GB587704A - An improved process for the purification of organic liquids - Google Patents

An improved process for the purification of organic liquids

Info

Publication number
GB587704A
GB587704A GB15345A GB15345A GB587704A GB 587704 A GB587704 A GB 587704A GB 15345 A GB15345 A GB 15345A GB 15345 A GB15345 A GB 15345A GB 587704 A GB587704 A GB 587704A
Authority
GB
United Kingdom
Prior art keywords
column
line
withdrawn
recovered
base
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
GB15345A
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.)
Standard Oil Development Co
Original Assignee
Standard Oil Development 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 Standard Oil Development Co filed Critical Standard Oil Development Co
Priority to GB15345A priority Critical patent/GB587704A/en
Publication of GB587704A publication Critical patent/GB587704A/en
Expired legal-status Critical Current

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/34—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping with one or more auxiliary substances
    • B01D3/36—Azeotropic distillation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/001—Processes specially adapted for distillation or rectification of fermented solutions

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

<PICT:0587704/III/1> The process of the parent Specification is modified to enable organic liquids soluble in water, e.g., lower alcohols and ketones to be recovered continuously instead of batchwise by the provision of successive distillation columns 50, 60. The crude liquid is introduced through line 51 into distillation column 50 which is supplied at the base with live steam. Low boiling impurities, together with steam and some of the material to be recovered, are removed overhead as vapours, which are condensed in condenser 53 and separated into two liquid layers in decanter 54. The upper layer is partly returned as reflux to column 50 and the remainder sent to mixer 72. The lower aqueous layer is withdrawn through line 57 and added to the crude liquid supply. The liquid from the base of column 50 is passed through line 61 to column 60 which is supplied at the base with live steam. The material to be recovered is withdrawn, as vapour, overhead, condensed in condenser 63, and passed to drum 64; part of the condensate is returned as reflux to column 60 and the remainder is withdrawn to storage as product. The high boiling impurities are withdrawn throngh line 67 to decanter 68 from which the upper non-aqueous layer is removed through line 71 and sent to mixer 72 where mixing with the low boiling impurities from column 50 takes place. The mixture is introduced into wash tower 70 where it is countercurrently contacted with water, the aqueous extract so obtained being added to the crude liquid supply through line 75. A modification is described in which column 60 is heated by means of closed steam.
GB15345A 1945-01-02 1945-01-02 An improved process for the purification of organic liquids Expired GB587704A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB15345A GB587704A (en) 1945-01-02 1945-01-02 An improved process for the purification of organic liquids

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB15345A GB587704A (en) 1945-01-02 1945-01-02 An improved process for the purification of organic liquids

Publications (1)

Publication Number Publication Date
GB587704A true GB587704A (en) 1947-05-02

Family

ID=9699341

Family Applications (1)

Application Number Title Priority Date Filing Date
GB15345A Expired GB587704A (en) 1945-01-02 1945-01-02 An improved process for the purification of organic liquids

Country Status (1)

Country Link
GB (1) GB587704A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2561680A (en) * 1949-07-20 1951-07-24 Cities Service Oil Co Purification of methanol by azeotropic distillation
US2979672A (en) * 1957-05-21 1961-04-11 Philips Corp Trigger circuit arrangement
US3159553A (en) * 1961-04-27 1964-12-01 California Research Corp Method of separating methanol from a mixture thereof with water, xylene, and esters

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2561680A (en) * 1949-07-20 1951-07-24 Cities Service Oil Co Purification of methanol by azeotropic distillation
US2979672A (en) * 1957-05-21 1961-04-11 Philips Corp Trigger circuit arrangement
US3159553A (en) * 1961-04-27 1964-12-01 California Research Corp Method of separating methanol from a mixture thereof with water, xylene, and esters

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