Patent US4528089A successfully refreshed from Google Patents.
US4528089A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Hydrogenation processes using carbon-containing molybdenum and tungsten sulfide catalysts
Assignee: ExxonMobil Technology and Engineering Co
•
Filing: 1983-11-16
•
Granted: 1985-07-09
•
Expires: 2003-11-16
Abstract
Abstract Sulfur and nitrogen-containing hydrocarbon feeds are upgraded by contacting said feed, at elevated temperature and in the presence of hydrogen, with a catalyst comprising a carbon-containing sulfide of a catalytic metal selected from the group consisting of tungsten, molybdenum and mixture thereof. In a preferred embodiment, these catalysts are promoted with certain transition metal sulfides such as cobalt sulfide. The catalyst may be preformed or formed in-situ in the feed or from catalyst precursor salts.
Inventors
- 👤 Theresa A. Pecoraro
- 👤 Russell R. Chianelli
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-03 20:52
CPC Classifications
B; B01; B01J; B01J27/00; B01J27/20; C; C10; C10G; C10G45/00; C10G45/02; C10G45/04
Claims Analysis
Total Claims: 33
Claim 1
Independent Claim
57 words
A process for upgrading hydrocarbon feeds comprising contacting said feed, at hydrotreating conditions and in the presence of hydrogen, with a catalyst comprising a poorly crystalline, carbon-containing metal sulfide having the formula MS 2-z C z' wherein 0.01≦z≦0.5 and 0.01≦z'≦3.0 and wherein M is a metal selected from the group consisting of Mo, W and mixtures thereof.
Claim 2
Dependent Claim
57 words
A process for upgrading hydrocarbon feeds comprising contacting said feed, at hydrotreating conditions and in the presence of hydrogen, with a catalyst comprising a poorly crystalline, carbon-containing metal sulfide having the formula MS 2-z C z' wherein 0.01≦z≦0.5 and 0.01≦z'≦3.0 and wherein M is a metal selected from the group consisting of Mo, W and mixtures thereof.
Claim 3
Dependent Claim
10 words
The process of claim 1 wherein said catalyst contains nitrogen.
Claim 4
Dependent Claim
23 words
The process of claim 2 wherein said nitrogen is present in said catalyst in an amount of less than about one weight percent.
Claim 5
Dependent Claim
19 words
The process of claim 3 wherein said hydrotreating conditions include a pressure ranging from about atmospheric to 5000 psig.
Claim 6
Dependent Claim
19 words
The process of claim 4 wherein said hydrotreating conditions include a temperature ranging from about 100° to 500° C.
Claim 7
Dependent Claim
16 words
The process of claim 5 wherein said catalyst is promoted with one or more promoter metals.
Claim 8
Dependent Claim
16 words
The process of claim 6 wherein said promoter metal comprises iron, cobalt, nickel and mixtures thereof.
Claim 9
Dependent Claim
23 words
The process of either of claims 5 or 7 wherein said hydrotreating conditions include a temperature of from about 200° to 450° C.
Claim 10
Dependent Claim
14 words
The process of claim 8 wherein said hydrogen pressure ranges from about 100-2500 psig.
Claim 11
Dependent Claim
54 words
A process for hydrotreating a hydrocarbon feed which comprises contacting said feed, at hydrotreating conditions and in the presence of hydrogen, with a poorly crystalline catalyst of the compositon MS 2-z C z' wherein 0.01≦z≦0.5 and 0.01≦z'≦3.0 and wherein M is a metal selected from the group consisting of Mo, W and mixtures thereof.
Claim 12
Dependent Claim
54 words
A process for hydrotreating a hydrocarbon feed which comprises contacting said feed, at hydrotreating conditions and in the presence of hydrogen, with a poorly crystalline catalyst of the compositon MS 2-z C z' wherein 0.01≦z≦0.5 and 0.01≦z'≦3.0 and wherein M is a metal selected from the group consisting of Mo, W and mixtures thereof.
Claim 13
Dependent Claim
16 words
The process of claim 10 wherein said catalyst contains less than about one weight percent nitrogen.
Claim 14
Dependent Claim
24 words
The process of either of claims 10 or 11 wherein said hydrotreating conditions include a pressure ranging from about 1 to about 5000 psig.
Claim 15
Dependent Claim
17 words
The process of claim 12 wherein said catalyst is promoted with one or more catalytic promoter metals.
Claim 16
Dependent Claim
16 words
The process of claim 13 wherein said promoter metal comprises iron, cobalt, nickel or mixtures thereof.
Claim 17
Dependent Claim
19 words
The process of claim 10 or 14 wherein said hydrotreating conditions include a temperature ranging from about 100°-500° C.
Claim 18
Dependent Claim
18 words
The process of claim 15 wherein said hydrotreating conditions include a pressure of about 100 to 2500 psig.
Claim 19
Dependent Claim
17 words
The process of claim 16 wherein said hydrotreating conditions include a temperature of from about 200°-400° C.
Claim 20
Dependent Claim
112 words
A process for hydrotreating a hydrocarbon feed which process comprises contacting said feed, at hydrotreating conditions and in the presence of hydrogen, with a catalyst comprising a poorly crystalline, nitrogen and carbon-containing sulfide of tungsten, molybdenum and mixtures thereof, wherein said catalyst has been formed by simultaneously contacting one or more catalyst precursors selected from the group consisting of (a) ammonium thiomolybdate or thiotungstate salts, (b) ammonium molybdate or tungstate salts, (c) substituted ammonium thiomolybdate or thiotungstate salt, and (d) substituted ammonium molybdate or tungstate salts and mixtures thereof, with sulfur, hydrogen and a hydrocarbon at a temperature of at least about 150° C. for a time sufficient to form said catalyst.
Claim 21
Dependent Claim
112 words
A process for hydrotreating a hydrocarbon feed which process comprises contacting said feed, at hydrotreating conditions and in the presence of hydrogen, with a catalyst comprising a poorly crystalline, nitrogen and carbon-containing sulfide of tungsten, molybdenum and mixtures thereof, wherein said catalyst has been formed by simultaneously contacting one or more catalyst precursors selected from the group consisting of (a) ammonium thiomolybdate or thiotungstate salts, (b) ammonium molybdate or tungstate salts, (c) substituted ammonium thiomolybdate or thiotungstate salt, and (d) substituted ammonium molybdate or tungstate salts and mixtures thereof, with sulfur, hydrogen and a hydrocarbon at a temperature of at least about 150° C. for a time sufficient to form said catalyst.
Claim 22
Dependent Claim
17 words
The process of claim 18 wherein said hydrocarbon used to form said catalyst comprises an aromatic hydrocarbon.
Claim 23
Dependent Claim
22 words
The process of claim 19 wherein said nitrogen is present in said catalyst in an amount of less than one weight percent.
Claim 24
Dependent Claim
16 words
The process of claim 20 wherein said catalyst is promoted with one or more promoter metals.
Claim 25
Dependent Claim
16 words
The process of claim 21 wherein said promoter metal comprises iron, cobalt, nickel and mixtures thereof.
Claim 26
Dependent Claim
144 words
A process for hydrotreating a hydrocarbon feed which comprises contacting said feed, at hydrotreating conditions and in the presence of hydrogen, with a catalyst comprising a poorly crystalline, carbon-containing sulfide of tungsten, molybdenum and mixture thereof, wherein said catalyst has been formed by simultaneously contacting one or more catalyst precursor salts, in the presence of sulfur and hydrogen and at an elevated temperature of at least about 150° C. with a hydrocarbon for a time sufficient to form said catalyst and wherein said precursor salt has the formula B x [MO y S 4-y ] wherein x is 1 or 2 and y is any value between 0 and 4, wherein M is Mo or W and wherein B is (a) an ammonium ion, or (b) an alkyl or aryl ion wherein said ion may contain from one to four alkyl or aryl groups.
Claim 27
Dependent Claim
144 words
A process for hydrotreating a hydrocarbon feed which comprises contacting said feed, at hydrotreating conditions and in the presence of hydrogen, with a catalyst comprising a poorly crystalline, carbon-containing sulfide of tungsten, molybdenum and mixture thereof, wherein said catalyst has been formed by simultaneously contacting one or more catalyst precursor salts, in the presence of sulfur and hydrogen and at an elevated temperature of at least about 150° C. with a hydrocarbon for a time sufficient to form said catalyst and wherein said precursor salt has the formula B x [MO y S 4-y ] wherein x is 1 or 2 and y is any value between 0 and 4, wherein M is Mo or W and wherein B is (a) an ammonium ion, or (b) an alkyl or aryl ion wherein said ion may contain from one to four alkyl or aryl groups.
Claim 28
Dependent Claim
10 words
The process of claim 23 wherein said catalyst contains nitrogen.
Claim 29
Dependent Claim
14 words
The process of claim 24 wherein said catalyst contains less than about 1% nitrogen.
Claim 30
Dependent Claim
17 words
The process of claim 25 wherein said hydrocarbon used to form said catalyst comprises an aromatic hydrocarbon.
Claim 31
Dependent Claim
21 words
The process of claim 26 wherein said catalyst is formed at a temperature of from about 200° C. to 600° C.
Claim 32
Dependent Claim
24 words
The process of either of claims 23, 25 or 27 wherein said hydrotreating conditions include a pressure of from about atmospheric to 5000 psig.
Claim 33
Dependent Claim
16 words
The process of claim 28 wherein said catalyst is promoted with one or more promoter metals.
References Cited (Backward Citations)
GB404422A
Cited
US2481824A
Cited
US2715603A
Cited
US2914462A
Cited
US2884370A
Cited
US2894903A
Cited
GB808336A
Cited
US3074783A
Cited
US3148135A
Cited
NL7510059A
Cited
NL7603197A
Cited
US4082652A
Cited
US4066530A
Cited
US4134825A
Cited
US4213850A
Cited
US4285804A
Cited
US4243553A
Cited
US4243554A
Cited
US4357229A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1988-07-08 | 1989-01-07 | 1989-07-09 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1992-07-08 | 1993-01-07 | 1993-07-09 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1996-07-08 | 1997-01-07 | 1997-07-09 | $7700.00 | Window Closed / Lapsed |