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US3920536A Expired / Lapsed US ⏱️ 0.0 years remaining

Coal dissolving process

Assignee: Sun Research and Development Co
•
Filing: 1973-01-15
•
Granted: 1975-11-18
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Expires: 1993-01-15
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Abstract

Abstract A process for dissolving sub-bituminous coal by heating said coal in the presence of a hydrogen donor oil, gaseous carbon monoxide, water, hydrogen, and an ammonium or alkali metal molybdate at a temperature of from about 400* to about 425*C and at a total pressure of from about 2000 to about 5000 psig.

Inventors

  • 👤 Walter H Seitzer
  • 👤 Robert W Shinn

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-27 18:42
CPC Classifications
C; C10; C10G; C10G1/00; C10G1/08; C10G1/086; Y; Y10; Y10S; Y10S208/00; Y10S208/951

Claims Analysis

Total Claims: 8
Claim 1
Independent Claim 117 words
THE PROCESS FOR DISSOLVING SUB-BITUMINOUS COAL WHICH COMPRISES HEATING AT ABOUT 400*C. TO ABOUT 425*C. UNDER A TOTAL PRESSURE OF FROM ABOUT 2000 TO ABOUT 5000 PSIG, A MIXTURE OF SAID FINELY DIVIDED COAL, A HYDROGEN DONOR OIL IN A WEIGHT RATIO TO SAID COAL OF FROM ABOUT 1:1 TO 5:1, CARBON MONOXIDE, HYDROGEN IN AN AMOUNT SUCH THAT ITS PARTIAL PRESSURE IS ABOUT THE SAME AS THAT OF SAID CARBON MONOXIDE, WATER IN AN AMOUNT SUCH THAT THE MOLAR RATIO OF WATER TO CARBON MONOXIDE IS FROM ABOUT 2:1 TO 1:2, AND AS A PROMOTER, AN ALKALI METAL OR AMMONIUM MOLYBDATE IN AN AMOUNT OF FROM ABOUT 0.5 TO ABOUT 10% BY WEIGHT OF SAID COAL.
Claim 2
Dependent Claim 117 words
THE PROCESS FOR DISSOLVING SUB-BITUMINOUS COAL WHICH COMPRISES HEATING AT ABOUT 400*C. TO ABOUT 425*C. UNDER A TOTAL PRESSURE OF FROM ABOUT 2000 TO ABOUT 5000 PSIG, A MIXTURE OF SAID FINELY DIVIDED COAL, A HYDROGEN DONOR OIL IN A WEIGHT RATIO TO SAID COAL OF FROM ABOUT 1:1 TO 5:1, CARBON MONOXIDE, HYDROGEN IN AN AMOUNT SUCH THAT ITS PARTIAL PRESSURE IS ABOUT THE SAME AS THAT OF SAID CARBON MONOXIDE, WATER IN AN AMOUNT SUCH THAT THE MOLAR RATIO OF WATER TO CARBON MONOXIDE IS FROM ABOUT 2:1 TO 1:2, AND AS A PROMOTER, AN ALKALI METAL OR AMMONIUM MOLYBDATE IN AN AMOUNT OF FROM ABOUT 0.5 TO ABOUT 10% BY WEIGHT OF SAID COAL.
Claim 3
Dependent Claim 19 words
The process of claim 1 where the oil is anthracene oil and the promoter is an alkali metal molybdate.
Claim 4
Dependent Claim 18 words
The process of claim 1 where the oil is a recycle oil and the promoter is sodium molybdate.
Claim 5
Dependent Claim 18 words
The process of claim 1 where the oil is a recycle oil and the promoter is ammonium molybdate.
Claim 6
Dependent Claim 15 words
The process of claim 1 where the CO and hydrogen are derived from producer gas.
Claim 7
Dependent Claim 121 words
The process of dissolving sub-bituminous coal to form a liquid product similar to crude oil which comprises heating at a temperature of about 415*C. and at a total pressure of about 3000 psig, a mixture of said finely divided coal, anthracene oil, hydrogen and carbon monoxide obtained as producer gas, water in an amount such that the molar ratio of water to carbon monoxide is from about 2:1 to 1:2, and ammonium molybdate, the weight ratio of oil to coal being about 2:1, the amount of hydrogen being such that its partial pressure is about the same as that of said carbon monoxide, and the amount of ammonium molybdate being from about 1% to about 7% by weight of said coal.
Claim 8
Dependent Claim 121 words
The process of dissolving sub-bituminous coal to form a liquid product similar to crude oil which comprises heating at a temperature of about 415*C. and at a total pressure of about 3000 psig, a mixture of said finely divided coal, anthracene oil, hydrogen and carbon monoxide obtained as producer gas, water in an amount such that the molar ratio of water to carbon monoxide is from about 2:1 to 1:2, and ammonium molybdate, the weight ratio of oil to coal being about 2:1, the amount of hydrogen being such that its partial pressure is about the same as that of said carbon monoxide, and the amount of ammonium molybdate being from about 1% to about 7% by weight of said coal.

References Cited (Backward Citations)

US1919108A Cited
GB406986A Cited
GB407227A Cited
US3687838A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1978-11-17 1979-05-19 1979-11-18 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1982-11-17 1983-05-19 1983-11-18 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1986-11-17 1987-05-19 1987-11-18 $7700.00 Window Closed / Lapsed

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