JPS6336924B2 - - Google Patents
Info
- Publication number
- JPS6336924B2 JPS6336924B2 JP26816684A JP26816684A JPS6336924B2 JP S6336924 B2 JPS6336924 B2 JP S6336924B2 JP 26816684 A JP26816684 A JP 26816684A JP 26816684 A JP26816684 A JP 26816684A JP S6336924 B2 JPS6336924 B2 JP S6336924B2
- Authority
- JP
- Japan
- Prior art keywords
- hot air
- hot
- discharge port
- waste
- stove
- 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.)
- Expired
Links
- 239000004033 plastic Substances 0.000 claims description 42
- 229920003023 plastic Polymers 0.000 claims description 42
- 239000002699 waste material Substances 0.000 claims description 38
- 238000010438 heat treatment Methods 0.000 claims description 17
- 230000014759 maintenance of location Effects 0.000 claims description 9
- 238000000034 method Methods 0.000 claims description 7
- 238000011038 discontinuous diafiltration by volume reduction Methods 0.000 claims description 6
- 239000012768 molten material Substances 0.000 claims description 2
- 230000002093 peripheral effect Effects 0.000 claims description 2
- -1 polyethylene Polymers 0.000 description 6
- 230000001877 deodorizing effect Effects 0.000 description 4
- 238000002844 melting Methods 0.000 description 4
- 230000008018 melting Effects 0.000 description 4
- 239000004698 Polyethylene Substances 0.000 description 3
- 238000007667 floating Methods 0.000 description 3
- 230000005484 gravity Effects 0.000 description 3
- 239000010813 municipal solid waste Substances 0.000 description 3
- 229920000573 polyethylene Polymers 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 238000007790 scraping Methods 0.000 description 2
- 229920001187 thermosetting polymer Polymers 0.000 description 2
- 239000002023 wood Substances 0.000 description 2
- 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 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 229920006328 Styrofoam Polymers 0.000 description 1
- 229920001807 Urea-formaldehyde Polymers 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000010794 food waste Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 229920001568 phenolic resin Polymers 0.000 description 1
- 239000005011 phenolic resin Substances 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 229920000915 polyvinyl chloride Polymers 0.000 description 1
- 239000004800 polyvinyl chloride Substances 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000011343 solid material Substances 0.000 description 1
- 239000008261 styrofoam Substances 0.000 description 1
- 229920005992 thermoplastic resin Polymers 0.000 description 1
- 239000002341 toxic gas Substances 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
- B29B13/00—Conditioning or physical treatment of the material to be shaped
- B29B13/02—Conditioning or physical treatment of the material to be shaped by heating
- B29B13/022—Melting the material to be shaped
-
- 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
Description
【発明の詳細な説明】
(産業上の利用分野)
この発明は、廃プラスチツクを加熱させて減容
処理する方法及び装置に関する。DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a method and apparatus for heating waste plastic to reduce its volume.
(背景技術)
一口に廃プラスチツクと言つても、その中には
ポリエチレン、ポリプロピレン、ポリ塩化ビニー
ル、ポリエスチレン等の熱可塑性樹脂と、フエノ
ール樹脂、尿素樹脂のような熱硬化性樹脂が混合
して含まれている他、多くの場合、土砂、紙、
木、生ゴミといつた他の廃棄物をも含んでいる。(Background technology) Waste plastics are a mixture of thermoplastic resins such as polyethylene, polypropylene, polyvinyl chloride, and polyethylene, and thermosetting resins such as phenolic resins and urea resins. In addition, it often contains soil, paper,
It also includes other waste materials such as wood and food scraps.
従来、上述した各種廃プラスチツクや、他の廃
棄物を含む広義の意味における廃プラスチツクを
減容処理する手段としては、この種廃プラスチツ
クを熱風滞留室へ吊設させた、下方に吐出口を設
けて成る漏斗状の溶融室内へ投入させて該溶融室
の外側からの間接加熱と、該溶融室に設けた熱風
導入管から導入させた熱風による直接加熱とによ
つて加熱させ、これを溶融させるものが公知であ
るが、その際、廃プラスチツクは吐出口付近に設
けた保持棒、その他の手段によつて熱風炉中に貯
溜保持されており、溶融した廃プラスチツクは掻
取手段、或いは熱風炉に対する振動手段によつて
炉壁に附着してしまうのを防止されつつ吐出口方
向へ掻き寄せられ、或いは強制流下されるもので
あつた。 Conventionally, as a means for reducing the volume of the above-mentioned various types of waste plastics and waste plastics in a broader sense including other wastes, this kind of waste plastics is suspended in a hot air retention chamber, and a discharge port is provided at the bottom. It is heated by indirect heating from the outside of the melting chamber and direct heating by hot air introduced from a hot air introduction pipe provided in the melting chamber to melt it. In this case, the waste plastics are stored and held in the hot air oven by a holding rod installed near the discharge port or other means, and the melted waste plastics are removed by a scraping means or the hot air oven. The vibrating means prevents the waste from adhering to the furnace wall, and the waste is scraped toward the outlet or forced down.
(技術的課題)
この発明の目的は、装置の構造を複雑にし、か
つ製作コストを高める、掻取手段や振動手段、及
び保持棒等を廃しても、廃プラスチツクを熱風炉
内部へ貯溜保持させておくことができ、しかも軟
化溶融した廃プラスチツクをスムーズに吐出口へ
落下させることのできる、廃プラスチツクの減容
処理方法及び装置を提供せんとするにある。(Technical Problem) An object of the present invention is to store and retain waste plastic inside a hot blast stove even if scraping means, vibrating means, holding rods, etc., which complicate the structure of the device and increase manufacturing costs, are eliminated. It is an object of the present invention to provide a method and apparatus for volume reduction processing of waste plastics, which can be used to store waste plastics and smoothly drop the softened and melted waste plastics to a discharge port.
(技術的手段)
上述した技術的課題を達成するためにこの発明
は、廃プラスチツクを下部に吐出口を開口させた
熱風炉内で減容処理するに当り、前記熱風炉に前
記吐出口部分を同軸方向に設けたところの内側に
障害物のない漏斗状のものを用い、前記吐出口を
容器で覆うと共に、前記熱風炉の周壁に設けた熱
風導入管より熱風を導入させつつ前記熱風炉内に
廃プラスチツクを投入させ、この廃プラスチツク
が熱風により炉壁に附着したり、前記吐出口より
落下したりしないように浮遊保持させつつ加熱さ
せるものである。(Technical Means) In order to achieve the above-mentioned technical problem, the present invention provides a method for reducing the volume of waste plastic in a hot blast furnace having a discharge opening at the bottom thereof. Using a funnel-shaped thing with no obstructions on the inside of the coaxial direction, cover the discharge port with a container, and introduce hot air into the hot air stove from the hot air introduction pipe provided on the peripheral wall of the hot air stove. The waste plastic is heated while being kept suspended so that it does not stick to the furnace wall or fall from the discharge port due to the hot air.
この発明はまた、加熱温度を300℃の範囲内に
して減容処理するものである。 The present invention also performs volume reduction treatment by keeping the heating temperature within the range of 300°C.
この発明はさらに、熱風室と、この熱風室内に
設けられた熱風炉とを含み、この熱風炉は大径部
から成る頭部と、先端に吐出口を設けた小径部か
ら成る首部を同軸方向に設けたところの内側に障
害物のない漏斗状のものと成し、前記頭部と首部
には前記熱風滞留室内の熱風を内部へ導入させる
熱風導入管を円周方向上下かつ下向きに複数個設
置し、前記吐出口には軟化溶融物を収容させる容
器を上下動可能に設けたものである。 The invention further includes a hot-air chamber and a hot-air stove provided in the hot-air chamber, and the hot-air stove has a head portion consisting of a large diameter portion and a neck portion consisting of a small diameter portion provided with a discharge port at the tip in the same axial direction. The head and neck are provided with a plurality of hot air introduction pipes extending upward and downward in the circumferential direction for introducing the hot air in the hot air retention chamber into the inside of the head and neck. A container for accommodating the softened molten material is provided at the discharge port so as to be movable up and down.
この発明はさらに、熱風導入管の先端が熱風炉
の内面部と面一になるように構成したものであ
る。 The present invention is further configured such that the tip of the hot air introduction pipe is flush with the inner surface of the hot air stove.
(作用)
上述したように構成することにより、熱風炉内
に投入された廃プラスチツクは、吐出口に保持
棒、その他の手段を設けなくとも直ちに落下して
しまうことなく、浮遊保持されつつ加熱されるの
で、軟化溶融しても炉壁へ附着してしまうことが
ないと共に、軟化溶融によつて比重の増加したも
のから順次浮遊保持状態から脱し、吐出口側へ落
下して行くので、目詰まりが生ずることなく、吐
出口側をスムーズに排出させることができるもの
である。(Function) With the above-described configuration, the waste plastics put into the hot blast furnace are heated while being suspended, without falling down immediately, even without providing a holding rod or other means at the discharge port. Therefore, even if it softens and melts, it will not stick to the furnace wall, and as the specific gravity increases due to softening and melting, it will gradually escape from the floating state and fall to the discharge port side, so it will not clog. This allows for smooth discharge from the discharge port side without causing any problems.
(実施例)
以下にこの発明の一実施例を図面に基づいて詳
細に説明すると、1は外気取入用のブロワーであ
り、例えばオイルバーナー2を取りつけた熱風発
生炉3に吸気管4を介して接続されている。熱風
発生炉3の上部には公知の脱臭槽5が設けられ、
この脱臭槽5には排気ブロワー6と循環ポンプ7
が取りつけられている。外気取入れ用のブロワー
1の左隣には、断熱壁8a,8bで構築された熱
風滞留室8が設けられ、断熱壁8aの一側には熱
風発生炉3の出口3aが開口している。熱風滞留
室8内部には大径部から成る頭部9aと、この大
径部の約3分の1の径を有する小径部から成る首
部9bを同軸方向に接続させた漏斗状の熱風炉9
が設けられると共に、首部9bの端部には吐出口
10bが開口している。熱風滞留室8の上部には
熱風炉9の開口上部10aを覆うように投入室1
1が設けられ、この投入室11には投入蓋12が
取り付けられている。熱風炉9の頭部9aと首部
9bには、円周方向上下に複数の熱風導入管1
3,13,13……が下向きに取りつけられると
共に、その噴出側は熱風炉9の内壁と面一になつ
ている。熱風炉9の吐出口10bの回りには排出
室14が設けられ、該排出室14には吐出口10
bに対向してこれを塞ぐかたちで容器15が例え
ば移動可能な油圧ジヤツキ20上に置かれると共
に、その一側に排出蓋16が取りつけられてい
る。そして、脱臭槽5に一方を接続させた排気管
17が、他方を排出室14と投入室11に各々接
続させている。(Embodiment) An embodiment of the present invention will be described below in detail based on the drawings. Reference numeral 1 denotes a blower for taking in outside air, which is connected to a hot air generating furnace 3 equipped with an oil burner 2 through an intake pipe 4. connected. A known deodorizing tank 5 is provided in the upper part of the hot air generating furnace 3.
This deodorizing tank 5 includes an exhaust blower 6 and a circulation pump 7.
is attached. A hot air retention chamber 8 constructed of heat insulating walls 8a and 8b is provided on the left side of the blower 1 for taking in outside air, and an outlet 3a of the hot air generating furnace 3 is opened on one side of the heat insulating wall 8a. Inside the hot air retention chamber 8, there is a funnel-shaped hot blast furnace 9 in which a head portion 9a consisting of a large diameter portion and a neck portion 9b consisting of a small diameter portion having a diameter approximately one-third of the large diameter portion are coaxially connected.
is provided, and a discharge port 10b is opened at the end of the neck portion 9b. An input chamber 1 is provided in the upper part of the hot air retention chamber 8 so as to cover the opening upper part 10a of the hot air stove 9.
1 is provided, and a charging lid 12 is attached to this charging chamber 11. A plurality of hot air introduction pipes 1 are installed in the head 9a and neck 9b of the hot air stove 9 in the upper and lower circumferential directions.
3, 13, 13, . A discharge chamber 14 is provided around the discharge port 10b of the hot air stove 9, and the discharge chamber 14 includes a discharge port 10b.
The container 15 is placed on, for example, a movable hydraulic jack 20 so as to face and close the container 15, and a discharge lid 16 is attached to one side of the container 15. The exhaust pipe 17 has one end connected to the deodorizing tank 5, and the other end connected to the discharge chamber 14 and the input chamber 11, respectively.
今、バーナー2に点火させ、ブロワー1をON
させ、熱風炉9内部が約200℃に達したのを確認
した後、投入蓋12を開いてモルトプレン、発泡
スチロール、ポリエチレン頭の種々雑多な廃プラ
スチツクの混合物を投入させてやり投入蓋12を
閉じる。 Now, ignite burner 2 and turn on blower 1.
After confirming that the inside of the hot-blast stove 9 has reached about 200°C, the charging lid 12 is opened and a mixture of miscellaneous waste plastics such as maltprene, styrofoam, and polyethylene head is charged, and the spear charging lid 12 is closed.
すると、この時すでに熱風発生炉3より熱風滞
留室8を通り、熱風導入管13,13,13……
より熱風炉9内に送り込まれている熱風は、渦を
巻いて熱風炉9の内壁に添つて下降し、首部9b
から吐出口10b側へ向かうが、該吐出口10b
は、容器15によつて塞がれていることから、反
転してさらに強い上昇気流となつて熱風炉9の上
方へ吹き上げているので、この風力により投入室
11より投入された軟化溶融前の廃プラスチツク
の最初のものは、そのまま吐出口10b側へ落下
してしまうことなく浮遊保持される。もつとも、
石や金属のような重いものは強い上昇気流にもか
かわらずそのまま容器15内に落下してしまう。 Then, at this time, the hot air has already passed through the hot air retention chamber 8 from the hot air generating furnace 3, and the hot air introduction pipes 13, 13, 13...
The hot air that is being sent into the hot air stove 9 spirals and descends along the inner wall of the hot air stove 9, and the hot air is sent into the hot air stove 9.
from the discharge port 10b, but the discharge port 10b
Since it is blocked by the container 15, it reverses and becomes an even stronger updraft and is blown upwards in the hot blast furnace 9. This wind force causes the unsoftened and melted material charged from the charging chamber 11 to The first piece of waste plastic is kept floating without falling directly to the discharge port 10b. However,
Heavy objects such as stones and metals fall into the container 15 despite the strong updraft.
投入された廃プラスチツクの量が多くなると、
該廃プラスチツクが小径になつた首部の部分で凝
縮されるので、この圧力によつて互いに吐出口側
へ落下するが防止される一方、この間においても
熱風導入管13,13,13……より導入される
熱風は、渦を巻いて熱風炉9の内壁と投入された
廃プラスチツクの塊の外周との間に間隙18を生
じさせているので、第2図に示したようにこの投
入された廃プラスチツクの19は、この導入され
た熱風の上昇気流と回転気流とによつて、熱風炉
9内において浮遊保持された状態で回転しつつ加
熱されることになる。 As the amount of waste plastic input increases,
Since the waste plastics are condensed at the neck portion where the diameter has become smaller, this pressure prevents them from falling toward the discharge port side, while at the same time, the waste plastics are also introduced from the hot air introduction pipes 13, 13, 13... The hot air swirls and creates a gap 18 between the inner wall of the hot air stove 9 and the outer periphery of the thrown-in lump of waste plastic, as shown in Fig. 2. The plastic 19 is rotated and heated in a floating state in the hot air stove 9 by the upward current of the introduced hot air and the rotating air current.
そして、この加熱は、熱風滞留室8内の熱風に
よる熱風炉9を介しての間接加熱と、熱風導入管
13,13,13……を介して熱風炉9内へ導入
される熱風による直接加熱による二段加熱であ
る。 This heating includes indirect heating by hot air in the hot air retention chamber 8 via the hot air stove 9, and direct heating by hot air introduced into the hot air stove 9 via the hot air introduction pipes 13, 13, 13... This is two-stage heating.
ところで、都市ゴミや産業廃棄物の中には、前
述したように極めて他種類のプラスチツクが混合
しており、その混合割合もさまざまである。した
がつて、熱風炉9内の加熱温度も150℃程度から
400℃程度まで選択の巾があるが、一般に400℃を
越える高温になると、プラスチツクの燃焼が始ま
り、有毒ガスの発生量が増加して好ましくないの
で、400℃以下に押えられる。 By the way, as mentioned above, many different types of plastics are mixed in municipal garbage and industrial waste, and the mixing ratios vary. Therefore, the heating temperature inside the hot air stove 9 is also around 150℃.
There is a wide selection range up to about 400°C, but in general, if the temperature exceeds 400°C, the plastic will begin to burn and the amount of toxic gas generated will increase, which is undesirable, so the temperature should be kept below 400°C.
しかし、300℃以上になるとプラスチツクの種
類によつてはダイオキシンの発生がみられるの
で、最も好ましい加熱温度は150℃〜200℃の範囲
である。この温度範囲であると、廃プラスチツク
は溶融することなく軟化して比重の増加と共に上
昇気流に抗して吐出口10b側へ落下する。熱風
炉9の加熱に間接加熱と直接加熱とを併用する理
由は、前者により熱風炉9全体に充分な熱を与
え、後者は直接加熱により熱風炉9内の加熱状態
を調整するためである。熱風炉9の周壁に円周方
向上下、かつ下向きに取り付けられた熱風導入管
13,13,13……から、下向き螺旋状に吹き
込まれる熱風は、熱風炉9の内壁の軟化溶融した
廃プラスチツクの付着を防止しつつ、該熱風炉9
内の投入廃プラスチツクを軟化溶融凝縮させ、熱
風炉9の中心部下方へ移動させる。 However, if the heating temperature exceeds 300°C, depending on the type of plastic, dioxin may be generated, so the most preferable heating temperature is in the range of 150°C to 200°C. In this temperature range, the waste plastic softens without melting, and as the specific gravity increases, it falls toward the discharge port 10b against the rising air current. The reason why indirect heating and direct heating are used together to heat the hot air stove 9 is that the former provides sufficient heat to the entire hot air stove 9, and the latter uses direct heating to adjust the heating state inside the hot air stove 9. The hot air blown downward spirally from the hot air introduction pipes 13, 13, 13, etc. attached to the circumferential wall of the hot air stove 9 upward and downward in the circumferential direction is used to absorb the softened and melted waste plastics on the inner wall of the hot air stove 9. While preventing adhesion, the hot air stove 9
The input waste plastic is softened, melted, condensed, and moved to the lower center of the hot blast furnace 9.
そして、ついには比重が増加して強い上昇気流
にもかかわらず、首部9bを通過して吐出口10
bより順次容器15内へ滴下乃至落下するにいた
る。 Finally, despite the increase in specific gravity and strong upward airflow, the air passes through the neck 9b and reaches the discharge port 10.
From b, the liquid drips or falls into the container 15 in sequence.
その際、軟化しない熱硬化性樹脂や、石、生ゴ
ミ等は、従来のもののように吐出口の部分に保持
棒等の障害物がないので、そのままか、或いは軟
化溶融したプラスチツクと共に容器15内へ引つ
かかることなくスムーズに落下する。 At this time, thermosetting resins that do not soften, stones, garbage, etc., are left in the container 15 as they are, or together with the softened and molten plastics, because there is no obstruction such as a holding rod at the discharge port unlike in conventional products. It falls smoothly without getting caught.
他方、木や紙等は燃焼し、そのうち灰その他の
固形物は軟化溶融したプラスチツクと共に吐出口
10bへ落下するが、燃焼ガスは他の発生ガスと
共に投入室11にいたり、その上部に接続させた
排気管17を介して脱臭槽5へ導かれ、脱臭され
た後排気ブロワー6によつて外部へ放出させられ
る。 On the other hand, wood, paper, etc. are burned, and ash and other solid materials fall into the discharge port 10b together with softened and molten plastic, but the combustion gas goes into the input chamber 11 along with other generated gases, and is connected to the upper part of the chamber 11. The odor is guided to the deodorizing tank 5 via the exhaust pipe 17, deodorized, and then discharged to the outside by the exhaust blower 6.
容器15に軟化溶融した廃プラスチツクが溜つ
たところで、排出蓋16を開して容器15を降下
させてこれを外部へ取り出し、固化成型させるも
のである。尚、この容器15による吐出口10b
の塞ぎは、必ずしも完全なものである必要はな
く、若干の隙間があつても、これによつて熱風炉
9内で廃プラスチツクを浮遊保持させる風量が確
保されている限り問題は生じない。 When the softened and molten waste plastics have accumulated in the container 15, the discharge lid 16 is opened, the container 15 is lowered, and the waste plastics are taken out to the outside and solidified and molded. Note that the discharge port 10b of this container 15
The sealing does not necessarily have to be complete, and even if there is a slight gap, no problem will occur as long as the amount of air that keeps the waste plastic suspended in the hot air stove 9 is ensured.
上述したようにして固化成型されたものは、溶
融軟化したプラスチツクをバインダーとして、そ
の他の軟化しないプラスチツクや廃棄物がコンパ
クトに固められた形状になる。例えば、発泡プラ
スチツクを主体とするゴミ等では、当初の体積の
数10分の1まで減容することができ、これを再生
処理(二次処理)する場合にも、また、埋立処理
する場合にもその取り扱いは極めて容易である。 The product solidified and molded as described above has a shape in which the melted and softened plastic is used as a binder, and other non-softened plastics and waste are solidified into a compact shape. For example, garbage mainly made of foamed plastic can be reduced to several tenths of its original volume, and can be recycled (secondary treatment) or landfilled. It is also extremely easy to handle.
(効果)
以上、詳細に説明したようにこの発明は、構造
が簡単なので故障が生ずる恐れを少なくし、大幅
なコストダウンを図れる装置で、種々雑多のもの
を含む廃プラスチツクを、目詰りを生じさせるこ
となく、極めてスムーズに連続して減容処理させ
ることができるという効果を奏し得る。(Effects) As explained in detail above, this invention is a device that has a simple structure, reduces the risk of failure, and can significantly reduce costs. It is possible to achieve the effect that the volume reduction process can be carried out extremely smoothly and continuously without causing any problems.
第1図はこの発明を概略的に示す一部断面正面
図であり、第2図はこの発明を説明するための要
部断面図である。
3……熱風発生炉、8……熱風滞留室、9……
熱風炉、13……熱風導入管、14……排出室、
15……容器。
FIG. 1 is a partially sectional front view schematically showing the present invention, and FIG. 2 is a sectional view of essential parts for explaining the invention. 3...Hot air generation furnace, 8...Hot air retention chamber, 9...
Hot air stove, 13... Hot air introduction pipe, 14... Discharge chamber,
15... Container.
Claims (1)
熱風炉内で減容処理するに当り、前記熱風炉に前
記吐出口部分を同軸方向に設けたところの内側に
障害物のない漏斗状のものを用い、前記吐出口を
容器で覆うと共に、前記熱風炉の周壁に設けた熱
風導入管より熱風を導入させつつ前記熱風炉内に
廃プラスチツクを投入させ、この廃プラスチツク
が熱風により炉壁に附着したり、前記吐出口より
落下したりしないように熱風で浮遊保持させつつ
加熱させることを特徴とする、廃プラスチツクの
減容処理方法。 2 加熱温度が300℃の範囲であることを特徴と
する、特許請求の範囲第1項記載の廃プラスチツ
クの減容処理方法。 3 熱風室と、この熱風室内に設けられた熱風炉
とを含み、この熱風炉は大径部から成る頭部と、
下端に吐出口を設けた小径部から成る首部を同軸
方向に設けたところの、内側に障害物のない漏斗
状のものと成し、前記頭部と首部には前記熱風滞
溜室内の熱風を内部へ導入させる熱風導入管を円
周方向上下かつ下向きに複数個設置し、前記吐出
口には軟化溶融物を収容させる容器を上下動可能
に設置したことを特徴とする、廃プラスチツクの
減容処理装置。 4 熱風導入管の先端が熱風炉の内面部と面一に
なるように構成したことを特徴とする、特許請求
の範囲第2項記載の廃プラスチツクの減容処理装
置。[Scope of Claims] 1. When waste plastic is subjected to volume reduction treatment in a hot blast furnace with a discharge port opened at the bottom, an obstacle is placed inside the hot blast furnace where the discharge port is provided coaxially. Using a hollow funnel-shaped object, the discharge port is covered with a container, and waste plastic is introduced into the hot air furnace while introducing hot air from a hot air introduction pipe provided on the peripheral wall of the hot air furnace. A method for reducing the volume of waste plastics, characterized by heating the waste plastics while keeping them suspended in hot air so that they do not stick to the furnace wall or fall from the discharge port. 2. The method for volume reduction of waste plastics according to claim 1, characterized in that the heating temperature is in the range of 300°C. 3. It includes a hot-air chamber and a hot-air stove installed in the hot-air chamber, and this hot-air stove has a head consisting of a large diameter part,
The neck part consisting of a small diameter part with a discharge port provided at the lower end is provided coaxially and is shaped like a funnel with no obstruction on the inside, and the head and neck part are used to direct hot air from the hot air retention chamber A method for reducing the volume of waste plastic, characterized in that a plurality of hot air introduction pipes are installed circumferentially upwardly and downwardly, and a container for storing the softened molten material is installed at the discharge port so as to be movable up and down. Processing equipment. 4. The waste plastic volume reduction processing apparatus according to claim 2, characterized in that the tip of the hot air introduction pipe is configured to be flush with the inner surface of the hot air stove.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59268166A JPS61273913A (en) | 1984-12-19 | 1984-12-19 | Method and device for volume-reducing disposal of waste plastic |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59268166A JPS61273913A (en) | 1984-12-19 | 1984-12-19 | Method and device for volume-reducing disposal of waste plastic |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS61273913A JPS61273913A (en) | 1986-12-04 |
JPS6336924B2 true JPS6336924B2 (en) | 1988-07-22 |
Family
ID=17454821
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP59268166A Granted JPS61273913A (en) | 1984-12-19 | 1984-12-19 | Method and device for volume-reducing disposal of waste plastic |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS61273913A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0345280U (en) * | 1989-09-07 | 1991-04-25 |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0181110A3 (en) * | 1984-10-22 | 1988-05-11 | Kissei Pharmaceutical Co. Ltd. | Histidine derivatives as renin inhibitors |
EP0206807A3 (en) * | 1985-06-28 | 1988-01-20 | Kissei Pharmaceutical Co. Ltd. | Novel amino acid derivatives |
US4853463A (en) * | 1985-09-04 | 1989-08-01 | Kissei Pharmaceutical Co., Ltd. | Amino acid derivatives |
JPS6322081A (en) * | 1986-07-11 | 1988-01-29 | Kissei Pharmaceut Co Ltd | Novel amino acid derivative |
US5240656A (en) * | 1991-05-21 | 1993-08-31 | Plastics Densification, Inc. | Treatment of waste |
GB2410919B (en) | 2004-02-13 | 2009-03-18 | David J Scheeres | Improvements in or relating to the treatment of waste |
GB0513148D0 (en) * | 2005-06-29 | 2005-08-03 | Taylor Products Ltd | Apparatus for thermally compacting expanded polystyrene boxes |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5718105B2 (en) * | 1977-07-11 | 1982-04-14 | ||
JPS59159313A (en) * | 1983-03-01 | 1984-09-08 | Moruton Hanbai Kk | Apparatus for melting treatment of foamed waste plastic |
JPS5946214B2 (en) * | 1975-05-29 | 1984-11-10 | ウェルファイド株式会社 | Production method of aminoketone derivatives |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS498568U (en) * | 1972-04-25 | 1974-01-24 | ||
JPS5718105U (en) * | 1980-06-24 | 1982-01-29 | ||
JPS5946214U (en) * | 1982-09-20 | 1984-03-27 | 猪田 裕三 | Styrofoam recycling processing machine |
JPS59159313U (en) * | 1983-04-12 | 1984-10-25 | 工藤 正雄 | Accessories with a container body that penetrates perfume and releases fragrance |
-
1984
- 1984-12-19 JP JP59268166A patent/JPS61273913A/en active Granted
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5946214B2 (en) * | 1975-05-29 | 1984-11-10 | ウェルファイド株式会社 | Production method of aminoketone derivatives |
JPS5718105B2 (en) * | 1977-07-11 | 1982-04-14 | ||
JPS59159313A (en) * | 1983-03-01 | 1984-09-08 | Moruton Hanbai Kk | Apparatus for melting treatment of foamed waste plastic |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0345280U (en) * | 1989-09-07 | 1991-04-25 |
Also Published As
Publication number | Publication date |
---|---|
JPS61273913A (en) | 1986-12-04 |
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