US3033364A - Treatment and recovery of material by flotation - Google Patents
Treatment and recovery of material by flotation Download PDFInfo
- Publication number
- US3033364A US3033364A US786009A US78600959A US3033364A US 3033364 A US3033364 A US 3033364A US 786009 A US786009 A US 786009A US 78600959 A US78600959 A US 78600959A US 3033364 A US3033364 A US 3033364A
- Authority
- US
- United States
- Prior art keywords
- flotation
- reagent
- dry
- liquid
- treatment
- 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
- 239000000463 material Substances 0.000 title description 33
- 238000005188 flotation Methods 0.000 title description 16
- 238000011282 treatment Methods 0.000 title description 8
- 238000011084 recovery Methods 0.000 title description 2
- 239000003153 chemical reaction reagent Substances 0.000 description 22
- 239000007788 liquid Substances 0.000 description 12
- 230000003750 conditioning effect Effects 0.000 description 7
- 238000000034 method Methods 0.000 description 7
- 239000011236 particulate material Substances 0.000 description 6
- 239000002245 particle Substances 0.000 description 5
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- 238000002386 leaching Methods 0.000 description 4
- 239000001117 sulphuric acid Substances 0.000 description 4
- 235000011149 sulphuric acid Nutrition 0.000 description 4
- 239000003795 chemical substances by application Substances 0.000 description 3
- ZOOODBUHSVUZEM-UHFFFAOYSA-N ethoxymethanedithioic acid Chemical compound CCOC(S)=S ZOOODBUHSVUZEM-UHFFFAOYSA-N 0.000 description 3
- 229910052500 inorganic mineral Inorganic materials 0.000 description 3
- 239000011707 mineral Substances 0.000 description 3
- 239000012991 xanthate Substances 0.000 description 3
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 2
- 229910052770 Uranium Inorganic materials 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- JFALSRSLKYAFGM-UHFFFAOYSA-N uranium(0) Chemical compound [U] JFALSRSLKYAFGM-UHFFFAOYSA-N 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 241000612118 Samolus valerandi Species 0.000 description 1
- WZECUPJJEIXUKY-UHFFFAOYSA-N [O-2].[O-2].[O-2].[U+6] Chemical compound [O-2].[O-2].[O-2].[U+6] WZECUPJJEIXUKY-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000001143 conditioned effect Effects 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- 239000000194 fatty acid Substances 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000008396 flotation agent Substances 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 238000007429 general method Methods 0.000 description 1
- 229910052595 hematite Inorganic materials 0.000 description 1
- 239000011019 hematite Substances 0.000 description 1
- LIKBJVNGSGBSGK-UHFFFAOYSA-N iron(3+);oxygen(2-) Chemical compound [O-2].[O-2].[O-2].[Fe+3].[Fe+3] LIKBJVNGSGBSGK-UHFFFAOYSA-N 0.000 description 1
- 238000003801 milling Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910000480 nickel oxide Inorganic materials 0.000 description 1
- GNRSAWUEBMWBQH-UHFFFAOYSA-N oxonickel Chemical compound [Ni]=O GNRSAWUEBMWBQH-UHFFFAOYSA-N 0.000 description 1
- 229920001021 polysulfide Polymers 0.000 description 1
- 238000009877 rendering Methods 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011343 solid material Substances 0.000 description 1
- 230000007928 solubilization Effects 0.000 description 1
- 238000005063 solubilization Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000003784 tall oil Substances 0.000 description 1
- 229910000439 uranium oxide Inorganic materials 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
-
- 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
-
- 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
- B03D2203/04—Non-sulfide ores
Definitions
- This invention relates to the conditioning of material for metallurgical treatment such, for instance, as flotation or leaching, or other treatments where the advantages of the invention may be of benefit.
- liquid reagents or reagents which may be placed in liquid form can be eifectively associated with the material to be treated while the latter is in the dry state.
- the reagent material may be applied to the material to be treated in any one of a number of different ways. If the material is originally in particulate form, such for instance as certain beach sands or tailings piles, the material may be tumbled in any conventional form of tumbling drum with the reagent added thereto at the desired rate in liquid form either as a spray or as drops added to the material as the latter is fed to the drum.
- the liquid reagent may be added in metered quantities to the feed to the mill before the latter is fed thereto or the appropriate quantity of reagent may be sprayed into the mill.
- the reagent may be added in the same manner as it is added in the case of a dry ball mill, tube mill or dry pebble mill, and in addition there is a further alternative that the reagent may be added as a spray of coarse or fine droplets to the airstream.
- the particulate material is collected dry with a reagent on it and may be then subjected to storage in the dry state for such period as may be appropriate having regard to the particular materials and/or processes involved.
- the association of the liquid with the particulate material apparently arises by virtue of the free energy which appears on surfaces of freshly comrninuted material or which is produced in the tumbling action of already particulate material.
- the liquid will tend to coat the particulate material, and such coating will be carried to completion in a period of time which varies markedly as the characteristics of the material vary.
- the material may be completely coated in an effective manner by the time the treated material is collected from the milling system or tumbling system employed, or, on the other hand, additional time of storage in the dry state may be required in order to enable completion of the coating.
- a typical example of the operation of the invention is in the application of liquid xanthate reagent to sulphide ores where the ore in its cornminuted state contains substantial quantities of slime.
- the xanthate is added to the ore in any of the manners aforesaid at the rate which is empirically determined as the most economical for the ore concerned, and after a suitable period of dry storage the treated material is subjected to flotation or flotation preceded by a short period of wet conditioning in essentially conventional manner.
- the surprising result achieved is that with a comparatively low reagent consumption the xanthate has become associated with the mineral in the ore and is associated as well with the slimes as with the particles of larger size which are normally considered more suitable for flotation.
- the problem of slimes which is an outstanding problem in flotation is eliminated.
- Another example of the operation of the invention is in preparing material for a leaching operation.
- concentrated sulphuric acid as the reagent to be applied for instance to the leaching of a uranium ore.
- the calculated quantity of concentrated sulphuric acid is added in any of the manners described above, and after a period of dry storage during which the sulphuric acid associates itself preferentially with the mineralized particles of ore While it is essentially in the non-reactivated concentrated form, the thus conditioned material is slurried with a calculated quantity of water bringing the concentration of the sulphuric acid to the optimum value for purposes of the particular leach.
- a third example of the operation of the invention is in the treatment of oxidized sulphide ores where the reagent employed is a sulphidizing agent.
- a calculated quantity of sulphidizing agent such as sodium polysulphide solution in concentrated form is applied to the ore in the manner above described, and the treated material is dry stored.
- the sulphidizing agent is found to associate itself preferentially with the mineralized particles eflfectively causing sulphidization of at least the surfaces of the oxidized particles, rendering the total mineral content amenable to flotation by conventional methods.
- the method of the invention is a general method for applying liquid reagents to solid material, and there are, in so far as present knowledge is concerned, no limitations on its applicability.
- the process of the invention is extremely effective in the application of flotation agents to oxide ores such as hematite, uranium oxide, nickel oxide, and the like, such flotation reagents generally being of an oily nature and encompassing such materials as tall oil, fuel oil, fatty acids, and many other substances known in the art, and too numerous to mention.
- a method of recovering material by flotation which comprises providing the material to be treated in the dry particulate form characterized by free energy on the surface thereof, associating an amount of a liquid flotation reagent with the dry particulate material suflicient to reagentize the material, maintaining the material associated with said liquid reagent as a mixture essentially in the dry state for a predetermined period of time and then sub jecting the thus treated material to separation by flotation.
- a method of recovering material by flotation which comprises, adding an amount of a liquid flotation reagent 10 faces thereof with which the reagent becomes associated 15 4. and then subjecting the oomminuted material to separation by flotation.
Landscapes
- Manufacture And Refinement Of Metals (AREA)
Description
United States Patent TREATMENT AND RECOVERY OF MATERIAL BY FLOTATION David Weston, 129 Adelaide St. W., Toronto 1,
Ontario, Canada No Drawing. Filed Jan. 12, 1959, Ser. No. 786,009
Claims priority, application Canada Sept. 5, 1958 3 Claims. (Cl. 2099) This invention relates to the conditioning of material for metallurgical treatment such, for instance, as flotation or leaching, or other treatments where the advantages of the invention may be of benefit.
For purposes of conditioning material for metallurgical treatment, it is frequently desired to associate particulate reagents with particles of material prior to introduction of said material to the actual metallurgical treatment which it is intended to carry out. In general, the practice has been in the past to carry out such conditioning when the material is suspended in a liquid pulp. In many cases, wet conditioning of this nature requires an excessive rate of reagent consumption, and in general such wet conditioning is ineflective to promote slimes. In addition, a substantial amount of power is consumed in the course of such wet conditioning treatments.
I have now found that liquid reagents or reagents which may be placed in liquid form can be eifectively associated with the material to be treated while the latter is in the dry state. According to the invention, the reagent material may be applied to the material to be treated in any one of a number of different ways. If the material is originally in particulate form, such for instance as certain beach sands or tailings piles, the material may be tumbled in any conventional form of tumbling drum with the reagent added thereto at the desired rate in liquid form either as a spray or as drops added to the material as the latter is fed to the drum. Where the material is not already in particulate form and the comminution unit is for instance a dry ball mill, tube mill or dry pebble mill, the liquid reagent may be added in metered quantities to the feed to the mill before the latter is fed thereto or the appropriate quantity of reagent may be sprayed into the mill. If the comminution unit employed is one in which the material is removed in an :airstream, the reagent may be added in the same manner as it is added in the case of a dry ball mill, tube mill or dry pebble mill, and in addition there is a further alternative that the reagent may be added as a spray of coarse or fine droplets to the airstream. In any of the foregoing events, the particulate material is collected dry with a reagent on it and may be then subjected to storage in the dry state for such period as may be appropriate having regard to the particular materials and/or processes involved. The association of the liquid with the particulate material apparently arises by virtue of the free energy which appears on surfaces of freshly comrninuted material or which is produced in the tumbling action of already particulate material. In any event, the liquid will tend to coat the particulate material, and such coating will be carried to completion in a period of time which varies markedly as the characteristics of the material vary. Thus, the material may be completely coated in an effective manner by the time the treated material is collected from the milling system or tumbling system employed, or, on the other hand, additional time of storage in the dry state may be required in order to enable completion of the coating.
A typical example of the operation of the invention is in the application of liquid xanthate reagent to sulphide ores where the ore in its cornminuted state contains substantial quantities of slime. In such instance, the xanthate is added to the ore in any of the manners aforesaid at the rate which is empirically determined as the most economical for the ore concerned, and after a suitable period of dry storage the treated material is subjected to flotation or flotation preceded by a short period of wet conditioning in essentially conventional manner. The surprising result achieved is that with a comparatively low reagent consumption the xanthate has become associated with the mineral in the ore and is associated as well with the slimes as with the particles of larger size which are normally considered more suitable for flotation. Thus, the problem of slimes which is an outstanding problem in flotation is eliminated.
Another example of the operation of the invention is in preparing material for a leaching operation. In this case, it may be desired to use concentrated sulphuric acid as the reagent to be applied for instance to the leaching of a uranium ore. The calculated quantity of concentrated sulphuric acid is added in any of the manners described above, and after a period of dry storage during which the sulphuric acid associates itself preferentially with the mineralized particles of ore While it is essentially in the non-reactivated concentrated form, the thus conditioned material is slurried with a calculated quantity of water bringing the concentration of the sulphuric acid to the optimum value for purposes of the particular leach. In this way, a particularly high eificiency is attained in the solubilization of the mineral while using extremely economical quantities of acid. The volume of water is kept to a minimum and filtration problems which are always of extreme importance in the leaching of uranium are reduced to a minimum.
A third example of the operation of the invention is in the treatment of oxidized sulphide ores where the reagent employed is a sulphidizing agent. In such an operation, a calculated quantity of sulphidizing agent such as sodium polysulphide solution in concentrated form is applied to the ore in the manner above described, and the treated material is dry stored. The sulphidizing agent is found to associate itself preferentially with the mineralized particles eflfectively causing sulphidization of at least the surfaces of the oxidized particles, rendering the total mineral content amenable to flotation by conventional methods.
While I have explained the manner of operation of the process of the invention in relation to three principal types of metallurgical operation, it is to be understood that the above examples are given by way of illustration only. The method of the invention is a general method for applying liquid reagents to solid material, and there are, in so far as present knowledge is concerned, no limitations on its applicability. In particular, it may be mentioned that the process of the invention is extremely effective in the application of flotation agents to oxide ores such as hematite, uranium oxide, nickel oxide, and the like, such flotation reagents generally being of an oily nature and encompassing such materials as tall oil, fuel oil, fatty acids, and many other substances known in the art, and too numerous to mention.
What I claim as my invention is:
1. A method of recovering material by flotation which comprises providing the material to be treated in the dry particulate form characterized by free energy on the surface thereof, associating an amount of a liquid flotation reagent with the dry particulate material suflicient to reagentize the material, maintaining the material associated with said liquid reagent as a mixture essentially in the dry state for a predetermined period of time and then sub jecting the thus treated material to separation by flotation.
2. The method of claim 1 wherein the free energy on the surface of the particulate material is eflected through tumbling and during which flotation reagent is associated with the material.
3. A method of recovering material by flotation which comprises, adding an amount of a liquid flotation reagent 10 faces thereof with which the reagent becomes associated 15 4. and then subjecting the oomminuted material to separation by flotation.
References Cited in the file of this patent UNITED STATES PATENTS 1,175,331 Atwater Mar. 14, 1916 1,889,027 Washburn Nov. 29, 1932 1,985,076 Breger Dec. 18, 1934 2,334,258 Gavin Nov. 16, 1943 2,437,164 Kramer Mar. 2, 1948 2,944,666 Bunge July 12, 1960 FOREIGN PATENTS 568,755 Germany June 23, 1933
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CA3033364X | 1958-09-05 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US3033364A true US3033364A (en) | 1962-05-08 |
Family
ID=4176980
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US786009A Expired - Lifetime US3033364A (en) | 1958-09-05 | 1959-01-12 | Treatment and recovery of material by flotation |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US3033364A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1984000704A1 (en) * | 1982-08-20 | 1984-03-01 | Phlotec Services Inc | Process for the selective separation of base metal sulfides and oxides contained in an ore |
| US4650569A (en) * | 1983-03-18 | 1987-03-17 | South American Placers, Inc. | Process for the selective separation of base metal sulfides and oxides contained in an ore |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1175331A (en) * | 1915-06-17 | 1916-03-14 | Richard M Atwater Jr | Process of concentrating copper values. |
| US1889027A (en) * | 1927-04-12 | 1932-11-29 | Titanium Pigment Co Inc | Recovery of titanium compounds |
| DE568755C (en) * | 1928-10-11 | 1933-01-23 | Alfred Roemelt | Process for the dry processing of dust-like material, such as coal dust, ore dust |
| US1985076A (en) * | 1930-08-16 | 1934-12-18 | Singmaster & Breyer Inc | Fine dry grinding |
| US2334258A (en) * | 1940-07-19 | 1943-11-16 | Crown Cork & Seal Co | Coating |
| US2437164A (en) * | 1944-12-08 | 1948-03-02 | Du Pont | Processing of titanium ores |
| US2944666A (en) * | 1956-04-04 | 1960-07-12 | Hanna Mining Co | Ore beneficiation |
-
1959
- 1959-01-12 US US786009A patent/US3033364A/en not_active Expired - Lifetime
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1175331A (en) * | 1915-06-17 | 1916-03-14 | Richard M Atwater Jr | Process of concentrating copper values. |
| US1889027A (en) * | 1927-04-12 | 1932-11-29 | Titanium Pigment Co Inc | Recovery of titanium compounds |
| DE568755C (en) * | 1928-10-11 | 1933-01-23 | Alfred Roemelt | Process for the dry processing of dust-like material, such as coal dust, ore dust |
| US1985076A (en) * | 1930-08-16 | 1934-12-18 | Singmaster & Breyer Inc | Fine dry grinding |
| US2334258A (en) * | 1940-07-19 | 1943-11-16 | Crown Cork & Seal Co | Coating |
| US2437164A (en) * | 1944-12-08 | 1948-03-02 | Du Pont | Processing of titanium ores |
| US2944666A (en) * | 1956-04-04 | 1960-07-12 | Hanna Mining Co | Ore beneficiation |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1984000704A1 (en) * | 1982-08-20 | 1984-03-01 | Phlotec Services Inc | Process for the selective separation of base metal sulfides and oxides contained in an ore |
| US4515688A (en) * | 1982-08-20 | 1985-05-07 | South American Placers, Inc. | Process for the selective separation of base metal sulfides and oxides contained in an ore |
| US4650569A (en) * | 1983-03-18 | 1987-03-17 | South American Placers, Inc. | Process for the selective separation of base metal sulfides and oxides contained in an ore |
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