ES347843A1 - Mixed-phase conversion product separation process - Google Patents

Mixed-phase conversion product separation process

Info

Publication number
ES347843A1
ES347843A1 ES347843A ES347843A ES347843A1 ES 347843 A1 ES347843 A1 ES 347843A1 ES 347843 A ES347843 A ES 347843A ES 347843 A ES347843 A ES 347843A ES 347843 A1 ES347843 A1 ES 347843A1
Authority
ES
Spain
Prior art keywords
stream
separating
liquid
liquid stream
vapour
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
ES347843A
Other languages
Spanish (es)
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.)
Universal Oil Products Co
Original Assignee
Universal Oil Products 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 Universal Oil Products Co filed Critical Universal Oil Products Co
Publication of ES347843A1 publication Critical patent/ES347843A1/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
    • C10G49/00Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00
    • C10G49/22Separation of effluents
    • 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
    • C10G5/00Recovery of liquid hydrocarbon mixtures from gases, e.g. natural gas

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)

Abstract

A process for separating a hot, mixed-phase conversion product effluent which contains hydrogen, normally liquid hydrocarbons and normally gaseous hydrocarbons, and which has been derived from the conversion of a hydrocarbon charge stock which boils above 400 F. comprises (a) separating said effluent in a first separation zone without substantial reduction in pressure to provide a first liquid stream and a first vapour stream, (b) cooling said first vapour stream to a temperature within a range of from 60 to 140 F., (c) separating the cooled first vapour stream in a second separating zone maintained at substantially the same pressure as said first separating zone, to provide a hydrogen-rich second vapour stream and a second liquid stream, (d) separating at least a portion of said first liquid stream in a third separation zone at a substantially reduced pressure, to provide a third liquid stream containing normally liquid hydrocarbons, and a third vapour stream, (e) cooling said third vapour stream and combining it with said second liquid stream, (f) separating the resulting mixture in a fourth separation zone maintained at a temperature within a range of from 60 to 140 F., to provide a fourth vapour stream containing normally gaseous hydrocarbons and a fourth liquid stream containing normally liquid hydrocarbons. A portion of the fourth liquid stream may be recycled to combine with the cooled first vapour stream a portion of the first liquid stream may be recycled to combine with the charge stock to the conversion zone. The process is described with reference to the conversion products of the hydrocracking of a black oil. Details of the hydrocracking process are given.
ES347843A 1966-11-30 1967-11-30 Mixed-phase conversion product separation process Expired ES347843A1 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US598067A US3371029A (en) 1966-11-30 1966-11-30 Mixed-phase conversion product separation process
OA53119A OA02549A (en) 1966-11-30 1967-12-06 A process for separating a mixed phase conversion product.
NL6717013A NL6717013A (en) 1966-11-30 1967-12-14

Publications (1)

Publication Number Publication Date
ES347843A1 true ES347843A1 (en) 1969-02-16

Family

ID=27351425

Family Applications (1)

Application Number Title Priority Date Filing Date
ES347843A Expired ES347843A1 (en) 1966-11-30 1967-11-30 Mixed-phase conversion product separation process

Country Status (13)

Country Link
US (1) US3371029A (en)
BE (1) BE707354A (en)
BR (1) BR6795153D0 (en)
CH (1) CH542276A (en)
DE (1) DE1645825A1 (en)
ES (1) ES347843A1 (en)
FR (1) FR1547873A (en)
GB (1) GB1197469A (en)
NL (1) NL6717013A (en)
OA (1) OA02549A (en)
SE (1) SE345870B (en)
TR (1) TR16585A (en)
YU (1) YU32372B (en)

Families Citing this family (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3437584A (en) * 1967-08-09 1969-04-08 Universal Oil Prod Co Method for converting heavy carbonaceous materials
US3437707A (en) * 1967-09-12 1969-04-08 Universal Oil Prod Co Process for aromatic alkylation and olefinic oligomerization
US3437708A (en) * 1967-09-12 1969-04-08 Universal Oil Prod Co Separation process for alkylated aromatic compounds and olefinic oligomerizaton products
US3437706A (en) * 1967-09-12 1969-04-08 Universal Oil Prod Co Process for aromatic alkylation and olefinic oligomerization
GB1276877A (en) * 1968-10-28 1972-06-07 Universal Oil Prod Co Process for the conversion and desulfurization of oil
US3617502A (en) * 1968-10-28 1971-11-02 Universal Oil Prod Co Desulfurization and conversion of hydrocarbonaceous black oils
US3594309A (en) * 1968-10-28 1971-07-20 Universal Oil Prod Co Conversion and desulfurization of hydrocarbonaceous black oils
US3549519A (en) * 1968-10-28 1970-12-22 Universal Oil Prod Co Mixed-phase thermal cracking process
US3546099A (en) * 1969-02-26 1970-12-08 Universal Oil Prod Co Method for separating the effluent from a hydrocarbon conversion process reaction zone
US3666658A (en) * 1970-11-23 1972-05-30 Universal Oil Prod Co Hydroprocessing product separation
US4159935A (en) * 1978-08-30 1979-07-03 Uop Inc. Conversion of hydrocarbonaceous black oils
US4159937A (en) * 1978-08-30 1979-07-03 Uop Inc. Mixed-phase reaction product effluent separation process
GB8807807D0 (en) * 1988-03-31 1988-05-05 Shell Int Research Process for separating hydroprocessed effluent streams
US5453177A (en) * 1994-01-27 1995-09-26 The M. W. Kellogg Company Integrated distillate recovery process
FR3046177B1 (en) * 2015-12-23 2018-02-02 Axens INSTALLATION AND METHOD COMPRISING IN COMMON THE COMPRESSION OF THE ACIDIC GASES OF THE HYDROCONVERSION OR HYDROTREATMENT UNIT AND THAT OF THE GASEOUS EFFLUENTS OF THE CATALYTIC CRACKING UNIT.
FR3046176A1 (en) * 2015-12-23 2017-06-30 Axens HYDROPROCESSING OR HYDROCONVERSION PROCESS WITH STRIPER AND LOW PRESSURE SEPARATOR BALL ON THE FRACTION SECTION
US10781380B2 (en) * 2015-12-29 2020-09-22 Uop Llc Process and apparatus for recovering hydrogen from hydroprocessed hot flash liquid
US10711205B2 (en) 2017-06-22 2020-07-14 Uop Llc Process for recovering hydroprocessed effluent with improved hydrogen recovery

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2007039342A1 (en) * 2005-09-26 2007-04-12 Symrise Gmbh & Co. Kg Intramolecular prins reaction and catalysts suitable therefor

Also Published As

Publication number Publication date
YU239567A (en) 1974-04-30
OA02549A (en) 1970-05-05
NL6717013A (en) 1969-06-17
CH542276A (en) 1973-11-15
BE707354A (en) 1968-04-01
SE345870B (en) 1972-06-12
YU32372B (en) 1974-10-31
DE1645825A1 (en) 1970-07-16
FR1547873A (en) 1968-11-29
BR6795153D0 (en) 1973-02-20
TR16585A (en) 1973-01-01
US3371029A (en) 1968-02-27
GB1197469A (en) 1970-07-08

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