CN107971123A - A kind of flotation and metallurgy method of irony coated mixed copper ore - Google Patents
A kind of flotation and metallurgy method of irony coated mixed copper ore Download PDFInfo
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- CN107971123A CN107971123A CN201711145244.9A CN201711145244A CN107971123A CN 107971123 A CN107971123 A CN 107971123A CN 201711145244 A CN201711145244 A CN 201711145244A CN 107971123 A CN107971123 A CN 107971123A
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- copper
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- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 title claims abstract description 144
- 229910052802 copper Inorganic materials 0.000 title claims abstract description 144
- 239000010949 copper Substances 0.000 title claims abstract description 144
- 238000005188 flotation Methods 0.000 title claims abstract description 38
- 238000000034 method Methods 0.000 title claims abstract description 36
- 238000005272 metallurgy Methods 0.000 title abstract description 3
- 238000002386 leaching Methods 0.000 claims abstract description 51
- 239000012141 concentrate Substances 0.000 claims abstract description 47
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims abstract description 42
- 238000007885 magnetic separation Methods 0.000 claims abstract description 42
- QAOWNCQODCNURD-UHFFFAOYSA-N sulfuric acid Substances OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims abstract description 22
- 229910052742 iron Inorganic materials 0.000 claims abstract description 21
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 18
- 238000003723 Smelting Methods 0.000 claims abstract description 15
- 238000003756 stirring Methods 0.000 claims abstract description 15
- 239000000203 mixture Substances 0.000 claims description 29
- 239000002002 slurry Substances 0.000 claims description 16
- 239000007787 solid Substances 0.000 claims description 16
- 239000004088 foaming agent Substances 0.000 claims description 15
- 229910001608 iron mineral Inorganic materials 0.000 claims description 11
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 claims description 8
- 229910052595 hematite Inorganic materials 0.000 claims description 7
- 239000011019 hematite Substances 0.000 claims description 7
- LIKBJVNGSGBSGK-UHFFFAOYSA-N iron(3+);oxygen(2-) Chemical compound [O-2].[O-2].[O-2].[Fe+3].[Fe+3] LIKBJVNGSGBSGK-UHFFFAOYSA-N 0.000 claims description 7
- 238000007254 oxidation reaction Methods 0.000 claims description 7
- 239000007788 liquid Substances 0.000 claims description 6
- 229910052979 sodium sulfide Inorganic materials 0.000 claims description 6
- GRVFOGOEDUUMBP-UHFFFAOYSA-N sodium sulfide (anhydrous) Chemical group [Na+].[Na+].[S-2] GRVFOGOEDUUMBP-UHFFFAOYSA-N 0.000 claims description 6
- TUZCOAQWCRRVIP-UHFFFAOYSA-N butoxymethanedithioic acid Chemical group CCCCOC(S)=S TUZCOAQWCRRVIP-UHFFFAOYSA-N 0.000 claims description 5
- 230000003647 oxidation Effects 0.000 claims description 5
- 239000002245 particle Substances 0.000 claims description 5
- 239000002253 acid Substances 0.000 abstract description 15
- 229910001779 copper mineral Inorganic materials 0.000 abstract description 14
- 239000002918 waste heat Substances 0.000 abstract description 6
- 239000000284 extract Substances 0.000 abstract 1
- 239000005751 Copper oxide Substances 0.000 description 26
- 229910000431 copper oxide Inorganic materials 0.000 description 26
- QPLDLSVMHZLSFG-UHFFFAOYSA-N Copper oxide Chemical compound [Cu]=O QPLDLSVMHZLSFG-UHFFFAOYSA-N 0.000 description 25
- 229910052500 inorganic mineral Inorganic materials 0.000 description 18
- 239000011707 mineral Substances 0.000 description 18
- OMZSGWSJDCOLKM-UHFFFAOYSA-N copper(II) sulfide Chemical compound [S-2].[Cu+2] OMZSGWSJDCOLKM-UHFFFAOYSA-N 0.000 description 12
- 238000011084 recovery Methods 0.000 description 9
- 229910052569 sulfide mineral Inorganic materials 0.000 description 8
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 7
- 238000010438 heat treatment Methods 0.000 description 5
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 4
- 238000000227 grinding Methods 0.000 description 4
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 3
- XOCUXOWLYLLJLV-UHFFFAOYSA-N [O].[S] Chemical compound [O].[S] XOCUXOWLYLLJLV-UHFFFAOYSA-N 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 235000014113 dietary fatty acids Nutrition 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000000194 fatty acid Substances 0.000 description 3
- 229930195729 fatty acid Natural products 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 238000005486 sulfidation Methods 0.000 description 3
- NEAQRZUHTPSBBM-UHFFFAOYSA-N 2-hydroxy-3,3-dimethyl-7-nitro-4h-isoquinolin-1-one Chemical compound C1=C([N+]([O-])=O)C=C2C(=O)N(O)C(C)(C)CC2=C1 NEAQRZUHTPSBBM-UHFFFAOYSA-N 0.000 description 2
- 229910021529 ammonia Inorganic materials 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- HHSPVTKDOHQBKF-UHFFFAOYSA-J calcium;magnesium;dicarbonate Chemical compound [Mg+2].[Ca+2].[O-]C([O-])=O.[O-]C([O-])=O HHSPVTKDOHQBKF-UHFFFAOYSA-J 0.000 description 2
- ZOOODBUHSVUZEM-UHFFFAOYSA-N ethoxymethanedithioic acid Chemical compound CCOC(S)=S ZOOODBUHSVUZEM-UHFFFAOYSA-N 0.000 description 2
- 150000004665 fatty acids Chemical class 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000005065 mining Methods 0.000 description 2
- 238000004537 pulping Methods 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 239000012991 xanthate Substances 0.000 description 2
- 108091005950 Azurite Proteins 0.000 description 1
- PIICEJLVQHRZGT-UHFFFAOYSA-N Ethylenediamine Chemical compound NCCN PIICEJLVQHRZGT-UHFFFAOYSA-N 0.000 description 1
- -1 Fatty acid salt Chemical class 0.000 description 1
- 241000784732 Lycaena phlaeas Species 0.000 description 1
- 241000907663 Siproeta stelenes Species 0.000 description 1
- BCKXLBQYZLBQEK-KVVVOXFISA-M Sodium oleate Chemical compound [Na+].CCCCCCCC\C=C/CCCCCCCC([O-])=O BCKXLBQYZLBQEK-KVVVOXFISA-M 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- BFNBIHQBYMNNAN-UHFFFAOYSA-N ammonium sulfate Chemical compound N.N.OS(O)(=O)=O BFNBIHQBYMNNAN-UHFFFAOYSA-N 0.000 description 1
- 229910052921 ammonium sulfate Inorganic materials 0.000 description 1
- 235000011130 ammonium sulphate Nutrition 0.000 description 1
- 230000001580 bacterial effect Effects 0.000 description 1
- 229910052626 biotite Inorganic materials 0.000 description 1
- 229910052948 bornite Inorganic materials 0.000 description 1
- 229910052947 chalcocite Inorganic materials 0.000 description 1
- 229910052951 chalcopyrite Inorganic materials 0.000 description 1
- DVRDHUBQLOKMHZ-UHFFFAOYSA-N chalcopyrite Chemical compound [S-2].[S-2].[Fe+2].[Cu+2] DVRDHUBQLOKMHZ-UHFFFAOYSA-N 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- BERDEBHAJNAUOM-UHFFFAOYSA-N copper(I) oxide Inorganic materials [Cu]O[Cu] BERDEBHAJNAUOM-UHFFFAOYSA-N 0.000 description 1
- LBJNMUFDOHXDFG-UHFFFAOYSA-N copper;hydrate Chemical compound O.[Cu].[Cu] LBJNMUFDOHXDFG-UHFFFAOYSA-N 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- HYHCSLBZRBJJCH-UHFFFAOYSA-M sodium hydrosulfide Chemical compound [Na+].[SH-] HYHCSLBZRBJJCH-UHFFFAOYSA-M 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 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
- 238000004073 vulcanization Methods 0.000 description 1
Classifications
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- 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
- B03B—SEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
- B03B9/00—General arrangement of separating plant, e.g. flow sheets
- B03B9/06—General arrangement of separating plant, e.g. flow sheets specially adapted for refuse
-
- 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
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C1/00—Magnetic separation
- B03C1/02—Magnetic separation acting directly on the substance being separated
-
- 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
- B03D2201/02—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
- B03D2201/04—Frothers
-
- 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
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/52—Mechanical processing of waste for the recovery of materials, e.g. crushing, shredding, separation or disassembly
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- Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
Abstract
本发明公开了一种铁质包裹型混合铜矿的选冶方法,属于选矿冶金技术领域。本发明将铁质包裹型混合铜矿进行浮选得到浮选铜精矿和浮选尾矿;浮选尾矿采用磁选得到铁质包裹的含铜磁选精矿和低品位含铜磁选尾矿;铁质包裹的含铜磁选精矿经细磨处理后,采用浓硫酸作为浸出剂,通过高温搅拌浸出回收其中的铜矿物;磁选精矿浸出后的高温矿浆与含铜磁选尾矿混合,利用其中的余热和余酸进一步回收尾矿中的铜矿物。本发明分级回收矿石中的铜矿物,针对性处理铁质包裹型混合铜矿,利用余热和余酸提取低品位含铜磁选尾矿中的铜资源,经济高效地解决了铁质包裹型混合铜矿难以回收的技术难题,提高了铜资源的综合利用率。
The invention discloses a method for dressing and smelting iron-wrapped mixed copper ore, which belongs to the technical field of ore dressing and metallurgy. The invention performs flotation on the iron-wrapped mixed copper ore to obtain flotation copper concentrate and flotation tailings; the flotation tailings adopts magnetic separation to obtain iron-wrapped copper-containing magnetic separation concentrate and low-grade copper-containing magnetic separation Tailings; iron-coated copper-containing magnetic separation concentrates are finely ground, and concentrated sulfuric acid is used as a leaching agent to recover copper minerals through high-temperature stirring and leaching; The tailings are mixed, and the waste heat and acid are used to further recover the copper minerals in the tailings. The present invention classifies and recycles copper minerals in ores, treats iron-wrapped mixed copper ore in a targeted manner, and extracts copper resources in low-grade copper-containing magnetic separation tailings by using waste heat and residual acid, and solves the problem of iron-wrapped mixed copper ore economically and efficiently. The technical problem that mixed copper ore is difficult to recycle has improved the comprehensive utilization rate of copper resources.
Description
技术领域technical field
本发明涉及一种铁质包裹型混合铜矿的选冶方法,属于选矿冶金技术领域。The invention relates to a method for dressing and smelting iron-wrapped mixed copper ore, which belongs to the technical field of ore dressing and metallurgy.
背景技术Background technique
铜是一种重要的有色金属,其在国民经济建设中的地位日趋重要。铜在自然界中主要以硫化物和氧化物的形式存在,常见的具有工业开采价值的硫化铜矿物有黄铜矿、辉铜矿、斑铜矿、铜蓝等,氧化铜矿物有孔雀石、蓝铜矿、赤铜矿、硅孔雀石等。然而,在铜矿开采加工过程中,除了单一的硫化铜和氧化铜矿外,硫化-氧化混合铜矿在铜矿资源中占有相当大的比例,因此,为了满足国民经济对铜金属的需要,降低铜的对外依存度,混合铜矿资源的高效开发和利用势在必行。Copper is an important non-ferrous metal, and its status in national economic construction is becoming more and more important. Copper mainly exists in the form of sulfide and oxide in nature. Common copper sulfide minerals with industrial mining value include chalcopyrite, chalcocite, bornite, copper blue, etc., and copper oxide minerals include malachite. , Azurite, Cuprite, Chrysocolla, etc. However, in the process of copper mining and processing, in addition to single copper sulfide and copper oxide ore, sulfide-oxidation mixed copper ore occupies a considerable proportion of copper ore resources. Therefore, in order to meet the needs of the national economy for copper metal, To reduce the external dependence of copper, the efficient development and utilization of mixed copper ore resources is imperative.
目前,硫化铜矿的浮选已较为成熟;氧化铜矿物的可浮性差于硫化铜矿物,常采用硫化浮选法和直接浮选法进行富集。采用硫化浮选法富集氧化铜矿在工业生产中得到广泛的应用,即使用硫化钠或硫氢化钠为硫化剂对矿石中的氧化铜矿物进行硫化,然后使用黄药类捕收剂进行捕收;氧化铜矿硫化过程中,可添加一定量的硫酸铵或乙二胺实现氧化铜矿物的强化硫化。直接浮选是采用脂肪酸或羟肟酸作为捕收剂对矿石中的氧化铜矿物进行直接浮选,但该法仅限于矿石中脉石矿物相对简单的氧化铜矿。此外,离析-浮选法、酸浸、氨浸、细菌浸出等技术常用来处理氧化铜矿。At present, the flotation of copper sulfide ore is relatively mature; the floatability of copper oxide minerals is worse than that of copper sulfide minerals, and sulfide flotation and direct flotation are often used for enrichment. The enrichment of copper oxide ore by sulfidation flotation is widely used in industrial production, that is, sodium sulfide or sodium hydrosulfide is used as a sulfide agent to sulfide the copper oxide minerals in the ore, and then the xanthate collector is used to sulfide the copper oxide ore. Collection; During the sulfidation process of copper oxide minerals, a certain amount of ammonium sulfate or ethylenediamine can be added to achieve enhanced sulfidation of copper oxide minerals. Direct flotation is to use fatty acid or hydroxamic acid as a collector to directly float copper oxide minerals in ores, but this method is limited to copper oxide ores with relatively simple gangue minerals in ores. In addition, techniques such as segregation-flotation, acid leaching, ammonia leaching, and bacterial leaching are commonly used to treat copper oxide ore.
对于硫化-氧化混合铜矿,浮选法仅能回收硫化铜矿物和部分氧化铜矿物;采用浸出法,矿石中的氧化铜矿物虽得到很好地回收,但其中的硫化铜矿物难以回收,当矿石中碳酸盐脉石矿物含量较高时,直接酸浸的成本较高;目前,选冶联合工艺是处理混合铜矿的有效方法,具有一定的灵活性,能够处理不同类型的矿石。申请号为200510010932.5的发明专利提出了一种从低品位高钙镁氧化铜矿原矿中提取铜的方法,所述方法首先通过常温常压氨浸技术溶解矿石中的氧化铜矿物,浸出尾渣采用浮选法回收其中的硫化铜矿物,实现了高钙镁氧硫混合铜矿的综合回收。申请号为201010178875.2的发明专利提出了一种高结合率碳酸盐脉石型氧硫混合铜矿的选冶方法,所述方法先通过浮选回收高结合率碳酸盐脉石型氧硫混合铜矿中的硫化铜矿物和游离氧化铜矿物,浮选尾矿用脂肪酸反浮选其中的钙镁碳酸盐矿物,得到含钙镁碳酸盐矿物低,含结合铜的中矿,再添加硫酸搅拌浸出结合铜,固液分离后的含铜溶液通过冶金方法获得铜产品。申请号为201310615690.7的发明专利针对低品位混合铜矿,首先选用新型高效捕收剂MA作为硫化铜矿捕收剂,直接浮选硫化铜矿,再分别通过硫化浮选和直接浮选回收氧化铜矿,分别选用新型高效捕收剂MA作为硫化浮选捕收剂,油酸钠作为氧化铜矿直接浮选捕收剂,浮选混合精矿集中进行酸浸处理,过滤之后收集滤液。For sulfide-oxidation mixed copper ore, the flotation method can only recover copper sulfide minerals and partial copper oxide minerals; by leaching, although the copper oxide minerals in the ore are well recovered, the copper sulfide minerals Difficult to recycle, when the content of carbonate gangue minerals in the ore is high, the cost of direct acid leaching is high; at present, the combined dressing and smelting process is an effective method for processing mixed copper ore, which has certain flexibility and can handle different types of ore. The invention patent with application number 200510010932.5 proposes a method for extracting copper from low-grade high-calcium magnesium copper oxide ore raw ore. The method first dissolves the copper oxide minerals in the ore by normal temperature and pressure ammonia leaching technology, and leaches the tailings The flotation method is used to recover the copper sulfide minerals, and the comprehensive recovery of high-calcium-magnesium-oxygen-sulfur mixed copper ores is realized. The invention patent with the application number 201010178875.2 proposes a method for beneficiation and smelting of high binding rate carbonate gangue-type oxygen-sulfur mixed copper ore. The method first recovers high binding rate carbonate gangue-type oxygen-sulfur mixed copper ore through flotation. Copper sulfide minerals and free copper oxide minerals in copper ore, the calcium magnesium carbonate minerals in the flotation tailings are reverse flotation with fatty acids, and the medium ore containing low calcium magnesium carbonate minerals and bound copper is obtained. Sulfuric acid is added to stir and leach bound copper, and the copper-containing solution after solid-liquid separation is used to obtain copper products through metallurgical methods. The invention patent with application number 201310615690.7 is aimed at low-grade mixed copper ore. Firstly, a new type of high-efficiency collector MA is selected as the collector for copper sulfide ore to directly float copper sulfide ore, and then copper oxide is recovered through sulfide flotation and direct flotation respectively. For the ore, the new high-efficiency collector MA was selected as the sulfide flotation collector, and sodium oleate was used as the direct flotation collector for copper oxide ore. The flotation mixed concentrate was concentrated for acid leaching treatment, and the filtrate was collected after filtration.
综上所述,氧硫混合铜矿可通过选矿、浸出、选冶联合等方法实现矿石中铜资源的综合回收,这些矿石采用常规的碎矿、磨矿能将其中的铜矿物解离,有利于后续的技术将其回收。但铜矿资源中,有一部分氧化铜矿与铁质矿物紧密共生,矿石中的氧化铜矿物被赤铁矿和褐铁矿包裹,采用常规的选冶方法难以将其回收。申请号为201710139088.9的发明专利提出了一种包裹型复杂氧化铜矿回收利用的方法,所述方法针对浮选难以回收、直接酸浸浸出率低的包裹型氧化铜矿,采用硫化,黄药、脂肪酸盐和羟肟酸联合浮选游离氧化铜,磁选回收矿石中的包裹铜矿物的铁质和黑云母矿物,分离出大量低品位含铜尾矿。含包裹型铜的粗精矿通过高温加压搅拌浸出强化回收其中的铜矿资源,高温浸出矿浆与低品位含铜尾矿混合继续进行余热余酸浸出尾矿中的铜矿物,使不能直接浮选回收和直接酸浸回收的包裹型氧化铜矿得以高效回收利用。申请号为201710139134.5的发明专利提出了一种固体包裹体氧化铜矿选冶联合回收利用的方法,采用强磁选分离获得包裹氧化铜的磁性产物,对磁性产物过滤,采用微波干燥及加热,利用微波对固体包裹体中不同矿物加热的选择性,使矿物之间升温不同、体积膨胀不同而产生裂纹,为后来的硫酸浸出提供扩散通道,提高浸出速率和浸出率,高效回收这种难处理铜矿资源。但这两种方法分别采用高温加压搅拌浸出和微波干燥及加热技术对矿石中的含铜包裹体进行处理,尽管铜的浸出率得以提高,但所用的高温加压搅拌浸出设备和微波干燥及加热设备成本较高,操作、维护要求较高,而且该方法主要针对氧化铜矿的回收。In summary, oxygen-sulfur mixed copper ore can achieve comprehensive recovery of copper resources in the ore through ore dressing, leaching, dressing and smelting, etc. These ores can be dissociated from the copper minerals by conventional crushing and grinding. It is beneficial for subsequent technology to recycle it. However, in copper ore resources, some copper oxide ores are closely symbiotic with iron minerals. The copper oxide minerals in the ore are wrapped by hematite and limonite, and it is difficult to recover them by conventional dressing and smelting methods. The invention patent with the application number 201710139088.9 proposes a method for recycling wrapped copper oxide ore, which is difficult to recover by flotation and has a low direct acid leaching rate. The method adopts vulcanization, xanthate, Fatty acid salt and hydroxamic acid are combined to flotation free copper oxide, and magnetic separation recovers iron and biotite minerals wrapped in copper minerals in the ore, and a large number of low-grade copper-containing tailings are separated. Coarse concentrate containing wrapped copper is leached under high temperature and pressure to strengthen the recovery of copper ore resources. The high-temperature leached slurry is mixed with low-grade copper-containing tailings to continue leaching the copper minerals in the tailings with waste heat and acid, so that the copper minerals in the tailings cannot be directly The coated copper oxide ore recovered by flotation and direct acid leaching can be efficiently recycled. The invention patent with the application number of 201710139134.5 proposes a method for the combined recycling and utilization of copper oxide ore with solid inclusions. It adopts strong magnetic separation to obtain the magnetic products wrapped in copper oxide, filters the magnetic products, uses microwave drying and heating, and utilizes The selectivity of microwave heating to different minerals in solid inclusions makes the minerals have different temperature rises and volume expansions to produce cracks, which provides diffusion channels for the subsequent sulfuric acid leaching, improves the leaching rate and leaching rate, and efficiently recovers this refractory copper. mine resources. However, these two methods use high-temperature pressure-stirring leaching and microwave drying and heating technology to treat the copper-containing inclusions in the ore. Although the copper leaching rate can be improved, the high-temperature pressure stirring leaching equipment used and microwave drying and The cost of heating equipment is high, and the operation and maintenance requirements are high, and this method is mainly aimed at the recovery of copper oxide ore.
发明内容Contents of the invention
本发明针对现有技术的不足,提供一种铁质包裹型混合铜矿的选冶方法,即将铁质包裹型混合铜矿进行浮选得到浮选铜精矿和浮选尾矿;浮选尾矿采用磁选得到铁质包裹的含铜磁选精矿和低品位含铜磁选尾矿;铁质包裹的含铜磁选精矿经细磨处理后,采用浓硫酸作为浸出剂,通过高温搅拌浸出回收其中的铜矿物;磁选精矿浸出后的高温矿浆与含铜磁选尾矿混合,利用其中的余热和余酸进一步回收尾矿中的铜矿物,使不能直接浮选回收和酸浸提取的铁质包裹型混合铜矿得以高效回收利用。Aiming at the deficiencies of the prior art, the present invention provides a dressing and smelting method of iron-encased mixed copper ore, that is, performing flotation on iron-encased mixed copper ore to obtain flotation copper concentrate and flotation tailings; flotation tailings The ore adopts magnetic separation to obtain iron-coated copper-containing magnetic separation concentrate and low-grade copper-containing magnetic separation tailings; after the iron-coated copper-containing magnetic separation concentrate is finely ground, concentrated sulfuric acid is used as the leaching agent, and the high-temperature Stirring leaching recovers the copper minerals; the high-temperature slurry after magnetic separation concentrate leaching is mixed with copper-containing magnetic separation tailings, and the waste heat and acid are used to further recover copper minerals in the tailings, so that direct flotation recovery is not possible. The iron-coated mixed copper ore extracted by acid leaching can be efficiently recycled.
一种铁质包裹型混合铜矿的选冶方法,其特征在于,具体步骤如下:A method for dressing and smelting iron-encapsulated mixed copper ore is characterized in that the specific steps are as follows:
(1)将铁质包裹型混合铜矿破碎、磨细至-74μm粒级的质量百分含量占70~80%,调浆至矿浆质量百分浓度为30~40%,以每吨铁质包裹型混合铜矿计,依次加入400~800g硫化剂、300~600g捕收剂和30~100g起泡剂,进行一次粗选作业得到一次粗选精矿和一次粗选尾矿,以每吨铁质包裹型混合铜矿计,在一次粗选尾矿中依次加入100~200g硫化剂、75~150g捕收剂和15~50g起泡剂进行二次粗选作业得到二次粗选精矿和二次粗选尾矿(二次粗选尾矿即为浮选尾矿),将一次粗选精矿和二次粗选精矿合并进行精选作业得到浮选铜精矿和精选尾矿,精选尾矿返回调浆进行一次粗选作业;(1) Crush and grind the iron-encapsulated mixed copper ore to a mass percentage of -74μm, which accounts for 70-80% of the mass percentage, and adjust the slurry until the mass percentage concentration of the ore pulp is 30-40%. For packaged mixed copper ore, add 400~800g vulcanizing agent, 300~600g collector, and 30~100g foaming agent in sequence, and perform a roughing operation to obtain a roughing concentrate and a roughing tailings. For the iron-coated mixed copper ore, add 100~200g vulcanizing agent, 75~150g collector and 15~50g foaming agent to the tailings of the primary roughing in order to carry out the secondary roughing operation to obtain the secondary roughing concentrate and secondary rougher tailings (secondary rougher tailings are flotation tailings), the first rougher concentrate and the second rougher concentrate are combined for concentration operations to obtain flotation copper concentrate and concentrated tailings ore, and the selected tailings return to the slurry for a roughing operation;
(2)在磁场强度为0.8~1.4T的条件下,将步骤(1)所得二次粗选尾矿进行磁选得到铁质包裹的含铜磁选精矿和低品位含铜磁选尾矿;(2) Under the condition of a magnetic field strength of 0.8~1.4T, the secondary roughing tailings obtained in step (1) are subjected to magnetic separation to obtain iron-coated copper-containing magnetic separation concentrates and low-grade copper-containing magnetic separation tailings ;
(3)根据步骤(2)所得含铜磁选精矿细磨至-45μm粒级的质量百分含量大于85%,调浆至矿浆的液固质量比为(2~3):1,在温度为75~90℃的搅拌条件下,加入浓硫酸得到矿浆混合物A并浸出120~180min得到浸出矿浆;(3) According to the step (2), the mass percentage of the finely ground copper-containing magnetic separation concentrate to -45 μm particle size is greater than 85%, and the liquid-solid mass ratio of the pulp is (2~3):1. Under the condition of stirring at a temperature of 75-90°C, add concentrated sulfuric acid to obtain a pulp mixture A and leaching for 120-180 minutes to obtain a leached pulp;
(4)将步骤(2)所得磁选尾矿加入到步骤(3)所得浸出矿浆并混合均匀得到矿浆混合物B并在搅拌条件下继续浸出180~240min,固液分离得到含铜浸出液和浸出尾渣;(4) Add the magnetic separation tailings obtained in step (2) to the leaching pulp obtained in step (3) and mix evenly to obtain the pulp mixture B, and continue leaching for 180~240min under stirring conditions, and separate the solid and liquid to obtain the copper-containing leachate and leaching tailings slag;
所述步骤(1)铁质包裹型混合铜矿中铜的质量百分数含量为1.0~1.8%,铜的氧化率不低于70%;以铁质包裹型混合铜矿中的铜含量为100%计,铜在铁质矿物中的含量为35~45%,铁质矿物为赤铁矿和/或褐铁矿;硫化剂为硫化钠,捕收剂为丁基黄药,起泡剂为2号油;In the step (1), the mass percentage of copper in the iron-wrapped mixed copper ore is 1.0-1.8%, and the oxidation rate of copper is not less than 70%; the copper content in the iron-wrapped mixed copper ore is 100% Calculated, the content of copper in iron minerals is 35~45%, and the iron minerals are hematite and/or limonite; the vulcanizing agent is sodium sulfide, the collector is butyl xanthate, and the foaming agent is 2 No. oil;
所述步骤(3)矿浆混合物A中硫酸的浓度为35~80g/L;The concentration of sulfuric acid in the step (3) pulp mixture A is 35 ~ 80g/L;
所述步骤(4)矿浆混合物B中的液固质量比为(2~3):1;The liquid-solid mass ratio in the pulp mixture B in the step (4) is (2~3):1;
所述步骤(4)的浸出过程利用步骤(3)浸出的余热和余酸,未进行额外加热,未添加新的浓硫酸。The leaching process of the step (4) utilizes the residual heat and residual acid leached in the step (3), without additional heating and without adding new concentrated sulfuric acid.
本发明的有益效果:Beneficial effects of the present invention:
(1)本发明先将铁质包裹型混合铜矿中的硫化铜矿物进行浮选分离,既获得了合格的浮选铜精矿,又减轻了后续浸出过程中硫化铜矿物的浸出难度;(1) In the present invention, the copper sulfide minerals in the iron-encapsulated mixed copper ore are first flotation-separated, which not only obtains qualified flotation copper concentrates, but also reduces the difficulty of leaching copper sulfide minerals in the subsequent leaching process ;
(2)本发明采用强磁选将浮选尾矿中赤铁矿和/或褐铁矿包裹的、浮选难以回收的铜矿物进行富集,为针对性浸出铁质包裹型铜矿提供原料;同时,强磁选分离出大量低品位含铜磁选尾矿,可大幅减少高温搅拌浸出过程中的矿石量,降低浸出成本;(2) The present invention uses strong magnetic separation to enrich the copper minerals wrapped in hematite and/or limonite in the flotation tailings, which are difficult to recover by flotation, and provide the targeted leaching of iron-wrapped copper ores. Raw materials; at the same time, a large number of low-grade copper-containing magnetic separation tailings are separated by strong magnetic separation, which can greatly reduce the amount of ore in the high-temperature stirring leaching process and reduce the cost of leaching;
(3)本发明采用细磨将铁质包裹的含铜磁选精矿中的铜矿物进一步解离,可提高磁选精矿中铜矿物的浸出速度和浸出率;磁选精矿浸出后的高温矿浆与含铜磁选尾矿混合,利用余热和余酸进一步回收损失于尾矿中的铜矿物,提高铜的回收率;(3) The present invention uses fine grinding to further dissociate the copper minerals in the copper-containing magnetic separation concentrate wrapped in iron, which can increase the leaching speed and leaching rate of copper minerals in the magnetic separation concentrate; The final high-temperature slurry is mixed with copper-containing magnetic separation tailings, and the copper minerals lost in the tailings are further recovered by using waste heat and waste acid to improve the recovery rate of copper;
(4)本发明分级回收矿石中的铜矿物,针对性处理铁质包裹型混合铜矿,利用余热和余酸浸取低品位含铜磁选尾矿中的铜资源,可经济高效地解决铁质包裹型混合铜矿难以回收的技术难题,提高铜资源的综合利用率。(4) The present invention classifies and recovers copper minerals in ores, specifically treats iron-wrapped mixed copper ores, and utilizes waste heat and waste acid to leach copper resources in low-grade copper-containing magnetic separation tailings, which can be solved economically and efficiently. The technical problem that iron-coated mixed copper ore is difficult to recycle can improve the comprehensive utilization rate of copper resources.
附图说明Description of drawings
图1为本发明的工艺流程图。Fig. 1 is a process flow diagram of the present invention.
具体实施方式Detailed ways
下面结合具体实施例对本发明作进一步详细说明,但本发明的保护范围并不限于所述内容。The present invention will be described in further detail below in conjunction with specific examples, but the protection scope of the present invention is not limited to the content described.
实施例1:本实施例的铁质包裹型混合铜矿中铜的质量百分数含量为1.0%,铜的氧化率为70%;以铁质包裹型混合铜矿中的铜含量为100%计,铜在铁质矿物中的含量为35%,铁质矿物为赤铁矿和褐铁矿;Embodiment 1: the mass percent composition of copper in the irony wrapped copper ore of the present embodiment is 1.0%, and the oxidation rate of copper is 70%; Taking the copper content in the iron wrapped copper mixed ore as 100%, The content of copper in iron minerals is 35%, and the iron minerals are hematite and limonite;
如图1所示,一种铁质包裹型混合铜矿的选冶方法,具体步骤如下:As shown in Figure 1, a kind of dressing and smelting method of iron-encapsulated mixed copper ore, concrete steps are as follows:
(1)将铁质包裹型混合铜矿破碎、磨细至-74μm粒级的质量百分含量占70%,调浆至矿浆质量百分浓度为30%,以每吨铁质包裹型混合铜矿计,依次加入400g硫化剂(硫化剂为硫化钠)、300g捕收剂(捕收剂为丁基黄药)和30g起泡剂(起泡剂为2号油),进行一次粗选作业得到一次粗选精矿和一次粗选尾矿,以每吨铁质包裹型混合铜矿计,在一次粗选尾矿中依次加入100g硫化剂、75g捕收剂和15g起泡剂进行二次粗选作业得到二次粗选精矿和二次粗选尾矿,将一次粗选精矿和二次粗选精矿合并进行精选作业得到浮选铜精矿和精选尾矿,精选尾矿返回调浆进行一次粗选作业;(1) Crush and grind the iron-coated mixed copper ore until the mass percentage of -74μm grain size accounts for 70%. In the mine plan, add 400g of vulcanizing agent (the vulcanizing agent is sodium sulfide), 300g of collector (the collector is butyl xanthate) and 30g of foaming agent (the foaming agent is No. 2 oil) in sequence to carry out a roughing operation To obtain the first roughing concentrate and the first roughing tailings, based on per ton of iron-encapsulated mixed copper ore, add 100g of vulcanizing agent, 75g collector and 15g foaming agent to the first roughing tailings for the second The roughing operation obtains the secondary roughing concentrate and the secondary roughing tailings, and the primary roughing concentrate and the secondary roughing concentrate are combined for the beneficiation operation to obtain the flotation copper concentrate and the beneficiation tailings, and the beneficiation The tailings return to pulping for a roughing operation;
(2)在磁场强度为0.8T的条件下,将步骤(1)所得二次粗选尾矿进行磁选得到铁质包裹的含铜磁选精矿和低品位含铜磁选尾矿;(2) Under the condition of a magnetic field strength of 0.8T, magnetically separate the secondary roughing tailings obtained in step (1) to obtain iron-encased copper-containing magnetic separation concentrates and low-grade copper-containing magnetic separation tailings;
(3)根据步骤(2)所得含铜磁选精矿细磨至-45μm粒级的质量百分含量为85%,调浆至矿浆的液固质量比为2:1,在温度为75℃的搅拌条件下,加入浓硫酸得到矿浆混合物A并浸出反应120min得到浸出矿浆,其中矿浆混合物A中硫酸的浓度为35g/L;(3) According to the step (2), the copper-containing magnetic separation concentrate obtained by fine grinding to -45μm particle size is 85% by mass, and the liquid-solid mass ratio of the pulp is 2:1, and the temperature is 75°C Under the stirring condition of the mixture, concentrated sulfuric acid was added to obtain the pulp mixture A and the leaching reaction was carried out for 120 minutes to obtain the leached pulp, wherein the concentration of sulfuric acid in the pulp mixture A was 35g/L;
(4)将步骤(2)所得磁选尾矿加入到步骤(3)所得浸出矿浆并混合均匀得到矿浆混合物B并在搅拌条件下继续浸出180min,固液分离得到含铜浸出液和浸出尾渣,其中矿浆混合物B中的液固质量比为2:1;(4) Add the magnetic separation tailings obtained in step (2) to the leaching pulp obtained in step (3) and mix uniformly to obtain a pulp mixture B, continue leaching for 180 minutes under stirring conditions, and separate solid and liquid to obtain copper-containing leachate and leaching tailings. Wherein the liquid-solid mass ratio in the slurry mixture B is 2:1;
本实施例中铜的综合回收率为90.2%。The comprehensive recovery rate of copper in the present embodiment is 90.2%.
实施例2:本实施例的铁质包裹型混合铜矿中铜的质量百分数含量为1.4%,铜的氧化率为79.2%;以铁质包裹型混合铜矿中的铜含量为100%计,铜在铁质矿物中的含量为39.5%,铁质矿物为赤铁矿和褐铁矿;Embodiment 2: the mass percent content of copper in the irony wrapped copper ore of the present embodiment is 1.4%, and the oxidation rate of copper is 79.2%; Taking the copper content in the iron wrapped mixed copper ore as 100%, The content of copper in iron minerals is 39.5%, and the iron minerals are hematite and limonite;
如图1所示,一种铁质包裹型混合铜矿的选冶方法,具体步骤如下:As shown in Figure 1, a kind of dressing and smelting method of iron-encapsulated mixed copper ore, concrete steps are as follows:
(1)将铁质包裹型混合铜矿破碎、磨细至-74μm粒级的质量百分含量占75%,调浆至矿浆质量百分浓度为35%,以每吨铁质包裹型混合铜矿计,依次加入550g硫化剂(硫化剂为硫化钠)、500g捕收剂(捕收剂为丁基黄药)和75g起泡剂(起泡剂为2号油),进行一次粗选作业得到一次粗选精矿和一次粗选尾矿,以每吨铁质包裹型混合铜矿计,在一次粗选尾矿中依次加入137.5g硫化剂、125g捕收剂和37.5g起泡剂进行二次粗选作业得到二次粗选精矿和二次粗选尾矿,将一次粗选精矿和二次粗选精矿合并进行精选作业得到浮选铜精矿和精选尾矿,精选尾矿返回调浆进行一次粗选作业;(1) Crush and grind the iron-coated mixed copper ore to a mass percentage of -74μm, which accounts for 75% of the mass percentage, and adjust the slurry to a mass percentage concentration of 35%. In the mine plan, add 550g of vulcanizing agent (the vulcanizing agent is sodium sulfide), 500g of collector (the collector is butyl xanthate) and 75g of foaming agent (the foaming agent is No. 2 oil) in order to carry out a roughing operation To obtain the first roughing concentrate and the first roughing tailings, based on per ton of iron-coated mixed copper ore, add 137.5g sulfiding agent, 125g collector and 37.5g foaming agent to the first roughing tailings successively The secondary roughing operation obtains the secondary roughing concentrate and the secondary roughing tailings, and the primary roughing concentrate and the secondary roughing concentrate are combined for the beneficiation operation to obtain the flotation copper concentrate and the concentrated tailings, The selected tailings are returned to the slurry for a roughing operation;
(2)在磁场强度为1.2T的条件下,将步骤(1)所得二次粗选尾矿进行磁选得到铁质包裹的含铜磁选精矿和低品位含铜磁选尾矿;(2) Under the condition of a magnetic field strength of 1.2T, magnetically separate the secondary roughing tailings obtained in step (1) to obtain iron-encased copper-containing magnetic separation concentrates and low-grade copper-containing magnetic separation tailings;
(3)根据步骤(2)所得含铜磁选精矿细磨至-45μm粒级的质量百分含量为88%,调浆至矿浆的液固质量比为2.5:1,在温度为85℃的搅拌条件下,加入浓硫酸得到矿浆混合物A并浸出反应150min得到浸出矿浆,其中矿浆混合物A中硫酸的浓度为60g/L;(3) According to the step (2), the mass percentage of the finely ground copper-containing magnetic separation concentrate to -45μm particle size is 88%. Under the agitation condition of above, add concentrated sulfuric acid to obtain pulp mixture A and leaching reaction for 150min to obtain leached pulp, wherein the concentration of sulfuric acid in pulp mixture A is 60g/L;
(4)将步骤(2)所得磁选尾矿加入到步骤(3)所得浸出矿浆并混合均匀得到矿浆混合物B并在搅拌条件下继续浸出210min,固液分离得到含铜浸出液和浸出尾渣,其中矿浆混合物B中的液固质量比为2.5:1;(4) Add the magnetic separation tailings obtained in step (2) to the leaching pulp obtained in step (3) and mix evenly to obtain a pulp mixture B, continue leaching for 210 minutes under stirring conditions, and separate solid and liquid to obtain copper-containing leachate and leaching tailings. Wherein the liquid-solid mass ratio in the slurry mixture B is 2.5:1;
本实施例中铜的综合回收率为88.7%。The comprehensive recovery rate of copper in the present embodiment is 88.7%.
实施例3:本实施例的铁质包裹型混合铜矿中铜的质量百分数含量为1.8%,铜的氧化率为87%;以铁质包裹型混合铜矿中的铜含量为100%计,铜在铁质矿物中的含量为45%,铁质矿物为赤铁矿和褐铁矿;Embodiment 3: the mass percent composition of copper in the irony wrapped copper ore of the present embodiment is 1.8%, and the oxidation rate of copper is 87%; Taking the copper content in the iron wrapped copper mixed ore as 100%, The content of copper in iron minerals is 45%, and the iron minerals are hematite and limonite;
如图1所示,一种铁质包裹型混合铜矿的选冶方法,具体步骤如下:As shown in Figure 1, a kind of dressing and smelting method of iron-encapsulated mixed copper ore, concrete steps are as follows:
(1)将铁质包裹型混合铜矿破碎、磨细至-74μm粒级的质量百分含量占80%,调浆至矿浆质量百分浓度为40%,以每吨铁质包裹型混合铜矿计,依次加入800g硫化剂(硫化剂为硫化钠)、600g捕收剂(捕收剂为丁基黄药)和100g起泡剂(起泡剂为2号油),进行一次粗选作业得到一次粗选精矿和一次粗选尾矿,以每吨铁质包裹型混合铜矿计,在一次粗选尾矿中依次加入200g硫化剂、150g捕收剂和50g起泡剂进行二次粗选作业得到二次粗选精矿和二次粗选尾矿,将一次粗选精矿和二次粗选精矿合并进行精选作业得到浮选铜精矿和精选尾矿,精选尾矿返回调浆进行一次粗选作业;(1) Crush and grind the iron-coated mixed copper ore until the mass percentage of -74μm grain size accounts for 80%, and adjust the slurry to a mass percentage concentration of 40%, and the iron-coated mixed copper ore per ton In the mine plan, add 800g vulcanizing agent (the vulcanizing agent is sodium sulfide), 600g collector (the collector is butyl xanthate) and 100g foaming agent (the foaming agent is No. 2 oil) in sequence, and carry out a roughing operation To obtain the first roughing concentrate and the first roughing tailings, based on per ton of iron-coated mixed copper ore, add 200g sulfiding agent, 150g collector and 50g foaming agent to the first roughing tailings for the second The roughing operation obtains the secondary roughing concentrate and the secondary roughing tailings, and the primary roughing concentrate and the secondary roughing concentrate are combined for the beneficiation operation to obtain the flotation copper concentrate and the beneficiation tailings, and the beneficiation The tailings return to pulping for a roughing operation;
(2)在磁场强度为1.4T的条件下,将步骤(1)所得二次粗选尾矿进行磁选得到铁质包裹的含铜磁选精矿和低品位含铜磁选尾矿;(2) Under the condition of a magnetic field strength of 1.4T, magnetically separate the secondary roughing tailings obtained in step (1) to obtain iron-encased copper-containing magnetic separation concentrates and low-grade copper-containing magnetic separation tailings;
(3)根据步骤(2)所得含铜磁选精矿细磨至-45μm粒级的质量百分含量为90%,调浆至矿浆的液固质量比为3:1,在温度为90℃的搅拌条件下,加入浓硫酸得到矿浆混合物A并浸出反应180min得到浸出矿浆,其中矿浆混合物A中硫酸的浓度为80g/L;(3) According to the step (2), the copper-containing magnetic separation concentrate obtained by finely grinding to -45μm particle size is 90% by mass, and the liquid-solid mass ratio of the slurry is 3:1, and the temperature is 90°C Under the stirring condition of the mixture, add concentrated sulfuric acid to obtain pulp mixture A and leaching reaction for 180min to obtain leached pulp, wherein the concentration of sulfuric acid in pulp mixture A is 80g/L;
(4)将步骤(2)所得磁选尾矿加入到步骤(3)所得浸出矿浆并混合均匀得到矿浆混合物B并在搅拌条件下继续浸出240min,固液分离得到含铜浸出液和浸出尾渣,其中矿浆混合物B中的液固质量比为3:1;(4) Add the magnetic separation tailings obtained in step (2) to the leaching pulp obtained in step (3) and mix uniformly to obtain a pulp mixture B, continue leaching for 240 minutes under stirring conditions, and separate solid and liquid to obtain copper-containing leachate and leaching tailings. Wherein the liquid-solid mass ratio in the slurry mixture B is 3:1;
本实施例中铜的综合回收率为86.5%。The comprehensive recovery rate of copper in the present embodiment is 86.5%.
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