CN116375271A - A lithium battery waste liquid treatment mechanism - Google Patents

A lithium battery waste liquid treatment mechanism Download PDF

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CN116375271A
CN116375271A CN202310385712.9A CN202310385712A CN116375271A CN 116375271 A CN116375271 A CN 116375271A CN 202310385712 A CN202310385712 A CN 202310385712A CN 116375271 A CN116375271 A CN 116375271A
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waste liquid
lithium battery
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王嫦
赵群芳
张淑琼
蒋光辉
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Guizhou Light Industry Technical College
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Abstract

本发明公开了一种锂电池废液处理机构,包括呈封闭结构的处理罐,处理罐顶部侧壁上设置有中央处理系统;处理罐内设置有多块密封隔板,多块密封隔板沿处理罐的高度方向间隔设置,多块密封隔板用于将处理罐分割成多个反应区域,多个反应区域由上至下依次为废液收集区域、反应沉淀区域、微生物降解区域和底部过滤排泄区域;废液收集区域用于存放锂电池废液,反应沉淀区域用于对锂电池废液进行酸碱平衡、对锂电池废液中的重金属离子进行沉淀和对对锂电池废液中的不容物进行沉淀,微生物降解区域通过微生物对锂电池废液中的有机物进行生物降解处理,消除锂电池废液中的有机物,简化了锂电池废液处理工艺,保障了处理后锂电池废液达到国家废水排放标准。

Figure 202310385712

The invention discloses a treatment mechanism for lithium battery waste liquid, which comprises a treatment tank in a closed structure. A central processing system is arranged on the top side wall of the treatment tank; The height direction of the treatment tank is set at intervals, and multiple sealed partitions are used to divide the treatment tank into multiple reaction areas. The multiple reaction areas are waste liquid collection area, reaction precipitation area, microbial degradation area and bottom filtration from top to bottom. Excretion area; the waste liquid collection area is used to store lithium battery waste liquid, and the reaction precipitation area is used for acid-base balance of lithium battery waste liquid, precipitation of heavy metal ions in lithium battery waste liquid and treatment of lithium battery waste liquid In the microbial degradation area, the organic matter in the lithium battery waste liquid is biodegraded by microorganisms, eliminating the organic matter in the lithium battery waste liquid, simplifying the treatment process of the lithium battery waste liquid, and ensuring that the lithium battery waste liquid after treatment reaches National Wastewater Discharge Standards.

Figure 202310385712

Description

一种锂电池废液处理机构A lithium battery waste liquid treatment mechanism

技术领域technical field

本发明属于电池废液处理技术领域,具体涉及一种锂电池废液处理机构。The invention belongs to the technical field of battery waste liquid treatment, and in particular relates to a lithium battery waste liquid treatment mechanism.

背景技术Background technique

锂电池在我们日常生活中越来越普及,作为当今新能源汽车的重要组成部分,汽车市场对锂电池的需求猛增,导致很多电池超级工厂应运而生,锂电池是一种相对清洁的新能源,但锂电池生产过程中产生的生产废水是典型的高浓度有机废水。废水主要含有N-甲基吡咯烷酮、碳粉、有机脂类和重金属离子等。虽然相对水量较少,但废水成分复杂,生物降解性差,不可生物降解,有一定毒性。如果将未经彻底处理的锂电池生产废水直接排放到水环境中,将极大地影响水生态环境,威胁人类健康。Lithium batteries are becoming more and more popular in our daily life. As an important part of today's new energy vehicles, the demand for lithium batteries in the automotive market has soared, leading to the emergence of many battery super factories. Lithium batteries are a relatively clean new energy , but the production wastewater generated during the production of lithium batteries is a typical high-concentration organic wastewater. Wastewater mainly contains N-methylpyrrolidone, carbon powder, organic lipids and heavy metal ions. Although the amount of water is relatively small, the wastewater has complex components, poor biodegradability, non-biodegradable, and certain toxicity. If the lithium battery production wastewater that has not been thoroughly treated is directly discharged into the water environment, it will greatly affect the water ecological environment and threaten human health.

而现有技术中,处理锂电池废液通常设置有处理池,如现有技术中的发明专利CN112687972A-一种锂电池废液中钴处理回收系统及方法,通过设置有电解池和气浮池用于处理电池废液,但是电解池和气浮池的占用面积大,电解池和气浮池且在处理锂电池废液的过程中,会将产生废气,废气会进入大气环境,造成环境污染,同时一般电解池和气浮池是通过混凝土搭建,存在无法移动和搬运、使用不灵活和搭建周期长等缺点。In the prior art, a treatment pool is usually provided for the treatment of lithium battery waste liquid, such as the invention patent CN112687972A in the prior art-a cobalt treatment and recovery system and method in lithium battery waste liquid, which is used for Treatment of battery waste liquid, but the electrolytic cell and air flotation pool occupy a large area, and the electrolytic cell and air flotation pool will generate waste gas during the process of processing lithium battery waste liquid, and the waste gas will enter the atmosphere and cause environmental pollution. The floating pool is built by concrete, which has disadvantages such as inability to move and carry, inflexible use and long construction period.

发明内容Contents of the invention

本发明的目的在于针对现有技术中的上述不足,提供一种锂电池废液处理机构,解决了现有通过处理池处理锂电池废液,存在使用不灵活和会将废气排入大气环境,造成二次环境污染的技术问题。The purpose of the present invention is to address the above-mentioned deficiencies in the prior art, to provide a lithium battery waste liquid treatment mechanism, which solves the problem of inflexible use and discharge of waste gas into the atmosphere in the existing treatment of lithium battery waste liquid through a treatment pool. Technical problems that cause secondary environmental pollution.

为达到上述目的,本发明采取的技术方案是:For achieving the above object, the technical scheme that the present invention takes is:

本发明提供一种锂电池废液处理机构,其包括呈封闭结构的处理罐,所述处理罐顶部侧壁上设置有中央处理系统;The invention provides a lithium battery waste liquid treatment mechanism, which includes a treatment tank in a closed structure, and a central processing system is arranged on the top side wall of the treatment tank;

处理罐内设置有多块密封隔板,所述多块密封隔板沿处理罐的高度方向间隔设置,多块密封隔板用于将处理罐分割成多个反应区域,多个反应区域由上至下依次为废液收集区域、反应沉淀区域、微生物降解区域和底部过滤排泄区域;There are multiple sealing partitions arranged in the treatment tank, and the multiple sealing partitions are arranged at intervals along the height direction of the processing tank. The multiple sealing partitions are used to divide the processing tank into multiple reaction areas, and the multiple reaction areas are formed by From the bottom to the bottom are the waste liquid collection area, the reaction precipitation area, the microbial degradation area and the bottom filter discharge area;

废液收集区域和处理罐的顶部形成密封区域,处理罐顶部设置有曝气装置、废液料斗装置和废气排气装置;The waste liquid collection area and the top of the treatment tank form a sealed area, and the top of the treatment tank is provided with an aeration device, a waste liquid hopper device and an exhaust gas exhaust device;

废液收集区域通过带有第一电磁阀的管道与所述反应沉淀区域连通;The waste liquid collection area communicates with the reaction precipitation area through a pipeline with a first solenoid valve;

反应沉淀区域所在处理罐位置的侧壁上设有絮凝剂添加装置和沉淀物卸料装置;The side wall of the treatment tank where the reaction precipitation area is located is provided with a flocculant adding device and a sediment unloading device;

反应沉淀区域通过带有第二电磁阀的管道与所述微生物降解区域连通;带有第二电磁阀的管道管口处设置有过滤网;反应沉淀区域侧壁上设置有检修窗口;The reaction precipitation area communicates with the microbial degradation area through a pipeline with a second electromagnetic valve; a filter screen is provided at the nozzle of the pipeline with the second electromagnetic valve; an inspection window is provided on the side wall of the reaction precipitation area;

微生物降解区域所在处理罐位置的侧壁上设有光合细菌投放装置;A photosynthetic bacteria delivery device is provided on the side wall of the treatment tank where the microbial degradation area is located;

微生物降解区域通过带有第三电磁阀的管道与所述底部过滤排泄区域连通,底部过滤排泄区域底部设置有出水口,所述出水口通过管道与外部过滤装置连通;The microbial degradation area communicates with the bottom filter discharge area through a pipeline with a third solenoid valve, and a water outlet is provided at the bottom of the bottom filter discharge area, and the water outlet communicates with an external filter device through a pipeline;

所述曝气装置、废液料斗装置、第一电磁阀、沉淀物卸料装置、第二电磁阀、光合细菌投放装置和第三电磁阀均与所述中央处理系统电性连接。The aeration device, waste liquid hopper device, first solenoid valve, sediment discharge device, second solenoid valve, photosynthetic bacteria feeding device and third solenoid valve are all electrically connected to the central processing system.

进一步地,所述中央处理系统为PLC控制器。Further, the central processing system is a PLC controller.

进一步地,所述曝气装置包括与所述处理罐顶部固定连接的充气泵,所述充气泵上连接有充气管,所述充气管的底端穿过处理罐的顶部位于所述废液收集区域内的底部,充气管自由端端部连接有带有多个出气孔的曝气头;Further, the aeration device includes an air pump fixedly connected to the top of the treatment tank, the air pump is connected with an inflation tube, and the bottom end of the inflation tube passes through the top of the treatment tank and is located at the waste liquid collection At the bottom of the area, the free end of the inflatable tube is connected with an aeration head with multiple air outlets;

所述废液料斗装置包括呈上大下小斗状结构的进液斗,所述进液斗的底部穿过处理罐顶部与废液收集区域连通,进液斗的底部设置有用于控制进液通断且与所述中央处理系统电性连接的第四电磁阀;The waste liquid hopper device includes a liquid inlet hopper with an upper, lower, and lower bucket-shaped structure. The bottom of the liquid inlet hopper passes through the top of the treatment tank and communicates with the waste liquid collection area. A fourth solenoid valve that is switched on and off and electrically connected to the central processing system;

废气排气装置包括设置于处理罐顶部且与废液收集区域连通的排气管,所述排气管上连通有废气过滤模块,所述废气过滤模块包括与废气管连通的废气箱体,所述废气箱体内可拆卸连接有多块活性炭板。The waste gas exhaust device includes an exhaust pipe arranged on the top of the treatment tank and communicated with the waste liquid collection area. The exhaust pipe is connected with an exhaust gas filter module, and the exhaust gas filter module includes an exhaust gas box communicated with the waste gas pipe. There are multiple active carbon plates detachably connected in the exhaust gas box.

进一步地,所述废气箱体上开设有多个供所述活性炭板穿过的缺口,每个所述缺口内均设置有一块活性炭板,每块活性炭板的形状与废气箱体的横截面相匹配;每个缺口的四周侧壁上设置有一圈密封橡胶圈。Further, the exhaust gas box is provided with a plurality of gaps for the activated carbon plate to pass through, and an activated carbon plate is arranged in each of the gaps, and the shape of each activated carbon plate is the same as the cross section of the exhaust gas box. matching; a sealing rubber ring is arranged on the side walls around each notch.

进一步地,所述反应沉淀区域所在处理罐位置的侧壁上设有采样管,所述采样管上设置有与所述中央处理系统电性连接的第六电磁阀,采样管的末端设置有与中央处理系统电性连接的电pH计和废水成分检测装置;Further, a sampling pipe is provided on the side wall of the processing tank where the reaction precipitation area is located, and a sixth electromagnetic valve electrically connected to the central processing system is provided on the sampling pipe, and a valve connected to the central processing system is provided at the end of the sampling pipe. An electric pH meter and a wastewater component detection device electrically connected to the central processing system;

所述絮凝剂添加装置包括与处理罐外壁固定连接的安装架,所述安装架上设置有酸液添加箱、碱液添加箱和絮凝剂添加箱,酸液添加箱内填充有酸液,碱液添加箱内填充有碱液,絮凝剂添加箱内填充有重金属捕捉剂;The flocculant adding device includes a mounting frame fixedly connected to the outer wall of the treatment tank, and the mounting frame is provided with an acid liquid adding box, an alkali liquid adding box and a flocculant adding box, and the acid liquid adding box is filled with acid liquid, alkali The liquid addition box is filled with lye, and the flocculant addition box is filled with heavy metal scavenger;

每个添加箱内均设置有一个与中央控制器电性连接的水泵,所述水泵用于将各个添加箱内的液体泵入反应沉淀区域内。Each addition box is provided with a water pump electrically connected to the central controller, and the water pump is used to pump the liquid in each addition box into the reaction precipitation area.

进一步地,所述反应沉淀区域的侧壁上开设有一个沉淀物排泄口,所述沉淀物排泄口通过管道连接有压滤模块;沉淀物排泄口的下侧与反应沉淀区域底部的所述密封隔板上端面平齐;Further, a sediment discharge port is provided on the side wall of the reaction precipitation area, and the sediment discharge port is connected with a filter press module through a pipeline; the lower side of the sediment discharge port is sealed with the bottom of the reaction precipitation area. The upper surface of the partition is flush;

反应沉淀区域底部的密封隔板内设置有第一安装槽,所述第一安装槽的一侧贯穿所述处理罐;A first installation groove is arranged in the sealing partition at the bottom of the reaction precipitation area, and one side of the first installation groove runs through the treatment tank;

沉淀物卸料装置包括设置有位于反应沉淀区域底部密封隔板上端面的刮板件,刮板件一端的下端面设置有转动轴,所述转动轴一端与刮板件下端面固定连接,另一端穿过反应沉淀区域底部密封隔板位于所述第一安装槽,转动轴与反应沉淀区域底部密封隔板之间设置有密封环;The sediment unloading device includes a scraper piece located on the upper surface of the sealed partition at the bottom of the reaction precipitation area. The lower end surface of one end of the scraper piece is provided with a rotating shaft, and one end of the rotating shaft is fixedly connected to the lower end surface of the scraper piece. One end passes through the bottom sealing partition of the reaction precipitation area and is located in the first installation groove, and a sealing ring is arranged between the rotating shaft and the bottom sealing partition of the reaction precipitation area;

位于第一安装槽内转动轴的端部设置有第一伞状从动齿轮;所述处理罐的外壁上设置有与所述中央控制器电性连接的第一电机,所述第一电机的输出端上水平设置有一根位于第一安装槽内的第一传动杆,所述第一传动杆上设置有一个与所述第一伞状从动齿轮啮合的第一伞状主动齿轮。The end of the rotating shaft located in the first installation groove is provided with a first umbrella-shaped driven gear; the outer wall of the processing tank is provided with a first motor electrically connected to the central controller, and the first motor A first transmission rod located in the first installation groove is horizontally arranged on the output end, and a first umbrella-shaped driving gear meshed with the first umbrella-shaped driven gear is arranged on the first transmission rod.

进一步地,所述处理罐为中空圆柱结构,所述刮板件包括第一刮板杆,所述第一刮板杆呈中空柱状结构,第一刮板杆的横截面呈底部具有开口的“门”字形结构;Further, the treatment tank is a hollow cylindrical structure, the scraper member includes a first scraper rod, the first scraper rod is a hollow columnar structure, and the cross section of the first scraper rod has an open bottom. "door" structure;

第一刮板杆的内部设置有第二刮板杆,所述第二刮板杆通过限位槽和限位块配合的方式与第一刮板件的内壁滑动连接,所述限位槽和限位块的长度方向与第一刮板件的长度方向同向,第二刮板杆的尾端与第一刮板杆之间设置有推力弹簧,第二刮板杆的自由端上滚动设置有滚珠;The inside of the first scraper rod is provided with a second scraper rod, and the second scraper rod is slidably connected with the inner wall of the first scraper member through the cooperation of the limiting groove and the limiting block, and the limiting groove and the The length direction of the limit block is in the same direction as the length direction of the first scraper member, a thrust spring is arranged between the tail end of the second scraper rod and the first scraper rod, and the free end of the second scraper rod is rolled There are balls;

第一刮板杆和第二刮板杆的下端面均与所述反应沉淀区域底部的所述密封隔板上端面接触;The lower end faces of the first scraper rod and the second scraper rod are in contact with the upper end face of the sealing partition at the bottom of the reaction precipitation area;

所述转动轴与第一刮板杆的一端固定连接,转动轴位于反应沉淀区域底部密封隔板的边缘处。The rotating shaft is fixedly connected with one end of the first scraper rod, and the rotating shaft is located at the edge of the sealing partition at the bottom of the reaction precipitation area.

进一步地,所述沉淀物排泄口的竖直投影呈圆弧结构,沉淀物排泄口对应的圆弧直径与所述密封隔板的直径相同,沉淀物排泄口的一侧与所述第一刮板杆的一端所在位置相接;Further, the vertical projection of the sediment discharge port is in a circular arc structure, the diameter of the arc corresponding to the sediment discharge port is the same as the diameter of the sealing partition, and one side of the sediment discharge port is connected to the first scraper. The position of one end of the plate rod is connected;

第一刮板杆的两侧壁上均设置有一个呈圆弧结构的推块,所述推块外侧的弧长大于沉淀物排泄口的弧长,推块外侧的圆弧线对应的圆弧直径与所述密封隔板的直径相同。Both side walls of the first scraper rod are provided with a push block in a circular arc structure, the arc length on the outside of the push block is greater than the arc length of the sediment discharge port, and the arc line corresponding to the outside of the push block The diameter is the same as that of the sealing partition.

进一步地,所述压滤模块包括设置于所述处理罐外部的过滤箱,所述过滤箱位于所述沉淀物排泄口的下方,过滤箱内设置可拆卸连接有过滤板,过滤箱的顶部设置有与沉淀物排泄口连通的管道,沉淀物排泄口处设置有与中央处理系统电性连接的第五电磁阀;所述第五电磁阀为常闭状态;过滤箱的底部设置有与所述微生物降解区域连通的排水管;过滤箱通过支撑架与处理罐的侧部固定连接。Further, the filter press module includes a filter box arranged outside the treatment tank, the filter box is located below the sediment discharge port, a filter plate is detachably connected to the filter box, and the top of the filter box is set There is a pipeline communicating with the sediment discharge port, and the fifth solenoid valve electrically connected to the central processing system is arranged at the sediment discharge port; the fifth solenoid valve is in a normally closed state; the bottom of the filter box is provided with a The drain pipe connected to the microbial degradation area; the filter box is fixedly connected to the side of the treatment tank through a support frame.

进一步地,所述光合细菌投放装置包括与所述微生物降解区域连通的光合细菌液添加箱;Further, the photosynthetic bacteria delivery device includes a photosynthetic bacteria liquid addition box communicated with the microbial degradation area;

微生物降解区域内竖直设置有多根光源灯柱,多根光源灯柱以所述处理罐的轴线为中心环向间隔均匀设置,每根光源灯柱的两端分别与微生物降解区域顶部和底部的所述密封隔板密封连接;A plurality of light source lamp posts are vertically arranged in the microbial degradation area, and the plurality of light source lamp posts are evenly arranged around the axis of the treatment tank in a circumferential direction, and the two ends of each light source lamp post are respectively connected to the top and bottom of the microbial degradation area The sealing partition of the sealing connection;

微生物降解区域还设置有灯柱刮壁装置;The microbial degradation area is also equipped with lamp post wall scraping device;

微生物降解区域底部的密封隔板内设置有第二安装槽,所述第二安装槽的一侧水平贯穿微生物降解区域底部的密封隔板;处理罐外壁上设置有与所述中央处理系统电性连接的第二电机,所述第二电机输出端上设置有一根位于第二安装槽内的第二传动杆,所述第二传动杆上设置有一个第二伞状主动齿轮;A second installation groove is arranged in the sealing partition at the bottom of the microbial degradation area, and one side of the second installation groove horizontally runs through the sealing partition at the bottom of the microbial degradation area; The connected second motor, the output end of the second motor is provided with a second transmission rod located in the second installation groove, and the second transmission rod is provided with a second umbrella-shaped driving gear;

灯柱刮壁装置包括设置于微生物降解区域中心位置的螺纹杆,所述螺纹杆上螺纹连接有一个支撑板,所述支撑板上设置有数量与多根光源灯柱数量相同的安装孔,每个所述安装孔内均设置有圆环刮板,每个所述圆环刮板均与光源灯柱的圆周外壁接触;The lamp post wall scraping device includes a threaded rod arranged at the center of the microbial degradation area. A support plate is threaded on the threaded rod. The support plate is provided with the same number of mounting holes as the number of multiple light source lamp posts. Each of the mounting holes is provided with a ring scraper, and each of the ring scrapers is in contact with the peripheral outer wall of the light source lamp post;

螺纹杆的顶端与微生物降解区域顶部的密封隔板转动连接,螺纹杆的底端穿过微生物降解区域底部的密封隔板位于所述第二安装槽内,螺纹杆的底端上设置有与所述第二伞状主动齿轮啮合的第二伞状从动齿轮。The top of the threaded rod is rotatably connected to the sealing partition at the top of the microbial degradation area, and the bottom end of the threaded rod passes through the sealing partition at the bottom of the microbial degradation area and is located in the second installation groove. The second bevel driven gear meshed with the second bevel drive gear.

本发明的有益效果为:1、本发明通过多块密封隔板将处理罐分为多个反应区域,具体地,废液收集区域用于存放锂电池废液,反应沉淀区域用于对锂电池废液进行酸碱平衡、对锂电池废液中的重金属离子进行沉淀和对锂电池废液中的不容物进行沉淀,微生物降解区域通过微生物对锂电池废液中的有机物进行生物降解处理,消除锂电池废液中的有机物,使得锂电池废液达到排放标准;本发明中的锂电池废液处理机构,将存放、酸碱平衡、沉淀重金属离子和不容物以及降解有机物的功能集中在一起,且在对锂电池废液进行处理的过程中,产生的有害气体被废气排气装置中的活性炭板捕捉,不会将有害气体泄出,不会产生二次污染。The beneficial effects of the present invention are as follows: 1. The present invention divides the treatment tank into a plurality of reaction areas through a plurality of sealing partitions, specifically, the waste liquid collection area is used to store lithium battery waste liquid, and the reaction precipitation area is used to treat lithium battery The acid-base balance of the waste liquid, the precipitation of heavy metal ions in the lithium battery waste liquid and the precipitation of the incompatible substances in the lithium battery waste liquid, the microbial degradation area uses microorganisms to biodegrade the organic matter in the lithium battery waste liquid to eliminate The organic matter in the lithium battery waste liquid makes the lithium battery waste liquid meet the discharge standard; the lithium battery waste liquid treatment mechanism in the present invention integrates the functions of storage, acid-base balance, precipitation of heavy metal ions and incompatible substances, and degradation of organic matter. Moreover, during the process of treating the lithium battery waste liquid, the harmful gas generated is captured by the activated carbon plate in the exhaust gas exhaust device, so that the harmful gas will not be released and secondary pollution will not occur.

2、本发明通过将废液收集区域、反应沉淀区域、微生物降解区域和底部过滤排泄区域集成在处理罐中,整个锂电池废液处理机构的搬运更为方便快捷,相较于通过处理池的方式处理锂电池废液,本方面可将锂电池废液处理机构直接设置于生产车间,减少了锂电池废液的转运,使用灵活,更适用于锂电池生产车间。2. The present invention integrates the waste liquid collection area, the reaction precipitation area, the microbial degradation area and the bottom filtration and discharge area in the treatment tank, so that the handling of the entire lithium battery waste liquid treatment mechanism is more convenient and quick, compared with the process of passing through the treatment tank In this aspect, the lithium battery waste liquid treatment mechanism can be directly installed in the production workshop, which reduces the transfer of lithium battery waste liquid, is flexible in use, and is more suitable for lithium battery production workshops.

3、本发明通过光合细菌投放装置将光合细菌液泵入微生物降解区域内,光源灯柱为光合细菌提供光源,光合细菌在光源灯柱的作用下进行不放氧光合作用,对锂电池废液中的有机物、硫化物、氨等进行微生物降解作用,达到锂电池废液处理的目的。3. The present invention pumps the photosynthetic bacteria solution into the microbial degradation area through the photosynthetic bacteria delivery device, and the light source lamp post provides light source for the photosynthetic bacteria, and the photosynthetic bacteria perform oxygen-free photosynthesis under the action of the light source lamp post, and the lithium battery waste liquid The organic matter, sulfide, ammonia, etc. in the battery are degraded by microorganisms to achieve the purpose of lithium battery waste liquid treatment.

4、本发明通过在反应沉淀区域设置有沉淀物卸料装置,实现对反应沉淀区域内沉淀的重金属离子絮状沉淀物和不溶于水的杂质进行刮除至沉淀物排泄口,压滤模块用于对重金属离子絮状沉淀物和不溶于水的杂质进行二次过滤,过滤后在过滤板上形成滤渣饼便于将有害物质进行固化,而过滤后的锂电池废液继续通过排水管进入微生物降解区域内,进行微生物降解反应。4. The present invention is provided with a sediment unloading device in the reaction precipitation area to realize the scraping of the heavy metal ion flocculent precipitate and water-insoluble impurities deposited in the reaction precipitation area to the sediment discharge port, and the filter press module is used It is used for secondary filtration of heavy metal ion flocculent precipitates and water-insoluble impurities. After filtration, a filter residue cake is formed on the filter plate to facilitate solidification of harmful substances, and the filtered lithium battery waste continues to enter the microbial degradation through the drain pipe. In the area, the microbial degradation reaction is carried out.

附图说明Description of drawings

为了更清楚地说明本发明实施例或现有技术中的技术方案,下面将对实施例或现有技术描述中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图仅仅是本发明的一些实施例,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据这些附图获得其他的附图In order to more clearly illustrate the technical solutions in the embodiments of the present invention or the prior art, the following will briefly introduce the drawings that need to be used in the description of the embodiments or the prior art. Obviously, the accompanying drawings in the following description are only These are some embodiments of the present invention. For those skilled in the art, other drawings can also be obtained based on these drawings without creative work.

图1为本发明中一种锂电池废液处理机构的结构示意图。Fig. 1 is a structural schematic diagram of a lithium battery waste liquid treatment mechanism in the present invention.

图2为曝气装置的放大结构示意图。Figure 2 is a schematic diagram of the enlarged structure of the aeration device.

图3为废液料斗装置的放大结构示意图。Fig. 3 is an enlarged structural schematic diagram of the waste liquid hopper device.

图4为废气排气装置的放大结构示意图。Fig. 4 is an enlarged structural schematic diagram of the exhaust gas exhaust device.

图5为絮凝剂添加装置安装在处理罐上的俯视结构示意图。Fig. 5 is a top view structural diagram of the flocculant adding device installed on the treatment tank.

图6为沉淀物卸料装置的安装结构示意图。Fig. 6 is a schematic diagram of the installation structure of the sediment unloading device.

图7为压滤模块的安装结构示意图。Fig. 7 is a schematic diagram of the installation structure of the filter press module.

图8为灯柱刮壁装置的安装结构示意图。Fig. 8 is a schematic diagram of the installation structure of the lamppost wall scraping device.

图9为刮板件设置在反应沉淀区域内的俯视结构示意图。Fig. 9 is a top view structural diagram of a scraper member disposed in the reaction precipitation area.

图10为刮板件的内部剖视结构示意图。Fig. 10 is a schematic diagram of the internal sectional structure of the scraper member.

图11为支撑板的俯视结构示意图。FIG. 11 is a schematic top view of the support plate.

其中,附图标记为:1、处理罐;2、中央处理系统;3、密封隔板;4、废液收集区域;5、反应沉淀区域;6、微生物降解区域;7、底部过滤排泄区域;8、曝气装置;81、充气泵;82、充气管;83、曝气头;9、废液料斗装置;91、进液斗;92、第四电磁阀;10、废气排气装置;101、排气管;102、废气箱体;103、活性炭板;104、缺口;105、密封橡胶圈;11、第一电磁阀;12、絮凝剂添加装置;121、安装架;122、酸液添加箱;123、碱液添加箱;124、絮凝剂添加箱;13、沉淀物卸料装置;131、刮板件;1311、第一刮板杆;1312、第二刮板杆;1313、推力弹簧;1314、滚珠;1315、推块;132、转动轴;133、第一伞状从动齿轮;134、第一电机;135、第一传动杆;136、第一伞状主动齿轮;14、第二电磁阀;15、过滤网;16、检修窗口;17、光合细菌投放装置;171、光合细菌液添加箱;18、第三电磁阀;19、出水口;20、外部过滤装置连通;21、采样管;22、第六电磁阀;23、电pH计;24、废水成分检测装置;25、沉淀物排泄口;26、压滤模块;261、过滤箱;262、过滤板;263、第五电磁阀;264、排水管;265、支撑架;27、第一安装槽;28、光源灯柱;29、灯柱刮壁装置;291、第二电机;292、第二传动杆;293、第二伞状主动齿轮;294、螺纹杆;295、支撑板;296、安装孔;297、圆环刮板;298、第二伞状从动齿轮;30、第二安装槽。Wherein, the reference signs are: 1. treatment tank; 2. central processing system; 3. sealing partition; 4. waste liquid collection area; 5. reaction precipitation area; 6. microbial degradation area; 7. bottom filter discharge area; 8. Aeration device; 81. Inflatable pump; 82. Inflatable pipe; 83. Aeration head; 9. Waste liquid hopper device; 91. Liquid inlet hopper; 92. Fourth solenoid valve; 10. Exhaust gas exhaust device; 101 , exhaust pipe; 102, exhaust gas box; 103, activated carbon plate; 104, gap; 105, sealing rubber ring; 11, first solenoid valve; 12, flocculant adding device; 121, installation frame; 122, acid solution adding Box; 123, lye adding box; 124, flocculant adding box; 13, sediment unloading device; 131, scraper piece; 1311, first scraper bar; 1312, second scraper bar; 1313, thrust spring ; 1314, ball; 1315, push block; 132, rotating shaft; 133, the first umbrella driven gear; 134, the first motor; 135, the first transmission rod; 136, the first umbrella driving gear; Two electromagnetic valves; 15, filter screen; 16, maintenance window; 17, photosynthetic bacteria feeding device; 171, photosynthetic bacteria liquid addition box; 18, the third electromagnetic valve; 19, water outlet; Sampling pipe; 22, sixth solenoid valve; 23, electric pH meter; 24, wastewater component detection device; 25, sediment discharge port; 26, filter press module; 261, filter box; 262, filter plate; 263, fifth Solenoid valve; 264, drain pipe; 265, support frame; 27, first installation groove; 28, light source lamp post; 29, lamp post wall scraping device; 291, second motor; 292, second transmission rod; 293, the first Two umbrella-shaped driving gears; 294, threaded rod; 295, support plate; 296, mounting hole; 297, ring scraper; 298, the second umbrella-shaped driven gear; 30, the second installation groove.

具体实施方式Detailed ways

下面对本发明的具体实施方式进行描述,以便于本技术领域的技术人员理解本发明,但应该清楚,本发明不限于具体实施方式的范围,对本技术领域的普通技术人员来讲,只要各种变化在所附的权利要求限定和确定的本发明的精神和范围内,这些变化是显而易见的,一切利用本发明构思的发明创造均在保护之列。The specific embodiments of the present invention are described below so that those skilled in the art can understand the present invention, but it should be clear that the present invention is not limited to the scope of the specific embodiments. For those of ordinary skill in the art, as long as various changes Within the spirit and scope of the present invention defined and determined by the appended claims, these changes are obvious, and all inventions and creations using the concept of the present invention are included in the protection list.

如图1~图11所示,本发明提供一种锂电池废液处理机构,其包括呈封闭结构的处理罐1,处理罐1顶部侧壁上设置有中央处理系统2;优选但不局限地,中央处理系统2为PLC控制器。As shown in Figures 1 to 11, the present invention provides a lithium battery waste liquid treatment mechanism, which includes a treatment tank 1 in a closed structure, and a central processing system 2 is arranged on the top side wall of the treatment tank 1; preferably but not limited , the central processing system 2 is a PLC controller.

处理罐1内设置有多块密封隔板3,多块密封隔板3沿处理罐1的高度方向间隔设置,多块密封隔板3用于将处理罐1分割成多个反应区域,多个反应区域由上至下依次为废液收集区域4、反应沉淀区域5、微生物降解区域6和底部过滤排泄区域7。Multiple sealing partitions 3 are arranged in the processing tank 1, and the multiple sealing partitions 3 are arranged at intervals along the height direction of the processing tank 1. The multiple sealing partitions 3 are used to divide the processing tank 1 into multiple reaction areas. From top to bottom, the reaction area is the waste liquid collection area 4 , the reaction precipitation area 5 , the microbial degradation area 6 and the bottom filter discharge area 7 .

废液收集区域4和处理罐1的顶部形成密封区域,处理罐1顶部设置有曝气装置8、废液料斗装置9和废气排气装置10;具体地,废液收集区域4用于存放锂电池废液,并通过曝气装置8向废液收集区域4内的锂电池废液进行充氧。The waste liquid collection area 4 and the top of the treatment tank 1 form a sealed area, and the top of the treatment tank 1 is provided with an aeration device 8, a waste liquid hopper device 9 and an exhaust gas exhaust device 10; specifically, the waste liquid collection area 4 is used to store lithium battery waste liquid, and oxygenate the lithium battery waste liquid in the waste liquid collection area 4 through the aeration device 8 .

在本实施例中,如图1和图2所示,曝气装置8包括与处理罐1顶部固定连接的充气泵81,充气泵81上连接有充气管82,充气管82的底端穿过处理罐1的顶部位于废液收集区域4内的底部,充气管82自由端端部连接有带有多个出气孔的曝气头83,通过中央处理系统2启动充气泵81,充气泵81通过充气管82和曝气头83向锂电池废液充氧,提高锂电池废液的含氧量,为后续微生物降解处理做好准备,同时向锂电池废液充氧,可以使锂电池废液中的不溶于水的杂质不易沉淀堵塞带有第一电磁阀11的管道;而且通过向废液收集区域4充氧,可以使得废液收集区域4内的有害气体泄出至废气排气装置10,废气排气装置10用于收集泄出的有害气体,避免有害气体进入大气环境而造成二次污染。In this embodiment, as shown in Figures 1 and 2, the aeration device 8 includes an air pump 81 fixedly connected to the top of the treatment tank 1, the air pump 81 is connected with an inflation tube 82, and the bottom end of the inflation tube 82 passes through The top of the treatment tank 1 is located at the bottom of the waste liquid collection area 4, and the free end of the inflation pipe 82 is connected with an aeration head 83 with a plurality of air outlets, and the air pump 81 is started by the central processing system 2, and the air pump 81 passes through The inflatable tube 82 and the aeration head 83 oxygenate the lithium battery waste liquid, increase the oxygen content of the lithium battery waste liquid, and prepare for the subsequent microbial degradation treatment. At the same time, oxygenate the lithium battery waste liquid to make the lithium battery waste liquid The water-insoluble impurities in the water are not easy to precipitate and block the pipeline with the first electromagnetic valve 11; and by charging the waste liquid collection area 4 with oxygen, the harmful gas in the waste liquid collection area 4 can be released to the exhaust gas exhaust device 10 , The exhaust gas exhaust device 10 is used to collect the leaked harmful gas, so as to prevent the harmful gas from entering the atmosphere and causing secondary pollution.

具体地,如图4所示,废气排气装置10包括设置于处理罐1顶部且与废液收集区域4连通的排气管101,排气管101上连通有废气过滤模块,废气过滤模块包括与废气管连通的废气箱体102,废气箱体102内可拆卸连接有多块活性炭板103;活性炭板103用于收集泄出的有害气体。Specifically, as shown in FIG. 4 , the waste gas exhaust device 10 includes an exhaust pipe 101 arranged on the top of the treatment tank 1 and communicating with the waste liquid collection area 4. The exhaust pipe 101 is communicated with a waste gas filter module, and the waste gas filter module includes The exhaust gas box 102 connected with the exhaust gas pipe has a plurality of activated carbon plates 103 detachably connected in the exhaust gas box 102; the activated carbon plates 103 are used to collect the leaked harmful gas.

具体地,废气箱体102上开设有多个供活性炭板103穿过的缺口104,每个缺口104内均设置有一块活性炭板103,每块活性炭板103的形状与废气箱体102的横截面相匹配;当活性炭板103达到使用寿命后,可以通过缺口104更换装配新的活性炭板103;每个缺口104的四周侧壁上设置有一圈密封橡胶圈105,密封橡胶圈105用于封堵活性炭板103顶部与缺口104之间的间隙,避免出现有害气体通过间隙进入到大气环境而造成二次污染的情况。Specifically, the exhaust gas box 102 is provided with a plurality of gaps 104 through which the activated carbon plates 103 pass, and each gap 104 is provided with an activated carbon plate 103, and the shape of each activated carbon plate 103 is consistent with the cross-section of the exhaust gas box 102. match; when the activated carbon plate 103 reaches the service life, a new activated carbon plate 103 can be replaced and assembled through the gap 104; a ring of sealing rubber ring 105 is arranged on the side wall around each gap 104, and the sealing rubber ring 105 is used to block the activated carbon The gap between the top of the plate 103 and the notch 104 prevents harmful gas from entering the atmosphere through the gap and causing secondary pollution.

如图3所示,废液料斗装置9的设置,便于锂电池废液通过废液料斗装置9进入到废液收集区域4内。具体地,废液料斗装置9包括呈上大下小斗状结构的进液斗91,进液斗91的底部穿过处理罐1顶部与废液收集区域4连通,进液斗91的底部设置有用于控制进液通断且与中央处理系统2电性连接的第四电磁阀92。As shown in FIG. 3 , the arrangement of the waste liquid hopper device 9 facilitates the lithium battery waste liquid to enter the waste liquid collection area 4 through the waste liquid hopper device 9 . Specifically, the waste liquid hopper device 9 includes a liquid inlet hopper 91 in the shape of an upper, lower, and lower bucket. The bottom of the liquid inlet hopper 91 passes through the top of the treatment tank 1 and communicates with the waste liquid collection area 4. The bottom of the liquid inlet hopper 91 is set There is a fourth electromagnetic valve 92 for controlling the on-off of liquid inlet and electrically connected with the central processing system 2 .

废液收集区域4通过带有第一电磁阀11的管道与反应沉淀区域5连通;The waste liquid collection area 4 communicates with the reaction precipitation area 5 through a pipeline with a first solenoid valve 11;

反应沉淀区域5所在处理罐1位置的侧壁上设有絮凝剂添加装置12和沉淀物卸料装置13;A flocculant addition device 12 and a sediment discharge device 13 are provided on the side wall of the treatment tank 1 where the reaction precipitation area 5 is located;

反应沉淀区域5通过带有第二电磁阀14的管道与微生物降解区域6连通;带有第二电磁阀14的管道管口处设置有过滤网15;反应沉淀区域5侧壁上设置有检修窗口16;检修窗口16的设置,便于检修人员的手臂进入,当过滤网15出现堵塞时,便于拿出过滤网15进行手动清理。The reaction precipitation area 5 communicates with the microbial degradation area 6 through a pipeline with a second electromagnetic valve 14; a filter screen 15 is provided at the nozzle of the pipeline with the second electromagnetic valve 14; an inspection window is provided on the side wall of the reaction precipitation area 5 16. The setting of the inspection window 16 is convenient for the arm of the maintenance personnel to enter, and when the filter screen 15 is blocked, it is convenient to take out the filter screen 15 for manual cleaning.

微生物降解区域6所在处理罐1位置的侧壁上设有光合细菌投放装置17;The side wall of the treatment tank 1 where the microbial degradation area 6 is located is provided with a photosynthetic bacteria delivery device 17;

微生物降解区域6通过带有第三电磁阀18的管道与底部过滤排泄区域7连通,底部过滤排泄区域7底部设置有出水口19,出水口19通过管道与外部过滤装置连通20;The microbial degradation area 6 communicates with the bottom filter drainage area 7 through a pipeline with a third electromagnetic valve 18, and the bottom of the bottom filter drainage area 7 is provided with a water outlet 19, and the water outlet 19 communicates with an external filter device 20 through a pipeline;

曝气装置8、废液料斗装置9、第一电磁阀11、沉淀物卸料装置13、第二电磁阀14、光合细菌投放装置17和第三电磁阀18均与中央处理系统2电性连接。The aeration device 8, the waste liquid hopper device 9, the first solenoid valve 11, the sediment discharge device 13, the second solenoid valve 14, the photosynthetic bacteria feeding device 17 and the third solenoid valve 18 are all electrically connected to the central processing system 2 .

具体地,本发明中的锂电池废液处理机构的工作流程为:生产线上的锂电池废液可以通过管道直接与进液斗91连通,当需要处理废液收集区域4内的锂电池废液时,需要通过中央处理系统2关闭第四电磁阀92,锂电池废液暂时存放至进液斗91内,避免后续的锂电池废液的进入,当处理废液收集区域4内的锂电池废液达到预设处理时间后,通过中央处理系统2打开第一电磁阀11,将废液收集区域4内的锂电池废液排入反应沉淀区域5内,然后关闭第一电磁阀11,打开第四电磁阀92,将进液斗91的锂电池废液继续排放至废液收集区域4内,实现废液收集区域4的连续处理。Specifically, the working process of the lithium battery waste liquid treatment mechanism in the present invention is as follows: the lithium battery waste liquid on the production line can be directly connected to the liquid inlet bucket 91 through a pipeline, and when it is necessary to process the lithium battery waste liquid in the waste liquid collection area 4 At this time, it is necessary to close the fourth electromagnetic valve 92 through the central processing system 2, and the lithium battery waste liquid is temporarily stored in the liquid inlet hopper 91 to avoid the subsequent entry of lithium battery waste liquid. When the lithium battery waste liquid in the waste liquid collection area 4 is processed After the liquid reaches the preset processing time, the first electromagnetic valve 11 is opened through the central processing system 2, and the lithium battery waste liquid in the waste liquid collection area 4 is discharged into the reaction precipitation area 5, and then the first electromagnetic valve 11 is closed, and the second electromagnetic valve is opened. Four electromagnetic valves 92 continue to discharge the lithium battery waste liquid in the liquid inlet hopper 91 into the waste liquid collection area 4 to realize continuous treatment in the waste liquid collection area 4 .

如图1和图5所示,通过絮凝剂添加装置12用于向反应沉淀区域5泵入酸液或碱液,用于调节反应沉淀区域5中锂电池废液的酸碱性,使得反应沉淀区域5中锂电池废液的pH值在6~7,适合于后续微生物的降解处理;通过絮凝剂添加装置12向反应沉淀区域5泵入重金属捕捉剂,重金属捕捉剂与锂电池废液中的重金属离子结合,形成絮状沉淀物,重金属捕捉剂的反应时间为2~3min,然后中央控制系统打开第二电磁阀14,将反应沉淀区域5中锂电池废液流入微生物降解区域6内,由于过滤网15的设置,使得重金属离子絮状沉淀物和不溶于水的杂质沉淀在反应沉淀区域5底部的密封隔板3的上端面,接着启动沉淀物卸料装置13,将絮状沉淀物和不溶于水的杂质刮除至沉淀物排泄口25,压滤模块26用于对重金属离子絮状沉淀物和不溶于水的杂质进行二次过滤,过滤后在过滤板262上形成滤渣饼便于将有害物质进行固化,而过滤后的锂电池废液继续通过排水管264进入微生物降解区域6内,进行微生物降解反应。As shown in Figures 1 and 5, the flocculant adding device 12 is used to pump acid or alkaline solution into the reaction precipitation area 5 to adjust the acidity and alkalinity of the lithium battery waste liquid in the reaction precipitation area 5, so that the reaction precipitation The pH value of the lithium battery waste liquid in area 5 is 6-7, which is suitable for the subsequent microbial degradation treatment; the heavy metal scavenger is pumped into the reaction precipitation area 5 through the flocculant adding device 12, and the heavy metal scavenger and the lithium battery waste liquid Heavy metal ions combine to form flocculent precipitates. The reaction time of the heavy metal scavenger is 2 to 3 minutes. Then the central control system opens the second solenoid valve 14 to flow the lithium battery waste liquid in the reaction precipitation area 5 into the microbial degradation area 6. Due to The setting of filter screen 15 makes the heavy metal ion floc precipitate and water-insoluble impurity precipitate on the upper end surface of the sealing partition 3 at the bottom of the reaction precipitation area 5, then start the sediment unloading device 13, the floc precipitate and The water-insoluble impurities are scraped off to the sediment discharge port 25, and the filter press module 26 is used for secondary filtration of the heavy metal ion flocculent sediment and water-insoluble impurities. After filtering, a filter residue cake is formed on the filter plate 262 to facilitate Harmful substances are solidified, and the filtered lithium battery waste liquid continues to enter the microbial degradation area 6 through the drain pipe 264 to undergo microbial degradation reactions.

具体地,如图7所示,压滤模块26包括设置于处理罐1外部的过滤箱261,过滤箱261位于沉淀物排泄口25的下方,过滤箱261内设置可拆卸连接有过滤板262,过滤箱261的顶部设置有与沉淀物排泄口25连通的管道,沉淀物排泄口25处设置有与中央处理系统2电性连接的第五电磁阀263;第五电磁阀263为常闭状态;过滤箱261的底部设置有与微生物降解区域6连通的排水管264;过滤箱261通过支撑架265与处理罐1的侧部固定连接。Specifically, as shown in FIG. 7 , the filter press module 26 includes a filter box 261 arranged outside the treatment tank 1, the filter box 261 is located below the sediment discharge port 25, and a filter plate 262 is detachably connected to the filter box 261. The top of the filter box 261 is provided with a pipeline communicating with the sediment discharge port 25, and the sediment discharge port 25 is provided with a fifth solenoid valve 263 electrically connected to the central processing system 2; the fifth solenoid valve 263 is in a normally closed state; The bottom of the filter box 261 is provided with a drain pipe 264 communicating with the microbial degradation area 6 ; the filter box 261 is fixedly connected to the side of the treatment tank 1 through a support frame 265 .

通过光合细菌投放装置17将光合细菌液泵入微生物降解区域6内,对锂电池废液中的有机物、硫化物、氨等进行微生物降解作用,达到锂电池废液处理的目的,使得锂电池废液达到排放标准。The photosynthetic bacteria liquid is pumped into the microbial degradation area 6 through the photosynthetic bacteria feeding device 17, and the organic matter, sulfide, ammonia, etc. The liquid meets the discharge standard.

处理完后的锂电池废液符合排放标准后进入底部过滤排泄区域7,底部过滤排泄区域7内的锂电池废液中含有微生物絮状物,通过出水口19排出至外部过滤装置,对锂电池废液中的微生物絮状物进行二次过滤沉淀后,排放沉淀完后的锂电池废液。The lithium battery waste liquid after treatment meets the discharge standard and then enters the bottom filter discharge area 7. The lithium battery waste liquid in the bottom filter discharge area 7 contains microbial flocs, and is discharged to the external filter device through the water outlet 19, which is harmful to the lithium battery. After the microbial flocs in the waste liquid undergo secondary filtration and precipitation, the lithium battery waste liquid after precipitation is discharged.

在本实施例中,反应沉淀区域5所在处理罐1位置的侧壁上设有采样管21,采样管21上设置有与中央处理系统2电性连接的第六电磁阀22,采样管21的末端设置有与中央处理系统2电性连接的电pH计23和废水成分检测装置24;电pH计23和废水成分检测装置24用于检测反应沉淀区域5内锂电池废液的pH值和废水成分,当pH值和废水成分满足预设值后,表明反应沉淀区域5中的当前锂电池废液反应完成,通过中央控制系统打开第二电磁阀14,将反应后的锂电池废液排入微生物降解区域6。具体地,废水成分参数包括但不局限为COD、BOD、浊度、电导率、和总有机碳等参数。In this embodiment, a sampling tube 21 is provided on the side wall of the processing tank 1 where the reaction precipitation area 5 is located, and the sampling tube 21 is provided with a sixth solenoid valve 22 electrically connected to the central processing system 2. The end is provided with an electric pH meter 23 and a waste water composition detection device 24 electrically connected to the central processing system 2; the electric pH meter 23 and the waste water composition detection device 24 are used to detect the pH value of the lithium battery waste liquid and the waste water composition, when the pH value and wastewater composition meet the preset value, it indicates that the reaction of the current lithium battery waste liquid in the reaction precipitation area 5 is completed, and the second solenoid valve 14 is opened through the central control system to discharge the reacted lithium battery waste liquid into the Microbial degradation zone 6. Specifically, the wastewater component parameters include but are not limited to parameters such as COD, BOD, turbidity, conductivity, and total organic carbon.

具体地,如图5所示,絮凝剂添加装置12包括与处理罐1外壁固定连接的安装架121,安装架121上设置有酸液添加箱122、碱液添加箱123和絮凝剂添加箱124,酸液添加箱122内填充有酸液,碱液添加箱123内填充有碱液,絮凝剂添加箱124内填充有重金属捕捉剂;每个添加箱内均设置有一个与中央控制器电性连接的水泵,水泵用于将各个添加箱内的液体泵入反应沉淀区域5内。Specifically, as shown in Figure 5, the flocculant addition device 12 includes a mounting frame 121 fixedly connected to the outer wall of the treatment tank 1, and the mounting frame 121 is provided with an acid solution addition box 122, an alkali solution addition box 123 and a flocculant addition box 124 , the acid solution addition box 122 is filled with acid solution, the lye addition box 123 is filled with lye, and the flocculant addition box 124 is filled with heavy metal scavenger; A connected water pump is used to pump the liquid in each addition tank into the reaction precipitation area 5 .

为了实现对反应沉淀区域5底部封闭隔板上端面的沉淀物进行刮除,反应沉淀区域5的侧壁上开设有一个沉淀物排泄口25,沉淀物排泄口25通过管道连接有压滤模块26;沉淀物排泄口25的下侧与反应沉淀区域5底部的密封隔板3上端面平齐。In order to scrape off the sediment on the upper surface of the closed partition at the bottom of the reaction precipitation area 5, a sediment discharge port 25 is provided on the side wall of the reaction precipitation area 5, and the sediment discharge port 25 is connected with a filter press module 26 through a pipeline ; The lower side of the sediment discharge port 25 is flush with the upper end surface of the sealing partition 3 at the bottom of the reaction precipitation area 5 .

如图6所示,反应沉淀区域5底部的密封隔板3内设置有第一安装槽27,第一安装槽27的一侧贯穿处理罐1。As shown in FIG. 6 , a first installation groove 27 is provided in the sealing partition 3 at the bottom of the reaction precipitation area 5 , and one side of the first installation groove 27 runs through the treatment tank 1 .

沉淀物卸料装置13包括设置有位于反应沉淀区域5底部密封隔板3上端面的刮板件131,刮板件131一端的下端面设置有转动轴132,转动轴132一端与刮板件131下端面固定连接,另一端穿过反应沉淀区域5底部密封隔板3位于第一安装槽27,转动轴132与反应沉淀区域5底部密封隔板3之间设置有密封环。The sediment discharge device 13 includes a scraper member 131 located on the upper end surface of the sealing partition 3 at the bottom of the reaction precipitation area 5 , and a rotating shaft 132 is provided on the lower end surface of one end of the scraper member 131 , and one end of the rotating shaft 132 is connected to the scraper member 131 The lower end surface is fixedly connected, and the other end passes through the bottom sealing partition 3 of the reaction precipitation area 5 and is located in the first installation groove 27 . A sealing ring is arranged between the rotating shaft 132 and the bottom sealing partition 3 of the reaction precipitation area 5 .

位于第一安装槽27内转动轴132的端部设置有第一伞状从动齿轮133;处理罐1的外壁上设置有与中央控制器电性连接的第一电机134,第一电机134的输出端上水平设置有一根位于第一安装槽27内的第一传动杆135,第一传动杆135上设置有一个与第一伞状从动齿轮133啮合的第一伞状主动齿轮136。A first bevel-shaped driven gear 133 is provided at the end of the rotating shaft 132 in the first installation groove 27; a first motor 134 electrically connected to the central controller is provided on the outer wall of the processing tank 1, and the first motor 134 A first transmission rod 135 located in the first mounting groove 27 is horizontally disposed on the output end, and a first bevel-shaped driving gear 136 meshing with the first bevel-shaped driven gear 133 is disposed on the first transmission rod 135 .

进一步地,过滤网15的上端面与反应沉淀区域5底部的密封隔板3上端面平齐,当第一电机134驱动刮板件131绕转动轴132旋转时,刮板件131下端将过滤网15上的沉淀物和不溶于水的杂质进行刮除至沉淀物排泄口25,避免堵塞过滤网15。Further, the upper end surface of the filter screen 15 is flush with the upper end surface of the sealing partition 3 at the bottom of the reaction precipitation area 5, and when the first motor 134 drives the scraper piece 131 to rotate around the rotation axis 132, the lower end of the scraper piece 131 will move the filter screen. The sediment on the 15 and the water-insoluble impurity are scraped off to the sediment discharge port 25 to avoid blocking the filter screen 15.

具体地,处理罐1为中空圆柱结构。如图9~图10所示,刮板件131包括第一刮板杆1311,第一刮板杆1311呈中空柱状结构,第一刮板杆1311的横截面呈底部具有开口的“门”字形结构。Specifically, the processing tank 1 is a hollow cylindrical structure. As shown in Figures 9 to 10, the scraper member 131 includes a first scraper rod 1311, the first scraper rod 1311 has a hollow columnar structure, and the cross section of the first scraper rod 1311 is in the shape of a "door" with an opening at the bottom structure.

第一刮板杆1311的内部设置有第二刮板杆1312,第二刮板杆1312通过限位槽和限位块配合的方式与第一刮板件131的内壁滑动连接,限位槽和限位块的长度方向与第一刮板件131的长度方向同向,第二刮板杆1312的尾端与第一刮板杆1311之间设置有推力弹簧1313,第二刮板杆1312的自由端上滚动设置有滚珠1314。The inside of the first scraper rod 1311 is provided with a second scraper rod 1312, and the second scraper rod 1312 is slidably connected with the inner wall of the first scraper member 131 through the cooperation of the limiting groove and the limiting block. The length direction of the limit block is in the same direction as the length direction of the first scraper member 131, and a thrust spring 1313 is arranged between the tail end of the second scraper rod 1312 and the first scraper rod 1311, and the second scraper rod 1312 Rolling balls 1314 are provided on the free end.

第一刮板杆1311和第二刮板杆1312的下端面均与反应沉淀区域5底部的密封隔板3上端面接触。转动轴132与第一刮板杆1311的一端固定连接,转动轴132位于反应沉淀区域5底部密封隔板3的边缘处。Both the lower end surfaces of the first scraper rod 1311 and the second scraper rod 1312 are in contact with the upper end surface of the sealing partition 3 at the bottom of the reaction precipitation area 5 . The rotating shaft 132 is fixedly connected to one end of the first scraper rod 1311 , and the rotating shaft 132 is located at the edge of the sealing partition 3 at the bottom of the reaction precipitation area 5 .

在推力弹簧1313的推力作用下,无论刮板件131处于哪个位置,刮板件131的整体长度相对应的发生改变,始终将第二刮板杆1312的自由端上的滚珠1314与反应沉淀区域5的侧壁抵紧接触,更加彻底地刮除反应沉淀区域5底部的密封隔板3上的沉淀物和不溶于水的杂质。Under the thrust of the thrust spring 1313, no matter which position the scraper member 131 is in, the overall length of the scraper member 131 will change correspondingly, always connecting the ball 1314 on the free end of the second scraper rod 1312 with the reaction precipitation area. The side walls of 5 are in close contact, and the sediment and water-insoluble impurities on the sealing partition 3 at the bottom of the reaction precipitation area 5 are scraped off more thoroughly.

进一步地,沉淀物排泄口25的竖直投影呈圆弧结构,沉淀物排泄口25对应的圆弧直径与密封隔板3的直径相同,沉淀物排泄口25的一侧与第一刮板杆1311的一端所在位置相接;第一刮板杆1311的两侧壁上均设置有一个呈圆弧结构的推块1315,推块1315外侧的弧长大于沉淀物排泄口25的弧长,推块1315外侧的圆弧线对应的圆弧直径与密封隔板3的直径相同。推块1315与沉淀物排泄口25的配合,避免刮板件131存在刮除死角。Further, the vertical projection of the sediment discharge port 25 is in a circular arc structure, the diameter of the arc corresponding to the sediment discharge port 25 is the same as the diameter of the sealing partition 3, and one side of the sediment discharge port 25 is connected to the first scraper rod. The positions of one end of 1311 are connected; the two sidewalls of the first scraper rod 1311 are provided with a push block 1315 in a circular arc structure, and the arc length of the outside of the push block 1315 is greater than the arc length of the sediment discharge port 25. The arc diameter corresponding to the arc line outside the block 1315 is the same as the diameter of the sealing partition 3 . The cooperation between the push block 1315 and the sediment discharge port 25 prevents the scraper member 131 from having a scraping dead angle.

在本实施例中,光合细菌投放装置17包括与微生物降解区域6连通的光合细菌液添加箱171;微生物降解区域6内竖直设置有多根光源灯柱28,多根光源灯柱28以处理罐1的轴线为中心环向间隔均匀设置,每根光源灯柱28的两端分别与微生物降解区域6顶部和底部的密封隔板3密封连接。光源灯柱28为光合细菌提供光源,光合细菌在光源灯柱28的作用下进行不放氧光合作用,对锂电池废液中的有机物、硫化物、氨等进行微生物降解作用,达到锂电池废液处理的目的。In the present embodiment, the photosynthetic bacteria delivery device 17 includes a photosynthetic bacteria liquid addition box 171 communicated with the microbial degradation area 6; a plurality of light source lamp posts 28 are vertically arranged in the microbial degradation area 6, and the plurality of light source lamp posts 28 are used for processing The axis of the tank 1 is centered and evenly spaced in the circumferential direction, and the two ends of each light source lamp column 28 are respectively sealed and connected with the sealing partitions 3 at the top and bottom of the microbial degradation area 6 . The light source lamp post 28 provides a light source for photosynthetic bacteria, and the photosynthetic bacteria perform oxygen-free photosynthesis under the action of the light source lamp post 28, and perform microbial degradation on organic matter, sulfide, ammonia, etc. purpose of liquid treatment.

如图8和图11所示,微生物降解区域6还设置有灯柱刮壁装置29;微生物降解区域6底部的密封隔板3内设置有第二安装槽30,第二安装槽30的一侧水平贯穿微生物降解区域6底部的密封隔板3;处理罐1外壁上设置有与中央处理系统2电性连接的第二电机291,第二电机291输出端上设置有一根位于第二安装槽30内的第二传动杆292,第二传动杆292上设置有一个第二伞状主动齿轮293;As shown in Figures 8 and 11, the microbial degradation area 6 is also provided with a lamppost wall scraping device 29; a second installation groove 30 is arranged in the sealing partition 3 at the bottom of the microbial degradation area 6, and one side of the second installation groove 30 The sealing partition 3 that runs horizontally through the bottom of the microbial degradation area 6; the outer wall of the treatment tank 1 is provided with a second motor 291 electrically connected to the central processing system 2, and the output end of the second motor 291 is provided with a Inside the second transmission rod 292, the second transmission rod 292 is provided with a second umbrella-shaped driving gear 293;

灯柱刮壁装置29包括设置于微生物降解区域6中心位置的螺纹杆294,螺纹杆294上螺纹连接有一个支撑板295,支撑板295上设置有数量与多根光源灯柱28数量相同的安装孔296,每个安装孔296内均设置有圆环刮板297,每个圆环刮板297均与光源灯柱28的圆周外壁接触。The lamppost wall scraping device 29 includes a threaded rod 294 arranged in the center of the microbial degradation area 6, a support plate 295 is threadedly connected to the threaded rod 294, and the support plate 295 is provided with installations having the same number as the plurality of light source lampposts 28. Holes 296 , each mounting hole 296 is provided with an annular scraper 297 , and each annular scraper 297 is in contact with the peripheral outer wall of the light source lamp post 28 .

螺纹杆294的顶端与微生物降解区域6顶部的密封隔板3转动连接,螺纹杆294的底端穿过微生物降解区域6底部的密封隔板3位于第二安装槽30内,螺纹杆294的底端上设置有与第二伞状主动齿轮293啮合的第二伞状从动齿轮298。The top of the threaded rod 294 is rotatably connected with the sealing partition 3 at the top of the microbial degradation zone 6, and the bottom end of the threaded rod 294 passes through the sealing partition 3 at the bottom of the microbial degradation zone 6 and is positioned in the second mounting groove 30. The bottom of the threaded rod 294 A second bevel driven gear 298 meshing with the second bevel drive gear 293 is arranged on the end.

通过中央控制系统控制第二电机291旋转,第二电机291通过第二传动杆292、第二伞状主动齿轮293和第二伞状从动齿轮298带动螺纹杆294旋转,而旋转螺纹杆294实现将旋转运动转化为支撑板295的竖直运动,进而带动支撑板295上的圆环刮板297对圆周外壁上的附着物进行清理,提高光源灯柱28的透光率和照射效率,保持光能的持续供给,提高了光合细菌微生物降解处理效率;同时竖直运动的支撑板295可以对微生物降解区域6内的锂电池废液起到一定的搅拌作用,实现将光合细菌液混合均匀,也可以提高光合细菌对锂电池废液处理效率。The rotation of the second motor 291 is controlled by the central control system, and the second motor 291 drives the threaded rod 294 to rotate through the second transmission rod 292, the second umbrella-shaped driving gear 293 and the second umbrella-shaped driven gear 298, and the rotating threaded rod 294 realizes Convert the rotary motion into the vertical motion of the support plate 295, and then drive the ring scraper 297 on the support plate 295 to clean the attachments on the outer wall of the circumference, improve the light transmittance and irradiation efficiency of the light source lamp post 28, and keep the light The continuous supply of energy improves the efficiency of photosynthetic bacteria microbial degradation treatment; at the same time, the vertically moving support plate 295 can stir the lithium battery waste liquid in the microbial degradation area 6 to achieve uniform mixing of the photosynthetic bacteria liquid, and also It can improve the treatment efficiency of photosynthetic bacteria on lithium battery waste liquid.

综上所述,本发明通过多块密封隔板3将处理罐1分为多个反应区域,具体地,废液收集区域4用于存放锂电池废液,反应沉淀区域5用于对锂电池废液进行酸碱平衡、对锂电池废液中的重金属离子进行沉淀和对锂电池废液中的不容物进行沉淀,微生物降解区域6通过微生物对锂电池废液中的有机物进行生物降解处理,消除锂电池废液中的有机物,使得锂电池废液达到排放标准;本发明中的锂电池废液处理机构,将存放、酸碱平衡、沉淀重金属离子和不容物以及降解有机物的功能集中在一起,且在对锂电池废液进行处理的过程中,产生的有害气体被废气排气装置10中的活性炭板103捕捉,不会将有害气体泄出,不会产生二次污染。In summary, the present invention divides the treatment tank 1 into a plurality of reaction areas through a plurality of sealing partitions 3, specifically, the waste liquid collection area 4 is used to store lithium battery waste liquid, and the reaction precipitation area 5 is used to clean the lithium battery. The acid-base balance of the waste liquid, the precipitation of heavy metal ions in the lithium battery waste liquid and the precipitation of the incompatible substances in the lithium battery waste liquid, the microbial degradation zone 6 biodegrades the organic matter in the lithium battery waste liquid through microorganisms, Eliminate the organic matter in the lithium battery waste liquid, so that the lithium battery waste liquid reaches the discharge standard; the lithium battery waste liquid treatment mechanism in the present invention integrates the functions of storage, acid-base balance, precipitation of heavy metal ions and incompatible substances, and degradation of organic matter , and during the process of treating the lithium battery waste liquid, the harmful gas generated is captured by the activated carbon plate 103 in the exhaust gas exhaust device 10, so that the harmful gas will not be released and secondary pollution will not occur.

Claims (10)

1. The lithium battery waste liquid treatment mechanism is characterized by comprising a treatment tank with a closed structure, wherein a central processing system is arranged on the side wall of the top of the treatment tank;
a plurality of sealing partition plates are arranged in the treatment tank, are arranged at intervals along the height direction of the treatment tank, and are used for dividing the treatment tank into a plurality of reaction areas, wherein the plurality of reaction areas sequentially comprise a waste liquid collecting area, a reaction sedimentation area, a microorganism degradation area and a bottom filtering and draining area from top to bottom;
the waste liquid collecting area and the top of the treatment tank form a sealing area, and the top of the treatment tank is provided with an aeration device, a waste liquid hopper device and a waste gas exhaust device;
the waste liquid collecting area is communicated with the reaction precipitation area through a pipeline with a first electromagnetic valve;
a flocculating agent adding device and a sediment discharging device are arranged on the side wall of the treatment tank where the reaction sedimentation area is located;
the reaction precipitation area is communicated with the microbial degradation area through a pipeline with a second electromagnetic valve; a filter screen is arranged at the pipe orifice of the pipeline with the second electromagnetic valve; an overhaul window is arranged on the side wall of the reaction precipitation area;
a photosynthetic bacteria throwing device is arranged on the side wall of the treatment tank where the microbial degradation area is positioned;
the microbial degradation area is communicated with the bottom filtering and draining area through a pipeline with a third electromagnetic valve, a water outlet is arranged at the bottom of the bottom filtering and draining area, and the water outlet is communicated with an external filtering device through a pipeline;
the aeration device, the waste liquid hopper device, the first electromagnetic valve, the sediment discharging device, the second electromagnetic valve, the photosynthetic bacteria throwing device and the third electromagnetic valve are electrically connected with the central processing system.
2. The lithium battery waste liquid treatment mechanism according to claim 1, wherein the central processing system is a PLC controller.
3. The lithium battery waste liquid treatment mechanism according to claim 1, wherein the aeration device comprises an inflator pump fixedly connected with the top of the treatment tank, an inflation tube is connected to the inflator pump, the bottom end of the inflation tube passes through the top of the treatment tank and is positioned at the bottom in the waste liquid collection area, and the free end of the inflation tube is connected with an aeration head with a plurality of air outlet holes;
the waste liquid hopper device comprises a liquid inlet hopper with a big top and a small bottom, the bottom of the liquid inlet hopper penetrates through the top of the treatment tank to be communicated with the waste liquid collecting area, and a fourth electromagnetic valve for controlling on-off of liquid inlet and electrically connected with the central processing system is arranged at the bottom of the liquid inlet hopper;
the exhaust gas exhaust device comprises an exhaust pipe which is arranged at the top of the treatment tank and communicated with the waste liquid collecting area, an exhaust gas filtering module is communicated on the exhaust pipe, the exhaust gas filtering module comprises an exhaust gas box body communicated with an exhaust gas pipe, and a plurality of activated carbon plates are detachably connected in the exhaust gas box body.
4. The lithium battery waste liquid treatment mechanism according to claim 3, wherein the exhaust gas box body is provided with a plurality of gaps for the active carbon plates to pass through, each gap is internally provided with an active carbon plate, and the shape of each active carbon plate is matched with the cross section of the exhaust gas box body; a circle of sealing rubber ring is arranged on the side wall around each notch.
5. The lithium battery waste liquid treatment mechanism according to claim 1, wherein a sampling tube is arranged on the side wall of the treatment tank where the reaction precipitation area is located, a sixth electromagnetic valve electrically connected with the central processing system is arranged on the sampling tube, and an electric pH meter and a waste water component detection device electrically connected with the central processing system are arranged at the tail end of the sampling tube;
the flocculant adding device comprises a mounting frame fixedly connected with the outer wall of the treatment tank, an acid liquor adding box, an alkali liquor adding box and a flocculant adding box are arranged on the mounting frame, acid liquor is filled in the acid liquor adding box, alkali liquor is filled in the alkali liquor adding box, and a heavy metal capturing agent is filled in the flocculant adding box;
each adding box is internally provided with a water pump electrically connected with the central controller, and the water pump is used for pumping liquid in each adding box into the reaction precipitation area.
6. The lithium battery waste liquid treatment mechanism according to claim 5, wherein a sediment drain is formed on the side wall of the reaction sedimentation area, and the sediment drain is connected with a filter pressing module through a pipeline; the lower side of the sediment drain is flush with the upper end surface of the sealing partition plate at the bottom of the reaction sediment area;
a first mounting groove is formed in the sealing partition plate at the bottom of the reaction precipitation area, and one side of the first mounting groove penetrates through the treatment tank;
the sediment discharging device comprises a scraper plate arranged on the upper end face of the bottom sealing partition plate of the reaction sedimentation area, a rotating shaft is arranged on the lower end face of one end of the scraper plate, one end of the rotating shaft is fixedly connected with the lower end face of the scraper plate, the other end of the rotating shaft penetrates through the bottom sealing partition plate of the reaction sedimentation area and is positioned in the first mounting groove, and a sealing ring is arranged between the rotating shaft and the bottom sealing partition plate of the reaction sedimentation area;
the end part of the rotating shaft positioned in the first mounting groove is provided with a first umbrella-shaped driven gear; the outer wall of the treatment tank is provided with a first motor electrically connected with the central controller, the output end of the first motor is horizontally provided with a first transmission rod positioned in a first mounting groove, and the first transmission rod is provided with a first bevel driving gear meshed with the first bevel driven gear.
7. The lithium battery waste liquid treatment mechanism according to claim 6, wherein the treatment tank is of a hollow cylindrical structure, the scraper member comprises a first scraper rod which is of a hollow columnar structure, and the cross section of the first scraper rod is of a door-shaped structure with an opening at the bottom;
the inside of the first scraper rod is provided with a second scraper rod, the second scraper rod is in sliding connection with the inner wall of the first scraper plate in a mode of matching a limit groove and a limit block, the length directions of the limit groove and the limit block are in the same direction as the length direction of the first scraper plate, a thrust spring is arranged between the tail end of the second scraper rod and the first scraper rod, and a ball is arranged at the free end of the second scraper rod in a rolling manner;
the lower end surfaces of the first scraper rod and the second scraper rod are contacted with the upper end surface of the sealing partition plate at the bottom of the reaction precipitation area;
the rotating shaft is fixedly connected with one end of the first scraper rod and is positioned at the edge of the sealing partition plate at the bottom of the reaction precipitation area.
8. The lithium battery waste liquid treatment mechanism according to claim 7, wherein the vertical projection of the sediment drain opening is in an arc structure, the diameter of an arc corresponding to the sediment drain opening is the same as the diameter of the sealing partition plate, and one side of the sediment drain opening is connected with the position of one end of the first scraper rod;
the two side walls of the first scraper rod are respectively provided with a pushing block with an arc structure, the arc length of the outer side of each pushing block is larger than that of a sediment drain opening, and the diameter of an arc corresponding to the arc line of the outer side of each pushing block is the same as that of the sealing partition plate.
9. The lithium battery waste liquid treatment mechanism according to claim 8, wherein the filter pressing module comprises a filter box arranged outside the treatment tank, the filter box is positioned below the sediment drain, a filter plate is detachably connected in the filter box, a pipeline communicated with the sediment drain is arranged at the top of the filter box, and a fifth electromagnetic valve electrically connected with the central processing system is arranged at the sediment drain; the fifth electromagnetic valve is in a normally closed state; the bottom of the filter box is provided with a drain pipe communicated with the microbial degradation area; the filter box is fixedly connected with the side part of the treatment tank through a support frame.
10. The lithium battery waste liquid treatment mechanism according to claim 1, wherein the photosynthetic bacteria putting device comprises a photosynthetic bacteria liquid adding tank communicated with the microbial degradation area;
a plurality of light source lamp posts are vertically arranged in the microbial degradation area, the light source lamp posts are uniformly arranged at intervals in the circumferential direction by taking the axis of the treatment tank as the center, and two ends of each light source lamp post are respectively and hermetically connected with the sealing partition plates at the top and the bottom of the microbial degradation area;
the microbial degradation area is also provided with a lamp post wall scraping device;
a second mounting groove is formed in the sealing partition plate at the bottom of the microbial degradation area, and one side of the second mounting groove horizontally penetrates through the sealing partition plate at the bottom of the microbial degradation area; a second motor electrically connected with the central processing system is arranged on the outer wall of the processing tank, a second transmission rod positioned in a second mounting groove is arranged at the output end of the second motor, and a second umbrella-shaped driving gear is arranged on the second transmission rod;
the lamp post wall scraping device comprises a threaded rod arranged at the central position of the microbial degradation area, a supporting plate is connected to the threaded rod in a threaded manner, the supporting plate is provided with mounting holes the number of which is the same as that of the plurality of light source lamp posts, circular ring scraping plates are arranged in each mounting hole, and each circular ring scraping plate is contacted with the circumferential outer wall of the light source lamp post;
the top of the threaded rod is rotationally connected with the sealing partition plate at the top of the microbial degradation area, the bottom of the threaded rod penetrates through the sealing partition plate at the bottom of the microbial degradation area and is positioned in the second mounting groove, and a second bevel driven gear meshed with the second bevel driving gear is arranged at the bottom of the threaded rod.
CN202310385712.9A 2023-04-12 2023-04-12 A lithium battery waste liquid treatment mechanism Withdrawn CN116375271A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN118305176A (en) * 2024-04-22 2024-07-09 陕西科技大学 In-situ mineralization extraction system and method for heavy metals in soil
CN118997310A (en) * 2024-07-29 2024-11-22 中国十七冶集团有限公司 Battery wastewater temporary storage pool with online monitoring function and method thereof

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN118305176A (en) * 2024-04-22 2024-07-09 陕西科技大学 In-situ mineralization extraction system and method for heavy metals in soil
CN118997310A (en) * 2024-07-29 2024-11-22 中国十七冶集团有限公司 Battery wastewater temporary storage pool with online monitoring function and method thereof

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Application publication date: 20230704