US4081460A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for the vapor phase oxidation of benzene to maleic anhydrides
Assignee: Scientific Design LLC
•
Filing: 1975-12-12
•
Granted: 1978-03-28
•
Expires: 1995-12-12
Abstract
Abstract Molybdenum - vanadium - oxygen oxidation catalyst for producing maleic anhydride from benzene is regenerated and stabilized in situ by the addition of up to 0.0012 gram mole of phosphorus per gram mole of vanadium in the vanadium - molybdenum - oxygen catalyst.
Inventors
- 👤 Ralph O. Kerr
- 👤 Gabe W. Strybos, Jr.
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-08 16:54
CPC Classifications
C; C07; C07C; C07C51/00; C07C51/16; C07C51/31; C07C51/313
Claims Analysis
Total Claims: 14
Claim 1
Independent Claim
216 words
In a process for the vapor phase oxidation of benzene to maleic anhydride wherein a stream consisting essentially of said benzene, at about 1.1 to 1.6 mol % of benzene based on the total gaseous stream and a flow rate of 50 to 200 grams of benzene per hour and oxygen, is contacted at a temperature in the range of 340°-500° C with a fixed bed vanadium -- molybdenum -- oxygen catalyst, having an atomic ratio of molybdenum to vanadium in the range of 0.05 to 0.95:1 and containing less than 25 percent by weight of other components based on the total weight of molybdenum and vanadium, there being an exotherm of reaction in said catalyst bed and wherein said catalyst gradually decreases in activity, the improvement comprising adding to said stream a volatilizable compound of a phosphorus halide or an organo-phosphorus compound selected from the group consisting of ##STR2## wherein R is phenyl or an alkyl radical of one to 6 carbon atoms and X is H or R, to contact said catalyst in an amount to deactivate only the portion of said catalyst bed containing the exotherm of reaction which was present in said catalyst bed prior to the addition of said phosphorus compound, thereby moving said exotherm down stream into said catalyst bed.
Claim 2
Dependent Claim
216 words
In a process for the vapor phase oxidation of benzene to maleic anhydride wherein a stream consisting essentially of said benzene, at about 1.1 to 1.6 mol % of benzene based on the total gaseous stream and a flow rate of 50 to 200 grams of benzene per hour and oxygen, is contacted at a temperature in the range of 340°-500° C with a fixed bed vanadium -- molybdenum -- oxygen catalyst, having an atomic ratio of molybdenum to vanadium in the range of 0.05 to 0.95:1 and containing less than 25 percent by weight of other components based on the total weight of molybdenum and vanadium, there being an exotherm of reaction in said catalyst bed and wherein said catalyst gradually decreases in activity, the improvement comprising adding to said stream a volatilizable compound of a phosphorus halide or an organo-phosphorus compound selected from the group consisting of ##STR2## wherein R is phenyl or an alkyl radical of one to 6 carbon atoms and X is H or R, to contact said catalyst in an amount to deactivate only the portion of said catalyst bed containing the exotherm of reaction which was present in said catalyst bed prior to the addition of said phosphorus compound, thereby moving said exotherm down stream into said catalyst bed.
Claim 3
Dependent Claim
19 words
The process according to claim 1 wherein said phosphorus compound has a volatilization temperature of 250° C or less.
Claim 4
Dependent Claim
13 words
The process according to claim 1 wherein said compound is a phosphorus halide.
Claim 5
Dependent Claim
13 words
The process according to claim 1 wherein said compound is an organo-phosphorus compound.
Claim 6
Dependent Claim
33 words
The process according to claim 1 wherein up to 0.0012 gram mole of phosphorus compound per gram mole of vanadium in the vanadium -- molybdenum -- oxygen catalyst is added to the catalyst.
Claim 7
Dependent Claim
23 words
The process according to claim 5 wherein from 0.00004 to 0.0008 gram mole of phosphorus compound per gram mole of vanadium is added.
Claim 8
Dependent Claim
27 words
The process according to claim 1 wherein said phosphorus compound is added to said catalyst during the vapor phase oxidation of benzene to produce maleic acid anhydride.
Claim 9
Dependent Claim
34 words
The process according to claim 1 wherein the phosphorus compound is a phosphorus halide of the structure PX n ' wherein X' is Cl, Br, I or F and n is 3 to 5.
Claim 10
Dependent Claim
16 words
The process according to claim 1 wherein said catalyst contains 0.0003 to 0.12 atom of phosphorus.
Claim 11
Dependent Claim
19 words
The process according to claim 1 wherein benzene or oxygen are discontinued from said feed during phosphorus compound addition.
Claim 12
Dependent Claim
10 words
The process according to claim 10 wherein benzene is discontinued.
Claim 13
Dependent Claim
10 words
The process according to claim 10 wherein oxygen is discontinued.
Claim 14
Dependent Claim
20 words
The process according to claim 1 wherein benzene and oxygen are discontinued from said feed during the phosphorus compound addition.
References Cited (Backward Citations)
US2294130A
Cited
US2967185A
Cited
US3296282A
Cited
US3849448A
Cited
GB1291354A
Cited
US3838067A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1981-03-27 | 1981-09-26 | 1982-03-28 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-03-27 | 1985-09-26 | 1986-03-28 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-03-27 | 1989-09-26 | 1990-03-28 | $7700.00 | Window Closed / Lapsed |