CN118223077A - A method for purifying cobalt electrolyte - Google Patents
A method for purifying cobalt electrolyte Download PDFInfo
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- CN118223077A CN118223077A CN202410223459.1A CN202410223459A CN118223077A CN 118223077 A CN118223077 A CN 118223077A CN 202410223459 A CN202410223459 A CN 202410223459A CN 118223077 A CN118223077 A CN 118223077A
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- Prior art keywords
- cobalt
- anolyte
- filtration
- filter
- current density
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- 239000010941 cobalt Substances 0.000 title claims abstract description 36
- 229910017052 cobalt Inorganic materials 0.000 title claims abstract description 36
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 title claims abstract description 36
- 239000003792 electrolyte Substances 0.000 title claims abstract description 18
- 238000000034 method Methods 0.000 title claims abstract description 18
- 238000001914 filtration Methods 0.000 claims abstract description 28
- 239000007788 liquid Substances 0.000 claims abstract description 20
- 238000006298 dechlorination reaction Methods 0.000 claims abstract description 14
- 239000002245 particle Substances 0.000 claims abstract description 10
- 239000012535 impurity Substances 0.000 claims abstract description 8
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 claims abstract description 5
- 229910052801 chlorine Inorganic materials 0.000 claims abstract description 5
- 239000000460 chlorine Substances 0.000 claims abstract description 5
- 238000011085 pressure filtration Methods 0.000 claims abstract 2
- GVPFVAHMJGGAJG-UHFFFAOYSA-L cobalt dichloride Chemical compound [Cl-].[Cl-].[Co+2] GVPFVAHMJGGAJG-UHFFFAOYSA-L 0.000 claims description 5
- 239000004744 fabric Substances 0.000 claims description 4
- 239000000706 filtrate Substances 0.000 claims description 2
- 239000000203 mixture Substances 0.000 claims 2
- 238000004070 electrodeposition Methods 0.000 claims 1
- 238000009472 formulation Methods 0.000 claims 1
- 230000003749 cleanliness Effects 0.000 abstract description 6
- 238000004140 cleaning Methods 0.000 abstract description 2
- 238000009854 hydrometallurgy Methods 0.000 abstract description 2
- 239000000243 solution Substances 0.000 description 6
- 230000009286 beneficial effect Effects 0.000 description 2
- 239000008151 electrolyte solution Substances 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 239000011859 microparticle Substances 0.000 description 2
- KJTLSVCANCCWHF-UHFFFAOYSA-N Ruthenium Chemical compound [Ru] KJTLSVCANCCWHF-UHFFFAOYSA-N 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 238000005363 electrowinning Methods 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 229910052707 ruthenium Inorganic materials 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25C—PROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
- C25C1/00—Electrolytic production, recovery or refining of metals by electrolysis of solutions
- C25C1/06—Electrolytic production, recovery or refining of metals by electrolysis of solutions or iron group metals, refractory metals or manganese
- C25C1/08—Electrolytic production, recovery or refining of metals by electrolysis of solutions or iron group metals, refractory metals or manganese of nickel or cobalt
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Electrolytic Production Of Metals (AREA)
Abstract
Description
技术领域Technical Field
本发明属于湿法冶金技术领域,具体涉及一种净化钴电解液的方法。The invention belongs to the technical field of hydrometallurgy, and in particular relates to a method for purifying cobalt electrolyte.
背景技术Background technique
电积钴在制备时,通常先将氯化钴溶液经深度净化除杂后与电积槽溢流出来的阴极液、脱氯后的阳极液配液,然后进入电积槽;在由种板产出的始极片经剪切加工后为阴极,阳极为钛涂钌不溶阳极,在直流电的作用下,阴极析出电钴,阳极产出氯气,最后阴极经过一段时间电积后产出电钴板,经烫洗后进行剪切、包装入库,但由于阳极产出的氯气具有强氧化性,使得部分隔膜架与隔膜袋粉化进入电积体系进而影响电积液洁净度,从而影响电积钴物理质量。When preparing electrolytic cobalt, the cobalt chloride solution is usually first deeply purified and impurities removed, and then mixed with the cathode liquid overflowing from the electrolytic cell and the anode liquid after dechlorination, and then enters the electrolytic cell; the starting electrode produced by the seed plate is sheared to become the cathode, and the anode is a titanium-coated ruthenium insoluble anode. Under the action of direct current, electrolytic cobalt is precipitated at the cathode and chlorine is produced at the anode. Finally, after a period of electrolysis, the cathode produces an electrolytic cobalt plate, which is sheared, sheared, packaged and stored. However, since the chlorine produced by the anode is highly oxidizing, part of the diaphragm frame and diaphragm bag are powdered and enter the electrolytic system, thereby affecting the cleanliness of the electrolytic solution and thus affecting the physical quality of the electrolytic cobalt.
发明内容Summary of the invention
本发明的目的是提供一种净化钴电解液的方法,用于解决现有电积钴在制备时电积液洁净度低从而影响电积钴物理质量的问题。The purpose of the present invention is to provide a method for purifying cobalt electrolyte, which is used to solve the problem that the cleanliness of the electrolytic solution is low during the preparation of the existing electrolytic cobalt, thereby affecting the physical quality of the electrolytic cobalt.
为实现上述目的,本发明提供如下技术方案:一种净化钴电解液的方法,具体按照以下步骤实施:To achieve the above object, the present invention provides the following technical solution: a method for purifying cobalt electrolyte, which is specifically implemented according to the following steps:
具体按照以下步骤实施:Follow these steps to implement it:
步骤1、将阳极液收集后输送至脱氯系统进行脱氯,去除阳极液中溶解的氯气,阳极液流量与电流密度相关;Step 1: Collect the anolyte and transport it to the dechlorination system for dechlorination to remove the chlorine dissolved in the anolyte. The flow rate of the anolyte is related to the current density.
步骤2、将步骤1中脱氯后的阳极液与槽尾溢流的阴极液输送至压滤机一次压滤去除不溶性颗粒与杂物,压滤流量与电流密度相关;Step 2, transporting the anolyte after dechlorination in step 1 and the cathode liquid overflowing from the tail of the tank to a filter press for one-time filtration to remove insoluble particles and impurities, and the filtration flow rate is related to the current density;
步骤3、将步骤2中的一次压滤后的阳极液输送至精密过滤器精密过滤去除不溶性微粒,精密过滤流量与电流密度相关;Step 3, transporting the anolyte after the primary filtration in step 2 to a precision filter for precision filtration to remove insoluble particles, wherein the precision filtration flow rate is related to the current density;
步骤4、将步骤3所述的精密过滤后阳极液与除杂后高浓度氯化钴溶液配液返入电积系统,钴浓度与电流密度相关。Step 4: returning the anode liquid after precise filtration described in step 3 and the high-concentration cobalt chloride solution after impurities removal to the electrowinning system, wherein the cobalt concentration is related to the current density.
进一步的,所述步骤1的阳极液流量为120-160ml/(A·m2·槽)。Furthermore, the anolyte flow rate of step 1 is 120-160 ml/(A·m2·tank).
进一步的,所述步骤2的阴极液流量为40-80ml/(A·m2·槽),一次压滤液流量为160-240 ml/(A·m2·槽),滤布型号为747、858、单丝滤布中的一种。Furthermore, the cathode liquid flow rate of step 2 is 40-80 ml/(A·m2·slot), the primary filtrate flow rate is 160-240 ml/(A·m2·slot), and the filter cloth model is one of 747, 858, and monofilament filter cloth.
进一步的,所述步骤3的精密过滤流量为150-230 ml/(A·m2·槽)。Furthermore, the precision filtration flow rate of step 3 is 150-230 ml/(A·m2·slot).
进一步的,所述步骤4的配制液钴浓度为50-80g/L。Furthermore, the cobalt concentration of the prepared solution in step 4 is 50-80 g/L.
与现有技术相比,本发明的有益效果如下:Compared with the prior art, the present invention has the following beneficial effects:
本发明具有以下有益效果:The present invention has the following beneficial effects:
该工艺采用压滤机与精密过滤器二次过滤,将不溶性颗粒、杂物、不溶性微粒分开过滤,提升钴电解液洁净度,减少清槽作业,降低劳动强度,减小安全风险;通过去除钴电解液不溶性微粒提升电积钴物理质量。This process uses a filter press and a precision filter for secondary filtration to separate insoluble particles, debris, and insoluble microparticles, thereby improving the cleanliness of the cobalt electrolyte, reducing tank cleaning operations, lowering labor intensity, and reducing safety risks; and improving the physical quality of electrolytic cobalt by removing insoluble microparticles from the cobalt electrolyte.
附图Attached photos
图1为钴电解液净化流程图。Figure 1 is a flow chart of cobalt electrolyte purification.
具体实施方式Detailed ways
下面结合具体实施方式对本发明进行详细说明。The present invention is described in detail below in conjunction with specific implementation modes.
一种净化钴电解液的方法,具体按照以下步骤实施:A method for purifying cobalt electrolyte is implemented in the following steps:
实施例一Embodiment 1
实验过程:experiment procedure:
步骤1、将阳极液收集后输送至脱氯系统进行脱氯,阳极液流量140ml/(A·m2·槽)。Step 1: Collect the anolyte and transport it to the dechlorination system for dechlorination. The anolyte flow rate is 140 ml/(A·m2·tank).
步骤2、脱氯后的阳极液与槽尾溢流的阴极液输送至压滤机一次压滤,压滤流量200ml/(A·m2·槽)。Step 2: The dechlorinated anolyte and the cathode liquid overflowing from the tail of the tank are transported to the filter press for one filtration, with a filtration flow rate of 200 ml/(A·m2·tank).
步骤3、一次压滤后液输送至精密过滤器精密过滤,精密过滤流量200ml/(A·m2·槽)。Step 3: After the first filtration, the liquid is transported to the precision filter for precision filtration, and the precision filtration flow rate is 200 ml/(A·m2·tank).
步骤4、精密过滤后液与除杂后高浓度氯化钴溶液配液返入电积系统,配制液钴浓度与60g/L。Step 4: The liquid after precision filtration and the high-concentration cobalt chloride solution after impurities removal are mixed and returned to the electrolytic system to prepare the cobalt concentration of the liquid to 60g/L.
实验结果:Experimental results:
实验结果见表1。The experimental results are shown in Table 1.
表1电积钴物理质量Table 1 Physical quality of electrolytic cobalt
实施例一实验结果表明,通过实施例一试验过程的钴电解液洁净度高,产出钴板物理质量较好。The experimental results of Example 1 show that the cobalt electrolyte obtained through the experimental process of Example 1 has high cleanliness and the physical quality of the produced cobalt plate is good.
实施例二:Embodiment 2:
实验过程:experiment procedure:
步骤1、将阳极液收集后输送至脱氯系统进行脱氯,阳极液流量160ml/(A·m2·槽)。Step 1: Collect the anolyte and transport it to the dechlorination system for dechlorination. The anolyte flow rate is 160 ml/(A·m2·tank).
步骤2、脱氯后的阳极液与槽尾溢流的阴极液输送至压滤机一次压滤,压滤流量230ml/(A·m2·槽)。Step 2: The dechlorinated anolyte and the cathode liquid overflowing from the tail of the tank are transported to the filter press for one filtration, and the filtration flow rate is 230 ml/(A·m2·tank).
步骤3、一次压滤后液输送至精密过滤器精密过滤,精密过滤流量230ml/(A·m2·槽)。Step 3: After the first filtration, the liquid is transported to the precision filter for precision filtration, and the precision filtration flow rate is 230 ml/(A·m2·tank).
步骤4、精密过滤后液与除杂后高浓度氯化钴溶液配液返入电积系统,配制液钴浓度与65g/L。Step 4: The liquid after precision filtration and the high-concentration cobalt chloride solution after impurities removal are mixed and returned to the electrolytic system to prepare the cobalt concentration of the liquid to 65g/L.
实验结果:Experimental results:
实验结果见表2。The experimental results are shown in Table 2.
表2电积钴物理质量Table 2 Physical quality of electrolytic cobalt
实施例二实验结果表明,通过实施例二试验过程的钴电解液洁净度高,产出钴板物理质量较好。The experimental results of Example 2 show that the cobalt electrolyte obtained through the experimental process of Example 2 has high cleanliness and the physical quality of the produced cobalt plate is good.
Claims (5)
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Country or region after: China Address after: No. 31 Beijing Road, Beijing Road Street, Jinchuan District, Jinchang City, Gansu Province 737100 Applicant after: Jinchuan Group Nickel Cobalt Co.,Ltd. Applicant after: LANZHOU JINCHUAN ADVANGCED MATERIALS TECHNOLOGY Co.,Ltd. Address before: No. 2 Lanzhou Road, Beijing Road Street, Jinchuan District, Jinchang City, Gansu Province Applicant before: Jinchuan Group Nickel Cobalt Co.,Ltd. Country or region before: China Applicant before: LANZHOU JINCHUAN ADVANGCED MATERIALS TECHNOLOGY Co.,Ltd. |