US1560170A - Concentration of ores - Google Patents
Concentration of ores Download PDFInfo
- Publication number
- US1560170A US1560170A US703260A US70326024A US1560170A US 1560170 A US1560170 A US 1560170A US 703260 A US703260 A US 703260A US 70326024 A US70326024 A US 70326024A US 1560170 A US1560170 A US 1560170A
- Authority
- US
- United States
- Prior art keywords
- acid
- mineral
- ore
- ores
- froth
- 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
- 239000002253 acid Substances 0.000 description 14
- 229910052500 inorganic mineral Inorganic materials 0.000 description 12
- 239000011707 mineral Substances 0.000 description 12
- 235000010755 mineral Nutrition 0.000 description 12
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 8
- 239000001117 sulphuric acid Substances 0.000 description 8
- 235000011149 sulphuric acid Nutrition 0.000 description 8
- 229910052802 copper Inorganic materials 0.000 description 6
- 239000010949 copper Substances 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 5
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 5
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 5
- 239000012991 xanthate Substances 0.000 description 5
- 241000512668 Eunectes Species 0.000 description 4
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 4
- 239000003795 chemical substances by application Substances 0.000 description 4
- ZOOODBUHSVUZEM-UHFFFAOYSA-N ethoxymethanedithioic acid Chemical compound CCOC(S)=S ZOOODBUHSVUZEM-UHFFFAOYSA-N 0.000 description 4
- 238000009291 froth flotation Methods 0.000 description 4
- 150000001450 anions Chemical class 0.000 description 3
- 150000001768 cations Chemical class 0.000 description 3
- 235000019441 ethanol Nutrition 0.000 description 3
- 239000003350 kerosene Substances 0.000 description 3
- JCBJVAJGLKENNC-UHFFFAOYSA-M potassium ethyl xanthate Chemical compound [K+].CCOC([S-])=S JCBJVAJGLKENNC-UHFFFAOYSA-M 0.000 description 3
- 239000010802 sludge Substances 0.000 description 3
- WHRZCXAVMTUTDD-UHFFFAOYSA-N 1h-furo[2,3-d]pyrimidin-2-one Chemical compound N1C(=O)N=C2OC=CC2=C1 WHRZCXAVMTUTDD-UHFFFAOYSA-N 0.000 description 2
- QGJOPFRUJISHPQ-UHFFFAOYSA-N Carbon disulfide Chemical compound S=C=S QGJOPFRUJISHPQ-UHFFFAOYSA-N 0.000 description 2
- 235000006173 Larrea tridentata Nutrition 0.000 description 2
- 244000073231 Larrea tridentata Species 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000003153 chemical reaction reagent Substances 0.000 description 2
- 229960002126 creosote Drugs 0.000 description 2
- 238000005188 flotation Methods 0.000 description 2
- 239000011121 hardwood Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- -1 5.0 pounds Substances 0.000 description 1
- 241000212342 Sium Species 0.000 description 1
- 238000003723 Smelting Methods 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 239000010665 pine oil Substances 0.000 description 1
- 229940072033 potash Drugs 0.000 description 1
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Substances [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 1
- 235000015320 potassium carbonate Nutrition 0.000 description 1
- 235000011118 potassium hydroxide Nutrition 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000003756 stirring Methods 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
- B03D1/001—Flotation agents
- B03D1/004—Organic compounds
- B03D1/012—Organic compounds containing sulfur
-
- 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
- B03D2203/00—Specified materials treated by the flotation agents; Specified applications
- B03D2203/02—Ores
-
- 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 relates to the froth-flotation concentration of ores, and is herein described as applied to the froth-flotation of certain ores with the aid of certain organic compounds containing sulphur. It has been found that the froth-flotation process is carried out much more efliciently when there are present in the ore pulp certain of the sulphur derivatives of carbonic acid such as those that yield anions and cat-ions in solution. According to the present invention,
- the froth-flotation process is carried out with the aid of a sulphur derivative of carbonic acid in-an acid ore pulp, the requisite acidity being usually obtained through the presence of sulphuric acid in the pulp.
- the amountof acid used may vary widely. Sometimes, in the case of an ore containing acid-soluble mineral enough has been used to dissolve a large proportion of the acidsoluble mineral, with the result that the re- 30. sulting metal-bearing pulp liquid carries it away. This may be precipitated, if desired, as is well known. Often, however, by a careful adjustni nt of conditions much less 7 acid can be use 85
- potassium xanthate was prepared as follows:
- Anaconda old gravity-concentration tailing reground for flotation were treated at per ton of solids, 0.67 pounds of a 30% solution of potassium xanthate in water, 3.96 pounds of kerosene acid sludge, and 11.45 pounds of chamber sulphuric acid.
Landscapes
- Manufacture And Refinement Of Metals (AREA)
- Paper (AREA)
Description
Patented Nov. 3, 1925.
UNITED sTAT s PATENT OFFICE- CARL PIERCE LEWIS, OF BTJ'RLINGAME, CALIFORNIA, ASSIGNOR TO MINERALS SEPARA- TION NORTH AMERICAN CQRBORATION, OF NEW YORK, N. Y., A CORPORATION OF MARYLAND.
No Drawing.
To all whom it may concern: I
Be it known that I, CARL PIERCE Lewis, a citizen of the United States, and a resident of Burlingame, county of San Mateo, State of California, have invented certain new and useful Improvements in Concentration of Ores, of which the following is a specification. t
This invention relates to the froth-flotation concentration of ores, and is herein described as applied to the froth-flotation of certain ores with the aid of certain organic compounds containing sulphur. It has been found that the froth-flotation process is carried out much more efliciently when there are present in the ore pulp certain of the sulphur derivatives of carbonic acid such as those that yield anions and cat-ions in solution. According to the present invention,
the froth-flotation process is carried out with the aid of a sulphur derivative of carbonic acid in-an acid ore pulp, the requisite acidity being usually obtained through the presence of sulphuric acid in the pulp.
The amountof acid used may vary widely. Sometimes, in the case of an ore containing acid-soluble mineral enough has been used to dissolve a large proportion of the acidsoluble mineral, with the result that the re- 30. sulting metal-bearing pulp liquid carries it away. This may be precipitated, if desired, as is well known. Often, however, by a careful adjustni nt of conditions much less 7 acid can be use 85 For laboratory purposes potassium xanthate was prepared as follows:
5198.4 ramsof 88.5% caustic potash was dissolved in 524 grams ethyl alcohol (denatured #5 formula) at a temperature of 40 124 F., in a reflux condenser; The solution was cooled to 58 F; It contained a large excess of alcohol over the theoretical amount needed for the subsequent reactions. To
this was added, while stirring, and. in a coolin bath, the theoretical amount of carbon disulphide. The reaction was substantially instantaneous, producing-a thickpul of otas'sium xanthate. Thepulpwas coole an centrifuged in a laboratory machine,
yielding crystals containing about 20%.
of pine oil and there is obtained a precipi- '--'.:Dur1ng asev'en and one half hours run cononiv'rnn'rron OF oREs.
Application and March 31, 1924. Serial No. 703,260.
the mother liquorgave excellent results in flotation. It was found in cases where sulphuric acid was used "according to the present invention that the centrifuged material yielded better results than the uncentrifuged. It has also been found that excellent results can be obtained by using,
instead of a pure or ordinary xanthate, the
product obtained when concentrated al-' coholic potash is mixed one-third its volume.
tate by adding CS in an amount somewhat in ;excess. of that needed to combine with the ethyl alcohol present.
In one test a pulp of Anaconda slimes was agitated with sulphuric acid at the rate of 25 pounds per ton, and the pine-oil-xanthate complex mixture at the rate of 0.4 pound per ton. The results are shown in the following table:
Assn s 'Recovcu, "2.1m.
Heads 100.0. 2.88 0on0 81.9 8.64 97.1 Tails 88. 1 12 2. 9 0
to a pulpof Anaconda v The other reagents used were a mixture of hardwood creosote and kerosene acid sludge, 5.0 pounds, and sulphuric acid, 20p0unds per ton. The tails contained 0.15%. sul: phide-copper and 0.23% acid soluble copper, making a total of-0.38% recovered copper :figainst a normalof 0.61% recovered i th "absence of xanth r p on current Anaconda slimes at; the rate of one .hundred and eleven tons per twentyfour hours in a minerals separation standard -machine, from a feed containing 3.28%
0.26% being acid soluble copper there was recovered a .concentrate contain-- ing 11.43% cu; and 36.9% insolubles, -the latter being a proportion desirable for smelting. The tailings contained 0.29% copper of which 0.20%- was acid soluble copper. This test was run at a temperature of 82 F. using for reagents, 7.89 pounds of kerosene acid sludge, 21.6 pounds of chamber sulphuric acid, 2.36 pounds of hardwood creosote, and 2.92 pounds of a twenty per cent. solution of potassium xanthate in water, all quantities being in pounds per short ton of ore.
Anaconda old gravity-concentration tailing reground for flotation were treated at per ton of solids, 0.67 pounds of a 30% solution of potassium xanthate in water, 3.96 pounds of kerosene acid sludge, and 11.45 pounds of chamber sulphuric acid.
Having thus described certain embodiments of the invention what is claimed is 1. The process of concentrating ores which consists m agitating a suitable acid pulp of an ore with a mineral-frothing agent and a sulphur derivative of carbonic acld yielding anions and cations in solution to produce by the action of both a mineral-bearing froth containing a large proportion of a mineral of the ore, and separating the froth.
2. The process of concentrating oreswhich consists in agitating a suitable acid pulp of an ore with a mineral-frothing agent and a xanthate to produce by the action of both a mineral-bearing froth containing a large proportion of a mineral of the ore, and separating the froth.
3. The process of concentrating ores which consists in agitating a suitable pulp of an ore with a mineral-frothing agent and a xanthate and sulphuric acid to produce b the action of both a mineral-bearing frot containing a large proportion of a mineral of the ore, and separating the froth.
4. The process of concentrating ores which consists in agitating a suitable pulp of an ore with a mineral-frothing, agent and a sulphur derivative of carbonic acid yielding anions and cations in solution and sulphuric acid to produce by the action of both a mineral-bearing froth containing a large proportion of a mineral of the ore, and
separating the froth.
In testimony whereof, I have aflixed my signature to this specification.
CARL PIERCE LEWIS.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US703260A US1560170A (en) | 1924-03-31 | 1924-03-31 | Concentration of ores |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US703260A US1560170A (en) | 1924-03-31 | 1924-03-31 | Concentration of ores |
Publications (1)
Publication Number | Publication Date |
---|---|
US1560170A true US1560170A (en) | 1925-11-03 |
Family
ID=24824681
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US703260A Expired - Lifetime US1560170A (en) | 1924-03-31 | 1924-03-31 | Concentration of ores |
Country Status (1)
Country | Link |
---|---|
US (1) | US1560170A (en) |
-
1924
- 1924-03-31 US US703260A patent/US1560170A/en not_active Expired - Lifetime
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