GB716710A - A process for the production of combustible gases from liquid or gaseous fuels - Google Patents

A process for the production of combustible gases from liquid or gaseous fuels

Info

Publication number
GB716710A
GB716710A GB5907/51A GB590751A GB716710A GB 716710 A GB716710 A GB 716710A GB 5907/51 A GB5907/51 A GB 5907/51A GB 590751 A GB590751 A GB 590751A GB 716710 A GB716710 A GB 716710A
Authority
GB
United Kingdom
Prior art keywords
regenerator
oxygen
steam
oil
gas
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
GB5907/51A
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.)
Heinrich Koppers GmbH
Original Assignee
Heinrich Koppers 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 Heinrich Koppers GmbH filed Critical Heinrich Koppers GmbH
Publication of GB716710A publication Critical patent/GB716710A/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
    • C01B3/36—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 oxygen or 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
    • 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
    • C01B3/46—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 discontinuously preheated non-moving solid materials, e.g. blast and run
    • 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
    • Y02P20/10—Process efficiency
    • Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Inorganic Chemistry (AREA)
  • Hydrogen, Water And Hydrids (AREA)

Abstract

716,710. Oil gas; cracking gaseous mixtures. KOPPERS GES., H. March 12, 1951 [March 15, 1950; Aug. 31, 1950; Feb. 27, 1951], No. 5907/51. Class 55 (2) In a process for the production of gas having a high content of carbon monoxide and hydrogen which may be used as town's gas or for synthesis purposes, liquid fue's such as mineral oils or tar or gaseous hydrocarbons are reacted or reformed with preheated steam and oxygen in a regenerator system operating with alternating direction of flow. The apparatus consists of two preheating regenerators 1 and 2 connected by ducts 16 to a reaction heat regenerator 3. Combustion chambers 4 and 5, into which heating fuel may be atomized through nozzles 6 and 7, are provided at the tops of regenerators 1 and 2 respectively. Regenerator 3 is divided by a mid-partition 17 into two vertical compartments into which gasmaking oil may be atomized from nozzles 8 and 9. In operation, steam and oxygen are admitted at 12 into regenerator 1, which has been heated during a previous cycle, and flow into regenerator 3. into which oil is injected through nozzle 9. The oil vaporizes and passes with the steam and oxygen through the regenerator wherein it is cracked and reacts with the steam and oxygen to form permanent gases. The gases pass through regenerator 2 which abstracts part of their heat and discharge to storage at 15. When regenerator 1 has cooled to below gas-making temperature, the " run " is stopped and a heating period commenced, air being admitted to regenerator 1 at 13 and liquid fuel at 6, the resulting combustion gases heating regenerators 3 and 2 and discharging at 14. The " run now takes place in the opposite direction, steam and oxygen being admitted to regenerator 2 at 12 and oil at 8, the cycle being completed by a heating period with gas flow in the same direction.
GB5907/51A 1950-03-15 1951-03-12 A process for the production of combustible gases from liquid or gaseous fuels Expired GB716710A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE716710X 1950-03-15

Publications (1)

Publication Number Publication Date
GB716710A true GB716710A (en) 1954-10-13

Family

ID=6626498

Family Applications (1)

Application Number Title Priority Date Filing Date
GB5907/51A Expired GB716710A (en) 1950-03-15 1951-03-12 A process for the production of combustible gases from liquid or gaseous fuels

Country Status (1)

Country Link
GB (1) GB716710A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1631535A2 (en) * 2003-02-28 2006-03-08 ExxonMobil Research and Engineering Company Hydrocarbon synthesis process using pressure swing reforming

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1631535A2 (en) * 2003-02-28 2006-03-08 ExxonMobil Research and Engineering Company Hydrocarbon synthesis process using pressure swing reforming
EP1631535B1 (en) * 2003-02-28 2016-07-13 ExxonMobil Research and Engineering Company Hydrocarbon synthesis process using pressure swing reforming

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