ES471942A1 - Procedimiento para la obtencion de gases de sintesis - Google Patents

Procedimiento para la obtencion de gases de sintesis

Info

Publication number
ES471942A1
ES471942A1 ES471942A ES471942A ES471942A1 ES 471942 A1 ES471942 A1 ES 471942A1 ES 471942 A ES471942 A ES 471942A ES 471942 A ES471942 A ES 471942A ES 471942 A1 ES471942 A1 ES 471942A1
Authority
ES
Spain
Prior art keywords
synthesis gas
manufacture
bars
separating
partial oxidation
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.)
Expired
Application number
ES471942A
Other languages
English (en)
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
BASF SE
Original Assignee
BASF SE
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 BASF SE filed Critical BASF SE
Publication of ES471942A1 publication Critical patent/ES471942A1/es
Expired legal-status Critical Current

Links

Classifications

    • 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
    • C01B3/50—Separation of hydrogen or hydrogen-containing gases from gaseous mixtures, e.g. purification
    • C01B3/56—Separation of hydrogen or hydrogen-containing gases from gaseous mixtures, e.g. purification by contacting with solids; Regeneration of used solids
    • C01B3/58—Separation of hydrogen or hydrogen-containing gases from gaseous mixtures, e.g. purification by contacting with solids; Regeneration of used solids including a catalytic reaction
    • 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
    • C01B3/36—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 using oxygen; using mixtures containing oxygen as gasifying agents
    • 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
    • C01B3/50—Separation of hydrogen or hydrogen-containing gases from gaseous mixtures, e.g. purification
    • 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
    • C01B3/50—Separation of hydrogen or hydrogen-containing gases from gaseous mixtures, e.g. purification
    • C01B3/506—Separation of hydrogen or hydrogen-containing gases from gaseous mixtures, e.g. purification at low temperatures
    • 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
    • C01B2203/0435—Catalytic purification
    • 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
    • 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
    • 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
    • C01B2203/049—Composition of the impurity the impurity being carbon

Landscapes

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

Abstract

Procedimiento para la obtención de gases de síntesis que contienen en esencia monóxido de carbono e hidrógeno, mediante oxidación parcial de hicdrocarburos o carbón con gases que contienen oxígeno en presencia de vapor de agua u otro moderador de temperatura apropiado, en un reactor de gas de síntesis no catalizado y sin rellenos, a una temperatura de entre 900 y 1700ºC (autotérmica) y una presión de entre 1 y 250 bares, enfriando, a continuación, los productos de reacción, separando el carbono particulado y eliminando las impurificaciones ácidas y llevando a cabo otros tratamientos ulteriores en el orden en sí conocido, caracterizado porque el producto de reacción se trata, después de separar el carbono particulado pero antes de eliminar los componentes ácidos, en una zona de hidrogenación catalizada a temperaturas de 150 a 230ºC.
ES471942A 1977-07-22 1978-07-21 Procedimiento para la obtencion de gases de sintesis Expired ES471942A1 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE2733105A DE2733105B1 (de) 1977-07-22 1977-07-22 Verfahren zur Herstellung von Synthesegasen durch partielle Oxidation

Publications (1)

Publication Number Publication Date
ES471942A1 true ES471942A1 (es) 1979-02-01

Family

ID=6014574

Family Applications (1)

Application Number Title Priority Date Filing Date
ES471942A Expired ES471942A1 (es) 1977-07-22 1978-07-21 Procedimiento para la obtencion de gases de sintesis

Country Status (12)

Country Link
JP (1) JPS5422403A (es)
BE (1) BE869167A (es)
DE (1) DE2733105B1 (es)
ES (1) ES471942A1 (es)
FR (1) FR2398107A1 (es)
GB (1) GB2002809A (es)
IT (1) IT1105096B (es)
NL (1) NL7807723A (es)
NO (1) NO782519L (es)
PT (1) PT68334A (es)
SE (1) SE7807932L (es)
YU (1) YU175278A (es)

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
IN153794B (es) * 1979-03-06 1984-08-18 Aeci Ltd
DE3020975A1 (de) * 1980-06-03 1981-12-10 Krupp-Koppers Gmbh, 4300 Essen Verfahren zur katalytischen behandlung von partialoxidationsrohgas
DE3037969A1 (de) * 1980-10-08 1982-05-13 Basf Ag, 6700 Ludwigshafen Verfahren zur entfernung von blausaeure aus wasserstoff enthaltenden gasen
DE69607423T2 (de) * 1995-08-08 2000-08-03 Exxon Research And Engineering Co., Florham Park Verfahren zur Beseitigung von Cyanwasserstoff aus Synthesegas
US6162373A (en) * 1995-10-03 2000-12-19 Exxon Research And Engineering Company Removal of hydrogen cyanide from synthesis gas (Law322)
DE19983179T1 (de) * 1998-04-27 2001-05-17 Toyo Engineering Corp Vergasungsverfahren
CA2650844C (en) 2006-04-28 2014-01-14 Haldor Topsoe A/S Process for the removal of hydrogen cyanide and formic acid from synthesis gas
BRPI0818853B1 (pt) * 2007-10-26 2018-11-21 Haldor Topsoe A/S processos para a redução na quantidade de compostos de enxofre, cianeto de hidrogênio, ácido fórmico e derivados de ácido fórmico em gás de síntese, para a preparação de metanol, éter dimetílico e/ou hidrocarbonetos em forma gasosa ou líquida a partir de gás de síntese, e, para apreparação de hidrocarbonetos em forma líquida a partir de gás de síntese
US9856141B2 (en) * 2016-01-07 2018-01-02 Fluor Technologies Corporation Method for avoiding expensive sour water stripper metallurgy in a gasification plant

Also Published As

Publication number Publication date
PT68334A (de) 1978-07-31
BE869167A (fr) 1979-01-22
JPS5422403A (en) 1979-02-20
NO782519L (no) 1979-01-23
DE2733105B1 (de) 1979-01-18
YU175278A (en) 1982-06-30
NL7807723A (nl) 1979-01-24
GB2002809A (en) 1979-02-28
FR2398107A1 (fr) 1979-02-16
IT7850245A0 (it) 1978-07-11
IT1105096B (it) 1985-10-28
SE7807932L (sv) 1979-01-23

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