CN116065197A - A kind of method utilizing electrolyzer to prepare gold electrolyte - Google Patents
A kind of method utilizing electrolyzer to prepare gold electrolyte Download PDFInfo
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Abstract
Description
技术领域technical field
本发明属于黄金电解精炼技术领域,涉及一种金电解液的制备工艺方法。The invention belongs to the technical field of gold electrolytic refining, and relates to a preparation process method of gold electrolyte.
背景技术Background technique
作为黄金精炼的重要生产方法,黄金电解精炼工艺在粗金提纯生产过程中已经被广泛应用。它属于利用含有一定浓度氯金酸和氯化氢的水溶液作为介质进行粗金提纯的精炼方法。黄金电解精炼的首要工序是为金电解造液,即制作氯金酸水溶液。所述氯金酸水溶液的传统制作方法分为以下两种。As an important production method of gold refining, the gold electrolytic refining process has been widely used in the production process of crude gold purification. It belongs to the refining method that uses an aqueous solution containing a certain concentration of chloroauric acid and hydrogen chloride as a medium for crude gold purification. The primary process of gold electrolytic refining is to make liquid for gold electrolysis, that is, to make an aqueous solution of chloroauric acid. The traditional preparation method of described chloroauric acid aqueous solution is divided into following two kinds.
一种为将粗金粉化成较细的颗粒金,或者利用碾片机将黄金碾压成较薄的金片,然后在耐腐蚀的容器内采用化学溶解法将金溶解,然后过滤得到含金溶液。将含金溶液转移至电解槽作为介质(即金电解液)用于金电解精炼。One is to pulverize coarse gold into finer particles of gold, or use a flaker to crush gold into thinner gold flakes, then dissolve the gold in a corrosion-resistant container by chemical dissolution, and then filter to obtain a gold-containing solution . The gold-containing solution is transferred to an electrolytic cell as a medium (ie, gold electrolyte) for gold electrorefining.
比如,公布号为CN110863215A 的中国发明专利公开了一种“一种用金电解阳极泥制备金电解液的方法”。该专利中的技术工艺涉及金电解液制作,其原料为黄金电解精炼过程中产出的副产品阳极泥。虽然阳极泥含金品位较高,但也含有一定量杂质,配制电解液需要先去除杂质,同时其粒度较细,这相当于省去化学溶解制作电解液的粉化过程。该专利中电解液制作方法是:先将阳极泥用王水溶解、过滤,然后还原去除杂质而得到含金纯度更高的金粉(粒度较细),然后再用王水溶解,得到含有一定浓度氯金酸的电解液,然后将其转移至金电解槽进行金电解精炼。它属于“将粗金粉化成较细的颗粒金,或者利用碾片机将黄金碾压成较薄的金片,然后在耐腐蚀的容器内采用化学溶解法将金溶解,然后过滤得到含金溶液。将含金溶液转移至电解槽作为介质(即金电解液)用于金电解精炼”的范畴。For example, the Chinese invention patent with the publication number CN110863215A discloses a "method for preparing gold electrolyte from gold electrolysis anode slime". The technical process in this patent involves the production of gold electrolyte, and its raw material is anode slime, a by-product produced during the gold electrolytic refining process. Although the anode slime contains a high grade of gold, it also contains a certain amount of impurities. To prepare the electrolyte, impurities need to be removed first. At the same time, its particle size is finer, which is equivalent to eliminating the pulverization process of chemical dissolution to make the electrolyte. The electrolyte preparation method in this patent is: first dissolve and filter the anode slime with aqua regia, then reduce and remove impurities to obtain gold powder with higher gold purity (fine particle size), and then dissolve it with aqua regia to obtain gold powder with a certain concentration Electrolyte of chloroauric acid, which is then transferred to a gold electrolytic cell for gold electrorefining. It belongs to the category of "pulverizing coarse gold into finer particles of gold, or using a flake machine to crush gold into thinner gold flakes, and then dissolving the gold by chemical dissolution in a corrosion-resistant container, and then filtering to obtain a gold-containing solution." .The transfer of gold-containing solution to an electrolytic cell as a medium (ie, gold electrolyte) for gold electrorefining" category.
再比如,公布号为CN104047024A的中国发明专利公开了一种“一次电解精炼制备高纯金的工艺”。该工艺涉及金电解液配制为取黄金原料纯度为99%的粗金,粉化或碾片后加入钛反应釜,然后加入一定比例的盐酸和硝酸并加热搅拌溶解黄金,反应结束后,过滤得金电解液,然后将其转移至金电解槽进行金电解精炼。它属于“将粗金粉化成较细的颗粒金,或者利用碾片机将黄金碾压成较薄的金片,然后在耐腐蚀的容器内采用化学溶解法将金溶解,然后过滤得到含金溶液。将含金溶液转移至电解槽作为介质(即金电解液)用于金电解精炼”的范畴。For another example, the Chinese invention patent with publication number CN104047024A discloses a "process for preparing high-purity gold by one-time electrolytic refining". The process involves the preparation of the gold electrolyte to take crude gold with a purity of 99% of the gold raw material, pulverize or flake it and add it to a titanium reactor, then add a certain proportion of hydrochloric acid and nitric acid and heat and stir to dissolve the gold. After the reaction is over, it is filtered to obtain Gold electrolyte, which is then transferred to a gold electrolytic cell for gold electrorefining. It belongs to the category of "pulverizing coarse gold into finer particles of gold, or using a flake machine to crush gold into thinner gold flakes, and then dissolving the gold by chemical dissolution in a corrosion-resistant container, and then filtering to obtain a gold-containing solution." .The transfer of gold-containing solution to an electrolytic cell as a medium (ie, gold electrolyte) for gold electrorefining" category.
另一种为隔膜槽电解法,它是将粗金熔铸成阳极板后挂入含有一定浓度盐酸的隔膜电解槽,此隔膜为阻隔金离子通过而允许氢离子和氯离子自由通过并耐高浓度盐酸,通入直流电进行电解造液的方法。The other is the diaphragm cell electrolysis method, which is to melt and cast crude gold into an anode plate and then hang it into a diaphragm electrolytic cell containing a certain concentration of hydrochloric acid. This diaphragm allows hydrogen ions and chloride ions to pass through freely and is resistant to high concentration Hydrochloric acid, the method of passing through direct current to carry out electrolytic solution.
比如,公布号为CN212771009U的中国实用新型专利公开了一种“黄金电解提纯自动化精炼设备”。该专利涉及制作离子(即氯金酸[AuCl4]ˉ离子)和氯化氢的水溶液(即金电解液制作),它利用了阳离子交换膜,使溶解的氯金酸不能运动到阴极析出,属于传统的隔膜槽电解法制作电解液中的一种。For example, the Chinese utility model patent whose publication number is CN212771009U discloses a kind of "gold electrolytic purification automatic refining equipment". This patent involves the production of an aqueous solution of ions (that is, chloroauric acid [AuCl4] ions) and hydrogen chloride (that is, the production of gold electrolyte), which uses a cation exchange membrane to prevent the dissolved chloroauric acid from moving to the cathode for precipitation, which belongs to the traditional diaphragm. One of the electrolytes produced by cell electrolysis.
再比如,公布号为CN111304695A的中国发明专利公开了“一种金精炼设备及方法”。For another example, the Chinese invention patent whose publication number is CN111304695A discloses "a kind of gold refining equipment and method".
其涉及“本方案无需配置电解液,直接将粗金阳极板挂在第一槽体的阳极棒上”,从专利上下文看也涉及隔膜电解,属于传统的隔膜槽电解法制作电解液中的一种。It involves "this solution does not need to configure an electrolyte, and directly hangs the thick gold anode plate on the anode rod of the first tank body". From the perspective of the patent context, it also involves diaphragm electrolysis, which belongs to one of the traditional methods of diaphragm cell electrolysis to produce electrolyte. kind.
以上两种金电解造液方法工序复杂繁琐,生产周期长,生产成本高,黄金损耗大。化学法易产生有毒有害气体,污染环境。隔膜槽电解法易产生含金废旧隔膜等含金固废,需要进一步处理回收金。The above two methods for making liquid by gold electrolysis have complex and cumbersome procedures, long production cycle, high production cost and large gold loss. Chemical methods are prone to produce toxic and harmful gases, polluting the environment. Diaphragm tank electrolysis is prone to produce gold-containing solid waste such as gold-containing waste diaphragms, which need further treatment to recover gold.
发明内容Contents of the invention
本发明所要解决的技术问题是,提供一种利用电解槽制备金电解液的方法,造液工序更简单、造液成本更低、电解精炼周期更短、黄金损耗更少并且降低有毒有害气体和含金废旧隔膜。The technical problem to be solved by the present invention is to provide a method for preparing gold electrolyte using an electrolytic cell, which has simpler liquid-making process, lower liquid-making cost, shorter electrolytic refining cycle, less gold loss, and reduces toxic and harmful gases and Gold-containing scrap diaphragm.
本发明采用的技术方案如下:The technical scheme that the present invention adopts is as follows:
一种利用电解槽制备金电解液的方法,包括以下步骤:将阳极板和阴极板装入电解槽并在电解槽中加入盐酸和作为氧化剂的硝酸;加热并控制电解槽内混酸溶液温度,开启整流器并控制电解电压;连续电解至配制电解液终点;其中,阳极板由粗金熔铸而成;其中,配制电解液终点的判定条件是:液面不再产生气泡,或者阴极析出电金覆盖极板面。A method for preparing gold electrolyte using an electrolytic cell, comprising the following steps: loading an anode plate and a negative plate into an electrolytic cell and adding hydrochloric acid and nitric acid as an oxidant into the electrolytic cell; heating and controlling the temperature of the mixed acid solution in the electrolytic cell, and opening Rectifier and control the electrolysis voltage; continuous electrolysis to the end of the preparation of the electrolyte; wherein, the anode plate is made of coarse gold melting and casting; among them, the judgment condition of the end of the preparation of the electrolyte is: no bubbles are generated on the liquid surface, or the electrode is covered with electrolytic gold by the cathode Board surface.
优选地,电解槽中所加入盐酸和硝酸的体积比为:36-38%分析纯盐酸:65-68%分析纯硝酸=(7-9):1;混酸液面高于电解槽循环溢流堰并低于电解袋上沿。Preferably, the volume ratio of hydrochloric acid and nitric acid added to the electrolytic cell is: 36-38% analytical pure hydrochloric acid: 65-68% analytical pure nitric acid = (7-9): 1; the mixed acid liquid level is higher than the electrolytic cell circulation overflow The weir is lower than the upper edge of the electrolytic bag.
优选地,电解槽内混酸溶液温度控制在50~70℃。Preferably, the temperature of the mixed acid solution in the electrolytic cell is controlled at 50-70°C.
优选地,电解电压为工作直流电压2~2.5V。Preferably, the electrolysis voltage is a working DC voltage of 2-2.5V.
优选地,所述阴极板材质为纯钛。Preferably, the cathode plate is made of pure titanium.
优选地,通过调节硝酸的加入量控制电解液含金浓度。Preferably, the concentration of gold in the electrolyte is controlled by adjusting the amount of nitric acid added.
优选地,所述阴极板为四边形板材,三个边沿被绝缘材料密封。Preferably, the cathode plate is a quadrangular plate, and three edges are sealed by insulating materials.
优选地,所述粗金含金纯度不小于98%。Preferably, the crude gold contains gold with a purity of not less than 98%.
本发明具有以下积极效果:The present invention has the following positive effects:
按照本发明的方法,粗金(即制作金电解液原料)无需进行粉化制成较细颗粒后进行化学法溶解,也无需隔膜槽,而是熔铸成阳极板挂入电解槽,加入配比一定浓度的盐酸和硝酸混合溶液,在电压电流和溶解药剂电化学溶解双重作用下,阳极金加速溶解形成氯金酸进入溶液,阴极表面所析出金粒径细微,活性较强,则立刻被硝酸和盐酸所溶解,抑制了其阴极金的析出。这样在未利用隔膜的情况下,直接使阳极金不断溶解产生氯金酸离子滞留于溶液中并且浓度不断增加,形成金电解液。该制作电解液方法更加突出的优点是控制硝酸的加入量即能控制电解液含金浓度,当加入的硝酸消耗殆尽时,无需转移电解液便可直接继续进行黄金电解精炼,产出合格金产品。According to the method of the present invention, coarse gold (that is, the raw material for making gold electrolyte) does not need to be pulverized into finer particles and then chemically dissolved, and there is no need for a diaphragm tank. A mixed solution of hydrochloric acid and nitric acid with a certain concentration, under the double action of voltage and current and the electrochemical dissolution of the dissolving agent, the anode gold accelerates to dissolve and form chloroauric acid into the solution. Dissolved with hydrochloric acid, inhibiting the precipitation of cathode gold. In this way, without using the diaphragm, the anode gold is directly dissolved to generate chloroauric acid ions to stay in the solution and the concentration is continuously increased to form a gold electrolyte. The more prominent advantage of this method of making electrolyte is that the concentration of gold in the electrolyte can be controlled by controlling the amount of nitric acid added. When the added nitric acid is exhausted, the electrolytic refining of gold can be continued directly without transferring the electrolyte, and qualified gold can be produced. product.
本方法省去了粗金粉化后化学溶解和隔膜电解制成金电解液,然后再将金电解液转移至电解槽精炼的工序,工序简化,生产周期大幅缩短。同时避免了化学法易产生有毒有害气体污染环境、隔膜槽电解法易产生含金废旧隔膜等含金固废需要进一步处理回收金的缺点。该发明简化了金电解液制作工序,同时具有降低电解液生产制作成本、减少黄金损耗(工序越多,金损耗越大)以及减轻员工劳动强度等优点。The method omits the process of chemically dissolving the coarse gold after pulverization and electrolyzing the diaphragm to form a gold electrolyte, and then transferring the gold electrolyte to an electrolytic cell for refining, thereby simplifying the process and greatly shortening the production cycle. At the same time, it avoids the disadvantages that the chemical method is easy to produce toxic and harmful gases to pollute the environment, and the electrolytic method of the diaphragm tank is easy to generate gold-containing waste diaphragms and other gold-containing solid wastes that require further processing to recover gold. The invention simplifies the production process of the gold electrolyte, and at the same time has the advantages of reducing the production cost of the electrolyte, reducing gold loss (the more processes, the greater the gold loss), and reducing the labor intensity of employees.
实施方式Implementation
下面结合实施例进一步说明本发明。Below in conjunction with embodiment further illustrate the present invention.
本发明利用电解槽制备金电解液的方法用于黄金电解精炼提纯,该工艺包括步骤S1至S7。The method of the present invention for preparing gold electrolyte by using an electrolytic cell is used for electrolytic refining and purification of gold, and the process includes steps S1 to S7.
S1:粗金熔铸阳极板为取40000g含金纯度为99.90%的黄金原料,在中频炉中熔化后浇铸成20块阳极板,每块阳极板重量约为2000g。S1: The crude gold melting and casting anode plate is made of 40000g of gold raw material with a gold content of 99.90% purity, which is melted in an intermediate frequency furnace and cast into 20 anode plates, each weighing about 2000g.
S2:将浸入电解液的阴极板三个边沿加绝缘材料密封,其中阴极板为纯钛板,用液化气火焰将浸入电解液的钛阴极板三个边沿加热后,热塑上聚丙烯粉并抚平表面,使其整洁光滑,所起作用主要用于钛极板边沿绝缘,防止阴极析出电金后将钛板包裹致使电金较难取下。S2: Seal the three edges of the cathode plate immersed in the electrolyte with insulating materials. The cathode plate is a pure titanium plate. After heating the three edges of the titanium cathode plate immersed in the electrolyte with a liquefied gas flame, thermoplastic polypropylene powder and Smooth the surface to make it clean and smooth. It is mainly used for edge insulation of the titanium plate to prevent the cathode from depositing electro-gold and wrapping the titanium plate so that it is difficult to remove the electro-gold.
S3:阳极板和阴极板装槽,其中所述阳极板挂在阳极导电棒钛钩上,每十块阳极板为一电解槽(即一个电解槽中安装十块阳极板),然后套入丙纶材质的电解袋内,装槽前需提前检查电解袋是否完好、无破损、无漏洞,否则更换新电解袋;阴极板挂在阴极导电棒上并螺丝紧固,以保持良好导电性。S3: The anode plate and the cathode plate are installed in the tank, wherein the anode plate is hung on the titanium hook of the anode conductive rod, and every ten anode plates is an electrolytic cell (that is, ten anode plates are installed in one electrolytic cell), and then inserted into the polypropylene In the electrolytic bag made of high-quality materials, it is necessary to check in advance whether the electrolytic bag is intact, undamaged, and leak-free before loading into the tank, otherwise, replace it with a new electrolytic bag; the cathode plate is hung on the cathode conductive rod and fastened with screws to maintain good conductivity.
S4:每个小电解槽加入18.7L30%分析纯盐酸和2.3L60%分析纯硝酸,共2个小电解槽,使混酸液面高于电解槽循环溢流堰,低于电解袋上沿。S4: Add 18.7L 30% analytically pure hydrochloric acid and 2.3L 60% analytically pure nitric acid to each small electrolytic cell, making a total of 2 small electrolytic cells, so that the mixed acid liquid level is higher than the electrolytic cell circulation overflow weir and lower than the upper edge of the electrolytic bag.
S5:加热装置为800W石英加热棒,控温装置为Pt100衬四氟测温热电偶,将混酸溶液升温至50℃以上。S5: The heating device is an 800W quartz heating rod, and the temperature control device is a Pt100-lined PTFE temperature-measuring thermocouple to raise the temperature of the mixed acid solution to above 50°C.
S6:开启电解,控制整流器直流工作电压2.5V,期间维护电解槽,保持混酸液位高度,期间液面蒸发多洗补加盐酸。S6: Turn on the electrolysis, control the DC working voltage of the rectifier to 2.5V, maintain the electrolytic cell during the period, keep the liquid level of the mixed acid, and add hydrochloric acid after the liquid surface evaporates during the period.
S7:连续电解时间7h,电解槽内循环混酸液面回复平静,无气泡产生,同时阴极表面析出一定量电金并且阴极析出电金完全覆盖极板面,金电解造液已经完成。S7: After continuous electrolysis for 7 hours, the circulating acid liquid level in the electrolytic cell returns to calm, no bubbles are generated, and at the same time, a certain amount of electrolytic gold is deposited on the surface of the cathode, and the electrolytic gold deposited on the cathode completely covers the surface of the electrode plate, and the electrolysis of gold has been completed.
提取阳极金残极并清洗干净,烘干称重约为22.80kg;取出阴极电金,烘干熔炼称重约为9.65kg;清理电解袋阳极泥烘干称重约为1.22kg;电解液体积约为42L,经计算电解液含金浓度约为150g/L,符合本发明黄金电解精炼电解液生产指标制作要求。如需求电解液含金大于或小于此浓度可适当增减硝酸加入体积比例。Extract the anode gold residue and clean it, dry and weigh about 22.80kg; take out the cathode gold, dry and smelt and weigh about 9.65kg; clean up the anode slime of the electrolytic bag and dry and weigh about 1.22kg; the volume of the electrolyte It is about 42L, and the gold-containing concentration of the electrolyte is calculated to be about 150g/L, which meets the production index production requirements of the gold electrolytic refining electrolyte of the present invention. If the gold content in the electrolytic solution is required to be greater or less than this concentration, the volume ratio of nitric acid can be appropriately increased or decreased.
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| CN118127574A (en) * | 2024-05-10 | 2024-06-04 | 山东黄金冶炼有限公司 | A method for extending the production cycle of gold electrolyte |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH11222693A (en) * | 1998-02-06 | 1999-08-17 | Dowa Mining Co Ltd | Method for electrolytically refining gold and device therefor |
| CN101122032A (en) * | 2007-05-21 | 2008-02-13 | 江西铜业集团公司 | One-step producing technique for high-purity gold |
| CN101985691A (en) * | 2010-12-01 | 2011-03-16 | 金川集团有限公司 | Method for preparing high-purity gold |
| CN103590071A (en) * | 2013-11-01 | 2014-02-19 | 白银有色集团股份有限公司 | Method for enhancing gold precipitation grade in gold electrorefining process |
| CN208279695U (en) * | 2018-06-12 | 2018-12-25 | 洛阳三轩金研环保科技有限公司 | A kind of efficient Gold electrolysis purifier for gold refining |
-
2023
- 2023-03-15 CN CN202310250011.4A patent/CN116065197A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH11222693A (en) * | 1998-02-06 | 1999-08-17 | Dowa Mining Co Ltd | Method for electrolytically refining gold and device therefor |
| CN101122032A (en) * | 2007-05-21 | 2008-02-13 | 江西铜业集团公司 | One-step producing technique for high-purity gold |
| CN101985691A (en) * | 2010-12-01 | 2011-03-16 | 金川集团有限公司 | Method for preparing high-purity gold |
| CN103590071A (en) * | 2013-11-01 | 2014-02-19 | 白银有色集团股份有限公司 | Method for enhancing gold precipitation grade in gold electrorefining process |
| CN208279695U (en) * | 2018-06-12 | 2018-12-25 | 洛阳三轩金研环保科技有限公司 | A kind of efficient Gold electrolysis purifier for gold refining |
Non-Patent Citations (2)
| Title |
|---|
| 吴玉: "金的电解精炼技术条件的控制", 中国有色冶金, no. 11, 28 October 1985 (1985-10-28), pages 24 - 26 * |
| 甘肃省生态环境厅: "2020年6月1日甘肃省生态环境厅对建设项目环境影响后评价文件进行备案受理情况的公示", pages 84 - 85, Retrieved from the Internet <URL:https://sthj.gansu.gov.cn/sthj/c113041/202006/e07ec0d445834b028810f51b54bbaa01.shtml> * |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN118127574A (en) * | 2024-05-10 | 2024-06-04 | 山东黄金冶炼有限公司 | A method for extending the production cycle of gold electrolyte |
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