CN105880007A - Separation method for tennantite and galena - Google Patents
Separation method for tennantite and galena Download PDFInfo
- Publication number
- CN105880007A CN105880007A CN201610214421.3A CN201610214421A CN105880007A CN 105880007 A CN105880007 A CN 105880007A CN 201610214421 A CN201610214421 A CN 201610214421A CN 105880007 A CN105880007 A CN 105880007A
- Authority
- CN
- China
- Prior art keywords
- galena
- tennantite
- concentrate
- inflation
- lead
- 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
Links
Classifications
-
- 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
- B03B—SEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
- B03B7/00—Combinations of wet processes or apparatus with other processes or apparatus, e.g. for dressing ores or garbage
-
- 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
- B03D2201/06—Depressants
Landscapes
- Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
Abstract
The invention discloses a separation method for tennantite and galena. The method includes the following steps that firstly, inflation and regrinding are conducted; secondly, lead concentrates A are obtained through screening and classifying; thirdly, chemical agent adding and size mixing are conducted; and fourthly, fast flotation separation is conducted so that lead concentrates B and tennantite concentrates can be obtained through floatation. By means of the method, selective ore grinding of the tennantite and the galena is achieved through inflation and regrinding, acid LR serves as the inhibitor of the galena, a beneficiation effect is good, high efficiency and environment friendliness are achieved, and the tennantite and the galena can be effectively separated.
Description
Technical field
The invention belongs to Copper-lead mixed concentrate separation ore-sorting field, be specifically related to the separation method of a kind of tennantite and galena.
Background technology
The Mineral separation of Copper-lead mixed concentrate is the most all the popular research direction of dresser author, the most both at home and abroad for copper
The research that lead separates is primarily referred to as Chalkopyrite and separates with galena, and less with the Separation Research of galena to tennantite.
Owing to having difficult floating easily suppression for tennantite relatively Chalkopyrite, therefore black to being associated with arsenic in production practices in early days
The copper of copper mine, lead ore mainly use the method for bulk flotation to obtain a Copper-lead mixed concentrate, then to bulk concentrate by adding
The Severely poisonous reagents such as cyanide carry out pressing down copper and float lead sorting, it is achieved copper, the separation of lead minerals.Continuous recently as environmental protection pressure
Strengthening, this method is gradually pressed down lead and floats copper method and replace, and presses down lead and floats copper and mainly use CMC, starch or bichromate conduct
The inhibitor of galena, but these inhibitor also have good inhibiting effect to tennantite, therefore for higher containing tennantite
Copper-lead mixed concentrate for, its separation index is the most not ideal enough.Therefore, find a kind of environmental protection, efficient tennantite with
The Mineral separation method of galena has the most positive realistic meaning.
Summary of the invention
Present invention solves the technical problem that and be, use inflation to regrind and achieve the selective milling of tennantite and galena;Pass through
Dongting Lake phragmites communis carboxymethyl cellulose and other medicament are carried out interworking, improvement, it is thus achieved that a kind of selectivity preferably modification has
Machine acidity LR inhibitor, it is achieved that the Selective depression to galena;Sieve classification fast-flotation of inflation being regrinded separates
Technique combines, and have effectively achieved the high efficiency separation of tennantite and galena.
In order to reach to solve the purpose of above-mentioned technical problem, the concrete technical scheme that the present invention provides is:
Described tennantite comprises the following steps with the separation method of galena:
(1) inflation is regrinded: is imported in ball mill by Copper-lead mixed concentrate (tennantite and the mixing sample ore of galena), fills
Enter the air of 1 3MPa pressure, ore grinding, abrasive material again must be inflated;Described inflation regrinds material middling particle particle diameter≤0.074mm's
Ore particle accounts for more than the 70% of ore particle gross mass;
(2) sieve classification: material of inflation being regrinded imports high frequency shale shaker and carries out classification, and undersize material is as lead concentrate A, sieve
Upper material enters dosing and sizes mixing operation;
(3) dosing is sized mixing: on-the-sieve material importing agitator step (2) obtained carries out dosing and sizes mixing, at agitator entrance
Place calculates acid LR inhibitor 80 200g of addition by ore pulp amount per ton and obtains dosing ore pulp material;Described acid LR inhibitor
By sulphuric acid and LS mass ratio 1:(3~5 in mass ratio) form, described LS is by sodium radio-phosphate,P-32 solution and carboxymethyl cellulose
1:(1 in mass ratio~6) composition;
(4) fast-flotation separates: dosing ore pulp material step (3) obtained imports pneumatic flotation cell and carries out one section quickly
FLOTATION SEPARATION, the froth pulp of flotation is the black copper concentrate of arsenic, and the material of flotation device bottom land is lead concentrate B;The lead concentrate that will obtain
A mixes as lead concentrate with lead concentrate B, it is achieved tennantite separates with galena.
Preferably, step (2) described high frequency shale shaker is 0.04mm high frequency shale shaker.Described acid LR inhibitor is by sulfur
Acid with LS 1:(3 in mass ratio~5) at normal temperatures stir be obtained by mixing;Described LS is fine with carboxymethyl by sodium radio-phosphate,P-32 solution
Dimension element 1:(1 in mass ratio~6) stir at 45~65 DEG C and be obtained by mixing;Described methylcellulose is with Lake Dongting area, Hunan
The phragmites communis of growth is that raw material fawns light yellow fibrous sprills prepared by method technique through water, and its molecular formula is:
C6H7O2(OH)2.5(OCH2COONa)1/2]70。
The separation principle of the present invention is: Copper-lead mixed concentrate through inflation regrind after make sieve classification operation feeding granularity reach-
0.074mm grade is more than more than 70%, it is ensured that the monomer dissociation between each mineral, and achieves the selection of part galena
Property fine grinding purpose, then to material use high-frequency screen carry out classification, it is thus achieved that screening product (undersize material) be lead concentrate
A, then adds acid LR inhibitor and sizes mixing for on-the-sieve material, and this inhibitor is a kind of interworking mixed solution, in strong acid
Property, in ore pulp, it mutually firmly can cover at its table after absorption after preferentially surface to galena carries out pickling and between galena
Face, the carboxyl in LR has the strongest hydrophilic simultaneously, and between the hydrone in itself and ore pulp, mutually absorption forms hydrogen bond and forms
Closing, the chemical bond energy powerful by material itself makes galena hydrophilic and suppressed, and tennantite is owing to containing arsenic in crystal, its
Before pulp potential system does not occurs significantly to reverse, and can not associate between inhibitor, float under bubble,
Tennantite and galena is made to obtain high efficiency separation.
The invention has the beneficial effects as follows, the stable in properties of acid LR inhibitor, and the inflation used is regrinded sieve classification
Fast-flotation separating technology flow process is reasonable, and ore dressing is effective, with low cost, it is achieved that tennantite effectively divides with galena
From.
In a word, the present invention uses inflation sieve classification fast-flotation of regrinding to separate and acid LR inhibitor method, has preferably
Adaptability, it is achieved that the high efficiency separation of tennantite and galena, inflation regrinding process can preferably realize to tennantite with
The selective milling of galena, acid LR inhibitor can realize the Selective depression to galena in fast-flotation operation.
The present invention has good stability, strong adaptability, the feature of medicament high-efficiency environment friendly concurrently.
Detailed description of the invention
The acid LR inhibitor that the present embodiment uses is by sulphuric acid and LS mass ratio 1:(3~5 in mass ratio) stir at normal temperatures
Mix and be obtained by mixing;LS is by sodium radio-phosphate,P-32 solution and carboxymethyl cellulose 1:(1 in mass ratio~6) stir at 45~65 DEG C and mix
Close and obtain;Methylcellulose is that the phragmites communis grown with Lake Dongting area, Hunan fawns light yellow fibrous prepared by method technique for raw material through water
Sprills, its molecular formula is: C6H7O2(OH)2.5(OCH2COONa)1/2]70。
Present embodiments provide a kind of from Copper-lead mixed concentrate the mixing sample ore of galena (tennantite with) separate tennantite
The method of concentrate and lead concentrate, specifically includes following steps:
(1) inflation is regrinded: is imported in ball mill by Copper-lead mixed concentrate (tennantite and the mixing sample ore of galena), fills
Enter the air of 1 3MPa pressure, ore grinding, abrasive material again must be inflated;Described inflation regrinds material middling particle particle diameter≤0.074mm's
Ore particle accounts for more than the 70% of ore particle gross mass;
(2) sieve classification: material of inflation being regrinded imports 0.04mm high frequency shale shaker and carries out classification, and undersize material is as lead essence
Ore deposit A, on-the-sieve material enters dosing and sizes mixing operation;
(3) dosing is sized mixing: on-the-sieve material importing agitator step (2) obtained carries out dosing and sizes mixing, at agitator entrance
Place calculates acid LR inhibitor 80 200g of addition by ore pulp amount per ton and obtains dosing ore pulp material;Described acid LR inhibitor
By sulphuric acid and LS 1:(3 in mass ratio~5) form, described LS is by quality by sodium radio-phosphate,P-32 solution and carboxymethyl cellulose
Than 1:(1~6) composition;
(4) fast-flotation separates: dosing ore pulp material step (3) obtained imports pneumatic flotation cell and carries out one section quickly
FLOTATION SEPARATION, the froth pulp of flotation is the black copper concentrate of arsenic, and the material of flotation device bottom land is lead concentrate B;The lead concentrate that will obtain
A mixes as lead concentrate with lead concentrate B, it is achieved tennantite separates with galena.
With the Copper-lead mixed concentrate of the present invention is directed to account for total copper mineral containing tennantite more than 90%, select acid LR inhibitor
Cu-Pb separation ore dressing controlled trial is carried out with the suppression of known macromolecular compound, bichromate inhibitor with described beneficiation method,
Result of the test is shown in Table 1.
Cu-Pb separation ore dressing comparative test result under table 1 Copper-lead mixed concentrate difference inhibitor
Knowable to the comparative test result of table 1, use the medicament of the present invention to separate with described beneficiation method in the copper concentrate obtained and contain
Cu is 20.53%, and the response rate is 93.99%, and containing Pb 50.67% in lead concentrate, the response rate is 95.69%, relatively other separation side
The corresponding index of method is the most excellent.
Claims (3)
1. a tennantite and the separation method of galena, it is characterised in that said method comprising the steps of:
(1) inflation is regrinded: is imported by Copper-lead mixed concentrate in ball mill, is filled with the air of 1 3MPa pressure, ore grinding, obtains inflation
Abrasive material again;Described inflation is regrinded and is expected that the ore particle of middling particle particle diameter≤0.074mm accounts for more than the 70% of ore particle gross mass;
(2) sieve classification: material of inflation being regrinded imports high frequency shale shaker and carries out classification, and undersize material is as lead concentrate A, oversize
Material enters dosing and sizes mixing operation;
(3) dosing is sized mixing: on-the-sieve material importing agitator step (2) obtained carries out dosing and sizes mixing, and presses in agitator porch
Ore pulp amount per ton calculates acid LR inhibitor 80 200g of addition and obtains dosing ore pulp material;Described acid LR inhibitor be by
Sulphuric acid and LS mass ratio 1:(3~5 in mass ratio) composition, described LS be by sodium radio-phosphate,P-32 solution with carboxymethyl cellulose by matter
Amount is than 1:(1~6) composition;
(4) fast-flotation separates: dosing ore pulp material step (3) obtained imports pneumatic flotation cell and carries out one section of fast-flotation
Separating, the froth pulp of flotation is the black copper concentrate of arsenic, and the material of flotation device bottom land is lead concentrate B;By obtain lead concentrate A with
Lead concentrate B mixes as lead concentrate, it is achieved tennantite separates with galena.
2. the method for claim 1, it is characterised in that step (2) described high frequency shale shaker is 0.04mm dither
Sieve.
3. the method for claim 1, it is characterised in that described acid LR inhibitor is by sulphuric acid and LS in mass ratio 1:
(3~5) are stirred at normal temperatures and are obtained by mixing;Described LS is by sodium radio-phosphate,P-32 solution and carboxymethyl cellulose in mass ratio 1:
(1~6) are stirred at 45~65 DEG C and are obtained by mixing;Described carboxymethyl cellulose is prepared by Dongting Lake phragmites communis.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201610214421.3A CN105880007B (en) | 2016-04-08 | 2016-04-08 | A kind of separation method of tennantite and galena |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201610214421.3A CN105880007B (en) | 2016-04-08 | 2016-04-08 | A kind of separation method of tennantite and galena |
Publications (2)
Publication Number | Publication Date |
---|---|
CN105880007A true CN105880007A (en) | 2016-08-24 |
CN105880007B CN105880007B (en) | 2018-03-06 |
Family
ID=57012764
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201610214421.3A Active CN105880007B (en) | 2016-04-08 | 2016-04-08 | A kind of separation method of tennantite and galena |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN105880007B (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106513182A (en) * | 2016-09-30 | 2017-03-22 | 青海省地质矿产测试应用中心 | Beneficiation method for arsenic-containing lead sulfide ore |
CN109201311A (en) * | 2018-08-14 | 2019-01-15 | 湖南埃铝环保科技有限公司 | A kind of high-sulphur alumyte desulfuration method |
CN111195563A (en) * | 2020-01-10 | 2020-05-26 | 昆明理工大学 | Preparation method and application method of inhibitor for separation of tennantite and chalcopyrite |
CN112973970A (en) * | 2021-03-02 | 2021-06-18 | 驰宏科技工程股份有限公司 | Method for removing arsenic in lead concentrate |
CN114798182A (en) * | 2022-04-22 | 2022-07-29 | 深圳市中金岭南有色金属股份有限公司 | Activating agent for improving floating rate of tennantite and application method thereof |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20080067112A1 (en) * | 2006-09-20 | 2008-03-20 | Kuhn Martin C | Methods for the recovery of molybdenum |
CN101775507A (en) * | 2010-02-26 | 2010-07-14 | 中钢矿业开发有限公司 | Extraction method for extracting vanadium pentoxide from low grade oxidized type navajoite |
CN102527498A (en) * | 2011-12-31 | 2012-07-04 | 元阳县华西黄金有限公司 | Non-cyanide ore dressing method for gold-copper-lead sulfide ore |
CN104289319A (en) * | 2008-07-25 | 2015-01-21 | 塞特克技术公司 | Flotation reagents and flotation processes utilizing same |
CN104785377A (en) * | 2015-05-06 | 2015-07-22 | 广西大学 | Preparation method for tennantite inhibitor |
CN105057072A (en) * | 2015-09-02 | 2015-11-18 | 云南华联锌铟股份有限公司 | Comprehensive recovery technology of multi-metal low-grade ore and ore-bearing waste rock resources thereof |
-
2016
- 2016-04-08 CN CN201610214421.3A patent/CN105880007B/en active Active
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20080067112A1 (en) * | 2006-09-20 | 2008-03-20 | Kuhn Martin C | Methods for the recovery of molybdenum |
CN104289319A (en) * | 2008-07-25 | 2015-01-21 | 塞特克技术公司 | Flotation reagents and flotation processes utilizing same |
CN101775507A (en) * | 2010-02-26 | 2010-07-14 | 中钢矿业开发有限公司 | Extraction method for extracting vanadium pentoxide from low grade oxidized type navajoite |
CN102527498A (en) * | 2011-12-31 | 2012-07-04 | 元阳县华西黄金有限公司 | Non-cyanide ore dressing method for gold-copper-lead sulfide ore |
CN104785377A (en) * | 2015-05-06 | 2015-07-22 | 广西大学 | Preparation method for tennantite inhibitor |
CN105057072A (en) * | 2015-09-02 | 2015-11-18 | 云南华联锌铟股份有限公司 | Comprehensive recovery technology of multi-metal low-grade ore and ore-bearing waste rock resources thereof |
Non-Patent Citations (1)
Title |
---|
S.布拉托维奇等: "秘鲁劳拉选矿厂新铜铅分离法的研究和应用", 《国外金属矿选矿》 * |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106513182A (en) * | 2016-09-30 | 2017-03-22 | 青海省地质矿产测试应用中心 | Beneficiation method for arsenic-containing lead sulfide ore |
CN109201311A (en) * | 2018-08-14 | 2019-01-15 | 湖南埃铝环保科技有限公司 | A kind of high-sulphur alumyte desulfuration method |
CN111195563A (en) * | 2020-01-10 | 2020-05-26 | 昆明理工大学 | Preparation method and application method of inhibitor for separation of tennantite and chalcopyrite |
CN112973970A (en) * | 2021-03-02 | 2021-06-18 | 驰宏科技工程股份有限公司 | Method for removing arsenic in lead concentrate |
CN114798182A (en) * | 2022-04-22 | 2022-07-29 | 深圳市中金岭南有色金属股份有限公司 | Activating agent for improving floating rate of tennantite and application method thereof |
Also Published As
Publication number | Publication date |
---|---|
CN105880007B (en) | 2018-03-06 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
AU2020336795B2 (en) | Pyrrhotite mineral processing method using low-alkali process of flotation followed by magnetic separation | |
CN105268559B (en) | The beneficiation method of low-grade copper sulfide ores | |
CN105880007A (en) | Separation method for tennantite and galena | |
CN102744151B (en) | Branch flotation technology for silicon calcium collophanite | |
CN107694762B (en) | A kind of composition and method for floating of the flotation collecting rutile from ore | |
CN103736569B (en) | A kind of beneficiation method of sulphide ore | |
CN101850295A (en) | Beneficiation method for producing high-quality iron ore concentrate by low-grade magnetic iron ore | |
CN108380397A (en) | A kind of recovery method of low concentration calcite type containing mica fluorite tailing | |
CN110292983A (en) | Beneficiation method containing golden secondary copper sulfide mineral | |
CN101985111A (en) | Copper-sulfur ore separation method | |
CN105013616B (en) | A kind of method that molybdenum concntrate and lead iron concentrate are separated in the lead sulfide mixed concentrate from molybdenum | |
CN102527498A (en) | Non-cyanide ore dressing method for gold-copper-lead sulfide ore | |
CN104128244B (en) | Method for recycling iron ore concentrate from iron tailings and obtained iron ore concentrate | |
CN107812617A (en) | One kind improves the difficult copper sulfide ore beneficiation of microfine and refers to calibration method | |
CN109604071A (en) | It is a kind of to reduce the stanniferous method for floating of troilite | |
CN107638949A (en) | Application of the cation etherification starch in Scheelite Flotation | |
CN108325756A (en) | A kind of barite beneficiation method rich in calcite and witherite | |
CN106861922A (en) | A kind of beneficiation method of zinc sulfide ore | |
CN106733220B (en) | A kind of zinc oxide ore slurry bubble sorting ore-dressing technique | |
CN117000434A (en) | Lepidolite collector and mineral separation method adopting lepidolite collector | |
CN107335531A (en) | A kind of method of separation by shaking table phosphorus ore | |
CN111841870A (en) | Energy-saving and environment-friendly ultra-pure fine iron powder continuous production process | |
CN108855586B (en) | Combined unit for coal flotation | |
CN1814354A (en) | Re-dressing utilizing method for non-ferrous metal tailings | |
CN107413534A (en) | Coarse grain flotation machine |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant |