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US4133747A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for processing raw coal

Assignee: Ministry of Natural Resources and Wildlife
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Filing: 1978-02-02
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Granted: 1979-01-09
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Expires: 1998-02-02
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Abstract

Abstract A method and apparatus for beneficiating crushed raw coal comprising: cleaning the crushed coal in bulk in cyclone separators using only water as a cleaning medium and obtaining a product of wet clean coal and wet reject material and also a stream of effluent; drying said wet clean coal and wet reject material by agglomerating after the addition of a small amount of oil and then centrifuging to obtain a product of clean dry coal and solid reject material and also a stream of effluent; treating the effluent stream from the cleaning step and the effluent stream from the drying step by means of flocculation to recover a product of coal and reject sludge which is returned to pass through the drying step again; and thus obtain clean water which is recycled and applied to the input of the cyclones in the cleaning step.

Inventors

  • 👤 Jan Visman

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-24 16:33
CPC Classifications
B; B03; B03B; B03B9/00; B03B9/005

Claims Analysis

Total Claims: 11
Claim 1
Independent Claim 274 words
A method for the beneficiation of crushed raw coal with the concomitant elimination of solids-containing liquid waste streams which comprises: (a) slurrying the crushed raw coal in water and subjecting the slurried coal to a first gravimetric separation whereby a light fraction comprising clean coal and a heavy coal and waste containing fraction are produced; (b) subjecting said light fraction to a first granulometric separation to produce a fine coal-containing fraction and a coarse, clean, coal product fraction; (c) subjecting said heavy coal and waste fraction to a second gravimetric separation to produce a middlings fraction and a heavy waste solids containing fraction; (d) dewatering both said middlings fraction and said heavy waste solids containing fraction, recycling said middlings fraction to the first gravimetric separation and passing said dewatered heavy solids fraction from the process as reject waste; (e) subjecting the liquid stream obtained by dewatering said middlings fraction to a third gravimetric separation to produce a light fraction containing finely divided coal and a heavy fraction containing waste solids; (f) subjecting said light fraction containing finely divided coal to a second granulometric separation to produce a coal sludge fraction and a reject effluent fraction containing finely divided waste material; (g) agglomerating said coal sludge fraction and dewatering it to produce a clean fine coal product fraction, and a waste-containing effluent fraction; (h) recycling said waste-containing effluent fraction to said third gravimetric separation; (i) flocculating the solids in said reject effluent fraction and separating the flocculated solids to produce a reject cake and a clarified water stream, and (j) recycling said clarified water stream to the coal slurry feed to said first gravimetric separation.
Claim 2
Independent Claim 274 words
A method for the beneficiation of crushed raw coal with the concomitant elimination of solids-containing liquid waste streams which comprises: (a) slurrying the crushed raw coal in water and subjecting the slurried coal to a first gravimetric separation whereby a light fraction comprising clean coal and a heavy coal and waste containing fraction are produced; (b) subjecting said light fraction to a first granulometric separation to produce a fine coal-containing fraction and a coarse, clean, coal product fraction; (c) subjecting said heavy coal and waste fraction to a second gravimetric separation to produce a middlings fraction and a heavy waste solids containing fraction; (d) dewatering both said middlings fraction and said heavy waste solids containing fraction, recycling said middlings fraction to the first gravimetric separation and passing said dewatered heavy solids fraction from the process as reject waste; (e) subjecting the liquid stream obtained by dewatering said middlings fraction to a third gravimetric separation to produce a light fraction containing finely divided coal and a heavy fraction containing waste solids; (f) subjecting said light fraction containing finely divided coal to a second granulometric separation to produce a coal sludge fraction and a reject effluent fraction containing finely divided waste material; (g) agglomerating said coal sludge fraction and dewatering it to produce a clean fine coal product fraction, and a waste-containing effluent fraction; (h) recycling said waste-containing effluent fraction to said third gravimetric separation; (i) flocculating the solids in said reject effluent fraction and separating the flocculated solids to produce a reject cake and a clarified water stream, and (j) recycling said clarified water stream to the coal slurry feed to said first gravimetric separation.
Claim 3
Dependent Claim 34 words
The process of claim 1 wherein said heavy fraction containing waste solids of step (e) is subjected to a fourth gravimetric separation to produce a light coal-containing fraction and a heavy waste sludge fraction.
Claim 4
Dependent Claim 28 words
The process of claim 2 wherein said first, second, third and fourth gravimetric separations are accomplished by passing the feed streams to said separations through compound water cyclones.
Claim 5
Dependent Claim 25 words
The process of claim 1 wherein the fine coal-containing fraction of step (b) is recycled to the slurried coal fed to said first gravimetric separation.
Claim 6
Dependent Claim 26 words
The process of claim 1 wherein the dewatered middlings fraction of step (d) is further comminuted by grinding before being recycled to said first gravimetric separation.
Claim 7
Dependent Claim 34 words
The process of claim 5 wherein said light coal-containing fraction is recycled to said third gravimetric separation and wherein said waste sludge fraction is dewatered to produce a reject cake and a reject effluent.
Claim 8
Dependent Claim 26 words
The process of claim 6 wherein said reject effluent is flocculated and thereafter separated to produce a reject cake and a clarified water stream for recycle.
Claim 9
Dependent Claim 21 words
The process of claim 1 wherein said coal sludge fraction is agglomerated by the addition of a small amount of oil.
Claim 10
Dependent Claim 53 words
The process of claim 1 wherein said flocculated solids in said reject effluent fraction are separated by treatment in a static thickener to produce clarified process water for recycle and a sludge which is further dewatered by treatment in a slugging centrifuge to produce a reject waste cake and additional clarified process water.
Claim 11
Dependent Claim 19 words
The process of claim 1 wherein said coarse coal product fraction and said fine coal product fraction are blended.

References Cited (Backward Citations)

US2724503A Cited
US3045818A Cited
USRE26720E Cited
US3408293A Cited
US3366247A Cited
US3487923A Cited
CA876860A Cited
US3856668A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1982-01-08 1982-07-10 1983-01-09 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1986-01-08 1986-07-10 1987-01-09 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1990-01-08 1990-07-10 1991-01-09 $7700.00 Window Closed / Lapsed

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