AU7979187A - Converting a stream containing heavy hydrocarbons into a stream containing hydrocarbons having a lower boiling range - Google Patents

Converting a stream containing heavy hydrocarbons into a stream containing hydrocarbons having a lower boiling range

Info

Publication number
AU7979187A
AU7979187A AU79791/87A AU7979187A AU7979187A AU 7979187 A AU7979187 A AU 7979187A AU 79791/87 A AU79791/87 A AU 79791/87A AU 7979187 A AU7979187 A AU 7979187A AU 7979187 A AU7979187 A AU 7979187A
Authority
AU
Australia
Prior art keywords
stream
stream containing
hydrocarbons
converting
boiling range
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
AU79791/87A
Other versions
AU593950B2 (en
Inventor
Petrus Matthias Marie Blauwhoff
Eduard Philip Kieffer
Robert Hendrik Van Dongen
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.)
Shell Internationale Research Maatschappij BV
Original Assignee
Shell Internationale Research Maatschappij BV
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 Shell Internationale Research Maatschappij BV filed Critical Shell Internationale Research Maatschappij BV
Publication of AU7979187A publication Critical patent/AU7979187A/en
Application granted granted Critical
Publication of AU593950B2 publication Critical patent/AU593950B2/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING 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
    • C10G65/00—Treatment of hydrocarbon oils by two or more hydrotreatment processes only
    • C10G65/02—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only
    • C10G65/10—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only cracking steps
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING 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
    • C10G65/00—Treatment of hydrocarbon oils by two or more hydrotreatment processes only
    • C10G65/02—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only
    • C10G65/12—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including cracking steps and other hydrotreatment steps

Abstract

Process for converting a stream containing heavy hydrocarbons comprising the steps of a) passing through a first conversion reactor (1) containing a conversion catalyst in the presence of hydrogen the stream at a temperature between 325 and 600 DEG C, a pressure between 1 and 30 MPa and at an hourly space velocity between 0.05 and 5 kg/1/hour to produce a primary converted stream; b) passing the primary converted stream to a first gas/liquid separator (4) and removing from the first gas/liquid separator (4) a gaseous stream and a liquid stream; c) passing the gaseous stream to a second conversion reactor (7); and d) passing through the second conversion reactor (7) containing a conversion catalyst in the presence of hydrogen the gaseous stream at a temperature between 325 and 600 DEG C, a pressure between 1 and 30 MPa and at an hourly space velocity between 0.1 and 10 kg/l/hour to produce a further converted stream having a lower boiling range. ;
AU79791/87A 1986-10-17 1987-10-15 Converting a stream containing heavy hydrocarbons into a stream containing hydrocarbons having a lower boiling range Ceased AU593950B2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB868624952A GB8624952D0 (en) 1986-10-17 1986-10-17 Converting stream containing heavy hydrocarbons into stream
GB8624952 1986-10-17

Publications (2)

Publication Number Publication Date
AU7979187A true AU7979187A (en) 1988-04-21
AU593950B2 AU593950B2 (en) 1990-02-22

Family

ID=10605932

Family Applications (1)

Application Number Title Priority Date Filing Date
AU79791/87A Ceased AU593950B2 (en) 1986-10-17 1987-10-15 Converting a stream containing heavy hydrocarbons into a stream containing hydrocarbons having a lower boiling range

Country Status (11)

Country Link
EP (1) EP0264158B1 (en)
JP (1) JP2932182B2 (en)
CN (1) CN1016966B (en)
AT (1) ATE66485T1 (en)
AU (1) AU593950B2 (en)
BR (1) BR8705511A (en)
CA (1) CA1297064C (en)
DE (1) DE3772319D1 (en)
ES (1) ES2024495B3 (en)
GB (1) GB8624952D0 (en)
GR (1) GR3002673T3 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8137531B2 (en) 2003-11-05 2012-03-20 Chevron U.S.A. Inc. Integrated process for the production of lubricating base oils and liquid fuels from Fischer-Tropsch materials using split feed hydroprocessing
WO2016102247A1 (en) 2014-12-22 2016-06-30 Sabic Global Technologies B.V. Process for producing c2 and c3 hydrocarbons
CN107109257A (en) 2014-12-22 2017-08-29 沙特基础工业全球技术有限公司 Method for producing C2 and C3 hydrocarbon

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3506566A (en) * 1968-05-20 1970-04-14 Sinclair Research Inc Conversion of clarified hydrocarbon oil to distillate hydrocarbon fuel oil of low pour point in two catalytic stages
BE793384A (en) * 1971-12-27 1973-06-27 Texaco Development Corp HYDROCRACKING PROCESS FOR THE CONVERSION OF HEAVY HYDROCARBONS IN GASOLINE WITH LOW SULFUR CONTENT
US3992283A (en) * 1974-09-23 1976-11-16 Universal Oil Products Company Hydrocracking process for the maximization of an improved viscosity lube oil
US4082647A (en) * 1976-12-09 1978-04-04 Uop Inc. Simultaneous and continuous hydrocracking production of maximum distillate and optimum lube oil base stock
US4158622A (en) * 1978-02-08 1979-06-19 Cogas Development Company Treatment of hydrocarbons by hydrogenation and fines removal
JPH0237389B2 (en) * 1981-08-20 1990-08-23 Jgc Corp ITSURYUGATAKOATSUEKISOSUISOKATOKOATSUKISOSUISOKATONOCHOKURETSUKOTEINYORISOJUSHITSUYUKARAKEISHITSUYUOSEIZOSURUHOHO
EP0128250A1 (en) * 1983-06-08 1984-12-19 Mobil Oil Corporation Catalytic dewaxing process
AU586980B2 (en) * 1984-10-29 1989-08-03 Mobil Oil Corporation An improved process and apparatus for the dewaxing of heavy distillates and residual liquids

Also Published As

Publication number Publication date
CN87106905A (en) 1988-06-22
EP0264158B1 (en) 1991-08-21
AU593950B2 (en) 1990-02-22
GR3002673T3 (en) 1993-01-25
BR8705511A (en) 1988-05-24
JPS63110286A (en) 1988-05-14
CA1297064C (en) 1992-03-10
JP2932182B2 (en) 1999-08-09
CN1016966B (en) 1992-06-10
EP0264158A1 (en) 1988-04-20
ATE66485T1 (en) 1991-09-15
ES2024495B3 (en) 1992-03-01
GB8624952D0 (en) 1986-11-19
DE3772319D1 (en) 1991-09-26

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Legal Events

Date Code Title Description
MK14 Patent ceased section 143(a) (annual fees not paid) or expired