CN104815762B - A kind of preparation method of tennantite collecting agent - Google Patents
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- 238000002360 preparation method Methods 0.000 title claims abstract description 9
- 229910052970 tennantite Inorganic materials 0.000 title claims abstract 10
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims abstract description 27
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 11
- 229910001868 water Inorganic materials 0.000 claims abstract description 11
- 229910052979 sodium sulfide Inorganic materials 0.000 claims abstract description 10
- GRVFOGOEDUUMBP-UHFFFAOYSA-N sodium sulfide (anhydrous) Chemical compound [Na+].[Na+].[S-2] GRVFOGOEDUUMBP-UHFFFAOYSA-N 0.000 claims abstract description 10
- 239000007788 liquid Substances 0.000 claims abstract description 6
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 claims abstract description 5
- 229910052938 sodium sulfate Inorganic materials 0.000 claims abstract description 5
- 235000011152 sodium sulphate Nutrition 0.000 claims abstract description 5
- -1 phosphate ester Chemical class 0.000 claims abstract description 3
- 238000003756 stirring Methods 0.000 claims abstract description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract 2
- 229910019142 PO4 Inorganic materials 0.000 claims abstract 2
- 239000010452 phosphate Substances 0.000 claims abstract 2
- 238000005188 flotation Methods 0.000 claims description 12
- 229910052500 inorganic mineral Inorganic materials 0.000 claims description 12
- 239000011707 mineral Substances 0.000 claims description 12
- 238000000034 method Methods 0.000 claims description 5
- 239000004088 foaming agent Substances 0.000 claims description 4
- 239000000178 monomer Substances 0.000 claims description 4
- 239000002002 slurry Substances 0.000 claims description 4
- 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 claims description 3
- 239000011734 sodium Substances 0.000 claims description 3
- 229910052708 sodium Inorganic materials 0.000 claims description 3
- 239000012190 activator Substances 0.000 claims description 2
- 239000000243 solution Substances 0.000 claims 5
- 238000007792 addition Methods 0.000 claims 1
- 238000000227 grinding Methods 0.000 claims 1
- 239000000203 mixture Substances 0.000 claims 1
- 229910052760 oxygen Inorganic materials 0.000 claims 1
- 239000001301 oxygen Substances 0.000 claims 1
- 239000011550 stock solution Substances 0.000 claims 1
- AQLMHYSWFMLWBS-UHFFFAOYSA-N arsenite(1-) Chemical compound O[As](O)[O-] AQLMHYSWFMLWBS-UHFFFAOYSA-N 0.000 description 23
- 229910052969 tetrahedrite Inorganic materials 0.000 description 14
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 8
- 229910052802 copper Inorganic materials 0.000 description 8
- 239000010949 copper Substances 0.000 description 8
- 238000011084 recovery Methods 0.000 description 6
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 5
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 4
- 229910001779 copper mineral Inorganic materials 0.000 description 4
- 229910000365 copper sulfate Inorganic materials 0.000 description 4
- ARUVKPQLZAKDPS-UHFFFAOYSA-L copper(II) sulfate Chemical compound [Cu+2].[O-][S+2]([O-])([O-])[O-] ARUVKPQLZAKDPS-UHFFFAOYSA-L 0.000 description 4
- 239000002994 raw material Substances 0.000 description 4
- 230000004913 activation Effects 0.000 description 3
- OMZSGWSJDCOLKM-UHFFFAOYSA-N copper(II) sulfide Chemical compound [S-2].[Cu+2] OMZSGWSJDCOLKM-UHFFFAOYSA-N 0.000 description 3
- 239000003814 drug Substances 0.000 description 3
- 150000002191 fatty alcohols Chemical class 0.000 description 3
- 239000003112 inhibitor Substances 0.000 description 3
- 229910052742 iron Inorganic materials 0.000 description 3
- 150000003904 phospholipids Chemical class 0.000 description 3
- 229940051841 polyoxyethylene ether Drugs 0.000 description 3
- 229920000056 polyoxyethylene ether Polymers 0.000 description 3
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 2
- 241000907663 Siproeta stelenes Species 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 235000011941 Tilia x europaea Nutrition 0.000 description 2
- 229910052785 arsenic Inorganic materials 0.000 description 2
- RQNWIZPPADIBDY-UHFFFAOYSA-N arsenic atom Chemical compound [As] RQNWIZPPADIBDY-UHFFFAOYSA-N 0.000 description 2
- HHSPVTKDOHQBKF-UHFFFAOYSA-J calcium;magnesium;dicarbonate Chemical compound [Mg+2].[Ca+2].[O-]C([O-])=O.[O-]C([O-])=O HHSPVTKDOHQBKF-UHFFFAOYSA-J 0.000 description 2
- 229910052947 chalcocite Inorganic materials 0.000 description 2
- 229910052951 chalcopyrite Inorganic materials 0.000 description 2
- DVRDHUBQLOKMHZ-UHFFFAOYSA-N chalcopyrite Chemical compound [S-2].[S-2].[Fe+2].[Cu+2] DVRDHUBQLOKMHZ-UHFFFAOYSA-N 0.000 description 2
- 239000012141 concentrate Substances 0.000 description 2
- 239000004571 lime Substances 0.000 description 2
- 229910001607 magnesium mineral Inorganic materials 0.000 description 2
- 229910052683 pyrite Inorganic materials 0.000 description 2
- NIFIFKQPDTWWGU-UHFFFAOYSA-N pyrite Chemical compound [Fe+2].[S-][S-] NIFIFKQPDTWWGU-UHFFFAOYSA-N 0.000 description 2
- 239000011028 pyrite Substances 0.000 description 2
- 229910052952 pyrrhotite Inorganic materials 0.000 description 2
- 239000000377 silicon dioxide Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000011593 sulfur Substances 0.000 description 2
- 229910052717 sulfur Inorganic materials 0.000 description 2
- 238000010408 sweeping Methods 0.000 description 2
- JPVYNHNXODAKFH-UHFFFAOYSA-N Cu2+ Chemical compound [Cu+2] JPVYNHNXODAKFH-UHFFFAOYSA-N 0.000 description 1
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- PFRUBEOIWWEFOL-UHFFFAOYSA-N [N].[S] Chemical compound [N].[S] PFRUBEOIWWEFOL-UHFFFAOYSA-N 0.000 description 1
- 229910001431 copper ion Inorganic materials 0.000 description 1
- BWFPGXWASODCHM-UHFFFAOYSA-N copper monosulfide Chemical class [Cu]=S BWFPGXWASODCHM-UHFFFAOYSA-N 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- ZOOODBUHSVUZEM-UHFFFAOYSA-N ethoxymethanedithioic acid Chemical compound CCOC(S)=S ZOOODBUHSVUZEM-UHFFFAOYSA-N 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 238000003306 harvesting Methods 0.000 description 1
- 239000012991 xanthate Substances 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
Landscapes
- Treatment Of Sludge (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Manufacture And Refinement Of Metals (AREA)
Abstract
Description
一、技术领域1. Technical field
本发明涉及一种砷黝铜矿捕收剂的制备方法,特别是针对砷黝铜矿的捕收剂的制备方法。The invention relates to a method for preparing a collector for arsenite tetrahedrite, in particular to a method for preparing a collector for arsenite tetrahedrite.
二、背景技术2. Background technology
目前国内外硫化铜的浮选回收一般都是采用硫酸或硫酸铜先活化,然后加黄药、黑药、硫氮等进行浮选捕收,硫化矿的浮选回收率在85~92%之间,捕收效果较为理想。但是当回收矿物为砷黝铜矿时,再采用以上捕收剂则效果不明显,其原因在于:一方面,砷黝铜矿可浮性不如其它硫化铜好;另一方面,由于砷离子较铜离子易氧化,影响其可浮性;再次,砷黝铜矿中有少量锌、铁离子以类质同象存在影响其可浮性。如何制备砷黝铜矿的选择性捕收剂以提高砷黝铜矿的回收率一直是国内外选矿界比较关注的问题。At present, the flotation recovery of copper sulfide at home and abroad is generally activated by sulfuric acid or copper sulfate, and then the flotation is collected by adding xanthate, black medicine, sulfur nitrogen, etc. The flotation recovery rate of sulfide ore is between 85% and 92%. , the harvesting effect is ideal. However, when the recovered mineral is arsenite, the effect of using the above collectors is not obvious. The reason is that: on the one hand, the buoyancy of arsenite is not as good as that of other copper sulfides; Copper ions are easily oxidized, which affects its buoyancy; thirdly, a small amount of zinc and iron ions in arsenite tetrahedrite exist in the same quality and shape, which affects its buoyability. How to prepare selective collectors for arsenite tetrahedrite to increase the recovery rate of arsenite tetrahedrite has always been a concern in the mineral processing circles at home and abroad.
三、发明内容3. Contents of the invention
本发明的目的在于提供一种砷黝铜矿捕收剂的制备方法,用该方法制备得的捕收剂能够在加少量硫酸铜活化的条件下实现砷黝铜矿高效浮选回收。The object of the present invention is to provide a preparation method of arsenite tetrahedrite collector. The collector prepared by the method can realize efficient flotation recovery of arsenite tetrahedrite under the condition of adding a small amount of copper sulfate for activation.
本发明采用以下技术方案实现上述目的:一种砷黝铜矿捕收剂的制备方法,包括如下步骤:首先将硫化钠、氢氧化钠和水按质量比硫化钠:氢氧化钠:水=1~2:1~2:2~5混合得溶液1,然后将25~30%的脂肪醇聚氧乙烯醚硫酸钠按质量比=1~2:3~7加入溶液1中,在温度70~75℃条件下搅拌至溶解得溶液2;然后将磷酸脂、发烟硫酸按质量比=1~2:1~3:3~7加入溶液2中,在2~3Mpa条件下反应得到的液体药剂即为所述砷黝铜矿捕收剂。The present invention adopts the following technical solutions to achieve the above object: a preparation method of arsenite tetrahedrite collector, comprising the steps of: first sodium sulfide, sodium hydroxide and water are mixed by mass ratio sodium sulfide: sodium hydroxide: water=1 ~2:1~2:2~5 were mixed to obtain solution 1, and then 25~30% fatty alcohol polyoxyethylene ether sodium sulfate was added to solution 1 according to the mass ratio = 1~2:3~7, at a temperature of 70~ Stir at 75°C until dissolved to obtain solution 2; then add phospholipids and oleum to solution 2 at a mass ratio of 1-2:1-3:3-7, and react under the condition of 2-3Mpa to obtain a liquid medicine It is the arsenite tetrahedrite collector.
浮选时,矿浆pH值为8.5~9;浮选过程中,将矿石磨矿至矿物单体解离后加入脉石抑制剂,然后加入活化剂,再加所述捕收剂,最后加起泡剂对砷黝铜矿进行捕收。During flotation, the pH value of the slurry is 8.5-9; during the flotation process, the ore is ground until the mineral monomers are dissociated, then the gangue inhibitor is added, then the activator is added, the collector is added, and finally Foaming agent to collect arsenite tetrahedrite.
捕收剂总用量为:80~100g/t。The total amount of collector is: 80~100g/t.
除另有说明外,本发明所述的百分比均为质量百分比,各组分含量百分数之和为100%。Unless otherwise specified, the percentages mentioned in the present invention are all mass percentages, and the sum of the content percentages of each component is 100%.
本发明的具体优点在于:Concrete advantages of the present invention are:
1、采用本发明制备得的捕收剂能够捕收砷黝铜矿,易溶于水,且具有良好的选择性及耐低温性能。1. The collector prepared by the present invention can collect arsenite, is easily soluble in water, and has good selectivity and low temperature resistance.
2、药剂用量少。2. The dosage of medicine is less.
四、具体实施方式4. Specific implementation
以下通过具体实施例对本发明的技术方案作进一步描述。The technical solutions of the present invention will be further described below through specific examples.
实施例1Example 1
本发明所述的砷黝铜矿捕收剂的制备方法的一个实例,包括以下步骤:An example of the preparation method of the arsenite tetrahedrite collector of the present invention comprises the following steps:
首先将硫化钠、氢氧化钠和水按质量比硫化钠:氢氧化钠:水=1:1:2混合得溶液1,然后将25%的脂肪醇聚氧乙烯醚硫酸钠按质量比=1:3加入溶液1中,在温度70℃条件下搅拌至溶解得溶液2;然后将磷酸脂、发烟硫酸按质量比=1:1:3加入溶液2中,在2Mpa条件下反应得到的液体药剂即为所述砷黝铜矿捕收剂。First sodium sulfide, sodium hydroxide and water are mixed by mass ratio sodium sulfide: sodium hydroxide: water=1:1:2 to obtain solution 1, then 25% fatty alcohol polyoxyethylene ether sodium sulfate is mixed by mass ratio=1 :3 is added to solution 1, stirred at a temperature of 70°C until dissolved to obtain solution 2; then phospholipids and oleum are added to solution 2 at a mass ratio of 1:1:3, and the resulting liquid is reacted under the condition of 2Mpa The agent is the arsenite tetrahedrite collector.
实施例2Example 2
本发明所述砷黝铜矿捕收剂的制备方法的另一个实例,包括以下步骤:Another example of the preparation method of the arsenite tetrahedrite collector of the present invention comprises the following steps:
首先将硫化钠、氢氧化钠和水按质量比硫化钠:氢氧化钠:水=2:2:5混合得溶液1,然后将30%的脂肪醇聚氧乙烯醚硫酸钠按质量比=2:7加入溶液1中,在温度75℃条件下搅拌至溶解得溶液2;然后将磷酸脂、发烟硫酸按质量比=2:3:7加入溶液2中,在3Mpa条件下反应得到的液体药剂即为所述砷黝铜矿捕收剂。First sodium sulfide, sodium hydroxide and water are mixed by mass ratio sodium sulfide: sodium hydroxide: water=2:2:5 to obtain solution 1, then 30% fatty alcohol polyoxyethylene ether sodium sulfate is mixed by mass ratio=2 :7 was added to solution 1, stirred at a temperature of 75°C until dissolved to obtain solution 2; then phospholipids and oleum were added to solution 2 in a mass ratio of 2:3:7, and the liquid obtained by reacting under the condition of 3Mpa The agent is the arsenite tetrahedrite collector.
实施例3Example 3
本实施例为所述砷黝铜矿捕收剂在浮选砷黝铜矿中的应用实例。This embodiment is an application example of the described arsenite collector in flotation of arsenite.
1、矿物原料:1. Mineral raw materials:
所用矿物原料硫化铜矿石,其中铜含量为5.23%、砷含量为1.07%、硫含量为7.92%、铁含量为3.10%,经物相分析表明,矿石中铜矿物以砷黝铜矿为主,另有少量黄铜矿、辉铜矿及孔雀石;脉石矿物主要有黄铁矿、磁黄铁矿、二氧化硅及碳酸盐的钙镁矿物。The copper sulfide ore used as the mineral raw material has a copper content of 5.23%, an arsenic content of 1.07%, a sulfur content of 7.92%, and an iron content of 3.10%. The phase analysis shows that the copper mineral in the ore is dominated by arsenite. Mainly, there are also a small amount of chalcopyrite, chalcocite and malachite; gangue minerals mainly include pyrite, pyrrhotite, silica and carbonate calcium magnesium minerals.
2、药剂制度及操作条件:将矿石磨矿至矿物单体解后加入石灰调矿浆pH到8.5~9,然后加腐殖酸钠800g/t作抑制剂,再加硫酸铜100g/t作活化剂,再加所述捕收剂80g/t,最后加起泡剂2#油70g/t对铜矿物进行捕收试验,结果表明采用以上药剂条件能够有效将砷黝铜矿高效浮选,在给矿铜含量5.23%条件下,经过一次粗选三次扫选及三次精选,得到含铜34.53%、回收率为91.21%浮选铜精矿。2. Chemical system and operating conditions: Grind the ore until the mineral monomers are decomposed, then add lime to adjust the pH of the slurry to 8.5-9, then add 800g/t sodium humate as an inhibitor, and then add 100g/t copper sulfate for activation agent, then add the collector agent 80g/t, and finally add foaming agent 2# oil 70g/t to carry out the collection test on copper minerals. Under the condition that the ore copper content is 5.23%, after one roughing, three times of sweeping and three times of beneficiation, a flotation copper concentrate with a copper content of 34.53% and a recovery rate of 91.21% is obtained.
实施例4Example 4
本实施例为所述的砷黝铜矿捕收剂浮在选砷黝铜矿中的另一应用实例。This embodiment is another application example of the arsenite collector floating in the arsenite extraction.
1、矿物原料:1. Mineral raw materials:
所用矿物原料硫化铜矿石,其中铜含量为7.35%、砷含量为1.56%、硫含量为8.24%、铁含量为5.16%,经物相分析表明,矿石中铜矿物以砷黝铜矿为主,另有少量黄铜矿、辉铜矿及孔雀石;脉石矿物主要有黄铁矿、磁黄铁矿、二氧化硅及碳酸盐的钙镁矿物。The copper sulfide ore used as the mineral raw material has a copper content of 7.35%, an arsenic content of 1.56%, a sulfur content of 8.24%, and an iron content of 5.16%. The phase analysis shows that the copper mineral in the ore is dominated by arsenite. Mainly, there are also a small amount of chalcopyrite, chalcocite and malachite; gangue minerals mainly include pyrite, pyrrhotite, silica and carbonate calcium magnesium minerals.
2、药剂制度及操作条件:将矿石磨矿至矿物单体解后加入石灰调矿浆pH到8.5~9,然后加腐殖酸钠800g/t作抑制剂,再加硫酸铜100g/t作活化剂,再加所述捕收剂100g/t,最后加起泡剂2#油70g/t对铜矿物进行捕收试验,结果表明采用以上药剂条件能够有效将砷黝铜矿高效浮选,在给矿铜含量7.35%条件下,经过一次粗选三次扫选及三次精选,得到含铜35.07%、回收率为92.16%浮选铜精矿。2. Chemical system and operating conditions: Grind the ore until the mineral monomers are decomposed, then add lime to adjust the pH of the slurry to 8.5-9, then add 800g/t sodium humate as an inhibitor, and then add 100g/t copper sulfate for activation agent, then add the collector agent 100g/t, and finally add foaming agent 2# oil 70g/t to carry out the collection test on copper minerals. Under the condition of feed copper content of 7.35%, after one roughing, three times of sweeping and three times of beneficiation, a flotation copper concentrate with a copper content of 35.07% and a recovery rate of 92.16% was obtained.
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CN109569892A (en) * | 2018-12-04 | 2019-04-05 | 林西金易来砷业有限公司 | A kind of composite inhibitor for copper arsenic mineral separating flotation |
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