US4284244A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for producing high grade molybdenum disulfide powder
Assignee: Cyprus Amax Minerals Co
•
Filing: 1979-09-19
•
Granted: 1981-08-18
•
Expires: 1999-09-19
Abstract
Abstract A process for producing a high grade molybdenum disulfide powder suitable for use in the formulation of chemicals and as an intermediate for synthesizing high purity molybdenum compounds by which an impure particulated molybdenite concentrate feed material is pulverized and thereafter is subjected to a plurality of purification treatments to effect a progressive extraction of the contaminating mineral constituents entrapped within the molybdenite particles. The purification treatments comprise a wash treatment of the molybdenite concentrate containing up to 10% by weight of hydrocarbon oil employing an aqueous solution forming a slurry which is subjected to successive steps of high shear agitation and low shear agitation to break up the agglomerated molybdenite particles and to effect a release of the mechanically entrapped very fine mineral particles which remain suspended in the aqueous liquid phase. At the completion of the high and low shear treatment, the slurry is transferred to a separator in which the agglomerated molybdenite particles are extracted from the predominant portion of the liquid phase which contains a substantial proportion of the released mineral contaminants. The molybdenite concentrate and the aqueous wash solution are transferred through the plurality of purification treatments in a countercurrent fashion. The resulting agglomerated molybdenite concentrate, free of the contaminants, is then subjected to regular froth flotation to remove any coarse contaminants.
Inventors
- 👤 Maurice R. Hoover
- 👤 Deepak Malhotra
- 👤 Fredrick N. Bender
- 👤 Richard A. Ronzio
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-31 13:48
CPC Classifications
B; B03; B03B; B03B9/00; B03D; B03D1/00; B03D1/02; B03D3/00; B03D3/06; B03D1/14; B03D1/1406
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
270 words
A process for producing a high purity molybdenum disulfide powder which comprises the steps of providing an impure particulated molybdenite concentrate, comminuting said concentrate, if necessary, to reduce its average particle size to a point where plus 99% liberation between gangue and molybdenite particles is obtained adjusting said concentrate if necessary to contain an oily substance in an amount of about 1-10% by weight; subjecting said concentrate comprising oily agglomerates of finely divided smaller molybdenite particles to a plurality of purification treatments each comprising: (a) forming a mixture of said concentrate with an aqueous solution to provide a solids concentration of about 1% to about 40%. (b) subjecting said mixture to a high shear agitation to break up the molybdenite particle agglomerates and to release at least a portion of the hydrophilic particulate contaminants mechanically entrapped therein and to effect a suspension of said particulate contaminants in the liquid phase, (c) introducing the said mixture into a quiescent zone to enable reagglomeration of the molybdenite particles while retaining a substantial portion of the released said particulate contaminants in the liquid phase, (d) separating the reagglomerated said molybdenite particles in the form of a slurry from a predominant portion of the liquid phase, (e) transferring the liquid phase to a next preceding purification treatment and transferring the separated slurry of reagglomerated said molybdenite particles to a next succeeding purification treatment in countercurrent fashion; and discarding the liquid phase as separated from the first of the plurality of said purification treatments and recovering the purified agglomerated molybdenum disulfide particles from the slurry separated from the last of the plurality of purification treatments.
Claim 2
Dependent Claim
270 words
A process for producing a high purity molybdenum disulfide powder which comprises the steps of providing an impure particulated molybdenite concentrate, comminuting said concentrate, if necessary, to reduce its average particle size to a point where plus 99% liberation between gangue and molybdenite particles is obtained adjusting said concentrate if necessary to contain an oily substance in an amount of about 1-10% by weight; subjecting said concentrate comprising oily agglomerates of finely divided smaller molybdenite particles to a plurality of purification treatments each comprising: (a) forming a mixture of said concentrate with an aqueous solution to provide a solids concentration of about 1% to about 40%. (b) subjecting said mixture to a high shear agitation to break up the molybdenite particle agglomerates and to release at least a portion of the hydrophilic particulate contaminants mechanically entrapped therein and to effect a suspension of said particulate contaminants in the liquid phase, (c) introducing the said mixture into a quiescent zone to enable reagglomeration of the molybdenite particles while retaining a substantial portion of the released said particulate contaminants in the liquid phase, (d) separating the reagglomerated said molybdenite particles in the form of a slurry from a predominant portion of the liquid phase, (e) transferring the liquid phase to a next preceding purification treatment and transferring the separated slurry of reagglomerated said molybdenite particles to a next succeeding purification treatment in countercurrent fashion; and discarding the liquid phase as separated from the first of the plurality of said purification treatments and recovering the purified agglomerated molybdenum disulfide particles from the slurry separated from the last of the plurality of purification treatments.
Claim 3
Dependent Claim
20 words
The process as defined in claim 1, in which at least three of said plurality of purification treatments are employed.
Claim 4
Dependent Claim
31 words
The process as defined in claim 1, in which the step of comminuting said concentrate, if necessary, is performed to reduce its average particle size to less than about 15 microns.
Claim 5
Dependent Claim
35 words
The process as defined in claim 1, in which the step of forming a mixture of said concentrate with an aqueous solution is performed to provide a solids concentration of about 5% to about 15%.
Claim 6
Dependent Claim
40 words
The process as defined in claim 1, including the further step of subjecting the recovered reagglomerated said purified molybdenum disulfide particles from a last purification treatment to a supplemental froth flotation extraction operation to remove residual coarse contaminating particles therefrom.
Claim 7
Dependent Claim
28 words
The process as defined in claim 1, in which said aqueous solution employed for forming said mixture comprises water containing controlled amounts of depressant agents and wetting agents.
Claim 8
Dependent Claim
41 words
The process as defined in claim 1, in which said aqueous solution employed for forming said mixture comprises an aqueous solution containing agents for adjusting the pH of said aqueous solution to within a range of about 8 to about 9.
Claim 9
Dependent Claim
28 words
The process as defined in claim 1, in which the step (b) is performed by subjecting said mixture to high-shear agitation in a chamber incorporating a high-shear agitator.
Claim 10
Dependent Claim
27 words
The process as defined in claim 1, in which the step (b) of subjecting said mixture to high-shear agitation is performed by a high speed centrifugal pump.
Claim 11
Dependent Claim
33 words
The process as defined in claim 1, in which the step (d) of separating the reagglomerated said molybdenite particles from a predominant portion of the liquid phase is performed in a settling unit.
Claim 12
Dependent Claim
32 words
The process as defined in claim 1, in which the step (d) of separating the reagglomerated said molybdenite particles from a predominant portion of the liquid phase is performed in a cyclone.
References Cited (Backward Citations)
US763259A
Cited
US1421862A
Cited
US2113727A
Cited
US2845936A
Cited
US3045818A
Cited
US3230282A
Cited
US3268071A
Cited
US3307790A
Cited
US3298617A
Cited
US3401794A
Cited
US3572500A
Cited
JPS479669U
Cited
US3919079A
Cited
US4089776A
Cited
US4083921A
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 |