CN85100345A - Floatation of antimony sulfide ore in slightly acidic medium - Google Patents

Floatation of antimony sulfide ore in slightly acidic medium Download PDF

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Publication number
CN85100345A
CN85100345A CN85100345.1A CN85100345A CN85100345A CN 85100345 A CN85100345 A CN 85100345A CN 85100345 A CN85100345 A CN 85100345A CN 85100345 A CN85100345 A CN 85100345A
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CN
China
Prior art keywords
antimony
flotation
sulfide ore
antimony sulfide
ore
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Withdrawn
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CN85100345.1A
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Chinese (zh)
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CN1009252B (en
Inventor
黄开国
李隆峰
张国祥
胡为柏
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Central South University
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Central South University
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Priority to CN 85100345 priority Critical patent/CN1009252B/en
Publication of CN85100345A publication Critical patent/CN85100345A/en
Publication of CN1009252B publication Critical patent/CN1009252B/en
Expired legal-status Critical Current

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Abstract

Floatation of antimony sulfide ore in slightly acidic medium belongs to antimony sulfide ore flotation field.With sulfuric acid or sulfurous acid, SO 2Adjust ore pulp to faintly acid, cooperate selective copper collector and lead salt activator, do not need foaming agent.Prescription is simple, and the medicine consumption is low, flotation speed is fast, and the sorting index height helps antimony-arsenic sorting.Single antimony sulfide ore (containing antimony 7.28%) flotation results, antimony concentrate grade 65%, the rate of recovery 98.2%, to containing the flotation of arsenic (0.55%) antimony sulfide ore, antimony concentrate contains arsenic and drops to 0.34%.

Description

Floatation of antimony sulfide ore in slightly acidic medium
The invention belongs to the antimony sulfide ore flotation.
The antimony sulfide ore flotation is carried out in neutral ore pulp usually, is activator with the plumbi nitras, and xanthate is a collecting agent, and terpenic oil is done foaming agent and formed traditional prescription.Nearly 6 kinds of more complicated prescription medications mix use with multiple senior sulphur hydrogen class collecting agent (as butyl xanthate, diethyldithiocarbamate etc.) and a large amount of supplementary catching agent (as shale oil, kerosene etc.), also need activator and foaming agent.Use this two classes prescription, flotation speed is slow, and floatation equipment is many, energy consumption is high; Floating agent is wide in variety, the medicine consumption is big; Floatation indicators low (external best index such as its ore deposit, Songyuan City grade 11% of South Africa Mel, antimony concentrate grade 61.94%, the rate of recovery 91.4%; Domestic index preferably such as China tin ore south of the mountains factory, raw ore contains antimony 3.19%, antimony concentrate grade 47.58%, the rate of recovery 93.97%), bad to the antimony sulfide ore sorting that contains arsenic, antimony concentrate contains the arsenic height (when antimony ore contains arsenic 0.58%, antimony concentrate contains arsenic 2.74%), influence antimony smelting recovery and antimony product quality, and environment is brought pollution nuisance.In addition, the SO of smeltery's discharge 2Pernicious gas also needs to administer and utilize.
In order to accelerate flotation speed, sorting antimony-arsenic mineral is simplified prescription, reduces the medicine consumption, improves floatation indicators, improves product quality, and the present invention adopts the faintly acid flotation of ore pulp.
Basic comprising of the present invention is: with sulfuric acid or sulfurous acid (SO 2) to adjust ore pulp suitable to the flotation antimony trisulfide to this pH value of faintly acid PH5~6(, and equipment is not had damage), with selective copper collector butyl ammonium aerofloat or other sulphur hydrogen class collecting agent flotation.When using butyl ammonium aerofloat, do not need foaming agent; During with sulphur hydrogen class collecting agent, still want foaming agent.Before antimony sulfide ore (comprising the antimony sulfide ore that the contains arsenic) flotation, press sulfuric acid (or sulfurous acid (SO 2)) 1000~4000 gram/tons, plumbi nitras 100~300 gram/tons, butyl ammonium aerofloat 150~300 gram/tons order add, and adjusts ore pulp; Through one roughing (5~10 minutes), once purging selection (3~5 minutes), primary cleaning, just can obtain the high-quality antimony concentrate.When raw ore contained antimony 4.5~7.2%, gained antimony concentrate grade was 60~65%, the rate of recovery 95~98%.When raw ore is when containing the antimony sulfide ore of arsenic 0.45~0.6%, the antimony concentrate arsenic content that flotation obtains is from the traditional prescription of 2.5~4.5%() be reduced to this prescription of 0.3~0.5%().
The present invention's following advantage of having compared with neutral flotation of ore pulp: 1. flotation time is short, and the medicine consumption is few.Antimony sulfide ore flotation in the faintly acid ore pulp (roughly selecting 10 minutes), antimony recovery can reach 97%; And flotation in neutral ore pulp (roughly selecting 10 minutes), the rate of recovery only 82.3%, even when collector dosage and flotation time doubled simultaneously, the rate of recovery still has only 94.3%.2. help antimony-arsenic sorting.When raw ore contains antimony 5.11%, arsenic 0.46%, do the antimony concentrate that collecting agent (needing foaming agent) obtained with xanthate and contain antimony 49.08%, arsenic 4.25%, antimony recovery 94.7%; Contain antimony 5.19%, arsenic 0.55% and work as raw ore, (do not need foaming agent) when doing collecting agent, can obtain antimony concentrate and contain antimony 56.1%, arsenic 0.34%, antimony recovery 95.6% with butyl ammonium aerofloat.It is low that antimony concentrate contains arsenic, helps shortening the antimony smelting cycle, reduces and smelt alkaline consumption and energy consumption, improves antimony smelting recovery and antimony product quality, alleviates the pollution of arsenic to environment.3. can utilize SO 2The acidity that waste gas, sulfurous acid, useless dilute sulfuric acid are adjusted ore pulp turns waste into wealth.
Embodiment: to containing the antimony sulfide ore raw ore of antimony 7.28%, before flotation, add sulfuric acid 2500 grams, plumbi nitras 150 grams, butyl ammonium aerofloat 180 gram adjustment ore pulps (PH=5.4) in proper order by ore per ton, through one roughing (10 minutes), once purging selection (5 minutes), primary cleaning, the small-sized closed circuit flotation experimental results that chats returns in proper order obtains antimony concentrate grade 65%, the rate of recovery 98.2%.

Claims (3)

1, antimony sulfide ore flotation comprises that with butyl ammonium aerofloat (or other sulphur hydrogen class) be that collecting agent, plumbi nitras are activator, the invention is characterized in to adopt sulfuric acid or sulfurous acid (SO 2), by 1000~4000 gram/tons, adjust pulp PH value to 5~6, flotation in the faintly acid ore pulp.
2, floatation of antimony sulfide ore in slightly acidic medium according to claim 1, it is characterized in that with butyl ammonium aerofloat 150~300 gram/tons be collecting agent, plumbi nitras 100~300 gram/tons are activator, the flotation antimony sulfide ore, during sorting antimony-arsenic mineral, need not add foaming agent.
3, floatation of antimony sulfide ore in slightly acidic medium according to claim 1 is characterized in that when single antimony sulfide ore contains antimony 7.28%, and best prescription is, sulfuric acid 2500 gram/tons, and plumbi nitras 150 gram/tons, butyl ammonium aerofloat 180 gram/tons, flotation pulp pH value are 5.4.
CN 85100345 1985-04-01 1985-04-01 Floatation of antimony sulfide ore in slightly acidic medium Expired CN1009252B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 85100345 CN1009252B (en) 1985-04-01 1985-04-01 Floatation of antimony sulfide ore in slightly acidic medium

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 85100345 CN1009252B (en) 1985-04-01 1985-04-01 Floatation of antimony sulfide ore in slightly acidic medium

Publications (2)

Publication Number Publication Date
CN85100345A true CN85100345A (en) 1986-08-20
CN1009252B CN1009252B (en) 1990-08-22

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN 85100345 Expired CN1009252B (en) 1985-04-01 1985-04-01 Floatation of antimony sulfide ore in slightly acidic medium

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CN (1) CN1009252B (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101623673B (en) * 2009-07-01 2013-01-30 湖南有色金属研究院 Beneficiation method of antimonyore
CN105170336A (en) * 2015-09-24 2015-12-23 长春黄金研究院 Method for improving antimony concentrate grade
CN106492996A (en) * 2016-11-02 2017-03-15 广西大学 A kind of stibnite and the flotation separation method of realgar
CN106492997A (en) * 2016-11-02 2017-03-15 广西大学 A kind of preparation method of realgar mineral inhibitor
CN110339947A (en) * 2019-08-15 2019-10-18 桃江久通锑业有限责任公司 A kind of antimony trisulfide flotation operation medicament

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101623673B (en) * 2009-07-01 2013-01-30 湖南有色金属研究院 Beneficiation method of antimonyore
CN105170336A (en) * 2015-09-24 2015-12-23 长春黄金研究院 Method for improving antimony concentrate grade
CN106492996A (en) * 2016-11-02 2017-03-15 广西大学 A kind of stibnite and the flotation separation method of realgar
CN106492997A (en) * 2016-11-02 2017-03-15 广西大学 A kind of preparation method of realgar mineral inhibitor
CN110339947A (en) * 2019-08-15 2019-10-18 桃江久通锑业有限责任公司 A kind of antimony trisulfide flotation operation medicament

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Publication number Publication date
CN1009252B (en) 1990-08-22

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