US4227024A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Preparation of 2,6-xylenol and catalyst composition useful therefor
Assignee: ConocoPhillips Co
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Filing: 1979-06-04
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Granted: 1980-10-07
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Expires: 1999-06-04
Abstract
Abstract A process for preparing 2,6-xylenol in high selectivity and a catalyst composition useful therein are disclosed. The process comprises reacting phenol, o-cresol or mixtures thereof with methanol in presence of water, hydrogen and a catalyst consisting essentially of Fe 2 O 3 , SnO 2 , Cr 2 O 3 , and K 2 O.
Inventors
- 👤 Bruce E. Leach
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 05:49
CPC Classifications
B; B01; B01J; B01J23/00; B01J23/70; B01J23/76; B01J23/84; B01J23/85; B01J23/86; B01J23/862; C; C07; C07C; C07C37/00; C07C37/11; C07C37/16; Y; Y02; Y02P; Y02P20/00; Y02P20/50; Y02P20/52
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
209 words
A process for preparing 2,6-xylenol in high selectivity wherein the process comprises reacting phenol, o-cresol or mixtures thereof with methanol in the presence of water using a catalyst consisting essentially of the following materials in percent by weight: Fe 2 O 3 --about 90 to about 97; SnO 2 --about 0.5 to about 5; Cr 2 O 3 --about 0.5 to about 5; K 2 O--about 0.01 to about 1, said process being characterized further in that: (a) prior to use the catalyst has been treated with hydrogen at a temperature of 300° to 500° C. at a flow rate of 2 to 6 volumes of hydrogen per minute per volume of reactor for 2 to 12 hours; (b) there is present about 1 to 10 moles of methanol per mole of phenol and/or o-cresol; (c) the amount of water is about 5 to about 15 weight percent, based on the total amount of phenol, o-cresol and methanol; (d) the amount of catalyst expressed as LHSV is about 0.1 to about 5; (e) the temperature is in the range of about 380° to about 420° C.; (f) the pressure is from atmospheric to 1,000 psig; and (g) the product mixture contains at least 99 weight percent o-cresol and 2,6-xylenol.
Claim 2
Dependent Claim
209 words
A process for preparing 2,6-xylenol in high selectivity wherein the process comprises reacting phenol, o-cresol or mixtures thereof with methanol in the presence of water using a catalyst consisting essentially of the following materials in percent by weight: Fe 2 O 3 --about 90 to about 97; SnO 2 --about 0.5 to about 5; Cr 2 O 3 --about 0.5 to about 5; K 2 O--about 0.01 to about 1, said process being characterized further in that: (a) prior to use the catalyst has been treated with hydrogen at a temperature of 300° to 500° C. at a flow rate of 2 to 6 volumes of hydrogen per minute per volume of reactor for 2 to 12 hours; (b) there is present about 1 to 10 moles of methanol per mole of phenol and/or o-cresol; (c) the amount of water is about 5 to about 15 weight percent, based on the total amount of phenol, o-cresol and methanol; (d) the amount of catalyst expressed as LHSV is about 0.1 to about 5; (e) the temperature is in the range of about 380° to about 420° C.; (f) the pressure is from atmospheric to 1,000 psig; and (g) the product mixture contains at least 99 weight percent o-cresol and 2,6-xylenol.
Claim 3
Dependent Claim
87 words
The process of claim 1 characterized further in that: (a) there is present about 1 to 10 moles of methanol per mole of phenol and/or o-cresol; (b) the amount of water is about 5 to about 15 weight percent, based on the total amount of phenol, o-cresol and methanol; (c) the amount of catalyst expressed as LHSV is about 0.1 to about 5; (d) the temperature is in the range of about 380° to about 420° C., and (e) the pressure is from atmospheric to 1,000 psig.
Claim 4
Dependent Claim
89 words
The process of claim 2 characterized further in that: (a) there is present about 3 to about 5 moles of methanol per mole of phenol and/or o-cresol; (b) the amount of water is about 8 to about 12 weight percent based on the total amount of phenol, o-cresol and methanol; (c) the amount of catalyst expressed as LHSV is about 0.2 to about 3 ; (d) the temperature is in the range of about 400° to about 415° C., and (e) the pressure is from atmospheric to 200 psig.
Claim 5
Dependent Claim
50 words
The process of claim 2 wherein the catalyst consists essentially of the following materials in percent by weight: Fe 2 O 3 --about 93 to about 96; SnO 2 --about 1 to about 3; Cr 2 O 3 --about 1 to about 3; K 2 O--about 0.02 to about 0.5.
Claim 6
Dependent Claim
50 words
The process of claim 3 wherein the catalyst consists essentially of the following materials in percent by weight: Fe 2 O 3 --about 93 to about 96; SnO 2 --about 1 to about 3; Cr 2 O 3 --about 1 to about 3; K 2 O--about 0.02 to about 0.5.
Claim 7
Dependent Claim
45 words
The process of claims 4 or 5 wherein the catalyst prior to use is treated with hydrogen at a temperature of 300° to 500° C. and a flow rate of 2 to 6 volumes per minute per volume of reactor for 2 for 12 hours.
Claim 8
Dependent Claim
117 words
The process of claim 1 wherein a mixture of, in parts by weight, 1 part of phenol and 1 part of o-cresol is reacted with 2 parts of methanol in the presence of 0.2 part of water, based on said phenol, o-cresol and methanol, at a temperature of 400°-410° C. in the presence of a catalyst containing, in weight percent, Fe 2 O 3 --94.8; SnO 2 --3; Cr 2 O 3 --2; K 2 O--0.2, said catalyst having been treated with hydrogen gas at 370° C. at a rate of 200 cc/min for 4 hours, said process being characterized further in that the amount of catalyst is about 0.5 volume per volume of liquid per hour.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1983-10-07 | 1984-04-07 | 1984-10-07 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1987-10-07 | 1988-04-07 | 1988-10-07 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1991-10-07 | 1992-04-07 | 1992-10-07 | $7700.00 | Window Closed / Lapsed |