JPS59213793A - Gasification furnace for waste plastic - Google Patents

Gasification furnace for waste plastic

Info

Publication number
JPS59213793A
JPS59213793A JP58087845A JP8784583A JPS59213793A JP S59213793 A JPS59213793 A JP S59213793A JP 58087845 A JP58087845 A JP 58087845A JP 8784583 A JP8784583 A JP 8784583A JP S59213793 A JPS59213793 A JP S59213793A
Authority
JP
Japan
Prior art keywords
furnace
chamber
combustion chamber
air
attached
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
Application number
JP58087845A
Other languages
Japanese (ja)
Inventor
Tatsuji Saitou
斉藤 太都司
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
SHINTOU KIKO KK
Original Assignee
SHINTOU KIKO KK
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by SHINTOU KIKO KK filed Critical SHINTOU KIKO KK
Priority to JP58087845A priority Critical patent/JPS59213793A/en
Publication of JPS59213793A publication Critical patent/JPS59213793A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/62Plastics recycling; Rubber recycling

Abstract

PURPOSE:To provide a gasification furnace capable of utilizing the environment- polluting waste plastics as a fuel source, and furnished with a number of air- feeding holes inclined toward a definite direction to cause gyration in a horizontal plane at the upper part of the combustion chamber, and with a double lid opening alternately to the outside and the inside of the furnace and attached to the inlet port of the raw material. CONSTITUTION:The objective furnace for the gasification of waste plastics has the following structure. A flow path is formed starting from the top of the combustion chamber 1, passing through the descending chamber 2 and the ascending chamber 3 and reaching the exhaust port 4; and a number of air-feeding holes 6 connected to an air feeding path of a compressor, are attached to the upper part of the combustion chamber 1 in a manner inclined toward a definite direction to cause a gyrating flow in a horizontal plane. An ignition burner 7 is attached to the combustion zone, and the inlet port 8 of the raw material is furnished with a double lids 9 and 10 which open alternately to the inside and the outside of the furnace.

Description

【発明の詳細な説明】 深尿等流動性廃棄物の処理用焼却炉や脱臭炉は、その処
理エネルギーとして従来重油が用いられて来た。しかし
重油も高価になってその負担は大きい。そこで上記負担
を軽減する目的から本発明はプラスチックの廃材を燃料
源として活用することをもくろみ開発したものである。
DETAILED DESCRIPTION OF THE INVENTION Conventionally, heavy oil has been used as the processing energy for incinerators and deodorizing furnaces for processing fluid waste such as deep urine. However, heavy oil has also become expensive, which is a big burden. Therefore, in order to reduce the above-mentioned burden, the present invention was developed with the intention of utilizing plastic waste as a fuel source.

以下図面に基いて、本発明の詳細な説明する図中1は燃
焼室であって、ここに廃材のプラスチックを破砕したも
のを投入して燃焼せしめるものである。プラスチックは
着火、燃焼は容易であるが、そのとき多量の煤煙と有害
ガスを発生する欠点が伴う。従って燃焼室1には上層部
へ多数の給気孔6が設けてありしかもこの給気孔6は送
気路5を介してコンプレッサーから空気を送入する如く
しである。各給気孔6はその向きを水平面内一定旋回方
向に傾斜させ燃焼気体が旋回するように配置されている
。同燃焼室1の下層部に点火バーナー7が設けてあり、
燃焼ガスは燃焼室1の上部から下降経路2および上昇経
路3をたどり排出口4に至る如く流気路が形成されてい
る。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Referring to the drawings, the present invention will be described in detail below. Reference numeral 1 in the drawings is a combustion chamber, into which crushed plastic waste is charged and combusted. Although plastics are easy to ignite and burn, they have the disadvantage of generating large amounts of soot and harmful gases. Therefore, a large number of air supply holes 6 are provided in the upper part of the combustion chamber 1, and these air supply holes 6 are designed to introduce air from a compressor through an air supply path 5. Each air supply hole 6 is arranged so that its direction is inclined in a certain swirling direction in a horizontal plane so that the combustion gas swirls. An ignition burner 7 is provided in the lower part of the combustion chamber 1,
A flow path is formed in which the combustion gas follows a descending path 2 and an ascending path 3 from the upper part of the combustion chamber 1 to an exhaust port 4 .

又原料投入口8には炉外と炉内へ交互に開通ずる如く、
二重蓋9.10が設けられている。上記炉内外へ交互に
開通するとは二重蓋9.10間に形成される室11が内
外へ同時に開通して投入口より火焔が噴出することを防
ぐもので蓋10が閉した状態で蓋9を開き、室11内へ
原料を投入する。次いで孟9を閉じた後蓋10を開いて
室11内の原料を燃焼室1内へ落下せしめる如くしたも
のである。
In addition, the raw material inlet 8 is opened alternately to the outside of the furnace and into the inside of the furnace.
A double lid 9.10 is provided. The above-mentioned opening to the inside and outside of the furnace alternately means that the chamber 11 formed between the double lids 9 and 10 is opened to the inside and outside at the same time to prevent flames from spewing out from the inlet, and the lid 9 is opened with the lid 10 closed. , the raw material is introduced into the chamber 11. Next, after closing the tray 9, the lid 10 is opened to allow the raw material in the chamber 11 to fall into the combustion chamber 1.

而して排出口4は吸引ブロワ−に連結し該吸引ブロワ−
を介しロータリーキルンに導くものである。
Therefore, the discharge port 4 is connected to a suction blower, and the suction blower is connected to the suction blower.
It leads to the rotary kiln through the rotary kiln.

面、図面に示す実施例でば流気路の経路3を形成する竪
形筒の周壁12に、多数の流気分岐路13を複数列に水
平面内一定旋回方向に傾斜して設&Jである。又14,
15は炉内の点検補修のための出入口兼灰掻出口、16
.16はガス回加!:(シ用点火バーナーである。
In the embodiment shown in the drawings, a large number of air flow branch passages 13 are installed in plural rows on the circumferential wall 12 of a vertical cylinder forming the air flow path 3 in a horizontal plane and inclined in a constant turning direction. Also 14,
15 is an entrance/exit and ash removal port for inspection and repair inside the furnace; 16
.. 16 is a gas cycle! :(It is an ignition burner for shi.

又点火バーナー7.16は重油だけでなく廃油の使用も
FIJ能であり燃油ff12 OA/h程度の小型のも
ので事足り、通常はプラスチック廃材が自身で燃えだす
と、この点火バーナー7.16は停止してよいものであ
る。
In addition, the ignition burner 7.16 is capable of using not only heavy oil but also waste oil, so a small fuel of about ff12 OA/h is sufficient.Usually, when plastic waste starts to burn on its own, this ignition burner 7.16 It is okay to stop.

更に前記排出口4に連結する吸引ブロヮ二は22kw程
度のものを使用して好結果を納めている。本発明は上述
の実施例に見られる如く構成された装置にかかわるもの
である。
Furthermore, the suction blower connected to the discharge port 4 has a power of about 22 kW, and good results have been achieved. The present invention relates to an apparatus constructed as seen in the embodiments described above.

次にこの装置の機能を説明すると破砕したプラスチック
廃材を燃焼室1的に投入し、点火バーナー7により点火
燃焼せしめるとき多数の給気孔6から給気し、かつ同給
気は旋回流を生じるので煤煙は次元を重ねて給気にめぐ
まれ燃焼を完全化して煤煙量を少なくする。温度800
℃以上の燃焼ガスには有害物は殆ど除去されているが上
述の本発明の実施例において、燃焼ガスの温度は120
0℃にも至り1立方米の燃焼ガス中煤塵量は0゜4g程
度である。
Next, to explain the function of this device, when crushed plastic waste is put into the combustion chamber 1 and ignited and combusted by the ignition burner 7, air is supplied through a large number of air supply holes 6, and the supplied air generates a swirling flow. The soot and smoke are absorbed into the supply air in multiple dimensions to complete combustion and reduce the amount of soot and smoke. temperature 800
Although most harmful substances are removed from the combustion gas at a temperature of 120 °C or higher, in the embodiment of the present invention described above, the temperature of the combustion gas is 120
The temperature reaches 0°C, and the amount of soot and dust in 1 cubic meter of combustion gas is about 0°4g.

尚ガスの旋回流は前述の燃焼室lの他に上昇室3におい
ても水平面内で発生し、遠心分離の作用で灰や固形物が
炉底に沈降すると共に、ガスが下降室2から上昇室3に
向って18o°方向を転じる際にも遠心力の作用で固形
物を分離し炉底に堆積せしめガス純度を向上せしめる効
果が大きい。
In addition to the combustion chamber 1 described above, the swirling flow of gas also occurs in the rising chamber 3 in a horizontal plane, and as a result of centrifugal separation, ash and solids settle to the bottom of the furnace, and gas flows from the descending chamber 2 to the rising chamber. Even when the direction is turned 18° toward the third direction, solid matter is separated by the action of centrifugal force and deposited on the bottom of the furnace, which has a great effect of improving gas purity.

故に本発明を実施することにより、得たる熱ガスをロー
タリーキルンに導いて流動性廃棄物処理の有効なエネル
ギー源とすることができ、一方公害をまねき易いプラス
チック廃棄物の処理にも役立つものである。
Therefore, by carrying out the present invention, the obtained hot gas can be led to a rotary kiln and used as an effective energy source for processing fluid waste, and on the other hand, it is also useful for processing plastic waste that tends to cause pollution. .

【図面の簡単な説明】[Brief explanation of drawings]

図面は本発明の実施例を示すものである。第1図はその
縦断面図、第2図は第1図のA−A断面図である。 1     燃焼室 2     下降室 3     上昇室 4     排出口 5     送気路 6     給気孔 7     点火)\−ナー 8     原料投入口 9.1〇  二重蓋 特許出願人   斉藤太都司(はが1名)代理人 弁理
士古田剛啓
The drawings illustrate embodiments of the invention. FIG. 1 is a longitudinal sectional view thereof, and FIG. 2 is a sectional view taken along line AA in FIG. 1 Combustion chamber 2 Descending chamber 3 Rising chamber 4 Discharge port 5 Air supply path 6 Air supply hole 7 Ignition)\-ner 8 Raw material input port 9.1〇 Double lid patent applicant Taitoji Saito (one person) Representative Patent attorney Takehiro Furuta

Claims (1)

【特許請求の範囲】[Claims] 燃焼室(1)の上部から下降室(2)および上昇室(3
)の経路をたどり排出口(4)に至る流気路を形成し、
コンプレッサーからの送気路(5)に連なる多数の給気
孔(6)を燃焼室(1)の上層部へ水平内面一定旋回方
向に傾斜して設けると共に火層部に点火バーナー(7)
を設けかつ原料投入口(8)へ炉外と炉内へ交互に開通
するごと(二重i(9,10)を設けてなるプラスチッ
ク廃材のガス化炉。
A descending chamber (2) and a rising chamber (3) are formed from the upper part of the combustion chamber (1).
) to form a flow path leading to the outlet (4),
A large number of air supply holes (6) connected to the air supply path (5) from the compressor are provided in the upper part of the combustion chamber (1) so that the horizontal inner surface is inclined in a constant rotation direction, and an ignition burner (7) is provided in the fire layer part.
A plastic waste gasification furnace is provided with a double I (9, 10) which alternately opens to the outside and inside of the furnace to the raw material inlet (8).
JP58087845A 1983-05-18 1983-05-18 Gasification furnace for waste plastic Pending JPS59213793A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58087845A JPS59213793A (en) 1983-05-18 1983-05-18 Gasification furnace for waste plastic

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58087845A JPS59213793A (en) 1983-05-18 1983-05-18 Gasification furnace for waste plastic

Publications (1)

Publication Number Publication Date
JPS59213793A true JPS59213793A (en) 1984-12-03

Family

ID=13926226

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58087845A Pending JPS59213793A (en) 1983-05-18 1983-05-18 Gasification furnace for waste plastic

Country Status (1)

Country Link
JP (1) JPS59213793A (en)

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5325604A (en) * 1976-08-20 1978-03-09 Hitachi Plant Eng & Constr Co Ltd Gasification of thermal decomposition residues and its apparatus
JPS5456608A (en) * 1977-09-27 1979-05-07 Neuhaus Schwermann Albert Process for producing fuel gas and fluidized bed reactor for carrying out same
JPS5653185A (en) * 1978-09-25 1981-05-12 Midland Ross Corp Method of running vertical continuous gasification furnace and said furnace
JPS5718786A (en) * 1980-05-29 1982-01-30 Szloboda David Tibor Method and apparatus for converting waste material to fuel gas

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5325604A (en) * 1976-08-20 1978-03-09 Hitachi Plant Eng & Constr Co Ltd Gasification of thermal decomposition residues and its apparatus
JPS5456608A (en) * 1977-09-27 1979-05-07 Neuhaus Schwermann Albert Process for producing fuel gas and fluidized bed reactor for carrying out same
JPS5653185A (en) * 1978-09-25 1981-05-12 Midland Ross Corp Method of running vertical continuous gasification furnace and said furnace
JPS5718786A (en) * 1980-05-29 1982-01-30 Szloboda David Tibor Method and apparatus for converting waste material to fuel gas

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