WO2021036918A1 - 一种废电解液可直接再生利用的废旧电池破碎分选方法 - Google Patents

一种废电解液可直接再生利用的废旧电池破碎分选方法 Download PDF

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WO2021036918A1
WO2021036918A1 PCT/CN2020/110413 CN2020110413W WO2021036918A1 WO 2021036918 A1 WO2021036918 A1 WO 2021036918A1 CN 2020110413 W CN2020110413 W CN 2020110413W WO 2021036918 A1 WO2021036918 A1 WO 2021036918A1
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sorting
waste
electrolyte
filtrate
lead paste
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PCT/CN2020/110413
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English (en)
French (fr)
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费跃波
陈炳敏
袁成
陈利华
施欢欢
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浙江浙矿重工股份有限公司
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Publication of WO2021036918A1 publication Critical patent/WO2021036918A1/zh

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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09B—DISPOSAL OF SOLID WASTE
    • B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09B—DISPOSAL OF SOLID WASTE
    • B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
    • B09B3/80—Destroying solid waste or transforming solid waste into something useful or harmless involving an extraction step
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00—Secondary cells; Manufacture thereof
    • H01M10/54—Reclaiming serviceable parts of waste accumulators
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09B—DISPOSAL OF SOLID WASTE
    • B09B2101/00—Type of solid waste
    • B09B2101/02—Gases or liquids enclosed in discarded articles, e.g. aerosol cans or cooling systems of refrigerators
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00—Technologies for solid waste management
    • Y02W30/50—Reuse, recycling or recovery technologies
    • Y02W30/84—Recycling of batteries or fuel cells

Definitions

  • the invention relates to the technical field of waste battery treatment, in particular to the technical field of waste battery electrolyte recovery and reuse.
  • waste lead-acid batteries are a major source of pollution in the natural environment. If the waste lead-acid batteries are not handled properly, it will have a serious impact on the environment.
  • the electrodes of lead-acid batteries are mainly made of lead and its oxides.
  • the liquid is a kind of storage battery of sulfuric acid solution. In the discharged state, the main component of the positive electrode is lead dioxide, and the main component of the negative electrode is lead; in the charged state, the main component of the positive and negative electrodes are lead sulfate. It is divided into exhaust-type batteries and maintenance-free lead-acid batteries.
  • the traditional waste lead-acid battery crushing and sorting system uses ship-shaped scraper and adds flocculant to the ship-shaped scraper cabin, so that the rapid precipitation of lead paste is the main Lead paste sorting and conveying process.
  • This traditional structure can realize large-volume crushing and high-precision sorting of waste lead-acid batteries.
  • the waste lead-acid batteries contain a large amount of waste electrolyte that produces chloride ions after being precipitated by flocculants. , After collection, the waste electrolyte cannot be directly reused after membrane filtration treatment, but can only be neutralized by the sewage station, which generates a large amount of hazardous waste, which is extremely costly and is extremely harmful to the environment.
  • the purpose of the present invention is to solve the problems in the prior art and propose a waste battery crushing and sorting method in which the waste electrolyte can be directly recycled. It can collect the waste battery electrolyte stock solution, which does not contain chloride ions, so that the electrolyte solution The original solution can be directly processed by membrane to remove the metal cations and then directly reused, thereby greatly reducing the generation of hazardous waste and reducing production costs.
  • the present invention proposes a method for crushing and sorting waste batteries in which waste electrolyte can be directly recycled, which includes the following steps:
  • Step S1 Feeding: Place the waste battery raw materials to be processed at the feeding end of the metal chain conveyor equipment;
  • Step S2 Primary crushing: The metal chain plate conveying equipment in step S1 transports the waste batteries to the primary hammer crusher, and the heavy alloy hammer in the primary hammer crusher hits at a high speed to make the waste batteries Broken into first grade crushed material;
  • Step S3 Primary sorting and waste electrolyte recovery: the first-grade crushed material falls into the primary lead paste sorting sieve, through high-frequency vibration and high-pressure water flushing, the lead paste particles and waste electrolyte stock solution pass through the separation sieve.
  • the 0.6 mm slotted screen falls into the first-level mixing tank below;
  • Step S4 Two-stage crushing: convey the screened material after the first-stage sorting to the second-stage crusher through the vibrating feeder, and pass the high-speed impact of the heavy alloy hammer in the second-stage hammer crusher to make waste The battery is broken into secondary crushed material;
  • Step S5 Secondary sorting: drop the secondary crushed material into the secondary lead paste sorting sieve, through high-frequency vibration and high-pressure water flushing, so that the lead paste particles and the original electrolyte solution pass through the sorting sieve with a gap of 0.6 mm. The screen falls into the secondary mixing tank below;
  • Step S6 Primary and secondary recovery: the lead paste falling through the screen during the screening is directly dropped into the primary and secondary lead paste mixing tanks under the lead paste sorting screen, and the agitator of the primary and secondary lead paste mixing tanks is opposite to the tank The mixture of waste electrolyte and lead paste in the body is continuously stirred until the mixture is adjusted to a certain density;
  • Step S7 solid-liquid separation: the mixture of the electrolyte stock solution and the lead paste after the stirring in step S6 is transported to the filter press through a horizontal centrifugal pump for solid-liquid separation, and the filtrate is extracted;
  • Step S8 Filtrate treatment: The electrolyte stock solution that has undergone solid-liquid separation in step S7 is transported to the filtrate stirring tank.
  • the filtrate stirring tank is equipped with a stirrer. The stirrer continuously stirs the filtrate.
  • the outside of the stirring tank is equipped with an acid pump. The acid pump transports the filtrate to the next process;
  • Step S9 membrane filtration: the filtrate is transported to the membrane filtration equipment through the acid pump in step S8, and the filtrate is membrane filtered through the membrane filtration equipment to remove the metal cations in the filtrate.
  • the electrolyte after removing the metal cations can be directly reused .
  • step S3 primary sorting and electrolyte stock recovery and step S5 secondary sorting are assisted by high-pressure water washing to drop the lead paste on the sorting screen through the screen.
  • the lead paste stirring tank is provided with a liquid level sensor and a weighing sensor, and the density of the mixture is adjusted by the cooperation of the liquid level sensor and the weighing sensor, and the finished product density of the mixture is 1.80-1.85 g/cm 3 .
  • the filtrate stirring tank is provided with a liquid level sensor in the filtrate stirring tank.
  • the electrolyte in the filtrate stirring tank provides high pressure for crushing and sorting through an acid pump. Circulating water, when the liquid level is high, the electrolyte is transported to the next process through the acid pump for membrane filtration.
  • the present invention adopts the material stirring collection process to replace the ship-shaped scraper sedimentation and transportation process, cancels the traditional flocculant addition process, and removes waste.
  • the electrolyte stock solution collected in the waste lead-acid battery is used as the circulating water of the whole system, and new water is not used as the sorting medium.
  • the collected electrolyte can be directly processed by membrane to remove the metal cations and then directly Reuse, when the original electrolyte solution contains unremovable anions, the original electrolyte solution cannot be directly reused in the battery. The process of this method does not use fresh water.
  • Fig. 1 is a schematic flow chart of a method for crushing and separating waste batteries in which waste electrolyte can be directly recycled according to the present invention.
  • the present invention is a method for crushing and sorting waste batteries in which waste electrolyte can be directly recycled, including the following steps:
  • Step S1 Feeding: Place the waste battery raw materials to be processed at the feeding end of the metal chain conveyor equipment;
  • Step S2 Primary crushing: The metal chain plate conveying equipment in step S1 transports the waste batteries to the primary hammer crusher, and the heavy alloy hammer in the primary hammer crusher hits at a high speed to make the waste batteries Broken into first grade crushed material;
  • Step S3 First-level sorting and waste electrolyte recovery: the first-level crushed material falls into the first-level lead paste sorting sieve, and through high-frequency vibration and high-pressure water flushing, the lead paste particles and waste electrolyte pass through the sorting sieve with a gap of 0.6 The millimeter slit screen falls into the first-level mixing tank below;
  • Step S4 Two-stage crushing: the screened material after the first-stage sorting is conveyed to the second-stage hammer crusher through the vibrating feeder, and is hit by the heavy alloy hammer in the second-stage hammer crusher at high speed. Break the used batteries into secondary crushed materials;
  • Step S5 Secondary sorting: drop the secondary crushed material into the secondary lead paste sorting sieve, through high-frequency vibration and high-pressure water flushing, so that the lead paste particles and waste electrolyte pass through the sorting sieve with a gap of 0.6 mm. The screen falls into the secondary mixing tank below;
  • Step S66 Primary and secondary recovery: the lead paste that falls through the screen during the screening is directly dropped into the primary and secondary lead paste mixing tanks under the lead paste sorting screen, and the agitator of the primary and secondary lead paste mixing tanks is opposite to the tank The mixture of waste electrolyte and lead paste in the body is continuously stirred until the mixture is adjusted to a certain density;
  • Step S7 solid-liquid separation: the mixture of waste electrolyte and lead paste after the stirring in step S6 is transported to the filter press through a horizontal centrifugal pump for solid-liquid separation, and the filtrate is extracted;
  • Step S8 Filtrate treatment: The electrolyte stock solution that has undergone solid-liquid separation in step S7 is transported to the filtrate stirring tank.
  • the filtrate stirring tank is equipped with a stirrer. The stirrer continuously stirs the filtrate.
  • the outside of the stirring tank is equipped with an acid pump. The acid pump transports the filtrate to the next process;
  • Step S9 membrane filtration: the filtrate is transported to the membrane filtration equipment through the acid pump in step S8, and the filtrate is membrane filtered through the membrane filtration equipment to remove the metal cations in the filtrate.
  • the electrolyte after removing the metal cations can be directly reused .
  • step Said step S3 primary sorting and electrolyte stock recovery and step S5 secondary sorting are assisted by high-pressure water washing to drop the lead paste on the sorting screen through the sieve, and said step S6 is the primary and secondary recovery
  • the medium-lead paste mixing tank is equipped with a liquid level sensor and a weighing sensor.
  • the density of the mixture is adjusted through the cooperation of the liquid level sensor and the weighing sensor.
  • the finished product density of the mixture is 1.80g/cm 3
  • the filtrate is processed in step S8
  • the filtrate mixing tank is equipped with a liquid level sensor.
  • the electrolyte in the filtrate mixing tank is provided with high-pressure circulating water for crushing and sorting through the acid pump, and when the liquid level is high, the acid is passed
  • the pump transports the electrolyte to the next process for membrane filtration.
  • Step S1 Feeding: Place the waste battery raw materials to be processed at the feeding end of the metal chain conveyor equipment;
  • Step S2 First-level crushing: the metal chain plate conveying equipment in step S1 transports the waste batteries to the first-level hammer crusher, and the heavy alloy hammer in the first-level hammer crusher hits at a high speed to make the waste batteries Broken into first grade crushed material;
  • Step S3 First-level sorting and waste electrolyte recovery: the first-level crushed material falls into the first-level lead paste sorting sieve, and through high-frequency vibration and high-pressure water flushing, the lead paste particles and waste electrolyte pass through the sorting sieve with a gap of 0.6 The millimeter slit screen falls into the first-level mixing tank below;
  • Step S4 Two-stage crushing: the screened material after the first-stage sorting is conveyed to the second-stage hammer crusher through the vibrating feeder, and is hit by the heavy alloy hammer in the second-stage hammer crusher at high speed. Break the used batteries into secondary crushed materials;
  • Step S5 Secondary sorting: drop the secondary crushed material into the secondary lead paste sorting sieve, through high-frequency vibration and high-pressure water flushing, so that the lead paste particles and waste electrolyte pass through the sorting sieve with a gap of 0.6 mm. The screen falls into the secondary mixing tank below;
  • Step S66 Primary and secondary recovery: the lead paste that falls through the screen during the screening is directly dropped into the primary and secondary lead paste mixing tanks under the lead paste sorting screen, and the agitator of the primary and secondary lead paste mixing tanks is opposite to the tank The mixture of waste electrolyte and lead paste in the body is continuously stirred until the mixture is adjusted to a certain density;
  • Step S7 solid-liquid separation: the mixture of waste electrolyte and lead paste after the stirring in step S6 is transported to the filter press through a horizontal centrifugal pump for solid-liquid separation, and the filtrate is extracted;
  • Step S8 filtrate treatment transport the electrolyte stock solution after solid-liquid separation in step S7 to the filtrate stirring tank, the filtrate stirring tank is equipped with a stirrer, and the stirrer continuously stirs the filtrate, and an acid pump is installed outside the stirring tank. The acid pump transports the filtrate to the next process;
  • Step S9 membrane filtration: the filtrate is transported to the membrane filtration equipment through the acid pump in step S8, and the filtrate is membrane filtered through the membrane filtration equipment to remove the metal cations in the filtrate.
  • the electrolyte after removing the metal cations can be directly reused .
  • step Said step S3 primary sorting and electrolyte stock recovery and step S5 secondary sorting are assisted by high-pressure water washing to drop the lead paste on the sorting screen through the sieve, and said step S6 is the primary and secondary recovery
  • the medium lead paste mixing tank is equipped with a liquid level sensor and a weighing sensor. The density of the mixture is adjusted through the cooperation of the liquid level sensor and the weighing sensor. The density of the finished mixture is 1.85g/cm 3 , and the filtrate is being processed in step S8
  • the filtrate mixing tank is equipped with a liquid level sensor.
  • the electrolyte in the filtrate mixing tank is provided with high-pressure circulating water for crushing and sorting through the acid pump, and when the liquid level is high, the acid is passed
  • the pump transports the electrolyte to the next process for membrane filtration.
  • Step S1 Feeding: Place the waste battery raw materials to be processed at the feeding end of the metal chain conveyor equipment;
  • Step S2 Primary crushing: The metal chain plate conveying equipment in step S1 transports the waste batteries to the primary hammer crusher, and the heavy alloy hammer in the primary hammer crusher hits at a high speed to make the waste batteries Broken into first grade crushed material;
  • Step S3 First-level sorting and waste electrolyte recovery: the first-level crushed material falls into the first-level lead paste sorting sieve, and through high-frequency vibration and high-pressure water flushing, the lead paste particles and waste electrolyte pass through the sorting sieve with a gap of 0.6 The millimeter slit screen falls into the first-level mixing tank below;
  • Step S4 Two-stage crushing: the screened material after the first-stage sorting is conveyed to the second-stage hammer crusher through the vibrating feeder, and is hit by the heavy alloy hammer in the second-stage hammer crusher at high speed. Break the used batteries into secondary crushed materials;
  • Step S5 Secondary sorting: drop the secondary crushed material into the secondary lead paste sorting sieve, through high-frequency vibration and high-pressure water flushing, so that the lead paste particles and waste electrolyte pass through the sorting sieve with a gap of 0.6 mm. The screen falls into the secondary mixing tank below;
  • Step S66 Primary and secondary recovery: the lead paste that falls through the screen during the screening is directly dropped into the primary and secondary lead paste mixing tanks under the lead paste sorting screen, and the agitator of the primary and secondary lead paste mixing tanks is opposite to the tank The mixture of waste electrolyte and lead paste in the body is continuously stirred until the mixture is adjusted to a certain density;
  • Step S7 solid-liquid separation: the mixture of waste electrolyte and lead paste after the stirring in step S6 is transported to the filter press through a horizontal centrifugal pump for solid-liquid separation, and the filtrate is extracted;
  • Step S8 filtrate treatment transport the electrolyte stock solution after solid-liquid separation in step S7 to the filtrate stirring tank, the filtrate stirring tank is equipped with a stirrer, and the stirrer continuously stirs the filtrate, and an acid pump is installed outside the stirring tank. The acid pump transports the filtrate to the next process;
  • Step S9 membrane filtration: the filtrate is transported to the membrane filtration equipment through the acid pump in step S8, and the filtrate is membrane filtered through the membrane filtration equipment to remove the metal cations in the filtrate.
  • the electrolyte after removing the metal cations can be directly reused .
  • step Said step S3 primary sorting and electrolyte stock recovery and step S5 secondary sorting are assisted by high-pressure water washing to drop the lead paste on the sorting screen through the sieve, and said step S6 is the primary and secondary recovery
  • the medium lead paste mixing tank is equipped with a liquid level sensor and a weighing sensor.
  • the density of the mixture is adjusted through the cooperation of the liquid level sensor and the weighing sensor.
  • the density of the finished mixture is 1.83g/cm 3
  • the filtrate is processed in step S8
  • the filtrate mixing tank is equipped with a liquid level sensor.
  • the electrolyte in the filtrate mixing tank is provided with high-pressure circulating water for crushing and sorting through the acid pump, and when the liquid level is high, the acid is passed
  • the pump transports the electrolyte to the next process for membrane filtration.

Abstract

一种废电解液可直接再生利用的废旧电池破碎分选方法，包括步骤S1给料；步骤S2一级破碎；步骤S3一级分选及电解液原液回收；步骤S4二级破碎；步骤S5二级分选；步骤S6一二级回收；步骤S7固液分离；步骤S8滤液处理；步骤S9膜过滤；采用物料搅拌收集工艺替代船型刮板机沉淀输送工艺，取消了传统的添加絮凝剂流程，去除电解液中的阳离子，采用废旧铅酸蓄电池中收集的废电解液作为整套系统循环水，不使用新水作为分选的介质，收集后的电解液可以直接通过膜处理去除其中的金属阳离子而后直接回用，采用该方法工艺，不使用新鲜水，大幅度减少了危险废物的产生，降低了生产成本，减少对环境的污染。

Description

一种废电解液可直接再生利用的废旧电池破碎分选方法 【技术领域】
本发明涉及废旧电池处理的技术领域，特别是废旧电池电解液回收再利用的技术领域。
【背景技术】
目前，废旧铅酸电池是自然环境中的一大污染源，如果废旧铅酸电池处理的不妥当，会对环境造成很严重的影响，铅酸电池的电极主要由铅及其氧化物制成，电解液是硫酸溶液的一种蓄电池。放电状态下，正极主要成分为二氧化铅，负极主要成分为铅；充电状态下，正负极的主要成分均为硫酸铅。分为排气式蓄电池和免维护铅酸电池，传统的废旧铅酸蓄电池破碎分选系统都是采用船型刮板机并向船型刮板机舱内添加絮凝剂，从而使铅膏快速沉淀作为主要的铅膏分选和输送工艺，这种传统结构可实现废旧铅酸蓄电池的大产量破碎和高精度分选，但废旧铅酸蓄电池中含有大量的废电解液在经过絮凝剂沉淀后产生了氯离子，废电解液在收集后无法通过膜过滤处理后直接回用，只能通过污水站中和处理，产生大量的危废，处理成本极高，对环境危害极大。
【发明内容】
本发明的目的就是解决现有技术中的问题，提出一种废电解液可直接再生利用的废旧电池破碎分选方法，能够收集废旧电池电解液原液，该原液中不含氯离子，使电解液原液可以直接通过膜处理去除其中的金属阳离子而后直接回用，从而大幅度减少了危险废物的产生，降低了生产成本。
为实现上述目的，本发明提出了一种废电解液可直接再生利用的废旧电池破碎分选方法，包括以下步骤：
步骤S1给料：将需要处理的废旧电池原料置于金属链板式输送设备的输料端；
步骤S2一级破碎：通过步骤S1中的金属链板式输送设备将废旧电池输送至一级锤式破碎机中，通过一级锤式破碎机中的重型合金锤头的高速击打，使废旧电池破碎成一级破碎料；
步骤S3一级分选及废电解液原液回收：一级破碎料落入一级铅膏分选筛，通过高频振动及高压水冲，使铅膏颗粒及废电解液原液通过分选筛间隙为0.6毫米的条隙筛网落入下方的一级搅拌罐中；
步骤S4二级破碎：将通过一级分选后的筛上物通过振动给料机输送到二级破碎机中，通过二级锤式破碎机中的重型合金锤头的高速击打，使废旧电池破碎成二级破碎料；
步骤S5二级分选：将二级破碎料落入二级铅膏分选筛，通过高频振动及高压水冲，使铅膏颗粒及电解液原液通过分选筛间隙为0.6毫米的条隙筛网落入下方的二级搅拌罐中；
步骤S6一二级回收：将筛选中透过筛网落下的铅膏直接落入铅膏分选筛下方的一、二级铅膏搅拌罐，一、二级铅膏搅拌罐的搅拌器对罐体内的废电解液和铅膏混合物进行不断搅拌，直至混合物调整到一定密度；
步骤S7固液分离：将步骤S6搅拌完成后的电解液原液与铅膏的混合物经卧式离心泵输送到压滤机进行固液分离，提取滤液；
步骤S8滤液处理：将步骤S7中经过固液分离的电解液原液输送至滤液搅拌罐中，滤液搅拌罐设有搅拌器，搅拌器对滤液进行不断搅拌，搅拌罐外侧设有酸液泵，通过酸液泵将滤液输送至下一工序；
步骤S9膜过滤：通过步骤S8中的酸液泵将滤液输送至膜过滤设备内，通过膜过滤设备对滤液进行膜过滤，去除滤液中的金属阳离子，去除金属阳离子 后的电解液可以直接回用。
作为优选，所述的步骤S3一级分选及电解液原液回收和步骤S5二级分选中通过高压水洗辅助将分选筛晒面上的铅膏透过筛网落下。
作为优选，所述的步骤S5铅膏搅拌中铅膏搅拌罐内设有液位传感器和称重传感器，通过液位传感器和称重传感器的配合调节混合物的密度，混合物的成品密度为1.80-1.85g/cm 3。
作为优选，所述的步骤S8滤液处理中滤液搅拌罐内设有液位传感器，通过液位传感器的调节，低液位时，滤液搅拌罐内的电解液通过酸液泵为破碎分选提供高压循环水，高液位时，通过酸液泵将电解液输送至下一道工序进行膜过滤。
本发明一种废电解液可直接再生利用的废旧电池破碎分选方法的有益效果：本发明采用物料搅拌收集工艺替代船型刮板机沉淀输送工艺，取消了传统的添絮凝剂加流程，去除废电解液中的阳离子，采用废旧铅酸蓄电池中收集的电解液原液作为整套系统循环水，不使用新水作为分选的介质，收集后的电解液可以直接通过膜处理去除其中的金属阳离子而后直接回用，当电解液原液中含有无法去除的阴离子时，电解液原液无法直接被回用于蓄电池，采用本方法工艺，不使用新鲜水，按照传统使用絮凝剂添加水的工艺会叠加产生含有大量无法直接回用的废电解液，这些废电解液需要进入污水处理站，经过添加碱性添加剂进入综合处理，综合处理后会产生含铅危废，产生量巨大，目前无有效处理手段，因此本发明的提出，大幅度减少了危险废物的产生，降低了生产成本,减少对环境的污染。
本发明的特征及优点将通过实施例结合附图进行详细说明。
【附图说明】
图1是本发明一种废电解液可直接再生利用的废旧电池破碎分选方法流程示意图。
【具体实施方式】
为使本发明的目的、技术方案和优点更加清楚明了，下面通过附图及实施例，对本发明进行进一步详细说明。但是应该理解，此处所描述的具体实施例仅仅用以解释本发明，并不用于限制本发明的范围。此外，在以下说明中，省略了对公知结构和技术的描述，以避免不必要地混淆本发明的概念
实施例一：
本发明一种废电解液可直接再生利用的废旧电池破碎分选方法，包括以下步骤：
步骤S1给料：将需要处理的废旧电池原料置于金属链板式输送设备的输料端；
步骤S2一级破碎：通过步骤S1中的金属链板式输送设备将废旧电池输送至一级锤式破碎机中，通过一级锤式破碎机中的重型合金锤头的高速击打，使废旧电池破碎成一级破碎料；
步骤S3一级分选及废电解液回收：一级破碎料落入一级铅膏分选筛，通过高频振动及高压水冲，使铅膏颗粒及废电解液通过分选筛间隙为0.6毫米的条隙筛网落入下方的一级搅拌罐中；
步骤S4二级破碎：将经过一级分选后的筛上物通过振动给料机输送到二级锤式破碎机中，通过二级锤式破碎机中的重型合金锤头的高速击打，使废旧电池破碎成二级破碎料；
步骤S5二级分选：将二级破碎料落入二级铅膏分选筛，通过高频振动及高压水冲，使铅膏颗粒及废电解液通过分选筛间隙为0.6毫米的条隙筛网落入下方的二级搅拌罐中；
步骤S66一二级回收：将筛选中透过筛网落下的铅膏直接落入铅膏分选筛下方的一、二级铅膏搅拌罐，一、二级铅膏搅拌罐的搅拌器对罐体内的废电解液和铅膏混合物进行不断搅拌，直至混合物调整到一定密度；
步骤S7固液分离：将步骤S6搅拌完成后的废电解液与铅膏的混合物经卧式离心泵输送到压滤机进行固液分离，提取滤液；
步骤S8滤液处理：将步骤S7中经过固液分离的电解液原液输送至滤液搅拌罐中，滤液搅拌罐设有搅拌器，搅拌器对滤液进行不断搅拌，搅拌罐外侧设有酸液泵，通过酸液泵将滤液输送至下一工序；
步骤S9膜过滤：通过步骤S8中的酸液泵将滤液输送至膜过滤设备内，通过膜过滤设备对滤液进行膜过滤，去除滤液中的金属阳离子，去除金属阳离子后的电解液可以直接回用。
所述的步骤S3一级分选及电解液原液回收和步骤S5二级分选中通过高压水洗辅助将分选筛晒面上的铅膏透过筛网落下，所述的步骤S6一二级回收中铅膏搅拌罐内设有液位传感器和称重传感器，通过液位传感器和称重传感器的配合调节混合物的密度，混合物的成品密度为1.80g/cm 3，所述的步骤S8滤液处理中滤液搅拌罐内设有液位传感器，通过液位传感器的调节，低液位时，滤液搅拌罐内的电解液通过酸液泵为破碎分选提供高压循环水，高液位时，通过酸液泵将电解液输送至下一道工序进行膜过滤。
实施例二：
步骤S1给料：将需要处理的废旧电池原料置于金属链板式输送设备的输料端；
步骤S2一级破碎：通过步骤S1中的金属链板式输送设备将废旧电池输送至一级锤式破碎机中，通过一级锤式破碎机中的重型合金锤头的高速击打， 使废旧电池破碎成一级破碎料；
步骤S3一级分选及废电解液回收：一级破碎料落入一级铅膏分选筛，通过高频振动及高压水冲，使铅膏颗粒及废电解液通过分选筛间隙为0.6毫米的条隙筛网落入下方的一级搅拌罐中；
步骤S4二级破碎：将经过一级分选后的筛上物通过振动给料机输送到二级锤式破碎机中，通过二级锤式破碎机中的重型合金锤头的高速击打，使废旧电池破碎成二级破碎料；
步骤S5二级分选：将二级破碎料落入二级铅膏分选筛，通过高频振动及高压水冲，使铅膏颗粒及废电解液通过分选筛间隙为0.6毫米的条隙筛网落入下方的二级搅拌罐中；
步骤S66一二级回收：将筛选中透过筛网落下的铅膏直接落入铅膏分选筛下方的一、二级铅膏搅拌罐，一、二级铅膏搅拌罐的搅拌器对罐体内的废电解液和铅膏混合物进行不断搅拌，直至混合物调整到一定密度；
步骤S7固液分离：将步骤S6搅拌完成后的废电解液与铅膏的混合物经卧式离心泵输送到压滤机进行固液分离，提取滤液；
步骤S8滤液处理：将步骤S7中经过固液分离的电解液原液输送至滤液搅拌罐中，滤液搅拌罐设有搅拌器，搅拌器对滤液进行不断搅拌，搅拌罐外侧设有酸液泵，通过酸液泵将滤液输送至下一工序；
步骤S9膜过滤：通过步骤S8中的酸液泵将滤液输送至膜过滤设备内，通过膜过滤设备对滤液进行膜过滤，去除滤液中的金属阳离子，去除金属阳离子后的电解液可以直接回用。
所述的步骤S3一级分选及电解液原液回收和步骤S5二级分选中通过高压水洗辅助将分选筛晒面上的铅膏透过筛网落下，所述的步骤S6一二级回收中铅膏搅拌罐内设有液位传感器和称重传感器，通过液位传感器和称重传感器的配 合调节混合物的密度，混合物的成品密度为1.85g/cm 3，所述的步骤S8滤液处理中滤液搅拌罐内设有液位传感器，通过液位传感器的调节，低液位时，滤液搅拌罐内的电解液通过酸液泵为破碎分选提供高压循环水，高液位时，通过酸液泵将电解液输送至下一道工序进行膜过滤。
实施例三：
步骤S1给料：将需要处理的废旧电池原料置于金属链板式输送设备的输料端；
步骤S2一级破碎：通过步骤S1中的金属链板式输送设备将废旧电池输送至一级锤式破碎机中，通过一级锤式破碎机中的重型合金锤头的高速击打，使废旧电池破碎成一级破碎料；
步骤S3一级分选及废电解液回收：一级破碎料落入一级铅膏分选筛，通过高频振动及高压水冲，使铅膏颗粒及废电解液通过分选筛间隙为0.6毫米的条隙筛网落入下方的一级搅拌罐中；
步骤S4二级破碎：将经过一级分选后的筛上物通过振动给料机输送到二级锤式破碎机中，通过二级锤式破碎机中的重型合金锤头的高速击打，使废旧电池破碎成二级破碎料；
步骤S5二级分选：将二级破碎料落入二级铅膏分选筛，通过高频振动及高压水冲，使铅膏颗粒及废电解液通过分选筛间隙为0.6毫米的条隙筛网落入下方的二级搅拌罐中；
步骤S66一二级回收：将筛选中透过筛网落下的铅膏直接落入铅膏分选筛下方的一、二级铅膏搅拌罐，一、二级铅膏搅拌罐的搅拌器对罐体内的废电解液和铅膏混合物进行不断搅拌，直至混合物调整到一定密度；
步骤S7固液分离：将步骤S6搅拌完成后的废电解液与铅膏的混合物经卧式离心泵输送到压滤机进行固液分离，提取滤液；
步骤S8滤液处理：将步骤S7中经过固液分离的电解液原液输送至滤液搅拌罐中，滤液搅拌罐设有搅拌器，搅拌器对滤液进行不断搅拌，搅拌罐外侧设有酸液泵，通过酸液泵将滤液输送至下一工序；
步骤S9膜过滤：通过步骤S8中的酸液泵将滤液输送至膜过滤设备内，通过膜过滤设备对滤液进行膜过滤，去除滤液中的金属阳离子，去除金属阳离子后的电解液可以直接回用。
所述的步骤S3一级分选及电解液原液回收和步骤S5二级分选中通过高压水洗辅助将分选筛晒面上的铅膏透过筛网落下，所述的步骤S6一二级回收中铅膏搅拌罐内设有液位传感器和称重传感器，通过液位传感器和称重传感器的配合调节混合物的密度，混合物的成品密度为1.83g/cm 3，所述的步骤S8滤液处理中滤液搅拌罐内设有液位传感器，通过液位传感器的调节，低液位时，滤液搅拌罐内的电解液通过酸液泵为破碎分选提供高压循环水，高液位时，通过酸液泵将电解液输送至下一道工序进行膜过滤。
上述实施例是对本发明的说明，不是对本发明的限定，任何对本发明简单变换后的方案均属于本发明的保护范围。

Claims (4)

  1. 一种废电解液可直接再生利用的废旧电池破碎分选方法，其特征在于：包括以下步骤：
    步骤S1给料：将需要处理的废旧电池原料置于金属链板式输送设备的输料端；
    步骤S2一级破碎：通过步骤S1中的金属链板式输送设备将废旧电池输送至一级锤式破碎机中，通过一级锤式破碎机中的重型合金锤头的高速击打，使废旧电池破碎成一级破碎料；
    步骤S3一级分选及废电解液回收：一级破碎料落入一级铅膏分选筛，通过高频振动及高压水冲，使铅膏颗粒及废电解液通过分选筛间隙为0.6毫米的条隙筛网落入下方的一级搅拌罐中；
    步骤S4二级破碎：将经过一级分选后的筛上物通过振动给料机输送到二级锤式破碎机中，通过二级锤式破碎机中的重型合金锤头的高速击打，使废旧电池破碎成二级破碎料；
    步骤S5二级分选：将二级破碎料落入二级铅膏分选筛，通过高频振动及高压水冲，使铅膏颗粒及废电解液通过分选筛间隙为0.6毫米的条隙筛网落入下方的二级搅拌罐中；
    步骤S6一二级回收：将筛选中透过筛网落下的铅膏直接落入铅膏分选筛下方的一、二级铅膏搅拌罐，一、二级铅膏搅拌罐的搅拌器对罐体内的废电解液和铅膏混合物进行不断搅拌，直至混合物调整到一定密度；
    步骤S7固液分离：将步骤S6搅拌完成后的废电解液与铅膏的混合物经卧式离心泵输送到压滤机进行固液分离，提取滤液；
    步骤S8滤液处理：将步骤S7中经过固液分离的电解液原液输送至滤液搅拌罐中，滤液搅拌罐设有搅拌器，搅拌器对滤液进行不断搅拌，搅拌罐外侧设有酸液泵，通过酸液泵将滤液输送至下一工序；
    步骤S9膜过滤：通过步骤S8中的酸液泵将滤液输送至膜过滤设备内，通过 膜过滤设备对滤液进行膜过滤，去除滤液中的金属阳离子，去除金属阳离子后的电解液可以直接回用。
  2. 如权利要求1所述的一种废电解液可直接再生利用的废旧电池破碎分选方法，其特征在于：步骤S3一级分选及废电解液回收和步骤S5二级分选中通过高压水洗辅助将分选筛晒面上的铅膏透过筛网落下。
  3. 如权利要求1所述的一种废电解液可直接再生利用的废旧电池破碎分选方法，其特征在于：所述的步骤S6一二级回收中铅膏搅拌罐内设有液位传感器和称重传感器，通过液位传感器和称重传感器的配合调节混合物的密度，混合物的成品密度为1.80-1.85g/cm 3。
  4. 如权利要求1所述的一种废电解液可直接再生利用的废旧电池破碎分选方法，其特征在于：所述的步骤S8滤液处理中滤液搅拌罐内设有液位传感器，通过液位传感器的调节，低液位时，滤液搅拌罐内的电解液通过酸液泵为破碎分选提供高压循环水，高液位时，通过酸液泵将电解液输送至下一道工序进行膜过滤。
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