CN201153145Y - Separating and selecting apparatus used after crushing waste lead accumulators - Google Patents
Separating and selecting apparatus used after crushing waste lead accumulators Download PDFInfo
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- CN201153145Y CN201153145Y CNU200720187655XU CN200720187655U CN201153145Y CN 201153145 Y CN201153145 Y CN 201153145Y CN U200720187655X U CNU200720187655X U CN U200720187655XU CN 200720187655 U CN200720187655 U CN 200720187655U CN 201153145 Y CN201153145 Y CN 201153145Y
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- 239000002699 waste material Substances 0.000 title claims abstract description 8
- 239000004033 plastic Substances 0.000 claims abstract description 28
- 229920003023 plastic Polymers 0.000 claims abstract description 28
- 239000004743 Polypropylene Substances 0.000 claims abstract description 16
- -1 polypropylene Polymers 0.000 claims abstract description 16
- 229920001155 polypropylene Polymers 0.000 claims abstract description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 10
- 230000002706 hydrostatic effect Effects 0.000 claims description 12
- 238000000926 separation method Methods 0.000 claims description 6
- 238000003756 stirring Methods 0.000 claims description 4
- 239000012141 concentrate Substances 0.000 claims 2
- 238000002156 mixing Methods 0.000 abstract description 5
- 230000008901 benefit Effects 0.000 abstract description 4
- 239000000463 material Substances 0.000 abstract description 4
- 239000000203 mixture Substances 0.000 abstract description 2
- 238000005192 partition Methods 0.000 description 8
- 239000002253 acid Substances 0.000 description 5
- 230000008719 thickening Effects 0.000 description 4
- 230000018044 dehydration Effects 0.000 description 3
- 238000006297 dehydration reaction Methods 0.000 description 3
- 239000003792 electrolyte Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 238000003723 Smelting Methods 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000012634 fragment Substances 0.000 description 2
- 229910001385 heavy metal Inorganic materials 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000010926 waste battery Substances 0.000 description 2
- 229920001875 Ebonite Polymers 0.000 description 1
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000012065 filter cake Substances 0.000 description 1
- 239000003673 groundwater Substances 0.000 description 1
- 238000003895 groundwater pollution Methods 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 238000011085 pressure filtration Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 238000003900 soil pollution Methods 0.000 description 1
- 239000002910 solid waste Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
-
- 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
Landscapes
- Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
Abstract
Description
技术领域 technical field
本实用新型属于有色金属冶炼行业的废旧铅蓄电池综合回收技术领域,尤其涉及一种将分离粉碎后的铅蓄电池各成分进行分离分选的废旧铅蓄电池粉碎后的分离分选装置。The utility model belongs to the technical field of comprehensive recycling of waste lead storage batteries in the non-ferrous metal smelting industry, in particular to a separation and sorting device for separating and sorting the components of the separated and crushed lead storage batteries after crushing.
背景技术 Background technique
随着汽车行业和电子产业的飞速发展,电池成为该行业产品中的重要组成部分,电池在给人们工作和生活带来便利的同时,也带来了污染隐患,用完后的废旧电池中含有大量重金属和电解液,废旧电池无论是深埋还是裸漏堆放,重金属和电解液都会溢出,造成地下水和土壤的污染,会严重危害人类健康。铅蓄电池是目前世界上产量和用途最广的一种电池,销售额占全球电池销售额的30%以上。目前从国内总体水平看,再生铅生产规模小、能耗高、工业技术落后,采用比较落后的工艺回收铅蓄电池,人工或采用简单的机械装置将废旧蓄电池进行解剖,电解液随处倾倒,将塑料外壳和隔板等固体废物就地堆放,取出铅栅和隔板分离后,铅膏和铅栅没有分离直接进反射炉里熔炼,环境污染严重,再加上工艺技术装备水平低,金属的回收和利用程度低。国际上比较先进的CX集成系统处理废旧铅蓄电池方法,整体系统投资较大,同等质量要求下的国产设备价格是进口的一半左右。With the rapid development of the automobile industry and the electronics industry, batteries have become an important part of the products in this industry. While batteries bring convenience to people's work and life, they also bring hidden dangers of pollution. Waste batteries after use contain A large amount of heavy metals and electrolytes, whether the used batteries are buried deep or stacked with bare drains, heavy metals and electrolytes will overflow, causing groundwater and soil pollution, which will seriously endanger human health. Lead storage battery is currently the most widely produced and used battery in the world, and its sales account for more than 30% of global battery sales. At present, from the perspective of the overall domestic level, the production scale of recycled lead is small, the energy consumption is high, and the industrial technology is backward. The relatively backward technology is used to recycle lead batteries, and the waste batteries are dissected manually or by simple mechanical devices. The electrolyte is dumped everywhere, and the plastic Solid waste such as casings and partitions are piled up on the spot. After the lead grid is taken out and separated from the partition, the lead paste and the lead grid are not separated and are directly melted in the reverberatory furnace. and low utilization. The relatively advanced CX integrated system in the world to deal with waste lead-acid batteries requires a large overall system investment, and the price of domestic equipment with the same quality requirements is about half of that of imported equipment.
发明内容 Contents of the invention
本实用新型的目的在于克服现有技术中存在的不足而提供一种利用CX集成系统处理废旧铅蓄电池,同时利用国产过滤机等设备,将蓄电池破碎后的不同碎料根据其物理性质的差异进行逐步清洗分离,达到每种成分都分离分选出来,以利于进行下一步分别处理的废旧铅蓄电池粉碎后的分离分选装置。The purpose of this utility model is to overcome the deficiencies in the prior art and provide a method of using the CX integrated system to process waste lead-acid batteries. Clean and separate step by step to achieve separation and sorting of each component to facilitate the separation and sorting device after the crushed waste lead-acid batteries are processed separately in the next step.
本实用新型的技术方案是这样实现的:包括带有进料口的铅泥振动筛,其特征在于:The technical scheme of the utility model is achieved in that it comprises a lead mud vibrating screen with a feed port, and is characterized in that:
在铅泥振动筛中设置有第一水力循环泵,铅泥振动筛的振动筛网下部通过铅泥浓缩传输器与铅泥搅拌槽接通,铅泥搅拌槽通过铅泥输送泵与压滤机接通;The first hydraulic circulation pump is installed in the lead mud vibrating screen, the lower part of the vibrating screen of the lead mud vibrating screen is connected to the lead mud mixing tank through the lead mud concentration conveyor, and the lead mud mixing tank is connected to the filter press through the lead mud delivery pump. connected;
铅泥振动筛的振动筛网上部的排料口通过管道与第一水力分离器相接通;第一水力分离器的上部由聚丙烯螺旋输送器与聚丙烯堆放区接通;第一水力分离器的中部排出口通过管道与塑料脱水筛接通,塑料脱水筛的排料口与静水分离器接通,静水分离器的下部通过重塑料和隔板螺旋输送器与重塑料和隔板堆放区接通;静水分离器的上部通过重塑料和隔板小螺旋输送器与聚丙烯螺旋输送器接通;第一水力分离器的下部通过铅栅浓缩螺旋输送机与第二水力分离器接通;The discharge opening on the upper part of the vibrating screen of the lead mud vibrating screen is connected to the first hydraulic separator through a pipeline; the upper part of the first hydraulic separator is connected to the polypropylene stacking area by a polypropylene screw conveyor; the first hydraulic separator The discharge port in the middle of the device is connected to the plastic dewatering screen through the pipeline, the discharge port of the plastic dewatering screen is connected to the hydrostatic separator, and the lower part of the hydrostatic separator is connected to the heavy plastic and partition stacking area through the heavy plastic and clapboard screw conveyor. Connected; the upper part of the hydrostatic separator is connected to the polypropylene screw conveyor through the heavy plastic and partition small screw conveyor; the lower part of the first hydraulic separator is connected to the second hydraulic separator through the lead grid thickening screw conveyor;
第二水力分离器下部通过第二水力循环泵输送的循环水和压缩空气搅拌,并且通过铅栅螺旋输送器与输送铅栅堆放区接通;第二水力分离器上面的溢流口与塑料脱水筛接通。The lower part of the second hydraulic separator is stirred by the circulating water and compressed air delivered by the second hydraulic circulating pump, and is connected to the lead grid storage area through the lead grid screw conveyor; the overflow port on the second hydraulic separator is connected with the plastic dehydration The sieve is switched on.
本实用新型的优点在于:The utility model has the advantages of:
1、将破碎后铅蓄电池混合物充分清洗分离,使铅栅、铅膏、聚丙烯外壳及隔板等可以分别作为原料再利用,节省资源;1. Fully clean and separate the crushed lead-acid battery mixture, so that the lead grid, lead paste, polypropylene shell and separator can be reused as raw materials to save resources;
2、对环境没有污染,具有良好的环境效益;2. No pollution to the environment and good environmental benefits;
3、本装置中,各个分离装置之间结构紧凑、合理,节约使用场地,实现了集约化生产;3. In this device, the structure of each separation device is compact and reasonable, which saves the use of space and realizes intensive production;
4、本装置中充分利用国产设备的优势,采取国产设备与进口设备相结合的方式,既满足系统的要求,又节约了资金;4. This device makes full use of the advantages of domestic equipment and adopts the combination of domestic equipment and imported equipment, which not only meets the requirements of the system, but also saves money;
附图说明 Description of drawings
图1是破碎后分离分选装置的示意图。Figure 1 is a schematic diagram of a separation and sorting device after crushing.
具体实施方式 Detailed ways
如图1所示,本实用新型包括带有进料口的铅泥振动筛1,其特征在于:在铅泥振动筛1中设置有第一水力循环泵14,铅泥振动筛1的振动筛网下部通过铅泥浓缩传输器9与铅泥搅拌槽10接通,铅泥搅拌槽10通过铅泥输送泵11与压滤机12接通;As shown in Figure 1, the utility model comprises the lead mud vibrating screen 1 that has feed inlet, is characterized in that: in lead mud vibrating screen 1, be provided with the first hydraulic circulation pump 14, the vibrating screen of lead mud vibrating screen 1 The lower part of the net is connected with the lead mud mixing tank 10 through the lead mud thickening conveyor 9, and the lead mud stirring tank 10 is connected with the filter press 12 through the lead mud delivery pump 11;
铅泥振动筛1的振动筛网上部的排料口通过管道与第一水力分离器2相接通;第一水力分离器2的上部由聚丙烯螺旋输送器5与聚丙烯堆放区接通;第一水力分离器2的中部排出口通过管道与塑料脱水筛7接通,塑料脱水筛7的排料口与静水分离器6接通,静水分离器6的下部通过重塑料和隔板螺旋输送器8与重塑料和隔板堆放区接通;静水分离器6的上部通过重塑料和隔板小螺旋输送器13与聚丙烯螺旋输送器5接通;第一水力分离器2的下部通过铅栅浓缩螺旋输送机3与第二水力分离器16接通;The discharge opening on the upper part of the vibrating screen of the lead mud vibrating screen 1 is connected with the first hydraulic separator 2 through a pipeline; the upper part of the first hydraulic separator 2 is connected with the polypropylene stacking area by a polypropylene screw conveyor 5; The middle outlet of the first hydroseparator 2 is connected to the plastic dewatering screen 7 through a pipeline, and the discharge port of the plastic dewatering screen 7 is connected to the hydrostatic separator 6, and the lower part of the hydrostatic separator 6 is conveyed by a screw through heavy plastic and a separator The device 8 is connected to the heavy plastic and partition stacking area; the upper part of the hydrostatic separator 6 is connected to the polypropylene screw conveyor 5 through the heavy plastic and partition small screw conveyor 13; the lower part of the first hydraulic separator 2 is connected to the lead The grid thickening screw conveyor 3 is connected with the second hydraulic separator 16;
第二水力分离器16下部通过第二水力循环泵15输送的循环水和压缩空气搅拌,并且通过铅栅螺旋输送器4与输送铅栅堆放区接通;第二水力分离器16上面的溢流口与塑料脱水筛7接通。The circulating water and the compressed air that the second hydraulic separator 16 bottom is conveyed by the second hydraulic circulation pump 15 are stirred, and are connected with the delivery lead grid stacking area by the lead grid screw conveyor 4; the overflow on the second hydraulic separator 16 Port is connected with plastic dewatering screen 7.
废旧带壳铅蓄电池在破碎机中粉碎成粒度不大于80毫米的碎料首先进入铅泥振动筛1中,在铅泥振动筛振动力及高压循环水喷头的喷射力作用下,铅泥通过振动筛网成为筛下物,经铅膏浓缩输送器9输送至铅泥搅拌槽10中,然后经铅泥浓浆泵11送往压滤机12中压滤,滤饼是含很少量水分的铅泥,送至底吹炉熔炼系统处理。筛上物随铅泥振动筛1的振动从排料口落入第一水力分离器2中,在第一循环泵14的供水压力及压缩空气的作用下,利用粉碎后的物料本身的密度等物理性质的差别,密度大的金属铅栅颗粒及铅棒等沉入第一水力分离器2的下部,由铅栅浓缩螺旋输送机3连续的洗涤并输送至第二水力分离器16的上部,在第二水力分离器16的下部用第二水力循环泵15输送的循环水和压缩空气搅拌,铅栅和铅极棒沉入下部,被铅栅螺旋输送器4输送铅栅堆放区;混入铅栅中的重塑料和隔板等稍轻的碎料在搅拌力的作用下浮在第二水力分离器16的上面,从溢流口溢流至塑料塑料脱水筛7中;在第一水力分离器中密度较大的硬橡胶和隔板之类的有机物滞留在第一水力分离器2的中部,在第一水力分离器2的中部排出口随循环水流进塑料脱水筛7中;进入塑料脱水筛7中的碎料在塑料脱水筛7里振动脱去水及混入的铅泥后,从排料口落入静水分离器6中,在静水分离器6中进行洗涤分离,其中的硬橡胶和隔板沉入到下部的螺旋输送器8中输送至重塑料和隔板堆放区;随重塑料和隔板一起带出的聚丙烯碎料浮在静水分离器的上部由小螺旋输送器13输送至聚丙烯螺旋输送器5中;在第一水力分离器中密度比较轻的碎料聚丙烯在水流及气流的作用下上浮到第一水力分离器2的上部,由聚丙烯螺旋输送器5连续的洗涤并输送至聚丙烯堆放区。Waste shelled lead-acid batteries are crushed in the crusher into fragments with a particle size of no more than 80 mm and first enter the lead mud vibrating screen 1. The sieve becomes the underscreen, which is transported to the lead mud mixing tank 10 through the lead paste concentration conveyor 9, and then sent to the filter press 12 for pressure filtration through the lead mud thick slurry pump 11, and the filter cake contains a small amount of water. Lead slime is sent to the bottom blowing furnace smelting system for processing. The oversize material falls into the first hydraulic separator 2 from the discharge port with the vibration of the lead mud vibrating screen 1, and under the action of the water supply pressure of the first circulation pump 14 and compressed air, the crushed material itself is used for density etc. Due to the difference in physical properties, dense metal lead grid particles and lead rods, etc. sink into the lower part of the first hydraulic separator 2, and are continuously washed by the lead grid thickening screw conveyor 3 and transported to the upper part of the second hydraulic separator 16. Stir with circulating water and compressed air delivered by the second hydraulic circulating pump 15 at the bottom of the second hydraulic separator 16, the lead grid and the lead pole sink into the lower part, and are transported to the lead grid stacking area by the lead grid screw conveyor 4; mixed with lead Heavy plastics in the grid and slightly lighter fragments such as clapboards float on the top of the second hydraulic separator 16 under the effect of stirring force, and overflow into the plastic dewatering screen 7 from the overflow port; Organic substances such as hard rubber and clapboards with medium density stay in the middle of the first hydraulic separator 2, and flow into the plastic dehydration screen 7 along with the circulating water at the discharge outlet in the middle of the first hydraulic separator 2; enter the plastic dehydration screen After the scraps in 7 are vibrated in the plastic dewatering screen 7 to remove water and mixed lead mud, they fall into the hydrostatic separator 6 from the discharge port, and are washed and separated in the hydrostatic separator 6. The board sinks into the lower part of the screw conveyor 8 and is transported to the heavy plastic and partition stacking area; the polypropylene scraps brought out together with the heavy plastic and the partition float on the upper part of the hydrostatic separator and are transported to the storage area by the small screw conveyor 13 In the polypropylene screw conveyor 5; in the first hydraulic separator, the crushed polypropylene with a relatively light density floats to the upper part of the first hydraulic separator 2 under the action of water flow and air flow, and is continuously transported by the polypropylene screw conveyor 5 Wash and transport to polypropylene dump.
Claims (1)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU200720187655XU CN201153145Y (en) | 2007-12-27 | 2007-12-27 | Separating and selecting apparatus used after crushing waste lead accumulators |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU200720187655XU CN201153145Y (en) | 2007-12-27 | 2007-12-27 | Separating and selecting apparatus used after crushing waste lead accumulators |
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| CN201153145Y true CN201153145Y (en) | 2008-11-19 |
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| CNU200720187655XU Expired - Fee Related CN201153145Y (en) | 2007-12-27 | 2007-12-27 | Separating and selecting apparatus used after crushing waste lead accumulators |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102148414A (en) * | 2011-03-07 | 2011-08-10 | 尚诚德 | Energy-saving and environment-friendly automatic disassembly and separation system for waste batteries |
| CN104014414A (en) * | 2014-05-23 | 2014-09-03 | 株洲金鼎高端装备有限公司 | Secondary sorting method for waste lead-acid battery broken materials |
| CN105080699A (en) * | 2014-05-22 | 2015-11-25 | 株洲鼎端装备股份有限公司 | Wet classifier |
| CN105742745A (en) * | 2016-03-22 | 2016-07-06 | 安徽华铂再生资源科技有限公司 | Shell-crushing and energy-saving cleaning technology for waste lead-acid storage battery |
| CN105846005A (en) * | 2016-03-22 | 2016-08-10 | 安徽华铂再生资源科技有限公司 | Waste lead-acid storage battery crushing-and-separation one-step energy-saving recycling process |
| CN108832218A (en) * | 2018-06-27 | 2018-11-16 | 湘潭大学 | Method and device for fluidized separation of lead paste |
| CN109225556A (en) * | 2018-08-24 | 2019-01-18 | 江苏华宏科技股份有限公司 | A kind of waste lithium cell graded crushing equipment and technique |
-
2007
- 2007-12-27 CN CNU200720187655XU patent/CN201153145Y/en not_active Expired - Fee Related
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102148414A (en) * | 2011-03-07 | 2011-08-10 | 尚诚德 | Energy-saving and environment-friendly automatic disassembly and separation system for waste batteries |
| CN102148414B (en) * | 2011-03-07 | 2013-01-02 | 尚诚德 | Energy-saving and environment-friendly automatic disassembly and separation system for waste batteries |
| CN105080699A (en) * | 2014-05-22 | 2015-11-25 | 株洲鼎端装备股份有限公司 | Wet classifier |
| CN104014414A (en) * | 2014-05-23 | 2014-09-03 | 株洲金鼎高端装备有限公司 | Secondary sorting method for waste lead-acid battery broken materials |
| CN105742745A (en) * | 2016-03-22 | 2016-07-06 | 安徽华铂再生资源科技有限公司 | Shell-crushing and energy-saving cleaning technology for waste lead-acid storage battery |
| CN105846005A (en) * | 2016-03-22 | 2016-08-10 | 安徽华铂再生资源科技有限公司 | Waste lead-acid storage battery crushing-and-separation one-step energy-saving recycling process |
| CN105742745B (en) * | 2016-03-22 | 2018-11-13 | 安徽华铂再生资源科技有限公司 | Waste and old lead acid accumulator is crushed the energy saving cleaning of shell |
| CN108832218A (en) * | 2018-06-27 | 2018-11-16 | 湘潭大学 | Method and device for fluidized separation of lead paste |
| CN109225556A (en) * | 2018-08-24 | 2019-01-18 | 江苏华宏科技股份有限公司 | A kind of waste lithium cell graded crushing equipment and technique |
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