US4401638A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for purifying silica sand
Assignee: Materias Primas Monterrey SA
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Filing: 1981-12-21
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Granted: 1983-08-30
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Expires: 2001-12-21
Abstract
Abstract A process of purifying silica sand comprises grinding sandstone, washing and desliming the ground sandstone to remove the major part of the clay-type binder, attrition-scrubbing the deslimed sand particles to release further amounts of binder therefrom, washing and desliming to remove said binder, drying and heating the sand particles, treating the hot sand with sulfuric acid to convert the iron oxides, ferrosilicates and ferro-aluminous impurities into water soluble compounds, attrition-scrubbing the hot suspension of the chemically treated sand to release the strongly adhering stains of said impurities, washing with cold water and desliming, conditioning the sand suspension with fatty acids or petroleum sulfonate collectors, a polyalcohol frothing agent and, if necessary, a mineral acid to bring the pH to from 1.5 to 7.0, carrying out a first froth-flotation to remove the remaining ferrosilicates and iron oxides, and carrying out a second froth-flotation with a fatty amine collector in the presence of sulfuric acid and/or hydrofluoric acid to activate the aluminosilicates and to remove the same at a pH of from 1.5 to 3.5.
Inventors
- 👤 Alejandro J. Caballero
- 👤 Ricardo I. Holcombe
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-07 07:45
CPC Classifications
B; B03; B03D; B03D1/00; B03D1/02; B03B; B03B9/00; B03D1/001; B03D1/002; B03D1/004; B03D1/008; B03D1/01; B03D1/012; C; C03; C03C; C03C1/00; C03C1/02; C03C1/022; B03D2201/00; B03D2201/007; B03D2201/02; B03D2201/04; B03D2203/00; B03D2203/005
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
208 words
A process of purifying silica sand comprising: a. grinding sandstone to obtain sand particles; b. washing and desliming said particles to remove a major portion of clay-type binder contained in said sandstone; c. attrition-scrubbing said deslimed sand particles to release further amounts of said binder from said particles; d. further washing and desliming said sand thereby essentially removing said further amounts of said binder; e. drying and heating said sand; f. treating said hot sand particles with a solution of sulfuric acid to convert at least one of impurities selected from the group consisting of iron oxides, ferro-silicates and ferro-aluminous compounds into water soluble compounds; g. attrition-scrubbing the resulting hot suspension of said acid treated sand particles to release strongly adhering stains of said impurities from said particles; h. washing said suspension with cold water and desliming; i. conditioning said suspension with collectors and frother; j. floating and removing at least one of remaining ferrosilicates and iron oxides in a first flotation step conducted at a pH ranging from 1.5 to 7; and k. floating and removing remaining aluminosilicates in a second flotation step using a fatty amine collector in the presence of at least one activator selected from the group consisting of sulfuric acid and hydrofluoric acid.
Claim 2
Dependent Claim
208 words
A process of purifying silica sand comprising: a. grinding sandstone to obtain sand particles; b. washing and desliming said particles to remove a major portion of clay-type binder contained in said sandstone; c. attrition-scrubbing said deslimed sand particles to release further amounts of said binder from said particles; d. further washing and desliming said sand thereby essentially removing said further amounts of said binder; e. drying and heating said sand; f. treating said hot sand particles with a solution of sulfuric acid to convert at least one of impurities selected from the group consisting of iron oxides, ferro-silicates and ferro-aluminous compounds into water soluble compounds; g. attrition-scrubbing the resulting hot suspension of said acid treated sand particles to release strongly adhering stains of said impurities from said particles; h. washing said suspension with cold water and desliming; i. conditioning said suspension with collectors and frother; j. floating and removing at least one of remaining ferrosilicates and iron oxides in a first flotation step conducted at a pH ranging from 1.5 to 7; and k. floating and removing remaining aluminosilicates in a second flotation step using a fatty amine collector in the presence of at least one activator selected from the group consisting of sulfuric acid and hydrofluoric acid.
Claim 3
Dependent Claim
37 words
The process of claim 1 further comprising the step of adjusting the pH of said suspension to be in the range of 1.5 to 7.0 by use of a mineral acid prior to said first flotation step.
Claim 4
Dependent Claim
34 words
A process according to claim 1 wherein said sand is heated to a temperature of from 100° to 250° C., preferably from 150° to 200° C. before being subjected to said sulfuric acid treatment.
Claim 5
Dependent Claim
43 words
A process according to claim 3 wherein said sulfuric acid treatment is carried out for a period of from 5 to 45 minutes in order to completely solubilize the iron oxides, ferrosilicates and ferro-aluminous impurities which stain the surface of the sand particles.
Claim 6
Dependent Claim
38 words
A process according to claim 4 wherein the attrition following the sulfuric acid treatment is carried out at a solids content of from 65 to 80% and for a period of time of from 1 to 10 minutes.
Claim 7
Dependent Claim
41 words
A process according to claim 1 wherein said first froth flotation is carried out at a pH of from 6 to 7 by using a mixture of oleic and linoleic acids as the collector and a polyalcohol as the foaming agent.
Claim 8
Dependent Claim
40 words
A process according to claim 1 wherein said first froth flotation is carried out at a pH of from 1.5 to 3.5 by using a synthetic petroleum sulfonate collector, in the presence of sulfuric acid and a polyalcohol foaming agent.
Claim 9
Dependent Claim
20 words
A process according to claim 1 wherein said second froth-flotation is effected at a pH of from 1.5 to 3.5.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1986-08-29 | 1987-02-28 | 1987-08-30 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1990-08-29 | 1991-02-28 | 1991-08-30 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1994-08-29 | 1995-02-28 | 1995-08-30 | $7700.00 | Window Closed / Lapsed |