Method of extracting metal-containing sulfide minerals or sulfidized metal-containing oxidized miner

专利摘要:
A froth flotation process for selectively recovering nonferrous metal containing sulfide minerals or sulfidized metal containing oxide minerals from ores. More particularly, this invention concerns a process for recovering metal containing sulfide minerals or sulfidized metal containing oxide minerals from an ore which comprises subjecting the ore, in the form of an aqueous pulp, to a froth flotation process in the presence of a flotating amount of a flotation collector wherein the collector has a hydrocarbon containing one or more monosulfide units, wherein the carbon atoms to which the sulfur atoms are bound are aliphatic or cycloaliphatic carbon atoms, the total carbon content of the hydrocarbon portion of the collector is such that the collector has sufficient hydrophobic character to cause the metal containing sulfide mineral or sulfidized metal containing oxide mineral particles to be driven to the air/bubble interface, under conditions such that the metal containing sulfide mineral or sulfidized metal containing oxide mineral is recovered in the froth.
公开号:SU1582978A3
申请号:SU4028936
申请日:1987-01-30
公开日:1990-07-30
发明作者:Р.Климпел Ричард；Д.Хансен Роберт；Дж.Строджни Эдвин
申请人:Дзе Дау Кемикал Компани (Фирма)；
IPC主号:

专利说明:

one
(21) 4028936/27-03
(86) PCT / US 86/00350 (02/18/86)
(22) 01/30/87
(31) 740091
(32) 05/31/85
(33) US
(46) 07/30/90. Bul P 28
(71) Dze Dau Chemical Company (US)
(72) Richard R. Klimpell, Robert D. Hansen and Edwin J. Strojny (US)
(53) 622.765.06 (088.8)
(56) Glembotsky V. A. and others. Flotation. M.: Nedra, 1973, p. 106-107.
US patent ff 4274950, cl. 209-166, published. 198 × 1.
(54) METHOD FOR EXTRACTING METAL-CONTAINING SULPHIDE MINERALS OR SULPHIDIZED METAL-CONTAINING OXIDIZED MINERALS FROM ORE
(57) The invention relates to a froth flotation process for the recovery of non-ferrous metal-containing sulphide or sulphided oxide minerals from ores. The goal is to increase the efficiency and selectivity of the process. The ore in the form of pulp is processed by a sulfur-containing collector and floated. A sulfide of the formula R, -S-R2, where R, is methyl, ethyl, epoh H, is introduced as a sulfur-containing collector.
I I
si, such as group - ЈJ - (J or
 /
ABOUT
a hydrocarbyl radical substituted with one or more cyano, halo, ether or hydrocarbyl thioester moieties; R2 is an aliphatic, cycloaliphatic, aromatic group or combination thereof containing 5 to 11 carbon atoms, R and R2 can be combined to form a heterocyclic ring structure with sulfur, provided sulfur is bound to an aliphatic or cycloaliphatic carbon atom. The total carbon content in the sulfide collector is 6-20 atoms. R, and R2 do not have the same hydrocarbon moieties. Preferred options for R (and RJ. 3 Cp f-crystals are given.
with SS
cl
with
The invention relates to a froth flotation process for extracting non-ferrous metal-containing sulphide or sulphided oxide minerals from ores, and more specifically to a process for recovering sulphide or sulphided oxide minerals containing metal from ores, which involves treating the ore in the form of an aqueous slurry. f
I
in the process of froth flotation in the presence of a flotation collector in an amount sufficient to provide froth flotation that contains a hydrocarbon with one or more monosulfide groups, carbon atoms (s) are bound to sulfur atoms, followed by -1 are aliphatic or cycloaliphatic carbon atoms

ate
and the total amount of carbon in the hydrocarbon is enough to communicate the hydrophobic ™ sufficient for the collector to bring the particles of a sulfide mineral or a sulfided oxide mineral containing metal to the air-bubble interface.
The purpose of the invention is to increase the efficiency and selectivity of the process.
A method for recovering metal-containing sulphide minerals or sulphidized oxidized minerals from ores includes ores, pulp treatment with a collector and flotation.
As the collector, the sulfide of the formula
R, - S - R2 where Rt is methyl, -ethyl, epoxy, such
I n
I I
as a group-C-C-or hydrocarbon
a radical, substituted by one or more cyano, halo, ether or hydrocarbyl thioether residues;
Ri is an aliphatic, cycloaliphatic, aromatic group or combination thereof containing from 5 to 11 f carbon atoms, and R7 and R2 can be combined to form a heterocyclic ring structure with sulfur, provided that sulfur is bound to aliphatic or cycloaliphatic carbon, with a total carbon content in the sulfide collector of 6-20 atoms. ,
In a preferred embodiment, R1 and RJ are independently an aliphatic, cycloaliphatic or alkyl moiety, unsubstituted or substituted or an alkyl moiety, unsubstituted or substituted with one or more hydroxyl, cyano, halo, OR3 or SR, wherein R3 is hydrocarbyl radical, a Rt nR can together with S form a heterocyclic ring. It is possible that Rf and R2 are an aliphatic or cycloaliphatic moiety, unsubstituted or substituted by one or more hydroxyl, cyano, halo, OR3 or SR3 moieties, where R and R2 can form a heterocyclic ring or S together to whom
o
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yes, R and R2 do not form a heterocyclic ring together with S and are alkyl, apenyl, alkynyl, cycloalkyl or cycloalkenyl unsubstituted or substituted with one or more hydroxyl, halo, cyano OR3 or R3 moieties, where R3 is an aliphatic or cycloaliphatic or optionally when R and R2 are independently alkyl or alkenyl, and in particular R is methyl or ethyl, R2 is an alkyl group With tf or alkenyl group, or an option when RJ and R2 are not identical hydrocarbon constituents, i.e. monosulfide groups are asymmetric. Moreover, R3 is aliphatic or cycloaliphatic} preferably R3 is alkyl, alkenyl, cycloalkyl or cycloalkenyl.
The total carbon content in the hydrocarbon portion of the monosulfide reservoir should be such that the reservoir is hydrophobic to the extent sufficient to remove the metal containing sulfide or sulfide oxide mineral to the air-bubble interface. In a preferred embodiment, the carbon content in the monosulfide collector should be so that the minimum carbon content is 4, preferably 6 or 8.
The maximum carbon content should be 20, preferably 16 or 12.
Cyclic substances suitable for use in this invention contain the following structures.
(N «) 2-С-С- (Н) 2 and kg $ (m)
#
where R and R4 are independently hydrogen, aryl, alkaryl, aralkyl, alkyl, alkenyl, alkynyl, cycloalkyl, cycloalkenyl, hydroxyl, cyano, halo, OR3 or SR3, where aryl, alkaryl, aralkyl, alkyl, alkenyl, alkynyl , cycloalkyl, cycloalkenyl can be unsubstituted or substituted by hydroxyl, cyano, OR3 or SR3 moieties, etc., and Rr is a linear or branched alkylene, alkenylene or alkynylene, unsubstituted or substituted hydroxyl, cyano, halo,
Orj sj hydrocarbyl or GUID-JQ heptyl, ethyl cyclooctyl sulphide,
rocarbyl, substituted or unsubstituted
hydroxyl, cyano, halo, ethereal,
hydrocarbyloxy or hydrocarbyl thioether, where two E can
It is clear that at least one R group is not hydrogen.
It is possible that the collectors correspond to the formula
(Rch) 3.l C (H) h-S-C (H) n (R,) 3V, (III)
propylbutyl sulphate, propyl propentyl sulphate, propylhexyl sulphide, propylheptyl sulphide, propyloxy sulphide, propylnonyl sulphide,
along with sulfur atom to form cyclide, butyldecyl sulphide, butyldecyl sulphide, butyldodecyl sulphide,
5 butylcyclopentyl sulphide, butylcyclohexyl sulphide, butylcycloheptyl sulphide, butylcyclo-octyl sulphide, pentylhexyl sulphide, pentylhexyl sulphide, pentylheptyl sulfur,
30 pentyl octyl sulphide, pentil tilnonyl sulphide, pentyl decyl sulphide, pentyl udecyl sulphide, pentileldodecyl sulphide, pentyl cycloheptyl sulfur, pentyl cyclohexyl sulphide,
with sulfur pentylcycloheptyl, sulfur pentylcyclohexyl, sulfur pentylcycloheptyl, pentylcyclooctyl, hexyl heptyl sulfur, hexyl octyl sulfur, hexylnonyl sulfur,
40 hexyl heterocycles, hexyl sildecyl sulfur, hexyl dodecyl sulfur, hexyl cyclopentyl sulfur, hexyl cyclohexyl sulfur, hexyl cycloheptyl sulfur, hexyl heterocyclic or heterocyclic ring; n is an integer of 0, 1, 2, or 3, provided that the total carbon content in the hydrocarbon portion of the reservoir is such that the reservoir is hydrophobic to the extent sufficient to bring the sulfide or sulfided oxide mineral containing metal to the air-bubble interface,
In a preferred embodiment, R {is aliphatic, cycloaliphatic aryl, alkaryl, or aralkyl, unsubstituted or substituted by cyano, hydroxyl, halo, OR3 or SR3, where R3 is defined above, or when R6 is aliphatic or cycloaliphatic - constituting, unsubstituted or substituted hydroxyl, cyano, halo, aliphatic ether, cycloaliphatic ether, or cycloaliphatic thioether, or the variant, when Rt is alkene alkyne, alkyl, cycloalkyl or cycloalkeni noy component, or a variant, when one group - C (H) "(R) is a methyl or ethyl moiety, and the other - C alkyl, or C .11 alkenilnoi co cyclooctyl, sulfur geptiloktil,
which is n, 1 or 4, preferably 2 or 3.
The collector is introduced at a concentration of i from 1 -10 to kg / kg ore.
Substances used in the proposed method are the following. sulfurous
geptilnonil sulfurous, sulphurous gep- tildetsil, sulfur geptilundetsil, geptildodetsil sulfide, sulfurous geptiltsiklopentil, sulfur geptil50 cyclohexyl, sulfur geptiltsiklook- Teal, sulfur oktilnonil, oktildetsil sulfide, sulfurous oktilundetsil, sulfur octyldodecyl, sernistty ok-- tiltsiklopentil, sulfur oktiltsiklos hexyl, sulfur oktiltsiklogeksil , octyl cycloheptyl sulfur, octyl cyclooctyl sulfide, octyl cyclodecid sulfur, nonyldecyl sulfur, nonylundecyl sulfur, non-sulfur sulfide propylbut sludge, propyl propyl, sulphate propylhexyl, sulphurous propylheptyl, sulphurous propyloctyl, sulfurous propylnonyl,
geptilnonil sulfurous, sulphurous gep- tildetsil, sulfur geptilundetsil, geptildodetsil sulfide, sulfurous geptiltsiklopentil, sulfur geptiltsiklogeksil, sulfur geptiltsiklook- Teal, sulfur oktilnonil, oktildetsil sulfide, sulfurous oktilundetsil, sulfur octyldodecyl, sernistty ok-- tiltsiklopentil, sulfur oktiltsiklogeksil, sulfur oktiltsiklogeksil, sulfurous octylcycloheptyl, octylcyclooctyl sulphide, octylcyclodecid sulphide, nonyldecyl sulphide, nonylundecyl sulphide, noniddodecyl sulphide, noni sulphurous liclopystatus
Aliphatic substances can be unbranched and branched, saturated and unsaturated hydrocarbons, such as alkanes, alkenes or alkanes. Cycloaliphatic substances can be saturated and unsaturated cyclic hydrocarbons, such as cycloalkenes and cycloalkanes.
Cycloalkanes are alkanes with one, two, three, or more cyclic rings. Cycloalkenes include mono-, di, and polycyclic groups with one or more double Eves.
Hydrocarbyls are organic radicals containing carbon and hydrogen atoms. The term hydrocarbyl includes the following organic radicals: alkyl, alkenyl, apkinyl, cycloalkyl, cycloalkenyl, aryl, aliphatic and cycloaliphatic aralkyl, and alkaryl. The term refers to biaryl, biphenyl-LU, phenyl, naphthyl, phenanthrenyl, anthracenyl, and two aryl groups linked by alkyl groups. The term alkaryl refers to alkyl-, alkenyl, or alkynyl-substituted aryl substituent groups, where aryl is defined above. The term aralkyl means an alkyl group, where aryl is defined above.
C (, -C. -Alkyl contains unbranched and branched methyl, ethyl, propyl, butyl, pentile, hexyl, heptyl, octyl, nonyl ”decyl, uncecyl, dodecyl, tridecyl, tetradecyl, pentadecyl, hexyl - sadecyl, heptadecyl, octadecyl, nonadecyl and eicosyl groups.
Halo means: chloro ™ - bromo or iodo groups,
The proposed process is suitable for recovery by froth flotation from ores containing metal-sulphide and sulphidized oxidized minerals. By ore is meant
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material extracted from the earth's interior, containing minerals containing the desired metals along with the waste rock. Waste rock refers to a portion of the material mined, free of valuable elements and subject to separation from metal-containing minerals,
The proposed method recovers metal-containing sulphide minerals, sulphide minerals containing copper, nickel, lead, zinc, molybdenum, as well as sulphide minerals containing copper. In addition, the preferred metal-containing sulfide minerals are minerals with a high natural hydrophobicity in the non-oxidized state.
The ores to which the proposed substances can be applied contain sulphide minerals containing copper, zinc, molybdenum, cobalt, nickel, lead, mouse, silver, chromium, gold, platinum, uranium, and mixtures thereof. Examples of minerals that can be concentrated in the froth flotation process of this invention include covellyn (CuS), chalcocite (Cu2S), chalcopyrite (CuFeS2) j valerite (Cu2Fe4S-f or Cu3Fe4S), bornite (CuЈFeS4), cu- banite ( Cu2), enargite Cu3 (AS, Sb) S4), tetrahedrite (Cu3 SbS2), tenantin (J) brochantin tCu / OH), SO), antlerite CCu3 S04 (OH) J; ; tamantine CCu3 (SbAS) S4j and bournonite (PbCuSbS3) containing copper, containing Vie lead minerals, such as galena (PbS), containing sulma materials, such as stibnite (Sb2S3), containing zinc minerals, such as sphalerite (ZnS) containing silver minerals, such as stefanite (Ag5SbS 4) and argentite (Ag2S), containing chromium minerals, such as daubreelite (FeSCrS3), containing nickel minerals, such as pentlandite C (FeNi) 3S, containing molybdenum materials, such as molybdenite (MoS2), containing platinum and palladium minerals, for example, Cooperir СФ1; (Аz5) гЗ, Л1р are electoral containing metals with lfidnyh minerals is - "include molybdenite (MoS2), chalcopyrite (CuFeS2) galena (PbS), sphalerite (ZnS), bornite (Cug-FeS), and pentlandite t (FeNi), S ,. .
Metal-containing sulfidized oxidized minerals are minerals treated with sulfidizing chemicals with
to give these minerals the properties of sulfide minerals and to ensure the extraction of these minerals in the process of froth flotation using collectors that extract sulfide minerals. Sulfidation imparts sulfide properties to oxide minerals. The sulfidation of oxide minerals is accomplished by contact with substances that react with the minerals to form a bond or affinity with sulfur. Such methods are well known in the art. Sodium hydrate, sulfuric acid and the corresponding sulfur-containing salts, such as sodium sulphide, can be used as reagent substances.
Among the metal containing sulfidirovane oxide minerals suitable for use in this invention are oxide minerals containing copper, aluminum, iron, tungsten, molybdenum, magnesium, chromium, nickel, titanium, manganese, tin, uranium, and mixtures thereof. Examples of metal-containing oxide minerals that can be concentrated in the process of froth flotation using this method use copper-containing minerals, such as cuprite (Cu20), tenorite (CuO), Malachite t (Cu2OH) 2C03, azurite GSi3 (OH) 2 (C03) 2 , Attacite Cu2C1 (OH) 3), chrysocolla (CuSi03), aluminum-containing minerals, for example corundum, zinc-containing minerals, for example zincite ZnO smithsonite (ZnC03), tungsten-containing minerals, for example wolframite (Fe, Mn) W04, nickel-containing minerals, for example bunse- Nit (NiO), molybdenum-containing materials, such as wulfenite (PbMoOij) and pbwellite (CaMo04), iron-containing minerals, such as hematite and magnetite; containing chromium minerals, such as chromite (FeOCr203), iron and titanium containing minerals, such as ilmenite, containing magnesium and aluminum minerals, such as spinel, containing iron and chromium minerals, such as rumite, containing titanium minerals, for example rutile, manganese-containing non-minerals, for example, pyrolusite, tin-containing minerals, for example, cassiterite, uranium-containing minerals, eg uranium, as well as uranium-carrying nonerals, for example, UiOHUjO uranium tar, and gummit (i03-n HgO).
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In a preferred embodiment of the isobrag, the use of blowing agents is contemplated. Any foaming agent known in the art and suitable for the extraction of the desired mineral is suitable, for example, SU alcohols, coniferous oils, creaeols, C ug polypropylene glycol alkyl ethers, glycols, fatty acids, polypropylene glycol dihydroxylates, polyols, soaps, alkylarylsulfonates; and the like. Mixtures of these blowing agents can also be used. According to this invention can be used any foaming agents that contribute to the process of froth flotation of ores.
Example 1 Penn flotation of a sulfide mineral containing copper. In the process of froth flotation of a copper-containing sulphide mineral, several proposed collectors were used, 500 g of copper ore, namely chalcopyrite of relatively high quality with a small amount of pyrite. Placed in a rod mill with 2.5 cm rods together with 257 g of deionized water and milled at 60 rpm for 420 rpm, resulting in a particle size distribution of 25% smaller than 100 mesh. Sufficient lime was added to the mill in an amount sufficient to obtain the desired pH in terms of the subsequent flotation process. The resulting suspension was transferred to a 1500 ml chamber with a froth flotation machine. The flotation cell rotated at a speed of 1150 rev / min and the pH value was adjusted to 8.5 added lime.
A collector (8 g / metric ton) was added to the flotation cell, and DOWFROTH 250 (18 g / metric ton) frother was added after 1 minute. After 1 minute, the air supply to the flotation cell was switched on with a flow rate of 4.5 l / min, and then automatic paddle to remove foam. Foam samples were taken che, - cut 0.5; 1.5; 3.5 and 8 min. The foam samples were dried overnight in an oven with the tailings of the flotation process. Dried samples are weighed, divided into appropriate portions for analysis, powdered with uniform particle sizes, and dissolved in acid for analysis. Samples
investigated on a DC plasma spectrograph;
The proposed collectors have higher rates of extraction and equilibrium yield than mercaptan and polysulfide collectors.
Example 2. Penna flotation of copper-molybdenum ore. Portions of homogeneous ore containing 1200 g of chalcopyrite and molybdenite were prepared. The preliminary procedure consisted of grinding 1200 g of batch with 800 ml of tap water in a ball mill with mixed ball loading (to produce approximately 13% of 100 mesh particles). The resulting pulp was transferred to a 1500 mm flotation cell equipped with an automatic vane removal system. The pH value of the pulp was adjusted to 10.2 with lime. After that, the pH value was not regulated. A standard methyl frother, isopropyl carbinip (M1BC), was used. Then a rough flotation was carried out in four stages.
The use of collectors according to this invention significantly increases the total amount of concentrate (grade), i.e. the proportion of the sulfide mineral containing the target metal in the final flotation product, as well as reducing the pyrite content in the concentrate, determined from the analysis of iron, and the improvement does not depend on the dosage. As a result, less material is supplied during the smelting process and the amount of sulfur decreases; per unit weight of the target metal.
-
Example 3. Penn flotation nickel-copper ore with a large content of a pyrite containing pyrite, a gel-containing sulfide mineral.
From the material prepared for the primary flotation, several samples were collected that were deposited. Pull into vessels of up to about 1200 grams of solids in each. The suspension contained the minerals chalcopyrite and penthlandin. The contents of each vessel are then used to derive the output as a function of time.
Flotation was carried out in a Denver chamber using a device for maintaining a constant level of pulp, equipped with an automatic Blade Ref -, e 10
15
20
25
thirty
35
 40
D5
. -Q -, "55
boron concentrate was performed after 1.0; 3.0; 6.0 and 12.0 minutes, the Collector was injected once, and foam collection was started 1 minute after starting the machine. The collector dose was 0.028 kg / m of material entering the flotation process. Concentrate samples were dried, weighed, ground, and statistically representative samples were prepared for analysis. From the standard mass balance equations, the dependence of the yield on time and the overall quality of the enriched ore was calculated.
In terms of copper output, the proposed collectors are comparable to sodium amylxanthate, however, they significantly increase the flotation rate. The collectors give a lower nickel yield compared to sodium amylxanthate, but significantly reduce the yield of undesirable iron containing sulfide mineral pyrrhotite. This is evidenced by the values of RfZ (pyrrhotite) and a more than 50% increase in the selectivity for the nickel sulfide mineral relative to the undesired iron sulfide mineral pyrrhotine.
Example 4 Penn flotation of complex A Pb / Zn / Cu / Ag ore.
The same samples of ore weighing 1000 g each were prepared. The ore contained galena, sphalerite, chalcopyrite and argentite. The sample used in each flotation operation was mixed in a rod mill with 500 ml of tap water and 7.5 ml of solution S02. After grinding for 6.5 minutes, 90% of the particles had sizes less than 200 mesh (75 microns). The milled pulp was transferred to a chamber with an automatic paddle to remove the foam, and the chamber was connected to a standard Denver flotation machine.
A two-step flotation process was performed. At the first stage, coarse flotation of copper — lead — silver was carried out, and at the second stage, coarse zinc flotation. Before the start of the first stage, 1.5 g / kg NAG03 (pH 9.5) was added, and then the collectors. For 5 minutes, the pulp was prepared by mixing and cooling the air, and then 2 minutes only by stirring. M1BC (standard dose of 0.015 ml / kg) was injected as a blowing agent.
31
The concentrate was collected during 5 minutes of flotation and marked as coarse copper - lead concentrate.
At the second stage, 0.5 kg / m was added to the chamber after the first stage. t
CuSO. Using lime supplements, the pH was adjusted to 10.5. Thereafter, the pulp was stirred for 5 minutes, the pH was again checked and adjusted to a value of 10.5 with lime. The collector was then added and mixed again for 5 minutes. M1BC frother was then added (standard dose 0.020 ml / kg). The concentrate was collected for 5 minutes and labeled as coarse zinc concentrate.
Concentrate samples were dried, weighed, and appropriate X-ray samples were prepared from them. According to the analysis and using the standard mass balance equations, yield and quality were calculated,
In addition, tests were performed at a lower pH in the first stage (without adding Na2CO3 pH
8.5) and with the addition of lime in the second stage with the pH adjusted to | 9.5. At the same time, 0.3 kg / m CuSO.,.,
Thus, during the flotation process, the proposed collectors replace a complex mixture of three optimized industrially produced collectors and provide comparable metal output and concentrate quality at a normal pH value and the addition of CuS04 when working with known collectors. Relevant tests at lower pH values and addition of CuSO It appears that these collectors significantly improve the quality (grade) of the metal compared to the three known collectors. This provides significant savings on lime and CuSO on an industrial scale. In this way, the pH is adjusted to 10.5 in the first and to 9.5 in the second step, CuS04 is added to increase the zinc yield.
conservation varieties. With a smaller amount of CuSO 4. The proposed collectors increase the yield of zinc and retain the grade.






Example 5. Penna flotation of copper-molybdenum ore.
In the rod mill with inch rods (2.5 cm) - placed 500 g of copper-molybdenum ore, 257 g deio14
0
sour water and some lime. The mixture was milled for 360 revolutions at a speed of 60 v / min to obtain particles with a desired size distribution (about 25% smaller than 100 mesh). A milled suspension containing various sulfide containing copper minerals and molybdenite were placed in an Agitair flotation cell with a 1500 ml cell capacity. Stirring in the flotation cell was carried out at a speed of 1150 rpm, and the pH value was adjusted to 8.5 by the addition of lime or hydrochloric acid.

A floatation chamber (45 g / mt) was added to the flotation cell and after a preparatory period of 1 min - DOWFROTH 250 foaming agent (36.4 g / mx x t). After holding for 1 minute, the air supply to the chamber was turned on with a flow rate of 4.5 l / min and an automatic blade was started to remove the foam. Foam samples were taken at 0.5; 1.5j i3.5 and 8 min. Samples were dried overnight with the flotation tails. The dried samples were weighed and divided into appropriate samples for analysis, which were then ground into powder and dissolved in acid for subsequent analysis in a DC plasma spectrograph.
The proposed collectors provide-. The yield of molybdenum is higher than with a standard reagent, but with a reduced yield of copper. The yield of undesired iron-containing sulfide minerals is significantly reduced.
Example 6 Penn Flotation Copper Ore
The procedure of Example 1 was repeated using ore from another slab of the same mine containing relatively high-quality chalcopyrite and a small amount of pyrite.
acquisitions
Formula and
A method for extracting metal-containing sulfide minerals or sulfidized metal-containing oxidized minerals from ores, including pulping ore, processing a pulp with a sulfur-containing collector, and flotation, characterized in that, in order to increase the efficiency and selectivity of the process, the input t sulfide formula
R (- S - R2,
where R1 is methyl, ethyl, epoxy, such as the group
n n

权利要求:
Claims (2)
[1]
I I
- / h
J j
V
or a hydrocarbon radical substituted by one or more simple halide
ether or hydrocarbon thioether moieties;
R-- an aliphatic, cycloaliphatic, aromatic group, or a combination of them, containing
5-11 carbon atoms; R1 and RJ
can be combined to form an epitio-ring structure with a sulfur atom, provided that the sulfur atom is attached to aliphatic or cycloaliphatic carbon atoms, the total carbon content in the sulfide collector is 6-20 carbon atoms, RI, and RJ are not identical hydrocarbon fragments.
[2]
2. A process according to claim 1, wherein R is methyl or ethyl and Rj is Ct-Cf-alkyl or C-SG1-alkenyl.
3, a method according to claim 1, characterized in that the concentration of the collector is 0.001-1.0 kg of collector per 1000 kg of ore subjected to froth flotation.
4 "The method according to claim 1, wherein R and R2 are combined to form an epitiole structure, wherein the collector has the general formula
20
, U4)
s
(B)
where r4 and r 4
independently hydrogen, and an aliphatic, cycloaliphatic, aromatic moiety or a combination thereof, unsubstituted or substituted by a hydroxy, cyano, OR3 or Cs moiety, where R3 is a hydrocarbon radical, provided that at least one of R4 or R4 does not is hydrogen.

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同族专利:

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公开号 | 公开日

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FI870368A|1987-01-28|

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ES552027A0|1987-10-16|

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ZW4086A1|1987-09-09|

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PL147849B1|1989-08-31|

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RO100591B1|1992-01-28|

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ES8800077A1|1987-10-16|

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SE8700376D0|1987-01-30|

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PL257991A1|1987-12-14|

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ZM1286A1|1988-12-30|

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CN106179767B|2016-09-23|2018-04-03|中南大学|A kind of application of the thiones flotation collector of 1,3,4 oxadiazole 2|

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CN108057525A|2017-11-27|2018-05-22|西北矿冶研究院|A kind of flotation collector that associated gold is improved for Treating Low-grade Copper Ores and copper-molybdenum and preparation method thereof|

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法律状态:
2005-05-10| REG| Reference to a code of a succession state|Ref country code: RU Ref legal event code: MM4A Effective date: 20040219 |

优先权:

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申请号 | 申请日 | 专利标题

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US74009185A| true| 1985-05-31|1985-05-31|

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