US1595299A - Manufacture of phenols - Google Patents
Manufacture of phenols Download PDFInfo
- 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
- Authority
- US
- United States
- Prior art keywords
- benzene
- phenol
- temperature
- oxides
- phenols
- 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 - Lifetime
Links
- 238000004519 manufacturing process Methods 0.000 title description 3
- 150000002989 phenols Chemical class 0.000 title description 2
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 42
- HEMHJVSKTPXQMS-UHFFFAOYSA-M sodium hydroxide Inorganic materials [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 14
- 238000000034 method Methods 0.000 description 11
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 9
- 238000010438 heat treatment Methods 0.000 description 6
- 229910052770 Uranium Inorganic materials 0.000 description 5
- DNYWZCXLKNTFFI-UHFFFAOYSA-N uranium Chemical compound [U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U] DNYWZCXLKNTFFI-UHFFFAOYSA-N 0.000 description 5
- 239000004215 Carbon black (E152) Substances 0.000 description 4
- 229930195733 hydrocarbon Natural products 0.000 description 4
- 230000003301 hydrolyzing effect Effects 0.000 description 4
- 235000011121 sodium hydroxide Nutrition 0.000 description 4
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 3
- 239000003513 alkali Substances 0.000 description 3
- 239000000839 emulsion Substances 0.000 description 3
- 229910044991 metal oxide Inorganic materials 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 230000000737 periodic effect Effects 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 description 2
- 229910052784 alkaline earth metal Inorganic materials 0.000 description 2
- -1 benzene hydrocarbon Chemical class 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 2
- YCIMNLLNPGFGHC-UHFFFAOYSA-N catechol Chemical compound OC1=CC=CC=C1O YCIMNLLNPGFGHC-UHFFFAOYSA-N 0.000 description 2
- 239000003518 caustics Substances 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 150000002430 hydrocarbons Chemical class 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 229910052750 molybdenum Inorganic materials 0.000 description 2
- 239000011733 molybdenum Substances 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 description 2
- 229910052721 tungsten Inorganic materials 0.000 description 2
- 239000010937 tungsten Substances 0.000 description 2
- 229910052720 vanadium Inorganic materials 0.000 description 2
- GPPXJZIENCGNKB-UHFFFAOYSA-N vanadium Chemical compound [V]#[V] GPPXJZIENCGNKB-UHFFFAOYSA-N 0.000 description 2
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- YNPNZTXNASCQKK-UHFFFAOYSA-N Phenanthrene Natural products C1=CC=C2C3=CC=CC=C3C=CC2=C1 YNPNZTXNASCQKK-UHFFFAOYSA-N 0.000 description 1
- DGEZNRSVGBDHLK-UHFFFAOYSA-N [1,10]phenanthroline Chemical compound C1=CN=C2C3=NC=CC=C3C=CC2=C1 DGEZNRSVGBDHLK-UHFFFAOYSA-N 0.000 description 1
- 150000001342 alkaline earth metals Chemical class 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 150000001555 benzenes Chemical class 0.000 description 1
- 150000004649 carbonic acid derivatives Chemical class 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- MIHINWMALJZIBX-UHFFFAOYSA-N cyclohexa-2,4-dien-1-ol Chemical compound OC1CC=CC=C1 MIHINWMALJZIBX-UHFFFAOYSA-N 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 235000003891 ferrous sulphate Nutrition 0.000 description 1
- 239000011790 ferrous sulphate Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 150000004679 hydroxides Chemical class 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- BAUYGSIQEAFULO-UHFFFAOYSA-L iron(2+) sulfate (anhydrous) Chemical compound [Fe+2].[O-]S([O-])(=O)=O BAUYGSIQEAFULO-UHFFFAOYSA-L 0.000 description 1
- 229910000359 iron(II) sulfate Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 235000011118 potassium hydroxide Nutrition 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 229910052761 rare earth metal Inorganic materials 0.000 description 1
- 150000002910 rare earth metals Chemical class 0.000 description 1
- 239000011541 reaction mixture Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000001577 simple distillation Methods 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C37/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom of a six-membered aromatic ring
- C07C37/01—Preparation 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
- C07C37/055—Preparation 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
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C37/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom of a six-membered aromatic ring
- C07C37/64—Preparation 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.
Landscapes
- 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.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US684910A US1595299A (en) | 1924-01-07 | 1924-01-07 | Manufacture of phenols |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US684910A US1595299A (en) | 1924-01-07 | 1924-01-07 | Manufacture of phenols |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1595299A true US1595299A (en) | 1926-08-10 |
Family
ID=24750050
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US684910A Expired - Lifetime US1595299A (en) | 1924-01-07 | 1924-01-07 | Manufacture of phenols |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1595299A (en) |
Cited By (5)
| 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 |
-
1924
- 1924-01-07 US US684910A patent/US1595299A/en not_active Expired - Lifetime
Cited By (5)
| 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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