feeding at a low level at least one gaseous reactant into a vertically extending slurry body of solid particles suspended in a suspension liquid, the slurry body being contained in at least two vertically extending shafts housed within a common reactor shell, each shaft being divided into a plurality of vertically extending channels at least some of which are in slurry flow communication and the slurry body being present in at least some of the channels. The gaseous reactant is allowed to react as it passes upwardly through the slurry body present in at least some of the channels of the shafts, thereby to form a non-gaseous and/or a gaseous product. Gaseous product, if present, and/or unreacted gaseous reactant is allowed to disengage from the slurry body in a head space above the slurry body.

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16-01-2014 дата публикации

METHOD FOR PRODUCING HYDROCARBONS

Номер: US20140018449A1
Автор: Shingu Masaki
Принадлежит:

A method for producing hydrocarbons includes: a synthesis step of synthesizing hydrocarbons by the Fischer-Tropsch synthesis reaction using a slurry bubble column reactor having a slurry containing catalyst particles and liquid hydrocarbons retained inside the reactor, and having a gas phase portion located above the slurry; a discharging step of passing the slurry through a filter positioned inside and/or outside the reactor, thereby separating and discharging the heavy liquid hydrocarbons; a backwash step of flushing liquid hydrocarbons through the filter in the opposite direction to the flow of the slurry, thereby returning the catalyst particles to the reactor; and a cooling and gas-liquid separation step of cooling the hydrocarbons discharged from the gas phase portion, and then separating and collecting the condensed light liquid hydrocarbons. The liquid hydrocarbons flushed through the filter in the backwash step include the light liquid hydrocarbons obtained in the cooling and gas-liquid separation step. 1. A method for producing hydrocarbons , the method comprising:a synthesis step of synthesizing hydrocarbons by a Fischer-Tropsch synthesis reaction, using a slurry bubble column reactor having a slurry comprising catalyst particles and liquid hydrocarbons retained inside the reactor, and having a gas phase portion located above the slurry,a discharging step of passing the slurry through a filter positioned inside and/or outside the reactor, thereby separating catalyst particles and heavy liquid hydrocarbons, and discharging the heavy liquid hydrocarbons,a backwash step of flushing liquid hydrocarbons through the filter in an opposite direction to a flow direction of the slurry, thereby returning catalyst particles accumulated on the filter to the slurry bed inside the reactor, anda cooling and gas-liquid separation step of cooling hydrocarbons discharged from the gas phase portion of the reactor that are gaseous under conditions inside the reactor, and then ...

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20-03-2014 дата публикации

METHOD FOR ESTIMATING CONTENT OF FINE PARTICLES IN SLURRY AND PROCESS FOR PRODUCING HYDROCARBON OIL

Номер: US20140080926A1
Автор: Hayasaka Kazuaki
Принадлежит:

A method for estimating a particulate content in a slurry of the present invention is a method for estimating a content of particulates having a predetermined particle size or less in a slurry with solid particles dispersed in hydrocarbons including a wax, the method including, based on a correlation between a visible light transmittance and a content of solid particles having the predetermined particle size or less at a temperature at which hydrocarbons including a wax are liquefied when the solid particles having the predetermined particle size or less are dispersed in the hydrocarbons, estimating a content of particulates having the predetermined particle size or less in the slurry from a visible light transmittance of a supernatant part when the slurry is left to stand at the temperature. 1. A method for estimating a content of particulates having a predetermined particle size or less in a slurry with solid particles dispersed in hydrocarbons including a wax , the method comprising , based on a correlation between a visible light transmittance and a content of solid particles having the predetermined particle size or less at a temperature at which hydrocarbons including a wax are liquefied when the solid particles having the predetermined particle size or less are dispersed in the hydrocarbons , estimating a content of particulates having the predetermined particle size or less in the slurry from a visible light transmittance of a supernatant part when the slurry is left to stand at the temperature.2. The method for estimating a particulate content in a slurry according to claim 1 , wherein the solid particle is a Fischer-Tropsch synthesis catalyst in which cobalt and/or ruthenium is supported by an inorganic oxide catalyst support.3. A process for producing a hydrocarbon oil by a Fischer-Tropsch synthesis reaction using a slurry bubble column reactor that retains a slurry containing catalyst particles and liquid hydrocarbons inside thereof and that has a ...

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17-04-2014 дата публикации

PROCESS FOR PRODUCING AT LEAST ONE PRODUCT FROM AT LEAST ONE GASEOUS REACTANT IN A SLURRY BED

Номер: US20140107232A1
Принадлежит: SASOL TECHNOLOGY (PROPRIETARY) LIMITED

A process for producing at least one product from at least one gaseous reactant includes feeding the gaseous reactant, as a gaseous feed or as part of a gaseous feed which is ax an inlet superficial gas velocity of at least 0.5 m/s, into a vessel holding an expanded slurry bed of solid catalyst particles suspended in a suspension liquid so that the gaseous reactant can bubble upwardly through die slurry bed. The slurry bed has a catalyst loading of less than 14% by volume of degassed slurry. The gaseous reactant is allowed to react catalytically at a pressure above atmospheric pressure as the gaseous reactant bubbles upwardly through the slurry bed to produce at least one product. The product and any unreacted gaseous reactant are withdrawn from the vessel. 1. A process for producing at least one product from at least one gaseous reactant , the process includingfeeding said at least one gaseous reactant, as a gaseous feed or as part of a gaseous feed which is at an inlet superficial gas velocity of at least 0.5 m/s, into a vessel holding an expanded slurry bed of solid catalyst particles suspended in a suspension liquid so that the gaseous reactant can bubble upwardly through the slurry bed, the slurry bed having a catalyst loading of less than 14% by volume of degassed slurry;allowing said at least one gaseous reactant to react catalytically at a pressure above atmospheric pressure as the gaseous reactant bubbles upwardly through the slurry bed to produce said at least one product; andwithdrawing said at least one product and any unreacted gaseous reactant from the vessel.2. The process as claimed in claim 1 , in which the gaseous feed includes at least CO and Has gaseous reactants claim 1 , and in which the gaseous feed is fed into the slurry bed to produce liquid and gaseous hydrocarbons claim 1 , with the catalyst being a hydrocarbon synthesis catalyst.3. The process as claimed in claim 1 , in which the inlet superficial gas velocity is at least 0.6 m/s.4. The ...

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05-06-2014 дата публикации

INJECTION OF ADDITIVE INTO A UNIT FOR SYNTHESISING HYDROCARBONS STARTING FROM SYNTHESIS GAS ENABLING A HOMOGENOUS CONCENTRATION OF CATALYST TO BE CONTROLLED AND MAINTAINED

Номер: US20140155500A1
Принадлежит:

The invention relates to a process for synthesising hydrocarbons starting from a feedstock containing synthesis gas. In the process a solid Fischer-Tropsch catalyst is employed in a three-phase reaction section operated so that the catalyst is maintained in suspension in a liquid phase by the circulation of a gaseous phase from the bottom to the top of the reaction section. The process utilizes conditions to control and maintain the homogeneity of the concentration of catalyst particles in the reaction section. 1. Process for synthesising hydrocarbons starting from a feedstock containing synthesis gas , in which a solid Fischer-Tropsch catalyst is employed in a three-phase reaction section operated so that said catalyst is maintained in suspension in a liquid phase by the circulation of a gaseous phase from the bottom to the top of said reaction section , characterised in that the following stages are carried out so as to control and maintain the homogeneity of the concentration of catalyst particles in the reaction section:{'sub': i', 'i', 'i', 'i', 'i, '(a) for all i between 1 and n−1, n representing the number of pressure measuring points disposed along the longitudinal axis of the reactor and being at least equal to 3, the differential pressures ΔPbetween two consecutive pressure measuring points spaced apart by Δhare measured and the pressure drops per metre ΔG=ΔP/Δhare calculated,'}{'sub': j', 'j+1', 'j', 'j+1', 'j, '(b) for each pressure drop per metre in said catalyst suspension in the liquid phase ΔG, a value is calculated corresponding to the difference between two consecutive pressure drops per metre divided by their mean (ΔG−ΔG)/((ΔG+ΔG)/2),'}(C) if at least one of the values calculated in the stage (b) is not less than 20%, at least one additive comprising at least one organosilicon polymer is injected at least at the bottom of said reaction section.2. Process according to claim 1 , such that the stages (a) to (c) are repeated over the course of time.3. ...

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18-04-2019 дата публикации

SLURRY BUBBLE COLUMN REACTOR FOR A FISCHER-TROPSCH PROCESS

Номер: US20190112532A1
Принадлежит:

The disclosure deals with a slurry bubble column reactor for converting a gas mixture comprising carbon monoxide and hydrogen into liquid hydrocarbons. The slurry bubble column reactor features a slurry bed of catalyst particles, an inlet conduit for feeding the gas mixture into the slurry bed, a filtration zone for separating the liquid hydrocarbons from the catalyst particles and a liquid outlet conduit for withdrawing the separated hydrocarbons from the filtration zone. The filtration zone is situated in the slurry bubble column reactor such that the slurry bed is found in a first and a second heat exchange zone with the filtration zone arranged between the first and the second heat exchange zone. 1. A slurry bubble column reactor for converting a gas mixture comprising carbon monoxide and hydrogen into liquid hydrocarbons featuring a slurry bed of catalyst particles , an inlet conduit for feeding the gas mixture into the slurry bed , a filtration zone for separating the liquid hydrocarbons from the catalyst particles and an liquid outlet conduit for withdrawing the separated hydrocarbons from the filtration zone , at wherein the filtration zone is situated in the slurry bubble column reactor such that the slurry bed is found in a first and a second heat exchange zone with the filtration zone arranged between the first and the second heat exchange zone.2. The slurry bubble column reactor according to wherein each heat exchange zone features a separate heat exchanger.3. The slurry bubble column reactor according to wherein the slurry bubble column reactor comprises a bottom zone and the inlet conduit is fluently connected to the bottom zone.4. The slurry bubble column reactor according to claim 3 , wherein the first heat exchange zone is situated next to the bottom zone of the slurry bubble column reactor.5. The slurry bubble column reactor according to claim 1 , wherein the filtration zone comprises at least one hollow and enclosed filter element and at least one ...

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03-05-2018 дата публикации

SLURRY PHASE APPARATUS

Номер: US20180117558A1
Принадлежит: SASOL TECHNOLOGY (PROPRIETARY) LIMITED

A method of operating a slurry phase apparatus includes feeding one or more gaseous reactants into a slurry body of solid particulate material suspended in a suspension liquid contained inside a vessel. The one or more gaseous reactants are fed into the slurry body through a gas distributor having downward facing gas outlets and are fed towards a fluid impermeable partition spanning across the vessel below the gas distributor. The partition divides the vessel into a slurry volume above the partition and a bottom volume below the partition. A differential pressure is maintained over the partition between predefined limits by manipulating or allowing changes in the pressure in the bottom volume by employing a pressure transfer passage establishing flow or pressure communication between the bottom volume and a head space above the slurry body. 19-. (canceled)10. A slurry phase apparatus which includesa slurry vessel to hold a slurry body comprising a liquid and solid particulate material with a head space volume above the slurry body;a gas distributor in a lower portion of the vessel which defines downwards facing gas outlets;a fluid impermeable partition spanning across the slurry vessel below the gas distributor partitioning the vessel into a slurry volume above the partition and a bottom volume below the partition; anda pressure transfer passage or conduit passing through or around the partition allowing transfer of pressure into and from the bottom volume, the pressure transfer passage in use establishing flow or pressure communication between the bottom volume and the head space volume in the slurry vessel above the slurry volume thereby to maintain a differential pressure over the partition between predefined limits by manipulating or allowing changes in the pressure in the bottom volume.11. The apparatus according to claim 10 , in which the fluid impermeable partition is planar or flat and arranged perpendicular to a longitudinal vertical central axis of the ...

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21-05-2020 дата публикации

Method and apparatus for preparing gasoline and aromatics by using fischer-tropsch synthesis exhaust

Номер: US20200157433A1

The present invention provides a method for preparing gasoline and aromatics by using Fischer-Tropsch synthesis exhaust. The method includes conducting an olefin conversion reaction on Fischer-Tropsch synthesis exhaust under the action of a first molecular sieve catalyst. A first refrigeration or cooling is conducted on an obtained product to obtain ultralow sulfur-containing gasoline and first-stage reaction gas. An alkaline aromatization reaction is conducted on the first-stage reaction gas under the action of a second molecular sieve catalyst. A second refrigeration or cooling is conducted on an obtained product to obtain aromatics. After the olefin conversion reaction, a gasoline component is separated and residual alkanes enter a second-stage fluidized bed reactor for the alkane aromatization reaction to produce aromatics. The present invention implements step conversion of different components in the Fischer-Tropsch exhaust, and has advantages of high reaction yield, easy catalyst regeneration and amplification, and the like.

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09-09-2021 дата публикации

SYSTEMS AND PROCESSES FOR DIRECT CRUDE OIL UPGRADING TO HYDROGEN AND CHEMICALS

Номер: US20210277318A1
Принадлежит: Saudi Arabian Oil Company

Systems and methods for direct crude oil upgrading to hydrogen and chemicals including separating an inlet hydrocarbon stream into a light fraction and a heavy fraction comprising diesel boiling point temperature range material; producing from the light fraction syngas comprising Hand CO; reacting the CO produced; producing from the heavy fraction and separating CO, polymer grade ethylene, polymer grade propylene, Ccompounds, cracking products, light cycle oils, and heavy cycle oils; collecting and purifying the COproduced from the heavy fraction; processing the Ccompounds to produce olefinic oligomerate and paraffinic raffinate; separating the cracking products; oligomerizing a light cut naphtha stream; hydrotreating an aromatic stream; hydrocracking the light cycle oils to produce a monoaromatics product stream; gasifying the heavy cycle oils; reacting the CO produced from gasifying the heavy cycle oils; collecting and purifying the CO; and processing and separating produced aromatic compounds into benzene and para-xylene. 1. A method for hydrocarbon separation and upgrading , the method comprising the steps of:separating an inlet hydrocarbon stream into a light fraction comprising naphtha boiling point temperature range material and a heavy fraction comprising diesel boiling point temperature range material;{'sub': '2', 'producing from the light fraction syngas comprising Hand CO;'}reacting the CO produced from the light fraction via at least one reaction selected from the group consisting of: carbonylation, polymerization, and water-gas shift;{'sub': 2', '4, 'producing from the heavy fraction and separating CO, polymer grade ethylene, polymer grade propylene, Ccompounds, cracking products comprising naphtha boiling point temperature range products with olefins and aromatics, light cycle oils, and heavy cycle oils;'}{'sub': '2', 'collecting and purifying the COproduced from the heavy fraction;'}{'sub': '4', 'processing the Ccompounds to produce olefinic ...

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17-09-2015 дата публикации

SYSTEM AND METHOD FOR CATALYST LOADING/MIXING

Номер: US20150258516A1
Принадлежит:

A catalyst loading system comprising: a vessel comprising at least one gas distribution nozzle at or near the bottom of the vessel, a top fluid distributor located at or near the top of the vessel, a catalyst inlet through which catalyst is introduced into the vessel, a first contact point at which catalyst introduced into the vessel first contacts the contents of the vessel, and a discharge outlet whereby catalyst exits the vessel. Methods of preparing catalyst slurry for introduction into a downstream reactor or in-situ activation within the vessel utilizing the catalyst loading system are also disclosed. 1. A catalyst loading system comprising:a vessel comprising at least one gas distribution nozzle at or near the bottom of the vessel, a top fluid distributor located at or near the top of the vessel, a catalyst inlet through which catalyst is introduced into the vessel, a first contact point at which catalyst introduced into the vessel first contacts the contents of the vessel, and a discharge outlet whereby catalyst slurry exits the vessel.2. The system of wherein the vessel further comprises temperature control apparatus whereby the contents of the vessel may be maintained at a desired temperature.3. The system of wherein the vessel is a catalyst activation reactor claim 1 , a catalytic reactor claim 1 , or both.4. The system of wherein the first contact point is located at a level below the level of the top fluid distributor.5. The system of wherein the top fluid distributor is a liquid distributor.6. The system of wherein the top fluid distributor comprises a plurality of distribution points or nozzles.7. The system of wherein the top fluid distributor comprises at least 8 nozzles.8. The system of further comprising a bottom distributor comprising the at least one gas distribution nozzle.9. The system of wherein the bottom distributor is a gas distributor.10. The system of wherein the bottom distributor comprises at least 8 distribution points or nozzles.11. ...

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18-12-2014 дата публикации

SLURRY PHASE APPARATUS

Номер: US20140371334A1
Принадлежит: SASOL TECHNOLOGY (PROPRIETARY) LIMITED

A method of operating a slurry phase apparatus includes feeding one or more gaseous reactants into a slurry body of solid particulate material suspended in a suspension liquid contained inside a vessel. The one or more gaseous reactants are fed into the slurry body through a gas distributor having downward facing gas outlets and are fed towards a fluid impermeable partition spanning across the vessel below the gas distributor. The partition divides the vessel into a slurry volume above the partition and a bottom volume below the partition. A differential pressure is maintained over the partition between predefined limits by manipulating or allowing changes in the pressure in the bottom volume by employing a pressure transfer passage establishing flow or pressure communication between the bottom volume and a head space above the slurry body. 1. A method of operating a slurry phase apparatus , the method includingfeeding one or more gaseous reactants into a slurry body of solid particulate material suspended in a suspension liquid contained inside a vessel, with a head space above the slurry body, the one or more gaseous reactants being fed into the slurry body through a gas distributor having downward facing gas outlets and being fed towards a fluid impermeable partition spanning across the vessel below the gas distributor, the partition dividing the vessel into a slurry volume above the partition and a bottom volume below the partition; andmaintaining a differential pressure over the partition between predefined limits by manipulating or allowing changes in the pressure in the bottom volume by employing a pressure transfer passage establishing flow or pressure communication between the bottom volume and the head space above the slurry body.2. The method according to claim 1 , in which the partition is planar or flat and arranged perpendicular to a longitudinal vertical central axis of the vessel claim 1 , thus defining a false floor or bottom for the vessel.3. The ...

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05-09-2019 дата публикации

A PROCESS FOR PRODUCING HYDROCARBONS

Номер: US20190270937A1
Принадлежит: SHELL OIL COMPANY

The present application relates to a process for producing normally gaseous, normally liquid, and optionally normally solid hydrocarbons from synthesis gas in a three-phase reactor, said reactor comprising a top middle and bottom part wherein the bottom and top part are fluidly connected via one or more reactor tubes, wherein one or more reactor tubes comprise randomly stacked catalyst bodies held stationary in the reactor tube and the reactor is at least partially filled with a liquid medium, said process comprising the steps of: (i) introducing the synthesis gas into the reactor via the bottom part; and (ii) contacting the synthesis gas with a stationary catalyst to catalytically convert the synthesis gas at an elevated temperature to obtain the normally gaseous, normally liquid, and optionally normally solid hydrocarbons from synthesis gas; (iii) withdrawing the normally gaseous, normally liquid, and optionally normally solid hydrocarbons; wherein the catalyst bodies have an open celled foam structure. 1. A process for producing normally gaseous , normally liquid , and optionally normally solid hydrocarbons from synthesis gas in a three-phase reactor , said reactor comprising a top middle and bottom part wherein the bottom and top part are fluidly connected via one or more reactor tubes , wherein one or more reactor tubes comprise randomly stacked catalyst bodies held stationary in the reactor tube and the reactor is at least partially filled with a liquid medium , said process comprising the steps of:(i) introducing the synthesis gas into the reactor via the bottom part of the reactor; and(ii) contacting the synthesis gas with a stationary catalyst to catalytically convert the synthesis gas at an elevated temperature to obtain the normally gaseous, normally liquid, and optionally normally solid hydrocarbons from synthesis gas;(iii) withdrawing the normally gaseous, normally liquid, and optionally normally solid hydrocarbons;wherein the randomly packed catalyst ...

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11-10-2018 дата публикации

Flexible Options for Utilizing Naphtha from a Low Temperature Fischer-Tropsch Process in a Plant Converting Biomass to Syncrude or Transportation Fuels

Номер: US20180291279A1
Принадлежит:

A bio-reforming reactor receives biomass to generate chemical grade syngas for a coupled downstream train of a low-temperature Fischer-Tropsch reactor train that uses this syngas derived from the biomass in the bio-reforming reactor. A renewable carbon content of the produced gasoline, jet fuel, and/or diesel derived from the coupled downstream train the low-temperature Fischer-Tropsch reactor train are optimized for recovery of renewable carbon content to produce fuel products with 100% biogenic carbon content and/or fuel products with 50-100% biogenic carbon content. The low-temperature Fischer-Tropsch reactor train produces syncrude, transportation fuels such as bio-gasoline or bio-diesel, or a combination thereof. 1. An integrated plant , comprising: wherein a first stage of the bio-reforming reactor includes a circulating fluidized bed reactor that has one or more media inputs to feed heat-absorbing media, a vessel to circulate the heat-absorbing media, and one or more biomass inputs to supply the biomass,', 'wherein the first stage is configured to cause a set of chemical reactions in the biomass to produce reaction products of constituent gases, tars, chars, and other components, which exit through a reactor output from the first stage,', {'sub': 1', '4, 'wherein a second stage of the bio-reforming reactor has an input configured to receive a stream of some of the reaction products including the constituent gases and at least some of the tars as raw syngas, and then chemically reacts the raw syngas within a vessel of the second stage to yield a chemical grade syngas by further processing including cracking and/or reforming the 1) tars, 2) light hydrocarbons (C-C) or 3) both into constituent molecules,'}, 'wherein the chemical grade syngas is mixed with a natural gas-derived syngas from a steam methane reformer to form a mixed syngas that is supplied to an input of the LTFT reactor train configured to produce LTFT fuel product, and', {'sub': 1', '5', '1', '5, ...

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27-10-2016 дата публикации

A METHOD OF SHUTTING DOWN AN OPERATING THREE-PHASE SLURRY BUBBLE COLUMN REACTOR

Номер: US20160310925A1
Принадлежит: SASOL TECHNOLOGY PROPRIETARY LIMITED

A method is provided of shutting down an operating three-phase slurry bubble column reactor () having downwardly directed gas distribution nozzles () submerged in a slurry body () of solid particulate material suspended in a suspension liquid contained inside a reactor vessel (), with the gas distribution nozzles () being in flow communication with a gas feed line () through which gas is being fed to the gas distribution nozzles () by means of which the gas is injected downwardly into the slurry body (). The method includes abruptly stopping flow of gas from the gas feed line () to the gas distribution nozzles () to trap gas in the gas distribution nozzles () thereby to inhibit slurry ingress upwardly into the gas distribution nozzles (). 1. A method of shutting down an operating three-phase slurry bubble column reactor having downwardly directed gas distribution nozzles submerged in a slurry body of solid particulate material suspended in a suspension liquid contained inside a reactor vessel , with the gas distribution nozzles being in flow communication with a gas feed line through which gas is being fed to the gas distribution nozzles by means of which the gas is injected downwardly into the slurry body , the method includingabruptly stopping flow of gas from the gas feed line to the gas distribution nozzles to trap gas in the gas distribution nozzles thereby to inhibit slurry ingress upwardly into the gas distribution nozzles.2. The method as claimed in claim 1 , wherein abruptly stopping flow of gas from the gas feed line to the gas distribution nozzles involves activating a fast response valve in the gas feed line to close off the gas feed line from the gas distribution nozzles.3. The method as claimed in claim 2 , wherein the fast response valve has a response time of between 1 and 10 seconds.4. The method as claimed in any of to claim 2 , wherein the gas distribution nozzles have outlets that are at the same elevation.5. The method as claimed in any of to ...

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27-12-2018 дата публикации

LOADING A CATALYST INTO A BUBBLE COLUMN FOR FISCHER-TOPSCH SYNTHESIS

Номер: US20180369776A1
Принадлежит: IFP ENERGIES NOUVELLES

A method for charging a catalyst into a reactor () comprising a separation loop (), comprising the following steps: 14021. A method for charging a catalyst into a synthesis reactor () , of the bubble column type , comprising a separation loop () , said method comprising the following steps:{'b': 40', '1, 'a) filling at least a portion of the synthesis reactor () with a solvent S;'}{'b': 21', '40', '1, 'b) filling at least a portion of the separation loop () of said synthesis reactor () with said solvent S;'}{'b': 1', '40', '21', '40, 'c) causing said solvent S to move from the synthesis reactor () to the separation loop () and from the separation loop to the synthesis reactor ();'}{'b': '40', 'd) heating the synthesis reactor () to a temperature of 100° C. or less;'}{'b': 40', '40, 'e) injecting an inert gas into the bottom of the synthesis reactor () and increasing the pressure of the synthesis reactor () in a manner such as to obtain an absolute pressure in the range 0.1 to 0.6 MPa;'}{'b': 2', '30, 'f) mixing said catalyst with a solvent S in a vessel () in order to obtain a liquid/solid mixture;'}{'b': 30', '40', '40, 'g) increasing the pressure in the vessel () to a pressure which is at least 0.2 MPa higher than the pressure of the synthesis reactor (), then sending the liquid/solid mixture obtained in step f) to the synthesis reactor ();'}{'b': 1', '2', '40', '21, 'h) withdrawing at least a portion of said solvent S and/or S contained in the synthesis reactor () and/or in the separation loop ().'}212. The method as claimed in claim 1 , characterized in that the solvent S is identical to the solvent S.312. The method as claimed in claim 1 , characterized in that the solvent S and/or the solvent S are selected from hydrogenated polyalphaolefin solvents or hydrogenated isoparaffinic solvents.4. The method as claimed in claim 1 , further comprising the following steps after step h):{'b': '40', 'i) heating the synthesis reactor () to a temperature in the range 150° ...

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12-12-2019 дата публикации

Graphene Modified Iron-Based Catalyst and Preparation and Application Thereof for Use in Fischer-Tropsch Reaction

Номер: US20190374928A1
Принадлежит:

The present disclosure disclosures a graphene modified iron-based catalyst and preparation and application thereof for use in Fischer-Tropsch reaction, belonging to the technical field of catalytic conversion of synthesis gas. The catalyst consists of, by mass percent, 0.01-30% of graphene, 0-20% of promoter and 60-99.99% of iron oxide powder. The preparation process of the catalyst is as follows: the graphene, the iron oxide powder and the promoter are sequentially placed in an aqueous solution for ultrasonic treatment and stirring, and then rotary evaporation, drying and calcining are conducted. The preparation method is simple. The catalyst shows excellent activity in the Fischer-Tropsch reaction, and maintains a high CO conversion rate of 90% or above for a long time at a very high reaction space velocity; meanwhile, the alkane content in a product is low, and an olefin-alkane ratio can reach 14, thus having an extremely high industrial application value. 1. A method for preparing a graphene modified iron-based catalyst , wherein raw materials comprise 0.01-30 parts by mass of graphene , 0-20 parts by mass of promoter and 60-99.99 parts by mass of iron oxide ,the method comprising the following steps:(1) dispersing the graphene in an aqueous solution at 10-80° C. to form a suspension, ultrasonically dispersing for 0.5-5 h, and then stirring for 1-24 h;(2) adding the iron oxide into the suspension formed in the step (1) according to a stoichiometric ratio, and continuously stirring for 0.5-24 h;(3) adding a precursor of the promoter into the suspension formed in the step (2) according to a stoichiometric ratio, and continuously stirring for 1-24 h; and(4) conducting rotary evaporation on a solution obtained in the step (3) to dryness, drying an obtained solid at 80-120° C. for 1-24 h, and then calcining in a gas of nitrogen, helium or argon at 250-800° C. for 1-24 h to obtain the graphene modified iron-based catalyst, andwherein when the promoter is 0 part by ...

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11-05-2021 дата публикации

合成气合成低碳烯烃的催化剂体系

Номер: CN109092316B

本发明涉及合成气合成低碳烯烃的催化剂体系,主要解决现有技术中低碳烯烃选择性低的问题。本发明采用合成气合成低碳烯烃的催化剂体系,包括以下组份:1)n质量份的活性组分,所述活性组分包括以原子比计,化学式如下的组合物:Fe 100 Mo a Cr b Cs c O x ;a的取值范围为50.0~250.0;b的取值范围为5.0~20.0;c的取值范围为1.0~9.5;x为满足催化剂中各元素化合价所需的氧原子总数;2)1质量份惰性组份:所述惰性组份包括选自SiO 2 、Al 2 O 3 、分子筛、ZrO 2 和TiO 2 中的至少一种;n大于0且90以下的技术方案较好的解决了上述问题,适用于合成气合成低碳烯烃的工业生产。

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30-01-2020 дата публикации

Fluidized bed processes and catalyst systems for fischer-tropsch conversion

Номер: WO2020023098A1
Принадлежит: GAS TECHNOLOGY INSTITUTE

Processes and catalyst systems are disclosed for performing Fischer-Tropsch (FT) synthesis to produce C 4 + hydrocarbons, such as gasoline boiling-range hydrocarbons and/or diesel boiling-range hydrocarbons. Advantageously, catalyst systems described herein have additional activity (beyond FT activity) for in situ hydroisomerization and/or hydrocracking of wax that is generated according to the distribution of hydrocarbons obtained from the FT synthesis reaction. This not only improves the yield of hydrocarbons ( e.g ., C 4-19 hydrocarbons) that are useful for transportation fuels, but also allows for alternative reactor types, such as a fluidized bed reactor.

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31-08-2021 дата публикации

Fluidized bed processes and catalyst systems for Fischer-Tropsch conversion

Номер: US11104852B2
Принадлежит: GAS TECHNOLOGY INSTITUTE

Processes and catalyst systems are disclosed for performing Fischer-Tropsch (FT) synthesis to produce C4+ hydrocarbons, such as gasoline boiling-range hydrocarbons and/or diesel boiling-range hydrocarbons. Advantageously, catalyst systems described herein have additional activity (beyond FT activity) for in situ hydroisomerization and/or hydrocracking of wax that is generated according to the distribution of hydrocarbons obtained from the FT synthesis reaction. This not only improves the yield of hydrocarbons (e.g., C4-19 hydrocarbons) that are useful for transportation fuels, but also allows for alternative reactor types, such as a fluidized bed reactor.

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25-11-2003 дата публикации

Method of modifying and controlling catalyst selectivity in a Fischer-Tropsch process

Номер: US6653357B1
Принадлежит: Sasol Technology Pty Ltd

The invention provides a method for controlling a selectivity profile of products of a Fischer-Tropsch synthesis process, wherein a catalyst promoter, either dissolved in solution or in a powdered form, is directly injected into the reactor medium, typically into the reactor feedstream. The Fischer-Tropsch process is typically a High Temperature Fischer Tropsch (HTFT) process, and a typical chemical promoter for the HTFT process is potassium. By adding or doping the reaction medium with the catalyst promoter during the synthesis process, the selectivity profile of olefins and paraffins in the product stream is significantly changed, with more olefins being formed whilst the level of paraffins is reduced, and typically the level of olefins in the C 2 -C 4 range is increased. The catalyst promoter may form part of a promoter-carrying compound, for example, potassium carbonate.

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17-04-1984 дата публикации

Process for the preparation of organic compounds

Номер: US4443561A
Принадлежит: Shell Oil Co

In a two-stage process for the conversion of H 2 -poor syngas into hydrocarbons and oxygenates in which uncoverted syngas from the first stage product is converted in a second stage into paraffins over a Ni, Co or Ru catalyst, the H 2 /CO molar ratio of the feed for the second stage is adjusted to the required value of 1.75-2.25 by blending this feed with an H 2 -rich syngas with an H 2 /CO molar ratio of at least above 1.75 which latter gas has been obtained by subjecting a small portion of the feed for the first stage to a high temperature (above 325° C.) CO-shift.

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01-08-2014 дата публикации

피셔-트롭쉬 합성반응을 이용한 탄화수소 화합물의 제조방법

Номер: KR20140095187A
Принадлежит: 한국에너지기술연구원

본 발명은 피셔-트롭쉬 합성반응을 이용한 탄화수소 화합물의 제조방법에 관한 것으로서, 본 발명의 피셔-트롭쉬 합성반응을 이용한 탄화수소 화합물의 제조방법은 촉매 환원 반응기에 철계 촉매를 장입하는 장입단계, 촉매 환원 반응기에 촉매 활성화를 위한 제1 합성가스를 주입하여 환원처리하는 환원단계, 촉매 환원 반응기에 제2 합성가스를 주입시켜 상기 환원단계에서 환원처리한 철계 촉매와 교반시키는 교반단계, 교반단계에서 교반된 제2 합성가스 및 환원처리된 철계 촉매를 연결된 관을 통해 온라인(online)으로 피셔-트롭쉬 합성 반응기로 주입하는 주입단계, 피셔-트롭쉬 합성 반응기에서 교반된 제2 합성가스 및 환원처리된 철계 촉매를 반응시켜 탄화수소 화합물을 제조하는 제조단계를 포함한다. 이를 통해 별도의 반응기에서 촉매를 환원(활성화)시켜 피셔-트롭쉬 반응기에 투입시키기 때문에 피셔-트롭쉬 합성 반응을 이용한 탄화수소 화합물의 제조과정에서 추가로 촉매를 투입하기 용이하고, 활성화된 촉매를 공급하여 피셔-트롭쉬 합성반응을 이용한 탄화수소 화합물이 제조되는 시간을 단축할 수 있다.

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01-08-2014 дата публикации

피셔-트롭쉬 합성반응에서의 촉매 환원 반응기

Номер: KR20140095189A
Принадлежит: 한국에너지기술연구원

본 발명은 피셔-트롭쉬 합성반응을 이용한 탄화수소 화합물의 제조 시스템에 관한 것으로서, 본 발명의 촉매 환원 반응기는 피셔-트롭쉬 합성반응을 이용한 탄화수소 화합물의 제조 시스템에 있어서, 철계 촉매가 장입되고, 제1 합성가스가 주입되어 상기 철계 촉매가 환원처리되고, 환원처리된 철계 촉매와 주입된 제2 합성가스를 교반하는 교반기를 포함한다. 이를 통해 별도의 반응기에서 촉매를 환원(활성화)시켜 피셔-트롭쉬 반응기에 투입시키기 때문에 피셔-트롭쉬 합성 반응을 이용한 탄화수소 화합물의 제조과정에서 추가로 촉매를 투입하기 용이하고, 활성화된 촉매를 공급하여 피셔-트롭쉬 합성반응을 이용한 탄화수소 화합물이 제조되는 시간을 단축할 수 있다.

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17-05-2022 дата публикации

费托催化剂在气固流化床中的活化方法及产品和应用

Номер: CN111036153B

本发明涉及费托催化剂活化领域,公开了一种气固流化床费托合成催化剂的活化方法,该方法包括:1)从第一温度以20‑25℃/h的升温速率升温至第二温度,在第二温度下恒温1‑2h;2)从第二温度以8‑15℃/h的升温速率升温至第三温度,在第三温度下通入含CO的活化气氛;3)从第三温度以5‑10℃/h的升温速率升温至第四温度,在第四温度下恒温6‑18h;4)从第四温度以10‑20℃/h的降温速率降温至第三温度,在第三温度下停止通入含CO的活化气氛;5)从第三温度降温至第五温度,即得活化态费托催化剂。该方法得到的活化态费托合成催化剂用于费托反应合成时,具有高的CO转化率,低的CH 4 选择性、低的CO 2 选择性,催化剂在活化反应过程中催化剂没有发生大量磨损破碎。

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25-03-2004 дата публикации

Reactor with multiple risers and consolidated transport

Номер: US20040059171A1
Автор: Walter Brookhart
Принадлежит: ExxonMobil Chemical Patents Inc

The present invention is directed to a hydrocarbon conversion apparatus. The apparatus comprises the following: a plurality of riser reactors, each of the riser reactors having a first end into which a catalyst can be fed and a second end through which the catalyst can exit the riser reactor; a separation zone provided to separate the catalyst from products of a reaction conducted in the hydrocarbon conversion apparatus; at least one transport conduit having a first end in fluid communication with at least two of the second ends of the riser reactors and a second end extending into the separation zone; and at least one catalyst return in fluid communication with the separation zone and the first ends of the riser reactors, the catalyst return being provided to transfer the catalyst from the separation zone to the first ends of the riser reactors.

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17-10-2006 дата публикации

Reactor with multiple risers and consolidated transport

Номер: US7122160B2
Автор: Walter R. Brookhart
Принадлежит: ExxonMobil Chemical Patents Inc

The present invention is directed to a hydrocarbon conversion apparatus. The apparatus comprises the following: a plurality of riser reactors, each of the riser reactors having a first end into which a catalyst can be fed and a second end through which the catalyst can exit the riser reactor; a separation zone provided to separate the catalyst from products of a reaction conducted in the hydrocarbon conversion apparatus; at least one transport conduit having a first end in fluid communication with at least two of the second ends of the riser reactors and a second end extending into the separation zone; and at least one catalyst return in fluid communication with the separation zone and the first ends of the riser reactors, the catalyst return being provided to transfer the catalyst from the separation zone to the first ends of the riser reactors.

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20-05-2011 дата публикации

System of liquid fuel synthesis

Номер: RU2418840C2

FIELD: oil and gas production. SUBSTANCE: system of liquid fuel synthesis consists of reforming unit converting stock hydrocarbon material for production of synthetic gas containing gaseous monoxide of carbon and gaseous hydrogen as basic components. Further, the system consists of a reactor synthesising liquid hydrocarbons out of gaseous monoxide of carbon and gaseous hydrogen contained in synthetic gas by means of reaction of Fischer- Tropsch synthesis. The system also includes a refinement processing unit treating liquid hydrocarbons synthesised in the reactor, and a unit heating liquid hydrocarbons introduced into the refinement processing unit with utilisation of spent gas. This gas is produced by combustion of gaseous fuel in a burner of the reforming unit and is withdrawn from the reforming unit as heat carrier. Spent gas is supplied into the refinement processing unit directly. The latter corresponds either to a rectifying column performing fraction distillation of liquid hydrocarbons into multitude of types of liquid fuel with different boiling temperature and/or to a reactor for hydrogenation of liquid hydrocarbons. EFFECT: increased heat efficiency of whole system of liquid fuel synthesis. 2 cl, 2 dwg РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) 2 418 840 (13) C2 (51) МПК ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ, ПАТЕНТАМ И ТОВАРНЫМ ЗНАКАМ (12) ОПИСАНИЕ C10G C10G C10L C10G C07C C07C C01B 2/00 45/00 1/04 7/00 1/04 9/00 3/24 (2006.01) (2006.01) (2006.01) (2006.01) (2006.01) (2006.01) (2006.01) ИЗОБРЕТЕНИЯ К ПАТЕНТУ Приоритет(ы): (30) Конвенционный приоритет: 30.03.2006 JP 2006-095516 (73) Патентообладатель(и): НИППОН СТИЛ ИНДЖИНИРИНГ КО., ЛТД. (JP) R U (24) Дата начала отсчета срока действия патента: 29.03.2007 (72) Автор(ы): ОНИСИ Ясухиро (JP), ВАКАМУРА Осаму (JP), ФУДЗИМОТО Кенитиро (JP) (21)(22) Заявка: 2008141283/04, 29.03.2007 (43) Дата публикации заявки: 27.04.2010 Бюл. № 12 2 4 1 8 8 4 0 (45) Опубликовано: 20.05.2011 Бюл. № 14 (56) Список документов ...

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27-10-2015 дата публикации

Suspension apparatus

Номер: RU2566406C2

FIELD: medicine. SUBSTANCE: invention relates to a suspension apparatus and to its work method. The suspension apparatus operation method includes supply of one or more gaseous reagents into a suspension of solid particles suspended in the suspension liquid in a vessel with free space above the suspension; the said one or more gaseous reagents are supplied into the suspension (through the gas distribution unit that has gas outlets directed downwards) and onto the baffler that is impermeable for liquid; the baffler occludes the vessel below the gas distribution unit and divides the vessel into the suspension volume (over the baffle) and the bottom volume (below the baffle); the method also involves maintenance of a differential pressure over the baffle within the preset limits by way of adjusting pressure in the bottom volume or letting it change with the help of the pressure transfer channel establishing a flow or connection of pressures between the bottom volume and the free space above the suspension. EFFECT: invention allows to minimise the uncooled volume occupied by the gas distribution device and the uncooled volume below the gas distribution device, inhibits and prevents catalyst settlement and sedimentation and enables a reliable and simple mechanical design. 9 cl, 4 dwg РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 566 406 C2 (51) МПК B01J 8/18 (2006.01) B01J 8/22 (2006.01) C10G 2/00 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ (21)(22) Заявка: ИЗОБРЕТЕНИЯ К ПАТЕНТУ 2013132155/05, 12.12.2011 (24) Дата начала отсчета срока действия патента: 12.12.2011 Приоритет(ы): (30) Конвенционный приоритет: (43) Дата публикации заявки: 20.01.2015 Бюл. № 2 (73) Патентообладатель(и): СЭСОЛ ТЕКНОЛОДЖИ (ПРОПРИЕТЕРИ) ЛИМИТЕД (ZA) 2 5 6 6 4 0 6 (45) Опубликовано: 27.10.2015 Бюл. № 30 R U 13.12.2010 US 61/422,457; 13.12.2010 ZA 2010/08969 (72) Автор(ы): ШТЕЙНБЕРГ Андре Петер (ZA), КЛЕЙНХАНС Эверт Филипус (ZA), ЛИ Маршал Стивен (US), НЕЛ Херман ...

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23-03-2022 дата публикации

Catalyst

Номер: KR102378451B1

피셔-트롭쉬 공정은 탄화수소성 공급 원료의 통상적으로 액체 및/또는 고체 탄화수소로의 전환에 사용될 수 있다. 공급 원료 (예, 천연 가스, 부수 가스 및/또는 석탄층 메탄, 석탄) 는 제 1 단계에서 수소 및 일산화탄소의 혼합물 (상기 혼합물은 흔히 합성 가스 또는 신가스로 칭함) 로 전환된다. 합성 가스 (또는 신가스) 는 이후에 하나 이상의 단계로 적합한 촉매 상에서 승온 및 압력에서 메탄 내지 200 개 이하의 탄소 원자를 포함하는 고분자중량 분자 범위의 파라핀성 화합물, 또는 특정한 상황 하에 훨씬 더 중질로 전환된다. 본 발명은 촉매, 상기 촉매의 제조 방법에 관한 것이다. 본 발명은 추가로 상기 방법에 의해 수득가능한 촉매에 관한 것이다. 본 발명은 추가로 상기 촉매를 포함하는 다관형 반응기에 관한 것이다. The Fischer-Tropsch process can be used for the conversion of hydrocarbonaceous feedstocks to conventional liquid and/or solid hydrocarbons. The feedstock (eg natural gas, by-gas and/or coal bed methane, coal) is converted in a first step into a mixture of hydrogen and carbon monoxide, which mixture is often referred to as syngas or syngas. Syngas (or syngas) is then converted in one or more steps at elevated temperature and pressure over a suitable catalyst to paraffinic compounds ranging from methane to high molecular weight molecules containing up to 200 carbon atoms, or even heavier under certain circumstances. do. The present invention relates to a catalyst and a method for preparing the catalyst. The present invention further relates to a catalyst obtainable by said process. The present invention further relates to a shell-and-tube reactor comprising said catalyst.

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27-05-2008 дата публикации

Filtration system for slurry hydrocarbon synthesis process using both small and large pore filter elements

Номер: US7378452B2
Принадлежит: ExxonMobil Research and Engineering Co

A method for separating and filtering solid particles from a hydrocarbon slurry liquid includes two or more filter sections in fluid communication with the hydrocarbon slurry. At least one filter section is comprised of one or more filter elements having a mean pore size of less than 10 microns, and at least one other section is comprised of one or more filter elements having a mean pore size of 10 microns or greater. The small pore filter (less than 10 microns) will exclude all or substantially all of the smaller catalyst fines produced by catalyst particle attrition. The liquid product removed from the small pore filters will be substantially free of particulates. The large pore filters (10 microns or greater) will exclude larger catalyst particles, but will allow the smaller fines to pass. The liquid product removed from the large pore filters will contain the fines generated from catalyst particle attrition.

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12-03-2008 дата публикации

源自气态反应物的液态产物以及可选的气态产物的制造

Номер: CN101142015A
Принадлежит: Sasol Technology Pty Ltd

本发明一种用于由气态反应物制造液态产物并可选地制造气态产物的方法,所述方法包括:将处于低水平高度的气态反应物进给到竖直延伸的料浆床中,该料浆床容纳悬浮在悬浮液中的固体颗粒,并且该料浆床围绕多个竖直延伸的封套式管道定位,每个所述封套式管道包括内管道以及外管道或者封套管道,在所述内管道和所述外管道之间限定封套空间,所述料浆床也位于所述内管道内部。随着所述气态反应物向上经过所述料浆床,允许所述气态反应物进行放热反应,从而形成液态产物,并可选地形成气态产物,并且随着所述液态产物与所述悬浮液形成在一起,还形成所述料浆床的液相,因此,在所述封套式管道外部和所述内管道内部发生反应。使冷却介质经过所述封套式管道的封套空间,从而从所述料浆床去除反应热。

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28-12-2018 дата публикации

合成气合成低碳烯烃的催化剂体系

Номер: CN109092316A

本发明涉及合成气合成低碳烯烃的催化剂体系,主要解决现有技术中低碳烯烃选择性低的问题。本发明采用合成气合成低碳烯烃的催化剂体系,包括以下组份:1)n质量份的活性组分,所述活性组分包括以原子比计,化学式如下的组合物:Fe 100 Mo a Cr b Cs c O x ;a的取值范围为50.0~250.0;b的取值范围为5.0~20.0;c的取值范围为1.0~9.5;x为满足催化剂中各元素化合价所需的氧原子总数;2)1质量份惰性组份:所述惰性组份包括选自SiO 2 、Al 2 O 3 、分子筛、ZrO 2 和TiO 2 中的至少一种;n大于0且90以下的技术方案较好的解决了上述问题,适用于合成气合成低碳烯烃的工业生产。

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13-02-2018 дата публикации

浆态床钴基费托合成催化剂离线再生方法及其装置

Номер: CN107684932A

本发明公开了一种浆态床钴基费托合成催化剂再生方法及其装置,方法包括以下步骤:1)气液分离和过滤处理;2)重质油分离处理和升温气提脱除碳氢化合物;3)升温氧化处理,升温氧化终了温度为300~400℃;4)升温还原处理,升温还原终了温度为300~400℃;5)将还原后的催化剂从流化床反应器转入配浆罐中,用重质油进行配浆。本发明中,重质油分离、升温气提脱除碳氢化合物、氧化及还原处理均在同一台流化床反应器内完成,设备投资成本低,整个再生过程中完全不涉及机械搅拌,无需进行催化剂的转移,降低了催化剂的损耗和磨损,再生效率高,工艺过程简单易于控制,操作简便。

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15-07-2015 дата публикации

烃的制造方法

Номер: CN103562350B
Автор: 新宫英树

本发明的烃的制造方法包括下述工序:合成工序,在该工序中,使用保持包含催化剂颗粒和液体烃的浆料、在上部具有气相部的气泡塔型浆料床反应器,并且利用费-托合成反应来合成烃;取出工序,在该工序中,使浆料在配置于反应器的内部和/或外部的过滤器中流动,从而使重质液体烃分离,取出重质液体烃;反冲洗工序,在该工序中,使液体烃沿着与浆料的流动方向相反的方向在过滤器中流动,使催化剂颗粒返回反应器内;和冷却-气液分离工序,在该工序中,将从气相部排出的烃冷却,并且将冷凝的轻质液体烃从气体成分中分离并回收。在反冲洗工序中流动的液体烃包含在冷却-气液分离工序中得到的轻质液体烃。

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02-12-2015 дата публикации

For being produced the method for at least one product in slurry bed system by least one gaseous reactant

Номер: CN103596674B
Принадлежит: Sasol Technology Pty Ltd

一种用于由至少一种气态反应物产生至少一种产物的方法,其包括将作为气态进料(59)或作为气态进料(59)的一部分的气态反应物以至少0.5m/s的入口表观气体速度供给至容器(12),使得气态反应物可通过浆态床(70)向上鼓泡,该容器容纳悬浮在悬浮液中的固体催化剂颗粒的扩展浆态床(70)。浆态床(70)具有的催化剂负载量以体积计算小于脱气浆液的14%;当气态反应物通过浆态床(70)向上鼓泡时,允许气态反应物在高于大气压力的压力下催化式地反应,以产生至少一种产物。产物和任何未反应的气态反应物从容器(12)中被排出。

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03-11-2017 дата публикации

It is a kind of to prepare catalyst of mixed alcohol and its preparation method and application for synthesis gas

Номер: CN107308950A

本发明公开了一种用于合成气制备混合醇的催化剂及其制备方法和应用,所述催化剂包括含Co的金属氧化物、含Cu的金属复合氧化物和第一载体,含Co的金属氧化物与含铜的金属复合氧化物的重量百分比为0.1~10:1,第一载体重量占催化剂总质量的5~50%。本发明的催化剂运用于浆态床反应器中可将合成气直接转化为混合醇,CO单程转化率为10~60%,总醇选择性为30~50 C%,甲烷选择性低于10 C%,C 2+ OH占到90%以上。由于该催化剂制备方法简单、易于重复、稳定性好,目标产物选择性高,具有潜在的工业应用前景。

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14-02-2012 дата публикации

Method and system for handling slurries of varying liquid rates and solids content

Номер: US8114915B2
Принадлежит: ExxonMobil Research and Engineering Co

A method and system for collecting a plurality of slurries containing solid particles of varying particle size distribution and amount and performing a classification and separation on the slurries is provided whereby a fines-rich stream and a stream containing substantially coarse particles is obtained. The method and system includes separating the fines from the slurry liquid and thickening the separated coarse particles in a settling zone for subsequent use.

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23-08-2006 дата публикации

Process for separating a catalyst from a liquid

Номер: CN1822896A
Принадлежит: Sastech Pty Ltd

将气体反应物(18)送入固体催化剂粒子在液体中的浆料床(14)。反应物随着它们向上穿过浆料床而反应,从而形成液体和气体产物。在第一过滤级(30)中,液体产物穿过具有控制尺寸为x微米的滤孔的过滤介质,从而除去大于x微米的较大催化剂粒子。对包含近尺寸和细催化剂粒子的第一滤液进行第二过滤(64),除去近尺寸粒子。在过滤介质上形成催化剂粒子滤饼。中断液体产物穿过过滤介质,并使第二滤液反向穿过而对过滤介质进行回洗,从过滤介质上除掉滤饼。

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17-11-2009 дата публикации

Design of slurry bubble column reactors: novel technique for optimum catalyst size selection contractual origin of the invention

Номер: US7619011B1
Принадлежит: US Department of Energy

A method for determining optimum catalyst particle size for a gas-solid, liquid-solid, or gas-liquid-solid fluidized bed reactor such as a slurry bubble column reactor (SBCR) for converting synthesis gas into liquid fuels considers the complete granular temperature balance based on the kinetic theory of granular flow, the effect of a volumetric mass transfer coefficient between the liquid and the gas, and the water gas shift reaction. The granular temperature of the catalyst particles representing the kinetic energy of the catalyst particles is measured and the volumetric mass transfer coefficient between the gas and liquid phases is calculated using the granular temperature. Catalyst particle size is varied from 20 μm to 120 μm and a maximum mass transfer coefficient corresponding to optimum liquid hydrocarbon fuel production is determined. Optimum catalyst particle size for maximum methanol production in a SBCR was determined to be in the range of 60-70 μm.

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10-06-2010 дата публикации

Method and system for handling slurries of varying liquid rates and solids content

Номер: US20100144906A1
Принадлежит: ExxonMobil Research and Engineering Co

A method and system for collecting a plurality of slurries containing solid particles of varying particle size distribution and amount and performing a classification and separation on the slurries is provided whereby a fines-rich stream and a stream containing substantially coarse particles is obtained. The method and system includes separating the fines from the slurry liquid and thickening the separated coarse particles in a settling zone for subsequent use.

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08-01-2015 дата публикации

Torrefaccion reacting apparatus using biomass

Номер: KR101479906B1
Принадлежит: 삼양에코너지 주식회사

본 발명은 바이오매스를 이용한 반탄화 연료생산장치 및 이를 이용한 반탄화 연료를 생산하는 방법에 관한 것으로, 더욱 상세하게는 고체 상태인 바이오매스를 이용하여 기체 상태인 수소, 일산화탄소, 메탄 등의 합성가스로 생산하는 가스화반응장치를 이용하여 반탄화 연료를 생산하는 바이오매스를 이용한 반탄화 연료생산장치로 이용하는 기술에 관한 것이다. 상기의 목적을 달성하기 위한 기술적 사상으로서의 본 발명은, 상측으로부터 목질계 바이오매스(biomass)를 투입하여 무산소 상태에서 가열하여 반탄화 연료를 생산하는 것으로, 상기 바이오매스가 채워진 내부 공간의 상측으로부터 건조영역(drying zone), 열분해영역(pyrolysis zone), 산화영역(combustion zone), 환원영역(reduction zone)이 순차적으로 형성된 반응기; 상기 반응기의 하부측에 형성되는 가스배출구에 구비되고, 상기 환원영역으로부터 배출되는 상기 합성가스와 외부로부터 공급되는 물을 상호 교차 유동시켜 열교환시키는 열교환유닛;을 포함하여 구성되어, 상기 반응기로 투입되는 목질계 바이오매스를 무산소 상태에서 가열하열 반탄화 연료를 생산할 수 있다.

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23-06-2010 дата публикации

Apparatus and method for conducting a Fischer-Tropsch systhesis reaction.

Номер: GB2466315A
Принадлежит: GTL F1 AG

A system for a Fischer-Tropsch synthesis using a three-phase reactor (11) in which a primary filter (21) removes coarse catalyst particles from the product and in which catalyst fines are removed in a secondary filter (14). Some or all portion of the product wax from the secondary filter is recycled back to the reactor (11), either as a back flush medium for the primary filter (21) or directly to the slurry in the reactor (11), whereby removal of catalyst fines is rendered independent of the rate of wax production. The system can also comprise a degasser (13) between the primary filter (21) and the secondary filter (14).

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26-05-2015 дата публикации

Slurry bubble column reactor

Номер: US9039980B2
Принадлежит: GTLFI AG

A slurry bubble column reactor with a gas distribution arrangement comprising an upper sparger, a lower sparger, and an open-ended tube. Gas from the lower sparger enters the tube and lowers the density of slurry in the tube. The difference in slurry density causes the slurry in the tube to rise, causing slurry outside the tube to move down, maintaining circulation and flushing catalyst from the vessel wall.

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09-01-2013 дата публикации

Apparatus and method for conducting a Fischer-Tropsch synthesis reaction

Номер: GB2466315B
Принадлежит: GTL F1 AG

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08-03-2016 дата публикации

Apparatus and method for conducting a fischer-tropsch synthesis reaction

Номер: US9278891B2
Принадлежит: GTL F1 AG

A system for a Fischer-Tropsch synthesis using a three-phase reactor in which a primary filter removes coarse catalyst particles from the product and in which catalyst fines are removed in a secondary filter. Some or all portion of the product wax from the secondary filter can be recycled back to the reactor, either as a back flush medium for the primary filter or directly to the slurry in the reactor, whereby removal of catalyst fines is rendered independent of the rate of wax production.

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29-05-2008 дата публикации

Process for the regeneration of a fischer tropsch catalyst

Номер: WO2008061861A1
Принадлежит: EVONIK DEGUSSA GmbH

The invention relates to a process for the regeneration of a deactivated wax covered Fischer-Tropsch catalyst, a pumpable suspension of deactivated catalyst being injected into a hot gas stream and the regenerated catalyst then being separated off from the gas stream, optionally further treated by calcination and/or reduction.

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13-04-2021 дата публикации

Loading of catalyst into bubble column for fischer-tropsch synthesis

Номер: CN108472614B
Принадлежит: IFP Energies Nouvelles IFPEN

一种将催化剂装载至包括分离环路(21)的反应器(40)中的方法,包括以下步骤:a)采用溶剂S1填充反应器(40);b)采用所述溶剂S1填充分离环路(21);c)使所述溶剂S1在合成反应器(40)和分离环路(21)中循环;d)在低于或等于100℃的温度下加热所述反应器(40);e)在反应器(40)的底部注入惰性气体;f)在容器(30)中混合所述催化剂和溶剂S2从而获得液/固混合物;g)提高容器(30)中的压力,然后将所述液/固混合物送至反应器(40);h)除去所述溶剂S1和/或S2。

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29-10-2019 дата публикации

The method of paste state bed reactor and F- T synthesis

Номер: CN110385089A

本发明涉及烃类合成领域,具体提供了一种浆态床反应器和费托合成方法,该反应器包括:自下而上设置的反应器入口段、气体分布器、反应段和气液固分离段,在所述反应段内部中下方设置有与反应器的液体产物流出口连通的固液分离器,在所述反应段内部中上方设置有多个脱气集液导流部件,所述脱气集液导流部件包括自上而下连通的漏斗状开口段和导流管段。与现有技术相比,本发明的反应器应用于气液固三相反应,能够明显改善催化剂的性能,且催化剂的磨损消耗明显减小。

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10-07-2015 дата публикации

Slurry bubble column reactor

Номер: KR101535058B1
Принадлежит: 한국에너지기술연구원

The present invention relates to a slurry bubble column reactor using coal synthetic gas, which reduces filtering burden of a filtering means, increases reaction efficiency by maintaining the uniformly dispersing status of a catalyst in a main body of a reactor, and enables to induce a Fischer-Tropsch reaction, and additionally wax creaking or isomerization reactions. According to the present invention, the reactor comprises: a dispersion means and a re-dispersion means installed in the main body of the reactor to disperse and re-disperse the introduced synthetic gas; a porous packet bed installed in an upper part of the main body of the reactor which is an upper part of the re-dispersion means positioned at the uppermost, and suppressing the catalyst to be moved toward the upper part; and a filtering means disposed in the upper part of the packet bed of the main body of the reactor and made to be reacted in the slurry in order to filter the generated synthetic fuel only and outflow the same to the outside. The reactor of present invention may further comprise a draft tube installed in the main body of the reactor to circulate the slurry.

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02-11-2022 дата публикации

Systems and processes for upgrading crude oil directly to hydrogen and chemicals

Номер: KR20220147128A
Принадлежит: 사우디 아라비안 오일 컴퍼니

유입 탄화수소 스트림을 경질 분획 및 디젤 비점 온도 범위 물질을 포함하는 중질 분획으로 분리하는 단계; 경질 분획으로부터 H 2 및 CO를 포함하는 합성가스를 생산하는 단계; 생산된 CO를 반응시키는 단계; 중질 분획으로부터, CO 2 , 중합체 등급 에틸렌, 중합체 등급 프로필렌, C 4 화합물, 분해 생산물, 경질 사이클 오일, 및 중질 사이클 오일을 분리하여 생산하는 단계; 중질 분획으로부터 생산된 CO 2 를 수집 및 정제하는 단계; C 4 화합물을 가공하여 올레핀계 올리고머레이트 및 파라핀계 라피네이트를 생산하는 단계; 분해 생산물을 분리하는 단계; 경질 컷 나프타 스트림을 올리고머화하는 단계; 방향족 스트림을 수소처리하는 단계; 경질 사이클 오일을 수소화분해하여 단일방향족 생산물 스트림을 생산하는 단계; 중질 사이클 오일을 가스화하는 단계; 중질 사이클 오일을 가스화하여 생산된 CO를 반응시키는 단계; CO 2 를 수집 및 정제하는 단계; 및 생산된 방향족 화합물을 벤젠 및 파라-자일렌으로 가공 및 분리하는 단계를 포함하는, 직접 원유를 수소 및 화학 물질로 업그레이드하기 위한 시스템 및 방법.

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14-11-2007 дата публикации

Method for temporarily interrupting a fischer-tropsch reaction in a three-phase bed reactor

Номер: CN101072634A
Принадлежит: Eni Spa, IFP Energies Nouvelles IFPEN

本发明涉及临时中断在三相反应区中对原料进行的费-托反应的方法,该原料至少含有一氧化碳和氢气,该三相反应区包括液相、气相和保持悬浮状的固体催化剂颗粒,所述的方法包括中断反应步骤a)和重新开始所述反应步骤b),在该方法中固体催化剂颗粒在反应区中保持悬浮状;a)在中断该反应步骤期间,停止供给原料;和建立抑制气层,该抑制气层含有1体积%以下的氢和至少5体积%至少一种选自一氧化碳和水的抑制化合物;和b)在反应重新开始步骤期间:在反应区中,建立氢含量至少20体积%的活化气层;和重新开始供给原料。

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26-04-2022 дата публикации

Fluidized bed process and catalyst system for fischer-tropsch conversion

Номер: CN112752829B
Принадлежит: National Institute Of Gas Technology

公开了用于进行费‑托(FT)合成以产生C 4 + 烃,例如汽油沸程烃和/或柴油沸程烃的工艺和催化剂体系。有利地,本文描述的催化剂体系对于蜡的原位加氢异构化和/或加氢裂化具有另外的活性(除了FT活性之外),所述蜡根据从FT合成反应获得的烃的分布而产生。这不仅提高了可用于运输燃料的烃(例如,C 4‑19 烃)的收率,而且还允许可选择的反应器类型,诸如流化床反应器。

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19-02-2014 дата публикации

Process for producing at least one product from at least one gaseous reactant in a slurry bed

Номер: CN103596674A
Принадлежит: Sasol Technology Pty Ltd

一种用于由至少一种气态反应物产生至少一种产物的方法,其包括将作为气态进料(59)或作为气态进料(59)的一部分的气态反应物以至少0.5m/s的入口表观气体速度供给至容器(12),使得气态反应物可通过浆态床(70)向上鼓泡,该容器容纳悬浮在悬浮液中的固体催化剂颗粒的扩展浆态床(70)。浆态床(70)具有的催化剂负载量以体积计算小于脱气浆液的14%;当气态反应物通过浆态床(70)向上鼓泡时,允许气态反应物在高于大气压力的压力下催化式地反应,以产生至少一种产物。产物和任何未反应的气态反应物从容器(12)中被排出。

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17-05-2005 дата публикации

Method for gas—solid contacting in a bubbling fluidized bed reactor

Номер: US6894183B2

The present invention relates to a method for gas-solid contacting in a bubbling fluidized bed reactor by: (a) introducing into a reactor with bed length to bed diameter ratio below about 5.0, a primary gas consisting essentially of reactant(s) of the reaction to be carried out in the bed of solid particles through a primary gas distributor located at the reactor bottom at a superficial gas velocity U p , which is very close or equivalent to the minimum fluidization velocity U mf , required for achieving the incipient fluidization of the solid particles in the bed to obtain an emulsion phase consisting essentially of the solid particles and the primary gas with little or no formation of gas bubbles to achieve incipient fluidization or liquid-like behavior of fluidizable solid particles; (b) forming gas bubbles in the incipiently fluidized bed by introducing through a secondary gas distributor located immediately above the primary gas distributor a secondary gas, selected from one of the reactants which is used in excess of that required for the reaction stoichiometry, steam, an inert or a mixture of two or more thereof at a superficial gas velocity, U s , which is related to the superficial velocity of the primary gas such that a ratio of the superficial velocity of the secondary gas to the superficial velocity of the primary gas U s /U p , is in the range from about 0.5 to about 10.0, preferably from about 1 to about 5.

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13-12-2012 дата публикации

Fischer-tropsch bubble column reactor feasible multi reaction

Номер: KR101211376B1
Принадлежит: 한국에너지기술연구원

The present invention relates to a FT bubble column reactor capable of a complex reaction, for this purpose is provided with a first dispersion means and a second dispersion means for partitioning the interior of the bubble tower reactor body so that two complex reaction zones can be formed, At the top of the first dispersing means a first reaction zone is formed which reacts with the Fe-catalyst and Fischer-Tropsch, and at the top of the second dispersing means the Fe / Co-catalyst or Co-catalyst and Fischer- A second reaction zone for the reaction of Fischer-Tropsch is formed to have different reaction conditions in a single bubble column reactor body.

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10-01-2020 дата публикации

LOADING THE CATALYST IN A BARBOTAGE COLUMN FOR FISHER-TROPHE SYNTHESIS

Номер: RU2018122962A
Принадлежит: Ифп Энержи Нувелль

РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2018 122 962 A (51) МПК C10G 2/00 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ЗАЯВКА НА ИЗОБРЕТЕНИЕ (21)(22) Заявка: 2018122962, 08.11.2016 (71) Заявитель(и): ИФП ЭНЕРЖИ НУВЕЛЛЬ (FR) Приоритет(ы): (30) Конвенционный приоритет: 08.12.2015 FR 1562031 (85) Дата начала рассмотрения заявки PCT на национальной фазе: 09.07.2018 (86) Заявка PCT: (87) Публикация заявки PCT: WO 2017/097525 (15.06.2017) A Адрес для переписки: 129090, Москва, ул. Б.Спасская, 25, строение 3, ООО "Юридическая фирма Городисский и Партнеры" R U (57) Формула изобретения 1. Способ загрузки катализатора в реактор синтеза (40) типа барботажной колонны, содержащей контур разделения (21), причем указанный способ включает следующие стадии: a) заполняют по меньшей мере части реактора синтеза (40) растворителем S1; b) заполняют по меньшей мере части контура разделения (21) указанного реактора синтеза (40) указанным растворителем S1; c) указанный растворитель S1 подвергают циркуляции от реактора синтеза (40) к контуру разделения (21) и от контура разделения к реактору синтеза (40); d) нагревают реактора (40) до температуры меньше или равной 100°C; e) вводят в нижнюю часть реактора синтеза (40) инертного газа и повышают давление в реакторе синтеза (40), до достижения абсолютного давления в интервале от 0,1 до 0,6 МПа; f) смешивают указанный катализатор с растворителем S2 в резервуаре (30), с получением смеси твердое/жидкое; g) повышают давление в резервуаре (30) до давления, по меньшей мере на 0,2 МПа выше давления в реакторе синтеза (40), затем направляют смеси твердое/жидкое, полученной на стадии f), в реактор синтеза (40); h) отводят по меньшей мере части указанного растворителя S1 и/или S2, Стр.: 1 A 2 0 1 8 1 2 2 9 6 2 (54) ЗАГРУЗКА КАТАЛИЗАТОРА В БАРБОТАЖНУЮ КОЛОННУ ДЛЯ СИНТЕЗА ФИШЕРАТРОПША 2 0 1 8 1 2 2 9 6 2 EP 2016/076938 (08.11.2016) R U (43) Дата публикации заявки: 10.01.2020 Бюл. № 1 (72) Автор(ы): ДЕГРАНЖ Режи (FR), ЭРО Жан-Филипп ( ...

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16-03-2018 дата публикации

Injection of additive to synthesis plant of hydrocarbons from synthesis gas, allowing to control and maintain uniform catalyst concentration

Номер: RU2647580C2

FIELD: chemistry; technological processes. SUBSTANCE: invention relates to process for synthesis of hydrocarbons from synthesis gas containing raw materials, in which solid Fischer-Tropsch catalyst is used in a three-phase reaction section, characterized in that said catalyst is maintained in suspension in the liquid phase by circulating the gas phase from the bottom upward in said reaction section. Wherein, in order to control and maintain a uniform concentration of catalyst particles in the reaction section, the following steps are carried out: (a) for any i that is in the range from 1 to n-1, where i is a natural integer from 1 to n-1, where n is the number of pressure measurement points along the longitudinal axis of the reactor and is at least 3, wherein measurement point 1 is the lowest point and measurement point n is the highest point in said reaction section, differential pressures are measured ΔP i between two consecutive pressure measurement points, spaced apart from each other by Δh i , and calculate the head loss per meter ΔG i = ΔP i / Δh i , (b) for each head loss per meter ΔG i in said catalyst suspension in the liquid phase, a value corresponding to the difference between two consecutive head loss per meter divided by their average value (ΔG i+1 – ΔG i )/((ΔG i+1 + ΔG i )/2 (c) if at least one of the values calculated in step (b) is greater than or equal to 5 %, inject at least one additive, containing at least one silicone polymer at least on the bottom of said reaction section. EFFECT: use of invention allows to improve hydrodynamics of the gas/liquid/solid phase flow in the reaction section. 9 cl, 1 dwg, 1 ex, 2 tbl РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 647 580 C2 (51) МПК C10G 2/00 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ (52) СПК C10G 2/32 (2017.08); C10G 2/344 (2017.08) (21)(22) Заявка: 2013153933, 04.12.2013 (24) Дата начала отсчета срока действия патента: Дата регистрации: 16.03. ...

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10-12-2014 дата публикации

IMPLEMENTATION OF METHODS USING A CATALYST, WHICH IS INACTIVATED IN TIME

Номер: RU2013119829A

1. Способ реализации синтеза углеводородов путем каталитического превращения одного или более реагентов в один или более продуктов в реакторе с псевдоожиженным слоем и катализатором, который инактивируется во времени, включающий в ходе каталитического циклана стадии A постепенное повышение рабочей температуры в реакторе для противодействия отрицательному влиянию инактивации катализатора на скорость превращения указанных одного или более реагентов, причем рабочая температура не превышает заданную максимальную рабочую температуру;на стадии B добавление катализатора, обладающего свойством увеличивать скорость превращения указанных одного или более реагентов, в реактор и снижение рабочей температуры реактора по меньшей мере для частичного противодействия влиянию добавленного катализатора на скорость превращения указанных одного или более реагентов, причем рабочая температура остается выше заданной минимальной рабочей температуры; иповторение стадий A и B до конца каталитического цикла или до конца производственного цикла2. Способ по п.1, в котором реактор с псевдоожиженным слоем представляет собой трехфазный суспензионный барботажный колонный реактор, содержащий наряду с газовой и твердой фазами непрерывную жидкую фазу.3. Способ по п.1, в котором реактор с псевдоожиженным слоем представляет собой двухфазный реактор с псевдоожиженным слоем и газовой и твердой фазами, но без непрерывной жидкой фазы.4. Способ по п.1, который реализуют так, что производительность реактора во время стабильной работы в ходе каталитического цикла остается, по существу, постоянной, причем скорость подачи указанных одного РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (51) МПК B01J 8/00 (11) (13) 2013 119 829 A (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ЗАЯВКА НА ИЗОБРЕТЕНИЕ (21)(22) Заявка: 2013119829/05, 10.10.2011 (71) Заявитель(и): СЭСОЛ ТЕКНОЛОДЖИ (ПРОПРИЕТЕРИ) ЛИМИТЕД (ZA) Приоритет(ы): (30) Конвенционный приоритет: 27.10.2010 US 61/407,067; 27.10.2010 ZA 2010/07687 (72) Автор(ы): ...

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30-09-2010 дата публикации

Method and system for synthesizing liquid hydrocarbon compounds

Номер: CA2755591A1
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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01-08-2018 дата публикации

Method for stopping operating three-phase bubble column reactor of suspension type

Номер: RU2663166C1

FIELD: technological processes.SUBSTANCE: invention relates to a method for stopping a working three-phase bubble column reactor of a suspension type. Method for stopping a column including downwardly directed gas distribution nozzles immersed in a major portion of a slurry of solid particulate material suspended in a slurry fluid contained within a reactor vessel in fluid communication with a gas supply line through which gas is supplied to the gas distribution nozzles, by means of which the gas is injected down into the main part of the slurry, and having exhaust ports that are at the same height, provides for a sudden stop of the gas flow from the gas supply line to the gas distribution nozzles by activating the high-speed valve on the gas supply line to shut off the gas supply line to the gas distribution nozzles, so as to keep the gas in the gas distribution nozzles to prevent the suspension from entering the gas distributing nozzles, while the high-speed valve is characterized by a response time of 1 to 5 seconds from the moment of activation until the valve is completely closed.EFFECT: invention provides an effective stopping of the reactor tower in which the suspension is prevented from entering the gas distributor and the flow of gas in the nozzles is not required.13 cl, 1 dwg РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 663 166 C1 (51) МПК B01J 8/18 (2006.01) B01J 8/22 (2006.01) B01J 4/00 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ (52) СПК B01J 8/18 (2018.05); B01J 8/22 (2018.05); B01J 4/00 (2018.05) (21)(22) Заявка: 2016127233, 04.12.2014 (24) Дата начала отсчета срока действия патента: (73) Патентообладатель(и): САСОЛ ТЭКНОЛОДЖИ ПРОПРИЭТЭРИ ЛИМИТЭД (ZA) Дата регистрации: 01.08.2018 (56) Список документов, цитированных в отчете о поиске: WO 2005/094979 A1, 13.10.2005. US 11.12.2013 ZA 2013/09350 2012/0177539 A1, 12.07.2012. WO 2005/026293 A1, 24.03.2005. RU 2365407 C2, 27.08.2009. (45) Опубликовано: 01. ...

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04-10-2022 дата публикации

System and process for direct upgrading of crude oil to hydrogen and chemicals

Номер: CN115151625A
Принадлежит: Saudi Arabian Oil Co

用于直接将原油提质为氢气和化学品的系统和工艺,包括将入口烃流分离成轻馏分和包含柴油沸点温度范围材料的重馏分;由轻馏分产生包含H 2 和CO的合成气;使产生的CO反应;从重馏分中产生并分离CO 2 、聚合级乙烯、聚合级丙烯、C 4 化合物、裂化产物、轻循环油和重循环油;收集和纯化重馏分产生的CO 2 ;加工C 4 化合物以产生烯烃低聚物和链烷烃残余液;分离裂化产物;低聚轻馏分(light cut)石脑油流;加氢处理芳烃流;对轻循环油进行加氢裂化以产生单芳烃产物流;气化重循环油;使重循环油气化产生的CO反应;收集和纯化CO 2 ;将产生的芳烃化合物加工并分离成苯和对二甲苯。

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22-10-2004 дата публикации

HIGH PRESSURE FISCHER-TROPSCH SYNTHESIS PROCESS USING OPTIMIZED REFRIGERATION FLUID

Номер: FR2843961B1

The process takes place in a reaction zone (1) containing a synthesis gas and a catalyst in a fluidized bed with a three-phase fluidization sequence, with a coolant fluid circulated through at least one internal heat exchange zone (2). The coolant fluid, selected from ethanol, methanol or a mixture of these, is fed into the heat exchange zone at a temperature close to its boiling point at the pressure of the reaction medium, i.e. 10-70degreesC, preferably 15-60degreesC, below the temperature of the reaction medium. The pressure of the reaction medium is 30-50 bars, and its temperature is 220-240degreesC.

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29-06-1984 дата публикации

Patent FR2509718B1

Номер: FR2509718B1
Автор: [UNK]

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12-01-2007 дата публикации

PROCESS FOR PROVISIONALLY INTERRUPTING A FISCHER-TROPSCH TYPE REACTION IN A THREE-PHASE BED REACTOR

Номер: FR2878845B1
Принадлежит: Eni Spa, IFP Energies Nouvelles IFPEN

A process for temporarily interrupting a Fischer-Tropsch type reaction carried out on a feed comprising at least carbon monoxide and hydrogen is carried out in a three-phase reaction zone comprising a liquid phase, a gas phase and solid catalyst particles maintained in suspension, said process comprising a step a) for interrupting the reaction and a step b) for restarting said reaction, during which the solid catalyst particles are maintained in suspension in the reaction zone; a) during the step for interrupting the reaction, supply of the feed is stopped, and a blanket of an inhibiting gas comprising less than 1% by volume of hydrogen and at least 5% by volume of at least one inhibiting compound selected from the group formed by carbon monoxide and water is established; and b) during the reaction restart step, in the reaction zone, a blanket of an activating gas with a hydrogen content of at least 20% by volume is established and supply of the feed is restarted.

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19-06-2013 дата публикации

Liquid fuel synthesis system

Номер: CN101432396B
Принадлежит: Nippon Steel Engineering Co Ltd

本发明的液体燃料合成系统(1)具备:对碳氢化合物原料进行重整,生成以一氧化碳气体及氢气为主成分的合成气的重整器(12);回收从重整器(12)排出的合成气的排热的排热锅炉(14);使合成气反应,进行液体燃料的合成反应的气泡塔式反应器(30);设在气泡塔式反应器(30)上,用于回收液体燃料的合成反应的反应热的导热管(32);利用从排热锅炉(14)或导热管(32)产生的水蒸气进行规定的热处理的热处理装置(24、40、70)。

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09-06-2017 дата публикации

LOADING A CATALYST IN A BUBBLE COLUMN FOR THE FISCHER-TROPSCH SYNTHESIS

Номер: FR3044565A1
Принадлежит: IFP Energies Nouvelles IFPEN

Procédé de chargement d'un catalyseur dans un réacteur (40) comprenant une boucle de séparation (21) comprenant les étapes suivantes : a) on remplit le réacteur (40) avec un solvant S1 ; b) on remplit la boucle de séparation (21) avec ledit solvant S1 ; c) on fait circuler ledit solvant S1 dans le réacteur de synthèse (40) et la boucle de séparation (21) ; d) on chauffe le réacteur (40) à une température inférieure ou égale à 100°C ; e) on injecte en fond du réacteur (40) un gaz inerte ; f) on mélange ledit catalyseur avec un solvant S2 dans une capacité (30) pour obtenir un mélange liquide/solide ; g) on augmente la pression dans la capacité (30) puis on envoie le mélange liquide/solide vers le réacteur (40) ; h) on soutire ledit solvant S1 et/ou S2. A method of loading a catalyst into a reactor (40) comprising a separation loop (21) comprising the following steps: a) filling the reactor (40) with a solvent S1; b) filling the separation loop (21) with said solvent S1; c) circulating said solvent S1 in the synthesis reactor (40) and the separation loop (21); d) heating the reactor (40) to a temperature of less than or equal to 100 ° C; e) injecting at the bottom of the reactor (40) an inert gas; f) mixing said catalyst with a solvent S2 in a capacity (30) to obtain a liquid / solid mixture; g) increasing the pressure in the capacity (30) and then sending the liquid / solid mixture to the reactor (40); h) withdrawing said solvent S1 and / or S2.

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19-03-2009 дата публикации

System and method for catalyst loading/mixing

Номер: CA2699784A1
Принадлежит: Individual

A catalyst loading system comprising: a vessel comprising at least one gas distribution nozzle at or near the bottom of the vessel, a top fluid distributor located at or near the top of the vessel, a catalyst inlet through which catalyst is introduced into the vessel, a first contact point at which catalyst introduced into the vessel first contacts the contents of the vessel, and a discharge outlet whereby catalyst exits the vessel. Methods of preparing catalyst slurry for introduction into a downstream reactor or in-situ activation within the vessel utilizing the catalyst loading system are also disclosed.

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16-07-2014 дата публикации

Apparatus for recycling light oil and system for manufacturing synthetic fuel using the same

Номер: KR101418910B1
Принадлежит: 한국에너지기술연구원

본 발명은 경유 재순환 장치 및 그를 갖는 합성연료 제조 시스템에 관한 것으로, 슬러리 기포탑 반응기(slurry bubble column reactor; SBCR)에서 생성되는 경유를 재순환시켜 반응기로 안정적으로 공급하면서 경유의 유량을 정밀하게 제어하면서 공급하기 위한 것이다. 본 발명에 따른 합성연료 제조 시스템은 슬러리 기포탑 반응기와 경유 재순환 장치를 포함한다. 슬러리 기포탑 반응기는 피셔-트롭쉬(Fischer-Tropsch) 합성반응으로 탄화수소 화합물을 생성한다. 그리고 경유 재순환 장치는 슬러리 기포탑 반응기에서 배출되는 기체 생성물로부터 경유를 분리하고, 분리한 경유를 증발시켜 합성가스와 함께 슬러리 기포탑 반응기로 공급한다. BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a gas oil recycling apparatus and a synthetic fuel production system having the gas oil recycling apparatus, . The synthetic fuel production system according to the present invention comprises a slurry bubble column reactor and a gas oil recirculation device. The slurry bubble column reactor produces a hydrocarbon compound in a Fischer-Tropsch synthesis reaction. The gas oil recirculation system separates the light oil from the gaseous product discharged from the slurry bubble column reactor, evaporates the separated light oil and supplies it to the slurry bubble column reactor together with the syngas.

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27-01-2020 дата публикации

Patent RU2018122962A3

Номер: RU2018122962A3
Автор: [UNK]
Принадлежит: [UNK]

`7ВУ’” 2018122962`” АЗ Дата публикации: 27.01.2020 Форма № 18 ИЗ,ПМ-2011 Федеральная служба по интеллектуальной собственности Федеральное государственное бюджетное учреждение ж 5 «Федеральный институт промышленной собственности» (ФИПС) ОТЧЕТ О ПОИСКЕ 1. . ИДЕНТИФИКАЦИЯ ЗАЯВКИ Регистрационный номер Дата подачи 2018122962/04(036315) 08.11.2016 РСТ/ЕР2016/076938 08.11.2016 Приоритет установлен по дате: [ ] подачи заявки [ ] поступления дополнительных материалов от к ранее поданной заявке № [ ] приоритета по первоначальной заявке № из которой данная заявка выделена [ ] подачи первоначальной заявки № из которой данная заявка выделена [ ] подачи ранее поданной заявки № [Х] подачи первой(ых) заявки(ок) в государстве-участнике Парижской конвенции (31) Номер первой(ых) заявки(ок) (32) Дата подачи первой(ых) заявки(ок) (33) Код страны 1. 1562031 08.12.2015 ЕК Название изобретения (полезной модели): [Х] - как заявлено; [ ] - уточненное (см. Примечания) ЗАГРУЗКА КАТАЛИЗАТОРА В БАРБОТАЖНУЮ КОЛОННУ ДЛЯ СИНТЕЗА ФИШЕРА- ТРОПША Заявитель: ИФП ЭНЕРЖИ НУВЕЛЛЬ, ЕК 2. ЕДИНСТВО ИЗОБРЕТЕНИЯ [Х] соблюдено [ ] не соблюдено. Пояснения: см. Примечания 3. ФОРМУЛА ИЗОБРЕТЕНИЯ: [Х] приняты во внимание все пункты (см. Примечания) [ ] приняты во внимание следующие пункты: [ ] принята во внимание измененная формула изобретения (см. Примечания) 4. КЛАССИФИКАЦИЯ ОБЪЕКТА ИЗОБРЕТЕНИЯ (ПОЛЕЗНОЙ МОДЕЛИ) (Указываются индексы МПК и индикатор текущей версии) С10С 2/00 (2006.01) 5. ОБЛАСТЬ ПОИСКА 5.1 Проверенный минимум документации РСТ (указывается индексами МПК) С10С 2/00, ВО11 8/18, ВО} 8/22 5.2 Другая проверенная документация в той мере, в какой она включена в поисковые подборки: 5.3 Электронные базы данных, использованные при поиске (название базы, и если, возможно, поисковые термины): ЕАРАТТУ, Езрасепек, ]-Р]1а Рав Рабеагсв, КОРТО, ОЗРТО 6. ДОКУМЕНТЫ, ОТНОСЯЩИЕСЯ К ПРЕДМЕТУ ПОИСКА Кате- Наименование документа с указанием (где необходимо) частей, Относится к гория* относящихся к предмету поиска пункту ...

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03-09-2019 дата публикации

Catalyst

Номер: US10399061B2
Принадлежит: Shell Oil Co

The Fischer-Tropsch process can be used for the conversion of hydrocarbonaceous feed stocks into normally liquid and/or solid hydrocarbons. The feed stock (e.g. natural gas, associated gas and/or coal-bed methane, coal) is converted in a first step into a mixture of hydrogen and carbon monoxide (this mixture is often referred to as synthesis gas or syngas). The synthesis gas (or syngas) is then converted in one or more steps over a suitable catalyst at elevated temperature and pressure into paraffinic compounds ranging from methane to high molecular weight molecules comprising up to 200 carbon atoms, or, under particular circumstances, even more. The present invention relates to a catalyst, a method for manufacturing said catalyst. The present invention further relates to a catalyst obtainable by said method. The present invention further relates to a multi tubular reactor comprising said catalyst.

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10-04-2008 дата публикации

Method for operating a fluidized bed reactor

Номер: DE112006000625T5
Принадлежит: Sasol Technology Pty Ltd

Verfahren zum Betreiben eines Zwei-Phasen-Fluidbettreaktors, wobei das Verfahren umfasst: Zuführen auf einem niedrigen Pegel von wenigstens einem gasförmigen Reaktant in einen sich vertikal erstreckenden Fluidkörper aus Festpartikeln, wobei der Fluidkörper in wenigstens zwei sich vertikal erstreckenden Schächten in einer gemeinsamen Reaktorschale enthalten ist, wobei jeder Schacht in eine Vielzahl von sich vertikal erstreckenden Kanälen unterteilt ist, von denen wenigstens einige in einer Fluidkommunikation stehen, wobei der Fluidkörper in wenigstens einigen der Kanäle vorhanden ist, Zulassen, dass der gasförmige Reaktant reagiert, wenn er nach sich oben durch den Fluidkörper in wenigstens einigen Kanälen der Schächte bewegt, um ein gasförmiges Produkt zu bilden, Zulassen, dass sich das gasförmige Produkt und/oder der nicht reagierte gasförmige Reaktant von dem Fluidkörper in einem Kopfraum oberhalb des Fluidkörpers lösen, und Entfernen des gasförmigen Produkts und des nicht reagierten gasförmigen Reaktants, sofern vorhanden, aus dem Kopfraum. A method of operating a two-phase fluidized bed reactor, the method comprising: Feeding at a low level at least one gaseous reactant into a vertically extending solid particle body of fluid, the body of fluid being contained in at least two vertically extending wells in a common reactor shell, each well being divided into a plurality of vertically extending channels, at least some of which are in fluid communication, the fluid body being present in at least some of the channels, Allowing the gaseous reactant to react as it moves upwardly through the fluid body in at least some of the ducts of the wells to form a gaseous product, Allowing the gaseous product and / or the unreacted gaseous reactant to dissolve away from the fluid body in a head space above the fluid body, and Removing the gaseous product and the unreacted gaseous reactant, if present, from the headspace.

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24-12-2014 дата публикации

PROCESS FOR THE PRODUCTION OF AT LEAST ONE PRODUCT FROM AT LEAST ONE GASEOUS REAGENT IN A SUSPENSION BED

Номер: PE20141999A1
Принадлежит: Sasol Technology Propietary Ltd

REFERIDA A UN PROCESO PARA LA PRODUCCION DE UN PRODUCTO A PARTIR DE POR LO MENOS UN REACTIVO GASEOSO, EL CUAL COMPRENDE ALIMENTAR DICHO REACTIVO GASEOSO, COMO UNA ALIMENTACION GASEOSA O COMO PARTE DE UNA ALIMENTACION GASEOSA EN UN RECIPIENTE QUE SOSTIENE UN LECHO DE SUSPENSION EXPANDIDO DE PARTICULAS DE CATALIZADOR SOLIDO SUSPENDIDAS EN UN LIQUIDO DE SUSPENSION DE MODO QUE EL REACTIVO GASEOSO PUEDE BURBUJEAR EN FORMA ASCENDENTE A TRAVES DEL LECHO DE SUSPENSION, DONDE EL LECHO DE SUSPENSION TIENE UNA CARGA DE CATALIZADOR INFERIOR A 14% EN VOLUMEN DE SUSPENSION DESGASIFICADA, LUEGO HACER REACCIONAR DICHO REACTIVO GASEOSO EN FORMA CATALITICA A UNA PRESION SUPERIOR A LA PRESION ATMOSFERICA, A MEDIDA QUE EL REACTIVO GASEOSO BURBUJEA EN FORMA ASCENDENTE A TRAVES DEL LECHO DE SUSPENSION PARA PRODUCIR UN PRODUCTO, RETIRAR DICHO PRODUCTO Y CUALQUIER OTRO REACTIVO GASEOSO NO REACCIONADO, DEL RECIPIENTE REFERRING TO A PROCESS FOR THE PRODUCTION OF A PRODUCT FROM AT LEAST ONE GASEOUS REAGENT, WHICH INCLUDES FEEDING SAID GASEOUS REAGENT, AS A GASEOUS FEED OR AS PART OF A GASEOUS FEED IN A CONTAINER HOLDING A SUSPENDED MILK SOLID CATALYST PARTICLES SUSPENDED IN A SUSPENSION LIQUID SO THAT THE GASEOUS REAGENT CAN BUBBLE UPWARDS THROUGH THE SUSPENSION BED, WHERE THE SUSPENSION BED HAS A LOWER 14% SUSPENSION LIGHTING CATALYST CHARGE IN LOWER VOLUME SUSPENSION CATALYST. REACT SAID GASEOUS REAGENT IN A CATALYTICAL FORM AT A PRESSURE GREATER THAN ATMOSPHERIC PRESSURE, AS THE GASEOUS REAGENT BUBBLES UPWARDS THROUGH THE SUSPENSION BED TO PRODUCE A PRODUCT, REMOVE ANY OTHER REACTIVE PRODUCT, AND REMOVE ANY OTHER REAGENT

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02-06-2023 дата публикации

System and process for direct upgrading of crude oil to hydrogen and chemicals

Номер: CN115151625B
Принадлежит: Saudi Arabian Oil Co

用于直接将原油提质为氢气和化学品的系统和工艺,包括将入口烃流分离成轻馏分和包含柴油沸点温度范围材料的重馏分;由轻馏分产生包含H 2 和CO的合成气;使产生的CO反应;从重馏分中产生并分离CO 2 、聚合级乙烯、聚合级丙烯、C 4 化合物、裂化产物、轻循环油和重循环油;收集和纯化重馏分产生的CO 2 ;加工C 4 化合物以产生烯烃低聚物和链烷烃残余液;分离裂化产物;低聚轻馏分(light cut)石脑油流;加氢处理芳烃流;对轻循环油进行加氢裂化以产生单芳烃产物流;气化重循环油;使重循环油气化产生的CO反应;收集和纯化CO 2 ;将产生的芳烃化合物加工并分离成苯和对二甲苯。

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01-09-2015 дата публикации

Hydrocarbon synthesis reaction apparatus, hydrocarbon synthesis reaction system, and liquid hydrocarbon recovery method

Номер: US9120981B2
Автор: Yasuhiro Onishi

A hydrocarbon synthesis reaction apparatus synthesizes hydrocarbons by a Fischer-Tropsch synthesis reaction. The apparatus includes a reactor; a flowing line; a first cooling unit; a second cooling unit; a first separating unit which separates the liquid hydrocarbons condensed by the first cooling unit from the gaseous hydrocarbons; and a second separating unit which separates the liquid hydrocarbons condensed by the second cooling unit from the gaseous hydrocarbons. The first cooling unit cools the hydrocarbons which flow through the flowing line to a temperature range equal to or lower than a condensing point at which a wax fraction condenses, and higher than a freezing point at which the wax fraction solidifies. The second cooling unit cools the hydrocarbons which flow through the flowing line to a temperature range lower than the temperature to which the gaseous hydrocarbons are cooled by the first cooling unit, and higher than a freezing point at which a middle distillate solidifies.

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03-03-2020 дата публикации

Loading a catalyst into a bubble column for Fischer-Topsch synthesis

Номер: US10576444B2
Принадлежит: IFP Energies Nouvelles IFPEN

A method for charging a catalyst into a reactor ( 40 ) comprising a separation loop ( 21 ), comprising the following steps: a) filling the reactor ( 40 ) with a solvent S 1; b) filling the separation loop ( 21 ) with said solvent S 1; c) causing said solvent S 1 to move in the synthesis reactor ( 40 ) and the separation loop ( 21 ); d) heating the reactor ( 40 ) to a temperature of 100° C. or less; e) injecting an inert gas into the bottom of the reactor ( 40 ); f) mixing said catalyst with a solvent S 2 in a vessel ( 30 ) in order to obtain a liquid/solid mixture; g) increasing the pressure in the vessel ( 30 ) then sending the liquid/solid mixture to the reactor ( 40 ); h) withdrawing said solvent S 1 and/or S 2.

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14-03-2017 дата публикации

Start-up method of hydrocarbon synthesis reaction apparatus

Номер: CA2889863C

This start up method for a hydrocarbon synthesis reaction apparatus is provided with: an initial slurry-filling step in which, during start up, the inside of a reaction vessel is filled with an initial preparation slurry amount which is less than a slurry amount during steady operation; and a CO-conversion-rate increasing step in which hydrocarbons to be synthesized when operation is initiated are added to the slurry to increase the height of the liquid level of the slurry, and the CO conversion rate is increased in accordance with the increase in the height of the liquid level of the slurry.

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13-08-2009 дата публикации

Liquid fuel synthesis system

Номер: JPWO2007114250A1
Принадлежит: Nippon Steel Engineering Co Ltd

この液体燃料合成システム1は、炭化水素原料を改質して一酸化炭素ガス及び水素ガスを主成分とする合成ガスを生成する改質器12と、合成ガスに含まれる一酸化炭素ガス及び水素ガスから液体炭化水素を合成する気泡塔型反応器30と、改質器12から気泡塔型反応器30への合成ガスの供給経路としての配管150と、改質器12で生成された合成ガスを少なくとも気泡塔型反応器30における所定の反応圧力以上に圧縮する第1圧縮装置110とを備える。 This liquid fuel synthesizing system 1 includes a reformer 12 that reforms a hydrocarbon raw material to generate a syngas mainly composed of carbon monoxide gas and hydrogen gas, and a carbon monoxide gas and hydrogen contained in the syngas. A bubble column reactor 30 for synthesizing liquid hydrocarbons from gas, a pipe 150 as a synthesis gas supply path from the reformer 12 to the bubble column reactor 30, and a synthesis gas generated in the reformer 12 And a first compression device 110 that compresses at least a predetermined reaction pressure in the bubble column reactor 30.

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13-05-2009 дата публикации

Liquid fuel synthesis system

Номер: CN101432395A
Принадлежит: Nippon Steel Engineering Co Ltd

本发明的液体燃料合成系统(1)具备:重整器(12),其对碳氢化合物原料进行重整,生成以一氧化碳气体及氢气为主成分的合成气;气泡塔式反应器(30),其由合成气中所含的一氧化碳气体及氢气来合成液体碳氢化合物;配管(150),其作为从重整器(12)向气泡塔式反应器(30)供给合成气的供给路径;第1压缩装置(110),其将在重整器(12)生成的合成气压缩到至少气泡塔式反应器(30)中的规定的反应压力以上。

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23-11-2022 дата публикации

Systems and processes for direct crude oil upgrading to hydrogen and chemicals

Номер: EP4090719A1
Принадлежит: Saudi Arabian Oil Co

Systems and methods for direct crude oil upgrading to hydrogen and chemicals including separating an inlet hydrocarbon stream into a light fraction and a heavy fraction comprising diesel boiling point temperature range material; producing from the light fraction syngas comprising H 2 and CO; reacting the CO produced; producing from the heavy fraction and separating CO 2 , polymer grade ethylene, polymer grade propylene, C 4 compounds, cracking products, light cycle oils, and heavy cycle oils; collecting and purifying the CO 2 produced from the heavy fraction; processing the C 4 compounds to produce olefinic oligomerate and paraffinic raffinate; separating the cracking products; oligomerizing a light cut naphtha stream; hydrotreating an aromatic stream; hydrocracking the light cycle oils to produce a monoaromatics product stream; gasifying the heavy cycle oils; reacting the CO produced from gasifying the heavy cycle oils; collecting and purifying the CO 2 ; and processing and separating produced aromatic compounds into benzene and para- xylene.

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14-07-2015 дата публикации

Process for producing at least one product from at least one gaseous reactant in a slurry bed

Номер: US9080108B2
Принадлежит: Sasol Technology Pty Ltd

A process for producing at least one product from at least one gaseous reactant includes feeding the gaseous reactant, as a gaseous feed or as part of a gaseous feed which is at an inlet superficial gas velocity of at least 0.5 m/s, into a vessel holding an expanded slurry bed of solid catalyst particles suspended in a suspension liquid so that the gaseous reactant can bubble upwardly through the slurry bed. The slurry bed has a catalyst loading of less than 14% by volume of degassed slurry. The gaseous reactant is allowed to react catalytically at a pressure above atmospheric pressure as the gaseous reactant bubbles upwardly through the slurry bed to produce at least one product. The product and any unreacted gaseous reactant are withdrawn from the vessel.

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09-06-2006 дата публикации

PROCESS FOR PROVISIONALLY INTERRUPTING A FISCHER-TROPSCH TYPE REACTION IN A THREE-PHASE BED REACTOR

Номер: FR2878845A1
Принадлежит: Eni Spa, IFP Energies Nouvelles IFPEN

Procédé d'interruption provisoire d'une réaction de type Fischer-Tropsch mise en oeuvre sur une charge comportant au moins du monoxyde de carbone et de l'hydrogène, dans une zone réactionnelle à lit triphasique comportant une phase liquide, une phase gazeuse et des particules solides de catalyseur maintenues en suspension, ledit procédé comprenant une étape a) d'interruption de la réaction et une étape b) de redémarrage de ladite réaction, pendant lesquelles on maintient les particules solides de catalyseur en suspension dans la zone réactionnelle,a) lors de l'étape d'interruption de la réaction, on arrête l'alimentation de la charge, et on établit, dans la zone réactionnelle, une couverture d'un gaz inhibant comportant moins de 1 % en volume d'hydrogène et au moins 5 % en volume d'au moins un composé inhibant choisi dans le groupe formé par le monoxyde de carbone et l'eau, etb) lors de l'étape de redémarrage de la réaction, on établit, dans la zone réactionnelle, une couverture d'un gaz activant ayant une teneur en hydrogène d'au moins 20 % en volume, et on redémarre l'alimentation de la charge. Process for temporarily interrupting a reaction of the Fischer-Tropsch type carried out on a feed comprising at least carbon monoxide and hydrogen, in a three-phase bed reaction zone comprising a liquid phase, a gas phase and solid particles of catalyst kept in suspension, said process comprising a step a) of interrupting the reaction and a step b) of restarting said reaction, during which the solid particles of catalyst are kept in suspension in the reaction zone, a) during the step of interrupting the reaction, the feed to the feed is stopped, and a blanket of an inhibiting gas comprising less than 1% by volume of hydrogen and at least 5% by volume of at least one inhibiting compound chosen from the group formed by carbon monoxide and water, andb) during the step of restarting the reaction, a blanket of d is ...

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04-09-2019 дата публикации

A process for producing hydrocarbons

Номер: EP3532567A1

The present application relates to a process for producing normally gaseous, normally liquid, and optionally normally solid hydrocarbons from synthesis gas in a three- phase reactor, said reactor comprising a top middle and bottom part wherein the bottom and top part are fluidly connected via one or more reactor tubes, wherein one or more reactor tubes comprise randomly stacked catalyst bodies held stationary in the reactor tube and the reactor is at least partially filled with a liquid medium, said process comprising the steps of: (i) introducing the synthesis gas into the reactor via the bottom part; and (ii) contacting the synthesis gas with a stationary catalyst to catalytically convert the synthesis gas at an elevated temperature to obtain the normally gaseous, normally liquid, and optionally normally solid hydrocarbons from synthesis gas; (iii) withdrawing the normally gaseous, normally liquid, and optionally normally solid hydrocarbons; wherein the catalyst bodies have an open celled foam structure.

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10-05-2010 дата публикации

LIQUID FUEL SYNTHESIS SYSTEM

Номер: RU2008140161A

1. Система синтеза жидкого топлива, включающая в себя: ! реформинг-установку, где углеводородное сырье преобразуется для получения синтез-газа, содержащего в качестве основных компонентов угарный газ и газообразный водород; ! реактор, где из угарного газа и газообразного водорода, входящих в состав синтез-газа, синтезируются жидкие углеводороды; ! магистраль подачи синтез-газа от реформинг-установки к реактору; ! первую компрессорную установку, находящуюся в магистрали подачи, где сжимается синтез-газ, полученный в реформинг-установке и имеющий давление по меньшей мере большее, чем заранее заданное давление в реакторе. ! 2. Система синтеза жидкого топлива по п.1, дополнительно включающая в себя паровой котел-утилизатор (восстанавливает тепло, выработанное в реформинг-установке, чтобы получать пар), в которой первая компрессорная установка приводится в действие паром полученным в паровом котле-утилизаторе, являющимся источником энергии. ! 3. Система синтеза жидкого топлива по п.1, дополнительно включающая в себя: ! магистраль рециркуляции, по которой непрореагировавший синтез-газ, отобранный от реактора, возвращается к впускному отверстию указанного реактора; ! вторую компрессорную установку, находящуюся в магистрали рециркуляции и предназначенную для сжатия непрореагировавшего синтез-газа до давления по меньшей мере большего, чем заранее заданное давление в реакторе. ! 4. Система синтеза жидкого топлива по п.3, дополнительно включающая в себя паровой котел-утилизатор (восстанавливает тепло, выработанное в реформинг-установке, чтобы получать пар), в которой вторая компрессорная установка приводится в дейст РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) 2008 140 161 (13) A (51) МПК C10G 2/00 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ, ПАТЕНТАМ И ТОВАРНЫМ ЗНАКАМ (12) ЗАЯВКА НА ИЗОБРЕТЕНИЕ (21), (22) Заявка: 2008140161/04, 29.03.2007 (71) Заявитель(и): НИППОН СТИЛ ИНДЖИНИРИНГ КО., ЛТД. (JP) (30) Конвенционный приоритет: 30.03.2006 JP 2006-095932 (43) Дата ...

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11-06-2021 дата публикации

Catalyst, preparation method and application thereof, reduction activation method of catalyst precursor and preparation method of low-carbon olefin

Номер: CN108722426B

本发明公开了一种催化剂及制备方法和应用以及催化剂前体还原活化方法以及低碳烯烃的制备方法。本发明公开了一种催化剂及其制备方法和应用,本发明还公开了采用上述催化剂的制备低碳烯烃的方法,所述催化剂含有载体以及负载在载体上的第VIII族金属元素,所述载体为氧化铝,至少部分第VIII族金属元素的价态为低于该金属元素的最高氧化价态;该催化剂的CO 2 ‑TPD脱附图中,在300‑600℃的温度区间内存在CO 2 高温脱附峰。根据本发明的催化剂,即便是在高空速的流化床反应器中于温和的反应条件下进行费托合成反应,也能获得较高的CO转化率,而且能明显提高低碳烯烃的选择性,同时还能获得更高的活性稳定性。

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01-02-2012 дата публикации

Synthesis method and synthesis system for liquid hydrocarbons

Номер: EP2412784A1
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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03-03-2005 дата публикации

High-pressure fischer-tropsch synthesis process using an optimized coolant

Номер: US20050049318A1
Принадлежит: Eni Spa, IFP Energies Nouvelles IFPEN

Process for synthesis of hydrocarbons by Fischer-Tropsch reaction starting from synthesis gas, operating in three-phase fluidization, the reactor having an exchanger immersed within the fluidized bed and using as coolant a fluid introduced at its boiling point at a pressure slightly greater than the pressure of the process, this boiling point being from 10 to 70° C. below the temperature of the process.

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