PL391521A1 - System for separating carbon dioxide and acid gas from synthesis gas and method for assembling the system for separation of carbon dioxide and acid gas from synthesis gas - Google Patents

System for separating carbon dioxide and acid gas from synthesis gas and method for assembling the system for separation of carbon dioxide and acid gas from synthesis gas

Info

Publication number
PL391521A1
PL391521A1 PL391521A PL39152110A PL391521A1 PL 391521 A1 PL391521 A1 PL 391521A1 PL 391521 A PL391521 A PL 391521A PL 39152110 A PL39152110 A PL 39152110A PL 391521 A1 PL391521 A1 PL 391521A1
Authority
PL
Poland
Prior art keywords
carbon dioxide
synthesis gas
gas
circuit
acid gas
Prior art date
Application number
PL391521A
Other languages
Polish (pl)
Other versions
PL219631B1 (en
Inventor
Pradeep Thacker
Original Assignee
General Electric Company
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 General Electric Company filed Critical General Electric Company
Publication of PL391521A1 publication Critical patent/PL391521A1/en
Publication of PL219631B1 publication Critical patent/PL219631B1/en

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/14—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
    • B01D53/1456—Removing acid components
    • B01D53/1462—Removing mixtures of hydrogen sulfide and carbon dioxide
    • 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
    • C01B3/50—Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification
    • C01B3/52—Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification by contacting with liquids; Regeneration of used liquids
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
    • C10K1/00—Purifying combustible gases containing carbon monoxide
    • C10K1/08—Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors
    • C10K1/10—Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors with aqueous liquids
    • C10K1/12—Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors with aqueous liquids alkaline-reacting including the revival of the used wash liquors
    • 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
    • C01B2203/0415—Purification by absorption in liquids
    • 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
    • C01B2203/0475—Composition of the impurity the impurity being carbon dioxide
    • 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
    • C01B2203/0485—Composition of the impurity the impurity being a sulfur compound
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
    • Y02C20/00—Capture or disposal of greenhouse gases
    • Y02C20/40—Capture or disposal of greenhouse gases of CO2
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00—Combustion technologies with mitigation potential
    • Y02E20/16—Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT]
    • Y02E20/18—Integrated gasification combined cycle [IGCC], e.g. combined with carbon capture and storage [CCS]
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/151—Reduction of greenhouse gas [GHG] emissions, e.g. CO2

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Organic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Analytical Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Gas Separation By Absorption (AREA)
  • Carbon And Carbon Compounds (AREA)

Abstract

Układ (100) do oddzielania dwutlenku węgla oraz gazu kwaśnego od gazu syntezowego, zawiera obwód oczyszczania gazu syntezowego (102) zawierający co najmniej jedną kolumnę absorpcyjną (108), połączoną połączeniem przepływowym z zasilaniem rozpuszczalnika ubogiego i zawiera obwód usuwania dwutlenku węgla (104), podłączony za obwodem oczyszczania gazu syntezowego (102). Obwód usuwania dwutlenku węgla (104) zawiera co najmniej jeden element składowy, który ułatwia usuwanie dwutlenku węgla z rozpuszczalnika po przejściu przez rozpuszczalnik przez obwód oczyszczania gazu syntezowego. Obwód usuwania dwutlenku węgla (104) zawiera również co najmniej jedną sprężarkę (138, 140, 142), która pracuje przy zasadniczo podobnym ciśnieniu, jak co najmniej jeden element składowy. Układ zawiera obwód usuwania gazu kwaśnego (106) podłączony za obwodem usuwania dwutlenku węgla (104). Obwód usuwania gazu kwaśnego (106) zawiera co najmniej jedną kolumnę absorpcyjną (110). Wynalazek obejmuje sposób montażu układu do oddzielania dwutlenku węgla oraz gazu kwaśnego od gazu syntezowego.The system (100) for separating carbon dioxide and sour gas from the synthesis gas includes a synthesis gas purification circuit (102) including at least one absorption column (108), connected by a flow connection to a lean solvent feed, and includes a carbon dioxide removal circuit (104), connected downstream of the synthesis gas purification circuit (102). The carbon dioxide removal circuit (104) includes at least one component that facilitates the removal of carbon dioxide from the solvent after the solvent has passed through the syngas purification circuit. The carbon dioxide removal circuit (104) also includes at least one compressor (138, 140, 142) that operates at a substantially similar pressure as the at least one component. The system includes a sour gas removal circuit (106) connected downstream of the carbon dioxide removal circuit (104). The sour gas removal circuit (106) includes at least one absorption column (110). The invention includes a method for assembling a system for separating carbon dioxide and sour gas from synthesis gas.

PL391521A 2009-06-17 2010-06-15 System for separating carbon dioxide and acid gas from synthesis gas and method for assembling the system for separation of carbon dioxide and acid gas from synthesis gas PL219631B1 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US12/486,211 US20100319254A1 (en) 2009-06-17 2009-06-17 Methods and system for separating carbon dioxide from syngas

Publications (2)

Publication Number Publication Date
PL391521A1 true PL391521A1 (en) 2010-12-20
PL219631B1 PL219631B1 (en) 2015-06-30

Family

ID=43352949

Family Applications (1)

Application Number Title Priority Date Filing Date
PL391521A PL219631B1 (en) 2009-06-17 2010-06-15 System for separating carbon dioxide and acid gas from synthesis gas and method for assembling the system for separation of carbon dioxide and acid gas from synthesis gas

Country Status (5)

Country Link
US (1) US20100319254A1 (en)
CN (1) CN101927120B (en)
AU (1) AU2010202532B2 (en)
CA (1) CA2706267C (en)
PL (1) PL219631B1 (en)

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JP5619151B2 (en) * 2009-05-26 2014-11-05 ビーエーエスエフ ソシエタス・ヨーロピアＢａｓｆ Ｓｅ Method for the recovery of carbon dioxide from a fluid stream, especially synthesis gas
CN103582693A (en) * 2011-06-03 2014-02-12 格雷特波因特能源公司 Hydromethanation of a carbonaceous feedstock
US9545597B2 (en) * 2011-12-01 2017-01-17 Statoil Petroleum As Continuously stirred tank reactor absorber and flash tank stripper system
WO2018044263A1 (en) * 2016-08-29 2018-03-08 Pilot Energy Solutions, Llc Three column hydrocarbon recovery from carbon dioxide enhanced oil recovery streams
EP3401001A1 (en) * 2017-05-12 2018-11-14 L'air Liquide, Société Anonyme Pour L'Étude Et L'exploitation Des Procédés Georges Claude Method and assembly for the separation of extraneous gases from a raw synthesis gas
EP3583997B1 (en) * 2018-06-18 2022-09-28 L'air Liquide, Société Anonyme Pour L'Étude Et L'exploitation Des Procédés Georges Claude Method and system for the production of synthesis gas

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Also Published As

Publication number Publication date
CN101927120B (en) 2014-12-31
US20100319254A1 (en) 2010-12-23
CA2706267A1 (en) 2010-12-17
AU2010202532B2 (en) 2016-09-08
CA2706267C (en) 2017-11-07
CN101927120A (en) 2010-12-29
AU2010202532A1 (en) 2011-01-13
PL219631B1 (en) 2015-06-30

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