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US4579650A Expired / Lapsed US ⏱️ 0.0 years remaining

Coal enhancement process and equipment

Assignee: Dow Chemical Co
•
Filing: 1985-03-28
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Granted: 1986-04-01
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Expires: 2005-03-28
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Abstract

Abstract A process for enhancing coal by removing the gangue (rock, shale, iron pyrites and the like) associated with the mined coal as it comes from the crushers before further treatment. The process described slurries the crushed run of the mine (ROM) coal with a heavy medium, such as perchloroethylene, for a short period of time at ambient or below temperatures, (i.e. slurry times of 5-30 minutes and temperatures of 90° C. to below -10° C.); thereafter allowing, in a substantially quiescent environment, the solids to settle or float as their inherent densities are greater or lesser respectively than the density of the heavy medium. After settling the float solids (mostly coal of lower sulfur and ash content) are separated from the heavy medium as one stream and the sink solids (mostly the gangue) as a second stream. These solids are each washed with hot (90° C.-100° C.) water and the vapor azeotrope which forms from the water and heavy medium mixture (azeotrope) removed. The now water wet solids are separated from the body of hot water and sent for further processing or loading. The solids, both the coal and the gangue, have a heavy medium content of less than about 400 parts heavy medium per million parts solids.

Inventors

  • 👤 Robert J. Nankee
  • 👤 Thomas A. Vivian

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 08:09
CPC Classifications
B; B03; B03B; B03B9/00; B03B9/005; B03B5/00; B03B5/28; B03B5/30; B03B5/44; B03B5/447

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 94 words
In a method for treating coal by the heavy media technique wherein the float and sink solids each individually are recovered and freed of liquid then dried to remove the residual heavy media retained thereon the improvement which comprises treating each solids portion with hot water at the temperature of from the heavy medium water azeotroping point to the boiling point of water for a time sufficient to remove a substantial portion of the heavy media or until the water comes off at its boiling point and thereafter separating the solids from the water.
Claim 2
Dependent Claim 94 words
In a method for treating coal by the heavy media technique wherein the float and sink solids each individually are recovered and freed of liquid then dried to remove the residual heavy media retained thereon the improvement which comprises treating each solids portion with hot water at the temperature of from the heavy medium water azeotroping point to the boiling point of water for a time sufficient to remove a substantial portion of the heavy media or until the water comes off at its boiling point and thereafter separating the solids from the water.
Claim 3
Dependent Claim 100 words
In a method for treating coal by the heavy media technique wherein the float and sink solids each individually are recovered and freed of liquid then dried to remove the residual heavy media retained thereon the improvement which comprises treating each solids portion with hot water at from the temperature of the heavy medium water azeotroping point to the boiling point of water thereby to remove a substantial portion of the boiling media or until the water comes off at its boiling point, thereafter separating the solids from the water, and, recovering the media from the water/media vapors by condensation.
Claim 4
Dependent Claim 100 words
In a method for treating coal by the heavy media technique wherein the float and sink solids each individually are recovered and freed of liquid then dried to remove the residual heavy media retained thereon the improvement which comprises treating each solids portion with hot water at from the temperature of the heavy medium water azeotroping point to the boiling point of water thereby to remove a substantial portion of the boiling media or until the water comes off at its boiling point, thereafter separating the solids from the water, and, recovering the media from the water/media vapors by condensation.
Claim 5
Dependent Claim 99 words
In a method for treating coal by the heavy media technique wherein the float and sink solids each individually are recovered and freed of liquid then dried to remove the residual heavy media retained thereon the improvement which comprises treating each solids portion with hot water at from the temperature of the heavy medium water azeotroping point to the boiling point of water to remove a substantial portion of the heavy media or until the water comes off at its boiling point, condensing said azeotrope to recover the media from the condensate, and separating the solids from the water.
Claim 6
Dependent Claim 99 words
In a method for treating coal by the heavy media technique wherein the float and sink solids each individually are recovered and freed of liquid then dried to remove the residual heavy media retained thereon the improvement which comprises treating each solids portion with hot water at from the temperature of the heavy medium water azeotroping point to the boiling point of water to remove a substantial portion of the heavy media or until the water comes off at its boiling point, condensing said azeotrope to recover the media from the condensate, and separating the solids from the water.

References Cited (Backward Citations)

US3347370A Cited
US4173530A Cited
US4198289A Cited
US4324560A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1989-03-31 1989-09-30 1990-04-01 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1993-03-31 1993-09-30 1994-04-01 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1997-03-31 1997-09-30 1998-04-01 $7700.00 Window Closed / Lapsed

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