SE7806994L - PARTIAL OXIDATION PROCESS - Google Patents

PARTIAL OXIDATION PROCESS

Info

Publication number
SE7806994L
SE7806994L SE7806994A SE7806994A SE7806994L SE 7806994 L SE7806994 L SE 7806994L SE 7806994 A SE7806994 A SE 7806994A SE 7806994 A SE7806994 A SE 7806994A SE 7806994 L SE7806994 L SE 7806994L
Authority
SE
Sweden
Prior art keywords
zone
steam
heat exchange
exchange
heat
Prior art date
Application number
SE7806994A
Other languages
Swedish (sv)
Other versions
SE413903B (en
Inventor
P L Paull
R Mccann
Original Assignee
Texaco Development Corp
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 Texaco Development Corp filed Critical Texaco Development Corp
Priority to SE7806994A priority Critical patent/SE413903B/en
Publication of SE7806994L publication Critical patent/SE7806994L/en
Publication of SE413903B publication Critical patent/SE413903B/en

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
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/46—Gasification of granular or pulverulent flues in suspension
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/72—Other features
    • C10J3/86—Other features combined with waste-heat boilers
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K3/00—Plants characterised by the use of steam or heat accumulators, or intermediate steam heaters, therein
    • F01K3/18—Plants characterised by the use of steam or heat accumulators, or intermediate steam heaters, therein having heaters
    • F01K3/185—Plants characterised by the use of steam or heat accumulators, or intermediate steam heaters, therein having heaters using waste heat from outside the plant
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22—STEAM GENERATION
    • F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B1/00—Methods of steam generation characterised by form of heating method
    • F22B1/02—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers
    • F22B1/18—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being a hot gas, e.g. waste gas such as exhaust gas of internal-combustion engines
    • F22B1/1838—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being a hot gas, e.g. waste gas such as exhaust gas of internal-combustion engines the hot gas being under a high pressure, e.g. in chemical installations

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Mechanical Engineering (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Energy (AREA)
  • Sustainable Development (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Hydrogen, Water And Hydrids (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

The invention relates to the use of the sensible heat from the outlet gases coming from the partial oxidation of a fuel, the said sensible heat being intended for the generation of superheated steam. According to the invention, the outlet gases coming from a gas generator 1, which are not cold, are led through two heat exchange zones 16,23, the water is converted into steam in the second of these zones 23, and the steam is superheated either in the first zone 16 by indirect heat exchange with the outlet gases, or in a third heat exchange zone 55 by indirect heat exchange with a liquid heat-exchange agent that has been heated up in the first zone by indirect heat exchange with the outlet gases. Part of the steam or the liquid heat-exchange agent may optionally be passed into the outlet gas stream through an opening 33 in the walls of the first zone 16A. <IMAGE>
SE7806994A 1978-06-19 1978-06-19 Preparation of a gas containing H2 and CO by the partial oxidation of a fuel containing carbon and hydrogen SE413903B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
SE7806994A SE413903B (en) 1978-06-19 1978-06-19 Preparation of a gas containing H2 and CO by the partial oxidation of a fuel containing carbon and hydrogen

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
SE7806994A SE413903B (en) 1978-06-19 1978-06-19 Preparation of a gas containing H2 and CO by the partial oxidation of a fuel containing carbon and hydrogen

Publications (2)

Publication Number Publication Date
SE7806994L true SE7806994L (en) 1979-12-20
SE413903B SE413903B (en) 1980-06-30

Family

ID=20335242

Family Applications (1)

Application Number Title Priority Date Filing Date
SE7806994A SE413903B (en) 1978-06-19 1978-06-19 Preparation of a gas containing H2 and CO by the partial oxidation of a fuel containing carbon and hydrogen

Country Status (1)

Country Link
SE (1) SE413903B (en)

Also Published As

Publication number Publication date
SE413903B (en) 1980-06-30

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