FR2230583A1 - Synthesis gas generation - using triple orifice burner designed to prevent heat induced damage - Google Patents

Synthesis gas generation - using triple orifice burner designed to prevent heat induced damage

Info

Publication number
FR2230583A1
FR2230583A1 FR7318897A FR7318897A FR2230583A1 FR 2230583 A1 FR2230583 A1 FR 2230583A1 FR 7318897 A FR7318897 A FR 7318897A FR 7318897 A FR7318897 A FR 7318897A FR 2230583 A1 FR2230583 A1 FR 2230583A1
Authority
FR
France
Prior art keywords
gas
sec
synthesis gas
hydrocarbon
burner
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.)
Granted
Application number
FR7318897A
Other languages
French (fr)
Other versions
FR2230583B1 (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.)
Texaco Development Corp
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 FR7318897A priority Critical patent/FR2230583A1/en
Publication of FR2230583A1 publication Critical patent/FR2230583A1/en
Application granted granted Critical
Publication of FR2230583B1 publication Critical patent/FR2230583B1/fr
Granted 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
    • C01B3/363—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 characterised by the burner used

Abstract

Synthesis gas is generated by partial oxidn. of normally liq. hydrocarbon streams at 1800-3500 degrees F using a design of burner injection assembly having three separate convergent concentric nozzles. The oil and O2 contg. gas are injected at relative velocities through the two central orifices such that atomisation of the oil takes place downstream from the burner. The third outer annular stream carries the moderator gas (generally steam) which functions to minimise turbulence of the hot prod. synthesis gas. Typical flow rates are liq. hydrocarbon 10-100 ft./sec., O2-contg. gas 110-600 ft./sec., and moderator gas at 55-300 ft./sec.; relative velocity difference of hydrocarbon and oxygen streams is maintained at >=100 ft./sec. The design prevents damage to the burner head caused by erosion and corrosion effects due to the high temps. involved.
FR7318897A 1973-05-24 1973-05-24 Synthesis gas generation - using triple orifice burner designed to prevent heat induced damage Granted FR2230583A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
FR7318897A FR2230583A1 (en) 1973-05-24 1973-05-24 Synthesis gas generation - using triple orifice burner designed to prevent heat induced damage

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR7318897A FR2230583A1 (en) 1973-05-24 1973-05-24 Synthesis gas generation - using triple orifice burner designed to prevent heat induced damage

Publications (2)

Publication Number Publication Date
FR2230583A1 true FR2230583A1 (en) 1974-12-20
FR2230583B1 FR2230583B1 (en) 1977-08-05

Family

ID=9119919

Family Applications (1)

Application Number Title Priority Date Filing Date
FR7318897A Granted FR2230583A1 (en) 1973-05-24 1973-05-24 Synthesis gas generation - using triple orifice burner designed to prevent heat induced damage

Country Status (1)

Country Link
FR (1) FR2230583A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2556332A1 (en) * 1983-12-09 1985-06-14 Shell Int Research PROCESS FOR PRODUCING SYNTHESIS GAS FROM HYDROCARBON FUEL

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2155185A5 (en) * 1971-10-04 1973-05-18 Texaco Development Corp

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2155185A5 (en) * 1971-10-04 1973-05-18 Texaco Development Corp

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2556332A1 (en) * 1983-12-09 1985-06-14 Shell Int Research PROCESS FOR PRODUCING SYNTHESIS GAS FROM HYDROCARBON FUEL

Also Published As

Publication number Publication date
FR2230583B1 (en) 1977-08-05

Similar Documents

Publication Publication Date Title
KR970001467B1 (en) Fluidic burner
GB1299696A (en) Gas turbine engine aerating nozzle
GB1139004A (en) Improvements in or relating to combustion devices
GB1414428A (en)
CA1269842A (en) Process for producing synthesis gas from hydrocarbon fuel
GB1512677A (en) Quench chambers in coal gasification plant
MXPA01001222A (en) System for providing proximate turbulent and coherent gas jets.
FR2230583A1 (en) Synthesis gas generation - using triple orifice burner designed to prevent heat induced damage
GB1413996A (en) Synthesis gas generation
US4634370A (en) Flare
US4519321A (en) Burner for the partial combustion of solid fuel
KR860008257A (en) Annular nozzles and processes for their use
JPS60126521A (en) Fuel injection valve of combustor for gas turbine
JPH0451725B2 (en)
GB1410923A (en) Fluid fuel burners
US4729885A (en) High mixing reactor process
GB1070049A (en) Improvements in or relating to burners for the combustion of liquid fuels with oxygen
GB840914A (en) Rocket engines
ES344299A1 (en) Synthesis Gas Generation
ES410445A1 (en) Liquid jet nozzle
GB910679A (en) Improvements in or relating to propulsion nozzles
US2810433A (en) Burner for oil-fired gas generator
GB1046916A (en) Rocket combustion chamber and method of feeding liquid propellents thereto
SU727236A1 (en) Nozzle for spraying and injecting liquid
GB872600A (en) Improvements in combustion ducts

Legal Events

Date Code Title Description
ST Notification of lapse