CN116393258B - 一种金红石的高效浮选方法 - Google Patents
一种金红石的高效浮选方法 Download PDFInfo
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- GWEVSGVZZGPLCZ-UHFFFAOYSA-N titanium dioxide Inorganic materials O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 title claims abstract description 96
- 238000005188 flotation Methods 0.000 title claims abstract description 71
- 238000000034 method Methods 0.000 title claims abstract description 29
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonia chloride Chemical compound [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 claims abstract description 40
- OWBTYPJTUOEWEK-UHFFFAOYSA-N butane-2,3-diol Chemical compound CC(O)C(C)O OWBTYPJTUOEWEK-UHFFFAOYSA-N 0.000 claims abstract description 24
- LMBWSYZSUOEYSN-UHFFFAOYSA-N diethyldithiocarbamic acid Chemical compound CCN(CC)C(S)=S LMBWSYZSUOEYSN-UHFFFAOYSA-N 0.000 claims abstract description 21
- 229950004394 ditiocarb Drugs 0.000 claims abstract description 21
- 235000019270 ammonium chloride Nutrition 0.000 claims abstract description 20
- WDIHJSXYQDMJHN-UHFFFAOYSA-L barium chloride Chemical compound [Cl-].[Cl-].[Ba+2] WDIHJSXYQDMJHN-UHFFFAOYSA-L 0.000 claims abstract description 17
- 229910001626 barium chloride Inorganic materials 0.000 claims abstract description 17
- 230000008569 process Effects 0.000 claims abstract description 16
- 239000003112 inhibitor Substances 0.000 claims abstract description 10
- 239000002131 composite material Substances 0.000 claims abstract description 7
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical group [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 claims abstract description 7
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 6
- 239000000203 mixture Substances 0.000 claims abstract description 6
- 238000000227 grinding Methods 0.000 claims abstract description 5
- 239000004115 Sodium Silicate Substances 0.000 claims abstract 2
- IOEJYZSZYUROLN-UHFFFAOYSA-M Sodium diethyldithiocarbamate Chemical compound [Na+].CCN(CC)C([S-])=S IOEJYZSZYUROLN-UHFFFAOYSA-M 0.000 claims abstract 2
- 230000003213 activating effect Effects 0.000 claims abstract 2
- 229910052911 sodium silicate Inorganic materials 0.000 claims abstract 2
- 239000012190 activator Substances 0.000 claims description 11
- 238000001994 activation Methods 0.000 claims description 5
- 230000004913 activation Effects 0.000 claims description 3
- 230000009471 action Effects 0.000 claims description 2
- 238000011084 recovery Methods 0.000 abstract description 21
- 239000003153 chemical reaction reagent Substances 0.000 abstract description 2
- 230000002195 synergetic effect Effects 0.000 abstract description 2
- 238000012360 testing method Methods 0.000 description 18
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 13
- 229910052500 inorganic mineral Inorganic materials 0.000 description 13
- 239000011707 mineral Substances 0.000 description 13
- 230000000694 effects Effects 0.000 description 12
- 229910010413 TiO 2 Inorganic materials 0.000 description 10
- 229910052719 titanium Inorganic materials 0.000 description 10
- -1 wherein Chemical compound 0.000 description 10
- 239000012141 concentrate Substances 0.000 description 9
- 229910001422 barium ion Inorganic materials 0.000 description 8
- 238000001179 sorption measurement Methods 0.000 description 8
- 239000010936 titanium Substances 0.000 description 6
- 238000002474 experimental method Methods 0.000 description 5
- 235000019353 potassium silicate Nutrition 0.000 description 5
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- 238000002156 mixing Methods 0.000 description 4
- 238000000926 separation method Methods 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical group [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 239000002253 acid Substances 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 3
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- 150000002500 ions Chemical class 0.000 description 3
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- 229910052751 metal Inorganic materials 0.000 description 3
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- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 3
- 239000004408 titanium dioxide Substances 0.000 description 3
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 3
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- TZCXTZWJZNENPQ-UHFFFAOYSA-L barium sulfate Chemical compound [Ba+2].[O-]S([O-])(=O)=O TZCXTZWJZNENPQ-UHFFFAOYSA-L 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 229910001919 chlorite Inorganic materials 0.000 description 2
- 229910052619 chlorite group Inorganic materials 0.000 description 2
- QBWCMBCROVPCKQ-UHFFFAOYSA-N chlorous acid Chemical compound OCl=O QBWCMBCROVPCKQ-UHFFFAOYSA-N 0.000 description 2
- 229910052802 copper Inorganic materials 0.000 description 2
- 239000010949 copper Substances 0.000 description 2
- 239000010433 feldspar Substances 0.000 description 2
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 2
- 230000003993 interaction Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 229910021645 metal ion Inorganic materials 0.000 description 2
- 239000010445 mica Substances 0.000 description 2
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- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- NIFIFKQPDTWWGU-UHFFFAOYSA-N pyrite Chemical compound [Fe+2].[S-][S-] NIFIFKQPDTWWGU-UHFFFAOYSA-N 0.000 description 2
- 229910052683 pyrite Inorganic materials 0.000 description 2
- 239000011028 pyrite Substances 0.000 description 2
- 239000002002 slurry Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- JPVYNHNXODAKFH-UHFFFAOYSA-N Cu2+ Chemical compound [Cu+2] JPVYNHNXODAKFH-UHFFFAOYSA-N 0.000 description 1
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 description 1
- 238000003723 Smelting Methods 0.000 description 1
- LCKIEQZJEYYRIY-UHFFFAOYSA-N Titanium ion Chemical compound [Ti+4] LCKIEQZJEYYRIY-UHFFFAOYSA-N 0.000 description 1
- 229910052612 amphibole Inorganic materials 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 229910001431 copper ion Inorganic materials 0.000 description 1
- 239000008367 deionised water Substances 0.000 description 1
- 229910021641 deionized water Inorganic materials 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- 125000004177 diethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
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- 239000000194 fatty acid Substances 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
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- 239000006260 foam Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000000383 hazardous chemical Substances 0.000 description 1
- 229910001608 iron mineral Inorganic materials 0.000 description 1
- SZVJSHCCFOBDDC-UHFFFAOYSA-N iron(II,III) oxide Inorganic materials O=[Fe]O[Fe]O[Fe]=O SZVJSHCCFOBDDC-UHFFFAOYSA-N 0.000 description 1
- YDZQQRWRVYGNER-UHFFFAOYSA-N iron;titanium;trihydrate Chemical compound O.O.O.[Ti].[Fe] YDZQQRWRVYGNER-UHFFFAOYSA-N 0.000 description 1
- RLJMLMKIBZAXJO-UHFFFAOYSA-N lead nitrate Chemical compound [O-][N+](=O)O[Pb]O[N+]([O-])=O RLJMLMKIBZAXJO-UHFFFAOYSA-N 0.000 description 1
- RVPVRDXYQKGNMQ-UHFFFAOYSA-N lead(2+) Chemical compound [Pb+2] RVPVRDXYQKGNMQ-UHFFFAOYSA-N 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 231100000956 nontoxicity Toxicity 0.000 description 1
- 229910052592 oxide mineral Inorganic materials 0.000 description 1
- SPBQTHJZZJMBJO-UHFFFAOYSA-N phenylmethoxyarsonic acid Chemical compound C(C1=CC=CC=C1)O[As](O)(O)=O SPBQTHJZZJMBJO-UHFFFAOYSA-N 0.000 description 1
- ABLZXFCXXLZCGV-UHFFFAOYSA-N phosphonic acid group Chemical group P(O)(O)=O ABLZXFCXXLZCGV-UHFFFAOYSA-N 0.000 description 1
- YVURAEQQLUQPFO-UHFFFAOYSA-N phosphoric acid;styrene Chemical compound OP(O)(O)=O.C=CC1=CC=CC=C1 YVURAEQQLUQPFO-UHFFFAOYSA-N 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 229910052952 pyrrhotite Inorganic materials 0.000 description 1
- 229910052604 silicate mineral Inorganic materials 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
- GCLGEJMYGQKIIW-UHFFFAOYSA-H sodium hexametaphosphate Chemical compound [Na]OP1(=O)OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])O1 GCLGEJMYGQKIIW-UHFFFAOYSA-H 0.000 description 1
- 235000019982 sodium hexametaphosphate Nutrition 0.000 description 1
- AWAJFEHOZQSMMS-UHFFFAOYSA-M sodium;carbamothioate Chemical group [Na+].NC([O-])=S AWAJFEHOZQSMMS-UHFFFAOYSA-M 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
- 239000000454 talc Substances 0.000 description 1
- 229910052623 talc Inorganic materials 0.000 description 1
- 239000008399 tap water Substances 0.000 description 1
- 235000020679 tap water Nutrition 0.000 description 1
- 239000001577 tetrasodium phosphonato phosphate Substances 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
- 238000005406 washing Methods 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
- B03D1/001—Flotation agents
- B03D1/018—Mixtures of inorganic and organic compounds
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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
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C1/00—Magnetic separation
- B03C1/02—Magnetic separation acting directly on the substance being separated
- B03C1/30—Combinations with other devices, not otherwise provided for
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- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
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- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
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- B03D2201/02—Collectors
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- B03D2203/02—Ores
- B03D2203/025—Precious metal ores
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Abstract
本发明公开一种金红石的高效浮选方法,将金红石破碎磨矿至‑74+45μm,以氯化钡和氯化铵的混合物为活化剂来活化金红石,然后加入复合捕收剂,抑制剂,进行一粗一扫三精浮选流程;所述复合捕收剂由2.3‑丁二醇、二乙基二硫代氨基甲酸钠组成,抑制剂为水玻璃;其中,2.3‑丁二醇含量为20‑70%,二乙基二硫代氨基甲酸钠30‑80%;本发明以氯化钡和氯化铵的组合药剂对金红石的浮选回收具有明显的协同效应;氯化钡和氯化铵的组合药剂离子在金红石表面生成的缔合物可以提高金红石回收率。
Description
技术领域
本发明涉及一种金红石的高效浮选方法,属于选矿技术领域。
背景技术
金属钛广泛用于飞机、火车等工业产品;目前金属钛的主要来源为金红石,且其是含钛量最高的矿物;在我国的金红石矿石中,大多存在粒度细,成分复杂等特点;在实际矿物浮选中,矿物表面溶解、循环用水等因素会使浮选矿浆存有不同价态的金属离子,会对浮选分离效果产生影响。
现有的浮选技术主要采用铜、铅离子作为活化剂,但铜离子、铅离子在金红石表面吸附后,会影响后续的冶炼制造钛白粉的工艺;现有金红石的浮选捕收剂主要是苯乙烯磷酸、苯甲基砷酸这两种环境危害大的有一定毒性的捕收剂,而且药剂的售价很高。
发明内容
本发明的目的在于提供一种金红石的高效浮选方法,具体包括以下步骤:将金红石破碎磨矿至-74+45μm,以氯化钡和氯化铵的混合物为活化剂来活化金红石,然后加入复合捕收剂、抑制剂,进行一粗一扫三精浮选;所述复合捕收剂由2.3-丁二醇、二乙基二硫代氨基甲酸钠组成,抑制剂为水玻璃,其中,2.3-丁二醇含量为20-70%,二乙基二硫代氨基甲酸钠30-80%。
优选的,本发明所述将金红石破碎磨矿至-74+45μm。
优选的,本发明所述活化过程中pH值为4~7。
优选的,本发明所述活化剂中氯化钡和氯化铵的质量比为1:1~3:1。
优选的,本发明所述活化剂的加入量为30-100g/t,活化时间为2-5min。
优选的,本发明所述混合捕收剂用量50-200g/t,作用时间3分钟,温度23-25℃。
金红石是一种氧化物矿物,比较稳定,但是对捕收剂的特异性很弱,本发明在金红石矿物表面添加特定的金属离子使其容易和捕收剂进行强吸附,增加其表面的疏水性,便于浮选分离。
本发明采用钡离子、氯化铵复配活化剂,活化剂的用量比铜、铅离子单独作用的用量降低30%;钡离子在金红石表面吸附,形成多金属离子表面,为捕收剂的吸附提供了更多的吸附位点;氯化铵的铵离子可以和钛原子配位,给钛原子提供多余电子,强化了钛原子和捕收剂的化学键合,从而提高了捕收剂的作用强度;此外,钡离子在后续酸法制取钛白粉的过程中,很容易形成硫酸钡沉淀,从而从酸液中去除,不影响钛白粉的制造过程,所以本发明使用的活化剂有突出优势。
本发明对通过钡离子活化的金红石直接采用二乙基二硫代氨基甲酸钠作为捕收剂,该捕收剂没有毒性,而且售价低,可以在矿山推广使用,同时使用2.3-丁二醇可以和二乙基二硫代氨基甲酸钠共吸附在金红石表面,其中2.3-丁二醇可以形成侨联式吸附结构,提高金红石表面的疏水性,可以减少捕收剂二乙基二硫代氨基甲酸钠的用量。
本发明的有益效果
(1)氯化钡和氯化铵的组合药剂对金红石的浮选回收具有明显的协同效应;氯化钡和氯化铵的组合药剂离子在金红石表面生成的缔合物可以提高金红石回收率;氯化钡加入到矿浆后,钡离子和金红石作用后,和金红石表面负电荷的氧离子反应,形成O-Ba产物,由于捕收剂可以和Ba离子成键,所以钡离子的加入就增加了金红石表面捕收剂的吸附位点,有利于捕收剂作用;氯化铵在溶液中解离出铵离子,铵离子可以和金红石表面的钛原子反应,形成络合物,并给予钛离子电子,从而强化钛离子和捕收剂的作用,也有利于捕收剂的吸附,从而提高金红石的浮选效率。
(2)与单一捕收剂相比,混合表面捕收剂具有更高的浮选选择性和更高的精矿回收率,同时减少了药剂消耗,大大降低了浮选成本;混合捕收剂中二乙基二硫代氨基甲酸钠只可以和金红石表面的一个钛原子作用,而吸附在金红石表面,加入部分2、3-丁二醇后,2、3-丁二醇中的两个羟基可以和金红石表面相连的两个钛原子键合,并由于键合减弱,不影响钛原子和二乙基二硫代氨基甲酸钠的作用,所以可以共吸附在金红石表面,从而充分提高金红石表面的疏水性;相较于单一的2.3-丁二醇和二乙基二硫代氨基甲酸钠,回收率分别提高10%、12%。
(3)本发明可以在常温和短时间内就能实现金红石高效浮选,得到更高的精矿回收率,减少药剂用量,在提高资源利用率的同时提高指标,增加效益,保护环境。
具体实施方式
下面结合具体实施例本发明作进一步的详细说明,但本发明的保护范围并不限于所述内容。
本发明实施例中所用金红石为云南某地的风化金红石,主要脉石矿物为石英、硅酸盐等;筛取38~74μm粒级产品用于试验,具体包括以下步骤:
(1)浮选试验采用XFGII型浮选机和40ml浮选槽进行;量取20mL的自来水加入到槽体容积为35mL的浮选槽中,矿样采用-74μm金红石,矿浆质量浓度为10%;每次试验取2g金红石加入浮选槽,加适量去离子水至固定液面,调整浮选机转速为1992r/min,搅拌2min,然后加入pH调整剂调节矿浆pH至6.5,pH调整剂为NaOH和HCl,搅拌2min。
(2)先用氯化钡和氯化铵(混合比例3:1)对金红石矿浆进行预处理3min,再加入混合捕收剂,其中复合捕收剂由2.3-丁二醇、二乙基二硫代氨基甲酸钠组成,2.3-丁二醇含量为20-70%,二乙基二硫代氨基甲酸钠30-80%;2.3-丁二醇和二乙基二硫代氨基甲酸钠的加入方式为分别依次加入,调节时间分别为3min和1min,加入抑制剂水玻璃,进行一粗一扫三精的浮选流程,浮选时间控制在1min。
(3)分别对浮选泡沫产品和槽内产品进行烘干、称重,计算浮选回收率,每次试验进行3次,取平3次的均值,得TiO2品位88.74%,金红石回收率为91.21%。
表1
通过表1可以看出,不使用活化剂浮选效果减弱;如果只用氯化铵活化,浮选金红石回收率降低,主要是因为少了Ba离子与捕收剂成键,金红石表面捕收剂的吸附位点变少;如果只用氯化钡活化,浮选金红石回收率降低,原因是相比实施例1,少了氯化铵在溶液中溶解出的铵离子与金红石表面的钛原子反应,钛离子和捕收剂间的作用效果减弱;加入活化剂以后,如果只加2.3-丁二醇浮选效果减弱,原因是相比实施例1,捕收剂与金红石表面钛原子间的作用效果减弱。如果只加只加二乙基二硫代氨基甲酸钠浮选效果大幅减弱,原因相比实施例1,没有了2.3丁二醇中羟基与金红石表面钛原子的键合,不能实现实施例1中金红石表面疏水性提高的效果,从而降低了浮选效果。
通过上述实验可以看出,同时使用2.-3丁二醇可以和二乙基二硫代氨基甲酸钠共吸附在金红石表面,其中2.3-丁二醇可以形成侨联式吸附结构,提高金红石表面的疏水性,可以减少捕收剂二乙基二硫代氨基甲酸钠的用量;氯化钡和氯化铵可以与金红石表面发生有利于捕收剂吸附的反应,钡离子与金红石表面的负电荷氧离子反应,铵离子与金红石表面的钛离子反应,强化其与捕收剂的作用,加强浮选效果;氯化铵和氯化钡共同强化捕收剂的吸附作用,从而提高金红石浮选效率。
对比实施例6
山西某金红石矿中金属矿物组成简单,主要为金红石、钛铁矿、磁铁矿及少量黄铁矿、磁黄铁矿等;脉石矿物以闪石、滑石、绿泥石为主,其次为长石、石英、云母等。该试验的选矿原则工艺流程为两次浮选抛尾一金红石浮选(一次粗选、两次精选)一浮选精矿除杂(弱磁选一强磁选一重选)的选矿流程。此试验采用的金红石浮选捕收剂BK423为膦酸类捕收剂、硫酸为矿浆pH调整剂。硫酸的用量为1000g/t,矿浆pH为6;获得精矿1含TiO289.58%、TiO2回收率46.84%,精矿2含TiO280.53%、TiO2回收率22.41%,精矿1与精矿2合计TiO2回收率为69.25%,金红石回收率为86.42%。
采用本发明的方法对金红石进行浮选试验;具体方法为:浮选试验采用XFGII型浮选机和40ml浮选槽进行;每个实验使用2g金红石(-74+45μm);先用氯化钡和氯化铵(混合比例3:1,添加量为50g/t)对金红石矿浆进行预处理3min,再加入混合捕收剂(2.3-丁二醇含量30%,二乙基二硫代氨基甲酸钠50%,添加量为100g/t);2.3-丁二醇和二乙基二硫代氨基甲酸钠的的调节次数分别为3min和1min,加入抑制剂水玻璃,进行一粗一扫三精的浮选流程,浮选时间控制在1min;每次试验进行3次;得TiO2品位88.74%,金红石回收率91.25%。
对比实施例7
山东某金红石矿含TFe25.32%,TiO25.74%,脉石矿物主要有石英、长石、云母、绿泥石、黄铁矿等,金红石和脉石矿物的嵌镶关系复杂,粒度微细,主要呈半自形柱状、短柱状、层状不均冬嵌布在脉石矿物之间。原试验采用原矿直接浮选实验,矿石在-0.043mm粒级占65%的磨矿细度下,采用碳酸钠、硝酸铅、六偏磷酸钠作为调整剂,改性脂肪酸作为捕收剂,经1粗3精3扫闭路浮选,可获得Ti02品位为72.52%,TiO2回收率为87.22%的金红石精矿。
采用本发明的方法对金红石进行浮选试验;具体方法为:浮选试验采用XFGII型浮选机和40ml浮选槽进行;每个实验使用2g金红石(-74+45μm);先用氯化钡和氯化铵(混合比例3:1,添加量为50g/t)对金红石矿浆进行预处理3min,再加入混合捕收剂(2.3-丁二醇含量30%,二乙基二硫代氨基甲酸钠50%,添加量为100g/t);2.3-丁二醇和二乙基二硫代氨基甲酸钠的的调节次数分别为3min和1min,加入抑制剂水玻璃,进行一粗一扫三精的浮选流程,浮选时间控制在1min;每次试验进行3次;得TiO2品位88.74%,金红石回收率91.25%。
对比实施例8
原试验所采用原生金红石矿样取自湖北枣阳某金红石矿,矿样经过颚式破碎机和对辊破碎机破碎至2mm以下,作为试验用样,矿样中TiO2含量为3.08%,含有部分含铁矿物,硅酸盐矿物较多。用磁选一重选一浮选相结合的联合工艺流程进行分选。将金红石矿样磨至细度-74μm 95%,给入平板磁选设备进行磁选,磁场强度为0.7T,在磁场强度0.7T;用苯乙烯膦酸和正辛醇作组合捕收剂;磁选抛尾20%左右,脱泥产品进入浮选得到浮选精矿TiO2品位70.98%,作业回收率88.60%。浮选精矿经磁选—焙烧—酸洗,最终得TiO2品位89.53%,金红石回收率74.78%。
采用本发明的方法对金红石进行浮选试验;具体方法为:浮选试验采用XFGII型浮选机和40ml浮选槽进行;每个实验使用2g金红石(-74+45μm);先用氯化钡和氯化铵(混合比例3:1,添加量为50g/t)对金红石矿浆进行预处理3min,再加入混合捕收剂(2.3-丁二醇含量30%,二乙基二硫代氨基甲酸钠50%,添加量为100g/t);2.3-丁二醇和二乙基二硫代氨基甲酸钠的的调节次数分别为3min和1min,加入抑制剂水玻璃,进行一粗一扫三精的浮选流程,浮选时间控制在1min;每次试验进行3次;得TiO2品位88.74%,金红石回收率91.25%。
Claims (6)
1.一种金红石的高效浮选方法,其特征在于:将金红石破碎磨矿,以氯化钡和氯化铵的混合物为活化剂来活化金红石,然后加入复合捕收剂,抑制剂,进行一粗一扫三精浮选流程;所述复合捕收剂由2.3-丁二醇、二乙基二硫代氨基甲酸钠组成,抑制剂为水玻璃;其中,2.3-丁二醇含量为20-70%,二乙基二硫代氨基甲酸钠30-80%。
2.根据权利要求1所述金红石的高效浮选方法,其特征在于:磨矿至-74+45μm。
3.根据权利要求1所述金红石的高效浮选方法,其特征在于:活化过程中pH值为4~7。
4.根据权利要求1所述金红石的高效浮选方法,其特征在于:活化剂中氯化钡和氯化铵的质量比为1:1~3:1。
5.根据权利要求4所述金红石的高效浮选方法,其特征在于:活化剂的加入量为30-100g/t,活化时间为2-5min。
6.根据权利要求1所述金红石的高效浮选方法,其特征在于:混合捕收剂用量50-200g/t,作用时间3分钟,温度23-25℃。
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CN1817468A (zh) * | 2006-03-13 | 2006-08-16 | 昆明理工大学 | 一种铁闪锌矿与闪锌矿的选矿活化剂 |
CN105665146A (zh) * | 2016-03-04 | 2016-06-15 | 中南大学 | 一种提高金红石浮选回收率的方法 |
CN107694762A (zh) * | 2017-11-10 | 2018-02-16 | 中南大学 | 一种从矿石中浮选捕收金红石的组合物及浮选方法 |
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US4501658A (en) * | 1982-08-25 | 1985-02-26 | Freeport Kaolin Company | Method of conditioning clay for flotation using in situ ferrous activator |
CN1817468A (zh) * | 2006-03-13 | 2006-08-16 | 昆明理工大学 | 一种铁闪锌矿与闪锌矿的选矿活化剂 |
CN105665146A (zh) * | 2016-03-04 | 2016-06-15 | 中南大学 | 一种提高金红石浮选回收率的方法 |
CN107694762A (zh) * | 2017-11-10 | 2018-02-16 | 中南大学 | 一种从矿石中浮选捕收金红石的组合物及浮选方法 |
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