Patent US4244813A successfully refreshed from Google Patents.
US4244813A
Expired / Lapsed
US
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Method of increasing fine coal filtration efficiency
Assignee: Bethlehem Steel Corp
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Filing: 1979-08-08
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Granted: 1981-01-13
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Expires: 1999-08-08
Abstract
Abstract Fine coals suspended in a coal flotation froth are more efficiently filtered when the flotation froth is subjected to a thickening operation prior to filtration. The thickening operation is accomplished by the use of a clarifier or thickener.
Inventors
- 👤 William H. Moyer, Jr.
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 23:02
CPC Classifications
B; B03; B03B; B03B9/00; B03B9/005; B03D; B03D1/00; B03D1/08
Claims Analysis
Total Claims: 6
Claim 1
Independent Claim
172 words
In a coal treatment process wherein raw coal fines of minus 65 mesh size are treated in a flotation process followed by filtration of the resultant flotation froth product containing water, coal particles and froth bubbles to isolate a fine coal product, the improvement comprising: (a) collecting the flotation froth product prior to filtration, (b) treating the collected flotation froth product in a thickening apparatus containing a sufficient body of aqueous liquid to physically decompose a portion of the froth and yield (1) a thickened froth which floats upon the surface of the body of aqueous liquid, (2) a coal containing aqueous liquid stream removed from a point between the surface of the aqueous liquid and the bottom of the thickening apparatus and (3) an underflow of a slurry of minus 65 mesh coal particles which sink to and are removed from the bottom of the thickening apparatus, (c) removing the thickened flotation froth from the thickening apparatus, and (d) filtering the thickened flotation froth to yield minus 65 mesh coal fines.
Claim 2
Dependent Claim
172 words
In a coal treatment process wherein raw coal fines of minus 65 mesh size are treated in a flotation process followed by filtration of the resultant flotation froth product containing water, coal particles and froth bubbles to isolate a fine coal product, the improvement comprising: (a) collecting the flotation froth product prior to filtration, (b) treating the collected flotation froth product in a thickening apparatus containing a sufficient body of aqueous liquid to physically decompose a portion of the froth and yield (1) a thickened froth which floats upon the surface of the body of aqueous liquid, (2) a coal containing aqueous liquid stream removed from a point between the surface of the aqueous liquid and the bottom of the thickening apparatus and (3) an underflow of a slurry of minus 65 mesh coal particles which sink to and are removed from the bottom of the thickening apparatus, (c) removing the thickened flotation froth from the thickening apparatus, and (d) filtering the thickened flotation froth to yield minus 65 mesh coal fines.
Claim 3
Dependent Claim
48 words
The coal treatment process of claim 1 additionally comprising: (a) collecting the underflow or slurried minus 65 mesh coal particles which are removed from the bottom of the thickening apparatus, and (b) combining said collected coal particles with said thickened flotation froth prior to filtration in step (d).
Claim 4
Dependent Claim
70 words
The coal treatment process of claim 2 further comprising: (a) removing the coal containing aqueous liquid stream taken from the thickening apparatus at a point beneath the flotation froth floating on the surface of the aqueous liquid and above the bottom of the thickening apparatus, and (b) returning said aqueous liquid stream to the prior flotation process for removal of minus 65 mesh coal particles suspended in the aqueous liquid.
Claim 5
Independent Claim
166 words
A method for recovering fine coal particles of minus 65 mesh and less from a froth-product containing water obtained in a froth-flotation type fine coal treatment system, comprising: (a) charging a froth-product containing coal fines of 65 mesh and less attached to bubbles within the froth into a thickener apparatus which uses an aqueous liquid body contained within the apparatus as a treatment and separation medium, (b) floating said froth-product upon the surface of said aqueous liquid for a time sufficient to dewater the froth-product and increase the solids content to thereby form a thickened froth-product, (c) skimming the thickened froth-product from atop said aqueous liquid in said thickener into a peripheral launder associated with said thickener, (d) passing said thickened froth-product from said launder to a filtration step, (e) filtering said thickened froth-product to separate said particles of coal from said water, and (f) removing said particles of minus 65 mesh coal as a filter cake and recycling said water to the froth-flotation treatment system.
Claim 6
Independent Claim
166 words
A method for recovering fine coal particles of minus 65 mesh and less from a froth-product containing water obtained in a froth-flotation type fine coal treatment system, comprising: (a) charging a froth-product containing coal fines of 65 mesh and less attached to bubbles within the froth into a thickener apparatus which uses an aqueous liquid body contained within the apparatus as a treatment and separation medium, (b) floating said froth-product upon the surface of said aqueous liquid for a time sufficient to dewater the froth-product and increase the solids content to thereby form a thickened froth-product, (c) skimming the thickened froth-product from atop said aqueous liquid in said thickener into a peripheral launder associated with said thickener, (d) passing said thickened froth-product from said launder to a filtration step, (e) filtering said thickened froth-product to separate said particles of coal from said water, and (f) removing said particles of minus 65 mesh coal as a filter cake and recycling said water to the froth-flotation treatment system.
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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) | 1984-01-13 | 1984-07-14 | 1985-01-13 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1988-01-13 | 1988-07-14 | 1989-01-13 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1992-01-13 | 1992-07-14 | 1993-01-13 | $7700.00 | Window Closed / Lapsed |