Patent US4423265A successfully refreshed from Google Patents.
US4423265A
Expired / Lapsed
US
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Process for snygas conversions to liquid hydrocarbon products
Assignee: Mobil Oil AS
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Filing: 1982-12-01
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Granted: 1983-12-27
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Expires: 2002-12-01
Abstract
Abstract The liquid carrier in a Fischer-Tropsch synthesis slurry reactor system is periodically or continually separated and subjected to cracking and isomerization in the presence of suitable catalysts. The treated carrier is returned to the reactor system and the accumulation of high viscosity paraffin in the reactor slurry is minimized. Suitable catalysts include a mixture of cracking and isomerization catalysts.
Inventors
- 👤 Yung-Feng Chu
- 👤 Tai-Sheng Chou
- 👤 Arthur W. Chester
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-26 19:37
CPC Classifications
C; C07; C07C; C07C1/00; C07C1/02; C07C1/04; C07C1/0485; C10; C10G; C10G11/00; C10G11/02; C10G11/04; C10G11/05
Claims Analysis
Total Claims: 15
Claim 1
Independent Claim
207 words
A process for converting synthesis gas to liquid hydrocarbons having a boiling range within that of gasoline and distillate comprising the steps of: (a) charging said synthesis gas to a Fischer-Tropsch synthess conversion zone comprising a catalyst providing CO reducing characteristics in a single or a combination of catalyst particles in direct contact with a suspending liquid medium; (b) separating at least a fraction of said suspending liquid medium containing dissolved heavier hydrocarbons from said catalyst particles; (c) contacting said separated suspending medium containing heavier hydrocarbons with a cracking and isomerization catalyst under conditions effective to crack and isomerize at least a portion of said heavier hydrocarbons to lighter hydrocarbons; (d) separating the resultant product stream of (c) into two streams; (e) removing an effluent stream from said conversion zone of (a) to a second reaction zone containing a crystalline zeolite catalyst; (f) returning one of said streams of (d) to said effluent stream from zone (a); (g) returning the remaining stream of (d) to said conversion zone of (a); and (h) contacting said effluent stream from said conversion zone of (a) with a crystalline zeolite catalyst to convert the product of said Fischer-Tropsch synthesis gas conversion to hydrocarbons boiling within the range of distillate and gasoline.
Claim 2
Dependent Claim
207 words
A process for converting synthesis gas to liquid hydrocarbons having a boiling range within that of gasoline and distillate comprising the steps of: (a) charging said synthesis gas to a Fischer-Tropsch synthess conversion zone comprising a catalyst providing CO reducing characteristics in a single or a combination of catalyst particles in direct contact with a suspending liquid medium; (b) separating at least a fraction of said suspending liquid medium containing dissolved heavier hydrocarbons from said catalyst particles; (c) contacting said separated suspending medium containing heavier hydrocarbons with a cracking and isomerization catalyst under conditions effective to crack and isomerize at least a portion of said heavier hydrocarbons to lighter hydrocarbons; (d) separating the resultant product stream of (c) into two streams; (e) removing an effluent stream from said conversion zone of (a) to a second reaction zone containing a crystalline zeolite catalyst; (f) returning one of said streams of (d) to said effluent stream from zone (a); (g) returning the remaining stream of (d) to said conversion zone of (a); and (h) contacting said effluent stream from said conversion zone of (a) with a crystalline zeolite catalyst to convert the product of said Fischer-Tropsch synthesis gas conversion to hydrocarbons boiling within the range of distillate and gasoline.
Claim 3
Dependent Claim
36 words
The process of claim 1 wherein said cracking and isomerization catalyst is a mixture of a first catalyst which functions primarily as a cracking catalyst and a second catalyst which functions primarily as an isomerization catalyst.
Claim 4
Dependent Claim
26 words
The process of claim 2 wherein said cracking and isomerization catalyst is a zeolite selected from the group consisting of ZSM-5, Zeolite X, and Zeolite Y.
Claim 5
Dependent Claim
27 words
The process of claim 2 wherein said isomerization catalyst is selected from the group consisting of platinum and palladium deposited on alumina, ZSM-5 zeolite or ZSM-beta zeolite.
Claim 6
Dependent Claim
26 words
The process of claim 1 wherein said zeolite catalyst of (h) is selected from the group consisting of ZSM-5, ZSM-11, ZSM-12, ZSM-23, ZSM-35, ZSM-38 and ZSM-48.
Claim 7
Dependent Claim
13 words
The process of claim 1 wherein said zeolite catalyst of (h) is ZSM-5.
Claim 8
Dependent Claim
16 words
The process of claim 1 wherein the cracking zone is contiguous to said slurry reactor zone.
Claim 9
Dependent Claim
18 words
The process of claim 1 wherein the cracking zone of (c) is separated from said Fischer-Tropsch reaction zone.
Claim 10
Dependent Claim
31 words
The process of claim 1 wherein the contacting of said suspending medium with a cracking and isomerizing catalyst is conducted at a temperature between about 400° F. and about 800° F.
Claim 11
Dependent Claim
24 words
The process of claim 1 wherein the contacting of said suspending medium is conducted at a pressure between about 0 and about 1000 psig.
Claim 12
Dependent Claim
27 words
The process of claim 1 wherein the contacting of said suspending medium is conducted at a liquid hourly space velocity of between about 0.1 and about 20.
Claim 13
Dependent Claim
25 words
The process of claim 1 wherein said cracking and isomerization catalyst contains one catalytic component which functions as both a cracking and an isomerization catalyst.
Claim 14
Dependent Claim
31 words
The process of claim 1 wherein said cracking and isomerization catalyst is a mixture of two or more catalysts each of which functions as both a cracking and an isomerization catalyst.
Claim 15
Dependent Claim
20 words
The process of claim 2 wherein said isomerization catalyst is a Group VIII metal deposited on alumina, or ZSM-5 zeolite.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1986-12-26 | 1987-06-27 | 1987-12-27 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1990-12-26 | 1991-06-27 | 1991-12-27 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1994-12-26 | 1995-06-27 | 1995-12-27 | $7700.00 | Window Closed / Lapsed |