CN114733870A - Metal recovery system and metal recovery method using same - Google Patents
Metal recovery system and metal recovery method using same Download PDFInfo
- Publication number
- CN114733870A CN114733870A CN202011587364.6A CN202011587364A CN114733870A CN 114733870 A CN114733870 A CN 114733870A CN 202011587364 A CN202011587364 A CN 202011587364A CN 114733870 A CN114733870 A CN 114733870A
- Authority
- CN
- China
- Prior art keywords
- metal
- colloid
- unit
- metal recovery
- recovery system
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 229910052751 metal Inorganic materials 0.000 title claims abstract description 167
- 239000002184 metal Substances 0.000 title claims abstract description 167
- 238000011084 recovery Methods 0.000 title claims abstract description 56
- 238000000034 method Methods 0.000 title claims abstract description 21
- 239000000084 colloidal system Substances 0.000 claims abstract description 99
- 239000002826 coolant Substances 0.000 claims abstract description 59
- 238000007654 immersion Methods 0.000 claims abstract description 4
- 238000001802 infusion Methods 0.000 claims description 14
- 238000004891 communication Methods 0.000 claims description 8
- 230000001537 neural effect Effects 0.000 claims description 8
- 230000005484 gravity Effects 0.000 claims description 6
- 238000007781 pre-processing Methods 0.000 claims description 5
- 239000012530 fluid Substances 0.000 claims description 3
- 238000002203 pretreatment Methods 0.000 claims 1
- 238000002791 soaking Methods 0.000 abstract description 31
- 238000007599 discharging Methods 0.000 abstract description 8
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 32
- 229910052802 copper Inorganic materials 0.000 description 32
- 239000010949 copper Substances 0.000 description 32
- 239000003292 glue Substances 0.000 description 25
- 239000010426 asphalt Substances 0.000 description 22
- 238000000926 separation method Methods 0.000 description 16
- 239000007788 liquid Substances 0.000 description 14
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 10
- 150000002739 metals Chemical class 0.000 description 9
- 239000002699 waste material Substances 0.000 description 8
- 238000010586 diagram Methods 0.000 description 7
- 238000004064 recycling Methods 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 238000007667 floating Methods 0.000 description 5
- 230000009477 glass transition Effects 0.000 description 5
- 229910052757 nitrogen Inorganic materials 0.000 description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- 238000003860 storage Methods 0.000 description 4
- 238000003723 Smelting Methods 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 229910052500 inorganic mineral Inorganic materials 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 230000007246 mechanism Effects 0.000 description 2
- 239000011707 mineral Substances 0.000 description 2
- 238000006467 substitution reaction Methods 0.000 description 2
- 230000007306 turnover Effects 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- 238000004378 air conditioning Methods 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 239000010791 domestic waste Substances 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 1
- 229910052737 gold Inorganic materials 0.000 description 1
- 239000010931 gold Substances 0.000 description 1
- 239000012943 hotmelt Substances 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 238000009991 scouring Methods 0.000 description 1
- 239000003923 scrap metal Substances 0.000 description 1
- 238000007790 scraping Methods 0.000 description 1
- 239000000741 silica gel Substances 0.000 description 1
- 229910002027 silica gel Inorganic materials 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 229910052709 silver Inorganic materials 0.000 description 1
- 239000004332 silver Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C4/00—Crushing or disintegrating by roller mills
- B02C4/02—Crushing or disintegrating by roller mills with two or more rollers
- B02C4/08—Crushing or disintegrating by roller mills with two or more rollers with co-operating corrugated or toothed crushing-rollers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B5/00—Operations not covered by a single other subclass or by a single other group in this subclass
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C2201/00—Codes relating to disintegrating devices adapted for specific materials
- B02C2201/06—Codes relating to disintegrating devices adapted for specific materials for garbage, waste or sewage
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Landscapes
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Food Science & Technology (AREA)
- Processing Of Solid Wastes (AREA)
- Manufacture And Refinement Of Metals (AREA)
Abstract
Description
技术领域technical field
本发明涉及一种金属回收系统及利用其的金属回收方法,更具体而言,本发明涉及用于处理包覆有胶体的金属的一种金属回收系统以及利用其的金属回收方法。The present invention relates to a metal recovery system and a metal recovery method utilizing the same, and more particularly, the present invention relates to a metal recovery system for processing colloid-coated metals and a metal recovery method utilizing the same.
背景技术Background technique
随着经济发展,中国台湾的金属消费量与日俱增,但因金属矿产资源的匮乏,中国台湾的金属来源多仰赖进口,而且金属冶炼过程会产生废气、废水、废渣污染而对生态环境造成压力。因此为稳定金属矿产等原生物料来源以确保经济发展以及减少金属冶炼过程中产生的废弃物以落实环境保护,加强由废金属回收再生金属有其不容忽视的重要性。With economic development, the consumption of metals in Taiwan, China is increasing day by day. However, due to the lack of metal mineral resources, Taiwan's metal sources are mostly imported, and the metal smelting process will produce waste gas, waste water, and waste residue pollution, which will put pressure on the ecological environment. Therefore, in order to stabilize the source of raw materials such as metal minerals to ensure economic development and reduce the waste generated in the metal smelting process to implement environmental protection, it is of great importance to strengthen the recycling of recycled metals from scrap metals.
根据环保数统计,2008年中国台湾回收了147万台一般废家电以及278万件废资讯物品。一般废家电包括电视机、洗衣机、电冰箱、冷暖气机与电风扇,而废资讯物品包括笔记型电脑、主机板、监视器、打印机、手机、键盘等。这些废家电以及废资讯物品中包括了许多可回收利用的金属,例如铜、铅、铝、铁等。According to the statistics of environmental protection statistics, in 2008, Taiwan recycled 1.47 million general waste household appliances and 2.78 million waste information items. General waste household appliances include televisions, washing machines, refrigerators, air conditioners and electric fans, while waste information items include notebook computers, motherboards, monitors, printers, mobile phones, keyboards, etc. These waste household appliances and waste information items include many recyclable metals, such as copper, lead, aluminum, iron, etc.
国内废弃冷气中的铜管被沥青胶包覆。沥青胶具有高黏度特性,因此无法轻易将铜管与沥青胶分离,进而造成了铜管回收上的困难。Copper pipes in domestic waste air-conditioning are covered with asphalt glue. Asphalt glue has high viscosity characteristics, so copper pipes cannot be easily separated from asphalt glue, which makes copper pipe recycling difficult.
目前工业界回收其上包覆有沥青胶的铜管的作法是以人工方式进行刮除。采取人工刮除的方式除了费工耗时以外,还无法将铜管上的沥青胶完整去除,具有高回收成本且回收的铜金属品质不佳等问题,因此仍有很大的改善空间。The current practice in the industry to recycle the copper pipes covered with asphalt glue is to scrape them off manually. In addition to being labor-intensive and time-consuming, the manual scraping method cannot completely remove the asphalt glue on the copper pipes, which has problems such as high recovery costs and poor quality of recovered copper metal, so there is still a lot of room for improvement.
发明内容SUMMARY OF THE INVENTION
本发明的一目的在于使胶体与金属分离并分别回收。An object of the present invention is to separate and recover colloids and metals separately.
本发明提供一种金属回收系统,其包括浸泡室、破碎单元以及分选单元,其中浸泡室具有第一进料口以及置于其内部空间中的冷却剂,破碎单元具有第三进料口以及第二出料口,且分选单元相应于第二出料口设置。包覆有胶体的金属被置于与移动单元连接的进料槽中以在浸泡室以及破碎单元之间移动并进出浸泡室的冷却剂以使上述胶体硬化或玻璃化。The present invention provides a metal recovery system comprising a soaking chamber, a crushing unit and a sorting unit, wherein the soaking chamber has a first feeding port and a coolant placed in its inner space, and the crushing unit has a third feeding port and The second discharge port, and the sorting unit is arranged corresponding to the second discharge port. The colloid-coated metal is placed in a feed trough connected to a moving unit to move between the soaking chamber and the crushing unit and into and out of the soaking chamber's coolant to harden or vitrify the colloid.
在一实施例中,金属回收系统进一步包括集料槽。集料槽具有第二进料口以及与第三进料口相连的第一出料口,进料槽通过移动单元在浸泡室的第一开口以及集料槽的第二进料口之间移动。In one embodiment, the metal recovery system further includes a sump. The collecting trough has a second feeding port and a first discharging port connected with the third feeding port, and the feeding trough is moved between the first opening of the soaking chamber and the second feeding port of the collecting trough through the moving unit .
在一实施例中,移动单元可包括:中空旋转平台;与中空旋转平台以及进料槽连接的转动装置;设置于中空旋转平台的空心处的移动单元本体;设置于移动单元本体上的升降装置;连接中空旋转平台以及升降装置的连接件;以及与中空旋转平台、升降装置以及转动装置连接以控制中空旋转平台、升降装置以及转动装置的移动控制模块。In one embodiment, the mobile unit may include: a hollow rotating platform; a rotating device connected with the hollow rotating platform and the feeding chute; a mobile unit body disposed at the hollow of the hollow rotating platform; a lifting device disposed on the mobile unit body ; a connector connecting the hollow rotating platform and the lifting device; and a movement control module connected with the hollow rotating platform, the lifting device and the rotating device to control the hollow rotating platform, the lifting device and the rotating device.
在一实施例中,金属回收系统可进一步包括与浸泡室流体连通的冷却剂输入管道。In one embodiment, the metal recovery system may further include a coolant input conduit in fluid communication with the soaking chamber.
在一实施例中,其中破碎单元可包括机械力破碎装置。In an embodiment, wherein the crushing unit may comprise a mechanical crushing device.
在一实施例中,分选单元可包括比重分选装置、尺寸分选装置、重量分选装置、或其任意组合。In one embodiment, the sorting unit may include a specific gravity sorting device, a size sorting device, a gravimetric sorting device, or any combination thereof.
在一实施例中,金属回收系统可进一步包括预处理单元,预处理单元在包覆有胶体的金属被置于进料槽之前对包覆有胶体的金属进行分类。In one embodiment, the metal recovery system may further include a pretreatment unit that classifies the colloid-coated metal before the colloid-coated metal is placed in the feed chute.
在一实施例中,预处理单元可包括感测模块以及分析模块,其中分析模块依据感测模块提供的数据进行类神经网络运算。In one embodiment, the preprocessing unit may include a sensing module and an analysis module, wherein the analysis module performs a neural network-like operation according to the data provided by the sensing module.
在一实施例中,类神经网络运算包括AlexNet、VGGNet或ResNet。In one embodiment, the neural network-like operation includes AlexNet, VGGNet, or ResNet.
本发明的另一目的在于提供利用上述金属回收系统的一种金属回收方法,其包括以下步骤:将包覆有胶体的金属置于冷却剂中以玻璃化上述胶体;将包覆有上述玻璃化胶体的金属移至破碎单元以对上述玻璃化胶体进行破碎;以及于分选单元中分离破碎的玻璃化胶体以及金属。Another object of the present invention is to provide a metal recovery method utilizing the above-mentioned metal recovery system, which comprises the following steps: placing the colloid-coated metal in a coolant to vitrify the above-mentioned colloid; The colloidal metal is moved to the crushing unit to crush the vitrified colloid; and the crushed vitrified colloid and the metal are separated in the sorting unit.
在一实施例中,金属回收方法可进一步包括在将包覆有胶体的金属置于冷却剂以前,于预处理单元中对包覆有胶体的金属进行分类。In one embodiment, the metal recovery method may further include sorting the colloid-coated metal in a pretreatment unit prior to placing the colloid-coated metal in the coolant.
本发明可达到利用金属上的胶体特性,以温度低于胶体的玻璃转化温度的冷却剂先将胶体硬化或玻璃化后对硬化或玻璃化的胶体进行破碎以达到完整分开胶体与金属,进而提升金属的回收品质。The present invention can utilize the colloid properties on the metal to first harden or vitrify the colloid with a coolant whose temperature is lower than the glass transition temperature of the colloid, and then break the hardened or vitrified colloid to achieve complete separation of the colloid and the metal, thereby improving the Recycling quality of metals.
附图说明Description of drawings
可参考以下附图来描述本发明,其中:The present invention may be described with reference to the following figures, in which:
图1为本发明一实施例的金属回收系统的流程示意图;1 is a schematic flow diagram of a metal recovery system according to an embodiment of the present invention;
图2为本发明一实施例的金属回收系统的示意图;2 is a schematic diagram of a metal recovery system according to an embodiment of the present invention;
图3为本发明一实施例的金属回收系统中与进料槽连接的移动单元的示意图;3 is a schematic diagram of a mobile unit connected to a feed chute in a metal recovery system according to an embodiment of the present invention;
图4为本发明一实施例的分选单元的示意图;4 is a schematic diagram of a sorting unit according to an embodiment of the present invention;
图5为本发明一实施例的金属回收方法的流程图。FIG. 5 is a flow chart of a metal recovery method according to an embodiment of the present invention.
符号说明Symbol Description
10:金属回收系统10: Metal recycling system
20:金属回收方法20: Metal Recovery Methods
3:金属或金属管3: Metal or Metal Tube
5:胶体5: Colloid
11:浸泡室11: Immersion Chamber
111:第一进料口111: The first feeding port
113:内部空间113: Interior Space
115:冷却剂115: Coolant
12:分选单元12: Sorting unit
120:分选单元本体120: sorting unit body
121:分离控制装置121: Separation control device
1211:第二步进马达1211: Second stepper motor
1213:转轴1213: Spindle
123:胶体分离装置123: Colloid separation device
125:金属收集装置125: Metal Collection Device
1251:向上开口1251: Opening up
127:液体127: Liquid
13::集料槽13:: Aggregate chute
131:第二进料口131: The second feed port
133:第一出料口133: The first discharge port
14A:冷却剂储存槽14A: Coolant Storage Tank
14B:冷却剂回收槽14B: Coolant recovery tank
141:冷却剂进入管道141: Coolant enters the pipe
142:冷却剂排出管道142: Coolant discharge pipe
143,144:控制阀143, 144: Control valve
15:移动单元15: Mobile Unit
151:移动单元本体151: Mobile unit body
153:中空旋转平台153: Hollow Rotary Platform
155:升降装置155: Lifting device
1551:主动轮1551: Drive Wheel
1552:从动轮1552: driven wheel
1553:链条1553: Chain
157:转动装置157: Turning device
1571:步进马达1571: Stepper Motor
1573:第一连接件1573: First connector
159:第二连接件159: Second connector
17:进料槽17: Feed chute
19:破碎单元19: Crushing unit
191:第三进料口191: The third feed port
193:第二出料口193: The second outlet
S200,S201,S203,S205:步骤S200, S201, S203, S205: Steps
具体实施方式Detailed ways
将省略可能不必要地混淆本发明目的的已知功能和构造的描述。Descriptions of known functions and constructions that may unnecessarily obscure the objects of the present invention will be omitted.
将进一步理解的是,当在本说明书中使用“包括”及/或“包括”时,其特指所述特征部件、整数、步骤、操作、元件、组分、及/或其群组的存在,但不排除存在或增加一个或多个其他特征部件、整数、步骤、操作、元件、组分、及/或其群组。当在本说明书中使用单数形式“一”时,除非上下文另外明确指出,否则也意图使其包括多个形式。It will be further understood that when "comprising" and/or "comprising" is used in this specification, it refers specifically to the presence of said features, integers, steps, operations, elements, components, and/or groups thereof , but does not preclude the presence or addition of one or more other features, integers, steps, operations, elements, components, and/or groups thereof. When the singular form "a" is used in this specification, it is also intended to include the plural unless the context clearly dictates otherwise.
将理解的是,虽然本文中可使用术语“第一”、“第二”等来描述各种元件、组件、区域、层及/或部分,但是这些元件、组件、区域、层及/或部分不应受到此些术语的限制。此些术语仅用于区分一个元件、组件、区域、层或部分与另一元件、组件、区域、层或部分。It will be understood that although the terms "first", "second", etc. may be used herein to describe various elements, components, regions, layers and/or sections, these elements, components, regions, layers and/or sections You should not be limited by these terms. These terms are only used to distinguish one element, component, region, layer or section from another element, component, region, layer or section.
图1为根据本发明一实施例的金属回收系统的流程示意图。本发明是利用胶体于玻璃转化温度硬化以及玻璃化的特性所设计的金属回收系统10。如图1所示,包覆有胶体的金属或金属管3可先经过预处理单元分类,接着依照分类被置于进料槽17中以进出浸泡室11,进浸泡室11中装有冷却剂以使胶体5硬化或玻璃化,其上包覆有硬化或玻璃化胶体5的金属或金属管3接着被移至集料槽13,然后依序经过破碎单元19以及分选单元12的处理以分离金属或金属管3以及胶体5。在一实施例中,预处理单元可被省略,包覆有胶体的金属或金属管3可不经过预处理单元分类地直接置于进料槽17中并接着进行后续步骤。FIG. 1 is a schematic flowchart of a metal recovery system according to an embodiment of the present invention. The present invention is a
图2为根据本发明一实施例的金属回收系统10的示意图。本发明的一实施例是关于一种金属回收系统10,其包括:浸泡室11、集料槽13、移动单元15、进料槽17、破碎单元19、以及分选单元12。浸泡室11具有第一进料口111以及置于浸泡室11的内部空间113中的冷却剂115。本发明的金属回收系统10用于处理其上包覆有胶体5的金属或金属管3。具体而言,金属回收系统10用于将其上包覆有胶体5的金属或金属管3的胶体5与金属或金属管3分开以回收金属或金属管3。胶体5的实施例可包括但不限于沥青胶、压克力胶、热熔胶、硅胶(硅利康)、或其任意组合。金属或金属管3的材料可包括例如铜、铝、黄金、银、铁、上述金属的合金或其任意组合,但不限于此。在一实施例中,胶体5可为沥青胶,而金属或金属管3可为铜或铜管。FIG. 2 is a schematic diagram of a
浸泡室11中的冷却剂115是根据胶体5的玻璃转化温度来决定。冷却剂115的实施例无具体限制,可采用任何具有使胶体5硬化或玻璃化的温度的冷却剂。冷却剂的实施例可包括但不限于液态氮、液态空气或其组合。冷却剂115的温度可≤-60℃、≤-65℃、≤-70℃、≤-75℃、≤-80℃、≤-85℃、≤-90℃、≤-95℃、≤-100℃、≤-105℃、≤-110℃、≤-115℃、≤-120℃、≤-125℃、≤-130℃、≤-135℃、≤-140℃、≤-145℃、≤-150℃、≤-155℃、或≤-160℃。在一实施例中,金属回收系统10可进一步包括与浸泡室11连通的冷却剂储存槽14A,浸泡室11的内部空间113通过冷却剂进入管道141与冷却剂储存槽14A连通,冷却剂115可通过冷却剂管道141进入浸泡室11的内部空间113。在一实施例中,金属回收系统10可进一步包括与浸泡室11连通的冷却剂回收槽14B,浸泡室11的内部空间113通过冷却剂排出管道142与冷却剂回收槽14B连通,通过冷却剂管道142,冷却剂115可直接自浸泡室11的内部空间113排出。冷却剂进入管道141与冷却剂排出管道142上可分别设置有控制阀143以及144,以控制冷却剂115输入浸泡室11与回收浸泡室11内的冷却剂115。通过冷却剂储存槽14A、冷却剂回收槽14B、冷却剂进入与排出管道141以及142以及控制阀143以及144可减少替换冷却剂115所需的时间以及步骤。The
集料槽13具有第二进料口131以及第一出料口133。集料槽13可与浸泡室11并连或者可与浸泡室11相隔一段距离。在一实施例中,浸泡室11与集料槽13不连通。在浸泡室11与集料槽13不连通的情况下,浸泡室11中的冷却剂115不会扩散至集料槽13,从而可减少冷却剂115的用量。在一实施例中,浸泡室11还可包括活动门板(图未示)。活动门板可覆盖第一进料口111以防止冷却剂115自浸泡室11的内部空间113扩散至外部,进而有效地将浸泡室11的内部空间113的温度维持在期望或特定温度范围内。The collecting
进料槽17设置于移动单元15上,并在第一进料口111以及第二进料口131之间旋转移动,且可升降并进出浸泡室11的内部空间113。在一实施例中,进料槽17可为具有开口的网状容器,但本发明不限于此。进料槽17可通过移动单元15在第一进料口111以及第二进料口131之间旋转移动并升降进出浸泡室11的内部空间113。在一实施例中,包覆有胶体5的金属或金属管3可被置于进料槽17中,移动单元15使进料槽17降低进入浸泡室11的冷却剂115中,且在冷却剂115中停留一段时间。由于冷却剂115具有可使包覆金属或金属管3的胶体5硬化或玻璃化的温度(即冷却剂115需具有低于胶体5的玻璃转化温度的温度),因此在浸泡于冷却剂115一段时间后,包覆金属或金属管3的胶体5将会硬化或玻璃化。在胶体5硬化或玻璃化后,移动单元15将进料槽17升高移出浸泡室11的内部空间113,接着进料槽17旋转移动至集料槽13的第二进料口131。移动单元翻转进料槽17以将进料槽17中的包覆有胶体5的金属或金属管3倒入集料槽13中。因此,移动单元15具有升降、旋转、翻转等动作的机构。进料槽17在冷却剂115中停留的时间可为1~120秒、10~120秒、20~120秒、30~120秒、40~120秒、50~120秒、60~120秒、70~120秒、80~60秒、90~120秒、100~120秒、110~120秒、10~110秒、10~100秒、10~90秒、10~80秒、10~70秒、10~60秒、10~50秒、10~40秒、10~30秒、10~20秒、20~100秒、20~90秒、20~80秒、20~70秒、20~60秒、20~50秒、20~40秒、20~30秒、30~100秒、30~90秒、30~80秒、30~70秒、30~60秒、30~50秒、或30~40秒,但本发明不限于此。根据胶体5的特性,进料槽17在冷却剂115中停留的时间可大于120秒。The feeding
图3为根据本发明实施例的金属回收系统10中与进料槽17连接的移动单元15的示意图。3 is a schematic diagram of the
参照图3,移动单元15包括中空旋转平台153、与中空旋转平台153以及进料槽17连接的转动装置157用于翻转进料槽17、设置于中空旋转平台153的空心处的移动单元本体(例如轴杆、支撑杆、柱、杆等)151、设置于移动单元本体151上的升降装置155、连接中空旋转平台153以及升降装置155的第二连接件159、以及与中空旋转平台153、升降装置155以及转动装置157连接以控制中空旋转平台153、升降装置155以及转动装置157的移动控制模块(图未示)。3, the
中空旋转平台153可为转盘为中空结构的任何现有的旋转机构。举例而言,中空旋转平台153可包括具有中空结构的转盘、用于支撑上述转盘的交叉滚子轴承或滚珠轴承、设于交叉滚子轴承或滚珠轴承下方的齿轮、以及与上述齿轮相接以驱动齿轮以及其上的元件旋转的步进马达或伺服马达。The hollow
转动装置157可包括第一步进马达1571以及第一连接件1573。第一步进马达1571可与进料槽17以及移动控制模块连接,移动控制模块可控制第一步进马达1571转动以翻转改变进料槽17的开口方向,倒出装载于进料槽17内的物品,在本发明中,为包覆有胶体5的金属或金属管3。The
转动装置157的第一步进马达1571可通过其中的第一连接件1573与中空旋转平台153连接。因此,转动装置157可通过旋转中空旋转平台153而旋转移动到期望位置。举例而言,移动控制模块可控制中空旋转平台153旋转以将进料槽17与转动装置157自第一进料口111上方旋转到第二进料口131上方。移动控制模块可在控制中空旋转平台153旋转以将转动装置157旋转到第二进料口131上方后,然后并控制转动装置157的第一步进马达1571转动以翻转进料槽17,倒出装载于进料槽17内的物品。The
中空旋转平台153可通过第二连接件159与升降装置155连接。升降装置155可包括但不限于油压升降装置、螺杆升降装置、滑轨升降装置或滑轮升降装置。图3以升降装置155为滑轮升降装置的实施例进行说明,但本发明不限于此。如图3所示,升降装置155可包括主动轮1551以及从动轮1552以及链条1553。主动轮1551以及从动轮1552分别设置于移动单元本体151的顶端以及底端,而链条1553可搭载于主动轮1551以及从动轮1552上。主动轮1551连接一马达。并由马达带动旋转,从而带动从动轮1552与链条1553。在一实施例中,从动轮1552的外径可大于主动轮1551的外径以降低链条1553脱落的可能。在另一实施例中,升降装置155可进一步包括惰轮以降低链条脱落的可能。链条1553通过第二连接件159与中空旋转平台153连接,因此于移动控制模块操纵主动轮1551转动以带动链条1553移动时,中空旋转平台153会被上升或下降至移动单元本体151上的期望位置。移动控制模块控制可在操纵主动轮1551转动以带动链条1553移动,进而将中空旋转平台153升降至移动单元本体151上的期望位置后,控制中空旋转平台153旋转以将转动装置157旋转到第二进料口131上方,最后再控制转动装置157的第一步进马达1571转动以翻转进料槽17,倒出装载于进料槽17内的物品。The hollow
通过本发明的移动单元15,进料槽17不但可在第一进料口111以及第二进料口131之间移动,还可进出浸泡室11的内部空间113,从而可实现将进料槽17内的物品(在本发明中,为包覆有胶体5的金属或金属管3)浸泡于浸泡室11的冷却剂115后、将进料槽17内的物品移出浸泡室11的内部空间113、接着再将进料槽17内的物品倒至集料槽13等一系列操作。Through the moving
参照图2,破碎单元19具有第三进料口191以及第二出料193口,且第三进料口191与集料槽13的第一出料口133相连。当集料槽13中包覆有胶体5的金属或金属管3聚集到一定的量时,集料槽13的第一出料口133可被打开以使集料槽13中包覆有胶体5的金属或金属管3移动到破碎单元19中以对硬化或玻璃化的胶体5进行破碎操作。破碎单元19中可包括任何可使硬化或玻璃化的胶体5破碎的破碎装置。在一实施例中,破碎单元19中可包括机械力破碎装置。机械力破碎装置可包括但不限于切割装置、击碎装置、辗压装置、压碎装置或其任意组合。机械力破碎装置的实施例可包括但不限于凸轮破碎装置、颚式破碎机、链条破碎装置或其任意组合。破碎后的胶体5以及金属或金属管3会通过第二出料口193移动到相应其设置的分选单元12中(参照图2)。2 , the crushing
图4为根据本发明一实施例的分选单元12的示意图。图4中以比重分选装置作为实施例来说明分选单元12的操作,但本发明不限于此。本发明的分选单元12无具体限制,其可为任何可将破碎的胶体5与金属或金属管3分离的装置。分选单元12的实施例可包括但不限于比重分选装置、尺寸分选装置、重量分选装置、或其任意组合。FIG. 4 is a schematic diagram of the sorting
参照图4,分选单元12包括分选单元本体120、分离控制装置121、胶体分离装置123、金属收集装置125以及液体127。如图4所示,液体127置于分选单元本体120内。液体127无具体限制,只要其密度小于金属或金属管3的密度且大于胶体5的密度而使胶体5在其中为浮体,而金属或金属管3在其中为沉体即可。举例而言,液体127可包括但不限于水。金属收集装置125可置于分选单元本体120底部以收集下沉的金属或金属管3。在一实施例中,金属收集装置125可为具有向上开口1251网状容器,但本发明不限于此。分离控制装置121可与分选单元本体120的一侧壁以及胶体分离装置123连接,并使将胶体分离装置123固定于分选单元本体120的上述侧壁与金属收集装置125之间。分离控制装置121可包含转动控制模块(图未示)、第二步进马达1211以及转轴1213。胶体分离装置123与转轴1213连接,且转轴1213可通过第二步进马达1211与转动控制模块连接。转动控制模块可通过控制第二步进马达1211来转动转轴1213。通过转动转轴1213,可使胶体分离装置123捞取动作以及待机动作之间进行切换。具体而言,在待机动作时点,转动控制模块会控制第二步进马达1211转动转轴1213,使胶体分离装置123往分选单元本体120的该侧壁方向转动以露出金属收集装置125的开口1251。在捞取动作时点,转动控制模块会控制第二步进马达1211转动转轴1213,使胶体分离装置123往金属收集装置125的方向转动以捞取浮于液体127中的胶体5。胶体分离装置123无具体限制,只要是可用以将浮于液体127中的胶体5取出的装置即可。在一实施例中,胶体分离装置123可为捞取勺,但本发明不限于此。金属收集装置125可在胶体分离装置123的捞取动作实质完毕之后自分选单元本体120底部取出以完成金属的回收。4 , the sorting
在一实施例中,本发明的金属回收系统可进一步包括在将包覆有胶体5的金属或金属管3置于进料槽17之前,先对包覆有胶体5的金属或金属管3进行分类的预处理单元。In one embodiment, the metal recovery system of the present invention may further include, before placing the metal or
预处理单元可包括感测模块以及分析模块。感测模块的实施例可包括但不限于影像提取装置、密度分析装置或红外线分析装置。分析模块可接收来自感测模块的数据,将上述数据与预建的识别模型进行比对,并依据比对结果对包覆有胶体5的金属或金属管3进行分类。在一实施例中,分析模块可依据感测模块提供的数据进行类神经网络运算,类神经网络运算的实施例可包括但不限于AlexNet、VGGNet或ResNet。类神经网络运算可依据感测模块提供的数据产生新的识别模型以替代预建的识别模型,进而提高分类的精准度。The preprocessing unit may include a sensing module and an analysis module. Embodiments of the sensing module may include, but are not limited to, an image capture device, a density analysis device, or an infrared analysis device. The analysis module can receive the data from the sensing module, compare the above data with the pre-built identification model, and classify the metal or
举例而言,在感测模块为影像提取装置的情况下,感测模块可先对包覆有胶体5的金属或金属管3进行影像提取。提取到的影像数据会被输入至分析模块中与分析模块中预建的识别模型进行比对,分析模块可依据比对结果判定包覆于金属或金属管3上的胶体5的量,并依据判定结果将包覆有胶体5的金属或金属管3分为,例如:金属或金属管3上无胶体5、只有部分金属或金属管3被胶体5包覆以及整个金属或金属管3都被胶体5包覆等三类,但本发明不限于此。举例而言,可将包覆有胶体5的金属或金属管3依据胶体5的量分为五类或更多,或是可依据胶体5的种类进行分类。分析模块可依据感测模块提供的提取到的影像数据进行类神经网络运算,并产生新的识别模型以替代预建的识别模型,进而提高分类的精准度。移动单元15可依据预处理单元的分类结果而调整进料槽17在冷却剂115中停留的时间。For example, when the sensing module is an image capturing device, the sensing module can first perform image capturing on the metal or
本发明进一步提供一种利用上述金属回收系统的金属回收方法。图5为根据本发明一实施例的金属回收方法20的流程图。如图5所述,本发明的金属回收方法20包括:将包覆有胶体的金属置于冷却剂中以玻璃化胶体的步骤S201;将包覆有玻璃化胶体的金属移至破碎单元以对玻璃化胶体进行破碎的步骤S203;以及于分选单元中分离破碎的玻璃化胶体以及金属的步骤S205。The present invention further provides a metal recovery method utilizing the above metal recovery system. FIG. 5 is a flowchart of a
在一实施例中,本发明的金属回收方法20可进一步包括在将包覆有胶体的金属置于冷却剂中以玻璃化胶体的步骤S201之前,在预处理单元中对包覆有胶体的金属进行分类的步骤S200。In one embodiment, the
以下以包覆有沥青胶的铜管作为实施例对本发明进行更详细的说明。Hereinafter, the present invention will be described in more detail by taking the copper pipe coated with asphalt glue as an example.
实施例Example
收集包覆有沥青胶的铜管,利用影像提取装置对包覆有沥青胶的铜管进行影像提取,将所提取到的数据传送到分析模块中与分析模块中预建的识别模型进行比对,分析模块依据比对结果判定将包覆有沥青胶的铜管分为:无沥青胶的纯铜管的类别I、部分铜管被沥青胶包覆的类别II、整个铜管被沥青胶包覆的类别III,且直接对类别I的铜管进行回收。Collect the copper pipes covered with asphalt glue, use the image extraction device to extract the image of the copper pipes covered with asphalt glue, and transmit the extracted data to the analysis module for comparison with the pre-built recognition model in the analysis module. , the analysis module judges the copper pipes covered with asphalt glue according to the comparison results into: Category I of pure copper pipes without asphalt glue, Category II of copper pipes covered with asphalt glue, and whole copper pipes covered with asphalt glue Class III covered, and direct recycling of Class I copper pipes.
通过与浸泡室流体连通的冷却剂管道输入液态氮至浸泡室的内部空间,直到液态氮达到一定的高度。Liquid nitrogen is fed into the interior space of the soaking chamber through a coolant line in fluid communication with the soaking chamber until the liquid nitrogen reaches a certain height.
将类别II的铜管置于进料槽中,并控制移动单元使类别II的铜管完全浸于液态氮中10~30秒,以脆化或玻璃化类别II的铜管上的沥青胶。接着控制移动单元使进料槽移出浸泡室的内部空间,并将进料槽中类别II的铜管倒于集料槽中。The class II copper pipes are placed in the feed tank, and the moving unit is controlled to completely immerse the class II copper pipes in liquid nitrogen for 10 to 30 seconds to embrittle or vitrify the asphalt glue on the class II copper pipes. Then, the moving unit is controlled to move the feed tank out of the inner space of the soaking chamber, and the copper pipes of Category II in the feed tank are poured into the collection tank.
将类别III的铜管置于进料槽中,并控制移动单元使类别III的铜管完全浸于液态氮中30~60秒,以脆化或玻璃化类别III的铜管上的沥青胶。接着控制移动单元使进料槽移出浸泡室的内部空间,并将进料槽中类别III的铜管倒于集料槽中。The class III copper pipes are placed in the feed tank, and the moving unit is controlled to completely immerse the class III copper pipes in liquid nitrogen for 30 to 60 seconds to embrittle or vitrify the asphalt glue on the class III copper pipes. The moving unit is then controlled to move the feed chute out of the inner space of the soaking chamber, and pour the Category III copper pipes in the feed chute into the collection chute.
打开集料槽的第一出料口,使集料槽中所有的铜管进入机械力破碎装置以破碎铜管上脆化或玻璃化的沥青胶。脆化或玻璃化的沥青胶以及铜管会自机械力破碎装置的第二出料口掉落到比重分选装置中。比重分选装置中的液体为水,破碎的沥青胶会浮于水上,而铜管会沉到水底的网篮中。将浮于水上的沥青胶用捞取勺捞出并置于胶收集槽中。待浮于水上的沥青胶捞除完毕后,将网篮取出即可获得其上的沥青胶被完整的去除的铜管,完成铜管的回收。Open the first discharge port of the collecting tank, and make all the copper pipes in the collecting tank enter the mechanical crushing device to break the brittle or vitrified asphalt glue on the copper pipes. The embrittled or vitrified asphalt glue and copper pipes will fall into the specific gravity sorting device from the second outlet of the mechanical crushing device. The liquid in the gravity separation device is water, the broken asphalt glue will float on the water, and the copper pipe will sink into the net basket at the bottom of the water. Remove the asphalt glue floating on the water with a scoop and place it in the glue collection tank. After the asphalt glue floating on the water is removed, take out the mesh basket to obtain a copper tube with the asphalt glue on it completely removed, thus completing the recovery of the copper tube.
本发明的金属回收系统以及金属回收方法是利用金属上的胶体特性,以温度低于胶体的玻璃转化温度的冷却剂先将胶体硬化或玻璃化后对硬化或玻璃化的胶体进行破碎以达到完整分开胶体与金属,进而提升金属的回收品质。The metal recovery system and the metal recovery method of the present invention utilize the colloid properties on the metal to first harden or vitrify the colloid with a coolant whose temperature is lower than the glass transition temperature of the colloid, and then crush the hardened or vitrified colloid to achieve complete integrity. Separating colloids and metals, thereby improving the quality of metal recycling.
以上概述本发明数个实施例的特征,以便在本发明所属技术领域中具有通常知识者可更易理解本发明实施例的观点。在本发明所属技术领域中具有通常知识者应理解,他们能以本发明实施例为基础,设计或修改其他制作工艺和结构,以达到与在此介绍的实施例相同的目的及/或优势。在本发明所属技术领域中具有通常知识者也应理解到,此类等效的制作工艺和结构并无悖离本发明的精神与范围,且他们能在不违背本发明的精神和范围之下,做各式各样的改变、取代和替换。The features of several embodiments of the present invention are summarized above, so that those with ordinary knowledge in the technical field to which the present invention pertains can more easily understand the viewpoints of the embodiments of the present invention. Those skilled in the art to which the present invention pertains should appreciate that they can, based on the embodiments of the present invention, design or modify other fabrication processes and structures to achieve the same purposes and/or advantages of the embodiments introduced herein. Those with ordinary knowledge in the technical field to which the present invention pertains should also understand that such equivalent manufacturing processes and structures do not depart from the spirit and scope of the present invention, and they can be used without departing from the spirit and scope of the present invention. , making all kinds of changes, substitutions, and substitutions.
Claims (11)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
TW109145941 | 2020-12-24 | ||
TW109145941A TWI760988B (en) | 2020-12-24 | 2020-12-24 | Metal recovery system and metal recovery method using the same |
Publications (2)
Publication Number | Publication Date |
---|---|
CN114733870A true CN114733870A (en) | 2022-07-12 |
CN114733870B CN114733870B (en) | 2023-11-21 |
Family
ID=82198805
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202011587364.6A Active CN114733870B (en) | 2020-12-24 | 2020-12-29 | Metal recycling system and metal recycling method utilizing same |
Country Status (2)
Country | Link |
---|---|
CN (1) | CN114733870B (en) |
TW (1) | TWI760988B (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
TWI800367B (en) * | 2022-04-30 | 2023-04-21 | 李漢揚 | Automatic recycling plastic cup collection system architecture |
Citations (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH02217155A (en) * | 1989-02-15 | 1990-08-29 | Mazda Motor Corp | Method and apparatus for casting into metallic mold |
US5431347A (en) * | 1991-12-02 | 1995-07-11 | Hitachi, Ltd. | System and method for disposing waste |
JPH07256231A (en) * | 1994-03-18 | 1995-10-09 | Hitachi Ltd | Method and apparatus for selecting and collecting metal |
JPH0857853A (en) * | 1995-07-12 | 1996-03-05 | Hitachi Ltd | Waste treatment device and treatment method |
JP2001283661A (en) * | 2000-03-31 | 2001-10-12 | Hitachi Zosen Corp | Waste wire recycling system |
JP2008178846A (en) * | 2007-01-26 | 2008-08-07 | Mitsubishi Heavy Ind Ltd | Method of and apparatus for sorting crushed industrial waste |
KR101270354B1 (en) * | 2013-02-12 | 2013-06-04 | 한국쓰리알환경산업(주) | Classification system for recyclable waste with object recognition mode |
CN106111673A (en) * | 2016-07-25 | 2016-11-16 | 朱建裕 | A kind of separating plastic and method of metal from electron wastes |
CN209095802U (en) * | 2018-09-18 | 2019-07-12 | 上海睿聚环保科技有限公司 | A kind of complete reclaimer of electrical type waste plastic |
CN110670009A (en) * | 2018-11-11 | 2020-01-10 | 海盐宝利机械有限公司 | Hot galvanizing production system |
CN111430086A (en) * | 2020-05-22 | 2020-07-17 | 湖南省正源储能材料与器件研究所 | Method and device for recycling wires and cables |
RU2731729C1 (en) * | 2019-07-01 | 2020-09-08 | Федеральное государственное бюджетное учреждение науки Институт теплофизики им. С.С. Кутателадзе Сибирского отделения Российской академии наук (ИТ СО РАН) | Processing complex of solid municipal wastes with automated sorting of inorganic part and plasma gasification of organic residue |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106623277B (en) * | 2017-02-16 | 2018-07-13 | 武汉大润科技有限公司 | A kind of metal hanger surface depainting equipment |
-
2020
- 2020-12-24 TW TW109145941A patent/TWI760988B/en active
- 2020-12-29 CN CN202011587364.6A patent/CN114733870B/en active Active
Patent Citations (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH02217155A (en) * | 1989-02-15 | 1990-08-29 | Mazda Motor Corp | Method and apparatus for casting into metallic mold |
US5431347A (en) * | 1991-12-02 | 1995-07-11 | Hitachi, Ltd. | System and method for disposing waste |
JPH07256231A (en) * | 1994-03-18 | 1995-10-09 | Hitachi Ltd | Method and apparatus for selecting and collecting metal |
JPH0857853A (en) * | 1995-07-12 | 1996-03-05 | Hitachi Ltd | Waste treatment device and treatment method |
JP2001283661A (en) * | 2000-03-31 | 2001-10-12 | Hitachi Zosen Corp | Waste wire recycling system |
JP2008178846A (en) * | 2007-01-26 | 2008-08-07 | Mitsubishi Heavy Ind Ltd | Method of and apparatus for sorting crushed industrial waste |
KR101270354B1 (en) * | 2013-02-12 | 2013-06-04 | 한국쓰리알환경산업(주) | Classification system for recyclable waste with object recognition mode |
CN106111673A (en) * | 2016-07-25 | 2016-11-16 | 朱建裕 | A kind of separating plastic and method of metal from electron wastes |
CN209095802U (en) * | 2018-09-18 | 2019-07-12 | 上海睿聚环保科技有限公司 | A kind of complete reclaimer of electrical type waste plastic |
CN110670009A (en) * | 2018-11-11 | 2020-01-10 | 海盐宝利机械有限公司 | Hot galvanizing production system |
RU2731729C1 (en) * | 2019-07-01 | 2020-09-08 | Федеральное государственное бюджетное учреждение науки Институт теплофизики им. С.С. Кутателадзе Сибирского отделения Российской академии наук (ИТ СО РАН) | Processing complex of solid municipal wastes with automated sorting of inorganic part and plasma gasification of organic residue |
CN111430086A (en) * | 2020-05-22 | 2020-07-17 | 湖南省正源储能材料与器件研究所 | Method and device for recycling wires and cables |
Also Published As
Publication number | Publication date |
---|---|
TWI760988B (en) | 2022-04-11 |
TW202225419A (en) | 2022-07-01 |
CN114733870B (en) | 2023-11-21 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US3086718A (en) | Method and apparatus for separating metallic particles | |
TWI760988B (en) | Metal recovery system and metal recovery method using the same | |
TW303310B (en) | ||
CN103752593A (en) | Process for selecting and recovering heavy metal substances in domestic garbage incineration slag | |
CN201153145Y (en) | Separating and selecting apparatus used after crushing waste lead accumulators | |
CN205761677U (en) | A kind of cable recovery and rinsing segregation apparatus | |
CN108080108A (en) | A kind of integrated circuit testing defective products chip processing apparatus | |
CN202921427U (en) | Flotation recycling gold and sliver device from zinc smelting acid leaching dregs | |
CN218743868U (en) | Waste metal classification and cleaning system | |
Hlabangana et al. | Application of the attainable region method to determine optimal conditions for milling and leaching | |
CN117000738A (en) | Municipal refuse recycling equipment and recycling method thereof | |
CN215655723U (en) | Steel mill resource recycling steel slag magnetic separation device | |
CN108277676A (en) | Waste paper pulp filters all-in-one machine and its application method | |
CN205217073U (en) | Drum -type slag crushing and screening device | |
CN204454657U (en) | A kind of leaded cullet resource utilization remanufacture line | |
Allen | Stirred Milling machine development and application extension | |
CN214422678U (en) | Scrap steel recycling and smelting equipment | |
CN207405213U (en) | A kind of lead ore pre-processing device automatically controlled | |
CN207405218U (en) | The automatic streamline production line of valuable metal in a kind of recycling lead ore | |
CN217702761U (en) | An uninterrupted grinding device for steel ball production | |
JP2011121032A (en) | Sorting apparatus, sorting method, and soil purification equipment | |
CN116571330B (en) | Intelligent dry-mixed mortar production device and manufacturing method | |
CN221715121U (en) | A cleaning mechanism for recycling iron furnace slag | |
CN216192600U (en) | High-temperature aluminium sediment separator in stokehold | |
KR102605120B1 (en) | Electronic waste recycling system for improving efficiency and workability |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant |