JPH0211307A - Treating of foamed polystyrene waste - Google Patents
Treating of foamed polystyrene wasteInfo
- Publication number
- JPH0211307A JPH0211307A JP63160682A JP16068288A JPH0211307A JP H0211307 A JPH0211307 A JP H0211307A JP 63160682 A JP63160682 A JP 63160682A JP 16068288 A JP16068288 A JP 16068288A JP H0211307 A JPH0211307 A JP H0211307A
- Authority
- JP
- Japan
- Prior art keywords
- foamed polystyrene
- polystyrene waste
- foamed
- dropped
- treating
- 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
- 239000002699 waste material Substances 0.000 title claims abstract description 17
- 229920006248 expandable polystyrene Polymers 0.000 title claims abstract description 12
- 238000000034 method Methods 0.000 claims description 11
- 239000004215 Carbon black (E152) Substances 0.000 claims description 2
- 229930195733 hydrocarbon Natural products 0.000 claims description 2
- 150000002430 hydrocarbons Chemical class 0.000 claims description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 2
- 239000008187 granular material Substances 0.000 abstract description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 abstract description 4
- 229910052742 iron Inorganic materials 0.000 abstract description 2
- 238000005192 partition Methods 0.000 abstract description 2
- 238000005485 electric heating Methods 0.000 abstract 2
- 239000004794 expanded polystyrene Substances 0.000 description 5
- 239000006260 foam Substances 0.000 description 5
- 239000004793 Polystyrene Substances 0.000 description 4
- 229920002223 polystyrene Polymers 0.000 description 4
- 238000001914 filtration Methods 0.000 description 2
- 235000013305 food Nutrition 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 229920003023 plastic Polymers 0.000 description 2
- 241000251468 Actinopterygii Species 0.000 description 1
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 1
- 238000003763 carbonization Methods 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 239000013530 defoamer Substances 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000010169 landfilling Methods 0.000 description 1
- 235000013372 meat Nutrition 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000013502 plastic waste Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000011973 solid acid Substances 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B17/00—Recovery of plastics or other constituents of waste material containing 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
Landscapes
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Mechanical Engineering (AREA)
- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
Abstract
Description
【発明の詳細な説明】 (産業上の利用分野) 本発明は発泡ポリスチレンの処理方法に関する。[Detailed description of the invention] (Industrial application field) The present invention relates to a method for treating expanded polystyrene.
(従来の技術)
近年プラスチックの合理性(便利さ)から、その使用量
は増加の一途をたどり、産業分野だけでなく一般家庭の
あらゆる分野に入りこんでいろ。そのため廃棄物の対応
策が社会問題化しており、従来行われてきた埋立て、焼
却等の手段では、間に合わぬばかりでなく、土地の利用
をさまたげると共に排ガス等により第2次公害を引き起
こすという問題も生じている。(Conventional technology) In recent years, due to the rationality (convenience) of plastics, the amount of plastic used has been increasing steadily, and it has entered not only the industrial field but also every field of ordinary households. Therefore, measures to deal with waste have become a social issue, and conventional methods such as landfilling and incineration are not only insufficient, but also hinder land use and cause secondary pollution due to exhaust gas, etc. is also occurring.
そこでプラスチック廃棄物の再利用について種々検討さ
れているが、経済性、安全性、再利用製品の品質等の点
で問題点が多く現実問題としてはごく一部が再利用され
ているにすぎない。Therefore, various studies are being conducted on the reuse of plastic waste, but there are many problems in terms of economy, safety, quality of recycled products, etc., and in reality, only a small portion is reused. .
特に発泡ポリスチレン製品は安価にして保温性等に優れ
ろところから各種食品容器等として大量に用いられてお
り、その廃棄物の処理は社会的に大きな問題となってい
る。In particular, expanded polystyrene products are used in large quantities as various food containers because they are inexpensive and have excellent heat retention properties, and the disposal of their waste has become a major social problem.
発泡ポリスチレン製品は通常発泡倍率が40〜70倍程
度といった高発泡倍率であるためこれを熱風等で脱泡し
縮小化する試みは従来からなされているが、安全性に劣
ると共に能率が低く、設備が高価につき、さらに縮小化
物が黒色化を伴う等の理由で再利用製品の品質や利用効
率も劣るといった問題を有していた。Expanded polystyrene products usually have a high expansion ratio of about 40 to 70 times, so attempts have been made to defoamer and reduce the size using hot air, etc., but this is not safe, has low efficiency, and requires equipment. However, there were problems in that the quality and efficiency of reuse of reused products were poor because they were expensive, and the reduced products tended to turn black.
(発明が解決しようする課!iり
本発明の目的は上記した問題点の解決にあり、特に発泡
ボリスチレン廃棄物を高い安全性をもって、安価に、再
利用しやすい状態にすると共に再利用製品の品質等にも
優れた発泡ポリスチレン廃棄物の処理方法を提供するこ
とにある。(The purpose of the present invention is to solve the above-mentioned problems, and in particular, to make foamed polystyrene waste highly safe, inexpensive, and easy to reuse, and to make recycled products. It is an object of the present invention to provide a method for processing expanded polystyrene waste that is excellent in quality.
(課題を解決するための手段)
本発明は発泡ポリスチレン廃棄物片を低加圧水蒸気で処
理して脱泡縮小化することからなる発泡ポリスチレン廃
棄物の処理方法にある。(Means for Solving the Problems) The present invention resides in a method for treating foamed polystyrene waste, which comprises treating foamed polystyrene waste pieces with low-pressure steam to defoam and reduce the size of the foamed polystyrene waste pieces.
本発明で用いられる発泡ポリスチレン廃棄物は特に制限
されず魚肉等の食品容器等として用いられたもの等適宜
の用途のものが用いられるが、特に30倍以上といった
高発泡倍率のものが好適に用いられる。The foamed polystyrene waste used in the present invention is not particularly limited, and those used as containers for foods such as fish and meat can be used as appropriate, but those with a high expansion ratio of 30 times or more are particularly preferred. It will be done.
発泡ポリスチレン廃棄物は通常処理がしやすいように5
〜50cm程度の大きさに切断されて密閉容器に充填さ
れる。次いで該容器に低加圧水蒸気を導入する。この低
加圧水蒸気は100℃より高い温度で脱泡を起こすに足
る温度以上で且つポリスチレン片どうしが相互に融着す
るよりは低い温度のものである。ここに相互に融着しな
いとは見掛上付着していてもたたく等の軽微の衝撃で分
離する状態を包含する意味である。換言すれば脱泡縮小
化物に閏撃を加えたときポリスチレン片どうしが付着し
たまま主に他の個所が破壊する状態になればポリスチレ
ン片どうしが相互に融着したことになる。かかる水蒸気
の温度としては通常120〜160℃、好ましくは13
0〜150℃、圧力としては3〜6kg/cJ、好まし
くは3.5〜4.5kg / cd程度であり、最適条
件は装置や発泡体の大きさ等に応じ決定されろ。条件を
もつ水蒸気としては一般的工場におけろ排スチーム等が
あり、従って水蒸気の費用も低額に抑えることができる
。また低加圧水蒸気を用いろ方法であるため、安全であ
ると共に被処理物の表面に水分が付着していても操作上
何ら問題なく予備処理が簡単にすむと共に、縮小槽の材
質や設計にも特別の配慮はいらない。Expanded polystyrene waste is usually separated into 5 types to make it easier to dispose of.
It is cut into pieces approximately 50 cm in size and filled into airtight containers. Low pressure steam is then introduced into the vessel. This low-pressure steam has a temperature above 100°C, which is sufficient to cause defoaming, but below a temperature that would cause the polystyrene pieces to fuse together. Here, the term "not fused to each other" includes a state in which even though they are apparently attached, they separate with a slight impact such as being hit. In other words, if a blow is applied to the defoamed and reduced product, and the polystyrene pieces remain attached to each other, but mainly other parts are destroyed, the polystyrene pieces have fused together. The temperature of such water vapor is usually 120 to 160°C, preferably 13°C.
The temperature is 0 to 150°C and the pressure is about 3 to 6 kg/cJ, preferably about 3.5 to 4.5 kg/cd, and the optimum conditions are determined depending on the equipment, the size of the foam, etc. Examples of steam with certain conditions include waste steam from general factories, and therefore the cost of steam can be kept low. In addition, since the filtration method uses low-pressure steam, it is safe, there are no operational problems even if moisture adheres to the surface of the treated object, and preliminary treatment is easy, and it is also easy to use due to the material and design of the reduction tank. No special consideration required.
上記の処理によって得られろ縮小片はその容積がもとの
容積のl/10〜1740程度に減少するが依然幾分の
発泡倍率(たとえば15倍以上)を有するものである。Although the volume of the reduced piece obtained by the above treatment is reduced to about 1/10 to 1740 of the original volume, it still has a certain expansion ratio (for example, 15 times or more).
その結果ポリスチレン自体は溶融せず発泡体と同じ分子
状態を実質上維持している。As a result, the polystyrene itself does not melt and maintains substantially the same molecular state as the foam.
このようにして得られた縮小片は単に運搬しやすい等の
利点の他に、黒色化等の品質劣化を実質上伴わず、粉砕
による粒状化が極めて容易であるという特徴をもってい
る。The reduced pieces thus obtained have the advantage of being easy to transport, as well as being substantially free of quality deterioration such as blackening, and are extremely easy to pulverize into granules.
そしてこの粒状化物は本質的に発泡体の不完全説泡物で
あり、溶融固結体でないため、移送、溶融等の次なる再
利用処理が極めて容易という特徴をもっている。また比
較的温和な水蒸気処理を経ただけであるため処理過程で
の炭化等に伴う不均質物の混入等がなく品質が安定して
いる。その結果この粒状物を溶融し、熱分解して発生し
た蒸気を固体酸触媒を用いてさらに熱分解した場合芳香
族炭化水素主体の極めて高品質の炭化水素油を高収率で
得ろことができろという特徴を示す。Since this granulated material is essentially an incomplete foamed material and is not a molten solid, it is characterized by being extremely easy to carry out subsequent recycling processes such as transportation and melting. In addition, since it has only undergone a relatively mild steam treatment, there is no inhomogeneous matter mixed in due to carbonization during the treatment process, and the quality is stable. As a result, when this granular material is melted and the vapor generated by thermal decomposition is further thermally decomposed using a solid acid catalyst, it is possible to obtain an extremely high quality hydrocarbon oil consisting mainly of aromatic hydrocarbons at a high yield. Shows the characteristic of .
ここで本発明の実施に有効な装置の一例を図面に基づい
て説明する。Here, an example of an apparatus effective for carrying out the present invention will be explained based on the drawings.
第1図は本発明方法の実施に用いろ装置の一例を示す断
面図である。FIG. 1 is a sectional view showing an example of a filtration apparatus used for carrying out the method of the present invention.
発泡ポリスチレン廃棄物1の投入口上部に発泡体切断用
電気ヒーター線2を設置する。この電気ヒーター線によ
り発泡体をたとえば5〜10cm程度の小片に切断する
。切断された発泡体小片は鉄製容器からなる縮小化槽3
に落下する。縮小化t1!I3へは低加圧水蒸気が4か
ら導入され5から排出されろ。An electric heater wire 2 for cutting foam is installed above the input port for foamed polystyrene waste 1. The foam is cut into pieces of, for example, about 5 to 10 cm using this electric heater wire. The cut foam pieces are placed in a reduction tank 3 consisting of an iron container.
to fall. Reduction t1! Low pressurized steam is introduced into I3 from 4 and discharged from 5.
ここで縮小化された脱泡縮小化物は粗砕aI6に落下さ
れたとえば10〜30間程度の粒状物に粉砕され、粒状
物は7から落下される。尚縮小化槽3の上部と下部には
仕切り8,9を設は断続的に開閉きれる。The defoamed and reduced product thus reduced in size is dropped into a coarse crusher aI 6 and crushed into particles of, for example, about 10 to 30 particles, and the granules are dropped from 7. Furthermore, partitions 8 and 9 are provided at the upper and lower parts of the reduction tank 3 and can be opened and closed intermittently.
尚縮小化槽を2又は3個併設して半連続的に縮小化作業
を行うことも好ましい。また縮小化槽は全体を保温して
おくことが好ましい。It is also preferable to provide two or three reduction tanks in parallel and perform the reduction work semi-continuously. Further, it is preferable to keep the entire reduction tank warm.
第1図は本発明の実施に用いる装置の一例を示す断面図
である。FIG. 1 is a sectional view showing an example of an apparatus used for carrying out the present invention.
Claims (1)
て脱泡縮小化することを特徴とする発泡ポリスチレン廃
棄物の処理方法。 2、水蒸気の温度が120〜160℃である請求項1に
記載の方法。 3 水蒸気の圧力が3〜6kg/cm^2である請求項
1又は2に記載の方法。 4、脱泡縮小化物を粉砕処理する請求項1に記載の方法
。 5、粉砕処理物を熱分解して炭化水素油に変換する請求
項4に記載の方法。[Claims] 1. A method for treating foamed polystyrene waste, which comprises treating foamed polystyrene waste pieces with low-pressure steam to defoam and reduce the size of the foamed polystyrene waste pieces. 2. The method according to claim 1, wherein the temperature of the steam is 120 to 160°C. 3. The method according to claim 1 or 2, wherein the pressure of the water vapor is 3 to 6 kg/cm^2. 4. The method according to claim 1, wherein the defoamed reduced product is pulverized. 5. The method according to claim 4, wherein the pulverized product is thermally decomposed and converted into hydrocarbon oil.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63160682A JPH0211307A (en) | 1988-06-30 | 1988-06-30 | Treating of foamed polystyrene waste |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63160682A JPH0211307A (en) | 1988-06-30 | 1988-06-30 | Treating of foamed polystyrene waste |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0211307A true JPH0211307A (en) | 1990-01-16 |
Family
ID=15720189
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP63160682A Pending JPH0211307A (en) | 1988-06-30 | 1988-06-30 | Treating of foamed polystyrene waste |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0211307A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0494613U (en) * | 1991-01-09 | 1992-08-17 | ||
WO1993014915A2 (en) | 1992-01-27 | 1993-08-05 | Fleischhauer, Rosa, Emilia | Method and device for the collection and regranulation of waste containing drawn plastics |
KR100373415B1 (en) * | 1995-12-01 | 2003-05-09 | 강순희 | Waste styrofoam treatment apparatus |
CN102341981A (en) * | 2009-03-16 | 2012-02-01 | 日本Ae帕瓦株式会社 | Three-phase common tank type gas insulated switchgear |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6045356B2 (en) * | 1979-10-08 | 1985-10-08 | 動力炉・核燃料開発事業団 | Direct contact type split cooler using elastic force |
-
1988
- 1988-06-30 JP JP63160682A patent/JPH0211307A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6045356B2 (en) * | 1979-10-08 | 1985-10-08 | 動力炉・核燃料開発事業団 | Direct contact type split cooler using elastic force |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0494613U (en) * | 1991-01-09 | 1992-08-17 | ||
WO1993014915A2 (en) | 1992-01-27 | 1993-08-05 | Fleischhauer, Rosa, Emilia | Method and device for the collection and regranulation of waste containing drawn plastics |
KR100373415B1 (en) * | 1995-12-01 | 2003-05-09 | 강순희 | Waste styrofoam treatment apparatus |
CN102341981A (en) * | 2009-03-16 | 2012-02-01 | 日本Ae帕瓦株式会社 | Three-phase common tank type gas insulated switchgear |
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