US2385079A - Use of lime in heavy-media separation process - Google Patents
Use of lime in heavy-media separation process Download PDFInfo
- Publication number
- US2385079A US2385079A US465910A US46591042A US2385079A US 2385079 A US2385079 A US 2385079A US 465910 A US465910 A US 465910A US 46591042 A US46591042 A US 46591042A US 2385079 A US2385079 A US 2385079A
- Authority
- US
- United States
- Prior art keywords
- medium
- constituents
- sink
- float
- ore
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 238000000926 separation method Methods 0.000 title description 8
- 235000008733 Citrus aurantifolia Nutrition 0.000 title description 4
- 235000011941 Tilia x europaea Nutrition 0.000 title description 4
- 239000004571 lime Substances 0.000 title description 4
- 239000000470 constituent Substances 0.000 description 35
- 238000000034 method Methods 0.000 description 20
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 18
- 229910000519 Ferrosilicon Inorganic materials 0.000 description 14
- 239000007787 solid Substances 0.000 description 13
- 229910052784 alkaline earth metal Inorganic materials 0.000 description 10
- 150000004649 carbonic acid derivatives Chemical class 0.000 description 10
- 230000005484 gravity Effects 0.000 description 10
- 150000001342 alkaline earth metals Chemical class 0.000 description 9
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 9
- 239000000920 calcium hydroxide Substances 0.000 description 9
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 9
- 239000001569 carbon dioxide Substances 0.000 description 9
- 229910002092 carbon dioxide Inorganic materials 0.000 description 9
- 238000006124 Pilkington process Methods 0.000 description 8
- 230000001464 adherent effect Effects 0.000 description 7
- ZLNQQNXFFQJAID-UHFFFAOYSA-L magnesium carbonate Chemical compound [Mg+2].[O-]C([O-])=O ZLNQQNXFFQJAID-UHFFFAOYSA-L 0.000 description 7
- 239000001095 magnesium carbonate Substances 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 6
- 235000014380 magnesium carbonate Nutrition 0.000 description 6
- 229910000021 magnesium carbonate Inorganic materials 0.000 description 6
- 229910001420 alkaline earth metal ion Inorganic materials 0.000 description 5
- 239000007900 aqueous suspension Substances 0.000 description 5
- 150000001875 compounds Chemical class 0.000 description 5
- 239000012634 fragment Substances 0.000 description 5
- 239000003513 alkali Substances 0.000 description 4
- 150000001341 alkaline earth metal compounds Chemical class 0.000 description 4
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L calcium sulfate Chemical compound [Ca+2].[O-]S([O-])(=O)=O OSGAYBCDTDRGGQ-UHFFFAOYSA-L 0.000 description 4
- 230000006866 deterioration Effects 0.000 description 4
- 229910052712 strontium Inorganic materials 0.000 description 4
- CIOAGBVUUVVLOB-UHFFFAOYSA-N strontium atom Chemical compound [Sr] CIOAGBVUUVVLOB-UHFFFAOYSA-N 0.000 description 4
- BVKZGUZCCUSVTD-UHFFFAOYSA-M Bicarbonate Chemical class OC([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-M 0.000 description 3
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 3
- 229910052788 barium Inorganic materials 0.000 description 3
- DSAJWYNOEDNPEQ-UHFFFAOYSA-N barium atom Chemical compound [Ba] DSAJWYNOEDNPEQ-UHFFFAOYSA-N 0.000 description 3
- 229910052791 calcium Inorganic materials 0.000 description 3
- 239000011575 calcium Substances 0.000 description 3
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- -1 alkaline earth metal carbonates Chemical class 0.000 description 2
- RQPZNWPYLFFXCP-UHFFFAOYSA-L barium dihydroxide Chemical compound [OH-].[OH-].[Ba+2] RQPZNWPYLFFXCP-UHFFFAOYSA-L 0.000 description 2
- 229910001863 barium hydroxide Inorganic materials 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 229910052710 silicon Inorganic materials 0.000 description 2
- 239000010703 silicon Substances 0.000 description 2
- 241000120283 Allotinus major Species 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- XZMCDFZZKTWFGF-UHFFFAOYSA-N Cyanamide Chemical compound NC#N XZMCDFZZKTWFGF-UHFFFAOYSA-N 0.000 description 1
- 229910017082 Fe-Si Inorganic materials 0.000 description 1
- 229910017133 Fe—Si Inorganic materials 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- 150000001450 anions Chemical class 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 229910000514 dolomite Inorganic materials 0.000 description 1
- 239000010459 dolomite Substances 0.000 description 1
- 150000004679 hydroxides Chemical class 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 235000011160 magnesium carbonates Nutrition 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- UUCCCPNEFXQJEL-UHFFFAOYSA-L strontium dihydroxide Chemical compound [OH-].[OH-].[Sr+2] UUCCCPNEFXQJEL-UHFFFAOYSA-L 0.000 description 1
- 229910001866 strontium hydroxide Inorganic materials 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03B—SEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
- B03B5/00—Washing granular, powdered or lumpy materials; Wet separating
- B03B5/28—Washing granular, powdered or lumpy materials; Wet separating by sink-float separation
- B03B5/30—Washing granular, powdered or lumpy materials; Wet separating by sink-float separation using heavy liquids or suspensions
- B03B5/44—Application of particular media therefor
- B03B5/442—Application of particular media therefor composition of heavy media
Definitions
- This invention relates to an improved process of beneficiation of ores containing carbonates by the sink and float process in a heavy medium.
- carbonate'ores and particularly ores containing carbonates of the alkaline earth metals, especially magnesite can be treated satisfactorily by a sink and fioat process with ferrosilicon medium if there is present in the medium a suflicient amount of anion of an alkaline earth metal in a form in which it is capable of reacting with carbon dioxide or bicarbonates.
- carbon dioxide is a serious factor in deterioration of ferrosilicon medium in the presence of carbonates such as carbonates of the alkaline earth metals.
- alkaline earth metal compounds such as calcium sulfate
- calcium hydroxide is the cheapest alkaline earth metal compound available and as it is also one of the best for use in the present invention it is preferred.
- Barium hydroxide and strontium hydroxide are of about equal activity but more expensive. The particular compound which sets free in water solution the alkaline earth metal ion is, therefore, not of great importance, although there is-some slight difference in efiectiveness between different compounds.
- the present invention should not be confused with the use of alkalies to prevent the attack of water on ferrosilicon at low pHs in the absence of carbonate ores.
- This phenomenon that is to say, the reaction of ferrosilicon with water in acid mediums is well known and can be counteracted to a large extent by the addition of any alkali.
- hydroxides of the alkaline earth metals will also produce this result, but it is apparently an entirely different result than that of the present invention because the improvements of the present invention are obtained when the alkaline earth metal compounds are not alkalies and the addition of alkalies which do not contain alkaline earth metal ions will not effect protection in the case of ferrosilicon media used with carbonate ores.
- Example 1 mixed with suflicient water to produce a medium having a specific gravity of 2.89. Th medium was transferred into a small cone and held in suspension by blowing air therethrough. 2.2 parts of a magnesite ore from the Pacific Northwest was added, the ore being sized i" tomesh, corresponding to the size of ore suitable for commercial treatment. Further samples of the same medium were prepared andrall oi the sample media were agitated by aeration in the cone for a period of 48 hours, samples being taken at 24 hour intervals. The first test sample received no addition; the second 7 lbs. per ton of calcium hydroxide; the third 18 lbs. per ton of barium hydroxide containing 8 molecules of water; the fourth 12 lbs.
- a method of beneficiating ores containing carbonates of the alkaline earth metals as a major constituent of the ore by the sink and float process which comprises subjecting fragments of the ore of a size suitable for sink and float separation to the action of a medium comprising an aqueous suspension or finelv divided ferroseconds by the Marsh funnel test (500/500).
- Example 2 A ferrosilicon medium was prepared as described in Example 1 and used for the sink and -float separation of dolomite from magnesite.
- the improved process of the present invention is applicable to other ores containing magnesium or other alkaline earth carbonates or carbonates of other metals, the action with magnesium carbonate being typical.
- the rate of deterioration of the medium will vary somewhat with different carbonate ores depending to a considerable extent at least on the tendency of the carbonate to form a bicarbonate by reaction with carbon dioxide of the air.
- a method of beneficiating ores containing carbonates as a. major constituent of the ore by the sink and 'float process which comprises sub- I the lighter? constituents oi the ore, whereby the lighter constituents float and the heavier constituents sink, removing the floating constituents and sinking constituents, removing adherent medium solids therefrom, said process involving extensive exposure to atmosphere, reusing said medium solids, and maintaining the viscosity of the medium by the addition of a sufllcient amount of a compound of an alkaline earth metal included in the group consisting of calcium, strontium and barium, and capable of reacting with gaseous carbon dioxide to maintain at all times free alkaline earth metal ions in the medium.
- a method of beneficiating ores containing magnesium carbonates as a major constituent of the ore by the sink and float process which comprises subjecting fragments of the ore of a size suitable for sink and float separation to the action of a medium comprising an aqueous suspension of finely divided ferrosilicon and having a specific gravity greater than the lighter constituents of the ore, whereby the lighter constituents float and the heavier constituents sink, removing the floating constituents and sinking constituents.
- a method of beneficiating ores containing carbonates as a major constituent of the ore by the sink and float process which comprises subjecting fragments of the ore of a size suitable for sink and float separation to the action of a medium comprising an aqueous suspension of finely divided ferrosilicon and having a specific gravity greater than the lighter constituents of the ore, whereby the lighter constituents float and the heavier constituents sink, removing the floating constituents and sinking constituents; removing adherent medium solids therefrom, said process involving extensive exposure to the at-- mosphere, reusing said medium solids, and maintaining the viscosity of the medium by the addition of calcium hydroxide to maintain at all times free calcium hydroxide in'the medium.
- a method of beneflciating ores containing carbonates of the alkaline earth metals as a major constituent of the ore by the sink and float process which comprises subjecting fragments of the ore of a size suitable for sink and float separation to the action of a medium comprising an aqueous suspension of finely divided a specific gravity greater than the lighter constituents of the ore, whereby the lighter constituents float and the heavier constituents sink,
Landscapes
- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
Description
Patented Sept. 18, 1945 USE OF LIME IN HEAVY-MEDIA SEPARATION PROCESS Norman Hedley and John Joseph Kress, Stamford, Conn, asslgnors to American Cyanamid mpany, New- York, N. Y., a corporation of No Drawing. Application November 17, 1942,
Serial No. 465,910
.6 Claims. (Cl. 209173) This invention relates to an improved process of beneficiation of ores containing carbonates by the sink and float process in a heavy medium.
Heavy media processes for beneficiation of ores by sink and float processes have attained great the ore, frequently gangue, float. It is necessary to remove adherent medium from both the float product and the sink product and a cleaning process is, therefore, necessary because usually the medium solids are sufliciently valuable so that they cannot be thrown away economically. This has made an improved heavy media process using magnetizable solids, particularly useful in the treatment of many ores, as the medium adhering to the sink and float product can be washed off and cleaned from associated impurities by simple magnetic cleaning. Among the magnetizable solids which can be used in this improved heavy media process ferrosilicon has many advantages as it has a high specific gravity and at the same time shows quite adequate rust resistance for most operations.
An important class of ores which can be bene-,
ficiated by the use of heavy media are the carbonate ores, of which those containing alkaline earth metal carbonates such as magnesite are of medium becomes entirely unusable. As it is obviously economically impractical to discard ferro-' silicon medium daily it appeared that magnesite ores could not be beneiiciated satisfactorily by sink and float process .using-ferrosilicon.
According to the present invention it has been found that carbonate'ores and particularly ores containing carbonates of the alkaline earth metals, especially magnesite, can be treated satisfactorily by a sink and fioat process with ferrosilicon medium if there is present in the medium a suflicient amount of anion of an alkaline earth metal in a form in which it is capable of reacting with carbon dioxide or bicarbonates. We have determined that carbon dioxide is a serious factor in deterioration of ferrosilicon medium in the presence of carbonates such as carbonates of the alkaline earth metals. While it seems probable that the action of carbon dioxide or of bicarbonates formed therewith on the ferrosilicon is a major factor in the deterioration of the ferrosilicon medium and may perhaps be the only factor, it is not desired to limit the invention to a theory in which the action of carbon dioxide is the only factor.
Within considerable limits the process of the,
present invention appears to be relatively unaffected by pH although of course an extremely acid circuit will cause rapid decomposition of the ferrosilicon. The relative unimportance of pH within considerable limits is shown by the fact that alkaline earth metal compounds, such as calcium sulfate, which are capable of reacting with carbon dioxide are effective and it is not necessary to use a basic alkaline earth metal compound, such as calcium hydroxide. However, calcium hydroxide is the cheapest alkaline earth metal compound available and as it is also one of the best for use in the present invention it is preferred. Barium hydroxide and strontium hydroxide are of about equal activity but more expensive. The particular compound which sets free in water solution the alkaline earth metal ion is, therefore, not of great importance, although there is-some slight difference in efiectiveness between different compounds.
The present invention should not be confused with the use of alkalies to prevent the attack of water on ferrosilicon at low pHs in the absence of carbonate ores. This phenomenon, that is to say, the reaction of ferrosilicon with water in acid mediums is well known and can be counteracted to a large extent by the addition of any alkali. Of course, hydroxides of the alkaline earth metals will also produce this result, but it is apparently an entirely different result than that of the present invention because the improvements of the present invention are obtained when the alkaline earth metal compounds are not alkalies and the addition of alkalies which do not contain alkaline earth metal ions will not effect protection in the case of ferrosilicon media used with carbonate ores.
The invention will be described in greater detail in conjunction with the followin examples:
Example 1 mixed with suflicient water to produce a medium having a specific gravity of 2.89. Th medium was transferred into a small cone and held in suspension by blowing air therethrough. 2.2 parts of a magnesite ore from the Pacific Northwest was added, the ore being sized i" tomesh, corresponding to the size of ore suitable for commercial treatment. Further samples of the same medium were prepared andrall oi the sample media were agitated by aeration in the cone for a period of 48 hours, samples being taken at 24 hour intervals. The first test sample received no addition; the second 7 lbs. per ton of calcium hydroxide; the third 18 lbs. per ton of barium hydroxide containing 8 molecules of water; the fourth 12 lbs. per ton of strontium by droxide containing 8 molecules of water; the fifth 8 lbs. per ton of calcium sulfate containing 2 molecules of water; and the sixth was aerated with air from which all carbon dioxide had been removed by passing through a 33% KOH solution. The results of the tests are shown in the following table, the viscosity being measured in iecting fragments of the ore of a size suitable for sink and float separation to the action of a medium comprising an aqueous suspension of finely divided ierrosilicon and having a specific gravity greater than the lighter constituents of the ore, whereby the lighter constituents float and the heavier constituents slnk, removing the floating constituents and sinking constituents, removing adherent medium solids therefrom, said process involving extensive exposure to the atmosphere, reusing said medium solids, and maintaining the viscosity of the medium-by the addition of a sufflcient amount of a compound oi an alkaline earth metal included in the group consisting of calcium, strontium and barium, and capable of reacting with gaseous carbon dioxideto maintain at all times alkaline earth metal ions in the medium.
2. A method of beneficiating ores containing carbonates of the alkaline earth metals as a major constituent of the ore by the sink and float process, which comprises subjecting fragments of the ore of a size suitable for sink and float separation to the action of a medium comprising an aqueous suspension or finelv divided ferroseconds by the Marsh funnel test (500/500). silicon and having a specific gravity greater than Characteristics of Fc-Bi medium Test No; Reagent added, lbalton Fe-Si Start of tent Alter 24 hours Alter 48 hours Viscosity Appearance Viscmlty Appearance Viscosity Appearance Seconds Seconds Seconds None- 22.5 Clean, black" 25.5 Green 41.0 Thick light green. 'llbs-lton GB(OH)Q 23.0 o 22.5 Clean, black- 22.0 Clean, black. 18lbs./tonBa(0H):.8Hi0. 22.0 n 21.5 .do 22.0 Do. 12 lbs.lton Sr(0H)s.8Ha0 23. 5 o 23. 0 Do. -lton c880i.2H2o 23.5 c.o 25.0 Do. 00: removed 23, 0 r n 22. 0 Do.
Example 2 A ferrosilicon medium was prepared as described in Example 1 and used for the sink and -float separation of dolomite from magnesite.
The process'was continued for many days and 3 parts of calcium hydroxide were added to the medium per day. Deterioration of the medium was practically negligible there being substantially no increase in viscosity and the medium remaining-a clean black without gelatinous green slime. The addition of lime did not afiect in any way the sink-and float procedure, except that slightly less ferrosilicon was needed to produce the same specific gravity as the added lime contributed slightly to increase the specific gravity.
A control test was run with the same ore but without the addition of calcium hydroxide. The viscosity of the medium increased rapidly and after less than 48Vhours it had become so viscous as to be practically unusable. The same characteristic gelatinous green slime was also noted. 4
The improved process of the present invention is applicable to other ores containing magnesium or other alkaline earth carbonates or carbonates of other metals, the action with magnesium carbonate being typical. The rate of deterioration of the medium will vary somewhat with different carbonate ores depending to a considerable extent at least on the tendency of the carbonate to form a bicarbonate by reaction with carbon dioxide of the air.
We claim:
l. A method of beneficiating ores containing carbonates as a. major constituent of the ore by the sink and 'float process, which comprises sub- I the lighter? constituents oi the ore, whereby the lighter constituents float and the heavier constituents sink, removing the floating constituents and sinking constituents, removing adherent medium solids therefrom, said process involving extensive exposure to atmosphere, reusing said medium solids, and maintaining the viscosity of the medium by the addition of a sufllcient amount of a compound of an alkaline earth metal included in the group consisting of calcium, strontium and barium, and capable of reacting with gaseous carbon dioxide to maintain at all times free alkaline earth metal ions in the medium.
3. A method of beneficiating ores containing magnesium carbonates as a major constituent of the ore by the sink and float process, which comprises subjecting fragments of the ore of a size suitable for sink and float separation to the action of a medium comprising an aqueous suspension of finely divided ferrosilicon and having a specific gravity greater than the lighter constituents of the ore, whereby the lighter constituents float and the heavier constituents sink, removing the floating constituents and sinking constituents. removing adherent medium solids therefrom, said process involving extensive exposure to the at- 'nosphere, reusing said medium solids, and maintaining the viscosity of the medium by the addition of a sufflcient amount of a compound of an alkaline earth metal included in the group consisting of calcium, strontium and barium, and capable of reacting with gaseous carbon dioxide to maintain at all times free alkaline earth metal ions in the medium.
4. A method of beneficiating ores containing carbonates as a major constituent of the ore by the sink and float process, which comprises subiecting fragments of the ore of a size suitable for sink and float separation to the action of a medium comprising an aqueous suspension of finely divided ferrosilicon and having a specific gravity greater than the lighter constituents of the ore, whereby the lighter constituents float and the heavier constituents sink, removing the floating constituents and sinking constituents; removing adherent medium solids therefrom, said process involving extensive exposure to the at-- mosphere, reusing said medium solids, and maintaining the viscosity of the medium by the addition of calcium hydroxide to maintain at all times free calcium hydroxide in'the medium.
1 5. A method of beneflciating ores containing carbonates of the alkaline earth metals as a major constituent of the ore by the sink and float process, which comprises subjecting fragments of the ore of a size suitable for sink and float separation to the action of a medium comprising an aqueous suspension of finely divided a specific gravity greater than the lighter constituents of the ore, whereby the lighter constituents float and the heavier constituents sink,
ierrosilicon and having a specific gravity greater than the lighter constituents of the ore, whereby the lighter constituents float and the heavier constituents sink, removing the floating-constituents and sinking constituents, removing adherent meremoving the floating constituents and sinking constituents, removing adherent medium solids therefrom, said process involving extensive exposure to the atmosphere, reusing said medium solids and maintaining low viscosity by the addition of sumcient calcium hydroxide to maintain at all times free calcium hydroxide in the medium.
NORMAN HEDIEY. JOHN JOSEPH KRESS.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US465910A US2385079A (en) | 1942-11-17 | 1942-11-17 | Use of lime in heavy-media separation process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US465910A US2385079A (en) | 1942-11-17 | 1942-11-17 | Use of lime in heavy-media separation process |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2385079A true US2385079A (en) | 1945-09-18 |
Family
ID=23849663
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US465910A Expired - Lifetime US2385079A (en) | 1942-11-17 | 1942-11-17 | Use of lime in heavy-media separation process |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US2385079A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2526519A (en) * | 1946-12-24 | 1950-10-17 | Separation Process Company | Preparation of calcareous cement raw material |
| US3578162A (en) * | 1969-10-01 | 1971-05-11 | Basic Inc | Beneficiation of magnesian ores or the like |
| US4189103A (en) * | 1978-03-10 | 1980-02-19 | International Minerals & Chemical Corporation | Method of beneficiating phosphate ores |
-
1942
- 1942-11-17 US US465910A patent/US2385079A/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2526519A (en) * | 1946-12-24 | 1950-10-17 | Separation Process Company | Preparation of calcareous cement raw material |
| US3578162A (en) * | 1969-10-01 | 1971-05-11 | Basic Inc | Beneficiation of magnesian ores or the like |
| US4189103A (en) * | 1978-03-10 | 1980-02-19 | International Minerals & Chemical Corporation | Method of beneficiating phosphate ores |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US4772382A (en) | Froth flotation of bastnaesite | |
| LU505722B1 (en) | Flotation reagent and flotation method for marmatite and jamesonite | |
| US2385079A (en) | Use of lime in heavy-media separation process | |
| CN106423572A (en) | Lead zinc ore flotation method adopting novel combined inhibitor | |
| CN104150489A (en) | Quartz ore purification method and quartz product thereof | |
| US3128248A (en) | Method for the purification of brine | |
| US4008151A (en) | Process for enrichment, by flotation, of phosphate ores with gangues containing carbonates | |
| US938432A (en) | Removal of silica in the manufacture of alumina. | |
| US1801318A (en) | Concentration of ores | |
| US2168762A (en) | cacos | |
| RU2164824C2 (en) | Apatite or flotation process | |
| US4040519A (en) | Froth flotation process for recovering sheelite | |
| US1807860A (en) | Separation of minerals | |
| CN110882827A (en) | Mineral processing method for improving quality and removing impurities from flotation niobium concentrate | |
| US4147614A (en) | Aqueous mixture of diesel oil, pine oil and diamine for conditioning of crushed magnesite ore in magnetic beneficiation process | |
| SU1058136A1 (en) | Collector for ore flotation | |
| US2393160A (en) | Separation of ores by the sink and float process | |
| US2292503A (en) | Purification of calcium carbonate | |
| SU1103900A1 (en) | Method of magnetic separation of iron ores | |
| US1079107A (en) | Ore concentration. | |
| US3382976A (en) | Method for preventing activation of silica in ore flotation | |
| SU1556759A1 (en) | Method of flotation of difficultly dressed graphite ores | |
| US1542684A (en) | Process for obtaining magnesia from dolomite | |
| US1628046A (en) | Ore flotation process | |
| US1863760A (en) | Separation of minerals by flotation |