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GB1463392A - Process for the production of olefinically unsaturated hydro carbons - Google Patents

Process for the production of olefinically unsaturated hydro carbons

Info

Publication number
GB1463392A
GB1463392A GB1135474A GB1135474A GB1463392A GB 1463392 A GB1463392 A GB 1463392A GB 1135474 A GB1135474 A GB 1135474A GB 1135474 A GB1135474 A GB 1135474A GB 1463392 A GB1463392 A GB 1463392A
Authority
GB
United Kingdom
Prior art keywords
cracking
zone
olefinically unsaturated
cracked
thermally
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
GB1135474A
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.)
Pullman Inc
Original Assignee
Pullman Inc
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 Pullman Inc filed Critical Pullman Inc
Publication of GB1463392A publication Critical patent/GB1463392A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G51/00Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only
    • C10G51/02Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only plural serial stages only
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2400/00Products obtained by processes covered by groups C10G9/00 - C10G69/14
    • C10G2400/20C2-C4 olefins

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

1463392 Olefins by two-stage cracking of hydrocarbon feedstock PULLMAN Inc 14 March 1974 [30 July 1973] 11354/74 Heading C5E A process for the production of olefinically unsaturated hydrocarbons comprises the steps of: (a) introducing a hydrocarbon feedstock comprising petroleum residium into the catalytic cracking zone of a heavy oil cracking unit in the presence of fluidized cracking catalyst at cracking conditions to produce a catalytically cracked effluent including a cracked naphtha fraction; (b) regenerating said fluidized cracking catalyst in the regeneration zone of the heavy oil cracking unit; (c) producing high pressure steam in said regeneration zone by indirect heat exchange; (d) passing the cracked naptha fraction to a thermal pyrolysis zone and thermally cracking said fraction to produce a thermally cracked effluent containing olefinically unsaturated hydrocarbons; (e) expanding said high pressure steam from step (c) to provide at least part of the gas compression energy required for recovery of the olefinically unsaturated hydrocarbons; and (f) recovering olefinicallyunsaturated hydrocarbons. A portion of the expanded high pressure steam may be mixed with the cracked naphtha fraction fed to the thermal pyrolysis zone. The cracking catalyst may be a zeolite and the catalytic cracking zone may be a transfer line reactor. Pyrolysis oil separated from the thermally cracked effluent may be recycled to the catalytic cracking zone. Pyrolysis gasoline separated from the thermally cracked effluent may be hydrotreated and recycled to the thermal pyrolysis zone.
GB1135474A 1973-07-30 1974-03-14 Process for the production of olefinically unsaturated hydro carbons Expired GB1463392A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US383620A US3862898A (en) 1973-07-30 1973-07-30 Process for the production of olefinically unsaturated hydrocarbons

Publications (1)

Publication Number Publication Date
GB1463392A true GB1463392A (en) 1977-02-02

Family

ID=23513955

Family Applications (1)

Application Number Title Priority Date Filing Date
GB1135474A Expired GB1463392A (en) 1973-07-30 1974-03-14 Process for the production of olefinically unsaturated hydro carbons

Country Status (18)

Country Link
US (1) US3862898A (en)
JP (1) JPS5037704A (en)
AR (1) AR214162A1 (en)
AT (1) AT340554B (en)
BE (1) BE817818A (en)
BR (1) BR7404967A (en)
CA (1) CA1013773A (en)
DE (1) DE2419436A1 (en)
DK (1) DK404774A (en)
ES (1) ES426794A1 (en)
FR (1) FR2239518B1 (en)
GB (1) GB1463392A (en)
IN (1) IN144320B (en)
NL (1) NL7405264A (en)
NO (1) NO742749L (en)
SE (1) SE391530B (en)
SU (1) SU650512A3 (en)
TR (1) TR18059A (en)

Families Citing this family (37)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4064038A (en) * 1973-05-21 1977-12-20 Universal Oil Products Company Fluid catalytic cracking process for conversion of residual oils
US4176084A (en) * 1975-07-08 1979-11-27 Exxon Research & Engineering Co. Process for regenerating metal-contaminated hydrocarbon conversion catalysts
US4009121A (en) * 1975-08-26 1977-02-22 Exxon Research And Engineering Company Method of temperature control in catalyst regeneration
CA1105406A (en) * 1976-04-29 1981-07-21 Fred S. Zrinscak, Sr. Catalytic cracking of metal-contaminated oils
US4162213A (en) * 1976-04-29 1979-07-24 Mobil Oil Corporation Catalytic cracking of metal-contaminated oils
US4143521A (en) * 1977-02-08 1979-03-13 Stone & Webster Engineering Corporation Process for the production of ethylene
US4444651A (en) * 1979-11-14 1984-04-24 Ashland Oil, Inc. Carbo-metallic oil conversion with controlled CO:CO2 ratio in multistage regeneration
JPS60179139A (en) * 1984-02-27 1985-09-13 Central Res Inst Of Electric Power Ind Apparatus for regenerating desulfurizing agent in purification of sulfide-containing gas
US4732740A (en) * 1984-10-09 1988-03-22 Stone & Webster Engineering Corporation Integrated heavy oil pyrolysis process
US4615795A (en) * 1984-10-09 1986-10-07 Stone & Webster Engineering Corporation Integrated heavy oil pyrolysis process
EP0344376A1 (en) * 1988-06-03 1989-12-06 Ching Piao Lin Process for converting heavy hydrocarbons to lighter hydrocarbons
US5087349A (en) * 1988-11-18 1992-02-11 Stone & Webster Engineering Corporation Process for selectively maximizing product production in fluidized catalytic cracking of hydrocarbons
US5120892A (en) * 1989-12-22 1992-06-09 Phillips Petroleum Company Method and apparatus for pyrolytically cracking hydrocarbons
US5944984A (en) * 1996-03-20 1999-08-31 Ormat Industries Ltd. Solvent deasphalting unit and method for using the same
US6033555A (en) * 1997-06-10 2000-03-07 Exxon Chemical Patents Inc. Sequential catalytic and thermal cracking for enhanced ethylene yield
ZA989153B (en) 1997-10-15 1999-05-10 Equistar Chem Lp Method of producing olefins and feedstocks for use in olefin production from petroleum residua which have low pentane insolubles and high hydrogen content
US6013852A (en) * 1997-11-21 2000-01-11 Shell Oil Company Producing light olefins from a contaminated liquid hydrocarbon stream by means of thermal cracking
FR2796078B1 (en) * 1999-07-07 2002-06-14 Bp Chemicals Snc PROCESS AND DEVICE FOR VAPOCRACKING HYDROCARBONS
EP1365004A1 (en) * 2002-05-23 2003-11-26 ATOFINA Research Production of olefins
JP4313237B2 (en) * 2004-03-29 2009-08-12 新日本石油株式会社 Hydrocracking catalyst and method for producing liquid hydrocarbon
WO2007114200A1 (en) * 2006-03-30 2007-10-11 Nippon Oil Corporation Hydrocracking catalyst and process for producing fuel substrate
US20070284285A1 (en) * 2006-06-09 2007-12-13 Terence Mitchell Stepanik Method of Upgrading a Heavy Oil Feedstock
US8658022B2 (en) 2010-11-23 2014-02-25 Equistar Chemicals, Lp Process for cracking heavy hydrocarbon feed
US8658019B2 (en) 2010-11-23 2014-02-25 Equistar Chemicals, Lp Process for cracking heavy hydrocarbon feed
US8663456B2 (en) 2010-11-23 2014-03-04 Equistar Chemicals, Lp Process for cracking heavy hydrocarbon feed
US9181146B2 (en) 2010-12-10 2015-11-10 Exxonmobil Chemical Patents Inc. Process for the production of xylenes and light olefins
US8658023B2 (en) * 2010-12-29 2014-02-25 Equistar Chemicals, Lp Process for cracking heavy hydrocarbon feed
US8937205B2 (en) 2012-05-07 2015-01-20 Exxonmobil Chemical Patents Inc. Process for the production of xylenes
US9181147B2 (en) 2012-05-07 2015-11-10 Exxonmobil Chemical Patents Inc. Process for the production of xylenes and light olefins
US8921633B2 (en) 2012-05-07 2014-12-30 Exxonmobil Chemical Patents Inc. Process for the production of xylenes and light olefins
US10603657B2 (en) 2016-04-11 2020-03-31 Saudi Arabian Oil Company Nano-sized zeolite supported catalysts and methods for their production
US11084992B2 (en) 2016-06-02 2021-08-10 Saudi Arabian Oil Company Systems and methods for upgrading heavy oils
US10301556B2 (en) * 2016-08-24 2019-05-28 Saudi Arabian Oil Company Systems and methods for the conversion of feedstock hydrocarbons to petrochemical products
US10689587B2 (en) 2017-04-26 2020-06-23 Saudi Arabian Oil Company Systems and processes for conversion of crude oil
JP2020527632A (en) 2017-07-17 2020-09-10 サウジ アラビアン オイル カンパニーSaudi Arabian Oil Company Systems and methods for processing heavy oils
CN111116292A (en) * 2018-10-30 2020-05-08 中国石油化工股份有限公司 Method and device for preparing low-carbon olefin from petroleum hydrocarbon
CN115698232A (en) * 2020-04-20 2023-02-03 埃克森美孚化学专利公司 Hydrocarbon Pyrolysis of Nitrogen-Containing Feeds

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2421615A (en) * 1943-12-28 1947-06-03 Standard Oil Dev Co Treating hydrocarbon fluids
US2521757A (en) * 1945-12-15 1950-09-12 Houdry Process Corp Conversion of heavy hydrocarbon materials
US2853455A (en) * 1952-09-09 1958-09-23 Sinclair Refining Co Method of temperature control in fluid catalyst regenerator units
NL251595A (en) * 1959-05-15 1900-01-01
US3401124A (en) * 1964-10-26 1968-09-10 Exxon Research Engineering Co Recovering energy from flue gas
US3532620A (en) * 1967-09-28 1970-10-06 Sinclair Research Inc Power recovery from catalyst regeneration gases

Also Published As

Publication number Publication date
BE817818A (en) 1974-11-18
FR2239518A1 (en) 1975-02-28
SU650512A3 (en) 1979-02-28
NO742749L (en) 1975-02-24
ATA620374A (en) 1977-04-15
BR7404967A (en) 1976-02-17
SE391530B (en) 1977-02-21
DE2419436A1 (en) 1975-02-13
TR18059A (en) 1976-09-10
NL7405264A (en) 1975-02-03
US3862898A (en) 1975-01-28
JPS5037704A (en) 1975-04-08
SE7409669L (en) 1975-01-31
ES426794A1 (en) 1976-07-16
CA1013773A (en) 1977-07-12
DK404774A (en) 1975-04-07
FR2239518B1 (en) 1977-10-14
AU7122674A (en) 1976-01-15
AR214162A1 (en) 1979-05-15
IN144320B (en) 1978-04-29
AT340554B (en) 1977-12-27

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Legal Events

Date Code Title Description
PS Patent sealed [section 19, patents act 1949]
746 Register noted 'licences of right' (sect. 46/1977)
PCNP Patent ceased through non-payment of renewal fee