GB777325A - Process and apparatus for the production of synthesis gas comprising hydrogen and carbon monoxide - Google Patents

Process and apparatus for the production of synthesis gas comprising hydrogen and carbon monoxide

Info

Publication number
GB777325A
GB777325A GB5458/53A GB545853A GB777325A GB 777325 A GB777325 A GB 777325A GB 5458/53 A GB5458/53 A GB 5458/53A GB 545853 A GB545853 A GB 545853A GB 777325 A GB777325 A GB 777325A
Authority
GB
United Kingdom
Prior art keywords
catalyst
inlet
reaction chamber
bed
cooling
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
GB5458/53A
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.)
Dr C Otto and Co GmbH
Original Assignee
Dr C Otto and Co GmbH
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 Dr C Otto and Co GmbH filed Critical Dr C Otto and Co GmbH
Publication of GB777325A publication Critical patent/GB777325A/en
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
    • C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
    • C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
    • C01B3/38—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
    • C01B3/386—Catalytic partial combustion
    • 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
    • C01B2203/02—Processes for making hydrogen or synthesis gas
    • C01B2203/025—Processes for making hydrogen or synthesis gas containing a partial oxidation step
    • C01B2203/0261—Processes for making hydrogen or synthesis gas containing a partial oxidation step containing a catalytic partial oxidation step [CPO]
    • 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
    • C01B2203/08—Methods of heating or cooling
    • C01B2203/0872—Methods of cooling
    • C01B2203/0883—Methods of cooling by indirect heat exchange
    • 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
    • C01B2203/10—Catalysts for performing the hydrogen forming reactions
    • C01B2203/1005—Arrangement or shape of catalyst
    • C01B2203/1011—Packed bed of catalytic structures, e.g. particles, packing elements
    • 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
    • C01B2203/10—Catalysts for performing the hydrogen forming reactions
    • C01B2203/1005—Arrangement or shape of catalyst
    • C01B2203/1011—Packed bed of catalytic structures, e.g. particles, packing elements
    • C01B2203/1017—Packed bed of catalytic structures, e.g. particles, packing elements characterised by the form of the structure
    • 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
    • C01B2203/10—Catalysts for performing the hydrogen forming reactions
    • C01B2203/1005—Arrangement or shape of catalyst
    • C01B2203/1035—Catalyst coated on equipment surfaces, e.g. reactor walls
    • 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
    • C01B2203/12—Feeding the process for making hydrogen or synthesis gas
    • C01B2203/1276—Mixing of different feed components

Abstract

<PICT:0777325/III/1> In the production of synthesis gas by the reaction of hydrocarbons and a gas containing oxygen in a reaction chamber containing a catalyst bed at a high temperature, undesired reactions are prevented and the desired reaction is controlled by feeding the reactants to the catalyst bed at a rate of flow above that at which he undesired reactions take place and optionally above the speed of ignition, cooling the reactants prior to their introduction into the reaction chamber, the cooling being to a temperature below that of ignition when the rate of flow is below the speed of ignition, and providing the reaction chamber with an internal coating of catalytically active material at those parts contacted by the reactants. As shown air introduced through inlet 1 is mixed first with oxygen from inlet 2 and then with a hydrocarbon gas from inlet 6. The resulting mixture is cooled by passing in spiral flow around a centre tube 10 which is surrounded by a coil 12, cooling water being passed through the central tube and surrounding coil via inlet 7 and outlet 13. The cooled mixture passes into a reaction chamber 18 which is lined with active catalyst material 14 and contains a catalyst bed 17. Movement of the mixing and cooling assembly with respect to the reaction chamber is made possible by stuffing box 15 and flexible connexions 16. The bed of catalyst may be arranged so that the size of the individual grains or the like of the catalyst decreases from the inlet to the outlet of the bed. Alternatively or in addition, when the catalyst consists of a catalyst and a carrier therefor, the concentration of the catalyst on the carrier may be increased from the inlet to the outlet. Inert refractory material may be placed at the inlet.
GB5458/53A 1952-03-01 1953-02-26 Process and apparatus for the production of synthesis gas comprising hydrogen and carbon monoxide Expired GB777325A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
AT777325X 1952-03-01

Publications (1)

Publication Number Publication Date
GB777325A true GB777325A (en) 1957-06-19

Family

ID=3680781

Family Applications (1)

Application Number Title Priority Date Filing Date
GB5458/53A Expired GB777325A (en) 1952-03-01 1953-02-26 Process and apparatus for the production of synthesis gas comprising hydrogen and carbon monoxide

Country Status (5)

Country Link
BE (1) BE517947A (en)
DE (1) DE952436C (en)
FR (1) FR1071555A (en)
GB (1) GB777325A (en)
NL (1) NL100615C (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU682751B2 (en) * 1994-03-25 1997-10-16 Exxon Research And Engineering Company Synthesis gas preparation by partial oxidation-steam reforming
US5824121A (en) * 1994-10-28 1998-10-20 Krupp Koppers Gmbh Apparatus for the pressure gasification of finely divided fuels

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE973776C (en) * 1954-03-08 1960-06-02 Power Gas Ltd Process for producing flammable gases
BE566186A (en) * 1957-04-18

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE558430C (en) * 1926-06-27 1932-09-07 I G Farbenindustrie Akt Ges Process for the production of hydrogen or nitrogen-hydrogen mixtures from hydrocarbons
DE653776C (en) * 1930-10-11 1937-12-03 Herbert Ritter Dr Production of nitrogen-hydrogen mixtures
DE616976C (en) * 1931-02-28
DE613507C (en) * 1932-05-25 1935-05-21 Hans Schmalfeldt Dipl Ing Furnace for the production of hydrogen by converting gases containing hydrocarbons
FR837904A (en) * 1937-06-16 1939-02-23 Metallgesellschaft Ag Apparatus for performing chemical reactions
FR976553A (en) * 1942-04-18 1951-03-20 Azote Office Nat Ind Process for the production of hydrogen and carbon monoxide

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU682751B2 (en) * 1994-03-25 1997-10-16 Exxon Research And Engineering Company Synthesis gas preparation by partial oxidation-steam reforming
US5824121A (en) * 1994-10-28 1998-10-20 Krupp Koppers Gmbh Apparatus for the pressure gasification of finely divided fuels

Also Published As

Publication number Publication date
FR1071555A (en) 1954-09-02
DE952436C (en) 1956-11-15
NL100615C (en)
BE517947A (en)

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