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US1595299A - Manufacture of phenols - Google Patents

Manufacture of phenols Download PDF

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Publication number
US1595299A
US1595299A US684910A US68491024A US1595299A US 1595299 A US1595299 A US 1595299A US 684910 A US684910 A US 684910A US 68491024 A US68491024 A US 68491024A US 1595299 A US1595299 A US 1595299A
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United States
Prior art keywords
benzene
phenol
temperature
oxides
phenols
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Expired - Lifetime
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US684910A
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William J Hale
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Dow Chemical Co
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Dow Chemical Co
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Publication date
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Priority to US684910A priority Critical patent/US1595299A/en
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Publication of US1595299A publication Critical patent/US1595299A/en
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    • 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
    • C07C37/055Preparation 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 the substituted group being bound to oxygen, e.g. ether group
    • 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
    • C07C37/64Preparation of O-metal compounds with O-metal group bound to a carbon atom belonging to a six-membered aromatic ring

Definitions

  • An autoclave is one-third filled with a 20 per cent. solution of caustic soda cont-ainin a small amount of an oxide of uranium, with or without varying small portions of the oxides of vanadium, molybdenum or tungsten.
  • An equal volume of benzene is then added and the contents of the autoclave heated quickly to a temperature in excess of 300 0., and preferably ranging from 320 to 400 (land under a correspondingly high pressure, i. e., under a pressure greater than the vapor tension of the reacting substances,
  • a method of hydrolyzing a benzene hydrocarbon to form a uni-valent phenol the step which consists in'heating a mixture of such hydrocarbon and caustic alkali solution in the presence of an oxide of uranium at a temperature of from approximately 300 to 400 C. and a pressure greater than the vapor tension of the reacting substances at such temperature.
  • a method of hydrolyzing benzene to form a uni-valent phenol the step which consists in heating an aerated emulsion o the benzene and caustic soda solution to a temperature of from approximately 300 to 400 C. and under a correspondin high pressure in the presence of an oxi e of a metal of Groups V and VI of the periodic system.

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

Description

Patented Aug. 10, 1926.
1,595,299 UNITED STATES PATENT. OFFICE.
WILLIAM J. I HALE, OF MIDLAND, MICHIGAN, ASSIGNOR. IO THE DOW CHEMICAL COMPANY, OF MIDLAND, MICHIGAN, A CORPORATION OE MICHIGAN.
MANUFACTURE or PHENOLS.
No Drawing.
The presence of phenol in the air-oxida- .tion products of benzene obtained by means the presence of ferrous sulfate at a temperature of 0., but the reaction product, con sisting chiefly of pyrocatechol, contains still other compounds in addition to a small quantity of phenol.
I have now discovered that thepresence of certain metallic oxides in a hot aerated benzene-caustic soda emulsion constitutes an admirable agency 'for mono-hydroxylization ofthis benzene without the appearance of undesirable polyhydric phenols and the tarry products usually obtained in these direct oxidation processes. Accordin ly, even thou h the portion of the benzene that is oxidize 0 benzene remains as pure benzene and when withdrawn from the system, together with the phenate, may be easily separated from the latter and. then used over again without intervening steps for its purification.
To the accomplishment of my improved method of direct oxidation of benzene for the manufacture of phenol I accordingly employ the steps hereinafter fully described an articularl pointed out in the'claims, the fbllowing description setting forth but one of the various ways in which the prin-.
ciple of the invention may be used. 1
It may be stated first that the production of a monohydric phenol from benzene is apparently dependent upon the concentration of alkali as well as upon the selection of the metallic oxide or oxides employed as the catalytic agent. It is also desirable that the operation be carried on at a relatively high temperature and under a correspondingly high ressure in order to avoid too pro longed heating. A caustic soda solution of from 20 tov 25 per cent concentration has been found to serve satisfactorily in the process. Caustic potash of course works oxides, 'apparently'give the best results.
to phenol may not be large, the
Application filed .Tanuary i, 1924. Serial No. 684,910.
somewhat better while the hydroxides of alkaline earth metals do not prove so eflicient, although the reaction will occur where "they are used. The last remark also applies to'the carbonates of the alkali earth metals which serve only to fair advantage. As the catalytic agent certain oxides of the fifth and sixth groups of the periodic system have proved to be most effective, viz, the
oxides of vanadium, molybdenum, tungsten, and uranium. As at present advised, the oxides of uranium, there being several such As an illustration of the practical procedure in carrying out my improved process, I give the following example An autoclave is one-third filled with a 20 per cent. solution of caustic soda cont-ainin a small amount of an oxide of uranium, with or without varying small portions of the oxides of vanadium, molybdenum or tungsten. An equal volume of benzene is then added and the contents of the autoclave heated quickly to a temperature in excess of 300 0., and preferably ranging from 320 to 400 (land under a correspondingly high pressure, i. e., under a pressure greater than the vapor tension of the reacting substances,
such pressure for the temperature range in question being approximately 3,000 pounds per square inch. After heating under these conditions for approximately one hour, the clear mixture is discharged from the auto.- clave and the benzene which has not been acted upon is removed by simple distillation. It is then ready for use over again in the next operation. The residual aqueous liquor which contains the hydrolyticoxidation product of the reaction, e. g. sodium phen'ate 1n the particular case acidified for the liberation of. phenol and the latter removed bv distillation. The salt layer remaining may be discarded or worked over for the recovery of the oxides of the rare earth metals used in the process.
1 It will be understood that the space left over in the autoclave after introducing the ingredients named above will be occupied by atmospheric air (or equivalent oxygen containing gas), to'which the reaction mixture is exposed while the autoclave is being heated. v I
Other modes of a plying the principle of my invention may be employed instead of the one explained, change being made as 1cin hand, is thereupon gards the method herein disclosed, provided the step or steps stated by any of the following claims or the equivalent of such stated step or steps be employed.
I therefore particularly point out and distinctly claim as my invention 1. In a method of hydrolyzing a benzene hydrocarbon to form a uni-valent phenol, the step which consists in heating a mixture of such hydrocarbon and caustic alkali solution in the presence of an oxide of a metal of Groups V and VI of the periodic system at a temperature of from approximately 300 to 400 C. and a pressure greater than the vapor tension of the reacting substances at such temperature.
2. In a method of hydrolyzing a benzene hydrocarbon to form a uni-valent phenol, the step which consists in'heating a mixture of such hydrocarbon and caustic alkali solution in the presence of an oxide of uranium at a temperature of from approximately 300 to 400 C. and a pressure greater than the vapor tension of the reacting substances at such temperature.
3. In a method of hydrolyzing benzene to form a uni-valent phenol, the step which consists in heating an aerated emulsion o the benzene and caustic soda solution to a temperature of from approximately 300 to 400 C. and under a correspondin high pressure in the presence of an oxi e of a metal of Groups V and VI of the periodic system.
4. In a method of hydrolyzing benzene to form a uni-valent phenol, the step which consists in heating an aerated emulsion of the benzene and caustic soda solution to a temperature of from approximately 300 to 400 C. and under a corresponding high pressure .in the presence of an oxide of uranium. I
Signed by me this 4th day of January, 1924.
WILLIAM J. HALE.
US684910A 1924-01-07 1924-01-07 Manufacture of phenols Expired - Lifetime US1595299A (en)

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2456597A (en) * 1944-09-09 1948-12-14 Socony Vacuum Oil Co Inc Production of phenol by catalytic oxidation of benzene
US3929913A (en) * 1973-02-16 1975-12-30 Brichima Spa Process for preparing diphenols
FR2421162A1 (en) * 1978-03-27 1979-10-26 Suntech CATALYTIC CONVERSION OF TOLUENE TO PHENOL AND FORMALDEHYDE
US4260808A (en) * 1978-11-03 1981-04-07 Suntech, Inc. Catalytic process for the conversion of toluene to equimolar amounts of phenol acetate and methylene diacetate
US5962752A (en) * 1997-07-31 1999-10-05 Sun Company, Inc. Leached alumina vanadyl catalysts for hydroxylation of aromatics using molecular oxygen as the terminal oxidant without coreductant

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2456597A (en) * 1944-09-09 1948-12-14 Socony Vacuum Oil Co Inc Production of phenol by catalytic oxidation of benzene
US3929913A (en) * 1973-02-16 1975-12-30 Brichima Spa Process for preparing diphenols
FR2421162A1 (en) * 1978-03-27 1979-10-26 Suntech CATALYTIC CONVERSION OF TOLUENE TO PHENOL AND FORMALDEHYDE
US4260808A (en) * 1978-11-03 1981-04-07 Suntech, Inc. Catalytic process for the conversion of toluene to equimolar amounts of phenol acetate and methylene diacetate
US5962752A (en) * 1997-07-31 1999-10-05 Sun Company, Inc. Leached alumina vanadyl catalysts for hydroxylation of aromatics using molecular oxygen as the terminal oxidant without coreductant

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