JP2000225384A - Method for separating heat-meltable plastic from waste, method for volume reducing treatment of waste, and apparatus for heat treatment of waste - Google Patents
Method for separating heat-meltable plastic from waste, method for volume reducing treatment of waste, and apparatus for heat treatment of wasteInfo
- Publication number
- JP2000225384A JP2000225384A JP11149655A JP14965599A JP2000225384A JP 2000225384 A JP2000225384 A JP 2000225384A JP 11149655 A JP11149655 A JP 11149655A JP 14965599 A JP14965599 A JP 14965599A JP 2000225384 A JP2000225384 A JP 2000225384A
- Authority
- JP
- Japan
- Prior art keywords
- waste
- plastic
- heating
- heat
- container
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 229920003023 plastic Polymers 0.000 title claims abstract description 125
- 239000004033 plastic Substances 0.000 title claims abstract description 125
- 238000010438 heat treatment Methods 0.000 title claims abstract description 110
- 239000002699 waste material Substances 0.000 title claims abstract description 95
- 238000000034 method Methods 0.000 title claims abstract description 34
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 56
- 238000005192 partition Methods 0.000 claims abstract description 37
- 239000007789 gas Substances 0.000 claims description 47
- 239000012943 hotmelt Substances 0.000 claims description 21
- 239000001301 oxygen Substances 0.000 claims description 21
- 229910052760 oxygen Inorganic materials 0.000 claims description 21
- 238000000926 separation method Methods 0.000 claims description 8
- 239000002918 waste heat Substances 0.000 claims description 7
- 238000011038 discontinuous diafiltration by volume reduction Methods 0.000 claims description 3
- 239000000463 material Substances 0.000 abstract description 13
- 230000003472 neutralizing effect Effects 0.000 abstract description 6
- 239000003795 chemical substances by application Substances 0.000 abstract description 4
- 238000011084 recovery Methods 0.000 abstract description 3
- 238000007599 discharging Methods 0.000 abstract 1
- 239000002893 slag Substances 0.000 abstract 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 16
- 229920005989 resin Polymers 0.000 description 15
- 239000011347 resin Substances 0.000 description 15
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 12
- BZHJMEDXRYGGRV-UHFFFAOYSA-N Vinyl chloride Chemical compound ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 description 12
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 description 12
- 229910000041 hydrogen chloride Inorganic materials 0.000 description 12
- 239000000126 substance Substances 0.000 description 11
- 230000002378 acidificating effect Effects 0.000 description 9
- -1 polyethylene Polymers 0.000 description 9
- 239000004698 Polyethylene Substances 0.000 description 6
- 229920000573 polyethylene Polymers 0.000 description 6
- 230000001877 deodorizing effect Effects 0.000 description 5
- 239000002906 medical waste Substances 0.000 description 5
- 238000002844 melting Methods 0.000 description 5
- 230000008018 melting Effects 0.000 description 5
- 229910052751 metal Inorganic materials 0.000 description 5
- 239000002184 metal Substances 0.000 description 5
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 4
- 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 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 239000002253 acid Substances 0.000 description 3
- 239000000460 chlorine Substances 0.000 description 3
- 229910052801 chlorine Inorganic materials 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 238000001704 evaporation Methods 0.000 description 3
- 239000000835 fiber Substances 0.000 description 3
- 238000004064 recycling Methods 0.000 description 3
- 238000007789 sealing Methods 0.000 description 3
- 238000005979 thermal decomposition reaction Methods 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 2
- 239000004743 Polypropylene Substances 0.000 description 2
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- 229910000019 calcium carbonate Inorganic materials 0.000 description 2
- 239000011521 glass Substances 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000010813 municipal solid waste Substances 0.000 description 2
- 229920001155 polypropylene Polymers 0.000 description 2
- 239000013049 sediment Substances 0.000 description 2
- 239000004449 solid propellant Substances 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- 206010021143 Hypoxia Diseases 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 210000004369 blood Anatomy 0.000 description 1
- 239000008280 blood Substances 0.000 description 1
- 210000001124 body fluid Anatomy 0.000 description 1
- 239000010839 body fluid Substances 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 125000001309 chloro group Chemical group Cl* 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 238000007033 dehydrochlorination reaction Methods 0.000 description 1
- 230000000249 desinfective effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005674 electromagnetic induction Effects 0.000 description 1
- 239000005038 ethylene vinyl acetate Substances 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000002657 fibrous material Substances 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000012634 fragment Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 229910052602 gypsum Inorganic materials 0.000 description 1
- 239000010440 gypsum Substances 0.000 description 1
- 230000001146 hypoxic effect Effects 0.000 description 1
- 208000015181 infectious disease Diseases 0.000 description 1
- 230000002458 infectious effect Effects 0.000 description 1
- 239000010781 infectious medical waste Substances 0.000 description 1
- 229910010272 inorganic material Inorganic materials 0.000 description 1
- 239000011147 inorganic material Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000011810 insulating material Substances 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000010297 mechanical methods and process Methods 0.000 description 1
- 239000008267 milk Substances 0.000 description 1
- 210000004080 milk Anatomy 0.000 description 1
- 235000013336 milk Nutrition 0.000 description 1
- 239000010812 mixed waste Substances 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 229920001200 poly(ethylene-vinyl acetate) Polymers 0.000 description 1
- 229920000515 polycarbonate Polymers 0.000 description 1
- 239000004417 polycarbonate Substances 0.000 description 1
- 229920005668 polycarbonate resin Polymers 0.000 description 1
- 239000004431 polycarbonate resin Substances 0.000 description 1
- 239000005020 polyethylene terephthalate Substances 0.000 description 1
- 229920000139 polyethylene terephthalate Polymers 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 239000004800 polyvinyl chloride Substances 0.000 description 1
- 229920000915 polyvinyl chloride Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
- 238000000197 pyrolysis Methods 0.000 description 1
- 238000009877 rendering Methods 0.000 description 1
- 238000011012 sanitization Methods 0.000 description 1
- 238000007790 scraping Methods 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 1
- 229920002554 vinyl polymer Polymers 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
- 239000013585 weight reducing agent Substances 0.000 description 1
- 239000000080 wetting agent Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
-
- 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
Landscapes
- Processing Of Solid Wastes (AREA)
- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、分別が実質的に不
可能な感染性プラスチック製品等の熱溶融性プラスチッ
クを含む医療用廃棄物や熱溶融性プラスチックを含む一
般廃棄物から熱溶融性プラスチックを分離するととも
に、塩化ビニル樹脂等の塩素含有樹脂を熱分解させて塩
化水素を除去することにより、熱溶融プラスチックの固
形燃料化、リサイクル、熱不溶融性廃棄物の熱分解、焼
却、埋め立て等を効率的に行えるようにする廃棄物から
の熱溶融性プラスチックの分離方法、廃棄物の加熱減容
処理方法及びそのための装置に関する。BACKGROUND OF THE INVENTION The present invention relates to heat-meltable plastics from medical wastes containing heat-meltable plastics such as infectious plastic products and the like and general wastes containing heat-meltable plastics, which are substantially inseparable. And thermal decomposition of chlorine-containing resins such as vinyl chloride resin to remove hydrogen chloride, making hot-melt plastics solid fuels, recycling, thermal decomposition of heat-insoluble waste, incineration, landfill, etc. The present invention relates to a method for separating hot-melt plastic from waste, a method for heating and reducing the volume of waste, and an apparatus therefor, which enables efficient wastewater treatment.
【0002】[0002]
【従来の技術】廃プラスチックは、本来は分別してリサ
イクルすることが望ましいが、分別に危険を伴う医療用
の感染性廃棄物や分別されずにプラスチックが混入した
一般の廃棄物(ゴミ)を、プラスチックと紙、繊維、そ
の他の廃棄物成分とに分離することは極めて困難であ
り、現在は、一般の廃棄物はプラスチックを含んだまま
焼却処分や埋め立て処分されているのが実情である。ま
た、医療用廃棄物は専門処理業者により焼却処分されて
いる。これらの廃棄物は、焼却に際してプラスチックが
急激に分解し、多量のガスを発生するため、高熱を発し
て炉の寿命を短くするだけでなく、黒煙や悪臭、ダイオ
キシンの発生等が問題となっている。また、これらの廃
棄物は無酸素熱分解法によって分解させることによりダ
イオキシンの発生を抑えることができるが、タールが発
生するという問題がある。そのために、このよう廃棄物
から熱溶融性プラスチックを分離・回収し、あるいは、
可燃性処理物を燃料として利用するために、熱溶融性プ
ラスチックを含む医療用廃棄物から熱溶融性プラスチッ
クと熱不溶融性成分とに分離する方法が提案されてい
る。2. Description of the Related Art Waste plastics are originally desirably separated and recycled. However, infectious wastes for medical use which involve danger of separation and general wastes (garbage) in which plastics are mixed without being separated, It is extremely difficult to separate plastic from paper, fiber, and other waste components. At present, general waste is incinerated or landfilled while containing plastic. In addition, medical waste is incinerated by specialized processors. In these wastes, plastics are rapidly decomposed during incineration, and a large amount of gas is generated, which not only generates high heat and shortens the life of the furnace, but also causes problems such as black smoke, bad smell, and generation of dioxin. ing. In addition, the generation of dioxin can be suppressed by decomposing these wastes by an oxygen-free thermal decomposition method, but there is a problem that tar is generated. For this purpose, the hot-melt plastic is separated and collected from the waste, or
In order to use the combustible material as a fuel, there has been proposed a method of separating a heat-fusible plastic and a heat-insoluble component from medical waste containing the heat-fusible plastic.
【0003】例えば、特開平8−57442号公報で
は、熱溶融性プラスチックを含む医療用廃棄物を、加熱
容器内の格子部材等で仕切られた上部で酸素遮断下に外
部から加熱して該プラスチックを溶融、流動状態とし、
この溶融プラスチックを格子部材等を通過させて該容器
の底部に設けた容器内に集め、プラスチックと非プラス
チック材料とを分離する方法が提案されている。この方
法では加熱処理後に装置全体を冷却することにより、殺
菌処理され、分別された固体プラスチックが回収され
る。加熱時に発生する臭気成分は加熱容器に接続された
アフターバーナーで燃焼させ、フィルターユニットを通
過させて大気中に放出される。[0003] For example, in Japanese Patent Application Laid-Open No. Hei 8-57442, medical waste containing a heat-meltable plastic is heated from the outside under an oxygen shield at an upper part partitioned by a lattice member or the like in a heating vessel. Into a molten, fluid state,
A method has been proposed in which the molten plastic is passed through a lattice member or the like, collected in a container provided at the bottom of the container, and separated from the plastic and the non-plastic material. In this method, the whole apparatus is cooled after the heat treatment, and the sterilized and separated solid plastic is collected. Odor components generated at the time of heating are burned by an afterburner connected to a heating container, and are discharged into the atmosphere through a filter unit.
【0004】また、特開平10−168224号公報に
は、ポリエチレンを含む可燃性の一般ごみを上記の方法
と同様に無酸素状態で外部から加熱し、ポリエチレンを
溶融させて分離、回収する方法及び回収ポリエチレン等
の廃プラスチックを加熱容器中で減圧下、無酸素状態で
外部から加熱して熱分解させ、生成ガス中の凝縮性成分
を油分として回収し、油分以外のガス(例えば、塩化水
素)を中和等により無害化する方法が開示されている。
この方法においては加熱容器下部に流下する溶融ポリエ
チレンは、取り出しドレンから溶融状態で取り出され
る。Japanese Patent Application Laid-Open No. H10-168224 discloses a method of heating combustible general waste containing polyethylene from the outside in an oxygen-free state in the same manner as the above method to melt and separate and recover polyethylene. Waste plastic such as recovered polyethylene is heated from the outside in a heating vessel under reduced pressure and in an oxygen-free state to be thermally decomposed, and the condensable components in the produced gas are recovered as oil, and a gas other than oil (eg, hydrogen chloride) A method for rendering harmless by neutralization or the like is disclosed.
In this method, the molten polyethylene flowing down to the lower portion of the heating vessel is taken out of the take-out drain in a molten state.
【0005】[0005]
【発明が解決しようとする課題】これらの方法によっ
て、廃棄物中の熱溶融性プラスチックと紙、金属等の熱
不溶性成分とが容易に分離され、塩化ビニル樹脂等の塩
化水素発生源となるプラスチックは熱分解し、分離され
た熱溶融性プラスチック中には塩素を含むプラスチック
は含まれないので、分離されたプラスチックはリサイク
ル使用や、固形燃料等としても使用可能である。By these methods, the heat-meltable plastic in the waste and the heat-insoluble component such as paper and metal can be easily separated, and the plastic used as a hydrogen chloride generating source such as a vinyl chloride resin can be obtained. Is thermally decomposed and the plastic containing chlorine is not contained in the separated hot-melt plastic, so the separated plastic can be used for recycling or as a solid fuel.
【0006】しかしながら、これらの方法では以下のよ
うな問題がある。上記の前者の方法では、加熱容器と溶
融プラスチックを溜める容器とが同一のキャビネット内
に設置されているために、分離されたプラスチック成分
を取り出すために、キャビネット内の加熱容器及びプラ
スチック回収容器を同時に冷却する必要がある。引き続
いて廃棄物を加熱処理する場合には再度加熱しなければ
ならず、加熱エネルギーの無駄が多い。また、固化した
プラスチック成分は容器に固着し、容器から固化プラス
チックを取り出す作業が大変であるという問題もある。
また、後者の方法においては、溶融プラスチックの加熱
容器からの取り出しはプラスチックが溶融した状態で配
管を通しておこなうことから配管の加熱が必要であり、
配管に固着したプラスチックの除去作業に多大な労力と
時間を要するという問題がある。However, these methods have the following problems. In the former method, since the heating container and the container for storing the molten plastic are installed in the same cabinet, the heating container and the plastic collection container in the cabinet are simultaneously removed to take out the separated plastic components. Requires cooling. If the waste is subsequently heated, it must be heated again, which wastes heating energy. There is also a problem that the solidified plastic component adheres to the container, and it is difficult to take out the solidified plastic from the container.
In addition, in the latter method, since the removal of the molten plastic from the heating container is performed through the pipe in a state where the plastic is melted, it is necessary to heat the pipe,
There is a problem that a large amount of labor and time are required for removing the plastic adhered to the pipe.
【0007】従って、本発明は上記の事情に鑑みてなさ
れたものであり、本発明の目的は、上記の問題点が解決
され、廃棄物から分離したプラスチックの回収が容易
で、回収に加熱を要しない廃棄物からの熱溶融性プラス
チックの分離方法及び熱溶融性プラスチックを含む廃棄
物の減容、消毒(殺菌)、無臭化が可能な廃棄物の加熱
処理方法並びにそのための廃棄物加熱処理装置を提供す
ることである。Therefore, the present invention has been made in view of the above circumstances, and an object of the present invention is to solve the above-mentioned problems, to facilitate the recovery of plastic separated from waste, and to use heating for recovery. Method for separating hot-melt plastic from unnecessary waste, and method for heat-treating waste capable of reducing, disinfecting (sterilizing), and deodorizing waste containing hot-melt plastic, and waste heat treatment apparatus therefor It is to provide.
【0008】[0008]
【課題を解決するための手段】かかる本発明によれば、
熱溶融性プラスチックを含む廃棄物を、仕切りで上下二
室に区分けされた加熱容器の上部室に入れ、該廃棄物を
無酸素あるいは低酸素状態で加熱して該廃棄物中の熱溶
融性プラスチックを溶融させ、該廃棄物を熱溶融性プラ
スチックと熱非溶融性廃棄物とに分離するに際し、加熱
溶融させたプラスチックを、溶融プラスチックを流下可
能に形成された仕切りを通して加熱容器の下部室の下部
に設けた水槽に落下させ、固化させることを特徴とする
廃棄物から熱溶融性プラスチックを分離する方法及び上
記の熱溶融性プラスチックが分離された熱非溶融性廃棄
物を無酸素あるいは低酸素状態で更に加熱して熱分解さ
せることを特徴とする廃棄物の減容処理方法並びに熱溶
融性プラスチックを含む廃棄物を無酸素あるいは低酸素
状態で加熱する加熱容器とその下部に設けられた水槽と
から構成され、上記加熱容器は、溶融プラスチックが流
下可能に形成された仕切りで上下二室に区分けされ、上
部室に上記廃棄物を入れて上記状態で加熱し、上記仕切
りを通して流下する溶融プラスチックを落下及び固化さ
せる水槽が下部室の下部に設置されていることを特徴と
する廃棄物の加熱処理装置が提供される。According to the present invention,
The waste containing the heat-fusible plastic is placed in the upper chamber of a heating vessel divided into upper and lower compartments by a partition, and the waste is heated in an oxygen-free or low-oxygen state, and the heat-fusible plastic in the waste is heated. When the waste is separated into hot-melt plastic and hot-non-meltable waste, the heated and melted plastic is passed through a partition formed so that the molten plastic can flow down to the lower part of the lower chamber of the heating vessel. A method for separating hot-melt plastic from waste characterized by being dropped into a water tank provided and solidified, and the above-mentioned hot non-meltable waste from which hot-melt plastic is separated is anoxic or hypoxic. And a method for reducing the volume of waste, characterized in that it is further heated and thermally decomposed, and the waste containing heat-meltable plastic is heated in an oxygen-free or low-oxygen state. The heating container is composed of a container and a water tank provided at the lower part thereof.The heating container is divided into upper and lower chambers by a partition formed so that molten plastic can flow down, and the waste is put in the upper chamber and heated in the above state. In addition, there is provided a waste heat treatment apparatus, wherein a water tank for dropping and solidifying molten plastic flowing down through the partition is provided at a lower portion of the lower chamber.
【0009】[0009]
【発明の実施の形態】次に発明の実施の形態を挙げて本
発明を更に詳細に説明する。本発明における熱溶融性プ
ラスチックを含む廃棄物からの該プラスチックの分離
は、加熱容器中の該廃棄物を無酸素下あるいは低酸素濃
度下の酸素遮断状態で加熱して熱溶融性プラスチックを
溶融させて該廃棄物から分離することは前記の提案方法
と同様であるが、分離して流下する溶融プラスチックを
加熱容器の下部に設けた水槽に落下させ、冷却固化させ
ることが特徴であり、分離したプラスチックの回収が極
めて容易である。BEST MODE FOR CARRYING OUT THE INVENTION Next, the present invention will be described in more detail with reference to embodiments of the present invention. In the present invention, the separation of the plastic from the waste containing the heat-meltable plastic is performed by heating the waste in a heating vessel in an oxygen-free state under an oxygen-free or low oxygen concentration to melt the heat-meltable plastic. Is separated from the waste by the same method as the above-mentioned proposed method, except that the molten plastic that separates and flows down is dropped into a water tank provided at the lower part of the heating vessel, and is cooled and solidified. It is very easy to collect plastic.
【0010】本発明が処理対象とする廃棄物は、加熱に
より溶融して流動化するプラスチックを含む廃棄物であ
れば特に制限されず、一般廃棄物、医療用廃棄物等が挙
げられる。又、プラスチックの種類も制限されず、例え
ば、ポリエチレン、ポリプロピレン、ポリエチレンテレ
フタレート、ポリカーボネート、エチレン−酢酸ビニル
共重合体等の結晶性を有するもの、ポリスチレン、ポリ
塩化ビニル(塩化ビニル樹脂)等の非結晶性のものが挙
げられる。The waste to be treated by the present invention is not particularly limited as long as the waste contains plastic which is melted and fluidized by heating, and examples thereof include general waste and medical waste. Further, the kind of plastic is not limited. For example, those having crystallinity such as polyethylene, polypropylene, polyethylene terephthalate, polycarbonate, and ethylene-vinyl acetate copolymer, and non-crystals such as polystyrene and polyvinyl chloride (vinyl chloride resin) Sex.
【0011】本発明においては、先ず、熱溶融性プラス
チック(以下では単にプラスチックと称することがあ
る。)を含む廃棄物を仕切りで上下2室に区分けされた
加熱容器の上部室に投入し、無酸素下あるいは低酸素濃
度下に加熱してプラスチックを溶融、流動化させる。プ
ラスチックを溶融させて流動化させるための加熱温度
は、プラスチックの種類によって相違はあるが、250
〜300℃の範囲が好ましい。溶融したプラスチックは
廃棄物中を重力で流下し、他の熱不溶融性廃棄物成分と
自然に分離する。プラスチックの分離を促進し、分離を
より確実にするために、プラスチックの分離中は加熱容
器内の温度を上記の範囲に保つことが好ましい。In the present invention, first, waste containing a hot-melt plastic (hereinafter, may be simply referred to as plastic) is put into an upper chamber of a heating vessel which is divided into upper and lower chambers by a partition. The plastic is melted and fluidized by heating under oxygen or low oxygen concentration. The heating temperature for melting and fluidizing the plastic varies depending on the type of the plastic.
The range of -300 ° C is preferred. The molten plastic flows down the waste by gravity and spontaneously separates from the other heat-insoluble waste components. In order to promote the separation of the plastic and to ensure the separation, it is preferable to keep the temperature in the heating vessel in the above range during the separation of the plastic.
【0012】その際、加熱容器内に紙や繊維質等を発火
させる濃度の酸素が存在する場合には、加熱温度を上記
の範囲に保つことは困難となる。更に、酸素濃度が高い
状態で上記の温度範囲を保持することができたとして
も、これはダイオキシンを発生させる条件を作ることに
もなるので、このような意味から加熱容器内の酸素濃度
が高いことは好ましくない。本発明における低酸素濃度
とは、プラスチックが分離された残余の廃棄物が発火し
ない濃度の酸素は存在してもよいことをいう。At this time, if oxygen is present in the heating container at a concentration that ignites paper, fiber, or the like, it is difficult to maintain the heating temperature within the above range. Furthermore, even if the above-mentioned temperature range can be maintained in a state where the oxygen concentration is high, since this also creates conditions for generating dioxin, the oxygen concentration in the heating vessel is high in this sense. It is not preferable. The low oxygen concentration in the present invention means that oxygen may be present at a concentration at which the residual waste from which the plastic is separated does not ignite.
【0013】加熱容器は、通常、加熱容器の外部から電
熱ヒーターやガスバーナー等で加熱される。加熱により
溶融、流動化したプラスチックは、その下部室への流下
を可能とする上下2室の仕切りを通って下部室の下部に
設けられた水槽へ落下し、冷却、固化する。必要により
仕切りを加熱することもできる。又、仕切りを通って流
下するプラスチック流を回転式カッター等で適当な大き
さに切断することによって、分離されたプラスチックを
取り扱い易い形状に固化させることもできる。仕切り
は、溶融、流動化したプラスチックが通過可能に形成さ
れておれば特に制限されず、例えば、適当な開口部を有
する仕切り板、火格子、金網等が挙げられる。The heating vessel is usually heated from outside the heating vessel by an electric heater or a gas burner. The plastic that has been melted and fluidized by heating falls through a partition between the upper and lower chambers that allows the plastic to flow into the lower chamber, falls into a water tank provided at the lower part of the lower chamber, and cools and solidifies. If necessary, the partition can be heated. Further, the separated plastic can be solidified into a shape that can be easily handled by cutting the plastic flow flowing down through the partition into an appropriate size using a rotary cutter or the like. The partition is not particularly limited as long as the molten and fluidized plastic is formed so as to be able to pass through, and examples thereof include a partition plate having a suitable opening, a grate, and a wire mesh.
【0014】尚、上記の加熱温度においては、廃棄物中
にしばしば含まれる塩化ビニル樹脂は分解して塩化水素
を発生する。従って、廃棄物中の熱溶融性プラスチック
が紙、金属等の無機物や繊維質等の熱不溶性の廃棄物成
分と分離するに適切な時間、加熱装置を上記温度に保持
することにより、この間に塩化ビニル樹脂は脱塩化水
素、更には分解し、溶融、流下により分離されるプラス
チック中の塩素含有量は少なくなるので、分離したプラ
スチックのリサイクルあるいは廃棄等に好都合である。
廃棄物中に塩化ビニル樹脂あるいはその他の酸性ガスを
発生する物質が含まれている可能性がある場合には、塩
化水素ガス等の酸性ガスを適当な方法で捕捉することが
必要である。At the above-mentioned heating temperature, the vinyl chloride resin often contained in the waste is decomposed to generate hydrogen chloride. Therefore, by keeping the heating device at the above-mentioned temperature for a time suitable for separating the heat-meltable plastic in the waste from inorganic materials such as paper and metal and heat-insoluble waste components such as fibrous materials, during this time, the chloride is removed. The vinyl resin is dehydrogenated and further decomposed, and the chlorine content in the plastic separated by melting and flowing is reduced, which is convenient for recycling or discarding the separated plastic.
If there is a possibility that the waste contains a vinyl chloride resin or another substance that generates an acidic gas, it is necessary to capture an acidic gas such as a hydrogen chloride gas by an appropriate method.
【0015】分離された熱溶融性プラスチックは水槽か
らベルトコンベヤー等の適当な手段で加熱容器外に取り
出され、リサイクルあるいは廃棄処分、酸素遮断下の熱
分解処理、プラスチック専用焼却炉での焼却処分等に付
すことができる。一方、加熱処理された廃棄物はその中
のプラスチックが除かれることによって減容する。更に
減容するために残余の廃棄物を熱溶融性プラスチックの
分離に引き続いて無酸素又は低酸素濃度雰囲気下に熱分
解させることができる。あるいは、酸素供給下に燃焼さ
せるか、あるいは埋め立て等のこれら以外の処理に付す
こともできる。The separated hot-melt plastic is taken out of the tank by a suitable means such as a belt conveyor from a water tank, and is recycled or disposed of, thermally decomposed under oxygen cutoff, incinerated in a plastic incinerator, etc. Can be attached to On the other hand, the volume of the heat-treated waste is reduced by removing the plastic therein. To further reduce the volume, the residual waste can be pyrolyzed in an oxygen-free or low oxygen concentration atmosphere following separation of the hot melt plastic. Alternatively, it may be burned under an oxygen supply or subjected to other treatment such as landfill.
【0016】残余の廃棄物を酸素遮断下に加熱分解させ
る場合には、通常、400〜600℃に加熱して該廃棄
物を熱分解させる。熱分解の結果、該廃棄物は炭化物と
して回収される。又、残余の廃棄物を酸素の存在下に燃
焼させる場合には発火するまで加熱して燃焼させるか、
あるいは直接該廃棄物に点火して燃焼させる。プラスチ
ック分離後の廃棄物を熱分解させる場合は勿論、廃棄物
からプラスチックを分離するために加熱処理する場合に
も、発生ガス中には前記の酸性ガス以外にも、臭気の発
生源となる若干量の有機物が含まれるので、発生ガス中
の有機物を捕捉又は熱分解してから大気中に放出するこ
とが必要である。In the case where the remaining waste is thermally decomposed under the cutoff of oxygen, the waste is usually heated to 400 to 600 ° C. to thermally decompose the waste. As a result of the pyrolysis, the waste is recovered as char. If the remaining waste is to be burned in the presence of oxygen, heat and burn until ignition,
Alternatively, the waste is directly ignited and burned. In addition to the above-described acid gas, the generated gas may be a source of odor, in addition to the above-mentioned acidic gas, in the case of performing heat treatment to separate the plastic from the waste, as well as in the case of thermally decomposing the waste after separating the plastic. Since an organic substance is contained in an amount, it is necessary to capture or thermally decompose the organic substance in the generated gas before releasing it to the atmosphere.
【0017】上記の熱溶融性プラスチックを含む廃棄物
の加熱処理に用いる装置は、処理する該廃棄物を投入、
加熱するための加熱容器、これを加熱する手段及び溶融
プラスチックを落下させる水槽とから構成される。加熱
容器は、廃棄物を加熱して廃棄物中の熱溶融性プラスチ
ックを溶融させて流動化させる際には酸素(空気)を遮
断することができるものであり、加熱容器内は溶融した
プラスチックが廃棄物中を重力で流下して廃棄物から分
離されるために、溶融プラスチックの通過が可能な仕切
りによって上下2室に仕切られており、上部室に加熱処
理される廃棄物が投入され、廃棄物中から溶融プラスチ
ックは仕切りを通過して下部室に流下する。The apparatus used for the heat treatment of the waste containing the hot-melt plastic includes the waste to be treated,
It comprises a heating vessel for heating, a means for heating the vessel, and a water tank for dropping the molten plastic. The heating vessel can block oxygen (air) when heating the waste to melt and fluidize the hot-melt plastic in the waste. In order to flow down the waste by gravity and to be separated from the waste, it is divided into two upper and lower chambers by a partition through which the molten plastic can pass. Molten plastic flows through the partition and flows down into the lower chamber.
【0018】尚、廃棄物中に、多量の血液や体液等の水
分を多量に含む場合には、例えば、仕切り板の上方に、
円筒状の加熱容器の場合にはその直径方向の軸の周りに
回転可能に取り付けた底を有する、適当な高さの液体蒸
発用容器に廃棄物を載せ、100℃近くに加熱して水分
を蒸発させた後、この容器を回転させて廃棄物を仕切り
板上に落下させてからプラスチックを加熱溶融させた
り、あるいは仕切り板を適当な手段、例えば、開口部を
開閉可能に形成し、多量に水分を含む廃棄物を加熱容器
に仕込む場合には、水分が仕切りを通過しないように開
口部を閉じ、先ずこれらの液体を蒸発させ、次いで仕切
りの開口部を開いてプラスチックを加熱溶融させること
もできる。水分の蒸発手段はこれらの例に限定されるも
のではない。If the waste contains a large amount of water such as a large amount of blood or body fluid, for example,
In the case of a cylindrical heating vessel, the waste is placed on a liquid evaporation vessel of suitable height having a bottom rotatably mounted around its diametric axis and heated to near 100 ° C. to remove moisture. After evaporating, the container is rotated to drop the waste onto the partition plate, and then the plastic is heated and melted, or the partition plate is formed by an appropriate means, for example, by opening and closing the opening, and a large amount is formed. If waste containing water is charged into the heating container, the openings may be closed to prevent moisture from passing through the partition, these liquids may first evaporate, and then the opening of the partition may be opened to heat and melt the plastic. it can. The means for evaporating water is not limited to these examples.
【0019】上記の仕切りは、溶融により流動化したプ
ラスチックが下部室に流下することができるような構造
であればよく、例えば、多数の孔を開けた仕切り板、適
当なメッシュサイズの金網状仕切り板、適当な間隔を有
する火格子様の仕切り桟等が挙げられるが、これらの例
に限定されるものではない。仕切りの下方には流下する
プラスチック流を適当な長さに切断するロータリーカッ
ター等の切断手段を設置することができる。また、プラ
スチックの流下を促進するために電熱ヒーター等の加熱
手段を仕切りに設置することもできる。The partition may have any structure that allows the plastic fluidized by melting to flow down to the lower chamber. For example, a partition plate having a large number of holes, a wire mesh partition having an appropriate mesh size, etc. Examples thereof include a plate, a grate-like partition bar having an appropriate interval, and the like, but are not limited to these examples. Below the partition, cutting means such as a rotary cutter for cutting the flowing plastic stream to an appropriate length can be provided. In addition, a heating means such as an electric heater can be provided in the partition to promote the flow of the plastic.
【0020】加熱容器の形状も特に制限されず、例え
ば、下部室は流動化プラスチックを底部に集め易い円錐
状あるいは四角錐状に、上部室は円筒状あるいは四角筒
状等に形成されたものが挙げられる。尚、上下2室の構
成割合は特に制限されず、溶融プラスチックの流下、分
離がスムーズに行われるように構成すればよい。加熱容
器の加熱手段は、該容器を外部から加熱することができ
るものであれば特に制限されず、例えば、都市ガス、プ
ロパンガス等を使用するバーナーや電熱ヒーター、電磁
誘導加熱装置等が挙げられる。The shape of the heating vessel is not particularly limited. For example, the lower chamber is formed in a conical shape or a quadrangular pyramid which facilitates collection of fluidized plastic at the bottom, and the upper chamber is formed in a cylindrical shape or a square cylindrical shape. No. The composition ratio of the upper and lower two chambers is not particularly limited, and it may be configured so that the flow and separation of the molten plastic are performed smoothly. The heating means of the heating vessel is not particularly limited as long as the vessel can be heated from the outside, and examples thereof include a burner using city gas, propane gas, an electric heater, an electromagnetic induction heating device, and the like. .
【0021】廃棄物から分離した溶融プラスチックを落
下させる水槽は、加熱容器下部室の下部に別途作製した
水槽を設置しても、加熱容器下部を直接水を張ることが
できる構造に形成してもよい。また、加熱容器下端を底
のない開放状態に形成し、この開放下端部を加熱容器と
は独立に設置した水槽に浸し、加熱容器の開放端部を水
で封じることもできる。このようにすることによって、
落下、固化したプラスチックの回収が容易となるだけで
なく、加熱容器の点検、掃除、仕切りの交換等も容易と
なり、含水率の高い廃棄物の処理においては凝縮水によ
る水面の調整も容易に行える等の利点が多く、好ましい
ものである。この場合には、加熱容器の水に浸す部分
は、該容器の他の部分とは断熱効果のあるガスケットを
介してフランジ等で固定することが好ましい。The water tank for dropping the molten plastic separated from the waste can be either a separately prepared water tank below the lower chamber of the heating vessel or a structure in which the lower part of the heating vessel can be directly filled with water. Good. Alternatively, the lower end of the heating vessel may be formed in an open state without a bottom, and the lower end of the opening may be immersed in a water tank installed independently of the heating vessel, and the open end of the heating vessel may be sealed with water. By doing this,
Not only is it easy to collect dropped and solidified plastic, but it is also easy to inspect, clean, and replace partitions in the heating vessel, and easily adjust the water surface with condensed water when treating waste with a high water content. There are many advantages such as these, which are preferable. In this case, it is preferable that the portion of the heating container immersed in water is fixed to the other portion of the heating container with a flange or the like via a gasket having an insulating effect.
【0022】水槽の水面と仕切りとの間隔は、近過ぎる
と溶融プラスチックが水槽に落下した時の跳ね返り水に
よって仕切りが冷却され、溶融プラスチックの落下が阻
害される場合があるので、このようなことを回避するた
めに、適当な間隔、例えば、20cm以上の間隔を開け
ることが好ましい。尚、廃棄物中に塩化ビニル樹脂等の
塩化水素ガスの発生源となるプラスチックが含まれてい
る可能性のある場合には、塩化水素を吸収する目的で水
槽中の水に炭酸カルシウム等の中和剤を添加しておくこ
とが好ましい。If the distance between the water surface of the water tank and the partition is too close, the partition may be cooled by the rebound water when the molten plastic falls into the water tank, and the drop of the molten plastic may be hindered. In order to avoid this, it is preferable to provide an appropriate interval, for example, an interval of 20 cm or more. If there is a possibility that plastics such as vinyl chloride resin that generate hydrogen chloride gas are contained in the waste, water in the water tank may be used to absorb hydrogen chloride in order to absorb hydrogen chloride. It is preferable to add a wetting agent.
【0023】硬質塩化ビニル樹脂の溶融開始温度は、通
常、200℃付近であるが、これより高温では脱塩化水
素反応により高粘度化が進み、硬質塩化ビニル樹脂は通
常仕切りから流下せずに仕切り上に残る。一方、軟質塩
化ビニル樹脂は溶融し、仕切りを流下して水槽に落下し
て沈降する場合と、高粘度化して仕切り上に残る場合が
ある。いずれの場合も、塩化水素ガスが発生する。塩化
ビル樹脂以外のプラスチックでは溶融時にはほとんど分
解しないので発生ガス量は少量である。水槽に落下し、
固化したプラスチックは、その密度によって水面に浮上
したり、沈下する。ポリエチレンやポリプロピレンは浮
上するが、通常、少量ではあるが塩化ビニル樹脂やポリ
カーボネート樹脂等は沈下する。また、仕切りの開口部
を通過して水槽に落下する金属、石膏等の無機物は沈下
し、紙片塊等は通常浮上する。The melting start temperature of the hard vinyl chloride resin is usually around 200 ° C. However, at a higher temperature, the viscosity increases due to the dehydrochlorination reaction, and the hard vinyl chloride resin is usually partitioned without flowing down from the partition. Remain on top. On the other hand, the soft vinyl chloride resin may be melted, flow down the partition, fall into the water tank, and settle, or may increase in viscosity and remain on the partition. In each case, hydrogen chloride gas is generated. Since plastics other than chlorinated building resins hardly decompose during melting, the amount of generated gas is small. Fall into the aquarium,
The solidified plastic floats or sinks on the water surface depending on its density. Polyethylene or polypropylene floats, but usually a small amount of vinyl chloride resin or polycarbonate resin sinks. In addition, inorganic substances such as metal and gypsum that fall into the water tank through the opening of the partition sink, and a lump of paper usually floats.
【0024】水槽に浮上したプラスチックは、水槽が加
熱容器を水封する場合には、廃棄物の加熱処理中あるい
は処理後に、水流、水車等の公知の機械的方法等によっ
て外部水面に取り出し、オーバーフローさせたり、すく
い取りやかき取り等の適当な手段によって回収すること
ができる。一方、沈降物は水槽下部にコンベヤー等を設
置することにより回収することができる。廃棄物の加熱
処理終了後、プラスチックが分離された処理物は仕切り
を外して水槽に落下させると、密度差によって金属等の
不燃物と紙、繊維等の可燃物に分離するので、例えば、
先ず、沈降物を上記と同様にしてコンベヤーにより回収
し、次いで、浮上した可燃物は水槽の水を除去した後コ
ンベヤー等により回収することができる。When the water tank seals the heating container with water, the plastic floating in the water tank is taken out to the external water surface during or after the heat treatment of the waste by a known mechanical method such as a water flow or a water wheel, and overflowed. It can be collected by any suitable means such as scooping, scooping or scraping. On the other hand, sediment can be collected by installing a conveyor or the like at the bottom of the water tank. After the heat treatment of the waste, the treated material from which the plastic has been separated is separated into non-combustible materials such as metal and paper, and combustible materials such as fibers when the material is dropped and dropped into a water tank.
First, the sediment is recovered by a conveyor in the same manner as described above, and then the combustible material that has floated can be recovered by a conveyor or the like after removing the water in the water tank.
【0025】廃棄物の加熱処理に際しては、前記のよう
に、廃棄物中のプラスチックを溶融、流動化させて分離
する際に、プラスチック中に塩化ビニル樹脂も含まれて
いる場合には、該樹脂が分解して塩化水素ガスを発生す
る。又、他の廃棄物成分からも加熱により若干の有機物
等が発生し臭気の原因となる。さらに、プラスチックが
除かれた廃棄物を更に酸素遮断化に加熱分解する際に
も、廃棄物成分によっては臭気源となる有機物質や酸性
ガス等が発生する可能性がある。従って、発生ガスを大
気中に放出する前に発生ガス中の酸性ガスや有機物質等
を捕捉、除去しておくことが望ましい。In the heat treatment of the waste, as described above, when the plastic in the waste is melted, fluidized and separated, if the plastic also contains a vinyl chloride resin, Decomposes to generate hydrogen chloride gas. Further, some organic substances and the like are also generated from other waste components by heating, which causes odor. Further, when the waste from which the plastic is removed is further thermally decomposed to block oxygen, depending on the waste component, an organic substance or an acid gas serving as an odor source may be generated. Therefore, it is desirable to capture and remove acidic gases and organic substances in the generated gas before releasing the generated gas into the atmosphere.
【0026】そのために、本発明の加熱処理装置の上部
には、発生ガス排出口を設け、配管により発生ガス処理
装置と連結させることができる。発生ガス処理装置とし
ては、例えば、塩化水素ガス等の酸性ガスを中和除去す
るスクラバー、発生有機物等を吸着させる脱臭装置、燃
焼させる燃焼装置等が挙げられるが、これら以外の装置
も連結可能である。For this purpose, a generated gas discharge port is provided at the upper part of the heat treatment apparatus of the present invention, and can be connected to the generated gas treatment apparatus by piping. Examples of the generated gas processing device include a scrubber for neutralizing and removing acidic gases such as hydrogen chloride gas, a deodorizing device for adsorbing generated organic substances, a combustion device for burning, and the like, but other devices can also be connected. is there.
【0027】例えば、塩化水素ガス等の酸性ガスは、発
生ガスを、例えば、スクラバーで炭酸カルシウム微粉末
のスラリー、石灰乳、水酸化ナトリウム等のアルカリの
水溶液と接触させて中和により除去することができる。
酸性ガスが少量の場合には、乾式でアルカリ性物質と接
触させて除去することもできる。酸性ガスの捕捉方法は
これらの方法に限定されず、他の従来公知の酸性ガスの
捕捉方法を用いることもできる。また、発生ガス中の有
機物質の除去には、例えば、上記のスクラバーで処理さ
れた発生ガスを高温に加熱あるいは自燃させて熱分解す
るか、適当な温度で触媒層を通過させて分解する方法、
活性炭等の吸着剤に吸着させる方法、発生ガスを冷却し
て有機物質を凝縮させる方法等が挙げられるが、これ以
外の方法であってもよい。For example, acidic gas such as hydrogen chloride gas is removed by neutralizing the generated gas by contacting it with a slurry of calcium carbonate fine powder, lime milk, or an aqueous alkali solution such as sodium hydroxide using a scrubber. Can be.
When the amount of the acidic gas is small, it can be removed by contacting it with an alkaline substance in a dry manner. The method for capturing the acidic gas is not limited to these methods, and other conventionally known methods for capturing an acidic gas can also be used. Further, to remove organic substances in the generated gas, for example, a method in which the generated gas treated with the above scrubber is heated or heated to a high temperature and thermally decomposed, or decomposed by passing through a catalyst layer at an appropriate temperature. ,
Examples of the method include a method of adsorbing on an adsorbent such as activated carbon, a method of cooling generated gas to condense organic substances, and the like, but other methods may be used.
【0028】本発明では加熱処理を減圧下に行い、必要
により発生ガスを上記のように処理する場合もあること
から、発生ガス排出口をブロアー等の任意の吸引手段と
連結させることができる。In the present invention, the heat treatment is performed under reduced pressure, and the generated gas may be processed as described above, if necessary. Therefore, the generated gas discharge port can be connected to any suction means such as a blower.
【0029】以上のようにして本発明の廃棄物の加熱処
理装置を用いることにより、熱溶融性プラスチックを含
む廃棄物(混合ゴミ)は、熱溶融性プラスチックと可燃
物と不燃物とに分離することができる。分離された熱溶
融性プラスチックは、塩化ビニル樹脂樹脂を除けばほと
んど分解していないので、組成によってはリサイクルが
可能である。また、通常の加熱処理条件では処理物は殺
菌されており、衛生的に無害化することが可能である。
また、水槽が加熱容器を水封する場合には、加熱容器の
一端は開放された構造に形成することができることか
ら、加熱による加熱容器の熱歪みを逃がすことが可能で
ある。更に、処理物の取り出し口を設ける必要もなく、
溶融プラスチックを取り出すための押出機等の設置の必
要もないために、装置の構造を著しく簡易にし、製造コ
ストを安くすることが可能である。By using the waste heat treatment apparatus of the present invention as described above, waste (mixed waste) containing hot-melt plastic is separated into hot-melt plastic, combustibles, and incombustibles. be able to. Since the separated hot-melt plastic is hardly decomposed except for the vinyl chloride resin, it can be recycled depending on the composition. Further, the processed material is sterilized under normal heat treatment conditions, and can be sanitized harmlessly.
In addition, when the water tank seals the heating container with water, one end of the heating container can be formed in an open structure, so that thermal distortion of the heating container due to heating can be released. Furthermore, there is no need to provide an outlet for the processed material
Since there is no need to provide an extruder or the like for removing the molten plastic, the structure of the apparatus can be significantly simplified, and the manufacturing cost can be reduced.
【0030】[0030]
【実施例】次に実施例を挙げて本発明を具体的に説明す
る。 実施例1 熱溶融性プラスチックが多く含まれている家庭から出た
不燃ごみ70リットル(4.0kg)を概略図を図1に
示す下端が水封された加熱処理装置1を用いて処理し
た。加熱処理装置1は、加熱容器2とその下端を水封す
るとともに溶融プラスチックを落下させる水封容器9と
から構成される。加熱容器2は直径30cm、内容積7
0リットル(下記の仕切り板5より上の部分)の円筒
で、その周面に設置した8KWの埋め込みヒーター(不
図示)と断熱材からなる加熱ジャケット3で外周が覆わ
れている。加熱容器2は架台4で支えられている。加熱
容器1の内部下方部にはヒーターを内蔵したパイプから
なる仕切り板5が、上端には開閉(密閉)可能な処理物
投入口6が、また、上方部には発生ガス排出口10がそ
れぞれ設けられている。加熱容器の下端は開放状態であ
り、その下方部の水封容器9中にその一部が浸される部
分7(30cm)は断熱性ガスケットを用いたフランジ
8によって加熱容器2に固定されている。水封容器9
は、直径が50cm、内容積240リットルの円筒状容
器である。水封容器9の6分目まで水を入れ、加熱容器
の下方部7の約5cmが水に漬かるように水封容器9の
設置高さを調整した。Next, the present invention will be described specifically with reference to examples. Example 1 70 liters (4.0 kg) of non-combustible garbage from homes containing a large amount of hot-melt plastic was treated using a heat treatment apparatus 1 whose lower end is water-sealed as shown in FIG. The heat treatment apparatus 1 includes a heating vessel 2 and a water-sealing vessel 9 for water-sealing the lower end thereof and dropping the molten plastic. The heating vessel 2 has a diameter of 30 cm and an internal volume of 7
A cylinder of 0 liter (part above the partition plate 5 described below), the outer periphery of which is covered by an embedded heater (not shown) of 8 KW and a heating jacket 3 made of a heat insulating material installed on the peripheral surface. The heating container 2 is supported by a gantry 4. A partition plate 5 composed of a pipe with a built-in heater is provided in a lower part of the inside of the heating vessel 1, a processing material inlet 6 which can be opened and closed (sealed) is provided at an upper end, and a generated gas outlet 10 is provided at an upper part. Is provided. The lower end of the heating container is open, and a portion 7 (30 cm) of which a part is immersed in a water sealing container 9 below is fixed to the heating container 2 by a flange 8 using a heat insulating gasket. . Water sealed container 9
Is a cylindrical container having a diameter of 50 cm and an internal volume of 240 liters. Water was poured into the water-sealed container 9 until the sixth minute, and the installation height of the water-sealed container 9 was adjusted so that about 5 cm of the lower part 7 of the heating container was immersed in water.
【0031】加熱容器の発生ガス排出口10は配管1
4、14′により酸性ガススクラバー11、吸引ブロワ
ー12及び消臭炉13と連結した。スクラバー11は下
端が開放状態の円筒状容器15で、その開放下端部を中
和剤の水溶液(炭酸カルシウムの2重量%懸濁溶液)を
充填した水封容器16に浸して水封する。水封容器16
内の中和剤はポンプPuにより円筒状容器15の上方部
に設けた中和剤シャワー装置17に送られる。スクラバ
ー11で処理された発生ガスは吸引ブロワー(常圧での
吸引能力0.5m3/min)12で吸引されて消臭炉
13に送られ、ガスこん炉18で燃焼させる。The generated gas outlet 10 of the heating vessel is connected to the pipe 1
4, 14 'connected to the acid gas scrubber 11, the suction blower 12, and the deodorizing furnace 13. The scrubber 11 is a cylindrical container 15 having an open lower end. The open lower end is immersed in a water seal container 16 filled with an aqueous solution of a neutralizing agent (a 2% by weight suspension of calcium carbonate), and sealed. Water sealed container 16
The neutralizing agent therein is sent to a neutralizing agent shower device 17 provided above the cylindrical container 15 by a pump Pu. The generated gas treated by the scrubber 11 is sucked by a suction blower (suction capacity at normal pressure: 0.5 m 3 / min) 12, sent to a deodorizing furnace 13, and burned in a gas furnace 18.
【0032】投入口6より加熱容器2内に処理物を投入
して投入口6を密閉し、ポンプPuを運転して中和剤シ
ャワー装置17を作動させ、ガスこん炉18を点火す
る。次に、吸引ブロワー12を作動させ、加熱容器2内
を水中10cmの減圧状態とし、ヒーターを作動させて
加熱容器の加熱を開始する。35分後に内温が250℃
に達した後、この温度を1時間保持し、ヒーターの作動
を停止した。1時間自然放冷した後、処理結果を確認し
た。その結果、水封容器9に落下、浮上したものはプラ
スチックの小塊が2kg、沈下したものは金属片が0.
3kgであり、一方、仕切り板5上に残ったものは、紙
及びガラス瓶が1.5kgであり、合計3.8kgが回
収された。プラスチックは仕切り板、紙やガラス瓶の表
面に付着して残ったものは極少量であり、ほぼ全量のプ
ラスチックは水封容器に落下した。上記の回収処理物の
容積は約5リットルであり、加熱処理による減容率は9
3%であった。The treated material is charged into the heating vessel 2 through the charging port 6, the charging port 6 is closed, the pump Pu is operated, the neutralizer shower device 17 is operated, and the gas furnace 18 is ignited. Next, the suction blower 12 is operated, the inside of the heating container 2 is evacuated to 10 cm in water, and the heater is operated to start heating the heating container. After 35 minutes, the internal temperature is 250 ° C
, The temperature was maintained for one hour, and the operation of the heater was stopped. After naturally cooling for one hour, the processing results were confirmed. As a result, 2 kg of small plastic lumps were dropped and floated in the water-seal container 9, and metal fragments were 0.1 kg in the case of sinking.
3 kg, while 1.5 kg of paper and glass bottles remained on the partition plate 5, and a total of 3.8 kg was collected. A very small amount of plastic adhered to the surface of the partition plate, paper or glass bottle and remained, and almost all of the plastic fell into the water-sealed container. The volume of the recovered material is about 5 liters, and the volume reduction rate by heat treatment is 9
3%.
【0033】[0033]
【発明の効果】以上の本発明によれば、プラスチックを
含む廃棄物から分離したプラスチックの回収が容易であ
り、廃棄物の減容、減量、同時に消毒、無臭化が達成さ
れる廃棄物の加熱処理方法及び加熱処理装置が提供され
る。According to the present invention described above, it is easy to recover the plastic separated from the waste containing the plastic, and the heating of the waste achieves volume reduction, weight reduction, disinfection and odorlessness of the waste. A processing method and a heat treatment apparatus are provided.
【図1】 本発明の加熱装置の一例の概略図である。FIG. 1 is a schematic view of an example of a heating device of the present invention.
1:加熱容器処理装置 2:加熱容器 3:加熱ジャケット 4:加熱処理装置支持架台 5:上下室の仕切り桟 6:廃棄物投入口 7:加熱容器の水に漬かる部分 8:フランジ部分 9:水封容器 10:発生ガス排出口 11:スクラバー 12:吸引ブロワー 13:消臭炉 14、14′:配管 15:円筒状容器 16:水封容器 17:中和剤シャワー装置 18:ガスこん炉 T:温度計 P:圧力計 Pu:ポンプ 1: Heating vessel treatment device 2: Heating container 3: Heating jacket 4: Heating treatment device support gantry 5: Partition bar in upper and lower chambers 6: Waste inlet 7: Submerged part of heating vessel 8: Flange part 9: Water Sealed container 10: Outlet of generated gas 11: Scrubber 12: Suction blower 13: Deodorizing furnace 14, 14 ': Piping 15: Cylindrical container 16: Water sealed container 17: Neutralizer shower device 18: Gas stove T: Thermometer P: Pressure gauge Pu: Pump
フロントページの続き Fターム(参考) 4D004 AA07 AA46 AA48 BA03 CA24 CA26 CA29 CA32 CA48 CB03 CB31 CB43 DA02 DA06 4F301 AC17 BA01 BA02 BA21 BA29 BE35 BF10 BF15 BF31 Continued on the front page F term (reference) 4D004 AA07 AA46 AA48 BA03 CA24 CA26 CA29 CA32 CA48 CB03 CB31 CB43 DA02 DA06 4F301 AC17 BA01 BA02 BA21 BA29 BE35 BF10 BF15 BF31
Claims (6)
仕切りで上下二室に区分けされた加熱容器の上部室に入
れ、該廃棄物を無酸素あるいは低酸素状態で加熱し、該
廃棄物中の熱溶融性プラスチックを溶融させて該廃棄物
を熱溶融性プラスチックと熱不融性廃棄物とに分離する
に際し、加熱溶融させたプラスチックを、溶融プラスチ
ックを流下可能に形成された仕切りを通して加熱容器の
下部室の下部に設けた水槽に落下させ、固化させること
を特徴とする廃棄物から熱溶融性プラスチックを分離す
る方法。1. A waste containing a hot-melt plastic,
The waste is put into the upper chamber of the heating vessel divided into upper and lower compartments, and the waste is heated in an oxygen-free or low-oxygen state, and the heat-meltable plastic in the waste is melted to melt the waste. Upon separation into conductive plastic and heat-infusible waste, the heated and melted plastic is dropped into a water tank provided at the bottom of the lower chamber of the heating vessel through a partition formed so that the molten plastic can flow down, and solidified. A method for separating hot melt plastic from waste.
た熱不溶融性廃棄物を無酸素あるいは低酸素状態で更に
加熱して熱分解させることを特徴とする廃棄物の減容処
理方法。2. A method for reducing the volume of a waste material, wherein the heat-insoluble waste material from which the heat-fusible plastic has been separated is further decomposed by further heating in an oxygen-free or low-oxygen state.
請求項2に記載の廃棄物の減容処理方法。3. The waste volume reduction method according to claim 2, wherein the generated gas is absorbed and / or decomposed.
酸素あるいは低酸素状態で加熱する加熱容器とその下部
に設けられた水槽とから構成され、上記加熱容器は、溶
融プラスチックが流下可能に形成された仕切りで上下二
室に区分けされ、上部室に上記廃棄物を入れて上記状態
で加熱し、上記仕切りを通して流下する溶融プラスチッ
クを落下及び固化させる水槽が下部室の下部に設置され
ていることを特徴とする廃棄物の加熱処理装置。4. A heating vessel for heating waste containing a hot-melt plastic in an oxygen-free or low-oxygen state and a water tank provided below the heating vessel, wherein the heating vessel is formed so that the molten plastic can flow down. A water tank that is divided into upper and lower compartments by the divided compartment, puts the waste into the upper compartment, heats in the above state, and drops and solidifies the molten plastic flowing down through the compartment is installed at the lower part of the lower compartment. Waste heat treatment apparatus characterized by the above-mentioned.
成されている請求項4に記載の廃棄物の加熱処理装置。5. The waste heat treatment apparatus according to claim 4, wherein the water tank is formed so as to seal the lower part of the heating vessel with water.
と連結される請求項4に記載の廃棄物の加熱処理装置。6. The waste heat treatment device according to claim 4, wherein the waste heat treatment device is connected to a device that absorbs and / or decomposes generated gas.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11149655A JP2000225384A (en) | 1998-11-30 | 1999-05-28 | Method for separating heat-meltable plastic from waste, method for volume reducing treatment of waste, and apparatus for heat treatment of waste |
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10-339340 | 1998-11-30 | ||
JP33934098 | 1998-11-30 | ||
JP11149655A JP2000225384A (en) | 1998-11-30 | 1999-05-28 | Method for separating heat-meltable plastic from waste, method for volume reducing treatment of waste, and apparatus for heat treatment of waste |
Publications (1)
Publication Number | Publication Date |
---|---|
JP2000225384A true JP2000225384A (en) | 2000-08-15 |
Family
ID=26479477
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP11149655A Pending JP2000225384A (en) | 1998-11-30 | 1999-05-28 | Method for separating heat-meltable plastic from waste, method for volume reducing treatment of waste, and apparatus for heat treatment of waste |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2000225384A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007229660A (en) * | 2006-03-02 | 2007-09-13 | Sunaoshi Purari Kk | Process for treating waste containing vinyl chloride resin |
JP2014108375A (en) * | 2012-11-30 | 2014-06-12 | Shinryo Corp | Method of recovering constituent material of solar cell element |
CN108556201A (en) * | 2018-03-22 | 2018-09-21 | 毛秋英 | A kind of Cardiological disposable plastic pipe breaker |
CN114435795A (en) * | 2022-02-25 | 2022-05-06 | 湘南学院 | Garbage classification system |
JP7561474B2 (en) | 2021-01-13 | 2024-10-04 | 第一高周波工業株式会社 | Method for separating resin-coated inner surface of metal pipe |
-
1999
- 1999-05-28 JP JP11149655A patent/JP2000225384A/en active Pending
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007229660A (en) * | 2006-03-02 | 2007-09-13 | Sunaoshi Purari Kk | Process for treating waste containing vinyl chloride resin |
JP2014108375A (en) * | 2012-11-30 | 2014-06-12 | Shinryo Corp | Method of recovering constituent material of solar cell element |
CN108556201A (en) * | 2018-03-22 | 2018-09-21 | 毛秋英 | A kind of Cardiological disposable plastic pipe breaker |
CN108556201B (en) * | 2018-03-22 | 2020-08-14 | 温州医科大学附属第一医院 | Disposable plastic tubing breaker for intracardiac branch of academic or vocational study |
JP7561474B2 (en) | 2021-01-13 | 2024-10-04 | 第一高周波工業株式会社 | Method for separating resin-coated inner surface of metal pipe |
CN114435795A (en) * | 2022-02-25 | 2022-05-06 | 湘南学院 | Garbage classification system |
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