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WO2018040264A1 - Organic polymer waste material treatment device - Google Patents

Organic polymer waste material treatment device Download PDF

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Publication number
WO2018040264A1
WO2018040264A1 PCT/CN2016/103331 CN2016103331W WO2018040264A1 WO 2018040264 A1 WO2018040264 A1 WO 2018040264A1 CN 2016103331 W CN2016103331 W CN 2016103331W WO 2018040264 A1 WO2018040264 A1 WO 2018040264A1
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Prior art keywords
flue gas
waste
cavity
oxygen
gas
Prior art date
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Ceased
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PCT/CN2016/103331
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French (fr)
Chinese (zh)
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WO2018040264A8 (en
Inventor
万志群
朱泽鑫
陈永明
朱锡鑫
朱锡勇
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Guangdong New Environmental Protection Technologies Co Ltd
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Guangdong New Environmental Protection Technologies Co Ltd
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Application filed by Guangdong New Environmental Protection Technologies Co Ltd filed Critical Guangdong New Environmental Protection Technologies Co Ltd
Priority to DE112016000566.0T priority Critical patent/DE112016000566B4/en
Priority to JP2019512808A priority patent/JP2019532798A/en
Priority to US15/576,132 priority patent/US20190218461A1/en
Publication of WO2018040264A1 publication Critical patent/WO2018040264A1/en
Publication of WO2018040264A8 publication Critical patent/WO2018040264A8/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
    • C10B53/07—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form of solid raw materials consisting of synthetic polymeric materials, e.g. tyres
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING 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
    • C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
    • C10G1/10—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal from rubber or rubber waste
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING 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
    • C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
    • C10G1/002—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal in combination with oil conversion- or refining processes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
    • B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
    • B09B3/40—Destroying solid waste or transforming solid waste into something useful or harmless involving thermal treatment, e.g. evaporation
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B47/00—Destructive distillation of solid carbonaceous materials with indirect heating, e.g. by external combustion
    • C10B47/28—Other processes
    • C10B47/32—Other processes in ovens with mechanical conveying means
    • C10B47/44—Other processes in ovens with mechanical conveying means with conveyor-screws
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B51/00—Destructive distillation of solid carbonaceous materials by combined direct and indirect heating
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B57/00—Other carbonising or coking processes; Features of destructive distillation processes in general
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING 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
    • C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/44—Details; Accessories
    • F23G5/442—Waste feed arrangements
    • F23G5/444—Waste feed arrangements for solid waste
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/44—Details; Accessories
    • F23G5/46—Recuperation of heat
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
    • F23G7/12—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of plastics, e.g. rubber
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2200/00—Waste incineration
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2203/00—Furnace arrangements
    • F23G2203/20—Rotary drum furnace
    • F23G2203/208—Rotary drum furnace with interior agitating members
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2203/00—Furnace arrangements
    • F23G2203/80—Furnaces with other means for moving the waste through the combustion zone
    • F23G2203/801—Furnaces with other means for moving the waste through the combustion zone using conveyors
    • F23G2203/8013—Screw conveyors
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2204/00—Supplementary heating arrangements
    • F23G2204/10—Supplementary heating arrangements using auxiliary fuel
    • F23G2204/103—Supplementary heating arrangements using auxiliary fuel gaseous or liquid fuel
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2206/00—Waste heat recuperation
    • F23G2206/10—Waste heat recuperation reintroducing the heat in the same process, e.g. for predrying
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2206/00—Waste heat recuperation
    • F23G2206/20—Waste heat recuperation using the heat in association with another installation
    • F23G2206/203—Waste heat recuperation using the heat in association with another installation with a power/heat generating installation
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2208/00—Safety aspects
    • F23G2208/10—Preventing or abating fire or explosion, e.g. by purging
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2209/00—Specific waste
    • F23G2209/28—Plastics or rubber like materials
    • 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
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00—Combustion technologies with mitigation potential
    • Y02E20/12—Heat utilisation in combustion or incineration of waste
    • 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
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/141—Feedstock
    • Y02P20/143—Feedstock the feedstock being recycled material, e.g. plastics
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00—Technologies for solid waste management
    • Y02W30/50—Reuse, recycling or recovery technologies
    • Y02W30/62—Plastics recycling; Rubber recycling

Definitions

  • the invention relates to a polymer waste material processing technology, and particularly relates to an organic polymer waste material processing device.
  • the first reaction of polymer (organic) waste in the high temperature field is gasification rather than combustion, and the alkane flammable gas produced by the product is thick and viscous with high volatilization. Therefore, the complete combustion of the polymer (organic) waste must be a combustion process that is all gas phase and must be completed in one space.
  • the object of the present invention is to provide an organic polymer waste material processing device, which is mainly for the decomposition treatment and effective utilization of organic polymer waste materials, and the system is harmless to the atmospheric environment, and is energy-saving and environmentally friendly. High recovery.
  • the invention relates to an organic polymer waste material processing device, which mainly comprises a flue gas circulation system, a weak oxygen circulation de-chaining device, an oil and gas separation system and a waste residue collection system, and the weak oxygen circulation de-chaining device is divided into an inner cavity and an outer cavity.
  • the cavity and the flue gas circulation system transport the low-temperature weak oxygen gas into the inner cavity, transport the high-temperature flue gas through the outer cavity, and then re-enter the flue gas circulation system, and enter the oil and gas separation system and the waste residue collection system respectively after the reaction of the inner cavity.
  • the feeding end of the inner cavity of the weak oxygen circulation de-chaining device is connected to the mixing portion, the discharging end of the inner cavity is connected to the separating portion, and the weak oxygen circulating de-chaining device is provided with a U-shaped pipe communicating with the outer cavity.
  • a side of the mixing unit is provided with a storage bin, a vibrating feeder and a screw conveyor from top to bottom,

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Processing Of Solid Wastes (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
  • Gasification And Melting Of Waste (AREA)

Abstract

本发明提供一种有机高分子废弃物料处理装置，主要由烟气循环系统、弱氧循环脱链装置、油气分离系统及废渣收集系统组成，所述弱氧循环脱链装置分为内腔及外腔，烟气循环系统将低温弱氧气体输送进入内腔进行脱链反应、将高温烟气输送经过外腔进行辅助加温后重新进入烟气循环系统，废弃物弱氧脱链反应后由内腔反应后分别进入油气分离系统及废渣收集系统，形成油、气、渣的高效分离。本发明采用无氧或弱氧脱链反应方式，使高分子分解后有害物质沉降收集，不排入大气影响生态环境，其烟气多通道循环使用，达到节能减排的有益效果，符合科学发展观。The invention provides an organic polymer waste material processing device, which is mainly composed of a flue gas circulation system, a weak oxygen circulation de-chaining device, an oil and gas separation system and a waste residue collection system, and the weak oxygen circulation de-chaining device is divided into an inner cavity and an outer cavity. The cavity and the flue gas circulation system transport the low-temperature weak oxygen gas into the inner cavity for the de-chain reaction, and the high-temperature flue gas is transported through the outer cavity for auxiliary heating and then re-enters the flue gas circulation system, and the waste is weakly oxygen-de-chained and reacted internally. After the cavity reaction, it enters the oil and gas separation system and the waste residue collection system respectively, forming an efficient separation of oil, gas and slag. The invention adopts an oxygen-free or weak oxygen de-chain reaction mode to collect and collect harmful substances after decomposition of the polymer, and does not discharge into the atmosphere to affect the ecological environment, and the flue gas is recycled in multiple channels, thereby achieving the beneficial effects of energy saving and emission reduction, and is in line with scientific development. View.

Description

一种有机高分子废弃物料处理装置Organic polymer waste material processing device 技术领域Technical field

本发明涉及高分子废弃物料处理技术，特指一种有机高分子废弃物料处理装置。The invention relates to a polymer waste material processing technology, and particularly relates to an organic polymer waste material processing device.

背景技术Background technique

高分子(有机)废弃物的完全燃烧技术是世界性难题，针对高分子(有机)废弃物热能转化、灭害减量高端市场需求的形成，迫使我们尽快地进行科学发展观的调整。高分子有机废物是一种多基的、组份和化学结构极为复杂的；甚至含阻燃组份的；固、液、气相的高分子(有机)废弃物。依据国家环保部现行的生活垃圾、危险废物、医疗废弃物相关标准和技术规范所涉及的，符合高分子(有机)废物燃烧特性的典型高分子(有机)废弃物有：废塑料；废橡胶；废油漆油墨；沥青质残渣油；动植物纤维、蛋白、脂肪等等。The complete combustion technology of polymer (organic) waste is a worldwide problem. The formation of high-end market demand for thermal energy conversion and destruction of polymer (organic) wastes forces us to adjust the scientific development concept as soon as possible. High-molecular organic waste is a multi-component, complex component and chemical structure; even a flame retardant component; solid, liquid, gas phase polymer (organic) waste. According to the current national environmental protection department's current domestic garbage, hazardous waste, medical waste related standards and technical specifications, typical polymer (organic) wastes that meet the combustion characteristics of polymer (organic) waste are: waste plastics; waste rubber; Waste paint ink; asphaltene residue oil; animal and plant fiber, protein, fat and so on.

高分子(有机)废物在高温场的第一反应，是气化而不是燃烧，其所生成的烷烃类可燃气体，呈浓黑粘稠状具高挥发扩散性。因此高分子(有机)废物的完全燃烧必然是全气相的、必须在空间一次性完成的燃烧反应过程。The first reaction of polymer (organic) waste in the high temperature field is gasification rather than combustion, and the alkane flammable gas produced by the product is thick and viscous with high volatilization. Therefore, the complete combustion of the polymer (organic) waste must be a combustion process that is all gas phase and must be completed in one space.

当前，很难找到一台真正不冒黑烟垃圾焚烧炉，其主要原因是高分子(有机)废弃物难以实现完全燃烧，高分子聚合物上下游产品的工业园、废五金拆解产业园、畜禽养殖场、火葬场等所在地，则是高分子(有机)废弃物的重灾区，成了有机污染物和持久性有机污染物扩散的源头。At present, it is difficult to find a real black smoke-free waste incinerator. The main reason is that polymer (organic) waste is difficult to achieve complete combustion, industrial parks for upstream and downstream products of polymer, waste metal dismantling industrial park, Livestock and poultry farms, crematoriums and other places are the hardest hit areas for polymer (organic) waste, and have become the source of the spread of organic pollutants and persistent organic pollutants.

发明内容Summary of the invention

本发明的目的在于针对已有的技术现状，提供一种有机高分子废弃物料处理装置，主要为有机高分子废弃物料的分解处理及有效利用，且该系统对大气环境无害，其节能、环保、高回收。The object of the present invention is to provide an organic polymer waste material processing device, which is mainly for the decomposition treatment and effective utilization of organic polymer waste materials, and the system is harmless to the atmospheric environment, and is energy-saving and environmentally friendly. High recovery.

为达到上述目的，本发明采用如下技术方案：In order to achieve the above object, the present invention adopts the following technical solutions:

本发明为一种有机高分子废弃物料处理装置，主要由烟气循环系统、弱氧循环脱链装置、油气分离系统及废渣收集系统组成，所述弱氧循环脱链装置分为内腔及外腔，烟气循环系统将低温弱氧气体输送进入内腔、将高温烟气输送经过外腔后重新进入烟气循环系统，由内腔反应后分别进入油气分离系统及废渣收集系统。The invention relates to an organic polymer waste material processing device, which mainly comprises a flue gas circulation system, a weak oxygen circulation de-chaining device, an oil and gas separation system and a waste residue collection system, and the weak oxygen circulation de-chaining device is divided into an inner cavity and an outer cavity. The cavity and the flue gas circulation system transport the low-temperature weak oxygen gas into the inner cavity, transport the high-temperature flue gas through the outer cavity, and then re-enter the flue gas circulation system, and enter the oil and gas separation system and the waste residue collection system respectively after the reaction of the inner cavity.

上述方案中，弱氧循环脱链装置内腔的进料端连接混合部，内腔的出料端连接分离部，且弱氧循环脱链装置上设有U型管道与外腔连通。In the above solution, the feeding end of the inner cavity of the weak oxygen circulation de-chaining device is connected to the mixing portion, the discharging end of the inner cavity is connected to the separating portion, and the weak oxygen circulating de-chaining device is provided with a U-shaped pipe communicating with the outer cavity.

进一步的，混合部一侧由上至下依次设有储料仓、振动给料器及螺旋输送机，所述 Further, a side of the mixing unit is provided with a storage bin, a vibrating feeder and a screw conveyor from top to bottom,

Claims (1)

Figure PCTCN2016103331-appb-100001
Figure PCTCN2016103331-appb-100001
PCT/CN2016/103331 2016-08-31 2016-10-26 Organic polymer waste material treatment device Ceased WO2018040264A1 (en)

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Application Number Priority Date Filing Date Title
DE112016000566.0T DE112016000566B4 (en) 2016-08-31 2016-10-26 Organic polymer waste materials treatment facility
JP2019512808A JP2019532798A (en) 2016-08-31 2016-10-26 Organic polymer waste treatment equipment
US15/576,132 US20190218461A1 (en) 2016-08-31 2016-10-26 Organic polymer waste material disposal device

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CN201610773749.9A CN106244186B (en) 2016-08-31 2016-08-31 A kind of organic polymer waste material processing unit
CN201610773749.9 2016-08-31

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