CN110170242A - Electronic waste, the exhaust treatment system of a kind of electronic waste smelting device and its composition - Google Patents
Electronic waste, the exhaust treatment system of a kind of electronic waste smelting device and its composition Download PDFInfo
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- CN110170242A CN110170242A CN201910283742.2A CN201910283742A CN110170242A CN 110170242 A CN110170242 A CN 110170242A CN 201910283742 A CN201910283742 A CN 201910283742A CN 110170242 A CN110170242 A CN 110170242A
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- 238000003723 Smelting Methods 0.000 title claims abstract description 82
- 239000010793 electronic waste Substances 0.000 title claims abstract description 59
- 239000000203 mixture Substances 0.000 title claims description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 26
- 239000002893 slag Substances 0.000 claims abstract description 21
- 239000007921 spray Substances 0.000 claims abstract description 10
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims abstract description 9
- 238000001179 sorption measurement Methods 0.000 claims abstract description 7
- PTVDYARBVCBHSL-UHFFFAOYSA-N copper;hydrate Chemical compound O.[Cu] PTVDYARBVCBHSL-UHFFFAOYSA-N 0.000 claims abstract description 6
- 239000003513 alkali Substances 0.000 claims abstract description 5
- HEMHJVSKTPXQMS-UHFFFAOYSA-M sodium hydroxide Inorganic materials [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 21
- 239000007788 liquid Substances 0.000 claims description 6
- 239000002826 coolant Substances 0.000 claims description 4
- 241000628997 Flos Species 0.000 claims 1
- 241001062472 Stokellia anisodon Species 0.000 claims 1
- 239000000835 fiber Substances 0.000 claims 1
- 238000002485 combustion reaction Methods 0.000 abstract description 23
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract description 21
- 239000003546 flue gas Substances 0.000 abstract description 21
- 239000007789 gas Substances 0.000 abstract description 11
- 239000000463 material Substances 0.000 abstract description 9
- 238000010791 quenching Methods 0.000 abstract description 7
- 230000000171 quenching effect Effects 0.000 abstract description 7
- 230000007613 environmental effect Effects 0.000 abstract description 6
- 229910052799 carbon Inorganic materials 0.000 abstract description 5
- 238000002844 melting Methods 0.000 abstract description 5
- 230000008018 melting Effects 0.000 abstract description 5
- 239000000428 dust Substances 0.000 abstract description 4
- 230000001590 oxidative effect Effects 0.000 abstract description 2
- 229910052760 oxygen Inorganic materials 0.000 description 20
- 239000001301 oxygen Substances 0.000 description 20
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 19
- 238000000034 method Methods 0.000 description 13
- 239000010949 copper Substances 0.000 description 10
- 229910052802 copper Inorganic materials 0.000 description 9
- 229910045601 alloy Inorganic materials 0.000 description 7
- 239000000956 alloy Substances 0.000 description 7
- 239000002184 metal Substances 0.000 description 7
- 229910052751 metal Inorganic materials 0.000 description 7
- 230000008569 process Effects 0.000 description 7
- 238000011084 recovery Methods 0.000 description 7
- 239000002912 waste gas Substances 0.000 description 7
- 238000012545 processing Methods 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 229910052718 tin Inorganic materials 0.000 description 5
- CPELXLSAUQHCOX-UHFFFAOYSA-N Hydrogen bromide Chemical compound Br CPELXLSAUQHCOX-UHFFFAOYSA-N 0.000 description 4
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 4
- 230000008901 benefit Effects 0.000 description 4
- 238000007664 blowing Methods 0.000 description 4
- 230000008859 change Effects 0.000 description 4
- 238000012423 maintenance Methods 0.000 description 4
- 150000002739 metals Chemical class 0.000 description 4
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- 230000000391 smoking effect Effects 0.000 description 4
- 238000010790 dilution Methods 0.000 description 3
- 239000012895 dilution Substances 0.000 description 3
- 239000010791 domestic waste Substances 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000005416 organic matter Substances 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- HGUFODBRKLSHSI-UHFFFAOYSA-N 2,3,7,8-tetrachloro-dibenzo-p-dioxin Chemical compound O1C2=CC(Cl)=C(Cl)C=C2OC2=C1C=C(Cl)C(Cl)=C2 HGUFODBRKLSHSI-UHFFFAOYSA-N 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 239000003245 coal Substances 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 229910052737 gold Inorganic materials 0.000 description 2
- 229910000042 hydrogen bromide Inorganic materials 0.000 description 2
- 230000010354 integration Effects 0.000 description 2
- 238000002955 isolation Methods 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 230000033116 oxidation-reduction process Effects 0.000 description 2
- 239000013618 particulate matter Substances 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 229920003023 plastic Polymers 0.000 description 2
- 229910052697 platinum Inorganic materials 0.000 description 2
- 238000000197 pyrolysis Methods 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 229910052709 silver Inorganic materials 0.000 description 2
- 238000005507 spraying Methods 0.000 description 2
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 1
- 229920000742 Cotton Polymers 0.000 description 1
- 235000019738 Limestone Nutrition 0.000 description 1
- 229910004298 SiO 2 Inorganic materials 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000000110 cooling liquid Substances 0.000 description 1
- 239000010459 dolomite Substances 0.000 description 1
- 229910000514 dolomite Inorganic materials 0.000 description 1
- 239000010792 electronic scrap Substances 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 230000004907 flux Effects 0.000 description 1
- 239000002920 hazardous waste Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000006028 limestone Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910001092 metal group alloy Inorganic materials 0.000 description 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical class C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 238000000638 solvent extraction Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/002—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by condensation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
- B01D53/04—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/77—Liquid phase processes
- B01D53/78—Liquid phase processes with gas-liquid contact
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B11/00—Obtaining noble metals
- C22B11/02—Obtaining noble metals by dry processes
- C22B11/021—Recovery of noble metals from waste materials
- C22B11/025—Recovery of noble metals from waste materials from manufactured products, e.g. from printed circuit boards, from photographic films, paper, or baths
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B15/00—Obtaining copper
- C22B15/0026—Pyrometallurgy
- C22B15/0056—Scrap treating
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B25/00—Obtaining tin
- C22B25/02—Obtaining tin by dry processes
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B25/00—Obtaining tin
- C22B25/06—Obtaining tin from scrap, especially tin scrap
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B7/00—Working up raw materials other than ores, e.g. scrap, to produce non-ferrous metals and compounds thereof; Methods of a general interest or applied to the winning of more than two metals
- C22B7/001—Dry processes
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D17/00—Arrangements for using waste heat; Arrangements for using, or disposing of, waste gases
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2251/00—Reactants
- B01D2251/30—Alkali metal compounds
- B01D2251/304—Alkali metal compounds of sodium
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- 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
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- 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
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Abstract
本发明公开的电子废料冶炼装置,包括炉缸、炉身和炉顶,炉缸底部两侧对称设有风嘴;炉身内部分为熔炼区和烟化区,炉顶对应熔炼区和烟化区上面分别设有加料口和烟气出口;炉身熔炼区端部侧壁上设熔炼渣放出口;炉身烟化区端部设有粗铜排放口。所述炉身外部设置有铜水套。还公开了一种电子废料、废气处理系统,依次连接电子废料冶炼装置、骤冷装置、布袋收尘装置、活性炭吸附装置、碱液喷淋装置和废气排放烟囱。本发明不仅可以实现电子废料中含碳物料的高效氧化燃烧,同时还能合理释放和利用燃烧总热量,避免局部炉温过高;对于电子废料燃烧后的烟气经处理后也能保证达到国家二类环境功能区的排放标准。
The electronic waste smelting device disclosed by the present invention comprises a furnace hearth, a furnace body and a furnace roof, and tuyeres are symmetrically arranged on both sides of the bottom of the furnace hearth; the inside of the furnace body is divided into a smelting area and a fuming area, and the furnace top corresponds to the melting area and the fuming area There are feeding ports and flue gas outlets on the top; smelting slag outlets are provided on the side wall of the end of the furnace body smelting zone; a blister copper discharge port is provided at the end of the furnace body fuming area. A copper water jacket is provided outside the furnace body. Also disclosed is an electronic waste and exhaust gas treatment system, which is sequentially connected with an electronic waste smelting device, a quenching device, a bag dust collecting device, an activated carbon adsorption device, an alkali spray device and an exhaust gas discharge chimney. The invention can not only realize efficient oxidative combustion of carbon-containing materials in electronic waste, but also can reasonably release and utilize the total heat of combustion to avoid excessive local furnace temperature; the flue gas after electronic waste combustion can also be guaranteed to reach national Emission standards for the second-class environmental functional area.
Description
技术领域technical field
本发明涉及有色金属冶炼、危险废物处理和资源循环利用技术领域,尤其是涉及一种电子废料冶炼装置及其组成的电子废料、废气处理系统。The invention relates to the technical fields of nonferrous metal smelting, hazardous waste treatment and resource recycling, in particular to an electronic waste smelting device and an electronic waste and waste gas treatment system composed of the device.
背景技术Background technique
国内废电路板的处理方式:一是土法处理,直接焚烧烟气未经处理排入大气,这种方法严重污染环境,近几年已被绝对禁止;二是是用选矿方式处理得金属合金和废塑料,合金进铜冶炼厂回收有价金属,废塑料需用填埋的方法处理,环境污染仍较严重,且有价金属回收率较低,这种方法目前在国内仍普遍使用;三是格林美股份有限公司采用热解分离回收金属技术,非金属成份纳入公司的副产品或残渣进一步环保处置,这种处理技术与西方发达国家目前采用的技术相似,每年处理废电路板约3万吨,但处理能力远远不能满足处理国内废电子废料的需求(国内废电路板年产量为50万吨以上)。目前,国内对环境保护的要求越来越高,开发有价金属综合回收率更高,能避免产生二次污染的的电子废物处理装置已是当务之急。把电子废物处理好对中国经济、社会和环境的可持续发展都有十分重要的意义。Domestic waste circuit boards are treated in the following ways: one is local treatment, and the flue gas is directly incinerated and discharged into the atmosphere without treatment. This method seriously pollutes the environment and has been absolutely banned in recent years; the other is to use mineral processing to obtain metal alloys. And waste plastics and alloys are sent to copper smelters to recycle valuable metals. Waste plastics need to be disposed of by landfill. The environmental pollution is still serious, and the recovery rate of valuable metals is low. This method is still widely used in China; 3. It is GEM Co., Ltd. that adopts pyrolysis separation and recovery of metal technology, and non-metallic components are incorporated into the company's by-products or residues for further environmental protection. This treatment technology is similar to the technology currently used by western developed countries. It processes about 30,000 tons of waste circuit boards every year. However, the processing capacity is far from meeting the demand for processing domestic waste electronic waste (the annual output of domestic waste circuit boards is more than 500,000 tons). At present, the domestic requirements for environmental protection are getting higher and higher, and it is urgent to develop electronic waste treatment devices that have a higher comprehensive recovery rate of valuable metals and can avoid secondary pollution. Proper disposal of electronic waste is of great significance to the sustainable development of China's economy, society and environment.
中国专利CN106929680B公开了一种电子废料的冶炼装置和冶炼方法,该电子废料的冶炼装置,包括:炉体,所述炉体内限定有炉膛,所述炉膛具有上端开口且包括反应区和位于所述反应区上方的气相区,所述炉体上设有与所述反应区连通的排料口;炉顶,所述炉顶与所述炉体相连且封盖所述炉膛的上端开口的一部分,所述炉顶上设有与所述炉膛连通的加料口、喷枪口和一次烧嘴口,所述一次烧嘴口处设有一次烧嘴;二次燃烧室,所述二次燃烧室内限定有下端敞开的二次燃烧腔,所述二次燃烧室上设有与所述二次燃烧腔连通的二次烧嘴口,所述二次烧嘴口处设有二次烧嘴,所述二次燃烧室盖设在所述上端开口的另一部分上且所述二次燃烧腔与所述炉膛连通,所述二次燃烧室上设有连通所述二次燃烧腔与外界的烟道,所述二次燃烧室位于所述炉膛的中心线的一侧;喷枪,所述喷枪穿设在所述喷枪口内且所述喷枪的下端伸入所述反应区内。Chinese patent CN106929680B discloses a smelting device and method for smelting electronic waste. The smelting device for electronic waste includes: a furnace body, the furnace body defines a furnace, the furnace has an upper end opening and includes a reaction zone and a In the gas phase area above the reaction zone, the furnace body is provided with a discharge port communicating with the reaction zone; the furnace roof, the furnace roof is connected to the furnace body and covers a part of the upper opening of the furnace, The top of the furnace is provided with a charging port, a spray gun port and a primary burner port communicated with the furnace, and the primary burner port is provided with a primary burner; a secondary combustion chamber is defined in the secondary combustion chamber A secondary combustion chamber with an open lower end, the secondary combustion chamber is provided with a secondary burner port communicating with the secondary combustion chamber, the secondary burner port is provided with a secondary burner, the secondary The secondary combustion chamber cover is arranged on the other part of the upper opening and the secondary combustion chamber communicates with the furnace, and the secondary combustion chamber is provided with a flue connecting the secondary combustion chamber with the outside world, so The secondary combustion chamber is located on one side of the center line of the furnace; the spray gun is installed in the mouth of the spray gun and the lower end of the spray gun extends into the reaction zone.
中国专利CN 102978405A公开了一种电子废料的侧吹连续冶炼工艺及装置。冶炼时,将经过一定程度破碎的电子废料、富含铜物料与熔剂一起通过熔炼区炉顶的加料口加入熔炼区炉内,掉落在熔炼区沉淀池表面的渣层上;两个加料口都是需要造渣反应,操作控制更加复杂,而且固定了物理隔离区,不能适应各种物料。Chinese patent CN 102978405A discloses a side blowing continuous smelting process and device for electronic waste. During smelting, electronic scraps, copper-rich materials and fluxes that have been crushed to a certain extent are fed into the furnace in the smelting area through the feeding port on the furnace roof of the smelting area, and fall on the slag layer on the surface of the sedimentation tank in the smelting area; two feeding ports Both require slagging reaction, the operation control is more complicated, and the physical isolation area is fixed, which cannot adapt to various materials.
这些用于电子废物冶炼的装置大部分都是ISAR氧气顶吹炉处理电子废料装置、闪速-电炉熔炼装置、含有物理隔离氧化-还原两区的侧吹装置、无氧电子废料热解装置。而存在问题包括:氧枪的采用极大地增加了运行与维护成本,而且,工艺技术参数也不尽合理;或者(例如闪速-电炉熔炼装置)需要非常细的电子废料原料,磨矿破碎成本急剧增加,而且电炉熔炼又没有充分利用上高碳含量、高热量的电子废料本身氧化热值;三是含有物理隔离氧化-还原两区熔炼的侧吹装置,操作难度较大。同时对最终排出的气体没有进行无害化处理。Most of these devices for electronic waste smelting are ISAR oxygen top-blown furnace processing electronic waste devices, flash-electric furnace smelting devices, side blowing devices with physical isolation oxidation-reduction zones, and oxygen-free electronic waste pyrolysis devices. The existing problems include: the use of the oxygen lance greatly increases the operation and maintenance costs, and the technical parameters of the process are not reasonable; The rapid increase, and the electric furnace smelting has not fully utilized the oxidation calorific value of the high-carbon and high-calorie electronic waste itself; the third is the side blowing device that physically isolates the oxidation-reduction two-zone smelting, which is difficult to operate. At the same time, no harmless treatment has been carried out on the finally discharged gas.
发明内容Contents of the invention
本发明的目的在于针对上述现有技术存在的问题,提供一种设备运行与维护成本低、原料适应性强、生产操作简单,可以直接弃渣和进行气体排放的电子废料冶炼装置及其组成的电子废料、废气处理处理系统。The purpose of the present invention is to solve the problems in the above-mentioned prior art, and provide an electronic waste smelting device and its components, which have low equipment operation and maintenance costs, strong raw material adaptability, simple production operation, and can directly discard slag and discharge gas. Electronic waste and waste gas treatment system.
本发明采用的技术方案是电子废料冶炼装置,包括炉缸、炉身和炉顶,炉缸底部两侧对称设有风嘴;炉身内部分为熔炼区和烟化区,炉顶对应熔炼区和烟化区上面分别设有加料口和烟气出口;炉身熔炼区端部侧壁上设熔炼渣放出口;炉身烟化区端部设有粗铜排放口。The technical scheme adopted in the present invention is an electronic waste smelting device, including a furnace hearth, a furnace body and a furnace roof, and tuyeres are arranged symmetrically on both sides of the furnace hearth bottom; A feeding port and a flue gas outlet are respectively provided on the fuming area; a smelting slag outlet is provided on the side wall at the end of the smelting area of the furnace body; a crude copper discharge port is provided at the end of the fuming area of the furnace body.
所述炉身外部设置有铜水套。A copper water jacket is provided outside the furnace body.
所述熔炼区的加料口称为熔炼区加料口,熔炼区的烟气出口称为熔炼区烟气出口。The feed port of the smelting zone is called the feed port of the smelting zone, and the flue gas outlet of the smelting zone is called the flue gas outlet of the smelting zone.
所述烟化区的加料口称为烟化区加料口,烟化区的烟气出口称为烟化区烟气出口。The feeding port of the smoking area is called the feeding port of the smoking area, and the flue gas outlet of the smoking area is called the flue gas outlet of the smoking area.
一种电子废料、废气处理系统,依次连接电子废料冶炼装置、骤冷装置、布袋收尘装置、活性炭吸附装置、碱液喷淋装置和废气排放烟囱。An electronic waste and exhaust gas treatment system is sequentially connected with an electronic waste smelting device, a quenching device, a bag dust collection device, an activated carbon adsorption device, an alkali spray device and a waste gas discharge chimney.
所述活性炭吸附装置为两或三块以上活性炭纤维棉组成。The activated carbon adsorption device is composed of two or more pieces of activated carbon fiber cotton.
所述碱液喷淋装置中的碱液为氢氧化钠液体。The lye in the lye spraying device is sodium hydroxide liquid.
所述骤冷装置中的冷却液为内部循环使用。The cooling liquid in the quenching device is used for internal circulation.
本发明的有益效果在于:本发明电子废料冶炼装置采用了富氧侧吹熔炼炉,炉内由可以动态调节的熔炼区与烟化区构成,无需进行物理分区,仅是通过在两区喷入不同的氧气浓度的气体进行分区,更适应电子废料组成的变化需要,因此,不仅具有设备维护成本低,处理效率高等优点,而且还实现了电子废料等高含碳物料的在富氧条件下的燃烧效果非常好。The beneficial effect of the present invention is that: the electronic waste smelting device of the present invention adopts an oxygen-enriched side-blown smelting furnace, and the furnace is composed of a smelting zone and a fuming zone that can be dynamically adjusted. Gases with different oxygen concentrations are divided into zones, which is more suitable for the change of electronic waste composition. Therefore, it not only has the advantages of low equipment maintenance cost and high processing efficiency, but also realizes the recovery of high carbon-containing materials such as electronic waste under oxygen-enriched conditions. Burns very well.
本发明电子废料冶炼装置处理电子废料无需物理分选等一系列预处理工序,烟化区产出的合金中Cu、Sn、Au、Ag、Pt的回收率均≥90wt%,熔炼区产出的炉渣中Cu和Sn的含量均≤1.0wt%,炉渣无需进一步贫化处理即可直接废弃,工艺简便,金属综合回收率高,缩短了处理流程,提高了处理能力及原料适应性,经济、社会与环境效益更加显著。The electronic waste smelting device of the present invention does not need a series of pretreatment procedures such as physical sorting to process electronic waste. The recovery rates of Cu, Sn, Au, Ag, and Pt in the alloy produced in the fuming zone are all ≥ 90wt%. The contents of Cu and Sn in the slag are both ≤1.0wt%. The slag can be discarded directly without further dilution treatment. And environmental benefits are more significant.
本发明电子废料冶炼装置及其组成的电子废料、废气处理处理系统是熔炼和烟气无害化处理的系统集成,熔炼装置操作简单,获得的低Cu含量的炉渣可以直接废弃,无需再次贫化。烟气处理后二噁英、溴化氢含量、颗粒物含量、二氧化硫含量等可以确保低于国家允许排放的标准,排放后厂区大气中污染因子含量可以稳定达到国家标准要求。The electronic waste smelting device of the present invention and the electronic waste and waste gas treatment system composed of it is a system integration of smelting and flue gas harmless treatment, the smelting device is easy to operate, and the obtained slag with low Cu content can be directly discarded without further dilution . After flue gas treatment, the content of dioxin, hydrogen bromide, particulate matter, and sulfur dioxide can be guaranteed to be lower than the national allowable emission standards, and the content of pollution factors in the atmosphere of the factory area after emission can stably meet the requirements of national standards.
综上所述,本发明不仅可以实现电子废料中含碳物料的高效氧化燃烧,同时还能合理释放和利用燃烧总热量,避免局部炉温过高;对于电子废料燃烧后的烟气经处理后也能保证达到国家二类环境功能区的排放标准。对社会经济和环境的可持续发展都有十分重要的意义。To sum up, the present invention can not only achieve high-efficiency oxidative combustion of carbon-containing materials in electronic waste, but also reasonably release and utilize the total heat of combustion to avoid excessive local furnace temperature; It can also ensure that the emission standards of the national second-class environmental function zone are met. It is of great significance to the sustainable development of social economy and environment.
附图说明Description of drawings
下面结合附图中的实施例对本发明作进一步的详细说明,但并不构成对本发明的任何限制。The present invention will be described in further detail below in conjunction with the embodiments in the accompanying drawings, but this does not constitute any limitation to the present invention.
图1是本发明电子废料冶炼装置结构示意图。Fig. 1 is a schematic diagram of the structure of the electronic waste smelting device of the present invention.
图2是本发明电子废料、废气处理系统示意图。Fig. 2 is a schematic diagram of the electronic waste and exhaust gas treatment system of the present invention.
附图标记:1、电子废料冶炼装置,2、骤冷装置,3、布袋收尘装置,4、活性炭吸附装置,5、碱液喷淋装置,6、废气排放烟囱;Reference signs: 1. Electronic waste smelting device, 2. Quenching device, 3. Bag dust collection device, 4. Activated carbon adsorption device, 5. Alkali spray device, 6. Exhaust gas discharge chimney;
101、炉缸;102、炉身;103、炉顶,104、风嘴,105、熔炼区,106、熔炼区加料口,107、烟化区,108、熔炼区烟气出口,109、烟化区烟气出口,110、烟化区加料口,111、熔炼渣放出口,112、粗铜排放口。101. Furnace hearth; 102. Furnace body; 103. Furnace top, 104. Tuyere, 105. Melting area, 106. Feed port of smelting area, 107. Fuming area, 108. Flue gas outlet of smelting area, 109. Fuming Area flue gas outlet, 110, feeding port of fuming area, 111, smelting slag discharge port, 112, blister copper discharge port.
具体实施方式Detailed ways
参阅附图,本发明电子废料冶炼装置1,包括炉缸101、炉身102和炉顶103,炉缸101底部两侧对称设有风嘴104;炉身102内部分为熔炼区105和烟化区107,炉顶103对应熔炼区105和烟化区107上面分别设有加料口和烟气出口;炉身102熔炼区105端部侧壁上设熔炼渣放出口111;炉身102烟化区107端部设有粗铜排放口112。Referring to the accompanying drawings, the electronic waste smelting device 1 of the present invention includes a furnace hearth 101, a furnace body 102 and a furnace roof 103, and both sides of the bottom of the furnace hearth 101 are symmetrically provided with tuyeres 104; the interior of the furnace body 102 is divided into a melting zone 105 and a fuming Zone 107, furnace roof 103 is respectively provided with feeding port and flue gas outlet above smelting zone 105 and fuming zone 107; smelting slag outlet 111 is set on the side wall of the end of furnace body 102 melting zone 105; furnace body 102 fuming zone The end of 107 is provided with blister copper discharge port 112 .
本发明没有采用传统的物理分区,而是通过两个分区的风嘴104供应不同浓度的氧气来进行分区,其中,熔炼区105风嘴104喷入的富氧空气中氧气浓度≥40%,瞬时供氧体积与入炉物料的比值=200-3000m3 氧气/t物料,烟化区107风嘴104喷入的含氧气体氧气浓度≥21%。两种浓度不同的氧气可产生温度不同的两个燃烧区域,熔炼区105烟气出口温度≥750℃,烟化区烟气出口109温度≥850℃。故而两个区域又分别产生不同的燃烧炉渣,熔炼区105产生的炉渣从熔炼渣放出口111排出,烟化区107产生的燃烧合金从粗铜排放口112排出,炉渣CaO/SiO2≥0.30(质量比),Fe/SiO2=0.05-1.0(质量比),Al2O3≤17%;熔炼产出合金Cu、Sn和Fe含量分别为89.56%、4.24%和0.71%;The present invention does not adopt traditional physical partitions, but supplies different concentrations of oxygen through the tuyeres 104 of the two partitions to carry out partitions, wherein the oxygen concentration in the oxygen-enriched air injected by the tuyeres 104 in the smelting zone 105 is ≥ 40%, and the instantaneous The ratio of the oxygen supply volume to the furnace material = 200-3000m 3 oxygen /t material , and the oxygen concentration of the oxygen-containing gas injected into the smoke zone 107 tuyere 104 is ≥ 21%. Two kinds of oxygen with different concentrations can produce two combustion zones with different temperatures, the temperature of the flue gas outlet 105 in the smelting zone is ≥750°C, and the temperature of the flue gas outlet 109 in the fuming zone is ≥850°C. Therefore, the two regions produce different combustion slags respectively. The slag produced in the smelting zone 105 is discharged from the smelting slag discharge port 111, and the combustion alloy produced in the fuming zone 107 is discharged from the blister copper discharge port 112. The slag CaO/SiO ≥ 0.30( Mass ratio), Fe/SiO 2 =0.05-1.0 (mass ratio), Al 2 O 3 ≤17%; Cu, Sn and Fe contents of alloy produced by smelting are 89.56%, 4.24% and 0.71% respectively;
另外,低温区(烟化区107)还可充分利用高温区(熔炼区105)燃烧产生的烟化热量来维持其区域所需燃烧温度,达到了节能减排的效果。In addition, the low-temperature zone (fuming zone 107) can also make full use of the fuming heat generated by combustion in the high-temperature zone (smelting zone 105) to maintain the required combustion temperature in the area, achieving the effect of energy saving and emission reduction.
进一步的,本发明在所述炉身102外部设置有铜水套。通过铜水套内部循环水的降温来维持炉身102内部的恒温,从而保证因炉身102长期温度过高而降低其使用寿命。Further, in the present invention, a copper water jacket is provided outside the furnace body 102 . The constant temperature inside the furnace body 102 is maintained by cooling the circulating water inside the copper water jacket, thereby ensuring that the service life of the furnace body 102 is reduced due to long-term excessive temperature.
本发明所述熔炼区105的加料口称为熔炼区加料口106,熔炼区105的烟气出口称为熔炼区烟气出口108。本发明所述烟化区107的加料口称为烟化区加料口110,烟化区107的烟气出口称为烟化区烟气出口109。本发明电子废料冶炼装置1采用了富氧侧吹熔炼炉,炉内由可以动态调节的熔炼区105与烟化区107构成,无需进行物理分区,仅是通过在两区喷入不同的氧气浓度的气体进行分区,更适应电子废料组成的变化需要,从而实现了产出炉渣可以直接废弃,因此,不仅具有设备维护成本低,处理效率高等优点,而且还实现了电子废料等高含碳物料的在富氧条件下的燃烧效果非常好。因上述两个区域的燃烧温度不同,为延长整体炉身102的使用寿命,本发明还可定期对换熔炼区105和烟化区107的使用。The feed port of the smelting zone 105 in the present invention is called the feed port 106 of the smelting zone, and the flue gas outlet of the smelting zone 105 is called the flue gas outlet 108 of the smelting zone. The feed port of the fuming zone 107 in the present invention is called the feed port 110 of the fuming zone, and the flue gas outlet of the fuming zone 107 is called the flue gas outlet 109 of the fuming zone. The electronic waste smelting device 1 of the present invention adopts an oxygen-enriched side-blowing smelting furnace, and the furnace is composed of a smelting zone 105 and a fuming zone 107 that can be dynamically adjusted. There is no need for physical partitioning, and only by injecting different oxygen concentrations into the two zones The gas is divided into partitions, which is more suitable for the change of electronic waste composition, so that the output slag can be directly discarded. Therefore, it not only has the advantages of low equipment maintenance cost and high processing efficiency, but also realizes the high carbon content of electronic waste. The combustion effect is very good under the condition of rich oxygen. Because the combustion temperatures of the above two areas are different, in order to prolong the service life of the whole furnace body 102, the present invention can also periodically change the use of the smelting area 105 and the fuming area 107.
一种电子废料、废气处理系统,依次连接电子废料冶炼装置1、骤冷装置2、布袋收尘装置3、活性炭吸附装置4、碱液喷淋装置5和废气排放烟囱6。An electronic waste and waste gas treatment system is sequentially connected with an electronic waste smelting device 1 , a quenching device 2 , a bag dust collector 3 , an activated carbon adsorption device 4 , an alkali spray device 5 and a waste gas discharge chimney 6 .
本发明所述活性炭附装置为两以上活性炭板组成。当然也可以采用三块或4块以上活性炭板组成,以更好的达到其使用效果。The activated carbon attachment device of the present invention is composed of more than two activated carbon plates. Of course, it can also be composed of three or more activated carbon plates to better achieve its use effect.
本发明所述碱液喷淋装置5中的碱液为氢氧化钠液体。也可采用其他具备同等功能使用效果的碱性液体。The lye in the lye spraying device 5 of the present invention is sodium hydroxide liquid. Other alkaline liquids with equivalent functions and effects can also be used.
本发明所述骤冷装置2中的冷却液为内部循环使用。同炉身102铜水套中的冷却液一样,骤冷装置2中的冷却液也可以循环使用。以达到节能减排的作用。The coolant in the quenching device 2 of the present invention is used for internal circulation. Like the coolant in the furnace body 102 copper water jacket, the coolant in the quenching device 2 can also be recycled. In order to achieve the effect of energy saving and emission reduction.
本发明电子废料冶炼装置1在使用过程中,首先将电子废料与硅石或铜冶炼渣、石灰石或白云石、粒煤按一定比例混合,然后分别通过熔炼区105加料口吹入电子废料冶炼装置1中熔炼区105进行溶炼,在熔炼区105通过熔炼区105风嘴104鼓入高氧浓度的富氧以充分烧掉电子废料中的有机物,燃烧有机物后的炉渣、合金混合物流入烟化区107,利用电子废料中燃烧有机物放出的烟化热量来维持炉温,在烟化区107鼓入低氧浓度的富氧以使合金与渣能良好分离,同时又可避免有价金属氧化入渣。自热产生大量的热量可以基本维持较高的炉温,如炉温下降,可加入适量的粒煤来调控炉温,操作简单方便。During the use of the electronic waste smelting device 1 of the present invention, the electronic waste is first mixed with silica or copper smelting slag, limestone or dolomite, and granular coal in a certain proportion, and then respectively blown into the electronic waste smelting device 1 through the feeding port of the smelting zone 105 Melting is carried out in the middle smelting zone 105, where high-oxygen-enriched oxygen is blown into the smelting zone 105 through the tuyere 104 of the smelting zone 105 to fully burn off the organic matter in the electronic waste, and the slag and alloy mixture after burning the organic matter flow into the fuming zone 107 The furnace temperature is maintained by using the fuming heat released from the combustion of organic matter in the electronic waste, and rich oxygen with low oxygen concentration is blown into the fuming zone 107 so that the alloy and slag can be separated well, and at the same time, the oxidation of valuable metals into the slag can be avoided. A large amount of heat generated by self-heating can basically maintain a relatively high furnace temperature. If the furnace temperature drops, an appropriate amount of granulated coal can be added to regulate the furnace temperature, and the operation is simple and convenient.
本发明电子废料冶炼装置1处理电子废料无需物理分选等一系列预处理工序,烟化区107产出的合金中Cu、Sn、Au、Ag、Pt的回收率均≥90wt%,熔炼区105产出的炉渣中Cu和Sn的含量均≤1.0wt%,炉渣无需进一步贫化处理即可直接废弃,工艺简便,金属综合回收率高,缩短了处理流程,提高了处理能力及原料适应性,经济、社会与环境效益更加显著。The electronic waste smelting device 1 of the present invention does not need a series of pretreatment procedures such as physical sorting to process electronic waste. The recovery rates of Cu, Sn, Au, Ag, and Pt in the alloys produced in the fuming zone 107 are all ≥ 90wt%, and the smelting zone 105 The contents of Cu and Sn in the output slag are both ≤1.0wt%, and the slag can be discarded directly without further dilution treatment. The process is simple, the comprehensive metal recovery rate is high, the treatment process is shortened, and the treatment capacity and raw material adaptability are improved. The economic, social and environmental benefits are more significant.
本发明电子废料冶炼装置1及其组成的电子废料、废气处理处理系统是熔炼和烟气无害化处理的系统集成,熔炼装置操作简单,获得的低Cu含量的炉渣可以直接废弃,无需再次贫化。烟气处理后二噁英、溴化氢含量、颗粒物含量、二氧化硫含量等可以确保低于国家允许排放的标准,排放后厂区大气中污染因子含量可以稳定达到国家标准要求。The electronic waste smelting device 1 of the present invention and the electronic waste and waste gas treatment system composed of it is a system integration of smelting and flue gas harmless treatment. change. After flue gas treatment, the content of dioxin, hydrogen bromide, particulate matter, and sulfur dioxide can be guaranteed to be lower than the national allowable emission standards, and the content of pollution factors in the atmosphere of the factory area after emission can stably meet the requirements of national standards.
在本发明的描述中,需要理解的是,术语“中心”、“上”、“下”、“前”、“后”、“竖直”、“水平”、“顶”、“底”、“内”、“外”、“轴向”、“径向”、“周向”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和简化描述,而不是指示或 暗示所指的装置或元件必须具有特定的方位、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。In describing the present invention, it is to be understood that the terms "center", "upper", "lower", "front", "rear", "vertical", "horizontal", "top", "bottom", The orientations or positional relationships indicated by "inner", "outer", "axial", "radial", and "circumferential" are based on the orientations or positional relationships shown in the drawings, and are only for the convenience of describing the present invention and simplifying Describes, but does not indicate or imply that the device or element referred to must have a specific orientation, be constructed in a specific orientation, and operate in a specific orientation, and therefore should not be construed as limiting the invention.
此外,术语“第一”、“第二”仅用于描述目的,而不能理解为指示或暗示相对重要性或者隐含指明所指示的技术特征的数量。由此,限定有“第一”、“第二”的特征可以明示 或者隐含地包括至少一个该特征。In addition, the terms "first" and "second" are used for descriptive purposes only, and cannot be interpreted as indicating or implying relative importance or implicitly specifying the quantity of indicated technical features. Thus, features defined as "first" and "second" may explicitly or implicitly include at least one of these features.
在本发明中,除非另有明确的规定和限定,术语“安装”、“相连”、“连接”、“固定”等术语应做广义理解,例如,可以是固定连接,也可以是可拆卸连接,或成一体;可以是 机械连接,也可以是电连接或彼此可通讯;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或两个元件的相互作用关系,除非另有明确的限定。对于 本领域的普通技术人员而言,可以根据具体情况理解上述术语在本发明中的具体含义。In the present invention, unless otherwise clearly specified and limited, terms such as "installation", "connection", "connection" and "fixation" should be understood in a broad sense, for example, it can be a fixed connection or a detachable connection , or integrated; can be mechanically connected, can also be electrically connected or can communicate with each other; can be directly connected, can also be indirectly connected through an intermediary, can be the internal communication of two components or the interaction relationship between two components, Unless expressly defined otherwise. Those of ordinary skill in the art can understand the specific meanings of the above terms in the present invention according to specific situations.
在本发明中,除非另有明确的规定和限定,第一特征在第二特征“上”或“下”可 以是第一和第二特征直接接触,或第一和第二特征通过中间媒介间接接触。而且,第 一特征在第二特征“上方”可以是第一特征在第二特征正上方或斜上方,或仅仅表示 第一特征水平高度高于第二特征。第一特征在第二特征“下方”可以是第一特征在第 二特征正下方或斜下方,或仅仅表示第一特征水平高度小于第二特征。In the present invention, unless otherwise clearly specified and limited, the first feature may be in direct contact with the first feature or the first and second feature may be in direct contact with the second feature through an intermediary. touch. Moreover, the fact that the first feature is "above" the second feature may mean that the first feature is directly above or obliquely above the second feature, or simply means that the level of the first feature is higher than that of the second feature. The fact that the first feature is "below" the second feature may mean that the first feature is directly below or obliquely below the second feature, or simply means that the first feature is less horizontal than the second feature.
在本说明书的描述中,参考术语“实施例”、“具体实施例”、“示例”或“具体示例”等的描述意指结合该实施例或示例描述的具体特征、结构、材料或者特点包含于本发明的至少一个实施例或示例中。在本说明书中,对上述术语的示意性表述不必须针对的是相同的实施例或示例。而且,描述的具体特征、结构、材料或者特点可以在任一个或多个实施 例或示例中以合适的方式结合。此外,在不相互矛盾的情况下,本领域的技术人员可以将 本说明书中描述的不同实施例或示例以及不同实施例或示例的特征进行结合和组合。In the description of this specification, descriptions with reference to the terms "embodiment", "specific embodiment", "example" or "specific example" mean that specific features, structures, materials or characteristics described in conjunction with the embodiment or example include In at least one embodiment or example of the invention. In this specification, the schematic representations of the above terms are not necessarily directed to the same embodiment or example. Furthermore, the specific features, structures, materials or characteristics described may be combined in any suitable manner in any one or more embodiments or examples. In addition, those skilled in the art can combine and combine different embodiments or examples and features of different embodiments or examples described in this specification without conflicting with each other.
尽管上面已经示出和描述了本发明的实施例,可以理解的是,上述实施例是示例性的, 不能理解为对本发明的限制,本领域的普通技术人员在本发明的范围内可以对上述实施例 进行变化、修改、替换和变型。Although the embodiments of the present invention have been shown and described above, it can be understood that the above embodiments are exemplary and should not be construed as limiting the present invention, and those skilled in the art can make the above-mentioned The embodiments are subject to changes, modifications, substitutions and variations.
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