CN114921815A - Method for replacing magnesium electrolytic cell anode without stopping cell - Google Patents
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Abstract
Description
技术领域technical field
本发明属于冶金技术领域,具体涉及一种不停槽更换镁电解槽阳极的方法。The invention belongs to the technical field of metallurgy, and in particular relates to a method for replacing the anode of a magnesium electrolytic cell without a bath.
背景技术Background technique
镁电解是制备金属镁的重要方法,多极槽镁电解技术在海绵钛生产中作为配套工艺被越来越多的企业采用,是镁钛联合企业实现镁钛-氯循环的关键工序,而如何节能降耗、延长槽使用寿命、提高单槽生产能力,一直是企业迫切需要解决的课题。电解槽阳极的使用周期一般为24个月,但在实际生产中,石墨阳极的平均寿命仅为18个月。Magnesium electrolysis is an important method for preparing magnesium metal. The multi-pole magnesium electrolysis technology is used by more and more enterprises as a supporting process in the production of sponge titanium. Saving energy and reducing consumption, prolonging the service life of the tank, and improving the production capacity of a single tank have always been issues that enterprises need to solve urgently. The life cycle of electrolytic cell anodes is generally 24 months, but in actual production, the average life of graphite anodes is only 18 months.
石墨阳极在高温电解的作用下容易发生破损和断裂(断裂位置在熔盐液面附近),石墨阳极因破损而逐渐减薄或断裂时,电压会升高,温度升高,电流效率下降。由于同一电解槽中一组石墨阳极的材质和环境不完全相同,破损断裂的速度也不完全一样,一但其中1-2块阳极断裂或失去电解作用,就不得不停槽休整。The graphite anode is prone to breakage and fracture under the action of high-temperature electrolysis (the breaking position is near the molten salt level). When the graphite anode is gradually thinned or broken due to breakage, the voltage will rise, the temperature will rise, and the current efficiency will drop. Because the material and environment of a group of graphite anodes in the same electrolytic cell are not exactly the same, and the speed of breakage and fracture is not completely the same, once 1-2 of the anodes break or lose their electrolytic effect, the cell has to be stopped for rest.
发明内容SUMMARY OF THE INVENTION
为解决上述多极镁电解槽结构中阳极老化、破损及断裂的问题,本发明提供一种不停槽更换镁电解槽阳极的方法,其目的在于:延长电解槽的寿命和提高电流效率,有助于降低镁电解的生产成本。In order to solve the problems of aging, damage and fracture of the anode in the above-mentioned multi-pole magnesium electrolytic cell structure, the present invention provides a method for replacing the anode of the magnesium electrolytic cell without changing the cell. Helps reduce the production cost of magnesium electrolysis.
本发明采用的技术方案如下:The technical scheme adopted in the present invention is as follows:
步骤A:阳极更换前,对新阳极以及电解槽进行预处理;步骤B:断直流更换阳极;步骤C:阳极电压降检测。Step A: Before replacing the anode, pre-treat the new anode and the electrolytic cell; Step B: Switch off the direct current to replace the anode; Step C: Check the voltage drop of the anode.
进一步的,所述步骤A中具体包括:Further, the step A specifically includes:
1)提前三天以上,将阳极上的陶瓷棒粘接完成,陶瓷棒粘接完成后,将阳极进行烘烤;1) More than three days in advance, the ceramic rods on the anode are bonded, and after the ceramic rods are bonded, the anodes are baked;
2)提前4小时以上,在阳极铝母线和阴极铝母线处安装直流截断装置;2) Install DC cut-off devices at the anode aluminum busbar and cathode aluminum busbar more than 4 hours in advance;
3)对电解槽提前升温至690~720℃;3) Warm up the electrolytic cell to 690-720°C in advance;
4)通过抽取的方式降低电解槽中的液镁高度,抽取后的液镁高度为0-40mm。4) The height of the liquid magnesium in the electrolytic cell is reduced by means of extraction, and the height of the liquid magnesium after extraction is 0-40mm.
其中,所述解槽中的液镁的抽取过程中采用刮镁耙尽量将液镁刮到抽镁口,液镁抽取后不补充氯化镁。Wherein, in the process of extracting the liquid magnesium in the solution tank, a magnesium scraping rake is used to scrape the liquid magnesium to the magnesium extraction port as much as possible, and magnesium chloride is not supplemented after the liquid magnesium is extracted.
进一步的,所述步骤B具体包括:Further, the step B specifically includes:
1)通过直流电截断装置单独将通入需更换阳极的电解槽的直流电切断;1) Separately cut off the direct current to the electrolytic cell where the anode needs to be replaced by the direct current cut-off device;
2)将电解槽已损坏的阳极之间的软连接断开;2) Disconnect the soft connection between the damaged anodes of the electrolytic cell;
3)通过天车将电解槽上部断裂部分阳极从电解槽内吊出;3) Lift out the broken anode of the upper part of the electrolytic cell from the electrolytic cell through the overhead crane;
4)作业人员穿戴防护用具将阳极处电解室侧壁处的粘接物清除干净;4) The operator wears protective equipment to remove the adhesive on the side wall of the electrolysis chamber at the anode;
5)降低电解质液位,至阳极断裂面以下约200mm;5) Lower the electrolyte level to about 200mm below the anode fracture surface;
6)利用撬棍将浸泡在电解质内的2块断裂阳极分开,用钢筋套将靠近隔墙侧的断裂阳极套牢,利用天车将阳极吊出电解槽;6) Use a crowbar to separate the two broken anodes immersed in the electrolyte, fasten the broken anodes close to the partition wall with a steel sleeve, and use a crane to lift the anodes out of the electrolytic cell;
7)待断裂的一块阳极吊出电解槽后,作业人员利用抓渣扒和抓渣盒将已吊出阳极处阴极床上部的渣块清理干净;7) After the broken anode is lifted out of the electrolytic cell, the operator uses the slag scraper and the slag grab box to clean up the slag on the top of the cathode bed that has been lifted out of the anode;
8)将渣块清理干净后,用天车将干燥完成待安装的一块完整阳极吊装至已清理完成的阳极口处,缓慢的将阳极装进阳极安装处,阳极下降至电解室盖上露出1/3时利用阳极夹具将阳极固定在电解室盖上,拧固阳极夹具上的螺栓,防止阳极下滑;8) After cleaning the slag, use a crane to hoist a complete anode to be installed to the anode port that has been cleaned, slowly install the anode into the anode installation place, and drop the anode to the cover of the electrolysis chamber to expose 1 When /3, use the anode clamp to fix the anode on the electrolysis chamber cover, and tighten the bolts on the anode clamp to prevent the anode from sliding down;
9)重复权利要求6、7中所述的步骤将阳极断裂的另一块阳极吊出,并清理渣块;9) Repeat the steps described in claims 6 and 7 to lift out another anode of the broken anode, and clean up the slag;
10)将镀银铜箔、冷却水套、铁夹板和待安装的另一块完整阳极进行初步组对;10) Preliminarily pair the silver-plated copper foil, cooling water jacket, iron splint and another complete anode to be installed;
11)重复权利要求8中所述的步骤,将组对好的阳极吊装至已清理完成的阳极安装口处,缓慢下降,待2块阳极将下降高度位置重合时,将2块阳极合并,安装螺栓并紧固;11) Repeat the steps described in claim 8, hoist the assembled anodes to the anode installation port that has been cleaned up, and slowly descend, when the two anodes will overlap the descending height positions, merge the two anodes and install them. Bolt and tighten;
12)松开阳极夹具,将紧固完成的阳极安装至预定位置,检查安装尺寸,确认尺寸无误后密封阳极;12) Loosen the anode clamp, install the tightened anode to the predetermined position, check the installation size, and seal the anode after confirming that the size is correct;
13)利用阳极软连接将电解槽阳极和阳极铝母线连接,完成新阳极的更换。13) Use the anode soft connection to connect the anode of the electrolytic cell to the anode aluminum busbar to complete the replacement of the new anode.
综上所述,由于采用了上述技术方案,本发明的有益效果是:To sum up, due to the adoption of the above-mentioned technical solutions, the beneficial effects of the present invention are:
在电解槽阳极断裂后,与现有技术中采用的停槽休整方案不同,本技术方案通过在线更换阳极的方式,在不停槽休整的情况下,短时间内恢复阳极正常工作,阻止电解槽持续热槽,平衡了电解槽的电极电势,恢复了电解时电解质、镁、氯气的正常循环,解决了电解槽阳极断裂后电极电势平衡、热平衡、电解质、镁、氯气循环平衡破坏,电解槽电流效率不断降低,导致电解槽最终死槽的问题,此技术方案执行后能够将电解槽从濒临死槽的状态恢复正常运行状态,延长电解槽的使用寿命,提高电流效率,降低镁电解生产成本。After the anode of the electrolytic cell is broken, different from the solution of stopping the tank for reconditioning adopted in the prior art, this technical solution can restore the normal operation of the anode in a short period of time without the reconditioning of the electrolytic cell by replacing the anode on-line, preventing the electrolytic cell from resting. The continuous hot cell balances the electrode potential of the electrolytic cell, restores the normal circulation of electrolyte, magnesium and chlorine gas during electrolysis, and solves the problem of electrode potential balance, thermal balance, electrolyte, magnesium, and chlorine gas after the anode of the electrolytic cell is broken. Efficiency continues to decrease, leading to the problem of the final dead cell of the electrolytic cell. After the implementation of this technical solution, the electrolytic cell can be restored to the normal operating state from the state of the dying cell, prolong the service life of the electrolytic cell, improve the current efficiency, and reduce the production cost of magnesium electrolysis.
附图说明Description of drawings
图1是本发明提供的一种不停槽更换镁电解槽阳极的方法的流程图。FIG. 1 is a flow chart of a method for continuously replacing the anode of a magnesium electrolytic cell provided by the present invention.
图2是本发明实施例2中采用本方法后电解槽周累计电流效率柱状图。FIG. 2 is a histogram of cumulative current efficiency around the electrolytic cell after the method is adopted in Example 2 of the present invention.
具体实施方式Detailed ways
为使本申请实施例的目的、技术方案和优点更加清楚,下面将结合本申请实施例中附图,对本申请实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅是本申请一部分实施例,而不是全部的实施例。通常在此处附图中描述和示出的本申请实施例的组件可以各种不同的配置来布置和设计。因此,以下对在附图中提供的本申请的实施例的详细描述并非旨在限制要求保护的本申请的范围,而是仅仅表示本申请的选定实施例。基于本申请的实施例,本领域技术人员在没有做出创造性劳动的前提下所获得的所有其他实施例,都属于本申请保护的范围。In order to make the purposes, technical solutions and advantages of the embodiments of the present application more clear, the technical solutions in the embodiments of the present application will be described clearly and completely below with reference to the accompanying drawings in the embodiments of the present application. Obviously, the described embodiments are only It is a part of the embodiments of the present application, but not all of the embodiments. The components of the embodiments of the present application generally described and illustrated in the drawings herein may be arranged and designed in a variety of different configurations. Thus, the following detailed description of the embodiments of the application provided in the accompanying drawings is not intended to limit the scope of the application as claimed, but is merely representative of selected embodiments of the application. Based on the embodiments of the present application, all other embodiments obtained by those skilled in the art without creative work fall within the protection scope of the present application.
在本申请实施例的描述中,需要说明的是,术语“上”、“下”、“左”、“右”、“竖直”、“水平”、“内”、“外”等指示的方位或位置关系为基于附图所示的方位或位置关系,或者是该发明产品使用时惯常摆放的方位或位置关系,仅是为了便于描述本申请和简化描述,而不是指示或暗示所指的装置或元件必须具有特定的方位、以特定的方位构造和操作,因此不能理解为对本申请的限制。此外,术语“第一”、“第二”、“第三”等仅用于区分描述,而不能理解为指示或暗示相对重要性。In the description of the embodiments of the present application, it should be noted that the terms "upper", "lower", "left", "right", "vertical", "horizontal", "inner", "outer", etc. The orientation or positional relationship is based on the orientation or positional relationship shown in the accompanying drawings, or the orientation or positional relationship that the product of the invention is usually placed in use, only for the convenience of describing the application and simplifying the description, rather than indicating or implying that The device or element must have a specific orientation, be constructed and operate in a specific orientation, and therefore should not be construed as a limitation of the present application. Furthermore, the terms "first", "second", "third", etc. are only used to differentiate the description and should not be construed as indicating or implying relative importance.
本发明提供不停槽更换镁电解槽阳极的方法能够在镁电解槽阳极出现破损或断裂时可以不停槽休整就可以进性阳极更换的方法,以延长电解槽的寿命和提高电流效率,有助于降低镁电解的生产成本,具有较强的应有前景。The invention provides a method for replacing the anode of a magnesium electrolytic cell without a bath. When the anode of the magnesium electrolytic cell is damaged or broken, the anode can be replaced without a break in the cell, so as to prolong the life of the electrolytic cell and improve the current efficiency. It helps to reduce the production cost of magnesium electrolysis, and has strong due prospects.
下面结合附图1对本发明作详细说明。The present invention will be described in detail below in conjunction with FIG. 1 .
实施例一:Example 1:
一种不停槽更换镁电解槽阳极的方法,包括以下步骤:A method for continuously replacing the anode of a magnesium electrolytic cell, comprising the following steps:
步骤1:提前三天将阳极上的陶瓷棒粘接完成。Step 1: The ceramic rods on the anode were bonded three days in advance.
步骤2:陶瓷棒粘接完成后,进行烘烤阳极。Step 2: After the ceramic rod is bonded, bake the anode.
步骤3:阳极更换前,提前4小时在阳极铝母线和阴极铝母线处安装直流截断装置,安装完成后等待命令。Step 3: Before anode replacement, install DC cut-off devices at the anode aluminum busbar and cathode aluminum busbar 4 hours in advance, and wait for the command after the installation is complete.
步骤4:对电解槽提前4小时升温,电解槽温度达到690~720℃。Step 4: The temperature of the electrolytic cell is increased 4 hours in advance, and the temperature of the electrolytic cell reaches 690-720°C.
步骤5:通过抽取的方式除去电解槽中的液镁,抽取过程中采用刮镁耙尽量将液镁刮到抽镁口,液镁抽取后不补充氯化镁。Step 5: The liquid magnesium in the electrolytic cell is removed by extraction, and the magnesium scraping rake is used to scrape the liquid magnesium to the magnesium extraction port as much as possible during the extraction process, and magnesium chloride is not supplemented after the liquid magnesium is extracted.
步骤6:抽液镁作业完成后,将电解槽已损坏阳极周围的密封材料清除干净。Step 6: After the magnesium extraction operation is completed, remove the sealing material around the damaged anode of the electrolytic cell.
步骤7:利用直流电截断装置单独将通入需更换阳极的电解槽的直流电切断。Step 7: Use the direct current cut-off device to cut off the direct current flowing into the electrolytic cell where the anode needs to be replaced.
步骤8:电解槽已损坏阳极阳极与阳极软连接断开。Step 8: The electrolytic cell is damaged anode The anode is disconnected from the anode soft connection.
步骤9:通过天车将电解槽上部断裂部分阳极从电解槽内吊出。Step 9: Lift the broken anode of the upper part of the electrolytic cell out of the electrolytic cell through the overhead crane.
步骤10:作业人员穿戴防护用具将阳极处电解室侧壁处的粘接物清除干净,防护服特征在于,耐高温、绝缘。Step 10: The operator wears protective equipment to remove the adhesive on the side wall of the electrolysis chamber at the anode. The protective clothing is characterized by high temperature resistance and insulation.
步骤11:降低电解质液位,至阳极断裂面以下约200mm。Step 11: Lower the electrolyte level to about 200mm below the fracture surface of the anode.
步骤12:利用撬棍将浸泡在电解质内的2块断裂阳极分开,用钢筋套将靠近隔墙侧的断裂阳极套牢,利用天车将阳极吊出电解槽。Step 12: Use a crowbar to separate the two broken anodes immersed in the electrolyte, secure the broken anode near the partition wall with a steel sleeve, and use a crane to lift the anode out of the electrolytic cell.
步骤13:待断裂的1块阳极吊出电解槽后,作业人员利用抓渣扒和抓渣盒将已吊出阳极处阴极床上部的渣块清理干净。Step 13: After the broken anode is lifted out of the electrolytic cell, the operator uses the slag scraper and the slag box to clean up the slag on the upper part of the cathode bed at the anode.
步骤14:将渣块清理干净后,用天车将干燥完成待安装的1块完整阳极吊装至已清理完成的阳极口处,缓慢的将阳极装进阳极安装处(注意电解质喷溅),阳极下降至电解室盖上露出1/3时利用阳极夹具将阳极固定在电解室盖上,拧固阳极夹具上的螺栓,防止阳极下滑.Step 14: After cleaning the slag, use a crane to hoist a complete anode that has been dried and installed to the cleaned anode port, and slowly install the anode into the anode installation place (pay attention to electrolyte splashing), the anode When 1/3 is exposed on the electrolysis chamber cover, use the anode clamp to fix the anode on the electrolysis chamber cover, and tighten the bolts on the anode clamp to prevent the anode from sliding down.
步骤15:重复步骤11、12中所述的步骤将阳极断裂的另1块阳极吊出,并清理渣块。Step 15: Repeat the steps described in steps 11 and 12 to lift out the other broken anode, and clean the slag.
步骤16:将镀银铜箔、冷却水套、铁夹板和待安装的另1块完整阳极进行初步组对(阳极螺栓无需紧固)。Step 16: Preliminarily pair the silver-plated copper foil, cooling water jacket, iron splint and another complete anode to be installed (the anode bolts do not need to be tightened).
步骤17:重复步骤13中所述的步骤,将组对好的阳极吊装至已清理完成的阳极安装口处,缓慢下降(注意电解质喷溅),待2块阳极将下降高度位置重合时,利用撬棍等工具将2块阳极合并,安装螺栓并紧固。Step 17: Repeat the steps described in Step 13, hoist the assembled anode to the cleaned anode installation port, and slowly lower it (pay attention to electrolyte splashing). When the two anodes overlap the lowering height, use Use tools such as a crowbar to combine the 2 anodes, install the bolts and tighten.
步骤18:松开阳极夹具,将紧固完成的阳极安装至预定位置,检查安装尺寸,确认尺寸无误后密封阳极。Step 18: Loosen the anode clamp, install the tightened anode to the predetermined position, check the installation size, and seal the anode after confirming that the size is correct.
步骤19:利用阳极软连接将电解槽阳极和阳极铝母线连接。Step 19: Use the anode soft connection to connect the anode of the electrolytic cell to the anode aluminum busbar.
步骤20:检测阳极电压降。Step 20: Detect the anode voltage drop.
本实施例中:选用本公司的多极性镁电解槽,6组阳极中1组完好,其余5组各断裂一块阳极,严重热槽,温度保持690℃以上,电压11.2V,电流效率29.48%,采用本发明提供的电解槽阳极的方法,对电解槽的一组阳极更换后,热槽现象消失,温度保持660℃~670℃,电压10.2V,阳极更换技术方案完成后,持续运行8个月,累计电流效率达到50.01%。In this example: the company's multi-polar magnesium electrolytic cell is used, 1 of the 6 groups of anodes is intact, and one anode of each of the remaining 5 groups is broken, the tank is seriously hot, the temperature is kept above 690 ℃, the voltage is 11.2V, and the current efficiency is 29.48% , using the method of the electrolytic cell anode provided by the present invention, after replacing a group of anodes in the electrolytic cell, the hot cell phenomenon disappears, the temperature is maintained at 660 ℃ ~ 670 ℃, the voltage is 10.2V, and after the anode replacement technical scheme is completed, 8 continuous operation month, the cumulative current efficiency reached 50.01%.
实施例二:Embodiment 2:
步骤1:阳极更换前,提前4小时在阳极铝母线和阴极铝母线处安装直流截断装置,安装完成后等待命令。Step 1: Before anode replacement, install DC cut-off devices at the anode aluminum busbar and cathode aluminum busbar 4 hours in advance, and wait for the command after the installation is complete.
步骤2:对电解槽提前2小时升温,电解槽温度达到680℃。Step 2: The temperature of the electrolytic cell was increased 2 hours in advance, and the temperature of the electrolytic cell reached 680°C.
步骤3:通过抽取的方式除去电解槽中的液镁,抽取过程中采用刮镁耙尽量将液镁刮到抽镁口。Step 3: Remove the liquid magnesium in the electrolytic cell by extraction, and use a magnesium scraping rake to scrape the liquid magnesium to the magnesium extraction port as much as possible during the extraction process.
步骤4:液镁抽取后补充氯化镁提高液下罐压力,调整电解质液位,使之升高到电解槽“零点”以上50mm。Step 4: After the liquid magnesium is extracted, magnesium chloride is added to increase the pressure of the submerged tank, and the electrolyte level is adjusted so that it rises to 50mm above the "zero point" of the electrolytic cell.
步骤5:利用直流电截断装置单独将通入需更换阳极的电解槽的直流电切断。Step 5: Use the direct current cut-off device to cut off the direct current flowing into the electrolytic cell where the anode needs to be replaced.
步骤6:电解槽已损坏阳极阳极与阳极软连接断开,并将其拆除。Step 6: Damaged Anode Electrolyzer The anode is disconnected from the anode soft connection and removed.
步骤7:关闭直流电截断装置,恢复直流电,试运行生产。Step 7: Turn off the DC cut-off device, restore the DC power, and run the production trial.
步骤8:检测其余阳极的电压降及电流分布。Step 8: Detect the voltage drop and current distribution of the remaining anodes.
步骤9:电流槽电流效率依然持续下降时,再进行阳极更换。Step 9: When the current efficiency of the current cell continues to decrease, the anode is replaced.
步骤10:提前5天将阳极上的陶瓷棒粘接完成。Step 10: The ceramic rods on the anode were bonded 5 days in advance.
步骤11:陶瓷棒粘接完成后,放在精炼炉或电解槽上烘烤5天。Step 11: After the ceramic rods are bonded, they are baked on a refining furnace or electrolytic cell for 5 days.
步骤12:对电解槽提前4小时升温,电解槽温度达到690~720℃。Step 12: The temperature of the electrolytic cell is increased 4 hours in advance, and the temperature of the electrolytic cell reaches 690-720°C.
步骤13:通过抽取的方式除去电解槽中的液镁,抽取过程中采用刮镁耙尽量将液镁刮到抽镁口,液镁抽取后不补充氯化镁。Step 13: remove the liquid magnesium in the electrolytic cell by means of extraction, use a magnesium scraping rake to scrape the liquid magnesium to the magnesium extraction port as much as possible during the extraction process, and do not replenish magnesium chloride after the liquid magnesium is extracted.
步骤14:抽液镁作业完成后,将电解槽已损坏阳极周围的密封材料清除干净。Step 14: After the magnesium extraction operation is completed, remove the sealing material around the damaged anode of the electrolytic cell.
步骤15:利用直流电截断装置单独将通入需更换阳极的电解槽的直流电切断。Step 15: Use the direct current cut-off device to cut off the direct current flowing into the electrolytic cell where the anode needs to be replaced.
步骤16:通过天车将电解槽上部断裂部分阳极从电解槽内吊出。Step 16: Lift the broken anode of the upper part of the electrolytic cell out of the electrolytic cell through the overhead crane.
步骤17:作业人员穿戴防护用具将阳极处电解室侧壁处的粘接物清除干净,防护服特征在于,耐高温、绝缘。Step 17: The operator wears protective equipment to remove the adhesive on the side wall of the electrolysis chamber at the anode. The protective clothing is characterized by high temperature resistance and insulation.
步骤18:降低电解质液位,至阳极断裂面以下约200mm。Step 18: Lower the electrolyte level to about 200mm below the fracture surface of the anode.
步骤19:利用撬棍将浸泡在电解质内的2块断裂阳极分开,用钢筋套将靠近隔墙侧的断裂阳极套牢,利用天车将阳极吊出电解槽。Step 19: Use a crowbar to separate the two broken anodes immersed in the electrolyte, secure the broken anode near the partition wall with a steel sleeve, and use a crane to lift the anode out of the electrolytic cell.
步骤20:待断裂的1块阳极吊出电解槽后,作业人员利用抓渣扒和抓渣盒将已吊出阳极处阴极床上部的渣块清理干净。Step 20: After the broken anode is lifted out of the electrolytic cell, the operator uses the slag scraper and the slag grab box to clean up the slag on the upper part of the cathode bed where the anode has been lifted out.
步骤21:将渣块清理干净后,用天车将干燥完成待安装的1块完整阳极吊装至已清理完成的阳极口处,缓慢的将阳极装进阳极安装处(注意电解质喷溅),阳极下降至电解室盖上露出1/3时利用阳极夹具将阳极固定在电解室盖上,拧固阳极夹具上的螺栓,防止阳极下滑.Step 21: After cleaning the slag, use the crane to hoist a complete anode that has been dried and installed to the cleaned anode port, and slowly install the anode into the anode installation place (pay attention to electrolyte splashing), the anode When 1/3 is exposed on the electrolysis chamber cover, use the anode clamp to fix the anode on the electrolysis chamber cover, and tighten the bolts on the anode clamp to prevent the anode from sliding down.
步骤22:重复步骤11、12中所述的步骤将阳极断裂的另1块阳极吊出,并清理渣块。Step 22: Repeat the steps described in Steps 11 and 12 to lift out the other broken anode, and clean the slag.
步骤23:将镀银铜箔、冷却水套、铁夹板和待安装的另1块完整阳极进行初步组对(阳极螺栓无需紧固)。Step 23: Preliminarily pair the silver-plated copper foil, cooling water jacket, iron splint and another complete anode to be installed (the anode bolts do not need to be tightened).
步骤24:重复步骤13中所述的步骤,将组对好的阳极吊装至已清理完成的阳极安装口处,缓慢下降(注意电解质喷溅),待2块阳极将下降高度位置重合时,利用撬棍等工具将2块阳极合并,安装螺栓并紧固。Step 24: Repeat the steps described in Step 13, hoist the assembled anode to the anode installation port that has been cleaned, and lower it slowly (pay attention to the splash of electrolyte). Use tools such as a crowbar to combine the 2 anodes, install the bolts and tighten.
步骤25:松开阳极夹具,将紧固完成的阳极安装至预定位置,检查安装尺寸,确认尺寸无误后密封阳极。Step 25: Loosen the anode clamp, install the tightened anode to the predetermined position, check the installation size, and seal the anode after confirming that the size is correct.
步骤26:利用阳极软连接将电解槽阳极和阳极铝母线连接。Step 26: Use the anode soft connection to connect the anode of the electrolytic cell to the anode aluminum busbar.
步骤27:检测阳极电压降。Step 27: Detect the anode voltage drop.
步骤28:电解质置换。Step 28: Electrolyte replacement.
本实施例中:选用本公司的多极性镁电解槽,该台电解槽运行时间为15个月,6组阳极中4组完好,其余2组断裂,严重热槽,温度保持690℃以上,电压12.1V,电流效率45.45%,参照图2,采用本发明提供的电解槽阳极的方法,对电解槽的2组阳极更换后,热槽现象消失,温度保持660℃~670℃,电压10.9V,阳极更换技术方案完成后,持续运行5周,累计电流效率由45.45%提升至69.84%。In this example: the multi-polar magnesium electrolytic cell of our company is selected. The operating time of this electrolytic cell is 15 months, 4 groups of 6 groups of anodes are in good condition, and the remaining 2 groups are broken, and the temperature is kept above 690 ℃. The voltage is 12.1V, and the current efficiency is 45.45%. Referring to Figure 2, using the method of the electrolytic cell anode provided by the present invention, after the two groups of anodes of the electrolytic cell are replaced, the hot cell phenomenon disappears, the temperature is maintained at 660 ° C ~ 670 ° C, and the voltage is 10.9V , After the anode replacement technical scheme is completed, it continues to run for 5 weeks, and the cumulative current efficiency is increased from 45.45% to 69.84%.
以上所述实施例仅表达了本申请的具体实施方式,其描述较为具体和详细,但并不能因此而理解为对本申请保护范围的限制。应当指出的是,对于本领域的普通技术人员来说,在不脱离本申请技术方案构思的前提下,还可以做出若干变形和改进,这些都属于本申请的保护范围。The above-mentioned embodiments only represent specific implementations of the present application, and the descriptions thereof are relatively specific and detailed, but should not be construed as limiting the protection scope of the present application. It should be pointed out that for those of ordinary skill in the art, without departing from the concept of the technical solution of the present application, several modifications and improvements can be made, which all belong to the protection scope of the present application.
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