GB1378023A - Gasification process - Google Patents

Gasification process

Info

Publication number
GB1378023A
GB1378023A GB144872A GB144872A GB1378023A GB 1378023 A GB1378023 A GB 1378023A GB 144872 A GB144872 A GB 144872A GB 144872 A GB144872 A GB 144872A GB 1378023 A GB1378023 A GB 1378023A
Authority
GB
United Kingdom
Prior art keywords
zone
coke
gas
line
steam
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
GB144872A
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.)
ExxonMobil Technology and Engineering Co
Original Assignee
Exxon Research and Engineering Co
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 Exxon Research and Engineering Co filed Critical Exxon Research and Engineering Co
Priority to US00294560A priority Critical patent/US3798483A/en
Publication of GB1378023A publication Critical patent/GB1378023A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10BDESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B55/00Coking mineral oils, bitumen, tar, and the like or mixtures thereof with solid carbonaceous material
    • C10B55/02Coking mineral oils, bitumen, tar, and the like or mixtures thereof with solid carbonaceous material with solid materials
    • C10B55/04Coking mineral oils, bitumen, tar, and the like or mixtures thereof with solid carbonaceous material with solid materials with moving solid materials
    • C10B55/08Coking mineral oils, bitumen, tar, and the like or mixtures thereof with solid carbonaceous material with solid materials with moving solid materials in dispersed form
    • C10B55/10Coking mineral oils, bitumen, tar, and the like or mixtures thereof with solid carbonaceous material with solid materials with moving solid materials in dispersed form according to the "fluidised bed" technique
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/46Gasification of granular or pulverulent flues in suspension
    • C10J3/48Apparatus; Plants
    • C10J3/482Gasifiers with stationary fluidised bed
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/46Gasification of granular or pulverulent flues in suspension
    • C10J3/48Apparatus; Plants
    • C10J3/485Entrained flow gasifiers
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00Details of gasification processes
    • C10J2300/09Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0913Carbonaceous raw material
    • C10J2300/093Coal
    • C10J2300/0933Coal fines for producing water gas
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00Details of gasification processes
    • C10J2300/09Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0983Additives
    • C10J2300/0993Inert particles, e.g. as heat exchange medium in a fluidized or moving bed, heat carriers, sand

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Combustion & Propulsion (AREA)
  • Dispersion Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Materials Engineering (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Coke Industry (AREA)

Abstract

1378023 Water gas; cooking EXXON RESEARCH & ENG CO 12 Jan 1972 [22 Jan 1971] 1448/72 Heading C5E Fuel gas is made from coke in a reactor which comprises a single vessel (110) divided into three zones (111, 112, and 113), by a process comprising (a) introducing heated coke from step (d) into a fluidized gasifying bed at 1600‹ to 2200‹ F. in the lower zone (112) to contact steam and an oxygen-containing gas; (b) passing the resulting hot gas to the intermediate zone (111); (c) introducing cool coke into this zone to heat the coke to at least 1050‹ F. and cool the gas at least to 1800‹ F., the gas velocity being high enough to lift the coke to the upper zone (113); (d) passing the cooled gas and heated coke to the upper zone and there disengaging them; and (e) recovering the cooled gas from the disengaging zone. As shown, a petroleum residuum is coked in the coker 101, and the resulting coke is removed by line 107 and transferred to the reactor 110 by steam introduced at 108. Air or oxygen may be injected at 109 to control the temperature. The coke is carried upwards through the zone 111 and heated by hot gases from the lower zone 112. It is disengaged from the gas by baffles 114 and cyclones 115, and part of it, controlled by a slide valve 119, passes into the gasifying zone 112. Here it is gasified by contact with air or oxygen from line 123 and steam from line 124. The resulting hot gas passes up through the zone 111, where it is cooled, and out through the cyclones 115. Line 120 controls the level of the fluidized bed in zone 112, by taking off any excess coke for recirculation. Another part of the hot coke in the zone 113 is taken off by the line 117, where steam is injected from line 118 to convey it back to the coker, where it supplies the heat needed for coking.
GB144872A 1970-05-20 1972-01-12 Gasification process Expired GB1378023A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US00294560A US3798483A (en) 1970-05-20 1972-10-03 Gaseous discharge display device with a layer of electrically resistant material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US10870971A 1971-01-22 1971-01-22

Publications (1)

Publication Number Publication Date
GB1378023A true GB1378023A (en) 1974-12-18

Family

ID=22323637

Family Applications (1)

Application Number Title Priority Date Filing Date
GB144872A Expired GB1378023A (en) 1970-05-20 1972-01-12 Gasification process

Country Status (7)

Country Link
US (1) US3759676A (en)
JP (1) JPS5544792B1 (en)
CA (1) CA968290A (en)
DE (1) DE2202394A1 (en)
GB (1) GB1378023A (en)
IT (1) IT946811B (en)
NL (1) NL7200893A (en)

Families Citing this family (22)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4203759A (en) * 1978-05-01 1980-05-20 Exxon Research & Engineering Co. Process for the preparation of a vanadium-containing metallic ash concentrate
DE3023297C2 (en) * 1980-06-21 1988-05-05 International Minerals & Chemical Luxembourg S.A., 2010 Luxembourg Process for the production of a preliminary product for the production of silicon carbide
JPS59103839A (en) * 1982-11-22 1984-06-15 松下電器産業株式会社 Prefabricated packing box for crisper
US5106587A (en) * 1987-08-11 1992-04-21 Stone & Webster Engineering Corp. Particulate solids cracking apparatus
US20020179493A1 (en) * 1999-08-20 2002-12-05 Environmental & Energy Enterprises, Llc Production and use of a premium fuel grade petroleum coke
US7513260B2 (en) * 2006-05-10 2009-04-07 United Technologies Corporation In-situ continuous coke deposit removal by catalytic steam gasification
US8361310B2 (en) * 2006-11-17 2013-01-29 Etter Roger G System and method of introducing an additive with a unique catalyst to a coking process
US8206574B2 (en) 2006-11-17 2012-06-26 Etter Roger G Addition of a reactor process to a coking process
US9011672B2 (en) 2006-11-17 2015-04-21 Roger G. Etter System and method of introducing an additive with a unique catalyst to a coking process
EP2097498A4 (en) 2006-11-17 2012-09-05 Roger G Etter Selective cracking and coking of undesirable components in coker recycle and gas oils
US8372264B2 (en) * 2006-11-17 2013-02-12 Roger G. Etter System and method for introducing an additive into a coking process to improve quality and yields of coker products
RU2688547C2 (en) 2014-06-20 2019-05-21 ЭкссонМобил Рисерч энд Энджиниринг Компани Coking in a fluidized bed to obtain fuel gas
FR3044014B1 (en) * 2015-11-20 2020-02-14 Haffner Energy THERMOLYSIS DEVICE AND METHOD
US10626338B2 (en) 2016-12-15 2020-04-21 Exxonmobil Research And Engineering Company Efficient process for converting heavy oil to gasoline
US10407631B2 (en) 2017-11-14 2019-09-10 Exxonmobil Research And Engineering Company Gasification with enriched oxygen for production of synthesis gas
WO2019099248A1 (en) 2017-11-14 2019-05-23 Exxonmobil Research And Engineering Company Fluidized coking with increased production of liquids
US10400177B2 (en) 2017-11-14 2019-09-03 Exxonmobil Research And Engineering Company Fluidized coking with increased production of liquids
WO2020041001A1 (en) 2018-08-22 2020-02-27 Exxonmobil Research And Engineering Company Waste upgrading and related systems
US10703984B2 (en) 2018-11-09 2020-07-07 Exxonmobil Research And Engineering Company Fluidized coking with oxygen-containing stripping gas
WO2021086509A1 (en) 2019-11-01 2021-05-06 Exxonmobil Chemical Patents Inc. Processes and systems for quenching pyrolysis effluents
WO2021150285A1 (en) 2020-01-20 2021-07-29 Exxonmobil Research And Engineering Company Ethanol production methods and systems that integrate flexicoking and fermentation
US11014810B1 (en) 2020-01-29 2021-05-25 Exxonmobil Research And Engineering Company Carbon capture, waste upgrade, and chemicals production using improved flexicoking

Also Published As

Publication number Publication date
IT946811B (en) 1973-05-21
US3759676A (en) 1973-09-18
CA968290A (en) 1975-05-27
DE2202394A1 (en) 1972-08-03
JPS5544792B1 (en) 1980-11-14
NL7200893A (en) 1972-07-25

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Legal Events

Date Code Title Description
PS Patent sealed [section 19, patents act 1949]
PCNP Patent ceased through non-payment of renewal fee