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GB654153A - Preparation of phenol by distillation of products of hydrolysis of monochlorobenzene - Google Patents

Preparation of phenol by distillation of products of hydrolysis of monochlorobenzene

Info

Publication number
GB654153A
GB654153A GB17774/47A GB1777447A GB654153A GB 654153 A GB654153 A GB 654153A GB 17774/47 A GB17774/47 A GB 17774/47A GB 1777447 A GB1777447 A GB 1777447A GB 654153 A GB654153 A GB 654153A
Authority
GB
United Kingdom
Prior art keywords
column
grm
water
phenol
chlorobenzene
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
GB17774/47A
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.)
Solvay SA
Original Assignee
Solvay SA
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 Solvay SA filed Critical Solvay SA
Publication of GB654153A publication Critical patent/GB654153A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C37/00Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom of a six-membered aromatic ring
    • C07C37/68Purification; separation; Use of additives, e.g. for stabilisation
    • C07C37/70Purification; separation; Use of additives, e.g. for stabilisation by physical treatment
    • C07C37/74Purification; separation; Use of additives, e.g. for stabilisation by physical treatment by distillation
    • C07C37/78Purification; separation; Use of additives, e.g. for stabilisation by physical treatment by distillation by azeotropic distillation
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C37/00Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom of a six-membered aromatic ring
    • C07C37/01Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom of a six-membered aromatic ring by replacing functional groups bound to a six-membered aromatic ring by hydroxy groups, e.g. by hydrolysis
    • C07C37/02Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom of a six-membered aromatic ring by replacing functional groups bound to a six-membered aromatic ring by hydroxy groups, e.g. by hydrolysis by substitution of halogen

Landscapes

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

Abstract

<PICT:0654153/III/1> In the preparation of phenol by hydrolysis of chlorobenzene in the presence of cuprous chloride as catalyst, the reaction products comprising phenol, hydrogen chloride and unchanged chlorobenzene and water, are introduced into a distillation column together with further quantities of chlorobenzene and water, the amount of water and conditions of the column being such that vapours of both the binary azeotrope C6H5Cl/H2O and the ternary azeotrope C6H5Cl/H2O/HCl are given off from the top of the column; these vapours are returned to the hydrolyser, preferably after passing through molten cuprous chloride, while phenol and hydrochloric acid are withdrawn from the base of the column. In the example the head of distillation column 2 is maintained at 97 DEG C. and the overhead vapours contain chlorobenzene (13290 grm.), water (5180 grm.) and hydrogen chloride (22 grm.). These vapours are bubbled through molten cuprous chloride in bath 7 and are then introduced into hydrolyser 1 which contains a metal silicate impregnated with cuprous chloride and is maintained at 450 DEG C. Chlorobenzene (1329 grm.) and water (213 grm.) are added at a and b to the vapours leaving the hydrolyzer, and the mixture is then introduced into column 2 which also receives 1769 grm. of water at c. The mixture withdrawn from the base of the column contains phenol (1000 grm.), hydrogen chloride (431 grm.) and water (1768 grm.). This mixture is cooled to atmospheric temperature in decanter 3 where it separates into two layers. The upper layer is introduced into column 4 and the lower layer into column 5; the top of each column being maintained at 107 DEG C. The condensed distillates from columns 4 and 5, which both contain phenol, hydrogen chloride and water, are brought together in decanter 6 where they divide into two layers: the upper layer is refluxed to column 4 and the lower layer to column 5. Phenol is withdrawn from the base of column 4, and hydrochloric acid from the base of column 5. In a second example, decanter 6 is dispensed with, and the distillates from columns 4 and 5 are passed to decanter 3.
GB17774/47A 1946-07-23 1947-07-04 Preparation of phenol by distillation of products of hydrolysis of monochlorobenzene Expired GB654153A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
BE654153X 1946-07-23

Publications (1)

Publication Number Publication Date
GB654153A true GB654153A (en) 1951-06-06

Family

ID=3876873

Family Applications (1)

Application Number Title Priority Date Filing Date
GB17774/47A Expired GB654153A (en) 1946-07-23 1947-07-04 Preparation of phenol by distillation of products of hydrolysis of monochlorobenzene

Country Status (2)

Country Link
ES (1) ES178978A1 (en)
GB (1) GB654153A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2988573A (en) * 1958-10-06 1961-06-13 Union Carbide Corp Process for producing phenol
US3221063A (en) * 1961-08-25 1965-11-30 Hooker Chemical Corp Distillation in raschig-phenol process

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2988573A (en) * 1958-10-06 1961-06-13 Union Carbide Corp Process for producing phenol
US3221063A (en) * 1961-08-25 1965-11-30 Hooker Chemical Corp Distillation in raschig-phenol process

Also Published As

Publication number Publication date
ES178978A1 (en) 1947-09-16

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