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US4428818A Expired / Lapsed US ⏱️ 0.0 years remaining

Liquefaction of coal

Assignee: Mobil Oil AS
•
Filing: 1982-12-07
•
Granted: 1984-01-31
•
Expires: 2002-12-07
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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)

US4045187A Cited
US4097361A Cited
US4125452A Cited
US4298453A Cited
US4277327A Cited
US4277326A Cited
US4306960A Cited
US4319981A Cited

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

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