US4330388A
Expired / Lapsed
US
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Short residence time coal liquefaction process including catalytic hydrogenation
Assignee: Chevron USA Inc
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Filing: 1980-09-09
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Granted: 1982-05-18
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Expires: 2000-09-09
Abstract
Abstract Normally solid dissolved coal product and a distillate liquid product are produced by continuously passing a feed slurry comprising raw feed coal and a recycle solvent oil and/or slurry together with hydrogen to a preheating-reaction zone (26, alone, or 26 together with 42), the hydrogen pressure in the preheating-reaction zone being at least 1500 psig (105 kg/cm 2 ), reacting the slurry in the preheating-reaction zone (26, or 26 with 42) at a temperature in the range of between about 455° and about 500° C. to dissolve the coal to form normally liquid coal and normally solid dissolved coal. A total slurry residence time is maintained in the reaction zone ranging from a finite value from about 0 to about 0.2 hour, and reaction effluent is continuously and directly contacted with a quenching fluid (40, 68) to substantially immediately reduce the temperature of the reaction effluent to below 425° C. to substantially inhibit polymerization so that the yield of insoluble organic matter comprises less than 9 weight percent of said feed coal on a moisture-free basis. The reaction is performed under conditions of temperature, hydrogen pressure and residence time such that the quantity of distillate liquid boiling within the range C 5 -454° C. is an amount at least equal to that obtainable by performing the process under the same condition except for a longer total slurry residence time, e.g., 0.3 hour. Solvent boiling range liquid is separated from the reaction effluent (83) and recycled as process solvent (16). The amount of solvent boiling range liquid is sufficient to provide at least 80 weight percent of that required to maintain the process in overall solvent balance.
Inventors
- 👤 Raymond P. Anderson
- 👤 David K. Schmalzer
- 👤 Charles H. Wright
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-29 05:59
CPC Classifications
C; C10; C10G; C10G1/00; C10G1/06; C10G1/065; C10G1/002
Claims Analysis
Total Claims: 33
Claim 1
Independent Claim
318 words
A process for producing a normally solid dissolved coal and a distillate liquid product from a raw coal feed which comprises continuously passing a feed slurry comprising said raw coal and a recycle solvent oil together with hydrogen through a preheating-reaction zone, the hydrogen pressure in said preheating-reaction zone being at least 1500 psig, reacting said slurry in said preheating-reaction zone at a temperature in the range of between about 455° and about 500° C. to dissolve said coal to form normally liquid coal and normally solid dissolved coal, maintaining a total slurry residence time within said temperature range at a finite value in the range of above 0 to about 0.2 hour, continuously withdrawing reaction effluent, continuously and directly contacting said reaction effluent with a quenching fluid to substantially immediately reduce the temperature of said reaction effluent to a temperature which is sufficiently below 425° C. to substantially inhibit polymerization, performing said reaction under conditions of temperature, hydrogen pressure and residence time such that the distillate liquid product of said reaction boiling within the range C 5 to 454° C. is an amount at least equal to that obtainable from said reaction by performing said process under the same conditions except for a total slurry residence time of 0.3 hour before quenching, separating said reaction effluent into fractions without hydrogenative reaction of said reaction effluent subsequent to quenching and before said separation step, one fraction comprising a first solvent boiling range liquid and a second fraction comprising normally solid dissolved coal, recycling said first solvent boiling range liquid as recycle solvent for forming said feed slurry without any hydrogenative reaction thereof following said quenching step, separating a portion of said normally solid dissolved coal from said second fraction and passing at least a portion of the separated normally solid dissolved coal and hydrogen to a catalytic hydrogenation zone for conversion to a second solvent boiling range liquid.
Claim 2
Dependent Claim
318 words
A process for producing a normally solid dissolved coal and a distillate liquid product from a raw coal feed which comprises continuously passing a feed slurry comprising said raw coal and a recycle solvent oil together with hydrogen through a preheating-reaction zone, the hydrogen pressure in said preheating-reaction zone being at least 1500 psig, reacting said slurry in said preheating-reaction zone at a temperature in the range of between about 455° and about 500° C. to dissolve said coal to form normally liquid coal and normally solid dissolved coal, maintaining a total slurry residence time within said temperature range at a finite value in the range of above 0 to about 0.2 hour, continuously withdrawing reaction effluent, continuously and directly contacting said reaction effluent with a quenching fluid to substantially immediately reduce the temperature of said reaction effluent to a temperature which is sufficiently below 425° C. to substantially inhibit polymerization, performing said reaction under conditions of temperature, hydrogen pressure and residence time such that the distillate liquid product of said reaction boiling within the range C 5 to 454° C. is an amount at least equal to that obtainable from said reaction by performing said process under the same conditions except for a total slurry residence time of 0.3 hour before quenching, separating said reaction effluent into fractions without hydrogenative reaction of said reaction effluent subsequent to quenching and before said separation step, one fraction comprising a first solvent boiling range liquid and a second fraction comprising normally solid dissolved coal, recycling said first solvent boiling range liquid as recycle solvent for forming said feed slurry without any hydrogenative reaction thereof following said quenching step, separating a portion of said normally solid dissolved coal from said second fraction and passing at least a portion of the separated normally solid dissolved coal and hydrogen to a catalytic hydrogenation zone for conversion to a second solvent boiling range liquid.
Claim 3
Dependent Claim
44 words
The process of claim 1, wherein sufficient second solvent boiling range liquid is separated from the reaction effluent of said hydrogenation zone and passed to said feed slurry to make up any recycle solvent deficiency and maintain the overall solvent balance of said process.
Claim 4
Dependent Claim
44 words
The process of claim 2, wherein the normally solid dissolved coal is reacted in said hydrogenation zone under a hydrogen pressure of between about 1000 and about 5000 psig while at a temperature in the range of between about 370° and about 510° C.
Claim 5
Dependent Claim
28 words
The process of claim 3, wherein the hydrogen pressure is between about 2000 and about 4000 psig and the temperature is between about 400° and about 480° C.
Claim 6
Dependent Claim
22 words
The process of claim 1, wherein said normally solid dissolved coal has a benzene soluble content of at least 50 weight percent.
Claim 7
Dependent Claim
22 words
The process of claim 5, wherein said normally solid dissolved coal has a benzene soluble content of at least 60 weight percent.
Claim 8
Dependent Claim
41 words
The process of claim 2, wherein the amount of said first solvent boiling range liquid is sufficient to provide at least 80 weight percent, but less than 100 weight percent of that required to maintain said process in overall solvent balance.
Claim 9
Dependent Claim
38 words
The process of claim 2, wherein the amount of said first solvent boiling range liquid is sufficient to provide between about 80 and about 95 weight percent of that required to maintain said process in overall solvent balance.
Claim 10
Dependent Claim
29 words
The process of claim 1, wherein said preheating-reaction zone comprises a first zone and a second zone, wherein said first zone is heated and said second zone is unheated.
Claim 11
Dependent Claim
13 words
The process of claim 9, wherein said first zone is a tubular zone.
Claim 12
Dependent Claim
13 words
The process of claim 1, wherein said preheating-reaction zone is a tubular zone.
Claim 13
Dependent Claim
23 words
The process of claim 1, wherein said reaction effluent is passed to a separation zone for separation of gases from said reaction effluent.
Claim 14
Dependent Claim
20 words
The process of claim 12, wherein said reaction effluent is contacted with said quenching fluid before entering said separation zone.
Claim 15
Dependent Claim
20 words
The process of claim 12, wherein said reaction effluent is contacted with said quenching fluid upon entering said separation zone.
Claim 16
Dependent Claim
14 words
The process of claim 1, wherein said quenching fluid is a cool distillate liquid.
Claim 17
Dependent Claim
11 words
The process of claim 1, wherein said quenching fluid is hydrogen.
Claim 18
Dependent Claim
39 words
The process of claim 1, wherein said distillate liquid product is produced in an amount at least equal to that obtainable by performing said process under the same conditions except for a total slurry residence time of 0.4 hour.
Claim 19
Dependent Claim
39 words
The process of claim 1, wherein said distillate liquid product is produced in an amount at least equal to that obtainable by performing said process under the same conditions except for a total slurry residence time of 0.5 hour.
Claim 20
Dependent Claim
36 words
The process of claim 1, wherein the amount of said first solvent boiling range liquid is sufficient to provide at least 90 weight percent of the amount required to maintain said process in overall solvent balance.
Claim 21
Dependent Claim
36 words
The process of claim 1, wherein the amount of said first solvent boiling range liquid is sufficient to provide at least 100 weight percent of the amount required to maintain said process in overall solvent balance.
Claim 22
Dependent Claim
26 words
The process of claim 1, wherein at least 40 weight percent of said coal feed is converted to solid dissolved coal on a moisture free basis.
Claim 23
Dependent Claim
19 words
The process of claim 1, wherein said fraction comprising normally solid dissolved coal is passed to a filtration step.
Claim 24
Dependent Claim
20 words
The process of claim 1, wherein said fraction comprising normally solid dissolved coal is passed to a solvent extraction step.
Claim 25
Dependent Claim
49 words
The process of claim 1, wherein said slurry is reacted in said preheating-reaction zone at a temperature in the range of 460° to 490° C., under a hydrogen pressure in the range of 2000 to 2500 psig and for a total slurry residence time of 0.02 to 0.15 hour.
Claim 26
Dependent Claim
43 words
The process of claim 24, wherein said slurry is reacted in said preheating-reaction zone at a temperature of about 475° C., under a hydrogen pressure of about 2000 psig and for a slurry residence time of between about 0.06 and about 0.135 hour.
Claim 27
Dependent Claim
32 words
The process of claim 1, wherein said second fraction comprises normally solid dissolved coal, mineral residue and solvent boiling range liquid, and at least a portion of said second fraction is recycled.
Claim 28
Dependent Claim
29 words
The process of claim 26, wherein said portion of said second fraction constitutes between about 20 and about 70 weight percent based upon the weight of said feed slurry.
Claim 29
Dependent Claim
18 words
The process of claim 1, wherein the yield of insoluble organic matter comprises less than 9 weight percent.
Claim 30
Dependent Claim
18 words
The process of claim 1, wherein the yield of insoluble organic matter comprises less than 8 weight percent.
Claim 31
Dependent Claim
30 words
The process of claim 1, wherein the hydrogen consumption of said process is between about 0.5 and about 2.5 weight percent of said coal feed on a moisture free basis.
Claim 32
Dependent Claim
31 words
The process of claim 1, wherein the hydrogen feed rate to said preheated-reaction zone is between about 0.5 and about 6.0 weight percent based upon the weight of the feed slurry.
Claim 33
Dependent Claim
27 words
The process of claim 31, wherein the hydrogen feed rate is between about 1.5 and about 4.0 weight percent based upon the weight of the feed slurry.
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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) | 1985-05-17 | 1985-11-16 | 1986-05-18 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1989-05-17 | 1989-11-16 | 1990-05-18 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1993-05-17 | 1993-11-16 | 1994-05-18 | $7700.00 | Window Closed / Lapsed |