GB1257558A - - Google Patents

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Publication number
GB1257558A
GB1257558A GB1257558DA GB1257558A GB 1257558 A GB1257558 A GB 1257558A GB 1257558D A GB1257558D A GB 1257558DA GB 1257558 A GB1257558 A GB 1257558A
Authority
GB
United Kingdom
Prior art keywords
glycol
column
tray
water
purification
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
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 filed Critical
Publication of GB1257558A publication Critical patent/GB1257558A/en
Expired legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C43/00Ethers; Compounds having groups, groups or groups
    • C07C43/02Ethers
    • C07C43/03Ethers having all ether-oxygen atoms bound to acyclic carbon atoms
    • C07C43/04Saturated ethers
    • C07C43/10Saturated ethers of polyhydroxy compounds
    • C07C43/11Polyethers containing —O—(C—C—O—)n units with ≤ 2 n≤ 10

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

1,257,558. Glycols, purification by distillation. UNION CARBIDE CORP. 21 Aug., 1969 [22 Aug., 1968], No. 41755/69. Heading BIB. [Also in Division C2] A glycol of the formula: in which R is H, CH 3 or C 2 H 5 and n is 1, 2, 3, or 4, is purified by feeding the impure glycol into a fractionating column wherein it is distilled under reflux in the presence of water so that there is at least 40% by weight of water at the glycol feed point and in part of the lower section of the column, the pressure being maintained at a value from 50 to 760mm Hg absolute, whereby the impurities distil off with water, and recovering the purified glycol from the bottoms fraction by distillation in a further column. If the impure glycol contains hydrolyzable impurities, a mineral acid is added to the first column in order to maintain the liquid in the lower section at a pH between 2 and 5; but the pH of the bottoms fraction is adjusted to a pH greater than 7 prior to further distillation. An example relates to the purification of spent monoethylene glycol containing terephthalic acid, terephthalic ester and carbonyl compounds. The spent glycol was mixed with an equal amount of ion-exchanged water and introduced as hot feed (75‹C) to the 10th tray (above the kettle) of a 20-tray oldershaw column. The bottoms fraction, consisting essentially of dry monoethylene glycol and minor amounts of diethylene glycol and triethylene glycol, was introduced to the 5th tray of a 15-tray oldershaw column. Purified monoethylene glycol was withdrawn as a liquid sidestream from the 10th tray. Other examples relate to the purification of diethylene glycol containing typical impurities generated during the manufacture of the glycol.
GB1257558D 1968-08-22 1969-08-21 Expired GB1257558A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US75473668A 1968-08-22 1968-08-22
BE746639 1970-02-27

Publications (1)

Publication Number Publication Date
GB1257558A true GB1257558A (en) 1971-12-22

Family

ID=25656797

Family Applications (1)

Application Number Title Priority Date Filing Date
GB1257558D Expired GB1257558A (en) 1968-08-22 1969-08-21

Country Status (5)

Country Link
BE (2) BE737770A (en)
DE (1) DE1942094A1 (en)
FR (1) FR2017970A1 (en)
GB (1) GB1257558A (en)
NL (1) NL6912836A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6514388B1 (en) 1998-09-23 2003-02-04 Basf Aktiengesellschaft Method for producing highly pure monoethylene glycol
US6605192B1 (en) 1998-09-23 2003-08-12 Basf Aktiengesellschaft Method for producing highly pure monoethylene glycol
EP3755682B1 (en) 2018-02-21 2023-01-18 Shell Internationale Research Maatschappij B.V. Stabilization of polyhydric alcohols by steam injection

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4830712A (en) * 1987-09-29 1989-05-16 Union Carbide Corporation Process for refining ethylene glycol

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6514388B1 (en) 1998-09-23 2003-02-04 Basf Aktiengesellschaft Method for producing highly pure monoethylene glycol
US6605192B1 (en) 1998-09-23 2003-08-12 Basf Aktiengesellschaft Method for producing highly pure monoethylene glycol
EP3755682B1 (en) 2018-02-21 2023-01-18 Shell Internationale Research Maatschappij B.V. Stabilization of polyhydric alcohols by steam injection

Also Published As

Publication number Publication date
BE737770A (en) 1970-02-23
DE1942094A1 (en) 1970-02-26
NL6912836A (en) 1970-02-24
FR2017970A1 (en) 1970-05-29
BE746639R (en) 1970-08-27

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Legal Events

Date Code Title Description
PS Patent sealed [section 19, patents act 1949]
PLNP Patent lapsed through nonpayment of renewal fees