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US4284413A Expired / Lapsed US ⏱️ 0.0 years remaining

In-line method for the beneficiation of coal and the formation of a coal-in-oil combustible fuel therefrom

Assignee: National Research Council Canada
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Filing: 1979-12-26
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Granted: 1981-08-18
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Expires: 1999-12-26
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Abstract

Abstract An in-line method for the beneficiation of coal and the formation of a coal-in-oil combustible fuel wherein the coal is wet pulverized, micro-agglomerated with light oil to dissociate a large amount of inorganic impurities and some water, agglomerated with heavy oil to form relatively larger agglomerates and dissociate mainly water with some inorganic impurities, and then mixed with further heavy oil to form the coal-in-oil combustible fuel.

Inventors

  • 👤 C. Edward Capes
  • 👤 William L. Thayer
  • 👤 Richard D. Coleman
  • 👤 Leonard Messer

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 06:52
CPC Classifications
C; C10; C10L; C10L1/00; C10L1/32; C10L1/322

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 250 words
An in-line method for the beneficiation of coal and the formation of a coal-in-oil combustible fuel therefrom, comprising: (a) comminuting coal in water to produce a coal-in-water slurry comprising impurity liberated coal particles at least as fine as 40 microns weight mean particle size, then (b) mixing the coal-in-water slurry with light oil as agglomerating liquid having a specific gravity of less than of the order of 1 g/cm 3 to micro-agglomerate the impurity liberated coal particles and primarily dissociate inorganic impurities and some water therefrom, the light oil agglomerating liquid being added at not more than of the order of 20 wt % of the total weight of the solids of the coal-in-water slurry, then (c) separating the micro-agglomerated, impurity liberated coal from the dissociated inorganic impurities and water, then (d) mixing the separated, micro-agglomerated, impurity liberated coal with heavy fuel oil, having a specific gravity greater than of the order of 0.9 g/cm 3 , as agglomerating liquid to produce relatively larger agglomerates comprising an average size no greater than of the order of 3 mm and primarily dissociate water with some inorganic impurities which were present in the micro-agglomerated, impurity liberated coal and leave a residual amount of at least of the order of 5 wt % water in the relatively larger agglomerates, then (e) separating the relatively larger agglomerates from the dissociated water and inorganic impurities, and then (f) mixing the separated, relatively larger agglomerates with make-up heavy oil additive to form a coal-in-oil combustible fuel.
Claim 2
Dependent Claim 250 words
An in-line method for the beneficiation of coal and the formation of a coal-in-oil combustible fuel therefrom, comprising: (a) comminuting coal in water to produce a coal-in-water slurry comprising impurity liberated coal particles at least as fine as 40 microns weight mean particle size, then (b) mixing the coal-in-water slurry with light oil as agglomerating liquid having a specific gravity of less than of the order of 1 g/cm 3 to micro-agglomerate the impurity liberated coal particles and primarily dissociate inorganic impurities and some water therefrom, the light oil agglomerating liquid being added at not more than of the order of 20 wt % of the total weight of the solids of the coal-in-water slurry, then (c) separating the micro-agglomerated, impurity liberated coal from the dissociated inorganic impurities and water, then (d) mixing the separated, micro-agglomerated, impurity liberated coal with heavy fuel oil, having a specific gravity greater than of the order of 0.9 g/cm 3 , as agglomerating liquid to produce relatively larger agglomerates comprising an average size no greater than of the order of 3 mm and primarily dissociate water with some inorganic impurities which were present in the micro-agglomerated, impurity liberated coal and leave a residual amount of at least of the order of 5 wt % water in the relatively larger agglomerates, then (e) separating the relatively larger agglomerates from the dissociated water and inorganic impurities, and then (f) mixing the separated, relatively larger agglomerates with make-up heavy oil additive to form a coal-in-oil combustible fuel.
Claim 3
Dependent Claim 44 words
A method according to claim 1, wherein the coal is initially pulverized in a dry pulverizer, air is scrubbed free from the dry, pulverized coal in a wet scrubber and then the scrubbed, pulverized coal is comminuted in water to produce the coal-in-water slurry.
Claim 4
Dependent Claim 43 words
A method according to claim 1, wherein the coal-in-water slurry is stirred with light oil agglomerating liquid initially in a high shear stirring device, to give an initial mixing, and then in at least one relatively lower blade speed, intermediate intensity mixing device.
Claim 5
Dependent Claim 27 words
A method according to claim 1, wherein the light oil as agglomerating liquid is selected from the group consisting of No. 2 fuel oil and diesel oil.
Claim 6
Dependent Claim 28 words
A method according to claim 1, wherein the heavy oil as agglomerating liquid is selected from the group consisting of No. 6 fuel oil and heavy residual oils.

References Cited (Backward Citations)

US3665066A Cited
US4138226A Cited
US4153419A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-08-17 1985-02-16 1985-08-18 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-08-17 1989-02-16 1989-08-18 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-08-17 1993-02-16 1993-08-18 $7700.00 Window Closed / Lapsed

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