BR112014007126A2 - processo para fornecer hidrogênio para uma reação de conversão de gás de síntese - Google Patents

processo para fornecer hidrogênio para uma reação de conversão de gás de síntese

Info

Publication number
BR112014007126A2
BR112014007126A2 BR112014007126A BR112014007126A BR112014007126A2 BR 112014007126 A2 BR112014007126 A2 BR 112014007126A2 BR 112014007126 A BR112014007126 A BR 112014007126A BR 112014007126 A BR112014007126 A BR 112014007126A BR 112014007126 A2 BR112014007126 A2 BR 112014007126A2
Authority
BR
Brazil
Prior art keywords
synthesis gas
gas conversion
conversion reaction
hydrogen
reaction zone
Prior art date
Application number
BR112014007126A
Other languages
English (en)
Inventor
Fayyaz-Najafi Babak
Kibby Charles
You Lixin
Husain Shabbir
Original Assignee
Chevron Usa Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Chevron Usa Inc filed Critical Chevron Usa Inc
Publication of BR112014007126A2 publication Critical patent/BR112014007126A2/pt

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C1/00—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
    • C07C1/02—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon from oxides of a carbon
    • C07C1/04—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon from oxides of a carbon from carbon monoxide with hydrogen
    • C07C1/0405—Apparatus
    • C07C1/041—Reactors
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/24—Stationary reactors without moving elements inside
    • B01J19/248—Reactors comprising multiple separated flow channels
    • B01J19/249—Plate-type reactors
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/008—Details of the reactor or of the particulate material; Processes to increase or to retard the rate of reaction
    • B01J8/009—Membranes, e.g. feeding or removing reactants or products to or from the catalyst bed through a membrane
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/0207—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid flow within the bed being predominantly horizontal
    • B01J8/0214—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid flow within the bed being predominantly horizontal in a cylindrical annular shaped bed
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/0242—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid flow within the bed being predominantly vertical
    • B01J8/0257—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid flow within the bed being predominantly vertical in a cylindrical annular shaped bed
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/06—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds in tube reactors; the solid particles being arranged in tubes
    • B01J8/067—Heating or cooling the reactor
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C7/00—Purification; Separation; Use of additives
    • C07C7/144—Purification; Separation; Use of additives using membranes, e.g. selective permeation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00106—Controlling the temperature by indirect heat exchange
    • B01J2208/00168—Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles
    • B01J2208/00212—Plates; Jackets; Cylinders
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/24—Stationary reactors without moving elements inside
    • B01J2219/2401—Reactors comprising multiple separate flow channels
    • B01J2219/245—Plate-type reactors
    • B01J2219/2451—Geometry of the reactor
    • B01J2219/2453—Plates arranged in parallel
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/24—Stationary reactors without moving elements inside
    • B01J2219/2401—Reactors comprising multiple separate flow channels
    • B01J2219/245—Plate-type reactors
    • B01J2219/2451—Geometry of the reactor
    • B01J2219/2456—Geometry of the plates
    • B01J2219/2459—Corrugated plates
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/24—Stationary reactors without moving elements inside
    • B01J2219/2401—Reactors comprising multiple separate flow channels
    • B01J2219/245—Plate-type reactors
    • B01J2219/2461—Heat exchange aspects
    • B01J2219/2462—Heat exchange aspects the reactants being in indirect heat exchange with a non reacting heat exchange medium
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/24—Stationary reactors without moving elements inside
    • B01J2219/2401—Reactors comprising multiple separate flow channels
    • B01J2219/245—Plate-type reactors
    • B01J2219/2475—Separation means, e.g. membranes inside the reactor
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/24—Stationary reactors without moving elements inside
    • B01J2219/2401—Reactors comprising multiple separate flow channels
    • B01J2219/245—Plate-type reactors
    • B01J2219/2476—Construction materials
    • B01J2219/2477—Construction materials of the catalysts
    • B01J2219/2481—Catalysts in granular from between plates

Abstract

1/1 resumo “processo para fornecer hidrogênio para uma reação de con versão de gás de síntese” a presente invenção se refere a um processo de conversão de gás de síntese para a realização do processo. um gás de varredura contendo hidrogênio é provocado a fluir através de uma membrana permseletiva de água adjacente a uma zona de reação de conversão de gás de síntese em que o gás de síntese é posto em contato com um catalisador e convertido em efluente incluindo água. a água é removida da zona de reação através da membrana. o gás de varredura tem pressão parcial de hidrogênio suficiente para fazer com que o hidrogênio passe através da membrana para a zona de reação.
BR112014007126A 2011-10-07 2012-03-28 processo para fornecer hidrogênio para uma reação de conversão de gás de síntese BR112014007126A2 (pt)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US13/224,600 US8425854B1 (en) 2011-10-07 2011-10-07 Process for providing hydrogen to a synthesis gas conversion reaction
PCT/US2012/030932 WO2013052151A1 (en) 2011-10-07 2012-03-28 Process for providing hydrogen to a synthesis gas conversion reaction

Publications (1)

Publication Number Publication Date
BR112014007126A2 true BR112014007126A2 (pt) 2017-04-18

Family

ID=48042471

Family Applications (1)

Application Number Title Priority Date Filing Date
BR112014007126A BR112014007126A2 (pt) 2011-10-07 2012-03-28 processo para fornecer hidrogênio para uma reação de conversão de gás de síntese

Country Status (6)

Country Link
US (1) US8425854B1 (pt)
AU (1) AU2012319146A1 (pt)
BR (1) BR112014007126A2 (pt)
CA (1) CA2850710A1 (pt)
DE (1) DE112012004158T5 (pt)
WO (1) WO2013052151A1 (pt)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10230131B2 (en) * 2013-07-11 2019-03-12 Gotion Inc. Method for producing a dehydrated liquid organic carbonate mixture
US9023901B2 (en) 2013-07-31 2015-05-05 Chevron U.S.A. Inc. System, process and reactor for conducting a synthesis gas conversion reaction
WO2015138898A1 (en) * 2014-03-13 2015-09-17 General Electric Company Reverse osmosis system for use with a wellbore and methods of assembling the same
EP3551327B1 (en) * 2016-12-09 2022-02-16 Velocys Technologies Limited Process for operating a highly productive tubular reactor
EP3517204A1 (en) * 2018-01-26 2019-07-31 Nederlandse Organisatie voor toegepast- natuurwetenschappelijk onderzoek TNO Reactor and process for the hydrogenation of carbon dioxide
CN112657435B (zh) * 2020-12-24 2022-05-31 中国人民解放军海军工程大学 Co2加氢合成甲醇膜反应器及总熵生产率最小优化方法
WO2023120494A1 (ja) * 2021-12-22 2023-06-29 日本碍子株式会社 リアクタ及び液体燃料合成方法

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4181675A (en) 1978-09-19 1980-01-01 Monsanto Company Process for methanol production
EP1089956B1 (en) * 1998-06-11 2003-11-05 Sasol Technology (Proprietary) Limited Production of hydrocarbons
US6946493B2 (en) 2003-03-15 2005-09-20 Conocophillips Company Managing hydrogen in a gas to liquid plant
WO2009088785A1 (en) * 2007-12-31 2009-07-16 Chevron U.S.A. Inc. Membrane reactor with in-situ dehydration and method for using the same
US20110160315A1 (en) 2009-12-30 2011-06-30 Chevron U.S.A. Inc. Process of synthesis gas conversion to liquid hydrocarbon mixtures using synthesis gas conversion catalyst and hydroisomerization catalyst

Also Published As

Publication number Publication date
CA2850710A1 (en) 2013-04-11
US20130090394A1 (en) 2013-04-11
US8425854B1 (en) 2013-04-23
AU2012319146A1 (en) 2014-04-10
DE112012004158T5 (de) 2014-07-10
WO2013052151A1 (en) 2013-04-11

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Legal Events

Date Code Title Description
B08F Application fees: application dismissed [chapter 8.6 patent gazette]
B08K Patent lapsed as no evidence of payment of the annual fee has been furnished to inpi [chapter 8.11 patent gazette]