CN109806980A - A kind of method and its application of malachite sulfur product control - Google Patents

A kind of method and its application of malachite sulfur product control Download PDF

Info

Publication number
CN109806980A
CN109806980A CN201910081680.7A CN201910081680A CN109806980A CN 109806980 A CN109806980 A CN 109806980A CN 201910081680 A CN201910081680 A CN 201910081680A CN 109806980 A CN109806980 A CN 109806980A
Authority
CN
China
Prior art keywords
malachite
sulfur product
product control
flotation
agent
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CN201910081680.7A
Other languages
Chinese (zh)
Other versions
CN109806980B (en
Inventor
卜显忠
陈瑶
史巾
陈彤
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Xian University of Architecture and Technology
Original Assignee
Xian University of Architecture and Technology
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Xian University of Architecture and Technology filed Critical Xian University of Architecture and Technology
Priority to CN201910081680.7A priority Critical patent/CN109806980B/en
Publication of CN109806980A publication Critical patent/CN109806980A/en
Application granted granted Critical
Publication of CN109806980B publication Critical patent/CN109806980B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Manufacture And Refinement Of Metals (AREA)

Abstract

A kind of method and its application of malachite sulfur product control, the sulphur for using 1:1 to match: thiocarbamide powder is as vulcanizing agent, iron powder is completed malachite using mechanochemical treatment in grinding process and is vulcanized as vulcanization reaction auxiliary agent, can be in one layer of CuFeS of malachite Surface Creation2Based on sulfide film, the sulfide film chemical stability and mechanical stability are strong, oxidation reaction will not occur in subsequent floatation process, product film will not mechanical detachment under the revolving speed of 160~180rpm for flotation device stirring rotator.Malachite flotation recovery rate after being vulcanized with this method can achieve 75.6%~82.5%, close to the floatation indicators of sulphide ore, have broad popularization and application prospect.

Description

A kind of method and its application of malachite sulfur product control
Technical field
The invention belongs to technical field of mineral processing, are related to the sulfide flotation of malachite, in particular to a kind of malachite sulphur Change the method and its application of product control.
Background technique
As mineral resources are increasingly poor thin miscellaneous, people are to the comprehensive recovery of resource, the quality of concentrate product and flotation point Requirement from effect is continuously improved, and the FLOTATION SEPARATION of complex multi-metal oxide ore also seems increasingly important.Malachite is relative to sulphur Change for copper mine, solubility is preferably and surface hydrophilicity is higher, is not easy flotation, therefore being firstly vulcanized before flotation is current using most For extensive method.Vulcanization is exactly to change mineral surfaces property by addition vulcanizing agent, and mineral surfaces is made to generate one layer of sulphide ore Film, improving hydrophobicity becomes easily floating, improves the rate of recovery.The vulcanizing agent being commonly used is vulcanized sodium or NaHS, Such vulcanizing agent has that vulcanization reaction is relatively slow, process is not easy to control, sulfide film stability difference, and the vulcanization generated Object film is easy to loose under the effect of ore pulp complex flowfield and falls off, and especially dosage is difficult to hold, vulcanized sodium or NaHS Dosage is very few cannot to ensure enough reducing atmospheres, vulcanization effect is not achieved, dosage is excessive again can be bright to subsequent flotation generation Aobvious inhibiting effect.
Summary of the invention
In order to overcome the disadvantage of above-mentioned malachite floatation indicators difference, the purpose of the present invention is to provide a kind of vulcanizations of malachite The method and its application of product control, this method can be effectively controlled malachite sulfur product, at one layer of malachite Surface Creation CuFeS2Based on sulfide film, the sulfide film hydrophobicity, mechanical stability and chemical stability are strong, in subsequent flotation Will not aoxidize in the process, react flotation device stirring rotator under the revolving speed of 50-60rpm product film will not mechanical detachment, Malachite sulfur product efficient vulcanization malachite and can be can be effectively controlled using this method, increase substantially the concentrate of malachite The rate of recovery.
To achieve the goals above, the technical solution adopted by the present invention is that:
A kind of method of malachite sulfur product control, uses sulphur and thiocarbamide powder as vulcanizing agent, iron powder is as sulphur Change reaction promoter, completes malachite using mechanochemical treatment in grinding process and vulcanize.
The mass ratio of the sulphur and thiocarbamide is 1:1.
The malachite is rear malachite fine crushing, partial size < 8mm.
The vulcanizing agent dosage is 300~1000g/t.
The vulcanization reaction auxiliary dosage is 100~300g/t.
The grinding mode is dry milling, and the ore grinding time is 5~15min.
It malachite will carry out flotation (use conventional flotation process) after vulcanization, flotation recovery rate reaches 75.6%~ 82.5%, close to the floatation indicators of sulphide ore, have broad popularization and application prospect.
The flotation uses butyl xanthate for collecting agent, and dosage 55-100mg/L, 2# oil is foaming agent, additional amount 1~4 μL/L。
The principle of the present invention is:
The sulphur for using 1:1 to match: thiocarbamide powder is as vulcanizing agent, and iron powder is as vulcanization reaction auxiliary agent, in grinding process It is middle that ion exchange occurs using mechanochemical treatment, it, should in the sulfide film based on one layer of CuFeS2 of malachite Surface Creation Sulfide film hydrophobicity, chemical stability and mechanical stability are strong, there is the raising using malachite flotation recovery rate.
Compared with the method for existing vulcanization malachite, curingprocess rate of the present invention is fast, high-efficient, easy to operate, Neng Goushi Now oxidation copper resource is maximally utilized.
Specific embodiment
Below with reference to the embodiment embodiment that the present invention will be described in detail.
Embodiment 1
In the grinding process of malachite, it is that 1:1 configures sulphur, thiocarbamide powder as vulcanizing agent according to mass ratio, presses The dosage of 300g/t is added in grinding machine, auxiliary agent iron powder is added according still further to the dosage of 100g/t, dry grind 5min;Using normal after ore grinding Advise method for floating, the butyl xanthate that dosage is 55mg/L is collecting agent, act on 3min, 2# oil be foaming agent, 1 μ L/L of additional amount, 1min is acted on, bubble 4min is scraped, malachite flotation recovery rate can achieve 75.6%.
With the scheme that sorts that vulcanizing agent is not added, this method improves 35 percentage points of the malachite rate of recovery.
Embodiment 2
In the grinding process of malachite, it is that 1:1 configures sulphur, thiocarbamide powder as vulcanizing agent according to mass ratio, presses The dosage of 500g/t is added in grinding machine, auxiliary agent iron powder is added according still further to the dosage of 200g/t, dry grind 10min;It is used after ore grinding Conventional flotation method, butyl xanthate are collecting agent, dosage 85mg/L, act on 3min, and 2# oil is foaming agent, 2 μ L/L of additional amount, 1min is acted on, bubble 4min is scraped, malachite flotation recovery rate can achieve 80.3%.
With the scheme that sorts that vulcanizing agent is not added, this method improves 39.7 percentage points of the malachite rate of recovery.
Embodiment 3
In the grinding process of malachite, it is that 1:1 configures sulphur, thiocarbamide powder as vulcanizing agent according to mass ratio, presses The dosage of 1000g/t is added in grinding machine, auxiliary agent iron powder is added according still further to the dosage of 300g/t, dry grind 15min;It is used after ore grinding Conventional flotation method, butyl xanthate are collecting agent, and dosage 100mg/L acts on 3min, and 2# oil is foaming agent, 4 μ L/ of additional amount L acts on 1min, scrapes bubble 4min, and malachite flotation recovery rate can achieve 82.5%.
With the scheme that sorts that vulcanizing agent is not added, this method improves 41.9 percentage points of the malachite rate of recovery.

Claims (8)

1. a kind of method of malachite sulfur product control, which is characterized in that use sulphur and thiocarbamide powder as vulcanizing agent, iron Powder is completed malachite using mechanochemical treatment in grinding process and is vulcanized as vulcanization reaction auxiliary agent.
2. the method for malachite sulfur product control according to claim 1, which is characterized in that the matter of the sulphur and thiocarbamide Amount is than being 1:1.
3. the method for malachite sulfur product control according to claim 1, which is characterized in that after the malachite is fine crushing Malachite, partial size < 8mm.
4. the method for malachite sulfur product control according to claim 1, which is characterized in that the vulcanizing agent dosage is 300~1000g/t.
5. the method for malachite sulfur product control according to claim 1, which is characterized in that the vulcanization reaction auxiliary agent is used Amount is 100~300g/t.
6. the method for malachite sulfur product control according to claim 1, which is characterized in that the grinding mode is dry type Ore grinding, ore grinding time are 5~15min.
7. the application of the method for the control of malachite sulfur product described in claim 1, which is characterized in that malachite carries out after vulcanization Flotation, flotation recovery rate reach 75.6%~82.5%.
8. applying according to claim 7, which is characterized in that the flotation uses butyl xanthate for collecting agent, dosage 55- 100mg/L, 2# oil are foaming agent, 1~4 μ L/L of additional amount.
CN201910081680.7A 2019-01-28 2019-01-28 Method for controlling malachite vulcanization products and application thereof Active CN109806980B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201910081680.7A CN109806980B (en) 2019-01-28 2019-01-28 Method for controlling malachite vulcanization products and application thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201910081680.7A CN109806980B (en) 2019-01-28 2019-01-28 Method for controlling malachite vulcanization products and application thereof

Publications (2)

Publication Number Publication Date
CN109806980A true CN109806980A (en) 2019-05-28
CN109806980B CN109806980B (en) 2020-12-01

Family

ID=66605641

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201910081680.7A Active CN109806980B (en) 2019-01-28 2019-01-28 Method for controlling malachite vulcanization products and application thereof

Country Status (1)

Country Link
CN (1) CN109806980B (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113634375A (en) * 2021-08-13 2021-11-12 西安建筑科技大学 Beneficiation method for low-grade mixed copper oxide ore
CN115487932A (en) * 2022-09-26 2022-12-20 昆明理工大学 Method for pretreatment-xanthate flotation of silicate type copper oxide ore surface

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB815088A (en) * 1954-07-12 1959-06-17 Phillips Petroleum Co Improvements in a process for the production of halogenated hydrocarbons
CN101125311A (en) * 2007-09-24 2008-02-20 昆明理工大学 Vulcanizing-flotation combing method for treating zinc kiln slag
WO2008048495A2 (en) * 2006-10-13 2008-04-24 Archer-Daniels-Midland Company Hydrogenation process and high monoene compositions obtained therefrom
KR101572861B1 (en) * 2014-08-21 2015-12-01 한국세라믹기술원 A method of flotation for copper oxide ore using multi-collector
CN105363565A (en) * 2015-11-11 2016-03-02 湖南有色金属研究院 Malachite catalytic activating agent and method for flotation of malachite through malachite catalytic activating agent
CN105363562A (en) * 2015-12-08 2016-03-02 中南大学 Beneficiation method of low-grade cuprite
CN108479827A (en) * 2018-04-03 2018-09-04 太原理工大学 Medium temperature hydrolyzation converts carbonyl sulfur and the difunctional coupled catalyst of deoxidation and preparation method

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB815088A (en) * 1954-07-12 1959-06-17 Phillips Petroleum Co Improvements in a process for the production of halogenated hydrocarbons
WO2008048495A2 (en) * 2006-10-13 2008-04-24 Archer-Daniels-Midland Company Hydrogenation process and high monoene compositions obtained therefrom
CN101125311A (en) * 2007-09-24 2008-02-20 昆明理工大学 Vulcanizing-flotation combing method for treating zinc kiln slag
KR101572861B1 (en) * 2014-08-21 2015-12-01 한국세라믹기술원 A method of flotation for copper oxide ore using multi-collector
CN105363565A (en) * 2015-11-11 2016-03-02 湖南有色金属研究院 Malachite catalytic activating agent and method for flotation of malachite through malachite catalytic activating agent
CN105363562A (en) * 2015-12-08 2016-03-02 中南大学 Beneficiation method of low-grade cuprite
CN108479827A (en) * 2018-04-03 2018-09-04 太原理工大学 Medium temperature hydrolyzation converts carbonyl sulfur and the difunctional coupled catalyst of deoxidation and preparation method

Non-Patent Citations (10)

* Cited by examiner, † Cited by third party
Title
丁辉: "铜绿山氧化矿尾矿综合利用研究与生产实践", 《金属矿山 增刊》 *
冯其明等: "我国几种难处理矿石的加工利用现状", 《金属矿山 增刊》 *
刘尚乐: "《建筑防水材料试验室手册》", 30 June 2006, 中国建材工业出版社 *
印万忠等: "国内外金属矿山难选矿选冶新技术进展", 《金属矿山 增刊》 *
周源等: "难选氧化铜矿石高效分选技术研究现状", 《金属矿山 增刊》 *
曹俊雅: "复杂型氧化铜矿生物硫化预处理基础研究", 《矿产综合利用》 *
武薇等: "氧化铜矿的浮选及研究进展", 《矿冶》 *
辽宁省石油化学工业厅: "《辽宁化工产品大全》", 31 December 1994, 辽宁科学技术出版社 *
郑伟: "氧化铜矿选矿药剂的工业应用", 《金属矿山 增刊》 *
黄波: "《界面分选技术》", 30 September 2008, 煤炭工业出版社 *

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113634375A (en) * 2021-08-13 2021-11-12 西安建筑科技大学 Beneficiation method for low-grade mixed copper oxide ore
CN115487932A (en) * 2022-09-26 2022-12-20 昆明理工大学 Method for pretreatment-xanthate flotation of silicate type copper oxide ore surface
CN115487932B (en) * 2022-09-26 2024-04-09 昆明理工大学 Method for surface pretreatment-xanthate flotation of silicate copper oxide ore

Also Published As

Publication number Publication date
CN109806980B (en) 2020-12-01

Similar Documents

Publication Publication Date Title
CN105750093B (en) A kind of method for floating of cupric oxide ore
CN107626441B (en) Recycle the beneficiation method and beneficiation reagent of copper in copper slag
CN109806980A (en) A kind of method and its application of malachite sulfur product control
CN109201320B (en) Beneficiation method for copper-cobalt ore containing easy-to-float gangue
CN103909020A (en) Flotation separation inhibitor and separation method of galena, pyrite and sphalerite
CN107812616A (en) A kind of difficulty selects the floatation separation process of lead zinc sulphur ore
CN107855211A (en) A kind of complicated difficult selects the beneficiation method of high-grade copper sulphur ore deposit
CN110237938B (en) Flotation reagent and flotation separation method of molybdenum, bismuth and sulfur polymetallic sulfide ore
CN111468304A (en) Composite inhibitor for pyrite and pumice in copper-sulfur ores and flotation separation method thereof
CN107051749A (en) A kind of zinc oxide ore intensified Daqu method
CN105057110B (en) A kind of technique of bulk concentrate reagent removal and the separation of lead antimony zinc-iron multi-metal sulfide
CN113856911B (en) Beneficiation method for high-sulfur copper gold and silver ore
CN106269290B (en) The method for floating of decopperized lead zinc from highgrade pyrite concentrate
CN104353557B (en) Method for reducing sulphur content in iron ore concentrate through flotation process
CN109261364A (en) The solution of pyrite presses down activation method in a kind of shallow crust structures
CN109266842A (en) A method of for copper mine arsenic removal
CN110743713A (en) Collecting agent-free flotation process method for copper sulfide minerals
CN105013618A (en) Heating floatation method for middling pulp in zinc oxide ore
CN105435956B (en) A kind of method that falcon centrifugal reselections are combined recycling wulfenite with flotation
CN109092552A (en) A method of bulk flotation sulphur, arsenic from vulcanization tailing
CN117816379B (en) Vulcanization flotation method for refractory zinc oxide ores
CN105689151B (en) A kind of technique that lead, zinc and sulphur are reclaimed from the Gold Concentrate under Normal Pressure phase analysis of high content argillization gangue
CN103194618B (en) Method for sulfurizing zinc oxide ore
CN109731693A (en) A kind of method of trithiocyanuric acid saturated solution sulfide flotation copper-lead Zinc oxide
CN109107773A (en) The method for electrochemical floatation of lead sulfide mixed concentrate is recycled in a kind of high-grade Pb-Zn deposits

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant