US1300516A - Separation of mixed sulfid ores. - Google Patents
Separation of mixed sulfid ores. Download PDFInfo
- Publication number
- US1300516A US1300516A US4084715A US4084715A US1300516A US 1300516 A US1300516 A US 1300516A US 4084715 A US4084715 A US 4084715A US 4084715 A US4084715 A US 4084715A US 1300516 A US1300516 A US 1300516A
- Authority
- US
- United States
- Prior art keywords
- separation
- froth
- mixed
- relatively high
- bleaching powder
- 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 19
- 239000000047 product Substances 0.000 description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 14
- ZKQDCIXGCQPQNV-UHFFFAOYSA-N Calcium hypochlorite Chemical compound [Ca+2].Cl[O-].Cl[O-] ZKQDCIXGCQPQNV-UHFFFAOYSA-N 0.000 description 13
- 239000007844 bleaching agent Substances 0.000 description 13
- 239000011701 zinc Substances 0.000 description 13
- 229910052500 inorganic mineral Inorganic materials 0.000 description 12
- 239000011707 mineral Substances 0.000 description 12
- 229910052725 zinc Inorganic materials 0.000 description 12
- 238000000034 method Methods 0.000 description 10
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 8
- ROOXNKNUYICQNP-UHFFFAOYSA-N ammonium persulfate Chemical compound [NH4+].[NH4+].[O-]S(=O)(=O)OOS([O-])(=O)=O ROOXNKNUYICQNP-UHFFFAOYSA-N 0.000 description 8
- 238000005188 flotation Methods 0.000 description 8
- 239000003795 chemical substances by application Substances 0.000 description 6
- 239000000203 mixture Substances 0.000 description 6
- 238000013019 agitation Methods 0.000 description 5
- 229910052709 silver Inorganic materials 0.000 description 5
- 238000005273 aeration Methods 0.000 description 4
- 229910001870 ammonium persulfate Inorganic materials 0.000 description 4
- 239000012141 concentrate Substances 0.000 description 3
- JRKICGRDRMAZLK-UHFFFAOYSA-L peroxydisulfate Chemical compound [O-]S(=O)(=O)OOS([O-])(=O)=O JRKICGRDRMAZLK-UHFFFAOYSA-L 0.000 description 3
- 241000206607 Porphyra umbilicalis Species 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000004332 silver Substances 0.000 description 2
- 238000011161 development Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 229940044949 eucalyptus oil Drugs 0.000 description 1
- 239000010642 eucalyptus oil Substances 0.000 description 1
- 238000009291 froth flotation Methods 0.000 description 1
- 229910052949 galena Inorganic materials 0.000 description 1
- JQJCSZOEVBFDKO-UHFFFAOYSA-N lead zinc Chemical compound [Zn].[Pb] JQJCSZOEVBFDKO-UHFFFAOYSA-N 0.000 description 1
- XCAUINMIESBTBL-UHFFFAOYSA-N lead(ii) sulfide Chemical compound [Pb]=S XCAUINMIESBTBL-UHFFFAOYSA-N 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000000126 substance 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
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
- B03D1/02—Froth-flotation processes
- B03D1/06—Froth-flotation processes differential
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S209/00—Classifying, separating, and assorting solids
- Y10S209/901—Froth flotation; copper
Definitions
- This invention is for improvements in or relating to the separation of sulfid ores by flotation and it relates more especially to the fractional or differential flotation of .certain sulfids from other sulfids.
- a process for the separation of mixed metalliferous minerals which consists in mixing an orecontaining mixed metalliferous minerals in a finely ground condition with water containing bleaching powder in solution and submitting it to froth flotation separation, whereby products are obtained relatively high in certain values and other prod ucts are'obtained relatively high in'other values.
- a process for the separation of mixed metalliferous minerals which consists in mixin an ore containing mixed metalliferous minerals in finely ground condition with water containing bleaching powder in solution, agitating the mixture to form a froth, and separating the froth, whereby a product relatively high in certain Values is obtained in the froth and a product relatively high in other values is obtained in the residues.
- a process for the separation of mixed metalliferous minerals which consists in mixing an ore containing mixed metalliferous minerals in a finely ground condition with water containing in solution bleaching powder and a small proportion of a frothing agent froth, and separating the froth, whereby a productvrelatively high in certain values is obtained in the froth and a product rela tively high in other values is obtained in the residues.
- a process for the separation of mixed metalliferous minerals which consists in mixing an ore containing mixed metalliferous minerals in a finely ground condition with water containing in solution bleaching powder and a persulfate, and'submitting it to flotation separation, whereby products are obtained relatively high in certain values and other products are obtained relatively high in other values.
- a process for the separation of mixed metalliferous minerals which consists in mixing an ore containing mixed metalliferous minerals in a finely ground condition with water containing in solution bleaching powder and a persulfate, agitating the mixture to form a froth, and separating the froth, whereby a product relatively high in certain values is obtained in the froth and a agitating the mixture to form a product relatively high in other values is obtained in the residues.
- a rocess for the separation of mixed metalli erous minerals which consists in mixing an ore containing mixed metalliferous minerals in a finely ground condition submitting it to flotation separation, whereby a flotation product is obtained relatively high in lead particles and residues are obtained relatively high in zinc particles.
- a process for the separation of zinc and lead which consists in mixing a zinc-lead ore in finely ground condition with water containing bleaching powder in solution, agitating the'mixture to form a froth, and separating the froth, whereby a product relatively high in lead is obtained in the froth and a product relatively high in zinc is obtained in the residues.
- a process for the separation of zinc and lead which consists in mixing a zinclead ore in finely'ground condition with water containing bleaching powder in solution and containing a small quantity of a -frothing agent, agitating the mixture to form a froth, and separating the froth, whereby a product relatively high in lead is obtained in the froth and a product relatively high in zinc is obtained in the residues.
- a process for the separation of zinc and lead which consists in mixing a zinclead ore in finel ground condition with water containing in solution bleaching powder and ammonium persulfate, thereafter adding "a small quantity of a frothing agent, and further agitating the mixture to form a froth, and separating the froth, whereby a product relatively high in lead is obtained in the froth and a product relatively high in zinc is-obtained in the residues.
Landscapes
- Manufacture And Refinement Of Metals (AREA)
Description
' oriuo.
ROWLAND THOMAS DRYLL WILLIAMS, 0]? BROKEN HILL, NEW SOUTH WALES,
AUSTRALIA, ASSIGNOR, BY MESNE ASSIGNMENTS, TO MINERALS SEPARA- TION NORTH AMERICAN CORPORATION.
SEPARATION OF MIXED SULFID ORES.
No Drawing.
To all whom it may concern."
Be it known that I, ROWLAND THoMAs DRYLL WILLIAMS, a subject of the King of England, residing at Broken Hill, New
South Wales, Australia, have invented-cer-' tain new and useful Improvements in the Separation of Mixed Sulfid Ores, of which the following is a specification.
This invention is for improvements in or relating to the separation of sulfid ores by flotation and it relates more especially to the fractional or differential flotation of .certain sulfids from other sulfids.
to Greenway Sulman and Higgins .No.
962678 granted June 28th, 1910, to Greenway and Lavers No. 1064723 granted June 17th, 1913, and to H. H. Greenway No. 1099699 granted June 9th, 1914, in which the ore is subjected to agitation and (or) aeration in Water in the presence of a frothing agent to roduce a scum or froth of metallic sulfids. urther, the invention is a devel opment of that described in the United States Patent No. 1067485 to Nutter and Lavers granted July 15th, 1913, that is to say, a separation is effected between the different metallic sulfids in the agitation-froth process by varying the controlling conditions, and particularly the chemical constitution of the solution employed. This invention is applicable to other methods of flotation separation, such as that known as film flotation and the'like.
I have discovered that by the addition t the circuit liquor or to the water in which the ore is suspended of bleaching powder with or without a persulfate such as ammonium persulfate a differential or preferential flotation separation of certain sulfids (such as galena) from other sulfids (such as blende) may be obtained.
I will now give some illustrations of the Specification of Letters Patent.
.low in zinc.
Patented Apr. 15, 1919.
Application filed July 20, 1915. Serial No. 40,847.
application of this invention to certain m1xed sulfid ores, though it will be understood that I do not confine myself to these conditions.
A sample of 153 lbs. of a Broken Hill slime was subjected to agitation and aeratlon in water to which 16 ozs. of bleaching powder and 6 ozs. of ammonium persulfate were added. When thoroughly agitated one oz. of eucalyptus oil Was added, and a further amount of one oz. of the oil was again added durlng the operation. Float concentrates were removed at intervals which were found to be relatively rich in lead and silver and The residues were found to be relatively low in silver and lead.
A sample of 2 lbs. of Broken Hill slimes assaying P1). 19.5%, Zn. 24.4% was su|b-. Jected to agitation and aeration in water to which an amount of bleaching powder had been added equivalent to 25 lbs. per ton and an amount of ammonium persulfate equiva lent to 25 lbs. per ton (without the addition of any other frothing agent) when float concentrates were obtained assaying Pb. 50.3% and Zn. 14.2%.
Another sample of 150 lbs. of, Broken Hill slimes assayin Pb. 10.2%, Zn. 16% and Ag.
v7 .1 ozs. was su jected to agitation and aeration in water to which an amount of bleaching powder equivalent to 17.5 lbs. per tonthe addition of any other frothing agent) when float concentrates were obtained assaying Pb. Zn. 14% and Ag. 49.2 ozs. per ton giving a recovery of 84.9% P-b.
Another sampleof 150 lbs. of Broken Hill slimes assaying Pb. 10.2%, Zn. 16% and Ag. 7.1 ozs. was subjected to agitation and aeration in water to which was added an amount of bleaching powder equivalent to 17.5 lbs. per ton of ore treated and an.
amount of iron-ammonium-alum equivalent to secure by Letters Patent is 1. A process for the separation of mixed metalliferous minerals which consists in mixing an orecontaining mixed metalliferous minerals in a finely ground condition with water containing bleaching powder in solution and submitting it to froth flotation separation, whereby products are obtained relatively high in certain values and other prod ucts are'obtained relatively high in'other values.
2. A process for the separation of mixed metalliferous minerals which consists in mixin an ore containing mixed metalliferous minerals in finely ground condition with water containing bleaching powder in solution, agitating the mixture to form a froth, and separating the froth, whereby a product relatively high in certain Values is obtained in the froth and a product relatively high in other values is obtained in the residues.
3. A process for the separation of mixed metalliferous minerals which consists in mixing an ore containing mixed metalliferous minerals in a finely ground condition with water containing in solution bleaching powder and a small proportion of a frothing agent froth, and separating the froth, whereby a productvrelatively high in certain values is obtained in the froth and a product rela tively high in other values is obtained in the residues. v
4:. A process for the separation of mixed metalliferous minerals which consists in mixing an ore containing mixed metalliferous minerals in a finely ground condition with water containing in solution bleaching powder and a persulfate, and'submitting it to flotation separation, whereby products are obtained relatively high in certain values and other products are obtained relatively high in other values.
5. A process for the separation of mixed metalliferous minerals which consists in mixing an ore containing mixed metalliferous minerals in a finely ground condition with water containing in solution bleaching powder and a persulfate, agitating the mixture to form a froth, and separating the froth, whereby a product relatively high in certain values is obtained in the froth and a agitating the mixture to form a product relatively high in other values is obtained in the residues.'
6. A rocess for the separation of mixed metalli erous minerals which consists in mixing an ore containing mixed metalliferous minerals in a finely ground condition submitting it to flotation separation, whereby a flotation product is obtained relatively high in lead particles and residues are obtained relatively high in zinc particles.
8. A process for the separation of zinc and lead which consists in mixing a zinc-lead ore in finely ground condition with water containing bleaching powder in solution, agitating the'mixture to form a froth, and separating the froth, whereby a product relatively high in lead is obtained in the froth and a product relatively high in zinc is obtained in the residues.
9. A process for the separation of zinc and lead which consists in mixing a zinclead ore in finely'ground condition with water containing bleaching powder in solution and containing a small quantity of a -frothing agent, agitating the mixture to form a froth, and separating the froth, whereby a product relatively high in lead is obtained in the froth and a product relatively high in zinc is obtained in the residues.
10. A process for the separation of zinc and lead which consists in mixing a zinclead ore in finel ground condition with water containing in solution bleaching powder and ammonium persulfate, thereafter adding "a small quantity of a frothing agent, and further agitating the mixture to form a froth, and separating the froth, whereby a product relatively high in lead is obtained in the froth and a product relatively high in zinc is-obtained in the residues.
In testimony whereof I have signed my name to this specification in the presence of two subscribing witnesses.
ROWLAND THOMAS DRYLL WILLIAMS.
Witnesses:
ARTH R GORE CoLLIsoN, LESLIE HERBERT BROADBENT.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US4084715A US1300516A (en) | 1915-07-20 | 1915-07-20 | Separation of mixed sulfid ores. |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US4084715A US1300516A (en) | 1915-07-20 | 1915-07-20 | Separation of mixed sulfid ores. |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1300516A true US1300516A (en) | 1919-04-15 |
Family
ID=3368057
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US4084715A Expired - Lifetime US1300516A (en) | 1915-07-20 | 1915-07-20 | Separation of mixed sulfid ores. |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1300516A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6827220B1 (en) * | 1998-08-11 | 2004-12-07 | Versitech, Inc. | Flotation of sulfide mineral species with oils |
-
1915
- 1915-07-20 US US4084715A patent/US1300516A/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6827220B1 (en) * | 1998-08-11 | 2004-12-07 | Versitech, Inc. | Flotation of sulfide mineral species with oils |
| US20060000753A1 (en) * | 1998-08-11 | 2006-01-05 | Young Tom L | Flotation of sulfide mineral species with oils |
| US7461745B2 (en) | 1998-08-11 | 2008-12-09 | Nalco Company | Flotation of sulfide mineral species with oils |
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