CN101816979B - Flotation activating agent of marmatite and blende and preparation method thereof - Google Patents
Flotation activating agent of marmatite and blende and preparation method thereof Download PDFInfo
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- CN101816979B CN101816979B CN201010124710.7A CN201010124710A CN101816979B CN 101816979 B CN101816979 B CN 101816979B CN 201010124710 A CN201010124710 A CN 201010124710A CN 101816979 B CN101816979 B CN 101816979B
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- 238000005188 flotation Methods 0.000 title claims abstract description 24
- 230000003213 activating effect Effects 0.000 title claims abstract description 16
- 238000002360 preparation method Methods 0.000 title claims abstract description 8
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims abstract description 28
- 229910021529 ammonia Inorganic materials 0.000 claims abstract description 13
- 229910052984 zinc sulfide Inorganic materials 0.000 claims description 36
- WGPCGCOKHWGKJJ-UHFFFAOYSA-N sulfanylidenezinc Chemical compound [Zn]=S WGPCGCOKHWGKJJ-UHFFFAOYSA-N 0.000 claims description 34
- 238000006243 chemical reaction Methods 0.000 claims description 31
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 24
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 14
- 238000007605 air drying Methods 0.000 claims description 6
- 239000012043 crude product Substances 0.000 claims description 6
- 230000006837 decompression Effects 0.000 claims description 6
- 238000001914 filtration Methods 0.000 claims description 6
- 238000002156 mixing Methods 0.000 claims description 6
- 239000013049 sediment Substances 0.000 claims description 6
- 238000004062 sedimentation Methods 0.000 claims description 6
- 239000007787 solid Substances 0.000 claims description 6
- 239000002904 solvent Substances 0.000 claims description 6
- 238000003756 stirring Methods 0.000 claims description 6
- 238000005406 washing Methods 0.000 claims description 6
- 239000003446 ligand Substances 0.000 claims description 4
- 239000011701 zinc Substances 0.000 abstract description 35
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 abstract description 34
- 229910052725 zinc Inorganic materials 0.000 abstract description 34
- 239000010949 copper Substances 0.000 abstract description 15
- 230000004913 activation Effects 0.000 abstract description 13
- 238000011084 recovery Methods 0.000 abstract description 12
- ARUVKPQLZAKDPS-UHFFFAOYSA-L copper(II) sulfate Chemical compound [Cu+2].[O-][S+2]([O-])([O-])[O-] ARUVKPQLZAKDPS-UHFFFAOYSA-L 0.000 abstract description 11
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 abstract description 10
- 229910052802 copper Inorganic materials 0.000 abstract description 10
- 235000008733 Citrus aurantifolia Nutrition 0.000 abstract description 9
- 235000011941 Tilia x europaea Nutrition 0.000 abstract description 9
- 239000003795 chemical substances by application Substances 0.000 abstract description 9
- 239000004571 lime Substances 0.000 abstract description 9
- 239000012141 concentrate Substances 0.000 abstract description 7
- 239000002184 metal Substances 0.000 abstract description 7
- 229910052751 metal Inorganic materials 0.000 abstract description 7
- 229910052569 sulfide mineral Inorganic materials 0.000 abstract description 7
- 238000004519 manufacturing process Methods 0.000 abstract description 5
- 150000001875 compounds Chemical class 0.000 abstract 2
- 230000005764 inhibitory process Effects 0.000 abstract 1
- 229910000069 nitrogen hydride Inorganic materials 0.000 abstract 1
- 229910000510 noble metal Inorganic materials 0.000 abstract 1
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 37
- 239000012190 activator Substances 0.000 description 35
- 238000000034 method Methods 0.000 description 23
- 229910052742 iron Inorganic materials 0.000 description 18
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 12
- 229910052500 inorganic mineral Inorganic materials 0.000 description 12
- 239000011707 mineral Substances 0.000 description 12
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 9
- 239000005864 Sulphur Substances 0.000 description 8
- 229910052738 indium Inorganic materials 0.000 description 7
- APFVFJFRJDLVQX-UHFFFAOYSA-N indium atom Chemical compound [In] APFVFJFRJDLVQX-UHFFFAOYSA-N 0.000 description 7
- 230000000694 effects Effects 0.000 description 5
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 4
- 238000000926 separation method Methods 0.000 description 4
- 229910052718 tin Inorganic materials 0.000 description 4
- XOLBLPGZBRYERU-UHFFFAOYSA-N tin dioxide Chemical compound O=[Sn]=O XOLBLPGZBRYERU-UHFFFAOYSA-N 0.000 description 4
- GZCWPZJOEIAXRU-UHFFFAOYSA-N tin zinc Chemical compound [Zn].[Sn] GZCWPZJOEIAXRU-UHFFFAOYSA-N 0.000 description 4
- 239000003513 alkali Substances 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 3
- 229910052737 gold Inorganic materials 0.000 description 3
- 239000010931 gold Substances 0.000 description 3
- 239000010970 precious metal Substances 0.000 description 3
- 229910052683 pyrite Inorganic materials 0.000 description 3
- NIFIFKQPDTWWGU-UHFFFAOYSA-N pyrite Chemical compound [Fe+2].[S-][S-] NIFIFKQPDTWWGU-UHFFFAOYSA-N 0.000 description 3
- 239000011028 pyrite Substances 0.000 description 3
- 239000011135 tin Substances 0.000 description 3
- GYHNNYVSQQEPJS-UHFFFAOYSA-N Gallium Chemical compound [Ga] GYHNNYVSQQEPJS-UHFFFAOYSA-N 0.000 description 2
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 2
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L calcium sulfate Chemical compound [Ca+2].[O-]S([O-])(=O)=O OSGAYBCDTDRGGQ-UHFFFAOYSA-L 0.000 description 2
- 230000002950 deficient Effects 0.000 description 2
- 238000006477 desulfuration reaction Methods 0.000 description 2
- 230000023556 desulfurization Effects 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 229910052733 gallium Inorganic materials 0.000 description 2
- 229910052732 germanium Inorganic materials 0.000 description 2
- GNPVGFCGXDBREM-UHFFFAOYSA-N germanium atom Chemical compound [Ge] GNPVGFCGXDBREM-UHFFFAOYSA-N 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 239000003112 inhibitor Substances 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- 238000010310 metallurgical process Methods 0.000 description 2
- 238000005065 mining Methods 0.000 description 2
- 229910052709 silver Inorganic materials 0.000 description 2
- 239000004332 silver Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 241000784732 Lycaena phlaeas Species 0.000 description 1
- 239000005083 Zinc sulfide Substances 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 229910052787 antimony Inorganic materials 0.000 description 1
- WATWJIUSRGPENY-UHFFFAOYSA-N antimony atom Chemical compound [Sb] WATWJIUSRGPENY-UHFFFAOYSA-N 0.000 description 1
- MJLGNAGLHAQFHV-UHFFFAOYSA-N arsenopyrite Chemical compound [S-2].[Fe+3].[As-] MJLGNAGLHAQFHV-UHFFFAOYSA-N 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 229910052951 chalcopyrite Inorganic materials 0.000 description 1
- DVRDHUBQLOKMHZ-UHFFFAOYSA-N chalcopyrite Chemical compound [S-2].[S-2].[Fe+2].[Cu+2] DVRDHUBQLOKMHZ-UHFFFAOYSA-N 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000009429 distress Effects 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 238000005530 etching Methods 0.000 description 1
- ZOOODBUHSVUZEM-UHFFFAOYSA-N ethoxymethanedithioic acid Chemical compound CCOC(S)=S ZOOODBUHSVUZEM-UHFFFAOYSA-N 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 238000009854 hydrometallurgy Methods 0.000 description 1
- NJWNEWQMQCGRDO-UHFFFAOYSA-N indium zinc Chemical compound [Zn].[In] NJWNEWQMQCGRDO-UHFFFAOYSA-N 0.000 description 1
- NNIPDXPTJYIMKW-UHFFFAOYSA-N iron tin Chemical compound [Fe].[Sn] NNIPDXPTJYIMKW-UHFFFAOYSA-N 0.000 description 1
- JQJCSZOEVBFDKO-UHFFFAOYSA-N lead zinc Chemical compound [Zn].[Pb] JQJCSZOEVBFDKO-UHFFFAOYSA-N 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 230000035945 sensitivity Effects 0.000 description 1
- 229910052950 sphalerite Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- AFNRRBXCCXDRPS-UHFFFAOYSA-N tin(ii) sulfide Chemical compound [Sn]=S AFNRRBXCCXDRPS-UHFFFAOYSA-N 0.000 description 1
- 239000012991 xanthate Substances 0.000 description 1
- -1 zinc and tin Chemical class 0.000 description 1
- DRDVZXDWVBGGMH-UHFFFAOYSA-N zinc;sulfide Chemical compound [S-2].[Zn+2] DRDVZXDWVBGGMH-UHFFFAOYSA-N 0.000 description 1
Abstract
The invention provides a flotation activating agent of marmatite and blende, which is a coordination compound of copper and ammonia and is characterized in that the molecular formula of the coordination compound is [Cu(NH3)x]2+, wherein X=1-8. The activating agent of the invention solves the problem of selected activation and inhibition of marmatite, overcomes the problems of low activation selection, low zinc concentrate grade, serious metal mutual containing and the like of common activating agent copper sulphate and solves the problems of high-efficiency enrichment and comprehensive recovery of concomitant rare and noble metal. The activating agent is activated under the condition that pH value is as low as 7-11, provides necessary guarantee for reducing lime dosage in production, reasonably and effectively recovers other sulfide minerals and comprehensively recovers rare metal, and has the advantages of high activation efficiency, low production cost and the like. The invention also applies a preparation method for the flotation activating agent.
Description
Technical field
The present invention relates to ore dressing engineering and rare precious metal comprehensive utilization technique field, particularly a kind of efficient activator for marmatite and Sphalerite flotation and its production and use.
Background technology
China's zinc metal reserves account for 15% of world's gross reserves, occupy the second in the world, and simultaneously China is also a zinc big producing country, and zinc metal output reached 374.9 ten thousand tons in 2007, ranked first in the world, and export volume reaches 27.56 ten thousand tons.development along with national economy, increase to zinc metal demand, in the urgent need to the resource of complicated difficult choosing is developed and is utilized, it is more domestic that leaded, zinc, sulphur, iron or zinc, copper, tin, iron, the plumbous zinc ore mountain of sulphur and zinc-tin mine etc. be in various degree the marmatite that contains choosing in distress all, for example, the large factory in Guangxi, the plumbous zinc ore in river three, the yellow sand level ground in Hunan, Pan Jiachong, the plumbous zinc ore of HERBA ONYCHII, the plumbous zinc ore in the Hezhang in Guizhou, the plumbous zinc ore in tin iron mountain in Qinghai, the plumbous zinc ore in the XiLin in Heilungkiang, the Fangniugou Pyrite in Jilin, therefore ox is washed in a pan plumbous zinc ore, the plumbous zinc ore of thick mother-in-law's col in Guangdong, all Long Xinxikuang and the lead ore of Lancang etc. in Yunnan.The marmatite iron content in these mines is generally 8-12%, have up to 26%, therefore, adopt suitable marmatite ore-dressing technique, marmatite is developed and utilized significant.
Zincblende, marmatite and wurtzite are three kinds of common zinc sulfide minerals.Zincblende (ZnS) belongs to isometric system, and crystalline form is often tetrahedron; Natural cleiophane contains zinc 67.1%, 32.9% sulphur.Wurtzite is general similar to the physical property of zincblende, generally rare in practice.The zincblende of iron content more than 6% is called marmatite [(Zn
XFe
1-XS)], zinc blend lattice is often sneaked into isomorph by Tie Tong, and the quantity of infiltrating iron is generally 6～12% (Gao Shida 26%).
In actual process, marmatite than zincblende show not easily-activated, floatability is poor, to characteristics such as medium sensitivities, it is more difficult to separate with mineral such as magnetic iron ore, pyrite and mispickel.Simultaneously, compare with other sulfide mineral, the floatability of marmatite or zincblende is far smaller than other sulfide minerals, general not activated marmatite or the flotation of zincblende need to need the above xanthate of 4 carbon with hybrid collector or chain length, make the flotation of zincblende seem more difficult.Therefore, activation is the important step in the marmatite ore dressing.Main with the activator of copper sulphate as marmatite in producing at present, however copper sulphate has following defective as activator:
(1) select marmatite for difficulty, the activation of copper sulphate is unsatisfactory, does not reach good index.
(2) activity function of copper sulphate strengthens along with the enhancing of alkalescence, therefore, the activation of copper sulphate is generally to carry out under a high-alkali environment, thereby certainly will add a large amount of lime aborning, so just suppress the flotation of the relatively poor zincblende of floatability, marmatite and oxidized mineral such as chalcopyrite.
(3) rolling up of lime consumption not only increases beneficiation cost, increases workman's workload, and from ore dressing and comprehensive the recovery and the angle of utilizing, the lime of large consumption is also worthless.After adjusting the pH value and suppress other sulfide minerals with a large amount of lime in selecting the zinc process, during next step flotation must come with a large amount of sulfuric acid and the lime in ore pulp, to reduce the pH value, perhaps add a large amount of activator activation and other sulfide minerals of flotation, this has not only further increased beneficiation cost, and the calcium sulfate that lime and sulfuric acid reaction generate is easy to blocking pipe, at the gravitational separation equipment surface scale, seriously affects the continuity of mineral processing circuit and the rate of recovery of gravity treatment; In addition, sulfuric acid also can produce etching problem to pipeline and preparation equipment.
(4) copper sulphate and combination activator thereof in the activation marmatite, also can activate difficult floating magnetic iron ore, increase the iron content in zinc concentrate, to follow-up hydrometallurgy process, zinc and indium further separated with enrichment very unfavorable.In order to suppress magnetic iron ore, the kind of inhibitor may many and large usage quantity, and flow process is also more complicated.If the activator that adopts is under low alkali condition, do not activate magnetic iron ore or pyrite and only activate marmatite and zincblende, can simplify the deironing sulfur removal technology, save production cost, improve grade and the rate of recovery of zinc concentrate zinc, indium, silver etc., reduce the content of iron and sulphur in zinc concentrate, reduce the element such as iron in zinc concentrate to the adverse effect of follow-up metallurgical process; Simultaneously, can also improve significantly the rate of recovery of reselection operation.
As seen, there are a lot of defectives in the conventional activator of the at present domestic and international marmatite that adopts and inhibitor, and its activation and the efficient that suppresses and selectively not high cause the rate of recovery of zinc and zinc concentrate grade not high, and metal contains seriously mutually.
Summary of the invention
The objective of the invention is: overcome the deficiency of existing activator copper sulphate, the dressing activator of the high marmatite of a kind of activation efficiency and zincblende is provided.This activator has the characteristics such as selective height, the rate of recovery are high, environmental friendliness.Because the pH value of needs is lower, the scope of application is wider.
Technical scheme of the present invention is: the dressing activator of making marmatite and zincblende with the complex of copper and ammonia is.Activator of the present invention can use under the low alkalinity environmental condition, according to the concrete condition of ore, is to use under 7～11 environment in the pH value, and is respond well.
The flotation activating of marmatite of the present invention and zincblende is the complex of copper and ammonia, it is characterized in that, the molecular formula of said complex is: [Cu (NH
3)
x]
2+, X=1 in formula～8.
The preparation method of the flotation activating of marmatite of the present invention and zincblende, it is characterized in that, preparation section is as follows, said in the operation of following a～c " by the suitable metered proportions of chemical reaction " refers to the completeness in order to react, the additional proportion of central ion, ligand must satisfy the corresponding conditions of chemical reaction at least, under the principle of not wasting, excessive 0.5～10.0 quality % of the comparable central ion of ligand;
A, by the suitable metered proportions of chemical reaction, ammonia is dissolved in a kind of solvent of selecting from the second alcohol and water, obtains the first solution (A), the concentration of solution is 0.5～25 quality %;
B, press the suitable metered proportions of chemical reaction with Cu (NO
3)
23H
2O or CuSO
45H
2O is dissolved in a kind of solvent of selecting from the second alcohol and water, obtains the second solution (B), and the concentration of solution is 0.5～50 quality %;
C, press the suitable metered proportions of chemical reaction with NaOH and Na
2CO
3Be dissolved in a kind of solvent of selecting from the second alcohol and water, obtain the third solution (C), the concentration of solution is 5～40 quality %;
Under d, stirring, A solution is gently joined in B solution, under the mixing speed of 150～200 rev/mins, reacted under room temperature 2～30 minutes, add again C solution, continue reaction 3～25 minutes under room temperature, add at last a kind of solution of selecting from the second alcohol and water, reaction generates the crude product of solids of sedimentation;
E, reacted solution decompression is filtered, use C
2H
5The sediment that the OH washing and filtering obtains blots with filter paper, then at air drying, namely obtains the flotation activating sterling.
This activator can adopt common copper to coordinate technique to be prepared with ammonia etc., in the ore dressing process in the plumbous zinc ore that contains marmatite and zincblende and zinc-tin ore deposit, as activator, the marmatite in ore and zincblende are activated, improve the floatability of marmatite and zincblende.In complex, the ratio of copper and ammonia etc. can be according to the situation of concrete ore dressing raw material, uses in lower pH value scope and certain consumption, need to not operate under high alkali environment.
This activator all can use in the flotation of marmatite and zincblende polymetallic ore and gravity separation technology.
The present invention adopts the complex of copper and ammonia etc. as activator, effect due to copper and ammonia etc., strengthened the hydrophobicity of surface of marmatite, make this activator only optionally activate marmatite, overcome conventional activator selectively not high, the zinc concentrate grade is not high and reclaim zinc and indium etc. for follow-up metallurgical process and cause disadvantageous technical bottleneck, has solved well the problem of marmatite floatation process activation efficiency.
Compare with prior art, the present invention has the following advantages or good effect:
1, solved a difficult difficult problem of selecting the marmatite activation;
2, activator of the present invention need to not activate under high pH value condition, mainly uses under neutrality, low alkalinity environment, and the ore pulp environment pH value of using is 7～11.This just provides necessary assurance for reducing lime consumption, reasonable effectively recovery other sulfide minerals, cassiterite in producing and comprehensively reclaiming rare precious metal.
3, the production cost of activator is lower than the cost of copper sulphate, be also that enterprise is under low basicity condition, realize efficient separation and the enrichment of zinc-sulphur, tin-sulphur, lead-zinc etc., and can create condition for carrying out effective desulfurization, reduction sulfuric acid consumption, raising zinc indium grade and the rate of recovery before reselection operation.
The specific embodiment:
The present invention is further elaborated below in conjunction with embodiment.
Embodiment 1
Get appropriate ammonia and be dissolved in ethanol, obtain the first solution (A), the concentration of solution is 0.5 quality %; Get appropriate Cu (NO
3)
23H
2O is dissolved in ethanol, obtains the second solution (B), and the concentration of solution is 0.5 quality %; Press the suitable metered proportions of chemical reaction with NaOH and Na
2CO
3Be dissolved in ethanol, obtain the third solution (C), the concentration of solution is 5 quality %; Under stirring, A solution is gently joined in B solution, under the mixing speed of 150 rev/mins, under room temperature, reaction is 2 minutes, then adds C solution, continues reaction 3 minutes under room temperature, adds at last entry, and reaction generates the crude product of solids of sedimentation; Reacted solution decompression is filtered, use C
2H
5The sediment that the OH washing and filtering obtains blots with filter paper, then at air drying, namely obtains the flotation activating sterling, is the Novel mineral activator of marmatite and zincblende.
Treat that ore dressing is the ore of Dachang, Guangxi, the elements such as leaded in ore, antimony, zinc, sulphur, iron, indium and silver, wherein mineral content contains 0.7～10.5% marmatite and 0.4% above zincblende, and in marmatite, the content of iron reaches 11% left and right.Adopt common ore-dressing technique, add this activator in floatation process, add common collecting agent, through conventional flotation, ore dressing environment pH value is 7.
Adopt this activator, through above-mentioned technical process, can reclaim well marmatite and zincblende.
Embodiment 2
Get appropriate ammonia and be dissolved in the water, obtain the first solution (A), the concentration of solution is 6.25 quality %; Get appropriate CuSO
45H
2O is dissolved in the water, and obtains the second solution (B), and the concentration of solution is 25 quality %; Press the suitable metered proportions of chemical reaction with NaOH and Na
2CO
3Be dissolved in the water, obtain the third solution (C), the concentration of solution is 20 quality %; Under stirring, A solution is gently joined in B solution, under the mixing speed of 200 rev/mins, under room temperature, reaction is 15 minutes, then adds C solution, continues reaction 10 minutes under room temperature, adds at last ethanol, and reaction generates the crude product of solids of sedimentation; Reacted solution decompression is filtered, use C
2H
5The sediment that the OH washing and filtering obtains blots with filter paper, then at air drying, namely obtains the flotation activating sterling, is the Novel mineral activator of marmatite and zincblende.
Treat that ore dressing is ore in imperial zinc-tin mining area all, wherein contain zinc, copper, tin, iron, sulphur, indium, gallium, germanium, gold and the element such as silver-colored, wherein mineral content contains 0.7～11.8% marmatite and 0.5% above zincblende, and in marmatite, the content of iron reaches more than 20%.Adopt common ore-dressing technique, add this activator in floatation process, then add common collecting agent, through conventional flotation, ore dressing environment pH value is 9.
Adopt this activator, through above-mentioned technical process, sub-elect marmatite and the 50% above zincblende of grade more than 46%, the rate of recovery can reach more than 90% respectively.
Embodiment 3
Get appropriate ammonia and be dissolved in the water, obtain the first solution (A), the concentration of solution is 25 quality %; Get appropriate Cu (NO
3)
2Be dissolved in the water, obtain the second solution (B), the concentration of solution is 50 quality %; Press the suitable metered proportions of chemical reaction with NaOH and Na
2CO
3Be dissolved in the water, obtain the third solution (C), the concentration of solution is 40 quality %; Under stirring, A solution is gently joined in B solution, under the mixing speed of 150 rev/mins, under room temperature, reaction is 30 minutes, then adds C solution, continues reaction 25 minutes under room temperature, adds at last ethanol, and reaction generates the crude product of solids of sedimentation; Reacted solution decompression is filtered, use C
2H
5The sediment that the OH washing and filtering obtains blots with filter paper, then at air drying, namely obtains the flotation activating sterling, is the Novel mineral activator of marmatite and zincblende.
Treat that ore dressing is the ore in lead ore of Lancang district, contain zinc, copper, iron, sulphur, indium, gold and the element such as silver-colored in ore, wherein mineral content contains 0.5～9.8% marmatite and 0.6% above zincblende.Adopt common ore-dressing technique, add this activator in floatation process, then add common collecting agent, with the process conventional flotation, ore dressing environment pH value is 11.
Adopt this activator, through above-mentioned technical process, sub-elect marmatite and the 46% above zincblende of grade more than 40%.
Embodiment 4
Get appropriate ammonia and be dissolved in ethanol, obtain the first solution (A), the concentration of solution is 5 quality %; Get appropriate CuSO
45H
2O is dissolved in ethanol, obtains the second solution (B), and the concentration of solution is 40%; Press the suitable metered proportions of chemical reaction with NaOH and Na
2CO
3Be dissolved in ethanol, obtain the third solution (C), the concentration of solution is 10 quality %; Under stirring, A solution is gently joined in B solution, under the mixing speed of 180 rev/mins, under room temperature, reaction is 20 minutes, then adds C solution, continues reaction 15 minutes under room temperature, adds at last entry, and reaction generates the crude product of solids of sedimentation; Reacted solution decompression is filtered, use C
2H
5The sediment that the OH washing and filtering obtains blots with filter paper, then at air drying, namely obtains the flotation activating sterling, is the Novel mineral activator of marmatite and zincblende.
Treat that ore dressing is ore in imperial zinc-tin mining area all, contain zinc, copper, tin, iron, sulphur, indium, gallium, germanium, gold and the element such as silver-colored in ore, wherein mineral content contains 0.7～11.8% marmatite and 0.5% above zincblende.Adopt common ore-dressing technique, add this activator in floatation process, then add common collecting agent, with the process conventional flotation, ore dressing environment pH value is 8.
Adopt this activator, through above-mentioned technical process, sub-elect marmatite and 50% above zincblende more than 45%, the rate of recovery can reach more than 90% respectively.
Comparison by activator of the present invention and copper sulphate, this novel activator has very large advantage, it is not only better to the activation effect of marmatite, and need to not activate under high pH value condition, this is significant aborning, it significantly reduces lime and sulfuric acid consumption in producing, reclaiming efficiently other sulfide minerals, cassiterite and comprehensively reclaiming rare precious metal provides necessary assurance.
The cost of activator of the present invention is lower than copper sulphate, be also that enterprise is under low basicity condition, realize carrying out effective desulfurization before zinc-sulfur highly effective separation and enrichment, reselection operation, reduce the sulfuric acid consumption, improve grade and the rate of recovery of the metals such as zinc and tin, market prospects are fine.
Claims (1)
1. the preparation method of the flotation activating of a marmatite and zincblende, it is characterized in that, preparation section is as follows, said in following 2.1～2.3 operation " by the suitable metered proportions of chemical reaction " refers to the completeness in order to react, the additional proportion of central ion, ligand must satisfy the corresponding conditions of chemical reaction at least, under the principle of not wasting, ligand is than excessive 0.5～10.0 quality % of central ion;
2.1, by the suitable metered proportions of chemical reaction, ammonia is dissolved in a kind of solvent of selecting from the second alcohol and water, obtain the first solution A, the concentration of solution is 0.5～25 quality %;
2.2, press the suitable metered proportions of chemical reaction with Cu (NO
3)
23H
2O or CuSO
45H
2O is dissolved in a kind of solvent of selecting from the second alcohol and water, obtains the second solution B, and the concentration of solution is 0.5～50 quality %;
2.3, press the suitable metered proportions of chemical reaction with NaOH and Na
2CO
3Be dissolved in a kind of solvent of selecting from the second alcohol and water, obtain the third solution C, the concentration of solution is 5～40 quality %;
2.4, the first solution A is gently joined in the second solution B under stirring, mixing speed at 150～200 rev/mins, reacted under room temperature 2～30 minutes, add again the third solution C, continue reaction 3～25 minutes under room temperature, add at last a kind of solution of selecting from the second alcohol and water, reaction generates the crude product of solids of sedimentation;
2.5, reacted solution decompression is filtered, use C
2H
5The sediment that the OH washing and filtering obtains blots with filter paper, then at air drying, namely obtains the flotation activating sterling.
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| CN105772226A (en) * | 2016-03-16 | 2016-07-20 | 云南缘矿科技开发有限公司 | Flotation activating agent for fine-grain cassiterite and preparing method of flotation activating agent |
| CN108940604B (en) * | 2018-07-27 | 2020-07-21 | 攀枝花学院 | Ferro-sphalerite flotation activator and preparation method and application thereof |
| CN111659531B (en) * | 2020-06-16 | 2021-03-23 | 昆明理工大学 | Method for flotation separation of lead-zinc sulfide ore containing intergrowth |
| CN111659529B (en) * | 2020-06-16 | 2021-02-19 | 昆明理工大学 | Method for separating and utilizing micro-fine particle embedded lead-zinc oxide ore by dressing and smelting |
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| US3936294A (en) * | 1974-08-28 | 1976-02-03 | Childress Kenneth A | Reagent for zinc ore and method of utilizing same |
| US6484883B1 (en) * | 2000-10-18 | 2002-11-26 | Phibro-Tech Inc. | Use of cupric chloride in zinc flotation |
| CN1680042A (en) * | 2004-04-05 | 2005-10-12 | 黎东明 | Stepped flotation of tin, lead and zinc sulfide mine |
| CN1817468A (en) * | 2006-03-13 | 2006-08-16 | 昆明理工大学 | Coal-dressing activator of ferrous blende and blende |
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| US3936294A (en) * | 1974-08-28 | 1976-02-03 | Childress Kenneth A | Reagent for zinc ore and method of utilizing same |
| US6484883B1 (en) * | 2000-10-18 | 2002-11-26 | Phibro-Tech Inc. | Use of cupric chloride in zinc flotation |
| CN1680042A (en) * | 2004-04-05 | 2005-10-12 | 黎东明 | Stepped flotation of tin, lead and zinc sulfide mine |
| CN1817468A (en) * | 2006-03-13 | 2006-08-16 | 昆明理工大学 | Coal-dressing activator of ferrous blende and blende |
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