CN108160341A - A kind of copper-cobalt ore strengthens the method that suppression copper carries molybdenum - Google Patents
A kind of copper-cobalt ore strengthens the method that suppression copper carries molybdenum Download PDFInfo
- Publication number
- CN108160341A CN108160341A CN201711264954.3A CN201711264954A CN108160341A CN 108160341 A CN108160341 A CN 108160341A CN 201711264954 A CN201711264954 A CN 201711264954A CN 108160341 A CN108160341 A CN 108160341A
- Authority
- CN
- China
- Prior art keywords
- copper
- molybdenum
- concentrate
- ore
- strengthens
- 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
Links
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 title claims abstract description 54
- 239000011733 molybdenum Substances 0.000 title claims abstract description 54
- 229910052750 molybdenum Inorganic materials 0.000 title claims abstract description 54
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 title claims abstract description 37
- 229910052802 copper Inorganic materials 0.000 title claims abstract description 37
- 239000010949 copper Substances 0.000 title claims abstract description 37
- 238000000034 method Methods 0.000 title claims abstract description 22
- RYTYSMSQNNBZDP-UHFFFAOYSA-N cobalt copper Chemical compound [Co].[Cu] RYTYSMSQNNBZDP-UHFFFAOYSA-N 0.000 title claims abstract description 19
- 230000001629 suppression Effects 0.000 title claims description 14
- 239000012141 concentrate Substances 0.000 claims abstract description 44
- 239000006260 foam Substances 0.000 claims abstract description 22
- WUUZKBJEUBFVMV-UHFFFAOYSA-N copper molybdenum Chemical compound [Cu].[Mo] WUUZKBJEUBFVMV-UHFFFAOYSA-N 0.000 claims abstract description 19
- 238000000227 grinding Methods 0.000 claims abstract description 19
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 14
- 238000003801 milling Methods 0.000 claims abstract description 11
- 238000005188 flotation Methods 0.000 claims abstract description 9
- HYHCSLBZRBJJCH-UHFFFAOYSA-M sodium hydrosulfide Chemical compound [Na+].[SH-] HYHCSLBZRBJJCH-UHFFFAOYSA-M 0.000 claims abstract description 9
- 241000530268 Lycaena heteronea Species 0.000 claims abstract description 6
- 239000004215 Carbon black (E152) Substances 0.000 claims description 6
- 229930195733 hydrocarbon Natural products 0.000 claims description 6
- 150000002430 hydrocarbons Chemical class 0.000 claims description 6
- 229910052739 hydrogen Inorganic materials 0.000 claims description 4
- 239000001257 hydrogen Substances 0.000 claims description 4
- 150000003839 salts Chemical class 0.000 claims description 4
- 229910052717 sulfur Inorganic materials 0.000 claims description 4
- 239000011593 sulfur Substances 0.000 claims description 4
- -1 sulfur hydrogen salt Chemical class 0.000 claims description 4
- 229910052500 inorganic mineral Inorganic materials 0.000 abstract description 8
- 239000011707 mineral Substances 0.000 abstract description 8
- 229910001779 copper mineral Inorganic materials 0.000 abstract description 7
- 238000011084 recovery Methods 0.000 abstract description 7
- 238000004064 recycling Methods 0.000 abstract description 5
- 238000000926 separation method Methods 0.000 abstract description 5
- 239000003350 kerosene Substances 0.000 abstract description 4
- 239000010453 quartz Substances 0.000 abstract description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 abstract description 3
- 230000005764 inhibitory process Effects 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- DVRDHUBQLOKMHZ-UHFFFAOYSA-N chalcopyrite Chemical compound [S-2].[S-2].[Fe+2].[Cu+2] DVRDHUBQLOKMHZ-UHFFFAOYSA-N 0.000 description 2
- 229910052951 chalcopyrite Inorganic materials 0.000 description 2
- 238000002161 passivation Methods 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229910052948 bornite Inorganic materials 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- ZOOODBUHSVUZEM-UHFFFAOYSA-N ethoxymethanedithioic acid Chemical compound CCOC(S)=S ZOOODBUHSVUZEM-UHFFFAOYSA-N 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 238000005191 phase separation Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000003014 reinforcing effect Effects 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
- 239000012991 xanthate Substances 0.000 description 1
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
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
- B03D1/02—Froth-flotation processes
-
- 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
- B03B1/00—Conditioning for facilitating separation by altering physical properties of the matter to be treated
-
- 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
- B03D1/002—Inorganic 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
- B03D1/00—Flotation
- B03D1/001—Flotation agents
- B03D1/004—Organic compounds
- B03D1/006—Hydrocarbons
-
- 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
- B03D2201/02—Collectors
-
- 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
-
- 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
- B03D2203/00—Specified materials treated by the flotation agents; Specified applications
- B03D2203/02—Ores
- B03D2203/04—Non-sulfide ores
Landscapes
- Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
Abstract
Strengthen the method for pressing down copper and carrying molybdenum the present invention relates to a kind of copper-cobalt ore, belong to minerals separation field.A. copper-molybdenum bulk concentrate by throw in advance tail, one roughing, scan three times with five times it is selected after obtain concentrate foam；B. copper deactivator is added in the concentrate foam obtained in step a；C. the ore pulp formed in step b enters grinding machine and regrinds；D. molybdenum collecting agent is added in the ore milling product obtained in step c；E. the product that step d is obtained enters essence six to smart ten flotation operations, obtains final copper concentrate and molybdenum concntrate.Pass through addition NaHS during being regrinded to smart five foams, copper mineral is unquenchable during solving the problems, such as copper-cobalt ore, smart five foams are regrinded while ensure that copper is effectively dissociated with molybdenum, the argillization phenomenon for avoiding a large amount of crush of gangue quartz mineral and generating, in addition it is added to kerosene to regrinding before product enters downstream, recycling of the subsequent job to molybdenum is enhanced, improves the rate of recovery of molybdenum.
Description
Technical field
The present invention relates to the copper-cobalt ore method in minerals separation field more particularly to a kind of sides for strengthening suppression copper and carrying molybdenum
Method.
Background technology
Copper-molybdenum ore reserves is very big in the world, and the copper-molybdenum in China is in the high_speed development stage, time for molybdenum in copper mine
It is always a bigger problem to receive.The few technique streams using diffeential floatation of the Beneficiation flowsheet of copper-molybdenum ore at present
Journey, mainstream sorting process are copper-molybdenum bulk flotation, and copper-molybdenum bulk concentrate presses down process for copper by floating molybdenum and carries out copper-cobalt ore, copper-molybdenum point
It is molybdenum concntrate from flotation froth, flotation tailing is copper concentrate.
Due to the very difficult inhibition of the secondary copper ores such as the bornite in floatation process and vitreous copper, floated using conventional suppression copper
Molybdenum technology, technic index is difficult to control, the rate of recovery and product quality fluctuation are big.In addition it is big in bulk concentrate during copper-cobalt ore
Interference can be generated to separation by measuring gangue mineral, and containing a large amount of shale mineral especially in China's low-grade copper molybdenum ore, this is right
Copper mineral is effectively inhibited to propose higher requirement in copper-cobalt ore technique.
Invention content
The present invention provides a kind of copper-cobalt ore and strengthens the method that suppression copper carries molybdenum, strengthen during copper-cobalt ore inhibit it is secondary
Copper mineral, while the recycling of molybdenum ore object is improved, it ensure that the grade and the rate of recovery of molybdenum concntrate.
The technical solution adopted by the present invention is that：Include the following steps：
A. copper-molybdenum bulk concentrate by coarse scan select in advance throw tail, one roughing, scan three times with five times it is selected after obtain essence
Ore deposit foam；
B. copper deactivator is added in the concentrate foam obtained in step a；
C. the ore pulp formed in step b enters grinding machine and regrinds；
D. molybdenum collecting agent is added in the ore milling product obtained in step c；
E. the product that step d is obtained enters essence six to smart ten flotation operations, obtains final copper concentrate and molybdenum concntrate.
Tail is thrown in the step a in advance to include primary pre- roughing and scan in advance three times.
Copper deactivator is sulfur hydrogen salt class inorganic salts in the step b, and dosage is 180~220g/t bulk concentrates.
It is NaHS that copper deactivator, which is sulfur hydrogen salt class inorganic salts, in the step b.
In the step c grinding machine be tower grinding machine, ore milling concentration 10%-12%.
Molybdenum collecting agent is non-polar hydrocarbon oil in the step d, and dosage is 480~520g/t bulk concentrates.
A kind of copper-cobalt ore disclosed in this invention strengthens suppression copper, and to carry molybdenum methodological science reasonable, easy to operate, it is easy to accomplish,
It has the following advantages compared with prior art：
1. the inhibition in efficient hardening copper-molybdenum bulk concentrate separation process to copper mineral, especially efficiently solves secondary
The unquenchable problem of copper mineral, and then improve molybdenum concentrate grade and the rate of recovery.Usually add in copper-molybdenum bulk concentrate separation process
NaHS is added to inhibit as copper mineral, the HS that NaHS is dissociated in ore pulp and generated-、S2-It can adsorb in chalcopyrite
Surface, prevents chalcopyrite and collecting agent phase separation, and mineral are suppressed due to surface hydrophilic ion.However in copper-molybdenum bulk concentrate still
Containing a certain amount of secondary pig copper, there are passivation phenomenons on secondary pig copper surface, its hardly possible is caused to inhibit hence into molybdenum concntrate, leads to molybdenum
Concentrate grade is difficult to reach sale requirement.In technical solution disclosed by the invention, copper suppression is added in smart five foam grinding processes
Preparation, smart five foams can generate a large amount of fresh surfaces in grinding process, and fresh surface is in the moment meeting of formation and copper deactivator
Interaction, so as to eliminate secondary copper surface passivation phenomenon, enhances the inhibition to copper, so as to improve the grade of molybdenum concntrate.
2. smart five foam regrinding process avoid bulk concentrate argillization problem, while enhance selected foam reagent removal, after being
Continuous operation prepares qualified molybdenum concntrate and provides guarantee.To the 5th selected foam of copper-cobalt ore in technical solution disclosed by the invention
Regrinded rather than bulk concentrate detach at the beginning of regrinded, this is because copper-molybdenum bulk concentrate by pre- coarse scan choosing, coarse scan
Choosing and five times it is selected after deviate from most gangue quartz impurity, while ensureing that copper and molybdenum effectively dissociate, avoid gangue
A large amount of crush of class mineral and the argillization phenomenon generated, in addition smart five foams deviate from the xanthate of a large amount of remainings in grinding process
Class collecting agent prepares qualified molybdenum concntrate for subsequent job and creates condition.
3. regrinding before product enters downstream and being added to collecting agent of the non-polar hydrocarbon oil as molybdenum, follow-up work is enhanced
Recycling of the industry to molybdenum improves the rate of recovery of molybdenum.In technical solution disclosed by the invention kerosene, essence five are added to regrinding product
Copper-molybdenum intergrowth can be dissociated accordingly during foam is regrinded, and kerosene can be made with newly-generated molybdenum ore object monomer surface at this time
With enhancing the recycling of this part molybdenum ore object, improve the rate of recovery of molybdenum concntrate.
4. technical solution operation disclosed by the invention is easy, equipment investment and power consumption are small, remarkable in economical benefits.This hair
The core technology that a kind of bright disclosed copper-cobalt ore reinforcing suppression copper puies forward molybdenum method is by being added during being regrinded to smart five foams
NaHS enhances the inhibition to copper mineral, while ensureing that copper is effectively dissociated with molybdenum, avoids a large amount of of gangue quartz mineral
In addition the argillization phenomenon for crushing and generating enters before downstream to regrinding product and is added to kerosene, enhances subsequent job pair
The recycling of molybdenum improves the rate of recovery of molybdenum.Therefore the technical solution is easy to operate, is not required to larger equipment investment and power disappears
Consumption, operating cost are low, it is easy to accomplish.
Description of the drawings
Fig. 1 is the flow chart of the present invention.
Specific embodiment
Embodiment 1
Include the following steps：
A. copper-molybdenum bulk concentrate throws tail in advance by coarse scan choosing, this throws tail and includes primary pre- roughing and sweep in advance three times in advance
Choosing, one roughing, scan three times with five times it is selected after obtain concentrate foam；
B. copper deactivator NaHS is added in the concentrate foam obtained in step a, dosage is 180g/t bulk concentrates；
C. the ore pulp formed in step b enters grinding machine and regrinds；Grinding machine be tower grinding machine, ore milling concentration 10%；
D. molybdenum collecting agent is added in the ore milling product obtained in step c, molybdenum collecting agent is non-polar hydrocarbon oil, and dosage is
480g/t bulk concentrates；
E. the product that step d is obtained enters essence six to smart ten flotation operations, obtains final copper concentrate and molybdenum concntrate.
Embodiment 2
Include the following steps：
A. copper-molybdenum bulk concentrate throws tail in advance by coarse scan choosing, this throws tail and includes primary pre- roughing and sweep in advance three times in advance
Choosing, one roughing, scan three times with five times it is selected after obtain concentrate foam；
B. copper deactivator NaHS is added in the concentrate foam obtained in step a, dosage is 200g/t bulk concentrates；
C. the ore pulp formed in step b enters grinding machine and regrinds；Grinding machine be tower grinding machine, ore milling concentration 11%.
D. molybdenum collecting agent is added in the ore milling product obtained in step c, molybdenum collecting agent is non-polar hydrocarbon oil, and dosage is
500g/t bulk concentrates；
E. the product that step d is obtained enters essence six to smart ten flotation operations, obtains final copper concentrate and molybdenum concntrate.
Embodiment 3
Include the following steps：
A. copper-molybdenum bulk concentrate throws tail in advance by coarse scan choosing, this throws tail and includes primary pre- roughing and sweep in advance three times in advance
Choosing, one roughing, scan three times with five times it is selected after obtain concentrate foam；
B. copper deactivator NaHS is added in the concentrate foam obtained in step a, dosage is 220g/t bulk concentrates；
C. the ore pulp formed in step b enters grinding machine and regrinds；Grinding machine be tower grinding machine, ore milling concentration 12%.
D. molybdenum collecting agent is added in the ore milling product obtained in step c, molybdenum collecting agent is non-polar hydrocarbon oil, and dosage is
520g/t bulk concentrates；
E. the product that step d is obtained enters essence six to smart ten flotation operations, obtains final copper concentrate and molybdenum concntrate.
Claims (6)
1. a kind of copper-cobalt ore strengthens the method that suppression copper carries molybdenum, which is characterized in that includes the following steps：
A. copper-molybdenum bulk concentrate by coarse scan select in advance throw tail, one roughing, scan three times with five times it is selected after obtain concentrate bubble
Foam；
B. copper deactivator is added in the concentrate foam obtained in step a；
C. the ore pulp formed in step b enters grinding machine and regrinds；
D. molybdenum collecting agent is added in the ore milling product obtained in step c；
E. the product that step d is obtained enters essence six to smart ten flotation operations, obtains final copper concentrate and molybdenum concntrate.
2. a kind of copper-cobalt ore according to claim 1 strengthens the method that suppression copper carries molybdenum, it is characterised in that：The step a
In throw tail in advance and include primary pre- roughing and scan in advance three times.
3. a kind of copper-cobalt ore according to claim 1 strengthens the method that suppression copper carries molybdenum, it is characterised in that：The step b
Middle copper deactivator is sulfur hydrogen salt class inorganic salts, and dosage is 180~220g/t bulk concentrates.
4. a kind of copper-cobalt ore according to claim 3 strengthens the method that suppression copper carries molybdenum, it is characterised in that：The step b
Middle copper deactivator is that sulfur hydrogen salt class inorganic salts are NaHS.
5. a kind of copper-cobalt ore according to claim 1 strengthens the method that suppression copper carries molybdenum, it is characterised in that：The step c
Middle grinding machine be tower grinding machine, ore milling concentration 10%-12%.
6. a kind of copper-cobalt ore according to claim 1 strengthens the method that suppression copper carries molybdenum, it is characterised in that：The step d
Middle molybdenum collecting agent is non-polar hydrocarbon oil, and dosage is 480~520g/t bulk concentrates.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711264954.3A CN108160341A (en) | 2017-12-02 | 2017-12-02 | A kind of copper-cobalt ore strengthens the method that suppression copper carries molybdenum |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711264954.3A CN108160341A (en) | 2017-12-02 | 2017-12-02 | A kind of copper-cobalt ore strengthens the method that suppression copper carries molybdenum |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108160341A true CN108160341A (en) | 2018-06-15 |
Family
ID=62524405
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201711264954.3A Pending CN108160341A (en) | 2017-12-02 | 2017-12-02 | A kind of copper-cobalt ore strengthens the method that suppression copper carries molybdenum |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108160341A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112973971A (en) * | 2021-03-05 | 2021-06-18 | 昆明理工大学 | Collecting agent, flotation agent and flotation method for copper-molybdenum separation |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2010019063A1 (en) * | 2008-08-13 | 2010-02-18 | Ljubomir Dragosan | Molybdenum process of identifying the collective concentrate cu-mo |
| CN103521359A (en) * | 2013-10-28 | 2014-01-22 | 长春黄金研究院 | High-concentration separation flotation technology for roughing of copper and molybdenum bulk concentrates |
| CN103934116A (en) * | 2014-04-29 | 2014-07-23 | 西藏华泰龙矿业开发有限公司 | Method for copper-molybdenum bulk concentrate floatation |
| CN104624389A (en) * | 2015-01-09 | 2015-05-20 | 临武县南方矿业有限责任公司 | Gravitation separation tailing cassiterite flotation method |
| CN105435953A (en) * | 2015-11-18 | 2016-03-30 | 西北矿冶研究院 | Beneficiation method for molybdenum-containing low-grade mixed copper ore |
| CN106391319A (en) * | 2016-11-27 | 2017-02-15 | 长春黄金研究院 | Method for improving grade of copper-molybdenum separated molybdenum concentrate of skarn copper-molybdenum ore |
-
2017
- 2017-12-02 CN CN201711264954.3A patent/CN108160341A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2010019063A1 (en) * | 2008-08-13 | 2010-02-18 | Ljubomir Dragosan | Molybdenum process of identifying the collective concentrate cu-mo |
| CN103521359A (en) * | 2013-10-28 | 2014-01-22 | 长春黄金研究院 | High-concentration separation flotation technology for roughing of copper and molybdenum bulk concentrates |
| CN103934116A (en) * | 2014-04-29 | 2014-07-23 | 西藏华泰龙矿业开发有限公司 | Method for copper-molybdenum bulk concentrate floatation |
| CN104624389A (en) * | 2015-01-09 | 2015-05-20 | 临武县南方矿业有限责任公司 | Gravitation separation tailing cassiterite flotation method |
| CN105435953A (en) * | 2015-11-18 | 2016-03-30 | 西北矿冶研究院 | Beneficiation method for molybdenum-containing low-grade mixed copper ore |
| CN106391319A (en) * | 2016-11-27 | 2017-02-15 | 长春黄金研究院 | Method for improving grade of copper-molybdenum separated molybdenum concentrate of skarn copper-molybdenum ore |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112973971A (en) * | 2021-03-05 | 2021-06-18 | 昆明理工大学 | Collecting agent, flotation agent and flotation method for copper-molybdenum separation |
| CN112973971B (en) * | 2021-03-05 | 2022-03-04 | 昆明理工大学 | A collector, flotation agent and flotation method for copper and molybdenum separation |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| KR102686662B1 (en) | Method for beneficiation of pyrrhotite by flotation after low-alkali line magnetization. | |
| CN102698875B (en) | Ore dressing technology for complex copper-zinc-sulfur multi-metal ore | |
| CN105289834B (en) | The zinc sulphur separation beneficiation method of zinc sulphide ore rich in magnetic iron ore | |
| CN110369122B (en) | Beneficiation method for efficiently recovering high-sulfur gold-copper ore | |
| CN102553717B (en) | Beneficiation process for high-sulfur hematite | |
| CN103143447B (en) | Beneficiation method of high-oxygenation-efficiency complicated copper ore containing co-associated metal | |
| CN110586330A (en) | Flotation process for recovering micro-fine mica from micro-fine iron tailings | |
| CN110237938B (en) | Flotation reagent and flotation separation method of molybdenum, bismuth and sulfur polymetallic sulfide ore | |
| CN104128246B (en) | A kind of beneficiation method of copper-zinc sulfide ore containing easy pumice gangue | |
| CN101549326A (en) | Technique for floatation separation of hard washing copper zinc sulfuration mine | |
| CN105327771B (en) | A kind of fine grinding and comprehensive reutilization ore-dressing technique method containing copper sulfide concentrate | |
| CN106622641B (en) | The method that rich indium marmatite is recycled in association polymetallic ore is total under low alkali from copper zinc indium | |
| CN106622634A (en) | Beneficiation method for copper-cobalt ore | |
| CN105381870A (en) | Beneficiation and enrichment method for molybdenum oxide ore | |
| CN110385194B (en) | Beneficiation method for recovering copper and molybdenum associated with gold and rhenium from porphyry type copper-molybdenum ore | |
| CN106733216A (en) | A kind of beneficiation method of the tin copper symbiotic sulfide ore rich in magnetic iron ore | |
| CN102274797A (en) | Sorting process capable of improving sorting indexes of siderite-containing ore | |
| CN110935560A (en) | Beneficiation method for recovering phosphorus from vanadium titano-magnetite tailings with extremely low phosphorus content | |
| CN114074024B (en) | Ore dressing method for recycling low-grade fluorite in tailings | |
| CN108339672B (en) | Process method for recovering potassium feldspar in potassium-rich slate | |
| CN108160341A (en) | A kind of copper-cobalt ore strengthens the method that suppression copper carries molybdenum | |
| CN109647613A (en) | A kind of raising delafossite recycling flotation technology | |
| CN109701750B (en) | Beneficiation method for recovering gold and silver from copper-nickel bulk concentrate | |
| CN107774456A (en) | Post machine joint is segmented asynchronous coarse concentrate regrinding and selects lead method | |
| CN117324114A (en) | Beneficiation method for low-grade complex embedded refractory copper lead zinc sulfide ore |
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 | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20180615 |
|
| WD01 | Invention patent application deemed withdrawn after publication |