AU2021105063A4 - Method for promoting sulphidizing flotation of copper oxide ore using amino acid - Google Patents
Method for promoting sulphidizing flotation of copper oxide ore using amino acid Download PDFInfo
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- AU2021105063A4 AU2021105063A4 AU2021105063A AU2021105063A AU2021105063A4 AU 2021105063 A4 AU2021105063 A4 AU 2021105063A4 AU 2021105063 A AU2021105063 A AU 2021105063A AU 2021105063 A AU2021105063 A AU 2021105063A AU 2021105063 A4 AU2021105063 A4 AU 2021105063A4
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- copper oxide
- flotation
- amino acid
- oxide ore
- ore pulp
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- QPLDLSVMHZLSFG-UHFFFAOYSA-N Copper oxide Chemical compound [Cu]=O QPLDLSVMHZLSFG-UHFFFAOYSA-N 0.000 title claims abstract description 81
- 239000005751 Copper oxide Substances 0.000 title claims abstract description 81
- 229910000431 copper oxide Inorganic materials 0.000 title claims abstract description 81
- 238000005188 flotation Methods 0.000 title claims abstract description 52
- 150000001413 amino acids Chemical class 0.000 title claims abstract description 32
- 238000000034 method Methods 0.000 title claims abstract description 23
- 230000001737 promoting effect Effects 0.000 title claims abstract description 8
- 229910052500 inorganic mineral Inorganic materials 0.000 claims abstract description 54
- 239000011707 mineral Substances 0.000 claims abstract description 54
- ZOOODBUHSVUZEM-UHFFFAOYSA-N ethoxymethanedithioic acid Chemical compound CCOC(S)=S ZOOODBUHSVUZEM-UHFFFAOYSA-N 0.000 claims abstract description 6
- 239000012991 xanthate Substances 0.000 claims abstract description 6
- 239000012190 activator Substances 0.000 claims abstract description 3
- TUZCOAQWCRRVIP-UHFFFAOYSA-N butoxymethanedithioic acid Chemical compound CCCCOC(S)=S TUZCOAQWCRRVIP-UHFFFAOYSA-N 0.000 claims description 8
- 239000000843 powder Substances 0.000 claims description 8
- 229910052979 sodium sulfide Inorganic materials 0.000 claims description 7
- GRVFOGOEDUUMBP-UHFFFAOYSA-N sodium sulfide (anhydrous) Chemical compound [Na+].[Na+].[S-2] GRVFOGOEDUUMBP-UHFFFAOYSA-N 0.000 claims description 7
- 238000006243 chemical reaction Methods 0.000 claims description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 6
- COLNVLDHVKWLRT-QMMMGPOBSA-N L-phenylalanine Chemical compound OC(=O)[C@@H](N)CC1=CC=CC=C1 COLNVLDHVKWLRT-QMMMGPOBSA-N 0.000 claims description 5
- KDXKERNSBIXSRK-UHFFFAOYSA-N Lysine Natural products NCCCCC(N)C(O)=O KDXKERNSBIXSRK-UHFFFAOYSA-N 0.000 claims description 5
- 239000004472 Lysine Substances 0.000 claims description 5
- COLNVLDHVKWLRT-UHFFFAOYSA-N phenylalanine Natural products OC(=O)C(N)CC1=CC=CC=C1 COLNVLDHVKWLRT-UHFFFAOYSA-N 0.000 claims description 5
- 230000002209 hydrophobic effect Effects 0.000 claims description 4
- 238000001035 drying Methods 0.000 claims description 2
- 238000001914 filtration Methods 0.000 claims description 2
- 239000004088 foaming agent Substances 0.000 claims description 2
- 238000000227 grinding Methods 0.000 claims description 2
- 239000002245 particle Substances 0.000 claims description 2
- 238000007873 sieving Methods 0.000 claims description 2
- 238000003756 stirring Methods 0.000 claims description 2
- 238000011084 recovery Methods 0.000 abstract description 8
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 abstract description 6
- 238000005486 sulfidation Methods 0.000 abstract description 4
- 239000008396 flotation agent Substances 0.000 abstract description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 5
- 239000003795 chemical substances by application Substances 0.000 description 5
- 229910052802 copper Inorganic materials 0.000 description 5
- 239000010949 copper Substances 0.000 description 5
- 230000003213 activating effect Effects 0.000 description 4
- 239000006260 foam Substances 0.000 description 4
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 3
- BFNBIHQBYMNNAN-UHFFFAOYSA-N ammonium sulfate Chemical compound N.N.OS(O)(=O)=O BFNBIHQBYMNNAN-UHFFFAOYSA-N 0.000 description 3
- 229910052921 ammonium sulfate Inorganic materials 0.000 description 3
- 235000011130 ammonium sulphate Nutrition 0.000 description 3
- 239000011541 reaction mixture Substances 0.000 description 3
- 239000011734 sodium Substances 0.000 description 3
- 229910052708 sodium Inorganic materials 0.000 description 3
- JPVYNHNXODAKFH-UHFFFAOYSA-N Cu2+ Chemical compound [Cu+2] JPVYNHNXODAKFH-UHFFFAOYSA-N 0.000 description 2
- 125000003277 amino group Chemical group 0.000 description 2
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 2
- 239000003153 chemical reaction reagent Substances 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 229910001431 copper ion Inorganic materials 0.000 description 2
- ZSFDBVJMDCMTBM-UHFFFAOYSA-N ethane-1,2-diamine;phosphoric acid Chemical compound NCCN.OP(O)(O)=O ZSFDBVJMDCMTBM-UHFFFAOYSA-N 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- 108091005950 Azurite Proteins 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical group [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- FVIGODVHAVLZOO-UHFFFAOYSA-N Dixanthogen Chemical compound CCOC(=S)SSC(=S)OCC FVIGODVHAVLZOO-UHFFFAOYSA-N 0.000 description 1
- PIICEJLVQHRZGT-UHFFFAOYSA-N Ethylenediamine Chemical compound NCCN PIICEJLVQHRZGT-UHFFFAOYSA-N 0.000 description 1
- VCUFZILGIRCDQQ-KRWDZBQOSA-N N-[[(5S)-2-oxo-3-(2-oxo-3H-1,3-benzoxazol-6-yl)-1,3-oxazolidin-5-yl]methyl]-2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidine-5-carboxamide Chemical compound O=C1O[C@H](CN1C1=CC2=C(NC(O2)=O)C=C1)CNC(=O)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F VCUFZILGIRCDQQ-KRWDZBQOSA-N 0.000 description 1
- 241000907663 Siproeta stelenes Species 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229910001779 copper mineral Inorganic materials 0.000 description 1
- BERDEBHAJNAUOM-UHFFFAOYSA-N copper(I) oxide Inorganic materials [Cu]O[Cu] BERDEBHAJNAUOM-UHFFFAOYSA-N 0.000 description 1
- OMZSGWSJDCOLKM-UHFFFAOYSA-N copper(II) sulfide Chemical compound [S-2].[Cu+2] OMZSGWSJDCOLKM-UHFFFAOYSA-N 0.000 description 1
- LBJNMUFDOHXDFG-UHFFFAOYSA-N copper;hydrate Chemical compound O.[Cu].[Cu] LBJNMUFDOHXDFG-UHFFFAOYSA-N 0.000 description 1
- 229960002377 dixanthogen Drugs 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 230000002401 inhibitory effect Effects 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 229910052592 oxide mineral Inorganic materials 0.000 description 1
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 description 1
- 150000004763 sulfides Chemical class 0.000 description 1
- GWBUNZLLLLDXMD-UHFFFAOYSA-H tricopper;dicarbonate;dihydroxide Chemical compound [OH-].[OH-].[Cu+2].[Cu+2].[Cu+2].[O-]C([O-])=O.[O-]C([O-])=O GWBUNZLLLLDXMD-UHFFFAOYSA-H 0.000 description 1
- 239000002351 wastewater 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
- B03D1/001—Flotation agents
- B03D1/004—Organic compounds
- B03D1/012—Organic compounds containing sulfur
-
- 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
- B03D1/01—Organic compounds containing nitrogen
-
- 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
- B03D1/06—Froth-flotation processes differential
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B15/00—Obtaining copper
- C22B15/0063—Hydrometallurgy
- C22B15/0084—Treating solutions
-
- 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
- B03D2203/00—Specified materials treated by the flotation agents; Specified applications
- B03D2203/02—Ores
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
Abstract
This disclosure provides a method for promoting copper oxide mineral flotation using an
amino acid, comprising. An amino acid as activator is added to a sulphidized copper oxide ore
pulp, and the sulphidized copper oxide ore pulp is subjected to flotation in a flotation machine
with xanthate as a collector. Based on the sulfidation flotation of the copper oxide mineral, the
method improves the flotation efficiency of the copper oxide mineral by adding an amino acid
during the flotation. The copper oxide mineral is crushed and sieved, and then the amino acid,
sulfide and related flotation agents are added to a flotation machine to carry out the flotation
within controlled time. Compared with the flotation without the addition of amino acids, the
flotation recovery rate of the copper oxide mineral is increased by up to 10%. Obviously, the
amino acid promotes the sulphidizing flotation of the copper oxide mineral. The method
disclosed herein provides a way for the industrial flotation of copper oxide minerals.
Description
This application relates to beneficiation of copper oxide ores, and more particularly to a
method for promoting sulphidizing flotation of a copper oxide ore using an amino acid.
Copper oxide mineral and mixed copper mineral account for 10%-15% of the worldwide
copper reserves. In China, the copper oxide mineral accounts for a quarter of the copper
reserves. Oxidation zones and huge copper oxide deposits are distributed on most of copper
sulfide deposits. The efficient exploitation and utilization of copper oxide mineral has become a
research highlight. The copper oxide mineral is dominated by malachite, azurite, cuprite and
chrysocolla. Industrially, the copper oxide minerals are usually floated by the sulfidation
xanthate method. Sodium sulfide is often employed as a sulphidizing agent in the sulfidation of
the copper oxide mineral. Specifically, it can combine with the copper ions on the surface of the
copper oxide mineral to form a copper sulfide film attaching to the mineral surface, improving
the hydrophobicity of the mineral surface to increase the adsorption rate of the collector and
promoting the formation of dixanthogen in the adsorption layer. In addition, it has been found
'0 that in addition to the sulfide, activating agents can also greatly improve the flotation efficiency
of copper oxide minerals. Ammonium sulfate and ethylenediamine phosphate are two
widely-used activating agents, where ammonium sulfate can effectively weaken the inhibitory
effect of sodium sulfide, and its synergy with ethylenediamine can effectively improve the
quality and recovery of mineral. These activating agents form insoluble sulfides with the copper
ions on the surface of the mineral to increase the hydrophobicity of the mineral, and allow the
mineral surface to be continuously dissolved. However, the addition amount of the sulfide,
ammonium sulfate and ammonium organics is relatively high in the industrial flotation, and the
flotation wastewater is difficult to treat and may pollute the ecological environment. Therefore,
it is of great industrial significance to develop an efficient and environmentally-friendly
activating agent.
Amino acid is an environment-friendly reagent, and has good compatibility with the ecological environment. The amino acids all have a carboxyl group and an amino group, and vary in the R group. The amino group may play a similar role as ethylenediamine phosphate to promote the sulfidation flotation of copper oxide minerals, and the carboxyl group can theoretically bind the copper ions on the surface of the sulphidized mineral. The R groups of some hydrophobic amino acids have a long carbon chain and a benzene ring, which may improve the hydrophobicity of copper oxide minerals in the flotation. In view of the above, an amino acid-based floatation method of copper oxide ores is designed herein, which can significantly enhance the floatation of copper oxide ores without causing environmental pollution.
An objective of the present disclosure is to provide a method for promoting sulphidizing
flotation of a copper oxide ore using an amino acid, which can improve the flotation recovery
rate of the copper oxide minerals at a relatively low consumption of amino acid. This
application provides a new approach for the selection of flotation reagents.
The technical solutions of the present disclosure are described as follows.
A method for promoting copper oxide mineral flotation using an amino acid, comprising:
subjecting a copper oxide ore pulp to sulphidization to obtain a sulphidized copper oxide
ore pulp; and
adding a solution of the amino acid as activator to the sulphidized copper oxide ore pulp
for reaction followed by flotation in a flotation machine in the presence of xanthate, wherein the
xanthate is used as a collector.
In some embodiments,
the copper oxide pulp is prepared through steps of:
(1) grinding a copper oxide ore to obtain a ground copper oxide mineral with a particle
size of 0.074 mm; and sieving the ground copper oxide mineral to obtain a 200-mesh copper
oxide mineral powder; and
(2) adding the copper oxide mineral powder and water to a flotation tank followed by
uniform stirring to obtain the copper oxide ore pulp with a concentration of 200-400 g/L.
In some embodiments, the sulphidization is carried out by adding 500-3500 g/t of sodium
sulfide to the copper oxide ore pulp; preferably, an addition amount of the sodium sulfide is
3000 g/t; 50-800 g/t of the amino acid is added to the sulphidized copper oxide ore pulp; preferably, an addition amount of the amino acid is 100 g/t; and the reaction is performed for 2-5 min; preferably, 3 min. In some embodiments, the flotation is performed through steps of: adding 50-300 g/t of butyl xanthate to the sulphidized copper oxide ore pulp for collection; adding 10-50 g/t of terpenic oil as a foaming agent to collect a floated copper oxide mineral; and subjecting the collected copper oxide mineral to filtration and drying; preferably, 200 g/t of the butyl xanthate is added to the sulphidized copper oxide pulp; and 10 g/t of the terpenic oil is added. In some embodiments, the amino acid is hydrophobic; preferably, the amino acid hydrophobic is phenylalanine or lysine. The beneficial effects of the present disclosure are described as follows. Based on the characteristics of the sulphidizing flotation of the copper oxide minerals, the present disclosure introduces an amino acid to improve the flotation efficiency. The copper oxide mineral is crushed and sieved, and then the amino acid, a sulfide and related flotation agents are added to a flotation machine to carry out the flotation within controlled time. Compared with the flotation without the addition of amino acids, the flotation recovery rate of the copper oxide mineral is increased by at most 10%. Obviously, the amino acid significantly promotes the sulphidizing flotation of copper oxide minerals. The method disclosed herein provides a way for the industrial flotation of copper oxide minerals.
DETAILED DESCRIPTION OF EMBODIMENTS The embodiments are illustrative of this disclosure, and not intended to limit the present disclosure.
Example 1 10 g of copper oxide mineral powder and 120 mL of water were added into a flotation tank, and were fully mixed by a stirrer. 3000 g/t of a sodium sulfide solution was then added, and then 0 g/t, 100 g/t, 300 g/t and 800 g/t of lysine were respectively added. The reaction mixture was reacted for 3 min, and then added with 200 g/t of butyl xanthate and 10 g/t of terpenic oil.
The foam was scraped, and the collected copper oxide mineral was filtered, dried and weighted.
It was confirmed that under the addition of 100 g/t of the lysine, the flotation recovery rate of
the copper oxide mineral reached 82%.
Comparative Example 1
10 g of copper oxide mineral powder and 120 mL of water were added into a flotation tank,
and were fully mixed by a stirrer. 3000 g/t of a sodium sulfde solution was then added. The
reaction mixture was reacted for 3 min, and then added with 200 g/t of butyl xanthate and 10 g/t
of terpenic oil, and were fully stirred. The foam was scraped, and the collected copper oxide
mineral was filtered, dried and weighted. It was confirmed that without the addition of lysine,
the flotation recovery rate of the copper oxide mineral flotation was 74%.
Example 2
10 g of copper oxide mineral powder and 120 mL of water were added into a flotation tank,
and were fully mixed by a stirrer. 3000 g/t of a sodium sulfide solution was then added, and
then 0 g/t, 100 g/t, 300 g/t and 800 g/t of phenylalanine were respectively added. The reaction
mixture was reacted for 3 min, and then added with 200 g/t of butyl xanthate and 10 g/t of
terpenic oil. The foam was scraped, and the collected copper oxide mineral was filtered, dried
and weighted. It was confirmed that under the addition of 100 g/t, 300 g/t, 800 g/t of the
phenylalanine, the flotation recovery rate of the copper oxide mineral flotation reached 82%,
83% and 85%, respectively.
Comparative Example 2
10 g of copper oxide mineral powder and 120 mL of water were added into a flotation tank,
and were fully mixed by a stirrer. 3000 g/t of a sodium sulfde solution was then added. The
reaction mixture was reacted for 3 min, and then added with 200 g/t of butyl xanthate and 10 g/t
of terpenic oil. The foam was scraped, and the collected copper oxide mineral was filtered,
dried and weighted. It was confirmed that without the addition of phenylalanine, the flotation
recovery rate of the copper oxide mineral flotation was 75%.
Claims (12)
1. A method for promoting flotation of a copper oxide ore using an amino acid,
comprising:
subjecting a copper oxide ore pulp to sulphidization to obtain a sulphidized copper oxide
ore pulp; and
adding a solution of the amino acid as activator to the sulphidized copper oxide ore pulp
for reaction followed by flotation in a flotation machine in the presence of xanthate, wherein the
xanthate is used as a collector.
2. The method according to claim 1, characterized in that the copper oxide pulp is prepared
through steps of:
(1) grinding a copper oxide ore to obtain a ground copper oxide mineral with a particle
size of 0.074 mm; and sieving the ground copper oxide mineral to obtain a 200-mesh copper
oxide mineral powder; and
(2) adding the copper oxide mineral powder and water to a flotation tank followed by
uniform stirring to obtain the copper oxide ore pulp with a concentration of 200-400 g/L.
3. The method according to claim 1, characterized in that the sulphidization is carried out
by adding 500-3500 g/t of sodium sulfide to the copper oxide ore pulp.
4. The method according to claim 1, characterized in that 50-800 g/t of the amino acid is
added to the sulphidized copper oxide ore pulp, and the reaction is performed for 2-5 min.
5. The method according to claim 4, characterized in that the reaction is performed for 3
min.
6. The method according to claim 1, characterized in that the flotation is performed
through steps of:
adding 50-300 g/t of butyl xanthate to the sulphidized copper oxide ore pulp for collection; adding 10-50 g/t of terpenic oil as a foaming agent to collect a floated copper oxide mineral; and subjecting the collected copper oxide mineral to filtration and drying.
7. The method according to claim 2, characterized in that the concentration of the copper oxide ore pulp is 350 g/L.
8. The method according to claim 1, characterized in that the amino acid is a hydrophobic amino acid.
9. The method according to claim 8, characterized in that the amino acid is phenylalanine or lysine.
10. The method according to claim 3, characterized in that 3000 g/t of the sodium sulfide is added to the copper oxide ore pulp.
11. The method according to claim 4, characterized in that 100 g/t of the amino acid is added to the sulphidized copper oxide ore pulp.
12. The method according to claim 6, characterized in that 200 g/t of the butyl xanthate is added to the sulphidized copper oxide pulp; and 10 g/t of the terpenic oil is added.
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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CN115090422A (en) * | 2022-06-17 | 2022-09-23 | 山东理工大学 | Amino acid type collecting agent and preparation method and application thereof |
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2021
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Cited By (2)
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CN115090422A (en) * | 2022-06-17 | 2022-09-23 | 山东理工大学 | Amino acid type collecting agent and preparation method and application thereof |
CN115090422B (en) * | 2022-06-17 | 2024-04-26 | 山东理工大学 | Amino acid type collector, and preparation method and application thereof |
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