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CN108031702B - Complete treatment equipment and treatment method for waste circuit board recovery - Google Patents

Complete treatment equipment and treatment method for waste circuit board recovery Download PDF

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CN108031702B
CN108031702B CN201711445509.7A CN201711445509A CN108031702B CN 108031702 B CN108031702 B CN 108031702B CN 201711445509 A CN201711445509 A CN 201711445509A CN 108031702 B CN108031702 B CN 108031702B
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circuit board
sorting
crushing
waste
tank
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CN108031702A (en
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孟大为
何正邦
穆红岩
刘涛
岳明珠
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Beijing Jingcheng Green Energy Co ltd
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Zhejiang Jingcheng Renewable Resources Co ltd
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B09DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09BDISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
    • B09B3/00Destroying solid waste or transforming solid waste into something useful or harmless
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B02CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02CCRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
    • B02C21/00Disintegrating plant with or without drying of the material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B09DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09BDISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
    • B09B3/00Destroying solid waste or transforming solid waste into something useful or harmless
    • B09B3/40Destroying solid waste or transforming solid waste into something useful or harmless involving thermal treatment, e.g. evaporation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B09DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09BDISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
    • B09B5/00Operations not covered by a single other subclass or by a single other group in this subclass
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G1/00Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10Feedstock materials
    • C10G2300/1003Waste materials
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/82Recycling of waste of electrical or electronic equipment [WEEE]

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Wood Science & Technology (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Food Science & Technology (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Thermal Sciences (AREA)
  • Organic Chemistry (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

The invention provides a complete set of treatment equipment and a treatment method for waste circuit board recovery, wherein the equipment comprises a pretreatment device, a waste circuit board recovery device and a waste circuit board recovery device, wherein an inlet of the pretreatment device is connected with an outlet of a feeding device and is used for pretreating the waste circuit board from the feeding device or electronic waste containing the waste circuit board; the inlet of the cracking oiling device is connected with the outlet of the pretreatment device and is used for carrying out cracking oiling treatment on the waste circuit board material output by the pretreatment device; the inlet of the crushing/sorting device is connected with the solid material outlet of the cracking oiling device and is used for further crushing and sorting the mixture of the metal and the glass fiber output by the cracking oiling device; and the inlet of the dust removal device is respectively connected with the dust outlets of the pretreatment device and the crushing/sorting device and is used for treating the dust which reaches the standard and is discharged. The equipment has the advantages of good decomposition effect, safety, labor saving, capability of continuously operating for 120 hours, low energy consumption, high productivity, no pollution and capability of reaching the metal recovery rate of 95-98 percent.

Description

用于废旧线路板回收的成套处理设备及处理方法Complete set of processing equipment and processing method for recycling waste circuit boards

技术领域technical field

本发明涉及一种用于废旧线路板回收的成套处理设备及处理方法,尤其 也是一种用于废旧线路板无害化的成套处理设备及处理方法,属于有色金属 再生产领域。The invention relates to a complete set of processing equipment and a processing method for recycling waste circuit boards, especially a complete set of processing equipment and a processing method for harmless waste circuit boards, belonging to the field of non-ferrous metal reproduction.

背景技术Background technique

我国是电器电子产品的生产大国,同时也是消费大国。随着时代的不断 发展,电器电子产品更新换代速度越来越快,大量电器电子产品进入淘汰高 峰期。据工信部2015年统计数据显示,我国每年电器和电子产品报废量在2 亿台以上,重量超过500万吨。废弃电器电子产品中含有的对人、动植物和 环境等产生危害的物质或元素,包括铅(Pb)、汞(Hg)、镉(Cd)、六价 铬(Cr6+)、多溴联苯(PBB)、多溴联苯醚(PBDE)、多氯联苯(PCBs)、 含有消耗臭氧层的物质以及国家规定的危险废物。随着电子垃圾的井喷式产 生和我国制造业向智能化、绿色化转型,对环保提出了更高的要求,对废旧 电子线路板进行回收处理成为一个亟待解决的社会化问题,也给废旧线路板 (PCB)回收利用市场迎来巨大的发展契机。my country is a big producer of electrical and electronic products, but also a big consumer. With the continuous development of the times, the upgrading speed of electrical and electronic products is getting faster and faster, and a large number of electrical and electronic products have entered the peak phase of elimination. According to the statistics of the Ministry of Industry and Information Technology in 2015, more than 200 million electrical and electronic products are scrapped in my country each year, with a weight of more than 5 million tons. Substances or elements contained in waste electrical and electronic products that are harmful to humans, animals, plants and the environment, including lead (Pb), mercury (Hg), cadmium (Cd), hexavalent chromium (Cr 6+ ), polybrominated biphenyls (PBB ), polybrominated diphenyl ethers (PBDE), polychlorinated biphenyls (PCBs), substances containing ozone-depleting substances, and hazardous wastes regulated by the state. With the blowout generation of electronic waste and the transformation of my country's manufacturing industry towards intelligence and greenness, higher requirements for environmental protection have been put forward. Recycling waste electronic circuit boards has become an urgent social problem that needs to be solved. The board (PCB) recycling market has ushered in a huge opportunity for development.

据有关资料介绍,世界印刷线路板业的年复增长率为8.7%,我国的年复 增长率为14.4%。全球约40%以上的线路板都在中国生产,珠江三角洲、长 江三角洲是我国线路板生产企业的集中地。废旧电路板是玻璃纤维强化树脂 和多种金属的混合物,加上线路板生产制造所产生的大量边角余料,如不妥 善处理,不但会造成有用资源的大量流失,而且会对环境产生严重的危害。 目前国内每年需要处理的废旧线路板在50万吨以上,市场规模在180亿元以 上,未来5年废旧线路板的产生量年复增长率达20%。According to relevant information, the annual compound growth rate of the world's printed circuit board industry is 8.7%, and that of my country is 14.4%. More than 40% of the circuit boards in the world are produced in China, and the Pearl River Delta and the Yangtze River Delta are the concentration places of circuit board manufacturers in my country. Waste circuit boards are a mixture of glass fiber reinforced resin and various metals, plus a large amount of leftovers produced by the production of circuit boards. If not properly disposed of, it will not only cause a large loss of useful resources, but also have a negative impact on the environment. serious hazard. At present, more than 500,000 tons of waste circuit boards need to be processed in China every year, and the market size is more than 18 billion yuan. In the next five years, the compound annual growth rate of waste circuit boards will reach 20%.

废旧印刷线路板作为电子废弃物的重要组件,一方面既含有铜、金、银 等多种普通金属和稀贵金属,具有较高的回收利用价值;另一方面也含有铅、 镉、聚氯乙烯塑料等多种重金属和有害物质,存在潜在的环境污染风险。废 旧线路板里贵金属的含量高达40%,最多的是铜,1吨PCB可提取200~350kg 铜;此外1吨废旧线路板可提取300g左右的金、及500~2000g其他贵金属。 废旧线路板回收利用项目是目前再生资源利用行业中盈利空间较高、发展空 间较广的项目,行业平均毛利率在17%左右。但同时,废旧线路板回收利用技术是目前废旧电器电子产品处理中最难以资源化的处理工艺。在国内,大 部分中小废旧线路板回收利用企业生产工艺落后,普遍采用焚烧、酸洗等野 蛮手段回收废旧线路板中的高价值金属物质,金属回收率低,环境污染严重。As an important component of electronic waste, waste printed circuit boards contain copper, gold, silver and other common metals and rare and precious metals, which have high recycling value; on the other hand, they also contain lead, cadmium, polyvinyl chloride, etc. A variety of heavy metals and harmful substances such as plastics have potential environmental pollution risks. The content of precious metals in waste circuit boards is as high as 40%, and the most is copper. 1 ton of PCB can extract 200-350kg of copper; in addition, 1 ton of waste circuit boards can extract about 300g of gold and 500-2000g of other precious metals. The waste circuit board recycling project is currently a project with relatively high profit potential and wide development space in the renewable resource utilization industry. The average gross profit rate of the industry is about 17%. But at the same time, the recycling technology of waste circuit boards is currently the most difficult treatment process in the treatment of waste electrical and electronic products. In China, most of the small and medium waste circuit board recycling enterprises have backward production technology, and generally adopt brutal methods such as incineration and pickling to recycle high-value metal substances in waste circuit boards. The metal recovery rate is low and the environmental pollution is serious.

目前企业对废旧线路板的处理方案主要采用物理分选技术、火法熔炼技 术、湿法冶金技术、裂解法四种。采取火法熔炼技术方案,则存在设备投资 高、处置成本高昂、不适合小规模废线路板处理的问题;采取湿法熔炼技术 方案,化学试剂消耗量大,产生大量难处理废水,环境污染大,适合贵金属 提炼,不适合覆铜线路板处理;采用物理分选技术方案,工艺简单、处理成 本低,适合废线路板和覆铜板处理,但无法解决环氧树脂问题;裂解法环境 友好,但无法解决玻璃纤维问题。At present, enterprises mainly use physical separation technology, pyromelting technology, hydrometallurgy technology and cracking method to deal with waste circuit boards. If the pyromelting technology scheme is adopted, there are problems of high equipment investment, high disposal cost, and is not suitable for small-scale waste circuit board treatment; if the wet smelting technology scheme is adopted, the consumption of chemical reagents is large, a large amount of difficult-to-treat wastewater is produced, and the environment is polluted , suitable for precious metal extraction, not suitable for copper clad circuit board treatment; physical separation technology scheme is adopted, the process is simple, the treatment cost is low, suitable for waste circuit board and copper clad laminate treatment, but it cannot solve the problem of epoxy resin; the pyrolysis method is environmentally friendly, But it can't solve the fiberglass problem.

发明内容Contents of the invention

为了克服现有技术的不足,本发明的目的在于提供一种用于废旧线路板 回收的成套处理设备,该成套处理设备主要包括破碎装置、油化装置和分选 装置,能实现废弃线路板资源化及无害化处理,不仅使铜、铝、玻璃纤维分 离回收,同时解决对环境的污染问题。本发明的另一目的在于提供一种用于 废旧线路板回收的处理方法,采取裂解法与物理分选相结合工艺,有效地控 制成本,保证环境友好,做到无害化。In order to overcome the deficiencies in the prior art, the object of the present invention is to provide a complete set of processing equipment for recycling waste circuit boards. Chemical and harmless treatment not only separates and recycles copper, aluminum, and glass fibers, but also solves the problem of environmental pollution. Another object of the present invention is to provide a treatment method for recycling waste circuit boards, which uses a combination of pyrolysis and physical separation to effectively control costs, ensure environmental friendliness, and achieve harmlessness.

为实现上述目的,本发明采用以下技术方案:To achieve the above object, the present invention adopts the following technical solutions:

一种用于废旧线路板回收的成套处理设备,包括:A complete set of processing equipment for recycling waste circuit boards, comprising:

预处理装置,其入口与进料装置的出口连接,用来对来自进料装置的废 旧线路板或含废旧线路板的电子废弃物进行预处理;A pretreatment device, the inlet of which is connected to the outlet of the feed device, is used to pretreat the waste circuit boards from the feed device or electronic waste containing waste circuit boards;

裂解油化装置,其入口与所述预处理装置的出口连接,用于对所述预处 理装置输出的废旧线路板物料进行裂解油化处理;A cracking and oiling device, the inlet of which is connected to the outlet of the pretreatment device, and is used for cracking and oiling the waste circuit board material output by the pretreatment device;

破碎/分选装置,其入口与所述裂解油化装置的固体物料出口连接,用于 对裂解油化装置输出的金属与玻璃纤维混合物进行进一步的破碎和分选处理;A crushing/separating device whose inlet is connected to the solid material outlet of the cracking and oiling device for further crushing and sorting treatment of the metal and glass fiber mixture output by the cracking and oiling device;

除尘装置,其入口分别与所述预处理装置和所述破碎/分选装置的灰尘出 口连接,用于处理灰尘使空气达标排放。The dust removal device, the inlet of which is connected with the dust outlet of the pretreatment device and the crushing/sorting device respectively, is used to process the dust to make the air discharge up to standard.

上述用于废旧线路板回收的成套处理设备中,作为一种优选实施方式, 所述预处理装置包括:第一预处理装置和/或第二预处理装置;其中,所述第 一预处理装置包括脱锡机,用于将锡、电子元件从所述废旧线路板上脱离下 来得到光板电路板;所述第二预处理装置包括第一破碎机、第一分选机和人 工分选平台,其中,所述第一破碎机用于对所述含废旧线路板的电子废弃物 进行破碎处理;所述第一分选机设置于所述第一破碎机之后,用于对破碎物 料进行筛分过滤处理;所述人工分选平台设置于第一分选机之前或之后,用于通过人工分选出较大的物料;优选地,所述第二预处理装置还包括:第一 磁选机,所述第一磁选机设置于所述第一破碎机和所述第一分选机之间。In the above-mentioned complete set of processing equipment for recycling waste circuit boards, as a preferred embodiment, the pretreatment device includes: a first pretreatment device and/or a second pretreatment device; wherein, the first pretreatment device It includes a tin remover, which is used to separate tin and electronic components from the waste circuit board to obtain a light board circuit board; the second pretreatment device includes a first crusher, a first sorting machine and a manual sorting platform , wherein, the first crusher is used to crush the electronic waste containing waste circuit boards; the first sorter is arranged after the first crusher to crush the crushed materials Sieving and filtering treatment; the manual sorting platform is arranged before or after the first sorting machine, for manually sorting larger materials; preferably, the second pretreatment device also includes: a first magnetic A sorting machine, the first magnetic separator is arranged between the first crusher and the first sorting machine.

上述用于废旧线路板回收的成套处理设备中,作为一种优选实施方式, 所述第一破碎机为链式破碎机。In the above complete set of processing equipment for recycling waste circuit boards, as a preferred embodiment, the first crusher is a chain crusher.

上述用于废旧线路板回收的成套处理设备中,作为一种优选实施方式, 所述第一分选机为波纹筛选槽或滚筒筛。In the above-mentioned complete set of processing equipment for recycling waste circuit boards, as a preferred embodiment, the first sorting machine is a corrugated screening tank or a drum screen.

上述用于废旧线路板回收的成套处理设备中,作为一种优选实施方式, 经所述第一破碎机处理后的物料为小于50mm×50mm的块料;经所述第一 分选机筛选出破碎物料的颗粒直径小于20mm~40mm;所述人工分选平台处 通过人工分选出大于100mm的物料。In the above-mentioned complete set of processing equipment for recycling waste circuit boards, as a preferred embodiment, the material processed by the first crusher is a block material smaller than 50mm×50mm; The particle diameter of the crushed material is less than 20mm to 40mm; the manual sorting platform manually sorts out the material larger than 100mm.

上述用于废旧线路板回收的成套处理设备中,作为一种优选实施方式, 所述裂解油化装置包括:热分解槽、触媒槽、冷却装置、储油箱和气体燃烧 器;其中,所述热分解槽的入口与所述预处理装置的出口连接;所述触媒槽 的入口与所述热分解槽的气体出口连接;所述冷却装置的入口与所述触媒槽 的出口连接;所述储油箱的入口与所述冷却装置的油出口连接;所述气体燃 烧器的入口与所述冷却装置的气体出口连接。In the above-mentioned complete set of processing equipment for recycling waste circuit boards, as a preferred embodiment, the cracking and oiling device includes: a thermal decomposition tank, a catalyst tank, a cooling device, an oil storage tank and a gas burner; wherein, the thermal The inlet of the decomposition tank is connected to the outlet of the pretreatment device; the inlet of the catalyst tank is connected to the gas outlet of the thermal decomposition tank; the inlet of the cooling device is connected to the outlet of the catalyst tank; the oil storage tank The inlet of the gas burner is connected with the oil outlet of the cooling device; the inlet of the gas burner is connected with the gas outlet of the cooling device.

上述用于废旧线路板回收的成套处理设备中,作为一种优选实施方式, 所述热分解槽包括热解槽、加热槽和反转装置,其中,所述热解槽是用于容 纳所述废旧线路板物料的场所,所述加热槽用于给所述热解槽加热使所述热 解槽内发生裂解反应,所述反转装置设置于所述加热槽和/或热解槽外部,用 于反转所述热解槽和所述加热槽,以便将所述热解槽中热解后的物料倾倒出 来。In the above-mentioned complete set of processing equipment for recycling waste circuit boards, as a preferred embodiment, the pyrolysis tank includes a pyrolysis tank, a heating tank and a reversing device, wherein the pyrolysis tank is used to accommodate the The place where the waste circuit board material is described, the heating tank is used to heat the pyrolysis tank to cause cracking reaction to occur in the pyrolysis tank, and the reversing device is arranged outside the heating tank and/or the pyrolysis tank , for reversing the pyrolysis tank and the heating tank, so as to dump out the pyrolyzed material in the pyrolysis tank.

上述用于废旧线路板回收的成套处理设备中,作为一种优选实施方式, 所述冷却装置为冷却塔,其内部设有气体冷却器、塔顶冷却器和冷却机兼循 环槽,其中,所述气体冷却器、塔顶冷却器用于冷却改质后的热裂解气,所 述冷却机兼循环槽用于回收油;所述气体燃烧器为燃烧炉。In the above-mentioned complete set of processing equipment for recycling waste circuit boards, as a preferred embodiment, the cooling device is a cooling tower, which is internally provided with a gas cooler, a tower top cooler, and a cooling machine and circulation tank, wherein, The gas cooler and tower top cooler are used to cool the reformed pyrolysis gas, and the cooler and circulation tank are used to recover oil; the gas burner is a combustion furnace.

上述用于废旧线路板回收的成套处理设备中,作为一种优选实施方式, 所述破碎/分选装置包括:第二破碎机、第二分选机、静电分选机;其中,In the above-mentioned complete set of processing equipment for recycling waste circuit boards, as a preferred embodiment, the crushing/separating device includes: a second crusher, a second sorting machine, and an electrostatic sorting machine; wherein,

所述第二破碎机的入口与所述裂解油化装置的固体物料出口连接,用于 对所述裂解油化装置输出的金属与玻璃纤维混合物进行进一步的粉碎处理;The inlet of the second crusher is connected to the solid material outlet of the cracking and oiling device for further pulverizing the metal and glass fiber mixture output by the cracking and oiling device;

所述第二分选机的入口与所述第二破碎机出口连接,用于分离所述第二 破碎机输出的物料中的重物和轻物;The inlet of the second classifier is connected to the outlet of the second crusher for separating heavy and light objects in the materials output by the second crusher;

所述静电分选机的入口与所述第二分选机的粉尘出口连接,用于分离粉 尘中的玻璃纤维和金属粉末;The inlet of the electrostatic separator is connected to the dust outlet of the second separator for separating glass fiber and metal powder in the dust;

优选地,所述破碎/分选装置还包括:第二磁选机,设置于所述第二破碎 机和所述第二分选机之间。Preferably, the crushing/separating device further includes: a second magnetic separator arranged between the second crusher and the second separator.

上述用于废旧线路板回收的成套处理设备中,作为一种优选实施方式, 所述第二破碎机为锤磨机。In the above complete set of processing equipment for recycling waste circuit boards, as a preferred embodiment, the second crusher is a hammer mill.

上述用于废旧线路板回收的成套处理设备中,作为一种优选实施方式, 所述第二分选机包括气流跳汰分选机和/或涡电流分选机。In the above-mentioned complete set of processing equipment for recycling waste circuit boards, as a preferred embodiment, the second separator includes an air jig separator and/or an eddy current separator.

上述用于废旧线路板回收的成套处理设备中,作为一种优选实施方式, 所述除尘装置包括除尘设备,所述除尘设备的入口分别与所述第一破碎机以 及所述第二破碎机的灰尘出口相连;优选地,所述除尘设备包括Z型筛、多 锥筛、旋风式除尘器和喷气式过滤器。In the above-mentioned complete set of processing equipment for recycling waste circuit boards, as a preferred embodiment, the dust removal device includes dust removal equipment, and the inlet of the dust removal equipment is connected to the first crusher and the second crusher respectively. The dust outlet is connected; preferably, the dust removal equipment includes a Z-type sieve, a multi-cone sieve, a cyclone dust collector and a jet filter.

上述用于废旧线路板回收的成套处理设备中,作为一种优选实施方式, 所述成套处理设备中各机台之间采用皮带输送机输送物料;优选地,所述皮 带输送机使用人字型橡胶皮带,且在所述皮带输送机上设有防护罩。In the above complete set of processing equipment for recycling waste circuit boards, as a preferred embodiment, a belt conveyor is used to transport materials between the machines in the complete set of processing equipment; preferably, the belt conveyor uses a herringbone Type rubber belt, and a protective cover is provided on the belt conveyor.

一种用于废旧线路板回收的处理方法,包括如下步骤:A processing method for recycling waste circuit boards, comprising the steps of:

预处理步骤:将不同种类的废旧线路板进行预处理;Pretreatment step: pretreating different types of waste circuit boards;

油化裂解步骤:将经所述预处理步骤处理后得到的废旧线路板物料进行 裂解油化处理,冷却后得到再生油和金属与玻璃纤维混合物;Oily cracking step: subjecting the waste circuit board material obtained after the pretreatment step to cracking and oily treatment, and obtain regenerated oil and a mixture of metal and glass fiber after cooling;

粉碎和分选步骤:将通过所述油化裂解步骤得到的金属与玻璃纤维混合 物先进行粉碎处理,然后进行分选处理,分别得到不同的回收材料。Crushing and sorting step: the metal and glass fiber mixture obtained through the oil cracking step is first pulverized, and then sorted to obtain different recycled materials.

上述用于废旧线路板回收的处理方法,作为一种优选实施方式,所述预 处理步骤包括第一预处理步骤和/或第二预处理步骤;其中,The above-mentioned treatment method for recycling waste circuit boards, as a preferred embodiment, the pretreatment step includes a first pretreatment step and/or a second pretreatment step; wherein,

所述第一预处理步骤为脱锡步骤,通过脱锡机将电子元件从废旧线路板 上脱离下来,得到光板电路板;The first pretreatment step is a tin removal step, and the electronic components are separated from the waste circuit board by a tin removal machine to obtain a light board circuit board;

所述第二预处理步骤包括如下子步骤:子步骤一,将含线路板的电子废 弃物进行破碎处理,以便将所述含线路板的电子废弃物中的金属和非金属进 行拆分、打散;子步骤二:将所述子步骤一得到的废旧线路板物料进行筛分 过滤得到一定粒径的破碎物料;优选地,所述破碎处理采用链式破碎机进行; 更优选地,所述第二预处理步骤中的子步骤二之前还有除铁子步骤和人工分 选的子步骤;进一步优选地,用磁选机除铁,通过人工分选的方式将>100mm 的物料分选出来;更进一步地,所述子步骤一中可使含线路板的电子废弃物破碎成小于50mm×50mm的块料,经所述子步骤处理后得到的破碎物料的 颗粒直径小于20mm~40mm。The second pretreatment step includes the following sub-steps: Sub-step 1, crushing the electronic waste containing circuit boards, so as to separate the metal and non-metal in the electronic waste containing circuit boards , breaking up; sub-step 2: sieving and filtering the waste circuit board material obtained in the sub-step 1 to obtain broken materials with a certain particle size; preferably, the crushing process is carried out using a chain crusher; more preferably, Before the sub-step 2 in the second pretreatment step, there are sub-steps of iron removal and manual sorting; further preferably, magnetic separator is used for iron removal, and the material of >100mm is separated by manual sorting selected; furthermore, in the first substep, the electronic waste containing the circuit board can be broken into blocks smaller than 50mm×50mm, and the particle diameter of the broken material obtained after the substep treatment is less than 20mm~40mm .

上述用于废旧线路板回收的处理方法,作为一种优选实施方式,所述裂 解油化步骤具体包括如下子步骤:The above-mentioned treatment method for the recovery of waste circuit boards, as a preferred embodiment, the cracking and oiling step specifically includes the following sub-steps:

裂解子步骤,将经所述预处理步骤处理后得到的废旧线路板物料加热进 行裂解反应,得到热裂解气和金属与玻璃纤维混合物;The cracking sub-step is to heat the waste circuit board material obtained after the pretreatment step to carry out cracking reaction to obtain pyrolysis gas and a mixture of metal and glass fiber;

改质子步骤,将所述裂解子步骤得到的热裂解气在催化剂的作用下,进 行改质,即将长碳链切断为短碳链;In the step of modifying the proton, the pyrolysis gas obtained in the cracking sub-step is modified under the action of a catalyst, that is, the long carbon chain is cut into a short carbon chain;

冷却子步骤,经所述改质子步骤的热裂解气进行冷却液化处理,得到液 态的再生油和废气;Cooling sub-step, cooling and liquefying the pyrolysis gas in the proton-modifying step to obtain liquid regenerated oil and waste gas;

优选地,所述裂解子步骤中加热的温度为400-600℃,压力≤0.05Mpa;Preferably, the heating temperature in the cracking sub-step is 400-600°C, and the pressure is ≤0.05Mpa;

所述冷却子步骤中,所述再生油中轻油、重油独立回收,所述废气经热 燃烧处理达标后排放,所述燃烧处理的温度优选为250℃-1050℃。In the cooling sub-step, the light oil and heavy oil in the regenerated oil are recovered independently, and the waste gas is discharged after thermal combustion treatment reaches the standard, and the temperature of the combustion treatment is preferably 250°C-1050°C.

上述用于废旧线路板回收的处理方法,作为一种优选实施方式,所述粉 碎和分选步骤具体包括如下子步骤:The above-mentioned processing method for recycling waste circuit boards, as a preferred embodiment, the crushing and sorting steps specifically include the following sub-steps:

粉碎子步骤,将所述裂解油化步骤产出的金属与玻璃纤维混合物进行粉 碎处理;Pulverizing sub-step, pulverizing the metal and glass fiber mixture produced in the cracking and oiling step;

分选子步骤,首先将经所述粉碎子步骤处理的物料经气流跳汰分选和/ 或涡电流分选分别得到混合金属产品、玻璃纤维和粉尘;然后所述粉尘通过 静电分选分别得到玻璃纤维和金属粉末;In the sorting sub-step, first, the materials processed in the crushing sub-step are separated by air-flow jigging and/or eddy current separation to obtain mixed metal products, glass fibers and dust; then the dust is obtained by electrostatic separation Glass fibers and metal powders;

优选地,所述粉碎处理采用锤磨机进行;Preferably, the crushing treatment is carried out using a hammer mill;

更优选地,所述分选子步骤之前还有除铁子步骤;More preferably, there is an iron removal sub-step before the sorting sub-step;

进一步优选地,采用气流跳汰分选时,如果经所述粉碎子步骤处理后的 物料中含有铝、红色金属、塑料时,需要进行二次分选。Further preferably, when adopting airflow jigging separation, if the material after the pulverization sub-step process contains aluminum, red metal, plastics, secondary separation is required.

上述用于废旧线路板回收的处理方法,作为一种优选实施方式,处理方 法还包括除尘步骤,通过除尘设备处理所述预处理步骤、和所述粉碎和分选 步骤中产生的灰尘;更优选地,所述第二预处理步骤进行破碎处理时、所述 粉碎和分选步骤中进行粉碎处理时产生的灰尘,都送入所述除尘装置进行除 尘处理使其达标排放。The above-mentioned processing method for recycling waste circuit boards, as a preferred embodiment, the processing method also includes a dust removal step, and the dust generated in the pretreatment step and the crushing and sorting step is processed by dust removal equipment; more Preferably, the dust generated during the crushing process in the second pretreatment step and the crushing process in the crushing and sorting steps is sent to the dust removal device for dust removal treatment so that it can be discharged up to standard.

本发明提供的技术方案带来的有益效果是:The beneficial effects brought by the technical scheme provided by the invention are:

1)分解效果好:将废旧线路板生产成重油和轻油,真正实现资源循环利 用,反应温度在500℃,不会产生二噁英等有害气体产生;同时可以使用本 身产生的再生油进行生产,减少了运行成本;1) The decomposition effect is good: the waste circuit board is produced into heavy oil and light oil, and the recycling of resources is truly realized. The reaction temperature is 500 ° C, and no harmful gases such as dioxin will be produced; at the same time, the recycled oil produced by itself can be used production, reducing operating costs;

3)安全性高:可以通过填充氮气紧急停止反应;通过二次燃烧可以将一 些温室气体分解;3) High safety: the reaction can be stopped urgently by filling nitrogen; some greenhouse gases can be decomposed by secondary combustion;

4)使用链式破碎机来拆解物料需要人工为7~9名,可以代替原来80~ 100名工人手工拆解,大大提高生产效率,避免了工人生产过程接触到有毒 有害物质;4) Using a chain crusher to dismantle materials requires 7 to 9 workers, which can replace the original 80 to 100 workers for manual dismantling, greatly improving production efficiency and avoiding workers' exposure to toxic and harmful substances during production;

5)环保效益高:生产过程中,无粉尘污染,生产过程中不产生废水、废 气等二次污染;5) High environmental benefits: no dust pollution during the production process, and no secondary pollution such as waste water and waste gas during the production process;

6)可以连续运行120小时,能耗低、产能高;6) It can run continuously for 120 hours, with low energy consumption and high production capacity;

7)金属回收率高,回收率可达到95%-98%,非金属粉末中金属含量< 1%。金属可直接分为铜、铁、铝等,且金属纯度高达99%远超国内物理分选 设备的纯净度(国内在80%以上),避免非金属混入金属中,造成二次污染。7) The metal recovery rate is high, the recovery rate can reach 95%-98%, and the metal content in the non-metallic powder is less than 1%. Metals can be directly divided into copper, iron, aluminum, etc., and the purity of metals is as high as 99%, far exceeding the purity of domestic physical separation equipment (more than 80% in China), so as to avoid the mixing of non-metals into metals and cause secondary pollution.

附图说明Description of drawings

图1为本发明优选实施例中的用于废旧线路板回收的成套处理设备的工 艺流程图及结构示意图;Fig. 1 is the process flow diagram and the structural representation of the complete set of processing equipment used for the recovery of waste circuit boards in the preferred embodiment of the present invention;

图中:1-脱锡机,3-第一破碎机,4-第一磁选机(即1#磁选机),5-第 一分选机,6-热分解槽,7-触媒槽,8-冷却装置,9-气体燃烧器、10-第二破 碎机,11-第二磁选机(即2#磁选机),12-第二分选机,13-静电分选机,14- 除尘设备,15-第一皮带输送机,16-第二皮带输送机。In the figure: 1-Tin removal machine, 3-The first crusher, 4-The first magnetic separator (i.e. 1# magnetic separator), 5-The first separator, 6-Thermolysis tank, 7-Catalyst tank , 8-cooling device, 9-gas burner, 10-second crusher, 11-second magnetic separator (i.e. 2# magnetic separator), 12-second separator, 13-electrostatic separator , 14- dust removal equipment, 15- the first belt conveyor, 16- the second belt conveyor.

具体实施方式Detailed ways

为使本发明的目的、技术方案和优点更加清楚,下面将结合附图对本发 明实施方式作进一步地详细描述。In order to make the purpose, technical solutions and advantages of the present invention clearer, the following will further describe in detail the embodiments of the present invention in conjunction with the accompanying drawings.

需要说明的是,在不冲突的情况下,本发明中的具体实施方式中的特征 可以相互组合。It should be noted that, in the case of no conflict, the features in the specific implementation manners of the present invention can be combined with each other.

在本发明的描述中,术语“上”、“下”、“前”、“后”、“左”、 “右”、“竖直”、“水平”、“顶”、“底”等指示的方位或位置关系为 基于附图所示的方位或位置关系,仅是为了便于描述本发明而不是要求本发 明必须以特定的方位构造和操作,因此不能理解为对本发明的限制。在本发 明的描述中,需要说明的是,除非另有明确的规定和限定,术语“安装”、 “相连”、“连接”应做广义理解,例如,可以是固定连接,也可以是可拆 卸连接,或一体地连接;可以是机械连接,也可以是电连接;可以是直接相 连,也可以通过中间媒介间接相连,可以是两个元件内部的连通。对于电和 通信领域而言,可以是有线连接,也可以是无线连接。对于本领域的普通技 术人员而言,可以具体情况理解上述术语在本发明中的具体含义。In the description of the present invention, the terms "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom" etc. indicate The orientation or positional relationship shown in the drawings is based on the orientation or positional relationship shown in the drawings, which is only for the convenience of describing the present invention and does not require that the present invention must be constructed and operated in a specific orientation, so it should not be construed as a limitation of the present invention. In the description of the present invention, it should be noted that, unless otherwise clearly stipulated and limited, the terms "installation", "connection" and "connection" should be understood in a broad sense, for example, it can be a fixed connection or a flexible connection. Detachable connection, or integral connection; it can be mechanical connection or electrical connection; it can be direct connection or indirect connection through an intermediary, and it can be the internal communication of two components. For electricity and communication, it can be a wired connection or a wireless connection. For those of ordinary skill in the art, the specific meanings of the above terms in the present invention can be understood in specific situations.

本发明提供用于废旧线路板回收的成套处理设备的一种优选实施方式, 参见图1,主要包括预处理装置、裂解油化装置、破碎/分选装置、除尘装置, 下面对以上部件及其连接关系一一进行说明。The present invention provides a preferred embodiment of a complete set of processing equipment for recycling waste circuit boards, see Figure 1, mainly including a pretreatment device, a cracking and oiling device, a crushing/sorting device, and a dust removal device. The above parts and The connections are explained one by one.

预处理装置,入口与进料装置的出口连接,用来对来自进料装置的废旧 线路板或含废旧线路板的电子废弃物进行预处理。具体地,预处理装置包括: 第一预处理装置和/或第二预处理装置;其中,第一预处理装置包括脱锡机1, 脱锡机1用于对废旧线路板进行预处理,即将锡、电子元件从废旧线路板上 脱离下来得到光板电路板,光板电路板可以直接送入裂解油化装置,锡、电 子元件可以回收;第二预处理装置包括第一破碎机3、第一分选机5和人工 分选平台,其中,第一破碎机3用于对含废旧线路板的电子废弃物进行破碎; 第一分选机5设置于第一破碎机3之后,用于对第一破碎机3破碎后的物料 进行筛分过滤,以利于后续的热裂解;人工分选平台设置于第一分选机5之 前或之后,用于通过人工分选出较大的物料。优选地,第二预处理装置还包 括:第一磁选机4(即图1中的1#磁选机),第一磁选机4设置于第一破碎 机3和第一分选机5之间,用于去除第一破碎机3破碎后的物料中的磁性物 质比如铁。本发明中预处理装置中,第一破碎机3可以是一般的破碎设备, 但优选为链式破碎机,其不但可以处理线路板而且可以直接处理小电子废弃 物,可以将来料拆开、打散、破碎,将连接的电线和塑料分开;第一分选机 5可以是一般的分选设备,优选为波纹筛选槽或滚筒筛。优选地,经第一破 碎机3处理后的物料为小于50mm×50mm的块料;经第一分选机5筛选出 破碎物料的颗粒直径小于20mm~40mm(比如22mm、25mm、28mm、32mm、35mm、38mm),人工分选平台处通过人工分选出大于100mm的物料。The pretreatment device, the inlet is connected with the outlet of the feeding device, and is used to pretreat the waste circuit boards from the feeding device or electronic waste containing waste circuit boards. Specifically, the pretreatment device includes: a first pretreatment device and/or a second pretreatment device; wherein, the first pretreatment device includes a tin remover 1, and the tin remover 1 is used to pretreat waste circuit boards, namely Tin and electronic components are separated from waste circuit boards to obtain bare circuit boards, which can be directly sent to the cracking and oiling device, and tin and electronic components can be recycled; the second pretreatment device includes the first crusher 3, the first Sorting machine 5 and artificial sorting platform, wherein, the first crusher 3 is used for crushing the electronic waste containing waste and old circuit boards; The first sorting machine 5 is arranged after the first crusher 3, for The materials crushed by a crusher 3 are screened and filtered to facilitate subsequent thermal cracking; the manual sorting platform is arranged before or after the first sorting machine 5 for manually sorting larger materials. Preferably, the second pretreatment device also includes: the first magnetic separator 4 (i.e. the 1# magnetic separator in Fig. 1), the first magnetic separator 4 is arranged on the first crusher 3 and the first separator 5, used to remove magnetic substances such as iron in the material crushed by the first crusher 3. In the pretreatment device in the present invention, the first crusher 3 can be general crushing equipment, but is preferably a chain crusher, which can not only process circuit boards but also directly process small electronic wastes, and can disassemble and break incoming materials. Scatter and crush, and separate the connected wires and plastics; the first sorting machine 5 can be a general sorting device, preferably a corrugated screening tank or a drum screen. Preferably, the material processed by the first crusher 3 is a block material smaller than 50mm×50mm; the particle diameter of the crushed material screened out by the first sorting machine 5 is less than 20mm to 40mm (such as 22mm, 25mm, 28mm, 32mm , 35mm, 38mm), the artificial sorting platform manually sorts out materials larger than 100mm.

裂解油化装置,入口与预处理装置的物料出口连接,用于对预处理装置 输出的废旧线路板物料(比如经分选后的破碎物料或者脱锡机1处理后的光 板线路板)进行裂解油化处理,分别得到再生油以及金属与玻璃纤维的混合 物。具体地,裂解油化装置包括:热分解槽6、触媒槽7、冷却装置8、储油 箱和气体燃烧器9,其中,热分解槽6的入口与预处理装置的出口连接,用 于将预处理装置输出的废旧线路板物料进行加热裂解处理,分别得到热裂解 气和金属与玻璃纤维混合物;触媒槽7的入口与热分解槽的气体出口连接, 来自热分解槽的热裂解气在触媒槽7内的催化剂的作用下进行改质(即长碳 链切断为短碳链);冷却装置8的入口与触媒槽7的出口连接,改质后的热 裂解气在冷却装置8中进行冷却、液化后油气分离;储油箱的入口与冷却装 置8的油出口连接用于回收再生油;气体燃烧器9的入口与冷却装置8的气 体出口连接,用于对冷却装置8排出的气体进行燃烧处理,燃烧处理后的气体达标排放。在本发明的优选实施例中,热分解槽6包括热解槽、加热槽和 反转装置,其中,热解槽是用于容纳废旧线路板物料的场所,加热槽用于给 热解槽加热使热解槽发生裂解反应,反转装置设置于所述加热槽和/或热解槽 外部,用于反转热解槽和加热槽,以便将热解槽中的热裂解反应后的固体物 料比如金属与玻璃纤维混合物倾倒出来。在本发明的优选实施例中,冷却装 置8为冷却塔,其内部设有气体冷却器、塔顶冷却器和冷却机兼循环槽,其 中,气体冷却器、塔顶冷却器用于冷却改质后的热裂解气,冷却机兼循环槽 用于回收油。在本发明的优选实施例中,气体燃烧器9可采用燃烧炉。加热 槽的热源可以是热裂解回收的再生油,也可以采用天然气。The cracking and oiling device, the inlet is connected to the material outlet of the pretreatment device, and is used to process the waste circuit board materials output by the pretreatment device (such as broken materials after sorting or bare circuit boards processed by the tin removal machine 1). Cracking oil treatment to obtain regenerated oil and a mixture of metal and glass fiber. Specifically, the cracking and oiling device comprises: thermal decomposition tank 6, catalyst tank 7, cooling device 8, oil storage tank and gas burner 9, wherein, the inlet of thermal decomposition tank 6 is connected with the outlet of pretreatment device, is used for The waste circuit board material output by the pretreatment device is subjected to thermal cracking treatment to obtain pyrolysis gas and a mixture of metal and glass fiber respectively; the inlet of the catalyst tank 7 is connected to the gas outlet of the pyrolysis tank, and the pyrolysis gas from the pyrolysis tank passes through the catalyst Under the effect of the catalyzer in the groove 7, upgrade (i.e. long carbon chain is cut into short carbon chain); , oil and gas separation after liquefaction; the inlet of the oil storage tank is connected to the oil outlet of the cooling device 8 for reclaiming regenerated oil; the inlet of the gas burner 9 is connected to the gas outlet of the cooling device 8 for the gas discharged from the cooling device 8 Combustion treatment is carried out, and the gas after combustion treatment is discharged up to the standard. In a preferred embodiment of the present invention, the pyrolysis tank 6 includes a pyrolysis tank, a heating tank and an inversion device, wherein the pyrolysis tank is a place for accommodating waste circuit board materials, and the heating tank is used to heat the pyrolysis tank The cracking reaction occurs in the pyrolysis tank, and the inversion device is arranged outside the heating tank and/or the pyrolysis tank for reversing the pyrolysis tank and the heating tank, so that the solid matter after the pyrolysis reaction in the pyrolysis tank Materials such as metal and fiberglass mixtures are poured out. In a preferred embodiment of the present invention, the cooling device 8 is a cooling tower, which is internally provided with a gas cooler, a tower top cooler and a cooling machine and a circulation tank, wherein the gas cooler and the tower top cooler are used for cooling the improved The degraded pyrolysis gas, the cooler and circulation tank are used to recover the oil. In a preferred embodiment of the present invention, the gas burner 9 can be a combustion furnace. The heat source of the heating tank can be regenerated oil recovered by pyrolysis, or natural gas.

具体地,本发明的裂解油化装置,入口与第二预处理装置的物料出口连 接,还与第一预处理装置(在本发明的实施例中即为脱锡机1)出口连接或 连通,在处理废旧线路板时,废旧线路板经脱锡机1处理后得到的光板线路 板自脱锡机1的出口输送至裂解油化装置中,在本发明的实施例中,即将脱 锡机1得到的光板线路板输送至热分解槽6的热解槽中,进行上述的加热裂 解处理。当处理的原料为含有废旧线路板的电子废弃物时,该废弃物经第一 分选机5分选后的物料进入热分解槽6中进行上述加热裂解处理。Specifically, in the cracking and oiling device of the present invention, the inlet is connected to the material outlet of the second pretreatment device, and is also connected or communicated with the outlet of the first pretreatment device (being the detinning machine 1 in the embodiment of the present invention) , when processing waste and old circuit boards, the bare circuit boards obtained after the waste and old circuit boards are processed by the tin removal machine 1 are transported to the cracking and oiling device from the outlet of the tin removal machine 1. In an embodiment of the present invention, the tin removal machine is about to 1. The bare circuit board obtained is delivered to the pyrolysis tank of the thermal decomposition tank 6, and the above-mentioned thermal cracking process is carried out. When the processed raw material is electronic waste containing waste and old circuit boards, the waste is sorted by the first sorter 5 into the thermal decomposition tank 6 to carry out the above-mentioned thermal cracking treatment.

破碎/分选装置,入口与裂解油化装置的出口连接,用于对裂解油化装置 输出的金属与玻璃纤维混合物进行进一步的破碎和分选处理。具体地,破碎/ 分选装置包括:第二破碎机10、第二分选机12、静电分选机13,其中,第 二破碎机10的入口与裂解油化装置的出口连接,用于对裂解油化装置输出的 金属与玻璃纤维混合物进行进一步的粉碎处理;第二分选机12的入口与第二 破碎机10出口连接,用于分离第二破碎机10输出的物料中的重物(如金属, 如铜、铝、不锈钢等)和轻物(如塑料,如玻璃纤维);静电分选机13的入 口与第二分选机12的粉尘出口连接,用于分离粉尘中的玻璃纤维和金属粉末。 优选地,破碎/分选装置还包括:第二磁选机11(即图1中的2#磁选机), 设置于第二破碎机10和第二分选机12之间,用于除铁。优选地,第二破碎 机10为锤磨机,锤磨机与一般破碎机相比处理效果更优;优选地,第二分选 机12包括气流跳汰分选机和/或涡电流分选机,气流跳汰分选机是按比重分 选,涡电流分选机是按磁性分选,可以同时设置但不同时开工,而是根据物 料情况进行选择使用。在本发明的优选实施例中,破碎/分选装置包括:锤磨 机、第二磁选机11、气流跳汰分选机、静电分选机13,其中锤磨机与热分解 槽6连接,用于对来自热分解槽6的金属与玻璃纤维混合物进行进一步的粉 碎,通过第二磁选机11分离出粉碎后的物料中的铁,再通过气流跳汰分选机 将物料中的有色金属(如铜、铝)和玻璃纤维分离开,最后将气流跳汰分选 机中的粉尘引入静电分选机13中,经静电分选机13从中分离出金属粉末和 玻璃纤维。Crushing/separating device, the inlet is connected to the outlet of the cracking and oiling device, which is used for further crushing and sorting treatment of the metal and glass fiber mixture output from the cracking and oiling device. Specifically, the crushing/separating device includes: a second crusher 10, a second separator 12, and an electrostatic separator 13, wherein the inlet of the second crusher 10 is connected with the outlet of the cracking oilification device for The metal and glass fiber mixture output from the pyrolysis oilification device are further pulverized; the inlet of the second classifier 12 is connected to the outlet of the second crusher 10, and is used to separate the heavy objects in the output of the second crusher 10 ( Such as metals, such as copper, aluminum, stainless steel, etc.) and light objects (such as plastics, such as glass fibers); the inlet of the electrostatic separator 13 is connected with the dust outlet of the second separator 12 for separating the glass in the dust Fiber and metal powder. Preferably, the crushing/separating device also includes: the second magnetic separator 11 (i.e. 2# magnetic separator in Fig. 1), arranged between the second crusher 10 and the second separator 12, for removing iron. Preferably, the second crusher 10 is a hammer mill, and the hammer mill has a better treatment effect than a general crusher; preferably, the second separator 12 includes an airflow jigging separator and/or eddy current separation The airflow jigging separator is based on specific gravity, and the eddy current separator is based on magnetic separation. They can be set at the same time but not started at the same time, but can be selected and used according to the material condition. In a preferred embodiment of the present invention, the crushing/separating device includes: a hammer mill, a second magnetic separator 11, an airflow jigging separator, and an electrostatic separator 13, wherein the hammer mill is connected with the thermal decomposition tank 6 , used to further pulverize the metal and glass fiber mixture from the thermal decomposition tank 6, separate the iron in the pulverized material through the second magnetic separator 11, and then separate the iron in the material through the air jig separator Non-ferrous metals (such as copper, aluminum) and glass fibers are separated, and finally the dust in the airflow jigging separator is introduced into the electrostatic separator 13, and the metal powder and glass fibers are separated by the electrostatic separator 13.

除尘装置,入口分别与预处理装置和破碎/分选装置的灰尘出口连接,用 于处理灰尘使空气达标排放。具体地,除尘装置包括除尘设备14,除尘设备 14的入口分别与第一破碎机3以及第二破碎机10的灰尘出口相连,用以排 出多余的空气、灰尘,减少扬尘量,提升工作环境。在本发明的优选实施例 中,除尘设备14包括Z型筛、多锥筛、旋风式除尘器和喷气式过滤器,Z 型筛、多锥筛、旋风式除尘器用于分离出不同轻重、不同颗粒的灰尘,喷气式过滤器用于进行最终的除尘。The dust removal device, the inlet is respectively connected with the dust outlet of the pretreatment device and the crushing/sorting device, which is used to treat the dust and make the air discharge up to standard. Specifically, the dust removal device includes a dust removal device 14, and the inlet of the dust removal device 14 is connected with the dust outlets of the first crusher 3 and the second crusher 10 respectively, so as to discharge excess air and dust, reduce the amount of dust, and improve the working environment . In a preferred embodiment of the present invention, the dust removal equipment 14 includes a Z-type sieve, a multi-cone sieve, a cyclone dust collector and a jet filter, and a Z-type sieve, a multi-cone sieve, and a cyclone dust collector are used to separate For particulate dust, jet filters are used for final dust removal.

优选地,上述成套处理设备中各机台之间采用皮带输送机输送物料。在 本发明的优选实施例中,为避免出料爬升时物料下滑,皮带输送机使用人字 型橡胶皮带;为了避免外物进入还对皮带输送机进行了封闭式处理,即设置 封闭式缓冲处理装置,比如,在皮带输送机上设有防护罩。Preferably, belt conveyors are used to transport materials between the machines in the above-mentioned complete set of processing equipment. In the preferred embodiment of the present invention, in order to avoid material slipping when the material is climbing up, the belt conveyor uses a herringbone rubber belt; in order to avoid the entry of foreign objects, the belt conveyor is also subjected to closed treatment, that is, a closed buffer treatment is set Devices, for example, with protective covers on belt conveyors.

本发明还提供一种用于废旧线路板回收的处理方法,包括如下步骤:The present invention also provides a processing method for recycling waste circuit boards, comprising the following steps:

预处理步骤:将不同种类的废旧线路板进行预处理;Pretreatment step: pretreating different types of waste circuit boards;

油化裂解步骤:将经预处理后得到的PCB废料进行裂解油化处理,冷却 后得到再生油和金属与玻璃纤维混合物;Oil cracking step: the pretreated PCB waste is subjected to cracking and oil treatment, and after cooling, regenerated oil and a mixture of metal and glass fiber are obtained;

粉碎和分选步骤:将通过油化裂解步骤得到的金属与玻璃纤维混合物先 进行粉碎处理,然后进行分选处理,分别得到不同的回收材料。Crushing and sorting steps: the metal and glass fiber mixture obtained through the oil cracking step is first pulverized and then sorted to obtain different recycled materials.

上述用于废旧线路板回收的处理方法中,作为一种优选实施方式,预处 理步骤包括第一预处理步骤和/或第二预处理步骤;其中,In the above-mentioned treatment method for recycling waste circuit boards, as a preferred embodiment, the pretreatment step includes a first pretreatment step and/or a second pretreatment step; wherein,

第一预处理步骤为脱锡步骤,即通过脱锡机将锡和电子元件从废旧线路 板上脱离下来,其中锡、电子元件(锡、铅、镍等重金属基本在电子元件中) 去除回收,留下光板电路板可直接进入裂解油化步骤进行裂解油化处理;The first pretreatment step is the detinning step, that is, the tin and electronic components are separated from the waste circuit board through the detinning machine, wherein tin and electronic components (heavy metals such as tin, lead, nickel, etc. are basically in the electronic components) are removed and recycled, Leaving the bare circuit board can directly enter the cracking and oiling step for cracking and oiling treatment;

第二预处理步骤包括如下子步骤:子步骤一,将含线路板的电子废弃物 进行破碎处理,以便将所述含线路板的电子废弃物中的铁等金属和塑料等非 金属进行拆分、打散;子步骤二:将子步骤一得到的废旧线路板进行筛分过 滤得到一定粒径的破碎物料;优选地,所述破碎处理采用链式破碎机进行。 优选地,所述第二预处理步骤中的子步骤二之前还有除铁子步骤和人工分选 的子步骤。更优选地,用磁选机除铁,通过人工分选的方式将>100mm的物 料分选出来。进一步优选地,子步骤一中可使含线路板的电子废弃物破碎成 小于50mm×50mm的块料,经过子步骤二的筛分过滤处理后,破碎物料的 颗粒直径小于20mm~40mm(比如22mm、25mm、28mm、32mm、35mm、 38mm)。The second pretreatment step includes the following sub-steps: sub-step 1, crushing the electronic waste containing circuit boards, so that metals such as iron and non-metals such as plastics in the electronic waste containing circuit boards are separated , breaking up; sub-step two: screening and filtering the waste circuit boards obtained in sub-step one to obtain broken materials of a certain particle size; preferably, the crushing process is carried out using a chain crusher. Preferably, there are sub-steps of iron removal sub-step and manual sorting before sub-step 2 in the second pretreatment step. More preferably, magnetic separator is used to remove iron, and the material >100mm is sorted out by means of manual sorting. Further preferably, in the sub-step 1, the electronic waste containing the circuit board can be broken into blocks smaller than 50mm×50mm, and after the sieving and filtering in the sub-step 2, the particle diameter of the broken material is less than 20mm-40mm (such as 22mm , 25mm, 28mm, 32mm, 35mm, 38mm).

上述用于废旧线路板回收的处理方法中,作为一种优选实施方式,所述 裂解油化步骤具体包括如下子步骤:In the above-mentioned treatment method for recycling waste circuit boards, as a preferred embodiment, the cracking and oiling step specifically includes the following sub-steps:

裂解子步骤,将经预处理后得到的PCB废料加热进行裂解反应,得到热 裂解气和金属与玻璃纤维混合物;The pyrolysis sub-step is to heat the PCB waste obtained after pretreatment to carry out the pyrolysis reaction to obtain pyrolysis gas and a mixture of metal and glass fiber;

改质子步骤,将裂解子步骤得到的热裂解气在催化剂的作用下,进行改 质,即将长碳链切断为短碳链;In the proton modification step, the pyrolysis gas obtained in the cracking sub-step is modified under the action of a catalyst, that is, the long carbon chain is cut into a short carbon chain;

冷却子步骤,经改质子步骤的热裂解气进行冷却液化处理,得到液态的 再生油和废气。In the cooling sub-step, the pyrolysis gas in the proton modification step is cooled and liquefied to obtain liquid regenerated oil and waste gas.

上述用于废旧线路板回收的处理方法中,作为一种优选实施方式,所述 裂解油化步骤中,裂解子步骤中加热的温度为400-600℃(比如410℃、420℃、 450℃、480℃、520℃、550℃、580℃、590℃)℃,压力≤0.05Mpa。裂解 步骤是在隔绝空气的条件下加热PCB废料,控制温度和压力,使PCB废料 中的有机物质被分解转化成油气,经冷凝收集后可回收。裂解子步骤是在无 氧的条件下进行的,因此可以抑制二噁英、呋喃的产生,废气产生量少,对环境污染小。In the above-mentioned treatment method for recycling waste circuit boards, as a preferred embodiment, in the cracking and oiling step, the heating temperature in the cracking sub-step is 400-600°C (such as 410°C, 420°C, 450°C, 480°C, 520°C, 550°C, 580°C, 590°C)°C, pressure ≤0.05Mpa. The cracking step is to heat the PCB waste under the condition of isolating the air, control the temperature and pressure, so that the organic matter in the PCB waste is decomposed and converted into oil and gas, which can be recycled after being condensed and collected. The cracking sub-step is carried out under anaerobic conditions, so the production of dioxins and furans can be suppressed, the amount of waste gas produced is small, and the environmental pollution is small.

上述用于废旧线路板回收的处理方法中,作为一种优选实施方式,冷却 子步骤中,在油/气分离后,其中,再生油中轻油、重油独立回收,废气经热 燃烧处理达标后排放。油回收过程中产生的未冷却的尾气(即废气),主要 包括甲烷、乙烷、乙烯、丙烷、丙烯、丁烯、丁烷等,经过气体燃烧器燃烧 后达标排放,燃烧炉温度在250℃-1050℃。In the above-mentioned treatment method for recycling waste circuit boards, as a preferred embodiment, in the cooling sub-step, after the oil/gas separation, wherein the light oil and heavy oil in the regenerated oil are recovered independently, and the waste gas is treated by thermal combustion after reaching the standard emission. The uncooled tail gas (i.e. exhaust gas) produced during the oil recovery process mainly includes methane, ethane, ethylene, propane, propylene, butene, butane, etc., and is discharged after being burned by a gas burner. The temperature of the burner is 250°C -1050°C.

上述用于废旧线路板回收的处理方法中,作为一种优选实施方式,所述 粉碎和分选步骤具体包括如下子步骤:In the above-mentioned processing method for recycling waste circuit boards, as a preferred embodiment, the crushing and sorting steps specifically include the following sub-steps:

粉碎子步骤,将所述裂解油化步骤产出的金属与玻璃纤维混合物进行粉 碎处理;优选地,所述粉碎处理采用锤磨机进行,利用不同金属具不同延展 性特性将其搓成种类不同、大小不同的金属球。The pulverization sub-step is to pulverize the metal and glass fiber mixture produced in the cracking and oiling step; preferably, the pulverization treatment is carried out with a hammer mill, and the different ductility characteristics of different metals are used to knead them into types Metal balls of different sizes.

分选子步骤,首先将经粉碎子步骤处理的物料经气流跳汰分选和/或涡电 流分选分别得到混合金属产品(如铜、铝、不锈钢)、玻璃纤维和粉尘;然 后粉尘通过静电分选分别得到玻璃纤维和金属粉末(如铜粉)。通过两道分 选将玻璃纤维与金属分离,分选出金属部分提高金属回收率,同时玻璃纤维 可以再次出售,有利于资源有效利用。更优选地,所述分选子步骤之前还有 除铁子步骤。更优选地,采用气流跳汰分选时,如果经粉碎子步骤处理的物 料中含有铝、红色金属(主要是指铜,还有少量锌,金、银等贵金属)、塑 料时,需要进行二次分选。Sorting sub-step, at first the materials processed by the crushing sub-step are separated by air flow jigging and/or eddy current separation to obtain mixed metal products (such as copper, aluminum, stainless steel), glass fiber and dust respectively; then dust Glass fiber and metal powder (such as copper powder) are obtained respectively by electrostatic separation. The glass fiber is separated from the metal through two sorting steps, and the metal part is sorted out to improve the metal recovery rate. At the same time, the glass fiber can be sold again, which is conducive to the effective utilization of resources. More preferably, there is also an iron removal sub-step before the sorting sub-step. More preferably, when air-flow jigging is adopted, if the material processed by the pulverizing sub-step contains aluminum, red metal (mainly refers to copper, also has a small amount of zinc, gold, silver and other precious metals), plastics, need Perform secondary sorting.

上述用于废旧线路板回收的处理方法中,作为一种优选实施方式,处理 方法还包括除尘步骤,通过除尘设备处理预处理步骤、粉碎和分选步骤中产 生的灰尘;更优选地,第二预处理步骤进行链式破碎时、以及粉碎和分选步 骤中粉碎处理时产生的灰尘,都送入除尘装置进行除尘处理后使其达标排放, 优选排出的气体含尘量低至10mg/m3In the above treatment method for recycling waste circuit boards, as a preferred embodiment, the treatment method also includes a dust removal step, and the dust generated in the pretreatment step, crushing and sorting steps is treated by dust removal equipment; more preferably, the second The dust generated during the chain crushing in the pretreatment step and the crushing process in the crushing and sorting steps are all sent to the dust removal device for dust removal treatment and then discharged up to the standard. The dust content of the discharged gas is preferably as low as 10mg/ m3 .

上述方法采用本发明的成套处理设备来完成,下面结合实施例,对本发 明的用于废旧线路板回收的成套处理设备及处理方法和用于废旧线路板回收 的处理方法进行说明。The above method is completed by the complete set of processing equipment of the present invention. The complete set of processing equipment and processing method for recycling waste circuit boards and the processing method for recycling waste circuit boards of the present invention will be described below in conjunction with the embodiments.

实施例Example

本优选实施例提供的用于废旧线路板回收的成套处理设备,结构如图1 所示,该设备的主要包括如下装置:脱锡机、磁选机、链式破碎机、波纹筛 选槽、热分解槽、触媒槽、冷却装置、储油箱、气体燃烧器(具体为燃烧炉)、 锤磨机、气流跳汰分选机、静电分选机、皮带输送机;上述装置均是市售产 品,具体如下:The complete set of processing equipment for the recycling of waste and old circuit boards provided by this preferred embodiment, the structure is as shown in Figure 1, and the equipment mainly includes the following devices: tin remover, magnetic separator, chain crusher, corrugated screening tank, Thermal decomposition tank, catalyst tank, cooling device, oil storage tank, gas burner (specifically combustion furnace), hammer mill, airflow jigging separator, electrostatic separator, belt conveyor; the above devices are commercially available products, as follows:

1)皮带输送机2条。用于输送各机台处放置的PCB物料,输送机长度 6000mm,为避免出料爬升时物料下滑,采用人字型黑色橡胶皮带,机身水 平仰角25度,机身材料使用20号钢材料,脚柱材料使用四方管,其头轮采 用磁性头轮,皮带线速度4455mm/min,使用电源AC3Φ×380V×50Hz之减速 马达驱动,处理能力在5000kg/hr以上。1) 2 belt conveyors. It is used to convey the PCB materials placed at each machine. The length of the conveyor is 6000mm. In order to avoid the material from falling when the discharge climbs, a herringbone black rubber belt is used. The horizontal elevation angle of the fuselage is 25 degrees, and the fuselage material is made of 20 steel materials , The foot column material is square tube, the head wheel is magnetic head wheel, the belt linear speed is 4455mm/min, and the power supply is AC3Φ×380V×50Hz deceleration motor drive, the processing capacity is above 5000kg/hr.

2)脱锡机1台。2) One desoldering machine.

3)带式磁选机3台,磁铁盘长宽不小于750*900mm,磁场强度不能低 于4000高斯。机架材料使用20号钢材料,皮带宽度是700mm,皮带材质是 双面橡胶材质包覆加强芯体。3) There are 3 belt magnetic separators, the length and width of the magnet discs are not less than 750*900mm, and the magnetic field strength cannot be lower than 4000 Gauss. The frame material is made of No. 20 steel material, the belt width is 700mm, and the belt material is double-sided rubber material covering the reinforced core.

4)链式破碎机1台。配有强大气流筛选功能的转子链式破碎机,其作用 是将废旧线路板破碎成小块料,其工作原理是通过对主动轴的动刀、从动轴 上的动刀与静刀对废旧电子线路板产生剪切作用,可使废旧电子线路板破碎 成小于50mm×50mm的块料。4) One chain crusher. The rotor chain crusher equipped with a powerful airflow screening function is used to crush waste circuit boards into small pieces. The electronic circuit board produces shearing action, which can break the waste electronic circuit board into pieces smaller than 50mm×50mm.

5)波纹筛选槽1台。5) One corrugated screening tank.

6)裂解油化装置。6) Cracking and oiling unit.

热分解槽:包括热解槽1个、加热槽1个和分解槽反转装置1个;热解 槽的反应罐的直径和高度800×2138mm,材质为304不锈钢,有效容量为 4.5m3;加热槽的炉直径和高度为600×3250mm,材质采用SS400+耐火保温 材料,采用油燃烧加热系统;分解槽反转装置长宽高3400×3800×5500mm, 材质为SS440,120℃反转。在设备的热分解槽被投入的废塑料等,加热分解 气体化。Pyrolysis tank: including one pyrolysis tank, one heating tank and one decomposition tank inversion device; the diameter and height of the reaction tank of the pyrolysis tank are 800×2138mm, the material is 304 stainless steel, and the effective capacity is 4.5m 3 ; The furnace diameter and height of the heating tank are 600×3250mm, the material is SS400+ refractory insulation material, and the oil combustion heating system is adopted; the length, width and height of the decomposition tank reversing device are 3400×3800×5500mm, the material is SS440, and it is reversed at 120°C. Waste plastics, etc. put into the thermal decomposition tank of the equipment are heated and decomposed and gasified.

触媒槽:触媒槽1个,反应器的直径和高度为770×885mm,材质为304 不锈钢,容量为0.35m3。热裂解气在触媒槽内的催化剂作用下,进行改质(长 碳链切断为短碳链)。Catalyst tank: 1 catalyst tank, the diameter and height of the reactor are 770×885mm, the material is 304 stainless steel, and the capacity is 0.35m 3 . Under the action of the catalyst in the catalyst tank, the pyrolysis gas is modified (long carbon chains are cut into short carbon chains).

冷却装置:冷却塔1个,长宽高为1400×31000×2275mm。循环水温 20℃;气体冷却器1个,直径和高度为712×2900mm,材质为304不锈钢、 SS440,采用油喷雾气体冷却法;塔顶冷却器1个,直径和高度为500× 2500mm,材质为304不锈钢、SS440,冷却能力46500大卡/H;冷却机兼循 环槽,长宽高900×1250×850mm,材质为304不锈钢,容量为0.75m3。冷 却器中进行冷却,液化,从而回收再生油。冷却回收分为两部分,即轻油、 重油独立回收。Cooling device: 1 cooling tower with a length, width and height of 1400×31000×2275mm. Circulating water temperature 20°C; 1 gas cooler with a diameter and height of 712×2900mm, made of 304 stainless steel and SS440, using oil spray gas cooling method; 1 tower cooler with a diameter and height of 500×2500mm, made of 304 stainless steel, SS440, cooling capacity 46500 kcal/H; cooling machine and circulation tank, length, width and height 900×1250×850mm, material is 304 stainless steel, capacity is 0.75m 3 . Cooling is carried out in the cooler, liquefied, and recycled oil is recovered. Cooling recovery is divided into two parts, that is, light oil and heavy oil are recovered independently.

油化装置架1个,材质为SS400(防锈)。One frame for oiling device, made of SS400 (anti-rust).

7)锤磨机1个:对裂解油化装置排出的固体物料即金属和玻璃纤维的混 合物进行进一步地破碎处理。利用不同金属具不同延展性特性将其搓成种类 不同、大小不同的金属球。7) One hammer mill: to further crush the solid material discharged from the pyrolysis oilification device, that is, the mixture of metal and glass fiber. Utilize the different ductility properties of different metals to knead them into metal balls of different types and sizes.

8)气流跳汰分选机1台。气流跳汰分选机可以根据物料的重量和颗粒构 成的差异,将重物(如金属)和轻物(如塑料)分选出来。物料沿着倾斜的 跳汰机平面作向上运动。通风器向物料运动的反方向吹风,使轻物料不能维 持向上运动而从气流跳汰分选机的下方出口出来,仅有重物会从上方出口出 来。气流跳汰分选机每次能分选两种物料。如果混合物料中含有如铝、红色 金属、塑料时,需要进行二次分选。在第一次分选时,能分选出重的金属和 轻的塑料。在二次分选时,可将相对较重的红色金属和相对轻的铝分选出来。8) One airflow jigging separator. The air jig separator can separate heavy objects (such as metal) and light objects (such as plastics) according to the weight of the material and the difference in particle composition. The material moves upward along the inclined jig plane. The ventilator blows air in the opposite direction of material movement, so that light materials cannot maintain upward movement and exit from the bottom of the air jig separator, and only heavy materials will exit from the top. The air jig separator can separate two kinds of materials each time. If the mixed material contains such as aluminum, red metal, plastic, secondary separation is required. In the first sorting, heavy metals and light plastics can be sorted out. During secondary separation, relatively heavy red metal and relatively light aluminum can be separated out.

9)静电分选机1台:主要用来分选出气流跳汰分选机输出的粉尘中少量 金属。主要工作原理利用固体物料中各组分在高压电场中电性的差异而实现 再分离的一种方法。9) One electrostatic separator: it is mainly used to separate a small amount of metal in the dust output by the airflow jig separator. The main working principle is a method to achieve re-separation by utilizing the difference in electrical properties of each component in a solid material in a high-voltage electric field.

10)除尘装置1套:链式破碎机在进行破碎的过程中会产生灰尘;另外, 在锤磨过程中,新鲜气流不断输进锤磨机,气流是用来冷却锤磨机和及其出 料,并能抽出在给料或是在锤磨过程中产生的细小物料和毛絮。经过旋风除 尘器分离出不同轻重、不同颗粒的灰尘。剩余的气流由气管传送至喷气式过 滤器进行最终的除尘。可以确保排出的气体含尘量低至10mg/m310) 1 set of dust removal device: the chain crusher will generate dust during the crushing process; in addition, during the hammer mill process, fresh air is continuously input into the hammer mill, and the air flow is used to cool the hammer mill and its outlet. material, and can extract the fine material and lint produced in the feeding or hammer milling process. Dust of different weights and different particles is separated by the cyclone dust collector. The remaining air is piped to the jet filter for final dust removal. It can ensure that the dust content of the discharged gas is as low as 10mg/m 3 .

参见图1,上述各装置的连接关系是:Referring to Fig. 1, the connection relationship of the above-mentioned devices is:

送料装置(图中未示出)的出口与脱锡机1的入口连接;脱锡机1的光 板线路板出口与热分解槽6的入口相连;The outlet of the feeding device (not shown in the figure) is connected with the inlet of the tin remover 1; the light board circuit board outlet of the tin remover 1 is connected with the inlet of the thermal decomposition tank 6;

送料装置(图中未示出)的出口经第一皮带输送机15与链式破碎机的入 口连接;链式破碎机的出口与第一磁选机4的入口相连;第一磁选机4的出 口与波纹筛选槽入口相连;波纹筛选槽的出口经第二皮带输送机16,与热分 解槽6的入口相连;第二皮带输送机16旁设有人工分选平台;The outlet of the feeding device (not shown in the figure) is connected with the entrance of the chain crusher through the first belt conveyor 15; the outlet of the chain crusher is connected with the entrance of the first magnetic separator 4; the first magnetic separator The outlet of 4 links to each other with the inlet of corrugated screening tank; the outlet of corrugated screening tank links to each other with the entrance of thermal decomposition tank 6 through the second belt conveyor 16; The second belt conveyor 16 is provided with manual sorting platform;

裂解油化装置中的热分解槽6、触媒槽7、冷却装置8依次相连;其中, 热分解槽6的固体出口与锤磨机的入口相连,热分解槽6的气体出口与触媒 槽7的入口连接;触媒槽7的出口与冷却装置8的入口连接;冷却装置8的 废气出口与气体燃烧器9的入口相连,冷却装置8的液体出口与储油箱连接;The thermal decomposition tank 6, the catalyst tank 7, and the cooling device 8 in the cracking oilification device are connected successively; wherein, the solid outlet of the thermal decomposition tank 6 is connected with the entrance of the hammer mill, and the gas outlet of the thermal decomposition tank 6 is connected with the outlet of the catalyst tank 7. The inlet is connected; the outlet of the catalyst tank 7 is connected with the inlet of the cooling device 8; the waste gas outlet of the cooling device 8 is connected with the inlet of the gas burner 9, and the liquid outlet of the cooling device 8 is connected with the oil storage tank;

分选装置中,锤磨机的入口与热分解槽的固体出口相连,锤磨机的出口 与第二磁选机11的入口相连;第二磁选机11的出口与气流跳汰分选机12 的入口相连;气流跳汰分选机12的粉尘出口与静电分选机13的入口相连;In the sorting device, the inlet of the hammer mill is connected to the solid outlet of the thermal decomposition tank, and the outlet of the hammer mill is connected to the inlet of the second magnetic separator 11; the outlet of the second magnetic separator 11 is connected to the airflow jigging separator The inlet of 12 is connected; the dust outlet of airflow jig separator 12 is connected with the inlet of electrostatic separator 13;

此外,链式破碎机3的灰尘出口与除尘设备14的入口相连;锤磨机的灰 尘出口与除尘设备14的入口相连。In addition, the dust outlet of the chain crusher 3 is connected to the inlet of the dust removal device 14; the dust outlet of the hammer mill is connected to the inlet of the dust removal device 14.

上采用述成套处理设备进行废旧线缆拆解回收的处理方法,工艺过程包 括:预处理步骤(包括脱锡;和/或,破碎-磁选-筛选);油化裂解步骤(裂 解-催化重整-气体冷却-油/气分离-气体燃烧);粉碎和分选步骤(破碎-磁选- 分选);以及除尘步骤。具体如下:The above-mentioned complete set of processing equipment is used to disassemble and recycle waste and old cables. The process includes: a pretreatment step (comprising detinning; and/or, crushing-magnetic separation-screening); an oily cracking step (cracking- catalytic reforming - gas cooling - oil/gas separation - gas combustion); crushing and sorting steps (crushing - magnetic separation - sorting); and dedusting steps. details as follows:

1)脱锡。采用脱锡机1将电子元件从废旧线路板上脱离下来分别得到电 子元件、锡和光板电路板。废旧线路板中锡、铅、镍等重金属基本在电子元 件中,电子元件去除后,废线路板中基本不含重金属。对于完整的线路板及 线路板边角料,经脱锡后直接进入热分解槽6,即进入下道工序——裂解工 序,如此可提高分选率。1) Detinning. The electronic components are separated from the waste circuit board by using the tin remover 1 to obtain the electronic components, tin and light board circuit board respectively. Heavy metals such as tin, lead, and nickel in waste circuit boards are basically contained in electronic components. After the electronic components are removed, the waste circuit boards basically do not contain heavy metals. For complete circuit boards and circuit board leftovers, directly enter the thermal decomposition tank 6 after de-tinning, that is, enter the next process-cracking process, so that the separation rate can be improved.

2)破碎-磁选-筛选。首先,将含有线路板的电子废弃物(如报废的手提 电脑)送入链式破碎机,进行链式破碎,将电子废弃物上面附着的铁、塑料 及较大的电子元器件打散掉,采用配有强大气流筛选功能的转子链式破碎机, 可使废旧电子线路板破碎成小于50mm×50mm的块料;然后,通过人工分 选出>100mm的物料;然后,再经第一磁选机4磁选除铁后,经波纹筛选槽 5进行筛选,筛选出颗粒直径小于20mm的破碎物料送入热分解槽6,即进 入下道工序——裂解工序。本发明中的破碎-磁选-筛选步骤是为了使物料在 后续的裂解更为彻底,提高裂解效率。2) Broken-magnetic separation-screening. First, the electronic waste containing circuit boards (such as scrapped laptops) is sent to the chain crusher for chain crushing, and the iron, plastic and larger electronic components attached to the electronic waste are broken up. The rotor chain crusher with powerful airflow screening function can be used to crush waste electronic circuit boards into pieces smaller than 50mm×50mm; then, the materials >100mm are manually sorted out; then, the first magnetic separation After the machine 4 magnetically separates and removes iron, it is screened by the corrugated screening tank 5, and the crushed materials with a particle diameter of less than 20mm are screened and sent to the thermal decomposition tank 6, which enters the next process—the cracking process. The crushing-magnetic separation-screening step in the present invention is in order to make the subsequent cracking of material more thorough, improve cracking efficiency.

3)裂解。在热分解槽6中进行,具体地,将经步骤1)或2)得到的废 旧线路板物料投入到热解槽,使用氮气置换出热解槽内空气,将热解槽装入 加热槽,通过加热槽进行外部加热,热解槽内温度达到500℃后,废旧线路 板物料中含有的塑料(如环氧树脂)发生热分解气化,气化结束后,热解槽 从加热槽中移出,换下一槽,继续生产。3) cracking. Carry out in the pyrolysis tank 6, specifically, put the waste circuit board material obtained through step 1) or 2) into the pyrolysis tank, use nitrogen to replace the air in the pyrolysis tank, and put the pyrolysis tank into the heating tank , external heating is carried out through the heating tank. After the temperature in the pyrolysis tank reaches 500 ° C, the plastic (such as epoxy resin) contained in the waste circuit board material will be thermally decomposed and gasified. Move out, change to the next tank, and continue production.

4)催化重整。热解槽内产生的分解气体被送到触媒槽,采用二氧化硅类 催化剂进行催化重整,将其改质成短碳链(长碳链切断)。4) Catalytic reforming. The decomposition gas generated in the pyrolysis tank is sent to the catalyst tank, and the silica catalyst is used for catalytic reforming to modify it into short carbon chains (long carbon chains are cut off).

5)气体冷却。包括气体冷区器、塔顶冷却器。通过催化改质产生的油气 在冷却装置8中进行液化,采用泵循环,使用油雾气体冷却法和多管水冷冷 却法,循环水温度20℃以下。5) Gas cooling. Including gas cooler, tower top cooler. The oil and gas produced by catalytic upgrading is liquefied in the cooling device 8, and the pump circulation is adopted, and the oil mist gas cooling method and the multi-tube water cooling method are used, and the temperature of the circulating water is below 20 °C.

6)油/气分离。关于油的回收,在冷却机兼循环槽中,使用油冷却器回 收油,泵循环式回收油到储油箱,其中轻油、重油独立回收。关于油回收过 程中产生的未冷却的尾气,主要包括甲烷、乙烷、乙烯、丙烷、丙烯、丁烯、 丁烷等,经过燃烧炉燃烧后达标排放,燃烧炉温度在250℃-1050℃。油化裂 解装置中的热分解槽的塑料消耗量是100kg,热解槽内温度为500℃;裂解后 产油质量为51.10kg,为塑料质量的51.1%;液化石油气气态密度为2.35kg/Nm3,液化石油气热值是44750Kj/m3。塑料分解后残余物质为塑料质 量的41.0%,则不凝气占塑料总质量的7.9%。6) Oil/gas separation. Regarding oil recovery, in the cooling machine and circulation tank, the oil cooler is used to recover oil, and the pump circulates the oil to the oil storage tank, in which light oil and heavy oil are recovered independently. The uncooled tail gas produced in the oil recovery process mainly includes methane, ethane, ethylene, propane, propylene, butene, butane, etc., which are discharged up to the standard after being burned in the combustion furnace. The temperature of the combustion furnace is 250°C-1050°C. The plastic consumption of the pyrolysis tank in the oil cracking device is 100kg, and the temperature in the pyrolysis tank is 500°C; the quality of oil produced after cracking is 51.10kg, which is 51.1% of the plastic mass; the gas density of liquefied petroleum gas is 2.35kg/ Nm 3 , the calorific value of liquefied petroleum gas is 44750Kj/m 3 . After the plastic is decomposed, the residual substance is 41.0% of the plastic mass, and the non-condensable gas accounts for 7.9% of the total plastic mass.

7)破碎-磁选-分选。步骤3)产生的金属与玻璃纤维混合物被送入锤磨 机10进行进一步的粉碎,在锤磨机内,高速旋转的刀片将小块物料进行进一 步的破碎,得到粒度小于2mm的细粒物料,利用不同金属具不同延展性特 性将其搓成种类不同、大小不同的金属球;然后通过第三磁选机11对铁金属 筛选;然后再通过气流跳汰分选机12,将有色金属(铜、铝、不锈钢)、玻 璃纤维、粉尘分离出来;最后再进一步经静电分选机13将其他金属粉末从灰 尘中分选出,最后剩玻璃纤维。7) Crushing-magnetic separation-sorting. The metal and glass fiber mixture produced in step 3) is sent to the hammer mill 10 for further pulverization, and in the hammer mill, the blades rotating at high speed further crush the small pieces of material to obtain fine particles with a particle size less than 2mm Materials, using different metals with different ductility characteristics, knead them into metal balls of different types and sizes; then pass through the third magnetic separator 11 to screen the iron metal; Metals (copper, aluminum, stainless steel), glass fibers, and dust are separated; finally, other metal powders are further separated from the dust by an electrostatic separator 13, and finally the glass fibers are left.

8)除尘及其他环保措施。主要处理废气、废水、固废和噪声。废水和噪 声是连续产生的;对于噪声,通过减振、隔声降低污染;对于废水,生活污 水经化粪池预处理后,纳入污水管网排放。裂解产生的废气主要通过燃烧炉 燃烧后达标排放,即废旧线路板裂解过程中废气(不凝气)约为废线路板质 量的1.42%,废气(不凝气)通过燃烧炉燃烧后生产H2O和CO2通过烟囱排 放,基本不产生废气污染。关于固废,对于分离出来的进行对外出售,对于 难熔残余物出售给相关回收单位。关于粉尘,通过除尘装置,具体经过Z型 筛、多锥筛、旋风除尘器分离出不同轻重、不同颗粒的灰尘,然后通过过滤 器进行最终的除尘,过滤器可以确保摆出的气体含尘量低至10mg/m38) Dust removal and other environmental protection measures. It mainly deals with waste gas, waste water, solid waste and noise. Waste water and noise are generated continuously; for noise, pollution is reduced through vibration reduction and sound insulation; for waste water, domestic sewage is discharged into the sewage pipe network after pretreatment in septic tanks. The waste gas produced by pyrolysis is mainly discharged through the combustion furnace after reaching the standard, that is, the waste gas (non-condensable gas) during the cracking process of waste circuit boards is about 1.42% of the mass of waste circuit boards, and the waste gas (non-condensable gas) is burned through the combustion furnace to produce H 2 O and CO 2 are discharged through the chimney, which basically does not produce exhaust gas pollution. As for solid waste, the separated ones are sold to the outside world, and the refractory residues are sold to relevant recycling units. Regarding the dust, through the dust removal device, the dust of different weights and different particles is separated through the Z-type sieve, the multi-cone sieve, and the cyclone dust collector, and then the final dust removal is carried out through the filter. The filter can ensure the dust content of the discharged gas. as low as 10mg/m 3 .

本实施例中整套生产线功率为775KW,处理废旧线路板年可产铁800t、 有色金属3200t(内含金银等贵金属约10吨)、油1500t。预处理装置中的 破碎生产线(执行步骤2)破碎-磁选-筛选的生产线):年正常运行小时大于 7000小时;破碎生产线正常连续不低于120小时,产量为2-3t/h(预处理完 成的线路板),设备理论最大产能为15000t/年(预处理完成的线路板);金 属分选效率大于98%。In the present embodiment, the power of the complete production line is 775KW, and the annual production of iron 800t, non-ferrous metals 3200t (containing about 10 tons of precious metals such as gold and silver), and oil 1500t can be processed for waste and old circuit boards. The crushing production line in the pretreatment device (executing step 2) crushing-magnetic separation-screening production line): the annual normal operation hours are greater than 7000 hours; the crushing production line is normally continuous for no less than 120 hours, and the output is 2-3t/h (pretreatment Completed circuit boards), the theoretical maximum production capacity of the equipment is 15,000t/year (preprocessed circuit boards); the metal separation efficiency is greater than 98%.

本发明提供的成套处理工艺,通过将电路板破碎及筛选、分选出小颗粒 物料,或者进行脱锡后得到的光板线路板,送入油化裂解装置的热分解槽进 行裂解反应,将原料部分热分解气化,剩下金属与玻璃纤维混合物;一方面, 在热分解槽产生的分解气体送至触媒槽,进行催化重整改质为短碳链物质, 然后通过对改质的油气进行液化,得到冷却油回收,油回收过程中产生的未 冷凝的尾气,经燃烧炉进行燃烧达标排放;另一方面将金属与玻璃纤维混合 物通过锤磨机进行进一步的粉碎,最后通过气流跳汰分选装置进行分选,使得铜、铝、不锈钢和玻璃纤维彻底分离回收,并进一步通过静电分选将金属 粉末和玻璃纤维分离回收。采用本发明提供的成套处理工艺,回收效率高、 分解效果好、环保无污染。The complete set of treatment process provided by the present invention is to send the circuit board into the thermal decomposition tank of the oil cracking device for cracking reaction by crushing, screening and sorting the circuit board to obtain small particle materials, or the bare circuit board obtained after detinning. Part of the raw material is thermally decomposed and gasified, leaving a mixture of metal and glass fiber; on the one hand, the decomposition gas generated in the thermal decomposition tank is sent to the catalyst tank for catalytic reforming and reforming into short carbon chain substances, and then the modified oil and gas are Liquefied to obtain cooling oil recovery, the uncondensed tail gas generated during the oil recovery process is burned in the combustion furnace to meet the standard discharge; on the other hand, the metal and glass fiber mixture is further pulverized through a hammer mill, and finally passed through the airflow jigging The sorting device is used for sorting, so that copper, aluminum, stainless steel and glass fiber are completely separated and recycled, and the metal powder and glass fiber are further separated and recycled through electrostatic sorting. Adopting the complete treatment process provided by the present invention has high recovery efficiency, good decomposition effect, environmental protection and no pollution.

由于PCB物料的复杂性,铜、铝和玻璃纤维的分离很难彻底,上述成套 处理设备即处理方法中各参数可根据实际运行情况核算结果进行调节,因此 在不违背本发明所附权利要求范围的前提下,在具体实施过程中,可以对本 发明中关键参数的选择做出一些适当的改变。本发明尤其适用于废旧线路板 的破碎、裂解和分选。Due to the complexity of PCB materials, the separation of copper, aluminum and glass fibers is difficult to complete. The parameters in the above-mentioned complete set of processing equipment, that is, the processing method, can be adjusted according to the calculation results of actual operating conditions. Therefore, without violating the scope of the appended claims of the present invention Under the premise, in the specific implementation process, some appropriate changes can be made to the selection of key parameters in the present invention. The invention is especially suitable for the crushing, cracking and sorting of waste circuit boards.

以上所述仅为本发明的较佳实施例,并不用以限制本发明,凡在本发明 的精神和原则之内,所作的任何修改、等同替换、改进等,均应包含在本发 明的保护范围之内。The above descriptions are only preferred embodiments of the present invention, and are not intended to limit the present invention. Any modifications, equivalent replacements, improvements, etc. made within the spirit and principles of the present invention should be included in the scope of the present invention. within the scope of protection.

Claims (9)

1. A complete set of treatment equipment for waste circuit board recovery, characterized in that, the equipment includes:
the inlet of the pretreatment device is connected with the outlet of the feeding device and is used for pretreating the waste circuit board from the feeding device or the electronic waste containing the waste circuit board;
the pretreatment device comprises: the first pretreatment device and/or the second pretreatment device; wherein,
the first pretreatment device comprises a tin removing machine which is used for removing tin and electronic elements from the waste circuit board to obtain a light panel circuit board;
the second pretreatment device comprises a first crusher, a first sorting machine and a manual sorting platform, wherein the first crusher is used for crushing the electronic waste containing the waste circuit board; the first separator is arranged behind the first crusher and is used for screening and filtering crushed materials; the manual sorting platform is arranged in front of or behind the first sorting machine and used for manually sorting out larger materials;
the second preprocessing unit further includes: the first magnetic separator is arranged between the first crusher and the first separator; the first crusher is a chain crusher; the first separator is a corrugated screening groove or a rotary screen; the material processed by the first crusher is lump material with the size less than 50mm multiplied by 50 mm; the particle diameter of the crushed material screened by the first separator is less than 20-40 mm; the manual sorting platform is used for manually sorting materials larger than 100 mm;
the inlet of the cracking oiling device is connected with the outlet of the pretreatment device and is used for carrying out cracking oiling treatment on the waste circuit board material output by the pretreatment device;
the pyrolysis oiling device comprises: the device comprises a thermal decomposition tank, a catalyst tank, a cooling device, an oil storage tank and a gas burner; wherein the inlet of the thermal decomposition tank is connected with the outlet of the pretreatment device; the inlet of the catalyst tank is connected with the gas outlet of the thermal decomposition tank; the inlet of the cooling device is connected with the outlet of the catalyst groove; the inlet of the oil storage tank is connected with the oil outlet of the cooling device; the inlet of the gas burner is connected with the gas outlet of the cooling device;
the thermal decomposition tank comprises a pyrolysis tank, a heating tank and a reversing device, wherein the pyrolysis tank is a place for containing the waste circuit board materials, the heating tank is used for heating the pyrolysis tank to enable cracking reaction to occur in the pyrolysis tank, and the reversing device is arranged outside the heating tank and/or the pyrolysis tank and is used for reversing the pyrolysis tank and the heating tank so as to pour out the materials pyrolyzed in the pyrolysis tank;
the cooling device is a cooling tower, and a gas cooler, a tower top cooler and a cooler and circulating tank are arranged in the cooling tower, wherein the gas cooler and the tower top cooler are used for cooling the modified pyrolysis gas, and the cooler and circulating tank is used for recovering oil; the gas burner is a combustion furnace;
when the waste circuit board is treated, the light board circuit board obtained after the waste circuit board is treated by the detinning machine is conveyed to a pyrolysis oiling device from an outlet of the detinning machine; when the electronic waste containing the waste circuit board is treated, the materials of the electronic waste sorted by the first sorting machine enter the thermal decomposition tank to be subjected to heating and cracking treatment;
the inlet of the crushing/sorting device is connected with the solid material outlet of the cracking oiling device and is used for further crushing and sorting the mixture of the metal and the glass fiber output by the cracking oiling device;
the crushing/sorting apparatus includes: a second crusher, a second classifier, an electrostatic classifier; wherein,
the inlet of the second crusher is connected with the solid material outlet of the cracking oiling device and is used for further crushing the mixture of the metal and the glass fiber output by the cracking oiling device; the second crusher is a hammer mill;
the inlet of the second separator is connected with the outlet of the second crusher and is used for separating heavy objects and light objects in the materials output by the second crusher; the second separator comprises an air flow jigging separator and/or an eddy current separator;
the inlet of the electrostatic separator is connected with the dust outlet of the second separator and is used for separating glass fibers and metal powder in dust;
the crushing/sorting apparatus further comprises: the second magnetic separator is arranged between the second crusher and the second separator;
the inlet of the dust removal device is respectively connected with the dust outlets of the pretreatment device and the crushing/sorting device and is used for processing dust so that the air is discharged after reaching the standard;
the dust removing device comprises dust removing equipment, and an inlet of the dust removing equipment is respectively connected with dust outlets of the first crusher and the second crusher; the dust removing equipment comprises a Z-shaped sieve, a multi-cone sieve, a cyclone dust remover and an air-jet filter.
2. The plant for recycling waste circuit boards as claimed in claim 1, wherein a belt conveyor is used for conveying materials between the machines in the plant.
3. The plant for recycling waste circuit boards as claimed in claim 2, wherein the belt conveyor uses a herringbone rubber belt, and a protective cover is arranged on the belt conveyor.
4. A processing method for waste circuit board recovery, which is implemented by using the complete processing equipment for waste circuit board recovery of any one of claims 1-3, and comprises the following steps:
a pretreatment step: pretreating different types of waste circuit boards;
an oil cracking step: carrying out cracking oiling treatment on the waste circuit board material obtained after the pretreatment step, and cooling to obtain regenerated oil and a mixture of metal and glass fiber;
crushing and sorting: and crushing the mixture of the metal and the glass fiber obtained in the oil cracking step, and then sorting to obtain different recycled materials respectively.
5. The processing method for recycling the waste circuit boards as claimed in claim 4, wherein the pretreatment step comprises a first pretreatment step and/or a second pretreatment step; wherein,
the first pretreatment step is a detinning step, and the electronic element is separated from the waste circuit board through a detinning machine to obtain a light panel circuit board;
the second preprocessing step includes the following substeps: the method comprises the following steps that firstly, electronic waste containing a circuit board is crushed, so that metal and nonmetal in the electronic waste containing the circuit board can be split and scattered; and a second substep: screening and filtering the waste circuit board material obtained in the first substep to obtain a crushed material with a certain particle size; the crushing treatment is carried out by adopting a chain crusher; a second substep in the second pretreatment step is also preceded by a substep of removing iron and a substep of manually sorting; removing iron by using a magnetic separator, and sorting out materials with the thickness of more than 100mm in a manual sorting mode; in the first substep, the electronic waste containing the circuit board can be crushed into blocks smaller than 50mm multiplied by 50mm, and the particle diameter of the crushed material obtained after the processing of the substep is smaller than 20 mm-40 mm.
6. The processing method for recycling waste circuit boards as claimed in claim 4 or 5, wherein the cracking and oiling step comprises the following substeps:
a cracking sub-step, namely heating the waste circuit board material obtained after the pretreatment step for cracking reaction to obtain pyrolysis gas and a mixture of metal and glass fiber;
a modification substep, namely modifying the pyrolysis gas obtained in the cracking substep under the action of a catalyst, namely cutting long carbon chains into short carbon chains;
and a cooling substep, wherein the pyrolysis gas after the modification substep is subjected to cooling liquefaction treatment to obtain liquid regenerated oil and waste gas.
7. The processing method for recycling waste circuit boards according to claim 6,
the heating temperature in the cracking sub-step is 400-600 ℃, and the pressure is less than or equal to 0.05Mpa;
in the cooling substep, light oil and heavy oil in the reclaimed oil are independently recovered, the waste gas is discharged after reaching the standard through hot combustion treatment, and the temperature of the combustion treatment is 250-1050 ℃.
8. The processing method for recycling waste circuit boards as claimed in claim 7, wherein the crushing and sorting step comprises the following substeps:
a crushing substep, crushing the mixture of the metal and the glass fiber produced in the cracking oiling step;
a separation substep, namely firstly subjecting the materials treated in the crushing substep to air flow jigging separation and/or eddy current separation to respectively obtain mixed metal products, glass fibers and dust; then the glass fiber and the metal powder are respectively obtained from the dust through electrostatic separation;
the crushing treatment is carried out by adopting a hammer mill;
the sorting substep is also preceded by a deironing substep;
when the air jigging separation is adopted, secondary separation is needed if the materials processed by the crushing substep contain aluminum, red metal and plastic.
9. The processing method for recycling waste circuit boards as claimed in claim 8, further comprising a dust removal step of processing dust generated in the pretreatment step and the pulverization and sorting step by a dust removal device; and when the second pretreatment step is used for crushing treatment, and the crushing and sorting steps are used for crushing treatment, the generated dust is sent to the dust removal device for dust removal treatment, so that the dust is discharged after reaching the standard.
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