CN111804439A - A kind of beneficiation method of carbon-containing lead-zinc sulfide ore - Google Patents
A kind of beneficiation method of carbon-containing lead-zinc sulfide ore Download PDFInfo
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- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 60
- 229910052799 carbon Inorganic materials 0.000 title claims abstract description 60
- JQJCSZOEVBFDKO-UHFFFAOYSA-N lead zinc Chemical compound [Zn].[Pb] JQJCSZOEVBFDKO-UHFFFAOYSA-N 0.000 title claims abstract description 27
- 238000000034 method Methods 0.000 title claims abstract description 26
- 239000005083 Zinc sulfide Substances 0.000 title claims abstract description 21
- 229910052984 zinc sulfide Inorganic materials 0.000 title claims abstract description 21
- 238000005188 flotation Methods 0.000 claims abstract description 38
- 239000003112 inhibitor Substances 0.000 claims abstract description 32
- 239000012141 concentrate Substances 0.000 claims abstract description 23
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 claims abstract description 22
- 229910052725 zinc Inorganic materials 0.000 claims abstract description 22
- 239000011701 zinc Substances 0.000 claims abstract description 22
- 229910052981 lead sulfide Inorganic materials 0.000 claims abstract description 6
- 229940056932 lead sulfide Drugs 0.000 claims abstract description 6
- 238000003756 stirring Methods 0.000 claims abstract description 4
- 239000004088 foaming agent Substances 0.000 claims abstract description 3
- 125000002057 carboxymethyl group Chemical group [H]OC(=O)C([H])([H])[*] 0.000 claims description 7
- 125000000542 sulfonic acid group Chemical group 0.000 claims description 7
- 235000008733 Citrus aurantifolia Nutrition 0.000 claims description 6
- 235000011941 Tilia x europaea Nutrition 0.000 claims description 6
- 239000004571 lime Substances 0.000 claims description 6
- 239000003795 chemical substances by application Substances 0.000 claims description 3
- 229910000365 copper sulfate Inorganic materials 0.000 claims description 3
- ARUVKPQLZAKDPS-UHFFFAOYSA-L copper(II) sulfate Chemical compound [Cu+2].[O-][S+2]([O-])([O-])[O-] ARUVKPQLZAKDPS-UHFFFAOYSA-L 0.000 claims description 3
- ZOOODBUHSVUZEM-UHFFFAOYSA-N ethoxymethanedithioic acid Chemical compound CCOC(S)=S ZOOODBUHSVUZEM-UHFFFAOYSA-N 0.000 claims description 3
- 239000012991 xanthate Substances 0.000 claims description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical group [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 2
- 125000004432 carbon atom Chemical group C* 0.000 claims description 2
- 229910052760 oxygen Inorganic materials 0.000 claims description 2
- 239000001301 oxygen Substances 0.000 claims description 2
- 230000002000 scavenging effect Effects 0.000 claims 2
- DRDVZXDWVBGGMH-UHFFFAOYSA-N zinc;sulfide Chemical compound [S-2].[Zn+2] DRDVZXDWVBGGMH-UHFFFAOYSA-N 0.000 claims 1
- 238000004513 sizing Methods 0.000 abstract description 6
- 239000012535 impurity Substances 0.000 abstract description 4
- 230000002401 inhibitory effect Effects 0.000 abstract description 2
- 238000004064 recycling Methods 0.000 abstract description 2
- 239000011133 lead Substances 0.000 description 22
- 239000002245 particle Substances 0.000 description 10
- 229910052500 inorganic mineral Inorganic materials 0.000 description 9
- 239000011707 mineral Substances 0.000 description 9
- 239000000243 solution Substances 0.000 description 8
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 6
- 239000003575 carbonaceous material Substances 0.000 description 5
- 238000001179 sorption measurement Methods 0.000 description 5
- 229940051841 polyoxyethylene ether Drugs 0.000 description 4
- 229920000056 polyoxyethylene ether Polymers 0.000 description 4
- 238000000926 separation method Methods 0.000 description 4
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- IGFHQQFPSIBGKE-UHFFFAOYSA-N Nonylphenol Natural products CCCCCCCCCC1=CC=C(O)C=C1 IGFHQQFPSIBGKE-UHFFFAOYSA-N 0.000 description 2
- 125000003118 aryl group Chemical group 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- UPHIPHFJVNKLMR-UHFFFAOYSA-N chromium iron Chemical compound [Cr].[Fe] UPHIPHFJVNKLMR-UHFFFAOYSA-N 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 229910052949 galena Inorganic materials 0.000 description 2
- XCAUINMIESBTBL-UHFFFAOYSA-N lead(ii) sulfide Chemical compound [Pb]=S XCAUINMIESBTBL-UHFFFAOYSA-N 0.000 description 2
- 229920005610 lignin Polymers 0.000 description 2
- 239000000693 micelle Substances 0.000 description 2
- SNQQPOLDUKLAAF-UHFFFAOYSA-N nonylphenol Chemical compound CCCCCCCCCC1=CC=CC=C1O SNQQPOLDUKLAAF-UHFFFAOYSA-N 0.000 description 2
- 230000001737 promoting effect Effects 0.000 description 2
- 239000002002 slurry Substances 0.000 description 2
- 229910052950 sphalerite Inorganic materials 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 229910021532 Calcite Inorganic materials 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 1
- 125000000129 anionic group Chemical group 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- LJSQFQKUNVCTIA-UHFFFAOYSA-N diethyl sulfide Chemical compound CCSCC LJSQFQKUNVCTIA-UHFFFAOYSA-N 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 229910000514 dolomite Inorganic materials 0.000 description 1
- 239000010459 dolomite Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- -1 ethyl thiazide Chemical class 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 230000005764 inhibitory process Effects 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 229910052683 pyrite Inorganic materials 0.000 description 1
- NIFIFKQPDTWWGU-UHFFFAOYSA-N pyrite Chemical compound [Fe+2].[S-][S-] NIFIFKQPDTWWGU-UHFFFAOYSA-N 0.000 description 1
- 239000011028 pyrite Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 229910052709 silver Inorganic materials 0.000 description 1
- 239000004332 silver Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 230000001629 suppression Effects 0.000 description 1
- 239000003451 thiazide diuretic agent Substances 0.000 description 1
- 239000011135 tin Substances 0.000 description 1
- 229910052718 tin Inorganic materials 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
- B03D1/001—Flotation agents
- B03D1/018—Mixtures of inorganic and organic compounds
-
- 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
- B03D2201/00—Specified effects produced by the flotation agents
- B03D2201/02—Collectors
-
- 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
- B03D2201/00—Specified effects produced by the flotation agents
- B03D2201/04—Frothers
-
- 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
- B03D2201/00—Specified effects produced by the flotation agents
- B03D2201/06—Depressants
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D2203/00—Specified materials treated by the flotation agents; Specified applications
- B03D2203/02—Ores
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- Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
Abstract
本发明公开了一种含碳硫化铅锌矿选矿方法,属于选矿技术领域,包括以下步骤:(1)对原矿进行磨矿,得到预定细度的矿浆;(2)向磨矿后的矿浆中加入碳抑制剂,搅拌均匀,得到调浆后的矿浆;(3)向调浆后的矿浆中加入捕收剂、起泡剂进行铅浮选,得到铅精矿和铅浮选尾矿;(4)向铅浮选尾矿中加入碳抑制剂,进行锌浮选,得到锌精矿和尾矿。本发明提供一种含碳硫化铅锌矿选矿方法,采用的抑制剂具有高选择性抑制作用,能够在硫化铅、锌浮选中高效选择抑制含碳杂质,便于实现硫化铅、锌的高效富集回收。
The invention discloses a method for beneficiation of carbon-containing lead-zinc sulfide ore, belonging to the technical field of beneficiation, comprising the following steps: (1) grinding raw ore to obtain ore pulp of predetermined fineness; Add carbon inhibitor, stir evenly, and obtain ore pulp after sizing; (3) add collector and foaming agent to the sizing pulp to carry out lead flotation to obtain lead concentrate and lead flotation tailings; ( 4) Adding carbon inhibitor to lead flotation tailings to carry out zinc flotation to obtain zinc concentrate and tailings. The invention provides a beneficiation method for carbon-containing lead-zinc sulfide ore. The inhibitor used has a high selective inhibitory effect, which can efficiently selectively inhibit carbon-containing impurities in the flotation of lead sulfide and zinc, so as to facilitate the realization of high-efficiency enrichment of lead sulfide and zinc. Set recycling.
Description
技术领域technical field
本发明属于选矿技术领域,涉及一种含碳硫化铅锌矿选矿方法。The invention belongs to the technical field of beneficiation, and relates to a beneficiation method for carbon-containing sulfide lead-zinc ore.
背景技术Background technique
硫化铅锌矿包含铅、锌、铜、银、硫和锡等多种金属,该矿矿石储量大,主要集中于云南、内蒙古、甘肃、广东、湖南和广西地区,其经济价值高,但矿物的嵌布粒度细,脉石中碳质含量较高,属难选矿石。The lead-zinc sulfide ore contains various metals such as lead, zinc, copper, silver, sulfur and tin. The mine has large ore reserves and is mainly concentrated in Yunnan, Inner Mongolia, Gansu, Guangdong, Hunan and Guangxi. Its economic value is high, but the mineral The inlaid particle size is fine, and the carbon content in the gangue is high, which is a refractory ore.
将有用矿物与脉石矿物分离,尤其是将目的矿物选择性分离是浮选的目的所在。在一些含碳质脉石型硫化铅锌矿矿床中,存在有一些密度较低,天然可浮性极强的碳质,在浮选过程中会进入泡沫层进而影响精矿品位。此外,这些碳质具有良好的吸附作用,会吸附矿浆中的浮选捕收剂,造成药剂消耗量增大,生产成本增加。探索研究硫化铅锌矿高效浮选方法,对促进硫化铅锌矿选矿技术进步,提高含碳硫化铅锌矿的资源利用水平具有重要意义。The purpose of flotation is to separate useful minerals from gangue minerals, especially to selectively separate target minerals. In some carbonaceous gangue-type lead-zinc sulfide deposits, there are some carbonaceous materials with low density and strong natural floatability, which will enter the foam layer during the flotation process and affect the concentrate grade. In addition, these carbonaceous materials have a good adsorption effect, which will adsorb the flotation collectors in the pulp, resulting in an increase in the consumption of chemicals and an increase in production costs. Exploring and studying the efficient flotation method of lead-zinc sulfide ore is of great significance for promoting the progress of beneficiation technology of lead-zinc sulfide ore and improving the resource utilization level of carbon-containing lead-zinc sulfide ore.
发明内容SUMMARY OF THE INVENTION
针对现有技术中“浮选硫化铅锌矿时含碳质脉石矿物较难抑制”的技术问题,本发明的目的在于提供一种含碳硫化铅锌矿选矿方法,以实现硫化铅锌矿和碳质脉石的分离。In view of the technical problem of "it is difficult to suppress carbonaceous gangue minerals during flotation of sulfide lead-zinc ore" in the prior art, the object of the present invention is to provide a beneficiation method for carbon-containing sulfide lead-zinc ore, so as to realize the sulfide lead-zinc ore and separation of carbonaceous gangue.
本发明提供一种含碳硫化铅锌矿选矿方法,包括以下步骤:The invention provides a beneficiation method for carbon-containing sulfide lead-zinc ore, comprising the following steps:
(1)对原矿进行磨矿,得到预定细度的矿浆;(1) Grinding the raw ore to obtain pulp with a predetermined fineness;
(2)向磨矿后的矿浆中加入碳抑制剂,搅拌均匀,得到调浆后的矿浆;(2) adding a carbon inhibitor to the ore pulp after grinding, stirring evenly, to obtain the ore pulp after sizing;
(3)向调浆后的矿浆中加入捕收剂、起泡剂进行铅浮选,得到铅精矿和铅浮选尾矿;(3) adding collector and foaming agent to the ore pulp after sizing to carry out lead flotation to obtain lead concentrate and lead flotation tailings;
(4)向铅浮选尾矿中加入碳抑制剂,进行锌浮选,得到锌精矿和尾矿;(4) adding a carbon inhibitor to the lead flotation tailings to carry out zinc flotation to obtain zinc concentrate and tailings;
所述碳抑制剂的结构式如下:The structural formula of the carbon inhibitor is as follows:
其中,R为含氧的亲水基团,n的值取4~10。Among them, R is an oxygen-containing hydrophilic group, and the value of n is 4-10.
优选的方案,R基团上C原子数为0~2。In a preferred scheme, the number of C atoms on the R group is 0-2.
优选的方案,R为磺酸基、羧甲基中的任意一种。In a preferred scheme, R is any one of sulfonic acid group and carboxymethyl group.
优选的方案,该碳抑制剂具有如下结构式中的一种或多种:A preferred scheme, the carbon inhibitor has one or more of the following structural formulas:
本发明提供的碳抑制剂,以壬基苯酚为亲碳基团,以聚氧乙烯醚和磺酸基/羧甲基为亲水基团,含碳质硫化铅锌矿浮选时,通过该抑制剂的使用,可以有效抑制碳的浮选,减少了碳杂质对捕收剂的消耗,降低精矿产品中碳含量,有利于提高精矿的选矿指标。In the carbon inhibitor provided by the invention, nonylphenol is used as the carbon-philic group, and polyoxyethylene ether and sulfonic acid group/carboxymethyl group are used as the hydrophilic group. During the flotation of carbonaceous lead-zinc sulfide ores, the The use of the inhibitor can effectively inhibit the flotation of carbon, reduce the consumption of carbon impurities on the collector, reduce the carbon content in the concentrate product, and help improve the beneficiation index of the concentrate.
优选的方案,步骤(1)中,将原矿磨至-0.074mm占80%以上。In a preferred solution, in step (1), the raw ore is ground to -0.074mm, accounting for more than 80%.
优选的方案,步骤(2)中,加入碳抑制剂50~150g/t,石灰3000~4000g/t,搅拌1~5min,得到调浆后的矿浆。In a preferred scheme, in step (2), 50-150 g/t of carbon inhibitor and 3,000-4,000 g/t of lime are added, and stirred for 1-5 minutes to obtain slurried pulp.
更优选的方案,所述的碳抑制剂的用量为50~100g/t。In a more preferred solution, the amount of the carbon inhibitor used is 50-100 g/t.
优选的方案,步骤(3)中,加入混合捕收剂50~60g/t与2号油20~40g/t进行铅粗选,浮选铅粗精矿经过两次精选得到铅精矿,经一次扫选得到铅浮选尾矿。In a preferred solution, in step (3), 50-60 g/t of mixed collector and 20-40 g/t of No. 2 oil are added to carry out lead rough separation, and lead concentrate is obtained by flotation of lead rough concentrate after two beneficiations, Lead flotation tailings are obtained after one sweep.
更优选的方案,采用质量比为乙硫氮:黄药=1:1作为混合捕收剂。A more preferred solution adopts a mass ratio of ethyl thiazide: xanthate=1:1 as the mixed collector.
优选的方案,步骤(4)中,铅浮选尾矿中加入碳抑制剂50~100g/t,石灰500~1500g/t,硫酸铜100~200g/t,混合捕收剂10~30g/t,2号油5~20g/t,经过一次粗选,两次精选,一次扫选,得到锌精矿和尾矿。In a preferred solution, in step (4), 50-100 g/t carbon inhibitor, 500-1500 g/t lime, 100-200 g/t copper sulfate, and 10-30 g/t mixed collector are added to the lead flotation tailings , No. 2 oil 5 ~ 20g/t, after a roughing, two selection, a sweep to get zinc concentrate and tailings.
本发明中所述的“g/t”是指药剂相对于原矿的添加量,如碳抑制剂的用量是100g/t,是指处理一吨原矿需要加入碳抑制剂100g。The "g/t" mentioned in the present invention refers to the addition amount of the agent relative to the raw ore. For example, the dosage of carbon inhibitor is 100g/t, which means that 100g of carbon inhibitor needs to be added to treat one ton of raw ore.
本发明所设计的碳抑制剂,碳质表面主要由芳香环构成,该抑制剂的亲碳基团为壬基苯酚的分子大平面结构,可与脉石中碳质表面的芳香基通过π-π堆积作用相互吸引而“锚固”于其表面;壬基苯酚-聚氧乙烯醚结构连接磺酸基/羧甲基,使整个分子在形成胶束时,自发的形成一个“空穴集团”将碳质包裹在内胶束层或形成亲水链覆盖在碳质表面。The carbon inhibitor designed in the present invention, the carbonaceous surface is mainly composed of aromatic rings, and the carbon-philic group of the inhibitor is the molecular large plane structure of nonylphenol, which can interact with the aromatic group on the carbonaceous surface in the gangue through π- The π stacking interaction attracts each other and is "anchored" on its surface; the nonylphenol-polyoxyethylene ether structure connects the sulfonic acid group/carboxymethyl group, so that when the whole molecule forms a micelle, a "hole group" will be formed spontaneously. The carbonaceous material is wrapped in the inner micelle layer or forms a hydrophilic chain covering the carbonaceous surface.
当抑制剂吸附于碳质表面后,抑制剂中磺酸基/羧甲基的电离使得碳质颗粒带上负电荷,在颗粒周围形成扩散双电层。当两个带有相同电荷的碳质颗粒相互靠近时,扩散双电层重叠产生的静电斥力迫使带电的碳质颗粒相互分开,阻止了其合并,促进了碳质在矿浆中的分散。此外碳质表面荷负电也可以有效通过静电斥力阻碍阴离子捕收剂在碳表面的吸附,从而增强对碳质颗粒的抑制作用。When the inhibitor is adsorbed on the carbonaceous surface, the ionization of the sulfonic acid group/carboxymethyl group in the inhibitor makes the carbonaceous particles negatively charged, forming a diffusion electric double layer around the particles. When two carbonaceous particles with the same charge approach each other, the electrostatic repulsion generated by the overlapping of the diffused electric double layer forces the charged carbonaceous particles to separate from each other, preventing them from merging and promoting the dispersion of carbonaceous in the slurry. In addition, the negative charge on the carbonaceous surface can also effectively hinder the adsorption of anionic collectors on the carbon surface through electrostatic repulsion, thereby enhancing the inhibition effect on carbonaceous particles.
与现有技术相比,本发明技术方案带来的有益效果:Compared with the prior art, the beneficial effects brought by the technical solution of the present invention:
本发明提供一种含碳硫化铅锌矿选矿方法,采用的碳抑制剂结构中拥有的亲水性的聚氧乙烯醚和磺酸基/羧甲基,当碳质颗粒表面吸附该类抑制剂后,聚氧乙烯醚连同磺酸基/羧甲基这端会伸展进入水溶液中,从而在所吸附的碳质颗粒表面形成有一定厚度的亲水性立体吸附层。当碳颗粒相互靠近时,吸附层开始重叠,即在碳质颗粒间产生空间位阻作用,重叠越多,空间位阻斥力越大,对碳质颗粒间凝聚作用的阻碍也越大,从而使得矿浆溶液中碳质得到很好的分散。同时由于这一层稳定的溶剂化水膜,不但具有极大的位阻斥力而且还具有极强的亲水性,这使得捕收剂更难以接近碳质表面。这即保证了碳质杂质的充分抑制,又大大降低了因碳质吸附所引起的捕收剂消耗。The invention provides a beneficiation method for carbon-containing lead-zinc sulfide ore, which adopts the hydrophilic polyoxyethylene ether and sulfonic acid group/carboxymethyl group in the carbon inhibitor structure, and when the surface of carbonaceous particles adsorbs such inhibitors Afterwards, the polyoxyethylene ether and the sulfonic acid group/carboxymethyl end will extend into the aqueous solution, thereby forming a hydrophilic three-dimensional adsorption layer with a certain thickness on the surface of the adsorbed carbonaceous particles. When the carbon particles are close to each other, the adsorption layers begin to overlap, that is, steric hindrance occurs between the carbonaceous particles. The carbon in the slurry solution is well dispersed. At the same time, due to this layer of stable solvated water film, it not only has great steric repulsion but also has strong hydrophilicity, which makes it more difficult for collectors to approach the carbonaceous surface. This not only ensures sufficient suppression of carbonaceous impurities, but also greatly reduces the consumption of collectors caused by carbonaceous adsorption.
本发明提供一种含碳硫化铅锌矿选矿方法,采用的抑制剂具有高选择性抑制作用,能够在硫化铅、锌浮选中高效选择抑制含碳杂质,便于实现硫化铅、锌的高效富集回收。The invention provides a method for beneficiation of carbon-containing lead-zinc sulfide ore. The inhibitor used has a high selective inhibitory effect, which can efficiently selectively inhibit carbon-containing impurities in the flotation of lead sulfide and zinc, so as to facilitate the realization of high-efficiency enrichment of lead sulfide and zinc. Set recycling.
附图说明Description of drawings
图1为本发明实施例1浮选方法的工艺流程图。FIG. 1 is a process flow diagram of the flotation method in Embodiment 1 of the present invention.
具体实施方式Detailed ways
下面将对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅是本发明一部分实施例,而不是全部实施例,基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。The technical solutions in the embodiments of the present invention will be clearly and completely described below. Obviously, the described embodiments are only a part of the embodiments of the present invention, rather than all the embodiments. Based on the embodiments of the present invention, ordinary skills in the art All other embodiments obtained by personnel without creative work fall within the protection scope of the present invention.
下面结合附图和具体实施例对本发明进一步说明。The present invention will be further described below with reference to the accompanying drawings and specific embodiments.
实施例1-3Examples 1-3
采用内蒙某含碳铅锌矿,其中主要金属矿物为闪锌矿、方铅矿和黄铁矿,其中锌品位为5.28%,铅品位为2.23%,铁品位为8.3%。其余金属矿物含量较低。脉石矿物主要为白云石、方解石和有机碳等。矿石中含碳量达4.75%。矿石性质复杂,铅锌共生关系紧密,有用矿物铅、锌与碳质关系密切,矿石中含有大量有机碳。这些碳质可浮性很好,如果浮选过程中直接对铅和锌进行浮选,碳质势必进入铅精矿和锌精矿而影响精矿品位,故解决该矿石浮选的关键在于有效分离方铅矿、闪锌矿与有机碳。A carbon-bearing lead-zinc ore in Inner Mongolia is used. The main metal minerals are sphalerite, galena and pyrite, of which the zinc grade is 5.28%, the lead grade is 2.23%, and the iron grade is 8.3%. The content of other metal minerals is lower. Gangue minerals are mainly dolomite, calcite and organic carbon. The carbon content in the ore reaches 4.75%. The nature of the ore is complex, the symbiotic relationship between lead and zinc is close, and the useful minerals lead, zinc and carbon are closely related, and the ore contains a lot of organic carbon. These carbonaceous materials have good floatability. If lead and zinc are directly flotated during the flotation process, the carbonaceous materials will inevitably enter the lead concentrate and zinc concentrate and affect the concentrate grade. Therefore, the key to solving the flotation of this ore is effective Separation of galena, sphalerite and organic carbon.
本发明一种含碳硫化铅锌矿选矿方法,如图1所示,包括以下步骤:A kind of beneficiation method for carbon-containing sulfide lead-zinc ore of the present invention, as shown in Figure 1, comprises the following steps:
(1)磨矿:将原矿进行磨矿,磨至-0.074mm占85%的细度;(1) Grinding: grinding the raw ore to a fineness of -0.074mm accounting for 85%;
(2)调浆:加入碳抑制剂100g/t,石灰3500g/t,搅拌3min,得到调浆后的矿浆;(2) Sizing: adding carbon inhibitor 100g/t, lime 3500g/t, stirring for 3min, to obtain ore pulp after sizing;
(3)铅浮选:加入混合捕收剂(乙硫氮:黄药=1:1)55g/t与2号油起泡剂30g/t进行铅粗选;浮选铅粗精矿经过两次精选得到铅精矿;经一次扫选得到铅浮选尾矿;(3) Lead flotation: add 55g/t mixed collector (ethyl sulfide: xanthate = 1:1) and No. 2 oil frother 30g/t for lead roughing; flotation of rough lead concentrate after two The lead concentrate is obtained by the second selection; the lead flotation tailings are obtained by the first sweep;
(4)锌浮选:铅浮选尾矿中加入碳抑制剂50g/t,石灰1000g/t,硫酸铜150g/t,混合捕收剂20g/t,2号油10g/t经过一次粗选,两次精选,一次扫选,得到锌精矿和尾矿。(4) Zinc flotation: add carbon inhibitor 50g/t, lime 1000g/t, copper sulfate 150g/t, mixed collector 20g/t, and No. 2 oil 10g/t to the lead flotation tailings after a rough separation , two selections and one sweep to obtain zinc concentrates and tailings.
对比例1Comparative Example 1
采用常规铁铬盐木质素作为碳抑制剂,按照以上流程和药剂用量,通过浮选试验得到的浮选结果列于表1。Using conventional iron-chromium salt lignin as carbon inhibitor, according to the above process and dosage of chemicals, the flotation results obtained by flotation test are listed in Table 1.
表1浮选结果Table 1 Flotation results
由表1可知,同采用常规铁铬盐木质素相比,铅精矿和锌精矿品位和回收率都较高,可见采用该高效抑制剂能够很好的抑制碳的上浮,有利于硫化铅锌矿的浮选捕收。It can be seen from Table 1 that compared with the use of conventional iron-chromium salt lignin, the grades and recovery rates of lead concentrate and zinc concentrate are higher. It can be seen that the use of this high-efficiency inhibitor can well suppress the floating of carbon, which is beneficial to lead sulfide. Flotation capture of zinc ore.
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