CN111558463A - Combined collecting agent for improving molybdenum recovery rate of low-copper high-molybdenum ore and application process thereof - Google Patents

Combined collecting agent for improving molybdenum recovery rate of low-copper high-molybdenum ore and application process thereof Download PDF

Info

Publication number
CN111558463A
CN111558463A CN202010348236.XA CN202010348236A CN111558463A CN 111558463 A CN111558463 A CN 111558463A CN 202010348236 A CN202010348236 A CN 202010348236A CN 111558463 A CN111558463 A CN 111558463A
Authority
CN
China
Prior art keywords
molybdenum
copper
low
recovery rate
concentrate
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
CN202010348236.XA
Other languages
Chinese (zh)
Other versions
CN111558463B (en
Inventor
杨俊龙
郭艳华
郭海宁
赵天岩
胡延明
包玺琳
苗梁
罗刚
彭贵熊
李福兰
郭臻雅
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.)
Northwest Research Institute of Mining and Metallurgy
Original Assignee
Northwest Research Institute of Mining and Metallurgy
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 Northwest Research Institute of Mining and Metallurgy filed Critical Northwest Research Institute of Mining and Metallurgy
Priority to CN202010348236.XA priority Critical patent/CN111558463B/en
Publication of CN111558463A publication Critical patent/CN111558463A/en
Application granted granted Critical
Publication of CN111558463B publication Critical patent/CN111558463B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

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
    • B03DFLOTATION; DIFFERENTIAL SEDIMENTATION
    • B03D1/00Flotation
    • B03D1/001Flotation agents
    • B03D1/004Organic compounds
    • B03D1/008Organic compounds containing oxygen
    • 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
    • B03D1/02Froth-flotation processes
    • 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
    • B03D1/08Subsequent treatment of concentrated product
    • 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
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

Landscapes

  • Chemical & Material Sciences (AREA)
  • Dispersion Chemistry (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Abstract

The invention relates to a combined collecting agent for improving the molybdenum recovery rate of low-copper high-molybdenum ores and an application process thereof, wherein the combined collecting agent is prepared from the following raw materials in parts by weight: 2-5 ℃ higher than 220 ℃ of fractionation grade kerosene; 1-2 parts of heavy wax; 2-3 parts of motor oil; 1-2 parts of tricyclic aromatic hydrocarbon; and v, 1-3% of fatty acid polyethylene alcohol ester as an emulsifier. The method has the advantages of simple process flow, strong applicability, low production cost, high molybdenum recovery rate and easy industrial popularization; the novel combined collecting agent which has good stability, a certain amount of aromatic hydrocarbons with large molecules, high viscosity, easy adsorption of coarse-grained ore and strong collecting capacity is synthesized after the emulsifier is adopted for emulsification, and the recovery rate of molybdenum in the low-copper high-molybdenum ore can be effectively improved. The application process comprises the steps of copper-molybdenum mixed flotation, copper-molybdenum separation, molybdenum rough concentrate concentration and the like by adding the combined collecting agent, so that copper concentrate and molybdenum concentrate with better indexes are finally obtained, and the high-efficiency recovery of molybdenum in low-copper high-molybdenum ores can be realized.

Description

Combined collecting agent for improving molybdenum recovery rate of low-copper high-molybdenum ore and application process thereof
Technical Field
The invention belongs to the technical field of mineral processing, and particularly relates to a combined collecting agent for improving the molybdenum recovery rate of low-copper high-molybdenum ores and an application process thereof.
Background
The molybdenum resource in China is very abundant, the reserve of the molybdenum resource accounts for about 25 percent of the total reserve of the molybdenum in the world, is second only to the United states and second in the world, and is one of six dominant mineral resources in China. Copper-molybdenum ore is one of the main sources for obtaining molybdenum concentrate, and countries handling copper-molybdenum ore abroad mainly include the united states, canada, chile and the like. The consumption of copper and molybdenum ore resources in China is large, and the development and utilization significance of low-grade copper and molybdenum ores is enhanced.
In the existing production process of low-copper high-molybdenum ore, the ore grinding fineness can not meet the requirement, so that the ore particles are thicker; meanwhile, because the copper content of the low-copper high-molybdenum ore is lower, the yield is lower during copper-molybdenum mixed flotation, and the problems of higher molybdenum content in tailings, low molybdenum recovery rate and the like exist.
Disclosure of Invention
The invention aims to solve the technical problem of the prior art and provides a combined collector which has better stability and strong collecting capability and can improve the molybdenum recovery rate of low-copper high-molybdenum ores and an application process thereof. The molybdenum in the low-copper high-molybdenum ore is recovered to the maximum extent. Carrying out copper and molybdenum mixed roughing, concentration and copper and molybdenum separation by adopting a combined collecting agent to obtain copper concentrate, and obtaining molybdenum concentrate after molybdenum concentration.
The invention relates to a combined collecting agent for improving the molybdenum recovery rate of low-copper high-molybdenum ores, which is characterized by being prepared from the following raw materials in parts by weight: 2-5 ℃ higher than 220 ℃ of fractionation grade kerosene; 1-2 parts of heavy wax; 2-3 parts of motor oil; 1-2 parts of tricyclic aromatic hydrocarbon; and v, 1-3% of fatty acid polyethylene alcohol ester as an emulsifier.
In the technical scheme of the combined collector for improving the molybdenum recovery rate of the low-copper high-molybdenum ore, the further preferable technical scheme is characterized in that:
1. the feed is prepared from the following raw materials in parts by weight: fractionation grade kerosene 2 above 220 ℃; 1 part of heavy wax; motor oil 2; a tricyclic aromatic hydrocarbon 1; emulsifier v fatty acid polyglycol ester 1;
2. the feed is prepared from the following raw materials in parts by weight: fractionation grade kerosene 5 above 220 ℃; heavy wax 2; motor oil 3; a tricyclic aromatic hydrocarbon 2; emulsifier v fatty acid polyethylene alcohol ester 3;
3. the feed is prepared from the following raw materials in parts by weight: 3.5 of fraction grade kerosene with the temperature higher than 220 ℃; 1.5 parts of heavy wax; 2.5 parts of motor oil; tricyclic aromatic hydrocarbon 1.5; emulsifier v fatty acid polyethylene alcohol ester 2.
The invention relates to an application process of a combined collecting agent for improving the molybdenum recovery rate of low-copper high-molybdenum ores, which is characterized by comprising the following steps of: grinding: grinding raw ore, wherein the content of the ground ore with the fineness of less than 0.074mm is 50% -60%, the grinding concentration is 50-60%, and a regulator is added during grinding, wherein the addition amount is 0-1000 g/t; ② copper molybdenum mixed flotation: adding a combined collecting agent into the ore pulp with the mass percentage concentration of 30-35% prepared in the step I, wherein the using amount of the combined collecting agent is 90-120 g/t, performing primary roughing and scavenging, and performing blank concentration twice to obtain copper-molybdenum mixed concentrate and tailings; ③ separating copper and molybdenum: after the copper-molybdenum bulk concentrate obtained in the second step is subjected to size mixing, adding a copper inhibitor, namely water glass and sodium sulfide, in a ratio of 1:4 and a dosage of 1500-1800 g/t, adding a combined collecting agent in a dosage of 50-60 g/t to perform copper-molybdenum separation, and obtaining copper concentrate and molybdenum rough concentrate; fourthly, molybdenum selection: and c, adding inhibitor water glass and sodium sulfide in a ratio of 1:2 after the molybdenum rough concentrate obtained in the step c is subjected to size mixing, wherein the using amount is 100-300 g/t, and carrying out concentration on the molybdenum rough concentrate to obtain molybdenum concentrate.
In the technical scheme of the combined collector for improving the molybdenum recovery rate of the low-copper high-molybdenum ore, the further preferable technical scheme is characterized in that:
1. the ore grinding fineness of 55% is less than 0.074 mm;
2. and the molybdenum rough concentrate concentration times are three times.
Compared with the prior art, the invention has the beneficial effects that: (1) the combined collector provided by the invention is obtained by emulsifying multiple single collectors, has the advantages of good stability, high viscosity, a certain amount of macromolecular aromatic hydrocarbon, easy adsorption of coarser granular ore and strong collecting capability, and can effectively improve the recovery rate of molybdenum in low-copper high-molybdenum ore; (2) the method has the advantages of simple process flow, less times of molybdenum rough concentrate concentration and effective saving of production cost. The method has the advantages of simple process flow, strong applicability, low production cost, high molybdenum recovery rate, easy industrial popularization and capability of realizing the high-efficiency recovery of molybdenum in low-copper high-molybdenum ores.
Drawings
FIG. 1 is a process flow diagram of the present invention.
Detailed Description
The following will clearly and completely describe the technical solutions in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
Example 1, a combined collector for improving the molybdenum recovery rate of low-copper high-molybdenum ores is prepared from the following raw materials in parts by weight: 2-5 ℃ higher than 220 ℃ of fractionation grade kerosene; 1-2 parts of heavy wax; 2-3 parts of motor oil; 1-2 parts of tricyclic aromatic hydrocarbon; and v, 1-3% of fatty acid polyethylene alcohol ester as an emulsifier.
Example 2, the combined collector for improving the molybdenum recovery rate of low-copper high-molybdenum ore according to example 1 is prepared from the following raw materials in parts by weight: fractionation grade kerosene 2 above 220 ℃; 1 part of heavy wax; motor oil 2; a tricyclic aromatic hydrocarbon 1; emulsifier v fatty acid polyethylene alcohol ester 1.
Example 3, the combined collector for improving the molybdenum recovery rate of low-copper high-molybdenum ore according to example 1 or 2 is prepared from the following raw materials in parts by weight: fractionation grade kerosene 5 above 220 ℃; heavy wax 2; motor oil 3; a tricyclic aromatic hydrocarbon 2; emulsifier v fatty acid polyethylene alcohol ester 3.
Example 4, the combined collector for improving the molybdenum recovery rate of low-copper high-molybdenum ore according to example 1 or 2 or 3 is prepared from the following raw materials in parts by weight: 3.5 of fraction grade kerosene with the temperature higher than 220 ℃; 1.5 parts of heavy wax; 2.5 parts of motor oil; tricyclic aromatic hydrocarbon 1.5; emulsifier v fatty acid polyethylene alcohol ester 2.
Example 5, an application process of a combined collector for improving the molybdenum recovery rate of low-copper high-molybdenum ores comprises the following steps: grinding: grinding raw ore, wherein the content of the ground ore with the fineness of less than 0.074mm is 50% -60%, the grinding concentration is 50-60%, and a regulator is added during grinding, wherein the addition amount is 0-1000 g/t; ② copper molybdenum mixed flotation: adding a combined collecting agent into the ore pulp with the mass percentage concentration of 30-35% prepared in the step I, wherein the using amount of the combined collecting agent is 90-120 g/t, performing primary roughing and scavenging, and performing blank concentration twice to obtain copper-molybdenum mixed concentrate and tailings; ③ separating copper and molybdenum: after the copper-molybdenum bulk concentrate obtained in the second step is subjected to size mixing, adding a copper inhibitor, namely water glass and sodium sulfide, in a ratio of 1:4 and a dosage of 1500-1800 g/t, adding a combined collecting agent in a dosage of 50-60 g/t to perform copper-molybdenum separation, and obtaining copper concentrate and molybdenum rough concentrate; fourthly, molybdenum selection: and c, adding inhibitor water glass and sodium sulfide in a ratio of 1:2 after the molybdenum rough concentrate obtained in the step c is subjected to size mixing, wherein the using amount is 100-300 g/t, and carrying out concentration on the molybdenum rough concentrate to obtain molybdenum concentrate. The middling is also added after the molybdenum rough concentrate is refined; the regulator is lime. According to the invention, the emulsifier is adopted to emulsify to synthesize the novel combined collecting agent which has good stability, a certain amount of aromatic hydrocarbons with larger molecules, high viscosity, easiness in adsorbing coarse-grained ore and strong collecting capability, and the recovery rate of molybdenum in the low-copper high-molybdenum ore can be effectively improved.
Example 6, the process of applying the combined collector for improving the molybdenum recovery rate of low-copper high-molybdenum ore according to example 5 comprises the following steps: grinding: grinding the raw ore, wherein the content of the grinding fineness of less than 0.074mm is 50%, the grinding concentration is 50%, and a regulator is added during grinding, wherein the addition amount is 10 g/t; ② copper molybdenum mixed flotation: adding a combined collecting agent into the ore pulp with the mass percentage concentration of 30% prepared in the step I, performing one-time roughing and one-time scavenging, and performing two-time blank concentration to obtain copper-molybdenum bulk concentrate and tailings; ③ separating copper and molybdenum: after the copper-molybdenum bulk concentrate obtained in the second step is subjected to size mixing, adding a copper inhibitor, namely water glass and sodium sulfide, in a ratio of 1:4 and a dosage of 1500g/t, adding a combined collecting agent, and performing copper-molybdenum separation by using a dosage of 50g/t to obtain copper concentrate and molybdenum rough concentrate; fourthly, molybdenum selection: and c, adding inhibitor water glass and sodium sulfide in a ratio of 1:2 after the molybdenum rough concentrate obtained in the step c is subjected to size mixing, wherein the using amount is 100g/t, and carrying out concentration on the molybdenum rough concentrate to obtain molybdenum concentrate.
Example 7, the process of using the combined collector for improving the molybdenum recovery rate of low-copper high-molybdenum ore according to example 5 or 6 comprises the following steps: grinding: grinding raw ore, wherein the content of the grinding fineness is less than 0.074mm and is 60%, the grinding concentration is 60%, and a regulator is added during grinding, wherein the addition amount is 1000 g/t; ② copper molybdenum mixed flotation: adding a combined collecting agent into the ore pulp with the mass percentage concentration of 35% prepared in the step I, performing one-time roughing and one-time scavenging, and performing two-time blank concentration to obtain copper-molybdenum bulk concentrate and tailings; ③ separating copper and molybdenum: after the copper-molybdenum bulk concentrate obtained in the second step is subjected to size mixing, adding a copper inhibitor, namely water glass and sodium sulfide in a ratio of 1:4 and an amount of 1800g/t, adding a combined collecting agent in an amount of 60g/t to perform copper-molybdenum separation, and obtaining copper concentrate and molybdenum rough concentrate; fourthly, molybdenum selection: and c, adding inhibitor water glass and sodium sulfide in a ratio of 1:2 after the molybdenum rough concentrate obtained in the step c is subjected to size mixing, wherein the using amount is 300g/t, and carrying out concentration on the molybdenum rough concentrate to obtain molybdenum concentrate.
Example 8, the process of using the combined collector for improving molybdenum recovery from low-copper high-molybdenum ores according to any one of examples 5 to 7, includes the following steps: grinding: grinding raw ore, wherein the content of the grinding fineness is less than 0.074mm and is 55%, the grinding concentration is 55%, and a regulator is added during grinding, wherein the adding amount is 500 g/t; ② copper molybdenum mixed flotation: adding a combined collecting agent into the ore pulp with the mass percentage concentration of 30-35% prepared in the step I, performing primary roughing and scavenging, and performing blank concentration twice to obtain copper-molybdenum mixed concentrate and tailings, wherein the using amount of the combined collecting agent is 100 g/t; ③ separating copper and molybdenum: after the copper-molybdenum bulk concentrate obtained in the second step is subjected to size mixing, adding a copper inhibitor, namely water glass and sodium sulfide in a ratio of 1:4 and a dosage of 1600g/t, adding a combined collecting agent in a dosage of 55g/t to perform copper-molybdenum separation, and obtaining copper concentrate and molybdenum rough concentrate; fourthly, molybdenum selection: and (4) adding inhibitor water glass and sodium sulfide in a ratio of 1:2 after the molybdenum rough concentrate obtained in the step (III) is subjected to size mixing, wherein the using amount is 200g/t, and carrying out concentration on the molybdenum rough concentrate to obtain molybdenum concentrate.
Example 9, in the application process of the combined collector for improving the molybdenum recovery rate of low-copper high-molybdenum ore according to any one of examples 5 to 8, the ore grinding fineness of the step (i) is less than 0.074mm, and the content of the ore grinding fineness is 55%.
Example 10, the process of using the combined collector for improving the molybdenum recovery rate of low-copper high-molybdenum ore according to any one of examples 5 to 9, wherein the molybdenum rough concentrate concentration time is three times.
Example 11, Xinjiang Soxhlet 1 Point of Low copper and high molybdenum ore, copper content 0.17%, molybdenum content 0.066%, grinding concentration 55%, adding lime 1000g/t during grinding, grinding fineness less than 0.074mm and content 55%. Adjusting the mass percentage concentration of the ore pulp to 32 percent, adding a combined collecting agent, carrying out one-time roughing and one-time scavenging by using 100g/t, and carrying out two-time blank concentration to obtain copper-molybdenum bulk concentrate and tailings. After the copper-molybdenum bulk concentrate is subjected to size mixing, adding a copper inhibitor, namely water glass, and sodium sulfide in a ratio of 1:4 and a dosage of 1500g/t, adding a combined collecting agent A3132, and performing copper-molybdenum separation in a dosage of 55g/t to obtain a copper concentrate and a molybdenum rough concentrate. Adding inhibitor water glass into the obtained molybdenum rough concentrate after size mixing, wherein the proportion of T17 is 1:2, the dosage is 200g/T, and the molybdenum rough concentrate is subjected to concentration for three times to obtain the molybdenum concentrate. Finally, the better indexes of 18.95 percent of copper grade in the copper concentrate, 92.45 percent of copper recovery rate, 49.87 percent of molybdenum grade in the molybdenum concentrate and 70.45 percent of molybdenum recovery rate are obtained.
Example 12, Xinjiang Soxhlet 2 Low-copper high-molybdenum ore, copper content 0.20%, molybdenum content 0.078%, ore grinding concentration 56%, adding lime 800g/t during ore grinding, and grinding fineness less than 0.074mm and content 57%. Adjusting the mass percentage concentration of the ore pulp to be 33 percent, adding the combined collecting agent, carrying out one-time roughing and one-time scavenging by using the amount of 110g/t, and carrying out two-time blank concentration to obtain copper-molybdenum bulk concentrate and tailings. After the copper-molybdenum bulk concentrate is subjected to size mixing, adding a copper inhibitor, namely water glass, and sodium sulfide in a ratio of 1:4 and a dosage of 1600g/t, adding a combined collecting agent A3132 in a dosage of 60g/t, and performing copper-molybdenum separation to obtain a copper concentrate and a molybdenum rough concentrate. Adding inhibitor water glass into the obtained molybdenum rough concentrate after size mixing, wherein the proportion of T17 is 1:2, the dosage is 250g/T, and the molybdenum rough concentrate is subjected to concentration for three times to obtain the molybdenum concentrate. Finally, the better indexes of 18.73 percent of copper grade in the copper concentrate, 93.73 percent of copper recovery rate, 48.31 percent of molybdenum grade in the molybdenum concentrate and 72.98 percent of molybdenum recovery rate are obtained.
Example 13, Xinjiang Soxhlet 3 points of Low copper and high molybdenum ore, copper content 0.15%, molybdenum content 0.060%, grinding concentration 56.5%, adding lime 600g/t during grinding, grinding fineness less than 0.074mm, content 54.5%. Adjusting the mass percentage concentration of the ore pulp to be 33 percent, adding the combined collecting agent, carrying out one-time roughing and one-time scavenging by using the amount of 90g/t, and carrying out two-time blank concentration to obtain copper-molybdenum bulk concentrate and tailings. After the copper-molybdenum bulk concentrate is subjected to size mixing, adding a copper inhibitor, namely water glass, and sodium sulfide in a ratio of 1:4 and a dosage of 1500g/t, adding a combined collecting agent A3132, and performing copper-molybdenum separation in a dosage of 52g/t to obtain a copper concentrate and a molybdenum rough concentrate. Adding inhibitor water glass into the obtained molybdenum rough concentrate after size mixing, wherein the proportion of T17 is 1:2, the dosage is 150g/T, and the molybdenum rough concentrate is subjected to concentration for three times to obtain the molybdenum concentrate. Finally, the better indexes of 18.24 percent of copper grade in the copper concentrate, 91.98 percent of copper recovery rate, 46.42 percent of molybdenum grade in the molybdenum concentrate and 70.22 percent of molybdenum recovery rate are obtained.
The above description is only for the preferred embodiments of the present invention, but the protection scope of the present invention is not limited thereto, and any person skilled in the art can substitute or change the technical solution of the present invention and the inventive concept thereof within the scope of the present invention.

Claims (7)

1. The combined collecting agent for improving the molybdenum recovery rate of the low-copper high-molybdenum ore is characterized by being prepared from the following raw materials in parts by weight: 2-5 ℃ higher than 220 ℃ of fractionation grade kerosene; 1-2 parts of heavy wax; 2-3 parts of motor oil; 1-2 parts of tricyclic aromatic hydrocarbon; and v, 1-3% of fatty acid polyethylene alcohol ester as an emulsifier.
2. The combined collector for improving the molybdenum recovery rate of low-copper high-molybdenum ores according to claim 1, which is prepared from the following raw materials in parts by weight: fractionation grade kerosene 2 above 220 ℃; 1 part of heavy wax; motor oil 2; a tricyclic aromatic hydrocarbon 1; emulsifier v fatty acid polyethylene alcohol ester 1.
3. The combined collector for improving the molybdenum recovery rate of low-copper high-molybdenum ores according to claim 1, which is prepared from the following raw materials in parts by weight: fractionation grade kerosene 5 above 220 ℃; heavy wax 2; motor oil 3; a tricyclic aromatic hydrocarbon 2; emulsifier v fatty acid polyethylene alcohol ester 3.
4. The combined collector for improving the molybdenum recovery rate of low-copper high-molybdenum ores according to claim 1, which is prepared from the following raw materials in parts by weight: 3.5 of fraction grade kerosene with the temperature higher than 220 ℃; 1.5 parts of heavy wax; 2.5 parts of motor oil; tricyclic aromatic hydrocarbon 1.5; emulsifier v fatty acid polyethylene alcohol ester 2.
5. The application process of the combined collecting agent for improving the molybdenum recovery rate of the low-copper high-molybdenum ore is characterized by comprising the following steps of:
grinding: grinding raw ore, wherein the content of the ground ore with the fineness of less than 0.074mm is 50% -60%, the grinding concentration is 50-60%, and a regulator is added during grinding, wherein the addition amount is 0-1000 g/t;
② copper molybdenum mixed flotation: adding a combined collecting agent into the ore pulp with the mass percentage concentration of 30-35% prepared in the step I, wherein the using amount of the combined collecting agent is 90-120 g/t, performing primary roughing and scavenging, and performing blank concentration twice to obtain copper-molybdenum mixed concentrate and tailings;
③ separating copper and molybdenum: after the copper-molybdenum bulk concentrate obtained in the second step is subjected to size mixing, adding a copper inhibitor, namely water glass and sodium sulfide, in a ratio of 1:4 and a dosage of 1500-1800 g/t, adding a combined collecting agent in a dosage of 50-60 g/t to perform copper-molybdenum separation, and obtaining copper concentrate and molybdenum rough concentrate;
fourthly, molybdenum selection: and c, adding inhibitor water glass and sodium sulfide in a ratio of 1:2 after the molybdenum rough concentrate obtained in the step c is subjected to size mixing, wherein the using amount is 100-300 g/t, and carrying out concentration on the molybdenum rough concentrate to obtain molybdenum concentrate.
6. The application process of the combined collector for improving the molybdenum recovery rate of the low-copper high-molybdenum ore according to claim 5, wherein the combined collector comprises the following steps: the content of the grinding fineness of less than 0.074mm in the step I is 55 percent.
7. The application process of the combined collector for improving the molybdenum recovery rate of the low-copper high-molybdenum ore according to claim 2, characterized in that: and the molybdenum rough concentrate concentration times are three times.
CN202010348236.XA 2020-04-28 2020-04-28 Combined collecting agent for improving molybdenum recovery rate of low-copper high-molybdenum ore and application process thereof Active CN111558463B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202010348236.XA CN111558463B (en) 2020-04-28 2020-04-28 Combined collecting agent for improving molybdenum recovery rate of low-copper high-molybdenum ore and application process thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202010348236.XA CN111558463B (en) 2020-04-28 2020-04-28 Combined collecting agent for improving molybdenum recovery rate of low-copper high-molybdenum ore and application process thereof

Publications (2)

Publication Number Publication Date
CN111558463A true CN111558463A (en) 2020-08-21
CN111558463B CN111558463B (en) 2022-05-31

Family

ID=72070575

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202010348236.XA Active CN111558463B (en) 2020-04-28 2020-04-28 Combined collecting agent for improving molybdenum recovery rate of low-copper high-molybdenum ore and application process thereof

Country Status (1)

Country Link
CN (1) CN111558463B (en)

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102744150A (en) * 2012-06-29 2012-10-24 广州有色金属研究院 Beneficiation method for lindgrenite
CN104722409A (en) * 2015-03-24 2015-06-24 四川省冶金地质勘查院 Flotation separation method of low / extra-low grade copper-molybdenum ore or chat
JP2017202481A (en) * 2015-12-24 2017-11-16 国立大学法人九州大学 Beneficiation method
CN110385194A (en) * 2019-07-15 2019-10-29 黑龙江多宝山铜业股份有限公司 A kind of beneficiation method of the copper of the high efficiente callback associated gold rhenium from porphyry copper mine, molybdenum
CN110653074A (en) * 2019-08-19 2020-01-07 西北矿冶研究院 Beneficiation method for treating ores with different properties by using same sorting process

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102744150A (en) * 2012-06-29 2012-10-24 广州有色金属研究院 Beneficiation method for lindgrenite
CN104722409A (en) * 2015-03-24 2015-06-24 四川省冶金地质勘查院 Flotation separation method of low / extra-low grade copper-molybdenum ore or chat
JP2017202481A (en) * 2015-12-24 2017-11-16 国立大学法人九州大学 Beneficiation method
CN110385194A (en) * 2019-07-15 2019-10-29 黑龙江多宝山铜业股份有限公司 A kind of beneficiation method of the copper of the high efficiente callback associated gold rhenium from porphyry copper mine, molybdenum
CN110653074A (en) * 2019-08-19 2020-01-07 西北矿冶研究院 Beneficiation method for treating ores with different properties by using same sorting process

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
胡元等: "铜钼矿的浮选工艺和浮选药剂研究进展", 《云南冶金》 *
赵天岩等: "新疆某铜钼矿提高选矿生产指标技术研究与生产实践", 《现代矿业》 *

Also Published As

Publication number Publication date
CN111558463B (en) 2022-05-31

Similar Documents

Publication Publication Date Title
CN102671769B (en) Beneficiation method for flotation and recovery of molybdenum from easy-floating gangue refractory molybdenum ore
CN111672636A (en) Spodumene ore flotation collector and preparation method and application method thereof
CN102218377B (en) Efficient copper-cobalt oxide ore combination collecting agent and copper oxide ore beneficiation method
CN101507950A (en) Mineral separation process capable of recovering micro scheelite from scheelite flotation tailings
CN111495608A (en) Flotation process for efficiently recovering lead, zinc and sulfur in multi-metal sulfide ore
CN112237985B (en) Method for recovering cassiterite from tin-containing sulfide ore
CN111450987A (en) Mineral separation process for medium-low grade mixed collophanite
CN111250269B (en) Novel collector for flotation of low-grade spodumene ores and spodumene ore dressing method
CN111468302B (en) Beneficiation inhibitor and purification method of molybdenum rough concentrate
CN108262156B (en) Beneficiation method for high-argillaceous and high-alkaline gangue low-grade refractory copper oxide ore
CN103878069A (en) Molybdenite separation method
CN111298978B (en) Method for flotation of lepidolite without desliming
CN111558463B (en) Combined collecting agent for improving molybdenum recovery rate of low-copper high-molybdenum ore and application process thereof
CN112718233A (en) Method for comprehensively recovering copper minerals and iron minerals from copper converter slag
CN113731637B (en) Low-grade mixed collophanite flotation method
CN115155824B (en) Mineral separation method for recovering tin from tin-containing fine mud
CN102773151B (en) Weathered collophanite graded processing technique
CN115814956A (en) Beneficiation method for low-grade spodumene ores
CN112742606B (en) Novel pyrrhotite composite activation agent and application thereof
CN112221719B (en) Method for improving recovery rate of associated gold from low-grade copper-sulfur ore
CN111515026B (en) Method for recovering micro-fine particle pyrite from sulfur-containing slime tailings
CN113976331A (en) Method for preparing high-purity pyrite by flotation mass transfer dynamics regulation
CN111437989A (en) Method for recovering rutile in durite-hectorite product
CN115069424B (en) Alkali-acid exchange flotation gold extraction process for carbonate type gold ore
CN1586729A (en) Process for extracting iron concentrate by sulfuric slag 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
GR01 Patent grant
GR01 Patent grant