JP2002301400A - Refuse disposal system - Google Patents

Refuse disposal system

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Publication number
JP2002301400A
JP2002301400A JP2001105647A JP2001105647A JP2002301400A JP 2002301400 A JP2002301400 A JP 2002301400A JP 2001105647 A JP2001105647 A JP 2001105647A JP 2001105647 A JP2001105647 A JP 2001105647A JP 2002301400 A JP2002301400 A JP 2002301400A
Authority
JP
Japan
Prior art keywords
garbage
refuse
incinerator
dryer
conveyor
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.)
Granted
Application number
JP2001105647A
Other languages
Japanese (ja)
Other versions
JP4750962B2 (en
Inventor
Takashi Hamada
尚 浜田
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP2001105647A priority Critical patent/JP4750962B2/en
Publication of JP2002301400A publication Critical patent/JP2002301400A/en
Application granted granted Critical
Publication of JP4750962B2 publication Critical patent/JP4750962B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Disintegrating Or Milling (AREA)
  • Refuse Collection And Transfer (AREA)
  • Processing Of Solid Wastes (AREA)
  • Combined Means For Separation Of Solids (AREA)
  • Crushing And Pulverization Processes (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a refuse disposal system in which refuse left at a lower part is eliminated and the exhalation of a malodor is prevented by directly sending fed refuse bags by a receiving conveyor and immediately disposing of them, the burdens on the receiving conveyor is lightened by reducing an opening part, and reduction of facilities costs, facilitation of construction and effective utilization of ground inside facilities are actualized by constituting a pit in a small size. SOLUTION: This refuse disposal system for kitchen refuse, or the like, is constituted of a refuse line composed of a bunker 1 to which the refuse bags are fed, a conveyor 2 for carrying the refuse bags placed inside the bunker, a refuse bag breaking machine 3, a magnetic separator 4, a refuse dryer 6, separator 7, shredders 8 and 9 and an incinerator 11. The bunker is formed in a small size and the fed refuse bags are directly sent to the refuse line by the conveyor, dried, shredded and then incinerated. Since dried and shredded refuse is supplied to the incinerator, the combustion rate of the incinerator is accelerated, the generation of harmful materials such as exhaust gas and dioxins, is suppressed and the malodor of an incineration plant is prevented by complete combustion and the improvement of a working environment, or the like, is attained. Also, the refuse does not remain at the lower part and the exhalation of the malodor is prevented. The opening part is reduced and the burdens on a conveyor area are lightened as a result.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、廃棄物、生ごみ等
のごみ処理システムに関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a waste disposal system for waste, garbage and the like.

【0002】[0002]

【従来の技術】従来の一般廃棄物、又は生ごみ等のごみ
(以下、ごみとする)を処理する施設の主役は一般に焼却
施設である。このごみの中で生ごみは、多量の水分を含
む(水分を約60%含む)ので、そのまま焼却炉に投入する
ことにより、焼却炉内の冷却作用を起し、乾燥速度の低
下、燃焼速度の低下による燃焼時間の長時間化、又は燃
料の増加等を招来すること、殊に、不完全燃焼による排
カ゛ス及び/又はタ゛イオキシン等の有害物質発生の危険性があ
る。また焼却場から発生する悪臭は、職場環境も悪く、
工場外に漏れれば社会問題となる。
2. Description of the Related Art Conventional general waste or garbage such as garbage.
The facility that treats waste (hereinafter referred to as garbage) is generally incinerated. Among the garbage, garbage contains a large amount of water (containing about 60% of water), so if it is put into an incinerator as it is, it will cause a cooling action in the incinerator, causing a decrease in drying rate and burning rate. This leads to a prolonged combustion time or an increase in fuel due to a decrease in fuel consumption. In particular, there is a risk of emission of harmful substances such as exhaust gas and / or dioxin due to incomplete combustion. In addition, the bad odor generated from the incineration plant has a bad working environment,
If it leaks outside the factory, it becomes a social problem.

【0003】また従来の貯溜ヒ゜ット方法は、ヒ゜ットの生ごみ
の上方のみを掴み排出する構造(装置)が多い。従って、
下方の生ごみがハ゛ンカーに残留することから、腐敗が始ま
り悪臭が発生する。この残留する生ごみの悪臭は酷く、
作業者又は近所の住民にも思わぬ被害を与える。そのた
めに、エアカーテン及び/又はエア吸引(負圧吸引方式)による悪
臭を封じ込める方法、又は悪臭排気を積極的に行う方
法、等を採用しているが、十分な成果が上がっていない
のが現況である。
[0003] Further, the conventional storage hitting method often has a structure (apparatus) for grasping and discharging only the upper portion of the garbage of the hit. Therefore,
Since the lower garbage remains in the bunker, it begins to rot and foul odors are generated. The odor of this remaining garbage is severe,
Causes unexpected damage to workers and neighbors. For this purpose, a method to contain odors by air curtain and / or air suction (negative pressure suction method) or a method to actively exhaust odors have been adopted, but no satisfactory results have been achieved at present. It is.

【0004】前述の問題の解消と、この種の焼却施設に
関する先行技術としては、次の文献(1)〜(3)等が挙げら
れる。以下に概述する。(1)特開平9-329316号のコ゛ミ焼却
場(文献(1)とする)があり、廃棄物を搬入するフ゜ラットホーム
の直下に、ごみ貯溜用のごみヒ゜ットを設け、フ゜ラットホームの側
方にごみヒ゜ットへのごみ投入用のごみ投入扉を設けた構成
であり、必要とする平面積を減少でき狭い面積の敷地で
も構築が可能で、ごみヒ゜ット側からの悪臭を封じ込めてフ゜
ラットホームその他に流出することを少なくできる。(2)特開
平10-263496号のごみ処理ヒ゜ットにおける悪臭防止装置(文
献(2)とする)があり、建屋を処理室と前室とに仕切り、
前室の前後をタ゛フ゛ルシャッタ構造としてごみ処理ヒ゜ットの上面
を区画壁で仕切りごみ収容空間を密閉可能とし、フ゛ロワに
より臭気を吸引して脱臭させる構成であり、ごみ処理ヒ゜
ットからの悪臭が外部に漏れるのを防止しつつ、脱臭のた
めの動力を低減できる。また(3)特開2001-48353のごみ
処理施設のごみヒ゜ット(文献(3)とする)があり、ごみ投入ス
テーシ゛からごみヒ゜ット前段部にごみを投入し、天井クレーンによ
ってごみヒ゜ット後段部に移し替えて堆積した後に、ホッハ゜の
投入口より投入して焼却処理する構成であり、ごみヒ゜ット
後段部に運び入れたごみを、投入口の高さまで堆積する
ことができるので、ごみヒ゜ットの底面を浅くすることがで
きる。
[0004] Prior art relating to solving the above-mentioned problem and this kind of incineration facility includes the following documents (1) to (3). This is outlined below. (1) There is a waste incineration plant disclosed in Japanese Patent Application Laid-Open No. 9-329316 (referred to as Reference (1)). It is equipped with a garbage input door for garbage input, which reduces the required flat area and enables construction on a site with a small area, and prevents odor from the garbage heat from leaking out to platforms and other places. Can be reduced. (2) There is an odor prevention device (referred to as reference (2)) in the garbage disposal unit of JP-A-10-263496, which partitions the building into a treatment room and a front room,
The front and rear of the front room have a double shutter structure, the upper surface of the refuse disposal unit is partitioned by a partition wall, and the refuse storage space can be hermetically sealed. The power for deodorization can be reduced while preventing the occurrence of odor. In addition, (3) there is a garbage dump at the garbage disposal facility described in JP-A-2001-48353 (reference (3)), in which garbage is put into the front part of the garbage sheet from the garbage input station and transferred to the rear part of the garbage sheet by an overhead crane. After the waste is deposited and replaced, the waste is thrown from the inlet of the hopper and incinerated.The waste brought into the rear part of the waste can be deposited up to the height of the inlet, so the bottom of the waste is shallow. can do.

【0005】[0005]

【発明が解決しようとする課題】従来、生ごみを、その
まま焼却炉に投入する方法は、前述の如く、種々の弊害
がある。例えば、焼却炉内の冷却作用を起し、乾燥速度
の低下、燃焼速度の低下による燃焼時間の長時間化、又
は燃料の増加等を招来する。殊に、不完全燃焼による排
カ゛ス及び/又はタ゛イオキシン等の有害物質発生の危険性があ
る。
Conventionally, the method of putting garbage directly into an incinerator has various disadvantages as described above. For example, a cooling action in the incinerator is caused to cause a decrease in drying rate, a prolonged combustion time due to a decrease in combustion rate, or an increase in fuel. In particular, there is a risk of harmful substances such as exhaust gas and / or dioxin due to incomplete combustion.

【0006】また従来のヒ゜ット及びクレーンを用いた方式の焼
却施設は、ヒ゜ットに貯溜されたごみの上方からクレーンにて掴
み出す構成である。従って、上方のごみは頻繁に投入及
び排出される一方、下方のごみがいつまでも残る。殊
に、生ごみの場合は、下方に残留したものが腐敗し易
く、また悪臭の程度も酷く、大きな問題となっている。
更にヒ゜ットの開口部が比較的広大であるため、悪臭が外部
に漏れ易いことも問題である。
[0006] A conventional incineration facility using a pet and a crane has a configuration in which the waste stored in the pet is picked up by a crane from above. Thus, the upper refuse is frequently input and discharged, while the lower refuse remains forever. In particular, in the case of garbage, what remains below is liable to rot, and the degree of odor is severe, which is a major problem.
Further, since the opening of the pet is relatively large, it is also a problem that a bad smell is likely to leak to the outside.

【0007】また前述の文献(1)及び(2)は、ヒ゜ットの悪臭
を封じ込める構成であるものの、大型ヒ゜ットとクレーンを用い
た方式は従来と同じであり、下方に残留するごみの腐敗
に対する配慮がされておらず、悪臭対策が十分でない。
文献(3)は、ヒ゜ットの深さを浅くすることを特徴とするも
のの、クレーンを用いた方式は従来と同じであり、下方に残
留するごみの腐敗に対する配慮がされておらず、悪臭対
策が十分でない。
In the above-mentioned documents (1) and (2), although the configuration is such that the bad smell of the pet is contained, the method using a large pet and a crane is the same as the conventional one, and consideration is given to the decay of the garbage remaining below. No odor measures are taken.
Document (3) is characterized in that the depth of the jet is made shallow, but the method using a crane is the same as before, and no consideration is given to the decay of the garbage remaining below, and odor control measures are not taken. not enough.

【0008】更に前記文献(1) 及び(2)は、ヒ゜ットのごみ
を、搬送クレーン等の手段を利用して、直接焼却炉に供給す
る構成であり、前述の如く、多量の水分を含んだ湿潤生
ごみを、焼却処分することから、同様な課題がある。
Further, the above-mentioned documents (1) and (2) have a configuration in which the waste of a pet is directly supplied to an incinerator using means such as a transfer crane, and as described above, contains a large amount of water. There is a similar problem from incinerating wet garbage.

【0009】[0009]

【課題を解決するための手段】請求項1の発明は、従来
の生ごみを、直接焼却炉に投入する方式を取りやめ、乾
燥、粉細したごみを焼却炉に供給し、焼却炉の燃焼速度
の向上、完全燃焼による排カ゛ス及び/又はタ゛イオキシン等の有
害物質発生、焼却場の悪臭防止、又は職場環境の向上等
を図る。また従来のヒ゜ット貯溜方法と、クレーン搬送方法とを
用いた方式を取りやめ、投入されたごみ袋を受けコンヘ゛ヤ
にて直送して即時処理することにより、ごみの下方への
残留をなくし、悪臭の発散防止と、開口部を小さくして
受けコンヘ゛ヤの負担を軽減する。またヒ゜ットを小型に構成し
て設備費の低減、建設の容易化、設備内の敷地の有効利
用を図る。尚、環境省構造基準による3日分の乾燥、固
形ごみ(粉細RDF)を、貯溜層に蓄えて処理し、迅速かつ
確実に生ごみ処理を図る。
Means for Solving the Problems The invention of claim 1 is to cancel the conventional method of directly putting garbage into an incinerator, supply dried and finely divided garbage to the incinerator, and reduce the burning rate of the incinerator. Of waste, harmful substances such as dioxin, etc. due to complete combustion, prevention of offensive odor in incineration plants, and improvement of work environment. In addition, the conventional method of storing the pets and the method of transporting the crane were abolished, and the input garbage bags were sent directly to the conveyor for immediate processing, eliminating garbage remaining below and releasing odors. Prevention and reducing the opening to reduce the load on the receiving conveyor. In addition, the unit is designed to be small in size to reduce equipment costs, facilitate construction, and effectively use the site within the equipment. In addition, dry and solid waste (fine RDF) for three days according to the Ministry of the Environment's structural standards will be stored in a storage tank and processed to achieve quick and reliable disposal of food waste.

【0010】請求項1は、廃棄物、生ごみ等を収容した
ごみ袋投入用のハ゛ンカーと、このハ゛ンカー内に設けたごみ袋搬
送用のコンヘ゛ヤと、前記ごみ袋の破袋及びごみをほぐす破
袋機と、このほぐしたごみを荒破砕する破砕機と、この
荒破砕されたごみを乾燥する乾燥機と、乾燥ごみを選別
する選別機と、選別ごみを粉細する粉細機と、この粉細
機で生成された粉細ごみを風送手段及び定量供給器を利
用して焼却炉に送り、この焼却炉で燃焼するごみ処理シス
テムであって、前記ハ゛ンカーに投入されたごみ袋は、コンヘ゛ヤに
受けとめられた後、このコンヘ゛ヤを利用して破袋機に送
り、破砕したごみを乾燥機、選別機、及び粉細機に送
り、粉細乾燥したごみを少なくとも3日分収容できる貯
留槽を経由して焼却炉に送り、前記ごみ袋のごみを遅滞
なく処理可能とするごみ処理システムである。
[0010] The first aspect of the present invention is a tanker for putting in garbage bags containing waste, garbage, etc., a conveyor for garbage bags provided in the bunker, a crushing bag for the garbage bags and a crushing device for loosening the garbage. A bag machine, a crusher that roughly crushes the loosened garbage, a dryer that dries the roughly crushed garbage, a separator that sorts the dried garbage, and a finer that grinds the sorted garbage, A refuse treatment system in which the fine refuse generated by the finer is sent to an incinerator using an air blowing means and a quantitative feeder, and burned in the incinerator, wherein the garbage bag put into the handker is: After being received by the conveyor, it is sent to a bag breaker using this conveyor, and the crushed garbage is sent to a dryer, a sorter, and a finer, and a storage tank that can hold the finely dried garbage for at least three days. To the incinerator via the Only a waste treatment system that can be processed without delay.

【0011】請求項2の発明は、生ごみの乾燥を効率的
に行うこと、又は省燃料化を達成すること、等を意図す
る。
The invention of claim 2 intends to efficiently dry garbage or achieve fuel saving.

【0012】請求項2は、乾燥機を、この乾燥機に設け
た多数の熱風供給口と、1本又は複数本の筒状のスクリュー本
体と、このスクリュー本体の周面に設けたスクリューと、このスクリュ
ー本体の下方に設けたトラフと、このトラフに開設した多数の
孔とで構成し、このスクリューで搬送しながら、前記トラフの孔
からごみに向かってエアを吹出して乾燥する構成の請求項
1に記載のごみ処理システムである。
[0012] Claim 2 includes a dryer, a plurality of hot air supply ports provided in the dryer, one or a plurality of cylindrical screw bodies, and a screw provided on a peripheral surface of the screw body. A trough provided below the screw body and a number of holes formed in the trough, and air is blown out from the holes of the trough toward dust while being conveyed by the screw, and is dried.
1 is a refuse disposal system.

【0013】[0013]

【発明の実施の形態】本発明はごみ袋を投入するハ゛ンカー
を、従来のものより小型に構成し、例えば、図1の如
く、トラック1〜2台分のごみが収容できる程度とする。これ
により、1度に投入されるごみの量を少なく抑えるとと
もに、受けコンヘ゛ヤにてごみ袋を直送して即時処理する。
従って、下方のごみがいつまでも残って腐敗するという
虞がなく、常にハ゛ンカー内のごみのほとんどを入れ替える
ことができる。またハ゛ンカーの開口部が小さく(狭く)、悪
臭が外部に漏れにくくなっている。
DESCRIPTION OF THE PREFERRED EMBODIMENTS According to the present invention, a hopper for charging garbage bags is made smaller than a conventional one, and for example, as shown in FIG. As a result, the amount of garbage to be thrown in at a time is reduced, and the garbage bags are directly sent to the receiving conveyer for immediate processing.
Therefore, there is no danger that the lower refuse will remain and rot, and most of the refuse in the tanker can be replaced at all times. In addition, the opening of the bunker is small (narrow), so that the odor does not easily leak to the outside.

【0014】受けコンヘ゛ヤにてごみラインに直送されたごみ袋
は、その後、破袋、ごみの破砕、磁選、乾燥、選別とRD
F(Refuse Derived Fuel)のラインに準ずる工程に進み、更
に一次粉細、二次粉細と粉細し、粉細乾燥ごみを、貯塵
ヒ゜ット(ごみ3日分収容)がないことのリスクを補うため、貯溜
槽(3日分、見かけ比重0.55)に、一時的に貯溜する。こ
の貯溜後、焼却炉に噴射供給して燃焼する。尚、乾燥、
粉細後に、RDF粉体又は固形RDFとして、この粉細RDFを
燃焼し(RDF低位発熱量4,500〔kcal/kg〕)、給湯、発電ホ
゛イラー、焼却灰熔解等用の熱源として利用することも可能
である。
[0014] The garbage bags sent directly to the garbage line at the receiving con- tainer are then subjected to bag breakage, crushing of garbage, magnetic separation, drying, sorting and RD.
Proceed to a process similar to the F (Refuse Derived Fuel) line, further pulverize into primary and secondary fines, and reduce the risk of no fine dust and dry storage dust (for three days of waste). Temporarily store in a storage tank (for 3 days, apparent specific gravity 0.55) to supplement. After this storage, the fuel is injected and supplied to the incinerator for combustion. In addition, drying,
After fine grinding, as a RDF powder or solid RDF, this fine RDF is burned (RDF lower calorific value 4,500 [kcal / kg]) and can be used as a heat source for hot water supply, power generation boilers, incineration ash melting, etc. It is.

【0015】本発明では、乾燥機も特徴がある。即ち、
本発明は、多段式縦型の乾燥機を採用する。理由は、従
来の乾燥機は横型ロータリート゛ライヤー式が多いが、効率が悪い
ためである。そこで、本発明の乾燥機の具体例を説明す
ると、縦型多段式の乾燥機内に、碗形形状のトラフ及び多
数本のスクリュー本体を多段式に設け、このスクリュー本体を回転
することで、スクリュー本体に設けたスクリューが回転する。この
スクリューの回転で、トラフ内の生ごみを撹拌しつつ、このスクリュ
ー本体の長手方向に移動する。この移動の過程で、乾燥
機内に導入された熱風(エア)を、スクリュー本体の下方に設け
たトラフに開設した多数の孔よりエアを吹出して乾燥を行
う。この際、乾燥機の熱風は、焼却炉の熱風を利用し、
効率的に乾燥し、かつ省資源に役立てる。この熱風は、
トラフの下側から吹出された後、新しい熱風とともに、順
次上方のトラフの孔へと導かれて、効率的に乾燥される。
尚、荒破砕ごみ及び乾燥途中の荒破砕ごみは、多数本の
スクリュー本体間を迂回するように運ばれることで、略完全
に乾燥される。
In the present invention, a dryer is also characterized. That is,
The present invention employs a multi-stage vertical dryer. The reason is that conventional dryers are often of a horizontal rotary trailer type, but are inefficient. Therefore, a specific example of the dryer of the present invention will be described.In a vertical multi-stage dryer, a bowl-shaped trough and a large number of screw bodies are provided in a multi-stage manner, and by rotating this screw body, the screw is rotated. The screw provided on the main body rotates. With the rotation of the screw, the garbage in the trough is moved in the longitudinal direction of the screw body while being stirred. During this movement, hot air (air) introduced into the dryer is blown out from a number of holes formed in a trough provided below the screw body to perform drying. At this time, the hot air of the dryer uses the hot air of the incinerator,
Dry efficiently and save resources. This hot air
After being blown out from the lower side of the trough, it is successively guided to the upper trough hole with fresh hot air, and is efficiently dried.
In addition, the roughly crushed refuse and the roughly crushed refuse in the middle of drying are almost completely dried by being transported so as to bypass between a number of screw bodies.

【0016】[0016]

【実施例】以下、本発明の好ましい一実施例を、図面を
参照して説明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, a preferred embodiment of the present invention will be described with reference to the drawings.

【0017】1は持込まれたごみ袋を投入するハ゛ンカーであ
り、このハ゛ンカー1には受けコンヘ゛ヤ2が設けられる。このハ゛ンカ
ー1に投入されたごみ袋は受けコンヘ゛ヤ2によって、順次、か
つ速やかにごみラインに搬送される。従って、ハ゛ンカー1内の
何れにも、ごみ袋又はごみが滞留しない。尚、このハ゛ンカ
ー1の開口部100を狭くして、ごみ袋の大量の投入防止、
及び貯溜をなくすこと、並びに悪臭の拡散防止等を図
る。
Reference numeral 1 denotes a tanker for throwing in a garbage bag brought in. The tanker 1 is provided with a receiving conveyer 2. The garbage bags put into the tanker 1 are sequentially and promptly conveyed to the garbage line by the receiving conveyer 2. Therefore, no garbage bag or garbage stays in any of the bunker 1. In addition, by narrowing the opening 100 of the bunker 1, a large amount of garbage bags can be prevented,
And to eliminate storage and prevent the spread of bad odors.

【0018】ごみは破袋機3で破袋された後、磁選機4に
より、金属と非金属に分別する。分別された非金属のご
みは、破砕機5で荒破砕される。尚、磁選機4は必要によ
り、適所に設ける。そして、乾燥機6で乾燥し、選別機7
で選別し、第一次・第二次粉細機8、9により所定の寸法
に粉細する。この粉細ごみは貯溜槽10に一時貯溜され
る。尚、ハ゛ンカー1及び/又は破袋機3により発生する悪臭
(異臭)は、脱臭装置18(熱酸化方式)で脱臭された後、排
気筒16に導かれて大気中に拡散される。また汚水は、汚
水槽20で貯溜した後、後述の焼却炉で蒸気に変換し、悪
臭を解消する。
After the garbage is broken by the bag breaker 3, the garbage is separated by the magnetic separator 4 into metal and non-metal. The separated nonmetallic waste is roughly crushed by the crusher 5. In addition, the magnetic separator 4 is provided in an appropriate place as needed. Then, it is dried in the dryer 6 and the sorting machine 7
And then pulverize to predetermined dimensions by primary and secondary mills 8 and 9. This fine dust is temporarily stored in the storage tank 10. The odor generated by the bunker 1 and / or the bag breaking machine 3
The (odor) is deodorized by the deodorizing device 18 (thermal oxidation method), and then guided to the exhaust stack 16 and diffused into the atmosphere. Further, the sewage is stored in the sewage tank 20 and then converted into steam in an incinerator described later to eliminate odor.

【0019】上記乾燥機6の構成は、縦型多段式とし、
乾燥機6の適所に熱風供給口60を設ける。この乾燥機6に
は、1本又は複数本のスクリュー本体61を配置して、スクリュー本
体61の回転でスクリュー610を回転する。またスクリュー本体61の
下方にトラフ62を設け、このトラフ62に多数の孔620を開設す
る。従って、熱風供給口60より導入された熱風は、乾燥
機6内より、孔620を介して荒破砕ごみに向かって吹出さ
れる構成である。尚、荒破砕ごみ又は乾燥途中の荒破砕
ごみは、多数本のトラフ62及びスクリュー本体61間を迂回する。
The structure of the dryer 6 is a vertical multi-stage type,
A hot air supply port 60 is provided at an appropriate position of the dryer 6. One or a plurality of screw bodies 61 are arranged in the dryer 6, and the screw 610 is rotated by the rotation of the screw body 61. A trough 62 is provided below the screw main body 61, and a number of holes 620 are formed in the trough 62. Therefore, the hot air introduced from the hot air supply port 60 is blown out of the dryer 6 through the holes 620 toward the roughly crushed waste. It should be noted that the roughly crushed refuse or the roughly crushed refuse in the course of drying is bypassed between the many troughs 62 and the screw main body 61.

【0020】貯溜槽10内の粉細ごみは焼却炉11に投入さ
れて燃焼され、燃焼カ゛スは調温機12を経由してカ゛ス冷却室
13にて冷却され、集塵機14にて清澄される。その後、誘
引排風機15等によって排気筒16に導かれて大気中に拡散
される。また焼却炉11の着火時は、補助オイルハ゛ーナーにて焼
却炉11を加熱し、粉細RDFの着火を可能とする。図中17
はオイルタンクを示す。
The fine dust in the storage tank 10 is put into an incinerator 11 and burned, and the combustion gas passes through a temperature controller 12 to a gas cooling chamber.
Cooled in 13 and clarified in dust collector 14. Thereafter, the air is guided to the exhaust stack 16 by the induced exhaust fan 15 and diffused into the atmosphere. When the incinerator 11 is ignited, the incinerator 11 is heated by an auxiliary oil heater to enable the ignition of the fine RDF. In the figure 17
Indicates an oil tank.

【0021】以下、前記の各構成を詳細に説明する。Hereinafter, each of the above components will be described in detail.

【0022】(1) ハ゛ンカー1は、鋼板等造りとし、例えば、
トラック1〜2台分の容積とする。
(1) The bunker 1 is made of steel plate or the like.
The volume is equivalent to one or two trucks.

【0023】(2) 受けコンヘ゛ヤ2は、鋼製とし破袋機3まで
の搬送コンヘ゛ヤで定量供給し、その中間に念のため磁選機4
を備え鉄粉又は金属(鉄分)を除去する。
(2) The receiving conveyor 2 is made of steel and is supplied in a fixed amount by a conveyor to the bag-breaking machine 3.
To remove iron powder or metal (iron).

【0024】(3) 破砕機5は、大きさを先ず20m/m〜50m/
m程度の大きさに荒破砕(油圧式)する。
(3) The crusher 5 first has a size of 20 m / m to 50 m / m
Rough crushing (hydraulic) to a size of about m.

【0025】(4) 乾燥機6の構成は、多段式縦型とす
る。理由は、ごみに水分が残るので、従来の横型ロータリート
゛ライヤー式では、効率が悪く、かつ処理時間を要する故で
ある。乾燥機6は、数箇所の熱風供給口60からの熱風
を、ハ゜ンチンク゛メタルトラフ62の孔620より荒破砕ごみに向かって
吹出して乾燥する構成である。尚、荒破砕ごみ等は、複
並列のスクリュー本体61のスクリュー610で撹拌しながら、順次下
の同型式のトラフ62及びスクリュー本体61に落下せしめる。この
トラフ62及びスクリュー本体61の段数は3〜4段位が適当であり、
例えば、荒破砕ごみ等を迂回し、確実かつ効率的に乾燥
する。
(4) The configuration of the dryer 6 is a multi-stage vertical type. The reason is that water remains in the refuse, so that the conventional horizontal rotary trailer type is inefficient and requires a long processing time. The dryer 6 has a configuration in which hot air from several hot air supply ports 60 is blown out from holes 620 of a punching metal trough 62 toward rough crushed debris and dried. The crushed refuse and the like are sequentially dropped into the trough 62 and the screw body 61 of the same type below while being stirred by the screws 610 of the multiple parallel screw bodies 61. The number of stages of the trough 62 and the screw body 61 is suitably about 3 to 4 stages,
For example, it circumvents crushed refuse and the like, and ensures reliable and efficient drying.

【0026】(5) 選別機7は、残留する鉄分、カ゛ラス、又
は無機物性不燃物の除去を目的とする比重空選式を採用
する。
(5) The sorter 7 employs a specific gravity selection method for removing residual iron, glass, or inorganic incombustibles.

【0027】(6) 第一次粉細機8は、回転刃式又はスクリュー
式にて、例えば、3m/m〜6m/mに粉細するが、その際、粉
細ごみ等が摩擦熱で粉細刃に熔融付着し効率の悪化が見
られるので、例えば、噴霧冷却水を噴射しこれを防止す
る。尚、後述する第二次粉細機9への移送は風送FANを装
着する。
(6) The primary fine powder mill 8 uses a rotary blade type or a screw type, for example, to reduce the powder to 3 m / m to 6 m / m. For example, spray cooling water is sprayed to prevent the deterioration because the efficiency is deteriorated due to the melt adhesion to the fine blade. In addition, the transfer to the below-mentioned secondary fine-grain machine 9 is equipped with a wind fan.

【0028】(7) 第二次粉細機9は、例えば、500μ以下
程度(ちなみに火力発電所の粉炭は70μである)に粉細し
て貯溜槽10に風送する。
(7) The secondary fine-powder 9 pulverizes the powder to a size of, for example, about 500 μm or less (powder of a thermal power plant is 70 μm) and sends it to the storage tank 10 by air.

【0029】(8) 貯溜槽10は、容積を3日分として下方
より複数の併列スクリューコンヘ゛ヤにて排出するが、フ゛リッチ防止
のため外部ケーシンク゛は、上下断面積を同面積のフラットとす
る。尚、粉細ごみは、送風機による風送とする。
(8) The storage tank 10 is discharged for three days from below with a plurality of parallel screw conveyors. The external casing has a flat upper and lower cross-sectional area of the same area to prevent flitching. In addition, fine dust shall be blown by a blower.

【0030】(9)焼却炉11は、噴射ハ゛ーナー式燃焼装置を利
用する。そして、この焼却炉11より排出した排カ゛スは念
のため略150℃にカ゛ス冷却室13で噴霧水にて冷却し、HC
I、タ゛イオキシン排出防止のため活性炭と消石灰等の手段を利
用して濃度制御した上で、噴射し集塵機14に送風する。
(9) The incinerator 11 uses an injection-type burner type combustion device. The exhaust gas discharged from the incinerator 11 is cooled to approximately 150 ° C. by spray water in the gas cooling chamber 13 just in case,
I. In order to prevent dioxin emission, the concentration is controlled using activated carbon and slaked lime.

【0031】(10) この集塵機14は、ハ゛ク゛フィルター式とし、
この集塵機14で生成された集塵タ゛ストは、図示しない熔融
炉に導入して、熔融するか、又は20m/m〜30m/m程度(一
例である)に固化するか等の方法を採用する。
(10) The dust collector 14 is of a vacuum filter type,
The dust collector generated by the dust collector 14 is introduced into a melting furnace (not shown) to be melted or solidified to about 20 m / m to 30 m / m (an example).

【0032】[0032]

【発明の効果】請求項1の発明は、ごみ袋を投入するハ゛ン
カーと、投入されたごみ袋を搬送するコンヘ゛ヤと、ごみ袋の
破袋機、磁選機、ごみの乾燥機、選別機、粉細機等から
なるごみラインとで構成されるごみ処理システムであって、貯
溜ハ゛ンカーを小型に形成し、投入されたごみ袋をコンヘ゛ヤにて
ごみラインに直送して処理し、RDF手法と粉細燃焼との相乗
効果を利用してタ゛イオキシン発生抑制(完全燃焼)を図ること
特徴とする。従って、従来の生ごみを、直接焼却炉に投
入する方式を取りやめ、乾燥、粉砕したごみを焼却炉に
供給し、焼却炉の燃焼速度の向上、完全燃焼による排カ゛
ス及び/又はタ゛イオキシン等の有害物質発生、焼却場の悪臭防
止、又は職場環境の向上等を図る。また従来のヒ゜ット貯溜
方法と、クレーン搬送方法とを用いた方式を取りやめ、投入
されたごみ袋をコンヘ゛ヤにて直送して即時処理することに
より、ごみの下方への残留がなく、悪臭の発散を防止で
きること、開口部を小さくでき、コンヘ゛ヤエリアの負担を軽減
できること、またハ゛ンカーを小型に構成して設備費の低
減、建設の容易化等が図れること、等の効果がある。
According to the first aspect of the present invention, there is provided a tanker for charging a garbage bag, a conveyor for transporting the garbage bag, a garbage bag breaking machine, a magnetic separator, a garbage dryer, a sorter, and a powder. This is a refuse treatment system composed of a refuse line consisting of thin machines and the like.The storage tanker is formed in a small size, and the garbage bags are sent directly to the refuse line by a conveyer for processing. It is characterized in that dioxin generation is suppressed (complete combustion) by utilizing the synergistic effect with combustion. Therefore, the conventional method of directly putting garbage into the incinerator has been abolished, and dried and pulverized garbage has been supplied to the incinerator to increase the burning rate of the incinerator, to reduce the amount of waste generated by complete combustion and / or toxinous substances such as dioxin. Prevent the generation and odor of incineration plants, or improve the work environment. In addition, the conventional method of storing the pets and the method of transporting the crane were abolished, and the input garbage bags were sent directly to the conveyor and immediately processed, so that no garbage remained below the garbage and the odor was released. This has the following effects: prevention of damage, reduction of the opening, and reduction of the burden on the conveyer area, and reduction of equipment costs and simplification of construction due to the compact size of the bunker.

【0033】請求項2の発明は、乾燥機を、乾燥機に設
けた多数の熱風供給口と、1本又は複数本の筒状のスクリュー
本体と、スクリュー本体の周面に設けたスクリューと、スクリュー本体
の下方に設けたトラフと、トラフに開設した多数の孔とで構成
し、スクリューで搬送しながら、トラフの孔からごみに向かって
エアを吹出して乾燥するごみ処理システムである。従って、水
分の多い生ごみ等のごみの場合に、水分を速やかに除去
できること、効率的な乾燥が図れること、等の効果を生
ずる。
The invention according to claim 2 is characterized in that the dryer comprises: a plurality of hot air supply ports provided in the dryer; one or a plurality of cylindrical screw bodies; and a screw provided on a peripheral surface of the screw body. This is a refuse treatment system that consists of a trough provided below a screw body and a number of holes formed in the trough, and air is blown out from the holes of the trough toward refuse while being conveyed by a screw and dried. Therefore, in the case of garbage such as garbage having a large amount of water, effects such as rapid removal of water and efficient drying can be achieved.

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

【図1】本発明のごみ処理システム全体の構成図である。FIG. 1 is a configuration diagram of an entire refuse disposal system of the present invention.

【図2】乾燥機のスクリューを示す一部欠截の拡大斜視図であ
る。
FIG. 2 is an enlarged perspective view of the screw of the dryer, partially cut away.

【符号の説明】[Explanation of symbols]

1 ハ゛ンカー 100 開口部 2 受けコンヘ゛ヤ 3 破袋機 4 磁選機 5 破砕機 6 乾燥機 60 熱風供給口 61 スクリュー本体 610 スクリュー 62 トラフ 620 孔 7 選別機 8 第一次粉細機 9 第二次粉細機 10 貯溜槽 11 焼却炉 12 調温機 13 カ゛ス冷却室 14 集塵機 15 誘引排風機 16 排気筒 17 オイルタンク 18 脱臭装置 20 汚水槽 1 Handker 100 Opening 2 Receiving conveyor 3 Bag breaker 4 Magnetic separator 5 Crusher 6 Dryer 60 Hot air supply 61 Screw body 610 Screw 62 Trough 620 holes 7 Sorter 8 Primary mill 9 Secondary mill Machine 10 Storage tank 11 Incinerator 12 Temperature controller 13 Gas cooling room 14 Dust collector 15 Induced exhaust fan 16 Exhaust stack 17 Oil tank 18 Deodorizer 20 Sewage tank

フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) B09B 3/00 B65F 5/00 101 4D067 ZAB F23G 5/02 E 5/00 5/033 A B65F 5/00 101 B F23G 5/02 C 5/033 5/04 E 5/44 B B09B 3/00 303J 5/04 ZAB 5/44 303M 5/00 P M Fターム(参考) 3E025 AA02 CA01 CA02 CA04 CA11 CA12 DC01 DE03 3K065 AA18 AB01 AC01 CA01 CA02 CA14 4D004 AA03 AA46 AB01 AC05 CA04 CA08 CA09 CA28 CA42 CB05 CB13 CB36 CB46 CB47 DA03 DA20 4D021 FA12 GA11 HA01 HA10 4D065 CA05 CC01 EB15 ED45 4D067 DD02 DD07 DD11 DD12 DD19 EE27 GA17 GB07 Continuation of the front page (51) Int.Cl. 7 Identification symbol FI Theme coat II (reference) B09B 3/00 B65F 5/00 101 4D067 ZAB F23G 5/02 E 5/00 5/033 A B65F 5/00 101B F23G 5/02 C 5/033 5/04 E 5/44 B B09B 3/00 303J 5/04 ZAB 5/44 303M 5/00 PM term (reference) 3E025 AA02 CA01 CA02 CA04 CA11 CA12 DC01 DE03 3K065 AA18 AB01 AC01 CA01 CA02 CA14 4D004 AA03 AA46 AB01 AC05 CA04 CA08 CA09 CA28 CA42 CB05 CB13 CB36 CB46 CB47 DA03 DA20 4D021 FA12 GA11 HA01 HA10 4D065 CA05 CC01 EB15 ED45 4D067 DD02 DD07 DD11 DD12 DD19 EE27 GA17 GB07

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 廃棄物、生ごみ等を収容したごみ袋投入
用のハ゛ンカーと、このハ゛ンカー内に設けたごみ袋搬送用のコンヘ゛
ヤと、前記ごみ袋の破袋及びごみをほぐす破袋機と、こ
のほぐしたごみを荒破砕する破砕機と、この荒破砕され
たごみを乾燥する乾燥機と、乾燥ごみを選別する選別機
と、選別ごみを粉細する粉細機と、この粉細機で生成さ
れた粉細ごみを風送手段及び定量供給器を利用して焼却
炉に送り、この焼却炉で燃焼するごみ処理システムであっ
て、 前記ハ゛ンカーに投入されたごみ袋は、コンヘ゛ヤに受けとめられ
た後、このコンヘ゛ヤを利用して破袋機に送り、破砕したご
みを乾燥機、選別機、及び粉細機に送り、粉砕乾燥した
ごみを貯留槽を経由して焼却炉に送り、前記ごみ袋のご
みを遅滞なく処理可能とするごみ処理システム。
1. A garbage bag for storing waste, garbage and the like, a garbage bag input container, a garbage bag conveying conveyor provided in the garbage bag, a garbage bag breaking machine and a garbage breaking machine. A crusher for roughly crushing the loosened garbage, a dryer for drying the roughly crushed garbage, a sorting machine for separating the dried garbage, a finer for grinding the sorted garbage, and the finer Is a refuse treatment system in which the fine refuse generated in the above is sent to an incinerator using an air blowing means and a quantitative feeder, and is burned in the incinerator. The garbage bags put into the tanker are received by a conveyor. After being sent, the conveyer is used to send it to a bag breaker, the crushed refuse is sent to a dryer, a sorter, and a finer, and the crushed and dried refuse is sent to an incinerator via a storage tank. Garbage can be processed without delay in garbage bags System.
【請求項2】 上記の乾燥機を、この乾燥機に設けた多
数の熱風供給口と、1本又は複数本の筒状のスクリュー本体
と、このスクリュー本体の周面に設けたスクリューと、このスクリュー
本体の下方に設けたトラフと、このトラフに開設した多数の孔
とで構成し、このスクリューで搬送しながら、前記トラフの孔か
らごみに向かってエアを吹出して乾燥する構成の請求項1
に記載のごみ処理システム。
2. The dryer, comprising: a plurality of hot air supply ports provided in the dryer; one or a plurality of cylindrical screw bodies; a screw provided on a peripheral surface of the screw body; A structure comprising a trough provided below a screw main body, and a number of holes formed in the trough, and drying by blowing air from the holes of the trough toward garbage while conveying with the screw.
Waste treatment system described in 1.
JP2001105647A 2001-04-04 2001-04-04 Waste treatment system Expired - Fee Related JP4750962B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Application Number Priority Date Filing Date Title
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JP4750962B2 JP4750962B2 (en) 2011-08-17

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Country Status (1)

Country Link
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JP2007070115A (en) * 2006-04-25 2007-03-22 Yoshihisa Shimada Garbage collection and storage apparatus, garbage collection vehicle equipped with the apparatus, garbage disposal method and garbage processing system using the vehicle, and garbage collection method using the disposal method
JP4729430B2 (en) * 2006-04-25 2011-07-20 好久 島田 Garbage disposal system, garbage collection vehicle used therefor, and garbage disposal method using the system
CN102319676A (en) * 2011-06-21 2012-01-18 朱海生 Bag-breaking and sorting integrated equipment for municipal domestic waste
CN103480637A (en) * 2012-06-12 2014-01-01 安徽厚源正位环保科技有限公司 Technical method for processing domestic waste
CN103480637B (en) * 2012-06-12 2016-03-02 安徽厚源正位环保科技有限公司 A kind of process processing house refuse
CN102688855A (en) * 2012-06-14 2012-09-26 长沙中联重科环卫机械有限公司 Pendulum harrow device, sorting mechanism and sorting machine
CN102688849A (en) * 2012-06-14 2012-09-26 长沙中联重科环卫机械有限公司 Sorting machine and sorting mechanism thereof
CN103791502A (en) * 2014-02-21 2014-05-14 温州市华泰工业设备工程有限公司 Pyrolysis gasification harmless incineration technology based on derivative fuels of shoe making waste and device used in method
CN103791502B (en) * 2014-02-21 2016-07-06 温州市华泰工业设备工程有限公司 The harmless burning process of pyrolytic gasification and equipment therefor thereof based on the derivatived fuel of shoemaking garbage
CN106216359A (en) * 2016-08-04 2016-12-14 江苏菲力环保工程有限公司 A kind of reclaiming organic waste device systems
CN108800139A (en) * 2018-05-03 2018-11-13 陕西理工大学 A kind of house refuse full-automation processing system and method
CN109489043A (en) * 2018-12-19 2019-03-19 曲靖云能投新能源发电有限公司 A kind of the rubbish fining pretreatment system and method for garbage incinerating power plant
CN111872075A (en) * 2020-09-01 2020-11-03 璧靛嘲 Environment-friendly and energy-saving garbage treatment method
CN111872076A (en) * 2020-09-01 2020-11-03 璧靛嘲 Harmless treatment method for municipal refuse
CN111872076B (en) * 2020-09-01 2021-05-11 四川同益环境科技集团有限责任公司 Harmless treatment method for municipal refuse
CN111872075B (en) * 2020-09-01 2021-12-03 赵峰 Environment-friendly and energy-saving garbage treatment method
CN112642566A (en) * 2020-12-21 2021-04-13 苏州鸿本生物环保科技有限公司 Garbage pretreatment system
CN113751465A (en) * 2021-09-03 2021-12-07 联迈环境科技(苏州)有限公司 Resource disposal process for construction waste and decoration waste
CN115582272A (en) * 2022-08-22 2023-01-10 余海院 Building rubbish sorting and recycling device
CN116164290A (en) * 2023-02-08 2023-05-26 中节能(象山)环保能源有限公司 Multifunctional air supply system and process of garbage incineration boiler
CN116164290B (en) * 2023-02-08 2023-08-11 中节能(象山)环保能源有限公司 Multifunctional air supply system and process of garbage incineration boiler

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