US4428818A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Liquefaction of coal
Assignee: Mobil Oil AS
•
Filing: 1982-12-07
•
Granted: 1984-01-31
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Expires: 2002-12-07
Abstract
Abstract Solvent refining of coal is conducted with a blend of coals calculated to maintain the phenols of the steady state recycle solvent within desired limits.
Inventors
- 👤 Frank J. Derbyshire
- 👤 Darrell D. Whitehurst
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-06 15:47
CPC Classifications
C; C10; C10G; C10G1/00; C10G1/04; C10G1/042; C10G1/008
Claims Analysis
Total Claims: 6
Claim 1
Independent Claim
247 words
In a process for solvent refining of a low rank coal of high oxygen content by mixing a comminuted coal charge with a hydrogen donor recycle solvent derived in the process maintaining the resultant mixture at reaction temperature in the presence of elemental hydrogen for a period of time sufficient to dissolve and react components of the coal, removing normally gaseous and solid materials from the effluent of said reaction, separating a liquid fraction boiling above about 400° F., recycling said liquid fraction to provide said hydrogen donor recycle solvent and recovering a liquid fuel product from the remainder of said effluent, the improvement for providing a hydrogen donor recycle solvent of greater benefit to the process which comprises separately subjecting said low rank coal and a coal of higher rank and lower oxygen content to test dissolution and reaction in admixture with a hydrogen donor solvent under hydrogen pressure at reaction temperature, analyzing the liquid products to determine the weight percent yield of phenols boiling above about 400° F., each of said reactions based on dry weight of the respective coals, calculating a blend ratio of the said coals which will yield less than 15 weight percent of phenols boiling above about 400° F. based on dry coal, adding to said low rank coal an amount of said coal of higher rank corresponding to said calculated blend ratio to provide a blended coal and supplying said blend coal to the process as said comminuted coal charge.
Claim 2
Dependent Claim
247 words
In a process for solvent refining of a low rank coal of high oxygen content by mixing a comminuted coal charge with a hydrogen donor recycle solvent derived in the process maintaining the resultant mixture at reaction temperature in the presence of elemental hydrogen for a period of time sufficient to dissolve and react components of the coal, removing normally gaseous and solid materials from the effluent of said reaction, separating a liquid fraction boiling above about 400° F., recycling said liquid fraction to provide said hydrogen donor recycle solvent and recovering a liquid fuel product from the remainder of said effluent, the improvement for providing a hydrogen donor recycle solvent of greater benefit to the process which comprises separately subjecting said low rank coal and a coal of higher rank and lower oxygen content to test dissolution and reaction in admixture with a hydrogen donor solvent under hydrogen pressure at reaction temperature, analyzing the liquid products to determine the weight percent yield of phenols boiling above about 400° F., each of said reactions based on dry weight of the respective coals, calculating a blend ratio of the said coals which will yield less than 15 weight percent of phenols boiling above about 400° F. based on dry coal, adding to said low rank coal an amount of said coal of higher rank corresponding to said calculated blend ratio to provide a blended coal and supplying said blend coal to the process as said comminuted coal charge.
Claim 3
Dependent Claim
26 words
A process according to claim 1 wherein said blend ratio is calculated to yield less than 10 weight percent of phenols boiling above about 400° F.
Claim 4
Dependent Claim
33 words
A process according to claim 1 wherein the hydrogen donor solvent used in said test dissolution and reaction is a mixture of tetralin or alkyl substituted tetralin and naphthalene or alkyl substituted naphthalene.
Claim 5
Dependent Claim
45 words
A process according to claim 1 wherein the pyrite content of each of said coals is determined and the blend ratio is set to also provide at least 1 weight percent of pyrite in said comminuted coal charge based on dry weight of said charge.
Claim 6
Dependent Claim
26 words
A process according to claim 4 wherein the blend ratio is set to provide at least 3 weight percent of pyrite in said comminuted coal charge.
References Cited (Backward Citations)
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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) | 1987-01-30 | 1987-08-01 | 1988-01-31 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-01-30 | 1991-08-01 | 1992-01-31 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-01-30 | 1995-08-01 | 1996-01-31 | $7700.00 | Window Closed / Lapsed |