CN107737667A - The method for improving high shale content cupric oxide ore mineral processing index - Google Patents

The method for improving high shale content cupric oxide ore mineral processing index Download PDF

Info

Publication number
CN107737667A
CN107737667A CN201711164099.9A CN201711164099A CN107737667A CN 107737667 A CN107737667 A CN 107737667A CN 201711164099 A CN201711164099 A CN 201711164099A CN 107737667 A CN107737667 A CN 107737667A
Authority
CN
China
Prior art keywords
roughing
ore
time
pretreatment
cupric oxide
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.)
Pending
Application number
CN201711164099.9A
Other languages
Chinese (zh)
Inventor
褚亦功
薛伟
张立征
李晓东
陈代雄
王立军
易运来
毛竞
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.)
Hunan Research Institute of Non Ferrous Metals
Original Assignee
Hunan Research Institute of Non Ferrous Metals
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 Hunan Research Institute of Non Ferrous Metals filed Critical Hunan Research Institute of Non Ferrous Metals
Priority to CN201711164099.9A priority Critical patent/CN107737667A/en
Publication of CN107737667A publication Critical patent/CN107737667A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION 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
    • B03BSEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
    • B03B7/00Combinations of wet processes or apparatus with other processes or apparatus, e.g. for dressing ores or garbage
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/08Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor
    • B01J19/10Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor employing sonic or ultrasonic vibrations
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION 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
    • B03BSEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
    • B03B9/00General arrangement of separating plant, e.g. flow sheets
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION 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
    • B03DFLOTATION; DIFFERENTIAL SEDIMENTATION
    • B03D1/00Flotation
    • B03D1/001Flotation agents
    • B03D1/018Mixtures of inorganic and organic compounds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION 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
    • B03DFLOTATION; DIFFERENTIAL SEDIMENTATION
    • B03D2201/00Specified effects produced by the flotation agents
    • B03D2201/02Collectors
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION 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
    • B03DFLOTATION; DIFFERENTIAL SEDIMENTATION
    • B03D2203/00Specified materials treated by the flotation agents; Specified applications
    • B03D2203/02Ores
    • B03D2203/04Non-sulfide ores

Landscapes

  • Chemical & Material Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Toxicology (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Abstract

The invention provides a kind of method for improving high shale content cupric oxide ore mineral processing index, comprise the following steps:Ore grinding, the content of raw ore ore grinding to 0.074mm is accounted for 85 95%, pulp density is 18 30%;Ultrasonic pretreatment, the obtained ore pulp is sent into ultrasonic wave tank diameter and carries out ultrasonic pretreatment, ore pulp after being pre-processed;Flotation, ore pulp after the obtained pretreatment is subjected to roughing and obtains rougher concentration and rougher tailings;It is selected to rougher concentration progress to obtain concentrate product;Rougher tailings row is scanned to obtain product from failing;The roughing and floating agent is added during scanning.The present invention solves the problems, such as slime coating, improves selectivity and collecting performance of the medicament to target minreal, so as to improve the grade and the rate of recovery of concentrate product copper using ultrasonic technology pretreatment oxidation of ore pulp copper flotation process.

Description

The method for improving high shale content cupric oxide ore mineral processing index
Technical field
The present invention relates to technical field of beneficiation, and in particular to a kind of method for improving high shale content cupric oxide ore mineral processing index.
Background technology
Copper is very important metals resources in modern industry, and copper mine is also very important mineral products money in the world today Source, copper metal mineral resources in China's are faced with the short situation of very severe at present, and China is that copper metal consumption figure first is big State, due to copper metal in modern Economy Development in occupation of critical role, the copper resource in China is very in short supply, largely now It is upper to rely on from external import.
Cupric oxide ore resource is the important component of copper resource, and reserves are relatively abundanter, so being provided to cupric oxide ore The development process in source and application are significant for metallurgy of copper industrial expansion, but cupric oxide technique of preparing is at present One of problem in current ore dressing.Because cupric oxide Component comparison is complicated, loosely organized frangible, hydrability is stronger, and contains A large amount of sludges, so cupric oxide technique of preparing has the problems such as technological process is complicated, medicament kind is more, dosage is big at present, obtain Concentrate product taste and the rate of recovery it is relatively low.
The content of the invention
In order to solve problems of the prior art, improve high shale content cupric oxide ore ore dressing the invention provides one kind and refer to Calibration method.This method solves asking for slime coating using ultrasonic technology pretreatment ore pulp-cupric oxide flotation process Topic, selectivity and collecting performance of the medicament to target minreal are improved, so as to reduce floating agent species and dosage, further improved The grade and the rate of recovery of concentrate product copper.
To achieve the above object, the invention provides it is a kind of improve high shale content cupric oxide ore mineral processing index method, specifically Scheme comprises the following steps:
S1:Ore grinding, using high shale content cupric oxide as raw ore, the content of raw ore ore grinding to -0.074mm is accounted for into 85-95%, adjusted Pulp density is 18-30%;
S2:Ultrasonic pretreatment, it is pre- that ultrasonic wave tank diameter progress ultrasonic wave is sent into the ore pulp overflow obtained in S1 Processing, ore pulp after being pre-processed;The ultrasonic pretreatment time is 5-10min, and frequency is 20kHz~50kHz, and power is 800~1200W.
S3:Flotation, ore pulp after the pretreatment obtained in S2 is subjected to roughing and obtains rougher concentration and rougher tailings;It is right The rougher concentration progress is selected to obtain concentrate product;Rougher tailings is scanned to obtain product from failing;The roughing and sweep Floating agent is added during choosing, the floating agent is the combination medicament that vulcanized sodium, penta xanthate and terpenic oil are formed.
Specifically, as a kind of preferred scheme, roughing number described in S3 is once to twice;The concentration times are two It is secondary to four times;The number of scanning is secondary to four times.
Specifically, as a kind of preferred scheme, the roughing number is twice;The concentration times is three times;It is described to sweep Number is selected as three times.
Specifically, as a kind of preferred scheme, amount of sodium sulfide is 800~2000g/t in the first time roughing, second Amount of sodium sulfide is 600~1200g/t in secondary roughing, scans, scans for the second time for the first time, scanning middle amount of sodium sulfide for the third time It is 80-400g/t;Penta xanthate dosage is 100~400g/t in first time roughing, and penta xanthate dosage is 80 in second of roughing ~300g/t, scan, scan for the second time for the first time, scan for the third time in penta xanthate dosage be 60-150g/t;First time roughing Middle terpenic oil dosage is 20-100g/t, and terpenic oil dosage is 20~50g/t in second of roughing, scans, sweeps for the second time for the first time It is 10-25g/t to select, scan middle terpenic oil dosage for the third time.
The present invention has the advantages that:
The method provided by the invention for improving high shale content cupric oxide ore mineral processing index, using the cupric oxide ore of high shale content as original Ore deposit, enter floatation system after raw ore ore grinding after ultrasonic pretreatment 5-10min, carry out cupric oxide flotation.This method is using super Technology of acoustic wave pre-processes before carrying out flotation, solves the problems, such as slime coating, improves selectivity and collecting of the medicament to target minreal Performance, so as to reduce floating agent species and dosage, further improve the grade and the rate of recovery of concentrate product copper.With without ultrasound The method of ripple pretreatment ore pulp is compared, and the copper concentrate Cu of acquisition grade improves more than 2%, and the rate of recovery improves more than 5%.This hair The bright selection for further optimizing floatation process technique and floating agent and dosage, mineral processing circuit letter provided by the invention Single, cost is low, easy to operate, environmental protection, is easy to industrial implementation.
Brief description of the drawings
Technical scheme in order to illustrate the embodiments of the present invention more clearly, it will use below required in embodiment Accompanying drawing is briefly described, it should be apparent that, drawings in the following description are some embodiments of the present invention, general for this area For logical technical staff, on the premise of not paying creative work, other accompanying drawings can also be obtained according to these accompanying drawings.
Accompanying drawing 1 is a kind of new method embodiment principle technological process for improving high shale content cupric oxide ore mineral processing index of the present invention Figure.
Accompanying drawing 2 is a kind of new method embodiment process chart for improving high shale content cupric oxide ore mineral processing index of the present invention.
Embodiment
For the ease of understanding the present invention, the present invention is made below in conjunction with Figure of description and preferred embodiment more complete Face, meticulously describe, but protection scope of the present invention is not limited to embodiment in detail below.
Unless otherwise defined, the implication that all technical terms used hereinafter are generally understood that with those skilled in the art It is identical.Technical term used herein is intended merely to describe the purpose of specific embodiment, is not intended to the limitation present invention Protection domain.
Except there is a special instruction, the various reagents used in the present invention, raw material be can be commercially commodity or Person can pass through product made from known method.
Embodiment 1:
Raw ore is certain cupric oxide 1 in the present embodiment, is high shale content cupric oxide ore ore, and grade is 1.03% or so, selects factory Using " two thick three sweep three essences " mineral processing circuit, method provided by the invention is respectively adopted and locates in advance without ultrasonic technology The method recovery copper of reason.
The present invention uses the mineral processing circuit of ultrasonic technology preprocess method:
(1) ore grinding, grinding machine progress ore grinding to the content that fineness is -0.074mm will be sent into after crushing raw ore and accounts for 88% or so, Size mixing to pulp density 20%;
(2) ultrasonic pretreatment, it is pre- that ultrasonic wave tank diameter progress ultrasonic wave is sent into the ore pulp overflow obtained in S1 Processing, ultrasonic pretreatment time are 8min, supersonic frequency 28kHz, power 900W, ore pulp after being pre-processed;
(3) flotation, ore pulp after the pretreatment obtained in S2 is sent into flotation cell, progress " roughing twice, is swept three times The mineral processing circuit of choosing, rougher concentration merging progress triple cleaning ", obtains concentrate product and product from failing after flotation;Institute State roughing and scan and floating agent is added in engineering, the floating agent is the combination that vulcanized sodium, penta xanthate and terpenic oil are formed Medicament;Amount of sodium sulfide is 1200g/t in the first time roughing, and amount of sodium sulfide is 650g/t in second of roughing, first It is secondary that to scan, scan for the second time, scanning middle amount of sodium sulfide for the third time be 200g/t;Penta xanthate dosage is in first time roughing 360g/t, penta xanthate dosage is 120g/t in second of roughing, scan, scan for the second time for the first time, scan for the third time in it is penta yellow Survival dose is 90g/t;Terpenic oil dosage is 80g/t in first time roughing, and terpenic oil dosage is 45g/t in second of roughing, It is 15g/t to scan, scan for the second time, scanning middle terpenic oil dosage for the third time for the first time.
(4) concentrate carries out press filtration after concentrator is dense and obtains concentrate product;
(5) mine tailing is delivered to Tailings Dam after efficient deep wimble thickener is dense.
Removed without the beneficiation method of ultrasonic technology pretreatment in above-mentioned steps outside ultrasonic pretreatment, other processing Measure is.
Removed without the beneficiation method of ultrasonic technology pretreatment in above-mentioned steps outside ultrasonic pretreatment, other processing Measure is.
From experimental data in table 1, the concentrate grade for the concentrate product for pre-processing to obtain without ultrasonic technology is 16.12%, copper recovery 80.20%.The characteristics of method provided by the invention is high containing mud for the ore deposit, and oxygenation efficiency is high, On the basis of original process structure is constant, using ultrasonic pretreatment ore pulp technology, concentrate grade is up to 18.20%, copper The rate of recovery bring up to 85.27%, method provided by the invention compared with without the method for ultrasonic pretreatment ore pulp, acquisition Copper concentrate Cu grade improves more than 2.08%, and the rate of recovery improves more than 5.07%.The grade 0.16% of copper in mine tailing, copper Loss late 14.73%.
Certain ultrasonication of cupric oxide 1 of table 1 and not ultrasonication beneficiation test result/%
Embodiment 2:
Raw ore is certain cupric oxide 2 in the present embodiment, is high shale content, high oxidation, the ore containing high basic gangue, can in raw ore The valuable element of recovery is copper, and grade is 1% or so, selects factory to be respectively adopted using " one thick three sweeps two essences " mineral processing circuit Method provided by the invention and the method recovery copper without ultrasonic technology pretreatment.
The present invention uses the mineral processing circuit of ultrasonic technology preprocess method:
(1) ore grinding, grinding machine will be sent into after crushing raw ore and carries out ore grinding, ore grinding to fineness is that -0.074mm content accounts for 85% Left and right, size mixing to pulp density 22%;
(2) ultrasonic pretreatment, ultrasonic wave tank diameter is sent into the ore pulp overflow obtained in (1), carries out ultrasonic wave Pretreatment, ultrasonic pretreatment time are 5min, supersonic frequency 40kHz, power 1000W, ore pulp after being pre-processed;
(3) flotation, ore pulp is sent into flotation cell after the pretreatment that will be obtained in (2), and progress " one roughing, is swept three times Choosing, rougher concentration merge carry out it is selected twice " mineral processing circuit, concentrate product and product from failing are obtained after flotation;Institute State roughing and scan and floating agent is added in engineering, the floating agent is the combination that vulcanized sodium, penta xanthate and terpenic oil are formed Medicament;Amount of sodium sulfide is 1500g/t in the roughing, scan, scan for the second time for the first time, scanning middle vulcanized sodium for the third time Dosage is 120g/t;Penta xanthate dosage is 270g/t in the roughing, scans, scans for the second time, scans for the third time for the first time In penta xanthate dosage be 85g/t;Terpenic oil dosage is 60g/t in the roughing, scans, scans for the second time for the first time, the 3rd It is secondary that to scan middle terpenic oil dosage be 15g/t.
Removed without the beneficiation method of ultrasonic technology pretreatment in above-mentioned steps outside ultrasonic pretreatment, other processing Measure is.
From experimental data in table 2, the concentrate grade for the concentrate product for pre-processing to obtain without ultrasonic technology is 17.05%, copper recovery 82.66%.The characteristics of method provided by the invention is high containing mud for the ore deposit, and oxygenation efficiency is high, On the basis of original process structure is constant, using ultrasonic pretreatment ore pulp technology, concentrate grade is up to 19.11%, copper The rate of recovery bring up to 88.14%, method provided by the invention compared with without the method for ultrasonic pretreatment ore pulp, acquisition Copper concentrate Cu grade improves more than 2.06%, and the rate of recovery improves more than 5.48%.The grade 0.19% of copper in mine tailing, copper Loss late 11.86%.
Certain ultrasonic pretreatment of copper mine 2 of table 2 with without ultrasonic pretreatment ore dressing result/%
Although above the present invention is made to retouch in detail with general explanation, embodiment and experiment State, but on the basis of the present invention, it can be made some modifications or improvements, this is apparent to those skilled in the art 's.Therefore, these modifications or improvements without departing from theon the basis of the spirit of the present invention, are belonged to claimed Scope.

Claims (4)

  1. A kind of 1. method for improving high shale content cupric oxide ore mineral processing index, it is characterised in that comprise the following steps:
    S1:Ore grinding, using high shale content cupric oxide as raw ore, broken ore grinding to -0.074mm content account for 85-95%, and pulp density is 18-30%;
    S2:Ultrasonic pretreatment, the ore pulp obtained in S1 is sent into ultrasonic wave tank diameter and carries out ultrasonic pretreatment, is obtained Ore pulp after pretreatment;The ultrasonic pretreatment time is 5-10min, and frequency is 20kHz ~ 50kHz, and power is 800 ~ 1200W;
    S3:Flotation, ore pulp after the pretreatment obtained in S2 is subjected to roughing and obtains rougher concentration and rougher tailings;To described Rougher concentration progress is selected to obtain concentrate product;Rougher tailings is scanned to obtain product from failing;The roughing and scanned Floating agent is added in journey, the floating agent is the combination medicament that vulcanized sodium, penta xanthate and terpenic oil are formed.
  2. 2. the method according to claim 1 for improving high shale content cupric oxide ore mineral processing index, it is characterised in that described in S3 Roughing number is once to twice;The concentration times are secondary to four times;The number of scanning is secondary to four times.
  3. 3. the method according to claim 2 for improving high shale content cupric oxide ore mineral processing index, it is characterised in that the roughing Number is twice;The concentration times is three times;The number of scanning is three times.
  4. 4. the method according to claim 3 for improving high shale content cupric oxide ore mineral processing index, it is characterised in that described first Amount of sodium sulfide is 800~2000g/t in secondary roughing, and amount of sodium sulfide is 600~1200g/t in second of roughing, for the first time It is 80-400g/t to scan, scan for the second time, scanning middle amount of sodium sulfide for the third time;Penta xanthate dosage is in first time roughing 100~400g/t, penta xanthate dosage is 80~300g/t in second of roughing, scans, scans for the second time, sweeps for the third time for the first time It is 60-150g/t to choose penta xanthate dosage;Terpenic oil dosage is 20-100g/t in first time roughing, loose in second of roughing Alcohol oil dosage is 20~50g/t, and it is 10-25g/t to scan, scan for the second time for the first time, scanning middle terpenic oil dosage for the third time.
CN201711164099.9A 2017-11-21 2017-11-21 The method for improving high shale content cupric oxide ore mineral processing index Pending CN107737667A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201711164099.9A CN107737667A (en) 2017-11-21 2017-11-21 The method for improving high shale content cupric oxide ore mineral processing index

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201711164099.9A CN107737667A (en) 2017-11-21 2017-11-21 The method for improving high shale content cupric oxide ore mineral processing index

Publications (1)

Publication Number Publication Date
CN107737667A true CN107737667A (en) 2018-02-27

Family

ID=61238957

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201711164099.9A Pending CN107737667A (en) 2017-11-21 2017-11-21 The method for improving high shale content cupric oxide ore mineral processing index

Country Status (1)

Country Link
CN (1) CN107737667A (en)

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5073253A (en) * 1990-07-11 1991-12-17 Phillips Petroleum Company Froth level measurement
CN101293194A (en) * 2008-06-24 2008-10-29 株洲市兴民科技有限公司 Method and technique for eliminating particle surface envelope in solution with ultrasound wave, and uses
CN102688807A (en) * 2012-06-19 2012-09-26 昆明理工大学 Floatation method for carrying out temperature control and mud suppression on mixed copper ore with high oxygenation rate and high mud content
CN102896047A (en) * 2012-10-08 2013-01-30 湖南有色金属研究院 Method for beneficiating high-peat copper sulphide ore
CN105935631A (en) * 2016-04-13 2016-09-14 中国矿业大学 Efficient desliming method for low-grade argillaceous zinc oxide ores
CN106492982A (en) * 2016-10-19 2017-03-15 湖南有色金属研究院 Copper-molybdenum bulk concentrate ultrasound wave disperses magnetic separation separating technology

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5073253A (en) * 1990-07-11 1991-12-17 Phillips Petroleum Company Froth level measurement
CN101293194A (en) * 2008-06-24 2008-10-29 株洲市兴民科技有限公司 Method and technique for eliminating particle surface envelope in solution with ultrasound wave, and uses
CN102688807A (en) * 2012-06-19 2012-09-26 昆明理工大学 Floatation method for carrying out temperature control and mud suppression on mixed copper ore with high oxygenation rate and high mud content
CN102896047A (en) * 2012-10-08 2013-01-30 湖南有色金属研究院 Method for beneficiating high-peat copper sulphide ore
CN105935631A (en) * 2016-04-13 2016-09-14 中国矿业大学 Efficient desliming method for low-grade argillaceous zinc oxide ores
CN106492982A (en) * 2016-10-19 2017-03-15 湖南有色金属研究院 Copper-molybdenum bulk concentrate ultrasound wave disperses magnetic separation separating technology

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
陈广等: "难选氧化铜矿的超声波助浸研究", 《有色金属(冶炼部分)》 *

Similar Documents

Publication Publication Date Title
CN103240185B (en) Novel lepidolite flotation method
CN105013603B (en) A kind of beneficiation method of copper nickel sulfide mineral
CN103495506B (en) A kind of medicament for iron ore reverse flotation and combinationally use method
CN102489407B (en) Mineral processing method for recycling scheelite/molybdenum oxide ores from molybdenum sulfide flotation tailings
CN104226461B (en) The beneficiation method of comprehensive recovery of gold zinc sulfur ferrum from discarded tailing
CN103551255B (en) Molybdenum oxide ore flotation collecting agent and using method
CN106000655B (en) A kind of method of selected scheelite under room temperature
CN104888947B (en) The magnetic separation of fine grain teeth cloth magnetic-red composite ore-centrifuge sorting process
CN102909124B (en) Iron-increasing and silicon-reducing reselection technique for mixed-type lean iron ore tailings
CN103418488A (en) Comprehensive recovery process of lithium polymetallic ore associated with fine niobium and tantalum
CN101972705A (en) Benefication method for copper nickel
CN103301950A (en) Combined cationic collector for reverse flotation desilication of hematite stone
CN103495509B (en) Micro-fine particle iron ore reverse flotation reagent and use method thereof
CN110339945B (en) Flotation separation method of copper-molybdenum bulk concentrate containing hydrophobic gangue micro-fine particles
CN107282312A (en) A kind of fine copper-sulphide ores sorting process of disseminated grain size
CN108380397A (en) A kind of recovery method of low concentration calcite type containing mica fluorite tailing
CN107638959A (en) Flotation method for inhibiting silicate gangue minerals in fluorite ores
CN110773313A (en) Environment-friendly efficient separation process of high-sulfur lead-zinc ore
CN107282287A (en) A kind of recycling water utilization method before copper-molybdenum Xuan Chang factories
CN104984835A (en) Selective flocculation-column flotation recovery method and system of micro-fine particle molybdenum cleaner tailings
CN104148163A (en) Beneficiation method for processing low grade tin-lead-zinc multi-metal oxidized ores
CN108043573A (en) Copper-molybdenum bulk concentrate magnetic separation-ultrasonic wave reagent removal-FLOTATION SEPARATION ore-dressing technique
CN201291151Y (en) Novel device for recovering iron ore in flotation tailings
CN110369121A (en) Screening-gravity separation technology is added before phosphorus ore direct flotation operation
CN107638949A (en) Application of the cation etherification starch in Scheelite Flotation

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
RJ01 Rejection of invention patent application after publication

Application publication date: 20180227

RJ01 Rejection of invention patent application after publication