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GB1336730A - Process and apparatus for the separation of a starting mixture with the aid of multistage liquid-liquid extraction - Google Patents

Process and apparatus for the separation of a starting mixture with the aid of multistage liquid-liquid extraction

Info

Publication number
GB1336730A
GB1336730A GB5623870A GB5623870A GB1336730A GB 1336730 A GB1336730 A GB 1336730A GB 5623870 A GB5623870 A GB 5623870A GB 5623870 A GB5623870 A GB 5623870A GB 1336730 A GB1336730 A GB 1336730A
Authority
GB
United Kingdom
Prior art keywords
components
liquid
starting mixture
separation
readily soluble
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
GB5623870A
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 INT RESEARCH
Shell Internationale Research Maatschappij BV
Original Assignee
SHELL INT RESEARCH
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 INT RESEARCH, Shell Internationale Research Maatschappij BV filed Critical SHELL INT RESEARCH
Publication of GB1336730A publication Critical patent/GB1336730A/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D11/00Solvent extraction
    • B01D11/04Solvent extraction of solutions which are liquid
    • B01D11/0488Flow sheets
    • 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
    • C10G21/00Refining of hydrocarbon oils, in the absence of hydrogen, by extraction with selective solvents

Landscapes

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

Abstract

1336730 Liquid/liquid extraction SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ BV 26 Nov 1970 [28 Nov 1969] 56238/70 Heading B1F In a process for the separation of components in a liquid starting mixture introduced at 1 into a multistage liquid-liquid extractor 2 using a selective solvent boiling higher than the starting mixture and introduced at 3, in which solvent at least one of the components is more readily soluble and at least one of the other components is less readily than the other component or components, a raffinate phase containing predominantly the less readily soluble component or components is drawn off at 4, an extract phase containing predominantly the more readily soluble component or components is drawn off at 5 and passed to distiller 6, from which distiller two streams 13 and 17 are obtained which contain the less readily soluble component or components from the extract phase 5, stream 13 having a higher boiling range than stream 17, and stream 17 is recycled to the extractor 2 at a stage nearer to the extract discharge 5 than the stage at which starting mixture is supplied from 1. The separation of hydrocarbon is exemplified.
GB5623870A 1969-11-28 1970-11-26 Process and apparatus for the separation of a starting mixture with the aid of multistage liquid-liquid extraction Expired GB1336730A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
NL6917887.A NL165940C (en) 1969-11-28 1969-11-28 METHOD FOR SEPARATING A MIXTURE OF AROMATIC AND NON-AROMATIC HYDROCARBONS USING MULTI-STAGE LIQUID / LIQUID EXTRACTION AND APPARATUS SUITABLE FOR CARRYING OUT THE METHOD

Publications (1)

Publication Number Publication Date
GB1336730A true GB1336730A (en) 1973-11-07

Family

ID=19808500

Family Applications (1)

Application Number Title Priority Date Filing Date
GB5623870A Expired GB1336730A (en) 1969-11-28 1970-11-26 Process and apparatus for the separation of a starting mixture with the aid of multistage liquid-liquid extraction

Country Status (9)

Country Link
JP (1) JPS501472B1 (en)
BE (1) BE759133A (en)
CA (1) CA931329A (en)
DE (1) DE2058293A1 (en)
ES (1) ES385915A1 (en)
FR (1) FR2072378A5 (en)
GB (1) GB1336730A (en)
NL (1) NL165940C (en)
ZA (1) ZA708038B (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2177356C2 (en) * 1995-10-19 2001-12-27 Байер Аг Multistage three-phase extractor
RU2178326C2 (en) * 1995-10-19 2002-01-20 Байер Аг Method of multi-phase extraction

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4333824A (en) * 1980-06-27 1982-06-08 Texaco Inc. Refining highly aromatic lube oil stocks
FR2492366B1 (en) * 1980-10-21 1986-09-05 Sumitomo Chemical Co PROCESS FOR RECOVERING AROMATIC HYDROCARBONS BY EXTRACTION WITH A SOLVENT AS WELL AS BY EXTRACTIVE DISTILLATION AND FRACTIONAL DISTILLATION
US4519901A (en) * 1981-12-18 1985-05-28 Exxon Research & Engineering Co. Extractive separation process
US6565742B1 (en) * 1997-09-03 2003-05-20 Gtc Technology Inc. Aromatics separation process and method of retrofitting existing equipment for same
ES2161151B1 (en) * 1999-07-01 2002-07-01 Gomez Gines Sanchez Distillation of fluid by fractional diffusion in another fluid comprises variable circulation velocities generation via pipe carrying soluble fluid

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2177356C2 (en) * 1995-10-19 2001-12-27 Байер Аг Multistage three-phase extractor
RU2178326C2 (en) * 1995-10-19 2002-01-20 Байер Аг Method of multi-phase extraction

Also Published As

Publication number Publication date
NL6917887A (en) 1971-06-02
BE759133A (en) 1971-05-19
CA931329A (en) 1973-08-07
ES385915A1 (en) 1973-12-16
ZA708038B (en) 1971-08-25
NL165940B (en) 1981-01-15
JPS501472B1 (en) 1975-01-18
DE2058293A1 (en) 1971-06-03
NL165940C (en) 1981-06-15
FR2072378A5 (en) 1971-09-24

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Legal Events

Date Code Title Description
PS Patent sealed
PCNP Patent ceased through non-payment of renewal fee