US4189375A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Coal liquefaction process utilizing selective heat addition
Assignee: RAG AG
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Filing: 1978-12-13
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Granted: 1980-02-19
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Expires: 1998-12-13
Abstract
Abstract A process for liquefying coal involving heating only a portion of a the total process hydrogen stream to increase its temperature to a relatively high level and admixing said heated hydrogen with only a portion of the total coal slurry in the upstream region of a dissolver zone. The hydrogen stream has a relatively low specific heat and the addition thereto of a relatively small amount of heat increases its temperature to a level which is sufficiently high to initiate hydrocracking reactions when the hot hydrogen stream is intermixed with only a portion of the dissolver feed slurry, provided that the dissolver feed slurry contains recycle mineral residue in an amount adequate to catalyze hydrocracking reactions. Because the recycle mineral residue catalyzes the exothermic hydrocracking reactions, sufficient process heat is generated to permit addition to the dissolver zone in a downstream region thereof the remainder of dissolver feed slurry and process hydrogen in a relatively cool condition.
Inventors
- 👤 Lawrence J. Kirby
- 👤 Thomas E. Richardson
- 👤 Bruce K. Schmid
- 👤 John V. Ward
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-31 18:03
CPC Classifications
C; C10; C10G; C10G1/00; C10G1/06; C10G1/065
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
253 words
A coal liquefaction process comprising passing feed coal together with recycle slurry comprising normally solid dissolved coal, normally liquid coal and mineral residue to a feed slurry mixing vessel operated at a pressure below process pressure; pressurizing mixing vessel effluent slurry to process pressure and passing said mixing vessel effluent slurry at process pressure to a preheater vessel; heating the slurry within said preheater vessel; preheating a first portion of a process hydrogen stream employing heat from outside of the process; mixing said preheated hydrogen with a first portion of preheater vessel effluent slurry to form a hydrogen-slurry mixture; passing said preheated hydrogen-slurry mixture to the upstream region of a dissolver zone to exothermically hydrocrack normally solid dissolved coal to liquid coal and hydrocarbon gases thereby increasing the temperature in the dissolver zone; passing a second and relatively cool portion of process hydrogen at a temperature below the temperature in the dissolver zone to a downstream region of said dissolver zone; passing a second portion of preheater vessel effluent slurry at a temperature below the temperature in said dissolver zone to a downstream region in said dissolver zone; passing a hot dissolver zone effluent stream through high temperature vapor-liquid separator means to remove an overhead stream comprising hydrogen, hydrocarbon gases and naphtha from a separator slurry comprising normally liquid coal and normally solid dissolved coal with suspended mineral residue; passing a portion of said separator slurry to product separation means; and recycling an other portion of said separator slurry to said mixing vessel.
Claim 2
Dependent Claim
253 words
A coal liquefaction process comprising passing feed coal together with recycle slurry comprising normally solid dissolved coal, normally liquid coal and mineral residue to a feed slurry mixing vessel operated at a pressure below process pressure; pressurizing mixing vessel effluent slurry to process pressure and passing said mixing vessel effluent slurry at process pressure to a preheater vessel; heating the slurry within said preheater vessel; preheating a first portion of a process hydrogen stream employing heat from outside of the process; mixing said preheated hydrogen with a first portion of preheater vessel effluent slurry to form a hydrogen-slurry mixture; passing said preheated hydrogen-slurry mixture to the upstream region of a dissolver zone to exothermically hydrocrack normally solid dissolved coal to liquid coal and hydrocarbon gases thereby increasing the temperature in the dissolver zone; passing a second and relatively cool portion of process hydrogen at a temperature below the temperature in the dissolver zone to a downstream region of said dissolver zone; passing a second portion of preheater vessel effluent slurry at a temperature below the temperature in said dissolver zone to a downstream region in said dissolver zone; passing a hot dissolver zone effluent stream through high temperature vapor-liquid separator means to remove an overhead stream comprising hydrogen, hydrocarbon gases and naphtha from a separator slurry comprising normally liquid coal and normally solid dissolved coal with suspended mineral residue; passing a portion of said separator slurry to product separation means; and recycling an other portion of said separator slurry to said mixing vessel.
Claim 3
Dependent Claim
43 words
The process of claim 1 including the steps of passing said overhead stream at process pressure to said preheater vessel for direct admixture with the slurry therein to heat the preheater slurry; and venting the preheater vessel to low temperature vapor-liquid separator means.
Claim 4
Dependent Claim
40 words
The process of claim 1 wherein said first portion of said process hydrogen stream comprises between about 20 and 90 volume percent of the total process hydrogen and is preheated to a temperature in the range 700° to 1,200° F.
Claim 5
Dependent Claim
29 words
The process of claim 1 wherein said first portion of preheater vessel effluent slurry comprises between about 30 and 90 weight percent of the total preheater vessel effluent slurry.
Claim 6
Dependent Claim
71 words
The process of claim 1 comprising passing wet feed coal to said mixing vessel and maintaining the temperature of said other portion of said separator slurry above the temperature in said mixing vessel so that said other portion of the separator slurry adds heat to the mixing vessel and dries the coal therein; and venting vapor from said mixing vessel independently of said mixing vessel effluent slurry to release water therefrom.
Claim 7
Dependent Claim
44 words
The process of claim 1 wherein the temperature of the slurry in said feed slurry mixing vessel is between about 300° and 500° F. and the residence time of the slurry in said feed slurry mixing vessel is between about 5 and 30 minutes.
Claim 8
Dependent Claim
23 words
The process of claim 1 wherein said second portion of process hydrogen is at a temperature in the range 100° to 600° F.
Claim 9
Dependent Claim
37 words
The process of claim 5 including the step of passing wet feed coal to a coal predrying zone to remove a portion of the moisture content thereof prior to passing the feed coal to said mixing vessel.
References Cited (Backward Citations)
US3791957A
Cited
US3823084A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1983-02-18 | 1983-08-20 | 1984-02-19 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1987-02-18 | 1987-08-20 | 1988-02-19 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1991-02-18 | 1991-08-20 | 1992-02-19 | $7700.00 | Window Closed / Lapsed |