US4158622A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Treatment of hydrocarbons by hydrogenation and fines removal
Assignee: Cogas Development Co
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Filing: 1978-02-08
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Granted: 1979-06-19
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Expires: 1998-02-08
Abstract
Abstract Hydrocarbonaceous material produced from pyrolysis of coal and shale is subjected to hydrogenation and fines removal by first passing it through an ebullating bed reactor in which the hydrocarbonaceous material is partially hydrogenated and partially vaporized. The vapor is then separated and further hydrogenated while the fines in the liquid portion are concentrated and removed as a slurry. The remaining liquid is vaporized, either by recycling it through the ebullating bed reactor or by flash evaporation, to rid it completely of fines. The thus vaporized remaining liquid is also subjected to further hydrogenation.
Inventors
- 👤 Eugene F. Schwarzenbek
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 03:12
CPC Classifications
C; C10; C10G; C10G1/00; C10G1/002; C10G65/00; C10G65/02
Claims Analysis
Total Claims: 18
Claim 1
Independent Claim
143 words
A method of treating hydrocarbonaceous material by hydrogenation to separate oxygen, sulfur and nitrogen and removal of fines, said method comprising the steps of (a) partially hydrogenating said material by passing it through ebullating catalytic bed reactor means along with hydrogen gas while allowing vaporization of some of said material during the hydrogenation reaction, but retaining a sufficient amount of said material in liquid form as a liquid portion to carry the accompanying fines through the reactor means, (b) separating the vapors from said liquid portion and accompanying fines transferred from said ebullating bed reactor means and subjecting said vapors to further hydrogenation, (c) concentrating said fines into a part of said liquid portion in step (b) to form a slurry and ejecting said slurry from said liquid portion, (d) subjecting another part of said liquid portion from step (b) to further hydrogenation.
Claim 2
Independent Claim
143 words
A method of treating hydrocarbonaceous material by hydrogenation to separate oxygen, sulfur and nitrogen and removal of fines, said method comprising the steps of (a) partially hydrogenating said material by passing it through ebullating catalytic bed reactor means along with hydrogen gas while allowing vaporization of some of said material during the hydrogenation reaction, but retaining a sufficient amount of said material in liquid form as a liquid portion to carry the accompanying fines through the reactor means, (b) separating the vapors from said liquid portion and accompanying fines transferred from said ebullating bed reactor means and subjecting said vapors to further hydrogenation, (c) concentrating said fines into a part of said liquid portion in step (b) to form a slurry and ejecting said slurry from said liquid portion, (d) subjecting another part of said liquid portion from step (b) to further hydrogenation.
Claim 3
Dependent Claim
19 words
A method according to claim 1 wherein said vapors are subjected to further hydrogenation in a fixed bed reactor.
Claim 4
Dependent Claim
34 words
A method according to claim 2 wherein the products from said fixed bed reactor are subjected to fractional separation and wherein hydrogen gas recovered therefrom is recycled back to said ebullating bed reactor means.
Claim 5
Dependent Claim
34 words
A method according to claim 1 wherein said another part of said liquid portion is combined with vapors which have been produced in said ebullating bed reactor means and is subjected to further hydrogenation.
Claim 6
Dependent Claim
27 words
A method according to claim 1 wherein step (d) is carried out by recycling the liquid portion remaining after step (c) through said ebullating bed reactor means.
Claim 7
Dependent Claim
33 words
A method according to claim 1 wherein step (a) of partially hydrogenating said hydrocarbonaceous material is carried out in stages by passing the oil serially through a plurality of separate ebullating bed reactors.
Claim 8
Dependent Claim
31 words
A method according to claim 6 wherein step (c) of concentrating said fines is performed separately on the liquid portion from each stage of said plurality of separate ebullating bed reactors.
Claim 9
Dependent Claim
38 words
A method according to claim 7 wherein said another part of said liquid portion from step (b) which precedes a successive ebullating bed reactor is further hydrogenated by passing said another part through said successive ebullating bed reactor.
Claim 10
Dependent Claim
26 words
A method according to claim 1 wherein the liquid portion remaining in step (a) has a fines concentration in the range of ten to twenty-five percent.
Claim 11
Dependent Claim
22 words
A method according to claim 1 wherein the liquid portion remaining in step (a) has a fines concentration of about twenty percent.
Claim 12
Dependent Claim
33 words
A method according to claim 1 wherein step (c) of concentrating said fines is carried out until the slurry thus formed and which is ejected has a fines concentration of about fifty percent.
Claim 13
Dependent Claim
18 words
A method according to claim 1 wherein said step of concentrating said fines is carried out by settling.
Claim 14
Dependent Claim
18 words
A method according to claim 1 wherein said step of concentrating said fines is carried out by centrifuging.
Claim 15
Dependent Claim
18 words
A method according to claim 1 wherein vapor is separated from step (c) by flashing said liquid portion.
Claim 16
Dependent Claim
40 words
A method according to claim 14 wherein the vapors produced in said flashing are condensed and the resulting liquid is separated from accompanying noncondensible gases and said liquid is added to said vapors which are further hydrogenated in step (b).
Claim 17
Dependent Claim
16 words
A method according to claim 15 wherein said liquid portion is heated prior to flash evaporation.
Claim 18
Dependent Claim
37 words
A method according to claim 16 wherein steam is injected into said liquid portion prior to said flash evaporation and wherein water produced in the course of condensation of said vapors is separated from the resulting liquid.
References Cited (Backward Citations)
USRE25770E
Cited
US2779777A
Cited
US3321393A
Cited
US3410792A
Cited
US3523888A
Cited
US3519554A
Cited
US3519553A
Cited
US3519555A
Cited
US3640816A
Cited
US3594305A
Cited
US3679573A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1982-06-18 | 1982-12-18 | 1983-06-19 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1986-06-18 | 1986-12-18 | 1987-06-19 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1990-06-18 | 1990-12-18 | 1991-06-19 | $7700.00 | Window Closed / Lapsed |