CA3254136A1 - Systèmes, dispositifs et procédés d'intensification de reformeurs et de synthèse chimique en aval - Google Patents

Systèmes, dispositifs et procédés d'intensification de reformeurs et de synthèse chimique en aval

Info

Publication number
CA3254136A1
CA3254136A1 CA3254136A CA3254136A CA3254136A1 CA 3254136 A1 CA3254136 A1 CA 3254136A1 CA 3254136 A CA3254136 A CA 3254136A CA 3254136 A CA3254136 A CA 3254136A CA 3254136 A1 CA3254136 A1 CA 3254136A1
Authority
CA
Canada
Prior art keywords
plant
reactor
reactor unit
flare gas
bpd
Prior art date
Legal status (The legal status 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 status listed.)
Pending
Application number
CA3254136A
Other languages
English (en)
Inventor
Paul E. Yelvington
Edwin Yik
John Anthony Dean
Joshua B. Browne
Original Assignee
M2X Energy 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
Priority claimed from PCT/US2022/029707 external-priority patent/WO2022245879A2/fr
Priority claimed from PCT/US2022/044724 external-priority patent/WO2023049450A1/fr
Application filed by M2X Energy Inc filed Critical M2X Energy Inc
Publication of CA3254136A1 publication Critical patent/CA3254136A1/fr
Pending legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
    • C07C29/15—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively
    • C07C29/151—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases
    • C07C29/152—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases characterised by the reactor used
    • 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
    • B01J19/18—Stationary reactors having moving elements inside
    • B01J19/1893—Membrane 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
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/80—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with zinc, cadmium or mercury
    • 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
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/50—Catalysts, in general, characterised by their form or physical properties characterised by their shape or configuration
    • B01J35/58—Fabrics or filaments
    • 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
    • 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
    • B01J8/04—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 passing successively through two or more beds
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen; Reversible storage of hydrogen
    • C01B3/02—Production of hydrogen; Production of gaseous mixtures containing hydrogen
    • C01B3/32—Production of hydrogen; Production of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide or air
    • C01B3/34—Production of hydrogen; Production of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide or air by reaction of hydrocarbons with gasifying agents
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/04—Integrated processes for the production of hydrogen or synthesis gas containing a purification step for the hydrogen or the synthesis gas
    • C01B2203/0405—Purification by membrane separation
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/04—Integrated processes for the production of hydrogen or synthesis gas containing a purification step for the hydrogen or the synthesis gas
    • C01B2203/0465—Composition of the impurity
    • C01B2203/0495—Composition of the impurity the impurity being water
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/06—Integration with other chemical processes
    • C01B2203/061—Methanol production
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/06—Integration with other chemical processes
    • C01B2203/068—Ammonia synthesis

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Inorganic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Hydrogen, Water And Hydrids (AREA)

Abstract

L'invention concerne des installations intensifiées comprenant des reformeurs chimiques et un équipement de synthèse chimique en aval. L'invention concerne également des systèmes, des procédés et des dispositifs permettant une intensification de processus (PI) qui conduit à la réduction du nombre de pièces, à une fonctionnalité de fusion, à l'élimination de goulots d'étranglement, à la réduction des coûts et à la modularisation de sous-systèmes pour une facilité d'assemblage et d'entretien en vue d'atteindre la simplification globale nécessaire pour obtenir un coût de produit compétitif à de petites échelles. Dans un mode de réalisation, les installations améliorées utilisent des reformeurs de moteur pour produire un gaz de synthèse, qui est en outre converti en produits finaux à l'aide de réacteurs en aval intensifiés.
CA3254136A 2022-05-17 2023-05-16 Systèmes, dispositifs et procédés d'intensification de reformeurs et de synthèse chimique en aval Pending CA3254136A1 (fr)

Applications Claiming Priority (7)

Application Number Priority Date Filing Date Title
PCT/US2022/029707 WO2022245879A2 (fr) 2021-05-18 2022-05-17 Systèmes et procédés de conversion de gaz de torche modulaires autonomes
USPCT/US2022/029707 2022-05-17
US202263343087P 2022-05-18 2022-05-18
US63/343,087 2022-05-18
PCT/US2022/044724 WO2023049450A1 (fr) 2021-09-26 2022-09-26 Procédés et systèmes associés à un moyeu de valorisation de méthanol modulaire
USPCT/US2022/044724 2022-09-26
PCT/US2023/067087 WO2023225532A2 (fr) 2022-05-17 2023-05-16 Systèmes, dispositifs et procédés d'intensification de reformeurs et de synthèse chimique en aval

Publications (1)

Publication Number Publication Date
CA3254136A1 true CA3254136A1 (fr) 2023-11-23

Family

ID=88836101

Family Applications (1)

Application Number Title Priority Date Filing Date
CA3254136A Pending CA3254136A1 (fr) 2022-05-17 2023-05-16 Systèmes, dispositifs et procédés d'intensification de reformeurs et de synthèse chimique en aval

Country Status (5)

Country Link
EP (1) EP4526280A2 (fr)
AU (1) AU2023273035A1 (fr)
CA (1) CA3254136A1 (fr)
MX (1) MX2024014249A (fr)
WO (1) WO2023225532A2 (fr)

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20070151451A1 (en) * 2005-12-22 2007-07-05 Rekers Dominicus M Process for the cooling, concentration or purification of ethylene oxide
WO2011031752A2 (fr) * 2009-09-08 2011-03-17 The Ohio State University Research Foundation Production de combustibles et produits chimiques de synthèse avec capture de co2 in situ
US9169773B2 (en) * 2012-04-18 2015-10-27 Massachusetts Institute Of Technology Engine reformer systems for lower cost, smaller scale manufacturing of liquid fuels

Also Published As

Publication number Publication date
EP4526280A2 (fr) 2025-03-26
AU2023273035A1 (en) 2024-12-12
WO2023225532A2 (fr) 2023-11-23
MX2024014249A (es) 2025-05-02
WO2023225532A3 (fr) 2024-03-14

Similar Documents

Publication Publication Date Title
Deshmukh et al. Scale-up of microchannel reactors for Fischer− Tropsch synthesis
RU2310677C2 (ru) Каталитический реактор и способ
RU2503613C2 (ru) Способ производства синтез-газа
EP2694433B1 (fr) Procédé de transformation du gaz en liquide à haute pression
RU2375406C2 (ru) Установка и способ каталитического синтеза фишера-тропша
US20240017235A1 (en) Systems, Devices and Methods for Intensification of Reformers and Downstream Chemical Synthesis
Saidi Application of catalytic membrane reactor for pure hydrogen production by flare gas recovery as a novel approach
US7109248B2 (en) Converting natural gas to longer-chain hydrocarbons
KR20060126604A (ko) 장쇄 탄화수소를 형성하기 위한 천연가스 처리방법
Brunetti et al. Membrane reactors for hydrogen production
US20060135630A1 (en) Producing longer-chain hydrocarbons from natural gas
Rahimpour et al. Enhancement of simultaneous hydrogen production and methanol synthesis in thermally coupled double-membrane reactor
Bayat et al. Simultaneous utilization of two different membranes for intensification of ultrapure hydrogen production from recuperative coupling autothermal multitubular reactor
EP4526280A2 (fr) Systèmes, dispositifs et procédés d'intensification de reformeurs et de synthèse chimique en aval
Frilund CO2 hydrogenation to methanol
WO2013093428A1 (fr) Fonctionnement d'un procédé catalytique fischer-tropsch
Greenblatt Design and Modeling of an Electrochemical Device Producing Methane/Oxygen and Polyethylene from In-Situ Resources on Mars
Ani et al. Application of a New Axial Flow Spherical Membrane Reactor in Methanol Steam Reforming Process for Large Scale Hydrogen Production: Modeling and Multi-Objective Optimization
RU2472765C1 (ru) Способ получения метанола
Tonkovich et al. Gas-to-liquids conversion of associated gas enabled by microchannel technology
Rahmani et al. Simulation study of an auto-thermal double-membrane reactor for the simultaneous production of hydrogen and methanol: comparison of two different hydrogen redistribution strategies along the reactor
El Sibai Model-based optimization and experimental investigation of CO2 methanation
WO2025033442A1 (fr) Dispositif de condensation
Ghani et al. Hydrogen-Self-Sufficient Ammonia Synthesis through Thermal Coupling with Endothermic Dehydrogenation Reactions
Hershkowitz et al. A Breakthrough Process for the Production of Hydrogen

Legal Events

Date Code Title Description
A00 Application filed

Free format text: ST27 STATUS EVENT CODE: A-0-1-A10-A00-A101 (AS PROVIDED BY THE NATIONAL OFFICE); EVENT TEXT: APPLICATION RECEIVED - PCT

Effective date: 20241115

A15 Pct application entered into the national or regional phase

Free format text: ST27 STATUS EVENT CODE: A-1-1-A10-A15-X000 (AS PROVIDED BY THE NATIONAL OFFICE); EVENT TEXT: NATIONAL ENTRY REQUIREMENTS DETERMINED COMPLIANT

Effective date: 20250205

A00 Application filed

Free format text: ST27 STATUS EVENT CODE: A-1-1-A10-A00-A102 (AS PROVIDED BY THE NATIONAL OFFICE); EVENT TEXT: COMPLIANCE REQUIREMENTS DETERMINED MET

Effective date: 20250206

P18 Priority claim added or amended

Free format text: ST27 STATUS EVENT CODE: A-1-1-P10-P18-P105 (AS PROVIDED BY THE NATIONAL OFFICE); EVENT TEXT: PRIORITY CLAIM REQUIREMENTS DETERMINED COMPLIANT

Effective date: 20250206

W00 Other event occurred

Free format text: ST27 STATUS EVENT CODE: A-1-1-W10-W00-W100 (AS PROVIDED BY THE NATIONAL OFFICE); EVENT TEXT: LETTER SENT

Effective date: 20250218

MFA Maintenance fee for application paid

Free format text: FEE DESCRIPTION TEXT: MF (APPLICATION, 2ND ANNIV.) - STANDARD

Year of fee payment: 2

U00 Fee paid

Free format text: ST27 STATUS EVENT CODE: A-1-1-U10-U00-U101 (AS PROVIDED BY THE NATIONAL OFFICE); EVENT TEXT: MAINTENANCE REQUEST RECEIVED

Effective date: 20250507

U11 Full renewal or maintenance fee paid

Free format text: ST27 STATUS EVENT CODE: A-1-1-U10-U11-U102 (AS PROVIDED BY THE NATIONAL OFFICE); EVENT TEXT: MAINTENANCE FEE PAYMENT PAID IN FULL

Effective date: 20250507

MFA Maintenance fee for application paid

Free format text: FEE DESCRIPTION TEXT: MF (APPLICATION, 3RD ANNIV.) - STANDARD

Year of fee payment: 3

U00 Fee paid

Free format text: ST27 STATUS EVENT CODE: A-1-1-U10-U00-U101 (AS PROVIDED BY THE NATIONAL OFFICE); EVENT TEXT: MAINTENANCE REQUEST RECEIVED

Effective date: 20260402

U11 Full renewal or maintenance fee paid

Free format text: ST27 STATUS EVENT CODE: A-1-1-U10-U11-U102 (AS PROVIDED BY THE NATIONAL OFFICE); EVENT TEXT: MAINTENANCE FEE PAYMENT PAID IN FULL

Effective date: 20260402