US1429544A - Differential flotation process - Google Patents
Differential flotation process Download PDFInfo
- Publication number
- US1429544A US1429544A US364033A US36403320A US1429544A US 1429544 A US1429544 A US 1429544A US 364033 A US364033 A US 364033A US 36403320 A US36403320 A US 36403320A US 1429544 A US1429544 A US 1429544A
- Authority
- US
- United States
- Prior art keywords
- metals
- metal
- flotation
- pulp
- selective
- 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
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 relates generally to flotation processes for concentration of ores; without specific restriction to any particular method of producing the flotation of the ore-as, for instance, whether the floating of the ore is produced by oil action, or by froth action.
- the invention also relates generally to flotation processes as applied to any kind of ore.
- the object of my invention is to produce an process for diflerentially floating minerals; to produce a flotation process which will cause selective flotation and separation of any particular minerals or metals desired, and cause separation of floatable minerals or metals from each other.
- I have discovered that, by the use of a suitable selective re-agent in the pulp, I can cause the selective flotation of ores in a commercially eflicient manner.
- Such separation I form by "using a solution that tends to dissolve, preferably, all of the minerals or metals present in the ore that I may desire to keep from floating; and I saturate this solution either with the particular metal I which I desire to selectively float, or with a metal which is electro-ne ative to another metal or other metals w ich I desire to float; or with a metal which satisfies both of these conditions at once.
- I may use a solvent solution that, in .itself, has a differential dimolving action on the different metals or minerals; and, in addition to directly utilizing that differential solubility I may saturate the solution with a metal, as herein set forth, for further selective action.
- cyanide will not readily dissolve molybdenite and, accordingly, I may use unmodified sodium cyanide as a selective re-agent to float molybdenite selectively from, say, ,cop-
- the concentrate from the flotation operation may of course be carried through any number of subsequent flotation operations as may be necessary or desirable to clean the concentrate and, in this case, to exclude the lead and zinc sulphides.
- the gangue, together with the metallic ores r not floated, is separated from the liquid sotill lution in any of the well known manners; and the solution is again used for forming a pulp with fresh ore; so that my selective re-agent-is kept in the cycle of operations, with only the comparatively small loss which is cause by cyanicides and the dissolvin of a certain small part of the relatively e ectro-negative metals in the cyanide.
- the gangue may then be subjected to another flotation operation or a positive as regards zinc) the one hand from such series of flotation operations, wherein the seleotivecyanide solution is saturated with lead.
- any particular metal or metals may be floated selectively, and each and all of the metals in an ore amenable to flotation may be selectively floated and thus separated from the others.
- ll may use zinc as the saturation metal; but lead and zinc, tor instance, are so close together in their characteristics that the use of lead as the saturation metal may take out enough of the zinc along with the lead to malre iteconomical in some cases to use lead ((a metal which is slightly electroas the saturation metal rather than zinc.
- the saturation metal should preterabl be electro-negative with relation tot e metal or mineral wished to be floated, it will be understood that a satura tion metal which is not too much electropositive (relatively) may be used eflectively in some cases.
- T find it highly e oient as applied to the usually dificult separation of copper from such metals as lead, zinc and iron; or the separation of silver and copper on metals as lead, zinc and iron on the other hand.
- T flnd it veryefioient for separation of silver from such metals as lead, zinc and iron; a copper saturated solution being used also in this case just as when both silver and copper are present.
- the gist of my invention consists in the use of a re-agent that tends to dissolve certain of the metals present and leaves others comparatively free; a re-agent that has a selective dissolving action on the several metals present. And when I speak of a tendency to dissolve or lackot such tendency ll speak relatively and do not necessarily mean that the reagent will dissolve one metal and have no action at all on another. l have described in detail one instance of such a selective dissolving reagent; but it will be understood that it do not thereby limit my invention to that particular ire-agent.
Landscapes
- Manufacture And Refinement Of Metals (AREA)
Description
Patented ept. 19, I922.
STATES P l@ E DIFFERENTIAL FLOTATION PROCESS.
3K0 Drawing.
To all whom it may concern:
Be it known that I, BLAMEY STEVENS, a citizen of Great Britain, residing. at Triunfo, Baja California, Mexico, have invented new and useful Improvements in Differential Flotation Processes, of which the following is a specification.
This invention relates generally to flotation processes for concentration of ores; without specific restriction to any particular method of producing the flotation of the ore-as, for instance, whether the floating of the ore is produced by oil action, or by froth action. The invention also relates generally to flotation processes as applied to any kind of ore.
The object of my invention is to produce an eficient process for diflerentially floating minerals; to produce a flotation process which will cause selective flotation and separation of any particular minerals or metals desired, and cause separation of floatable minerals or metals from each other.
I have discovered that, by the use of a suitable selective re-agent in the pulp, I can cause the selective flotation of ores in a commercially eflicient manner. Such separation I form by "using a solution that tends to dissolve, preferably, all of the minerals or metals present in the ore that I may desire to keep from floating; and I saturate this solution either with the particular metal I which I desire to selectively float, or with a metal which is electro-ne ative to another metal or other metals w ich I desire to float; or with a metal which satisfies both of these conditions at once. It will be un- 4 derstood that I may use a solvent solution that, in .itself, has a differential dimolving action on the different metals or minerals; and, in addition to directly utilizing that differential solubility I may saturate the solution with a metal, as herein set forth, for further selective action. cyanide will not readily dissolve molybdenite and, accordingly, I may use unmodified sodium cyanide as a selective re-agent to float molybdenite selectively from, say, ,cop-
per, or almost any other mineral; and if then I wish to make further selection I may, in such circumstances saturate the cyanide with another metal, say copper; which would then cause the copper also to float. I
This solvent as above described is my For instance,
Application filed March 8, 1920. Serial No, 364=,@33.
selective re-agent. Its use and its effect will be best understood, and the invention as a whole will be best understood, from a description of my process as applied more or less specifically to a certain class of ores '11 some well known process of flotation.
Accordingly, I will proceed, for the purposes of 'making my invention clear and explicit, but not for the purpose of limiting my invention to the specific details set forth, to a detailed description of the application of my process to that kind of ores which is most universally treated by flotationnamely, sulphide ores; taking for instance an ore which contains silver, copper, lead and zinc.
Suppose for instance, that Iwish to selectively float the silver and copper and keep the ead and zinc in the pulp, I proceed generally as in any of the ordinary and well known methods of flotation. For instance, the pulp containing the sulphides ofthese four metals, ment, say tions, all of which is well known; and also mixed with a suitable proportion of selective agent, either acid or alkali or neither as desired, and in suitable proportions,
which is also all Well known. To this pulp, I add my specially prepared selective resay that in a sulphide oreis mixed with a floating elea suitable oil in proper proporselective re-agent to 250 pounds of ore,
m wli ere the proportion of ore to water in the pulp is one to four. Little difference in result is noted, whether the solution is acid,
neutral or alkaline.
Whensuch a pulp, carryin my selective re-agent, is treated in any of t e well known flotation machines, asfor'instance in amachine which beats air into the pulp and thus forms a frothI find that the silver and copper sulphides are floated, whereas the lead and zinc are kept in the pulp. In general, I find that the metal with which that the electro-positive or the cyanide solution is saturated will be floated; and that all metals which are electro-positive with relation to that saturation metal will also be floated; while all ores of metals relatively electro-negative to the metal of saturation (that is, having a greater solubilityproduct or an ability to displace the metal of saturation in the solution) will be kept in the pulp. It is Well understood. electro-negative relation of similar compounds of metals is more or less the-same as the relation of the metals themselves. This seems to be due to the tact that those metals which are relatively electro-negative have the power of going into the solution in spite oi the fact that the solution is already saturated with one particular metal, in this case, copper. The lead and zinc in this case start to replace the copper in the solution, but do not have opportunity to displace any appreciable amount of it during the period of time that the pulp is in the flotation cells. T might state the matter in this way; that the afinity of the saturated selective solution for the lead and zinc prevents the lead and zinc from floating. The lead and zinc therefore drop down in the solution with the rest of the gangue, and may be separated from the solution with the remainder of the gangue in any of the usual manners.
The concentrate from the flotation operation may of course be carried through any number of subsequent flotation operations as may be necessary or desirable to clean the concentrate and, in this case, to exclude the lead and zinc sulphides. In a single operation of flotation concentration, according to my process, there may be a certain amount of the relatively electro-negative metals floated in the first concentrate; but when there are no grains containing two minerals or metals my process so efleotively floats the disired metals, and so eflectively cuts down the flotation of the undesired metals that usually, one or two successive flotations of the concentrate will sufice to eliminatepractically entirely the relatively electro-nega-= tive metals and give a relatively pure concentrate, with a high percentage of ultimate recovery, of the desired metal or metals.
The gangue, together with the metallic ores r not floated, is separated from the liquid sotill lution in any of the well known manners; and the solution is again used for forming a pulp with fresh ore; so that my selective re-agent-is kept in the cycle of operations, with only the comparatively small loss which is cause by cyanicides and the dissolvin of a certain small part of the relatively e ectro-negative metals in the cyanide.
Audit, for instance, in such a case as here stated, it is desired next to selectively float the lead, the gangue may then be subjected to another flotation operation or a positive as regards zinc) the one hand from such series of flotation operations, wherein the seleotivecyanide solution is saturated with lead. It will thus be understood that, by
agents, any particular metal or metals may be floated selectively, and each and all of the metals in an ore amenable to flotation may be selectively floated and thus separated from the others. If both zinc and lead are desired, ll may use zinc as the saturation metal; but lead and zinc, tor instance, are so close together in their characteristics that the use of lead as the saturation metal may take out enough of the zinc along with the lead to malre iteconomical in some cases to use lead ((a metal which is slightly electroas the saturation metal rather than zinc. Thus, although it have said that the saturation metal should preterabl be electro-negative with relation tot e metal or mineral wished to be floated, it will be understood that a satura tion metal which is not too much electropositive (relatively) may be used eflectively in some cases.
I find to process of eneral applicability, and T find it highly e oient as applied to the usually dificult separation of copper from such metals as lead, zinc and iron; or the separation of silver and copper on metals as lead, zinc and iron on the other hand. And T flnd it veryefioient for separation of silver from such metals as lead, zinc and iron; a copper saturated solution being used also in this case just as when both silver and copper are present.
I wish to state, after giving this detailed description, that the gist of my invention consists in the use of a re-agent that tends to dissolve certain of the metals present and leaves others comparatively free; a re-agent that has a selective dissolving action on the several metals present. And when I speak of a tendency to dissolve or lackot such tendency ll speak relatively and do not necessarily mean that the reagent will dissolve one metal and have no action at all on another. l have described in detail one instance of such a selective dissolving reagent; but it will be understood that it do not thereby limit my invention to that particular ire-agent.
Having described a preferred form of my invention, ll claim: a
1. In a flotation pulp, adding to that pulp a selective re-agent. which is a solvent for floatable metals in the ore being treated and which is saturated with one of such metals, then floating thatmetal of saturation.
2. In a flotation process, pro string a flotation pulp, adding to that pu p a selective ire-agent which is a solvent for floatable metals in the ore being treated and which the use of a proper selective re-agent, or retee flotation process, preparing a' is saturated with one of such metals, then forming a froth in the solution and thereby floating that metal of saturation.
3. In a flotation process, preparing a floadding to that pulp a-selective tation pulp ire-agent which is a solvent for floatable metals in the ore being treated and which is saturated with one of such metals, then forming a froth in the solution and thereby floating that metal of saturation and all metals electro-positive relatively to it.
4. In a flotation process, preparing a flotation pulp adding to that pulp a selective re-agent which is a solvent for fioatable metals in the ore being treated and which is saturated witha-metal which is not substantially electro-positive relatively to the metal Wished to be floated, and then floating that last mentioned metal.
5. In a processof floating metal in a pulp containing several different metals, the use in the pulp of a selective re-agent which is a solvent of the fioatable metals in the ore being treated and Which is saturated with a metal not substantially electro-positive to the metal Wished to be floated;
In Witness" that I claim the foregoing l have hereunto subscribed my name this 23d day of February, 1920.
BLAMEY STEVENS.-
Witness':
VIRGINIA BEBINGER.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US364033A US1429544A (en) | 1920-03-08 | 1920-03-08 | Differential flotation process |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US364033A US1429544A (en) | 1920-03-08 | 1920-03-08 | Differential flotation process |
Publications (1)
Publication Number | Publication Date |
---|---|
US1429544A true US1429544A (en) | 1922-09-19 |
Family
ID=23432742
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US364033A Expired - Lifetime US1429544A (en) | 1920-03-08 | 1920-03-08 | Differential flotation process |
Country Status (1)
Country | Link |
---|---|
US (1) | US1429544A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2620068A (en) * | 1951-08-16 | 1952-12-02 | American Cyanamid Co | Depression of copper minerals from ores and concentrates |
US2664199A (en) * | 1952-08-27 | 1953-12-29 | Phelps Dodge Corp | Flotation recovery of molybdenite |
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 |
-
1920
- 1920-03-08 US US364033A patent/US1429544A/en not_active Expired - Lifetime
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2620068A (en) * | 1951-08-16 | 1952-12-02 | American Cyanamid Co | Depression of copper minerals from ores and concentrates |
US2664199A (en) * | 1952-08-27 | 1953-12-29 | Phelps Dodge Corp | Flotation recovery of molybdenite |
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 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN103909020A (en) | Flotation separation inhibitor and separation method of galena, pyrite and sphalerite | |
US1429544A (en) | Differential flotation process | |
US2070076A (en) | Separation of molybdenite from copper sulphides | |
US1678259A (en) | Process of concentrating mixed-sulphide ores | |
US2957576A (en) | Recovery of molybdenite by flotation | |
US2154092A (en) | Process of flotation concentration of ores | |
US2317413A (en) | Process for the concentration of boron chemically combined from its ores by autoflotation | |
US1659396A (en) | Process of concentrating ores and minerals by flotation | |
CN115921123A (en) | Novel galena-chalcopyrite separation composite inhibitor and application thereof | |
US2007176A (en) | Differential froth flotation | |
US1788331A (en) | Concentration process for flotable substances as ores, coals, graphite, and the like | |
US1274505A (en) | Separation of mixed metallic sulfids. | |
US2403640A (en) | Separation of cobaltite | |
JPH0371181B2 (en) | ||
US1182890A (en) | Separation of metallic sulfids. | |
US1554216A (en) | Froth-flotation concentration of ores | |
US1628046A (en) | Ore flotation process | |
US1094760A (en) | Process for recovering metalliferous constituents of ores. | |
US2105901A (en) | Froth flotation method | |
US2225626A (en) | Process for treating lead oxidized ores | |
US1833427A (en) | Flotation concentration of metalliferous minerals | |
US1421585A (en) | Concentration of ores by flotation | |
US1831808A (en) | Preparing oxidized minerals for concentration by froth flotation | |
US2044851A (en) | Froth flotation concentration of ores | |
US1879871A (en) | Method of flotation |