JPH10129805A - Organic waste recycling vehicle - Google Patents

Organic waste recycling vehicle

Info

Publication number
JPH10129805A
JPH10129805A JP8285239A JP28523996A JPH10129805A JP H10129805 A JPH10129805 A JP H10129805A JP 8285239 A JP8285239 A JP 8285239A JP 28523996 A JP28523996 A JP 28523996A JP H10129805 A JPH10129805 A JP H10129805A
Authority
JP
Japan
Prior art keywords
raw material
gas
screw
organic waste
path
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
JP8285239A
Other languages
Japanese (ja)
Inventor
Kazufumi Atsumizu
和文 温水
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 JP8285239A priority Critical patent/JPH10129805A/en
Publication of JPH10129805A publication Critical patent/JPH10129805A/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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P60/00Technologies relating to agriculture, livestock or agroalimentary industries
    • Y02P60/80Food processing, e.g. use of renewable energies or variable speed drives in handling, conveying or stacking
    • Y02P60/87Re-use of by-products of food processing for fodder production

Landscapes

  • Fodder In General (AREA)
  • Refuse-Collection Vehicles (AREA)
  • Processing Of Solid Wastes (AREA)
  • Crushing And Pulverization Processes (AREA)

Abstract

PROBLEM TO BE SOLVED: To realize a self-propelled recycling device for gathering organic waste and reproducing it and distributing a reproduced produce. SOLUTION: This is a vehicle 1 having a recycling device for dehydration from a raw material such as organic matter or organic waste. The reproduction device comprises a raw material hopper 3 for crushing or kneading the raw material while adjusting the oil rate of the dumped raw material, a carrying passage 4 for receiving the raw material from the raw material hopper 3 and sending it out, a stirring mixing device 6 for packing the raw material received from the carrying passage 4 into a closed passage 5 having heating means or insulation means and for carrying it in one direction and then kicking, stirring or crushing it to the direction nearly orthogonal to the carrying direction to remove water from it, and a gas treating section 7 for treating steam or waste gas discharged from the raw material hopper 3 or the stirring mixing device 6.

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、有機廃棄物である
生ゴミ、塵芥、各種食肉工場から出される屍肉又は汚物
を原料として回収すると共に、これら原料を飼料又は肥
料として利用できる形態へと再生処理する有機廃棄物再
生処理車に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention recovers raw garbage, garbage, and dead meat or filth from various meat factories, which are organic wastes, and converts the raw materials into a form that can be used as feed or fertilizer. The present invention relates to an organic waste recycling vehicle for recycling.

【0002】[0002]

【従来の技術】近年は、生ゴミ、塵芥、各種食肉工場か
ら出される屍肉又は汚物等の有機廃棄物を脱水、粉末化
することで、飼料又は肥料として再生利用する例が広く
見受けられるようになってきている。これは、有機廃棄
物を処分するよりも再生して利用する方が経済的価値が
あることのほか、端的に有機廃棄物に含まれるタンパク
質等の成分が、飼料や肥料に適していることが再認識さ
れたことによる。こうした再生処理においては、原料と
なる有機廃棄物を適度に脱水、脱油する必要があり、古
くは油温脱水処理が知られているが、このほか撹拌混合
機(クッカ又はドライヤーと呼ばれる)において少量の油
で原料を炒める方式(通称「炒め方式」)が用いられる(特
開平7-35477号、特開平7-47254号)。通常、各工場やホ
テル、レストラン等に、前記方式を用いた再生処理設備
が配され、個別に生ゴミや塵芥を処理していた。
2. Description of the Related Art In recent years, it has been widely seen that organic waste such as garbage, garbage, carcasses or filth discharged from various meat factories is dehydrated and powdered to be recycled as feed or fertilizer. It is becoming. This is because it is more economical to recycle and use organic waste than to dispose of it.In addition, the fact that components such as proteins contained in organic waste are suitable for feed and fertilizers Because it was re-recognized. In such a regeneration treatment, it is necessary to appropriately dehydrate and deoil the organic waste as a raw material, and in the old days, oil temperature dehydration treatment is known, but in addition to this, in a stirring mixer (called a cooker or a dryer). A method in which a raw material is fried with a small amount of oil (commonly referred to as “fried method”) is used (Japanese Patent Application Laid-Open Nos. 7-35477 and 7-47254). Usually, each factory, hotel, restaurant, and the like are provided with a reprocessing facility using the above method, and individually treat garbage and garbage.

【0003】[0003]

【発明が解決しようとする課題】有機廃棄物の再生利用
といっても、現実は各工場やホテル、レストランにそれ
ぞれ専用の再生処理設備を設けなければならず、実際に
はまだ多くの工場、ホテル等が再生処理設備をもってい
ないのが現状である。これは、一般の専用の再生処理設
備は大型のものが多く、小さな工場やホテル等から日々
出される生ゴミや塵芥の量に比べて、初期投資が高額
で、また運用コストや維持費も掛かるため、なかなか普
及しないのである。例えば、上記「炒め方式」を例に採る
と、原料である生ゴミの種類を問わずに処理するには、
原料を粉砕するミキサー、原料の油分調整機能を兼ねた
ホッパ、原料の脱水処理をする撹拌混合機、撹拌混合機
から出される油分を含んだ水蒸気を冷却するコンデン
サ、水分と油分とを分離する濾過装置等が必要となり、
各部を小さくしても限界があることから、どうしても設
備全体が大型化せざるを得なかったのである。
[0007] Even in the case of recycling organic waste, in reality, each factory, hotel, and restaurant must be provided with a dedicated recycling processing facility. In practice, many factories, At present, hotels do not have reprocessing facilities. This is because most of the general-purpose reprocessing equipment is large, and the initial investment is high, and the operation and maintenance costs are higher than the amount of garbage and garbage that is discharged daily from small factories and hotels. Therefore, it is not easily spread. For example, taking the above-mentioned “stir-fry method” as an example, in order to treat garbage regardless of the type of raw garbage,
Mixer for crushing raw materials, hopper that also has function of adjusting oil content of raw materials, stirring mixer for dehydrating raw materials, condenser for cooling water vapor containing oil output from stirring mixer, filtration for separating water and oil components Equipment is required,
Even if each part was made smaller, there was a limit, so the entire equipment had to be enlarged.

【0004】有機廃棄物の再生利用を促進させるには、
より多くの工場、ホテル等に設備が設置されるのが好ま
しいのであるが、これは上述のとおり現実的には難し
い。それならば、特定個所に再生処理設備を設け、この
再生処理設備に各所から出される生ゴミや塵芥等を収集
し、一括して処理する方法も考えられる。しかし、この
方法であると、再生処理を終えてできた飼料又は肥料を
改めて輸送しなければ利用できず、原料の収集、製品の
配送といった輸送費がかさんでしまう。
[0004] To promote the recycling of organic waste,
It is preferable that equipment be installed in more factories, hotels, and the like, but this is practically difficult as described above. In that case, a method is also conceivable in which a recycling facility is provided at a specific location, and garbage, trash, and the like discharged from various locations are collected in the recycling facility and processed collectively. However, according to this method, the feed or fertilizer produced after the regeneration treatment cannot be used unless it is transported again, and the transportation cost such as raw material collection and product delivery is increased.

【0005】そこで、各別に専用の再生処理設備を設け
ることのできない比較的小さな工場やホテル等から出さ
れる生ゴミ、塵芥等の有機廃棄物の再生処理を実現する
ために、有機廃棄物の収集、再生処理、製品の配送を担
うことのできる自走式の再生処理設備を実現するため、
「炒め方式」を基本として、車両搭載のために各部の小型
化を図ると共に、各部の連結又は配置について工夫する
ために検討した。
[0005] Therefore, in order to realize the recycling of organic waste such as garbage and garbage discharged from relatively small factories and hotels where it is not possible to provide a dedicated recycling facility, collection of organic waste is performed. In order to realize self-propelled reprocessing equipment that can take charge of reprocessing and product delivery,
Based on the "stir-fry method", we studied to reduce the size of each part for mounting on a vehicle and to devise the connection or arrangement of each part.

【0006】[0006]

【課題を解決するための手段】検討の結果開発したもの
が、有機物又は有機廃棄物等の原料を脱水処理する再生
処理装置を搭載した車両であって、再生処理装置が、投
入した原料の油分調整を図りながら粉砕又は混練する原
料ホッパと、この原料ホッパから原料を受け取り送り出
す移送経路と、移送経路から受け取った原料を加熱手段
又は保温手段を有する密閉経路内に閉じ込めて一方向へ
移送しつつ移送方向の略直角方向へ原料を跳ね上げて撹
拌又は粉砕しながらこの原料を脱水処理する撹拌混合機
と、原料ホッパ又は撹拌混合機から放出される水蒸気及
び廃ガスを処理するガス処理部とからなる有機廃棄物再
生処理車(以下、処理車と略する)である。ホッパにおい
て原料に予熱を加え、水分を取り除く予備処理をしても
よい。
SUMMARY OF THE INVENTION As a result of the study, what has been developed is a vehicle equipped with a reprocessing device for dehydrating a raw material such as organic matter or organic waste, wherein the regenerating device has an oil content of the input raw material. A raw material hopper for pulverizing or kneading while adjusting, a transfer path for receiving and sending the raw material from the raw material hopper, and confining the raw material received from the transfer path in a closed path having a heating means or a heat retaining means and transferring the raw material in one direction. A stirrer-mixer for dewatering the raw material while agitating or pulverizing the raw material by flipping it up in a direction substantially perpendicular to the transfer direction, and a gas processing unit for processing steam and waste gas discharged from the raw material hopper or the stirrer-mixer. Organic waste recycling vehicle (hereinafter abbreviated as a processing vehicle). In the hopper, the raw material may be preheated to perform a pretreatment for removing water.

【0007】移送部は、原料を圧縮しながら移送する送
りスクリューであって、スクリュー入口からスクリュー
出口へ至る経路にピッチを徐々に狭めていくスクリュー
と、前記スクリュー出口近傍には前記スクリューを省い
てカッタを取り付け、スクリュー出口に圧縮した原料を
細長く押し出すオリフィス状の多孔板を配した構成とす
る。また、撹拌混合機は、一定長の密閉経路を複数連結
して長尺の処理経路を構成してなり、各密閉経路は撹拌
機入口から撹拌機出口へ向けて登り勾配を有するように
する。
The transfer section is a feed screw for transferring the raw material while compressing it. The screw gradually narrows the pitch in a path from the screw inlet to the screw outlet, and the screw is omitted near the screw outlet. A cutter is attached, and an orifice-shaped perforated plate that extrudes the compressed raw material into an elongated shape is disposed at the screw outlet. In addition, the stirring mixer has a long processing path formed by connecting a plurality of closed paths of a predetermined length, and each closed path has an ascending gradient from the inlet of the stirrer to the outlet of the stirrer.

【0008】ガス処理部は、(1)水蒸気及び廃ガスを燃
やして燃焼ガスを生成するボイラーであって、燃焼ガス
を大気中へ放出すると共に、この燃焼ガスの一部を原料
ホッパ又は撹拌混合機へ供給し加熱媒体として利用す
る、又は(2)ガス処理部が負圧下の密閉水槽内へ導いた
水蒸気及び廃ガスを冷却により液化するエジェクターで
あって、水蒸気及び廃ガスを水底へ向けて放出し、水槽
内の迂回壁を廻って水面へ向けて上昇させる過程で水蒸
気を液化し、廃ガスから異物を除去する、ものが好まし
い。
The gas processing section (1) is a boiler that burns water vapor and waste gas to generate a combustion gas. The boiler discharges the combustion gas into the atmosphere, and also uses a part of the combustion gas as a raw material hopper or an agitated mixer. (2) an ejector that cools and liquefies steam and waste gas introduced into a closed water tank under negative pressure by the gas processing unit, and uses the steam and waste gas to the bottom of the water. It is preferable that the water vapor is liquefied in the process of discharging and rising toward the water surface around the bypass wall in the water tank to remove foreign matter from waste gas.

【0009】本発明の処理車は、地上設置型の従来の再
生処理設備に比べ、全処理工程を構成する装置の数を少
なくし、車両上の設置スペースに十分な再生処理設備を
構築した点に特徴がある。まず、従来原料を溜めておく
ホッパ、原料の油分調整を図るミキサを、本発明のホッ
パのみで実現する。移送経路は、後工程の脱水処理を効
率よく実施するため、ピッチを狭めたスクリューで油分
調整を終えた原料を圧搾し、カッタ及びオリフィス板で
細かく分断して原料を撹拌混合機へ送り出す。撹拌混合
機は、長い処理経路を得るため、撹拌機入口から撹拌機
出口へ向けて登り勾配とした一定長の密閉経路を複数連
結して長尺の処理経路を構成している。各密閉経路を交
差させるようにすると、前段の撹拌機出口と後段の撹拌
機入口とを略垂下方向に最短で結ぶことができる。
The processing vehicle according to the present invention has a reduced number of devices constituting all the processing steps and a sufficient regeneration processing facility in the installation space on the vehicle, as compared with the conventional ground-based regeneration processing equipment. There is a feature. First, a conventional hopper for storing a raw material and a mixer for adjusting the oil content of the raw material are realized only by the hopper of the present invention. In the transfer path, in order to efficiently carry out the dehydration treatment in the post-process, the raw material whose oil content has been adjusted is squeezed by a screw with a narrow pitch, finely divided by a cutter and an orifice plate, and sent out to a stirring mixer. In order to obtain a long processing path, the stirring and mixing machine forms a long processing path by connecting a plurality of closed paths of a fixed length having an ascending gradient from the stirrer inlet to the stirrer outlet. When the closed paths intersect, the outlet of the former-stage agitator and the inlet of the latter-stage agitator can be connected in the shortest direction in a substantially vertical direction.

【0010】エジェクターからなるガス処理部は、水蒸
気又は廃ガスを液化しながら水槽の水をフィルタとして
異物を除去するもので、従来の排水処理装置に比べ、液
化のためのコンデンサを省略して、装置数の低減に寄与
している。負圧下の密閉水槽は、負圧による低温環境と
水槽内の大量な水がもつ大きな熱容量とにより、水蒸気
及び廃ガスの熱量を奪い、液化を実現する。これによ
り、異物は水面へ浮かび上がるか、水底に沈澱すること
になり、水槽内に設けた迂回壁の先に排水口を設けるこ
とで、異物を水槽内に残して水のみを水槽外へ出すこと
ができる。
[0010] The gas treatment section composed of an ejector removes foreign substances by using water in a water tank as a filter while liquefying steam or waste gas. Compared with a conventional wastewater treatment apparatus, a condenser for liquefaction is omitted. This contributes to a reduction in the number of devices. The closed water tank under negative pressure deprives steam and waste gas of heat and liquefies due to the low temperature environment due to negative pressure and the large heat capacity of a large amount of water in the water tank. As a result, the foreign matter comes to the surface of the water or settles on the bottom of the water. By providing a drain port at the end of the bypass wall provided in the water tank, the foreign matter is left in the water tank and only the water is taken out of the water tank. be able to.

【0011】ボイラーからなるガス処理部は、撹拌混合
機(脱水処理)又はホッパ(予備処理)に必要な加熱媒体と
しての燃焼ガスを供給すると共に、前記撹拌混合機又は
ホッパから出される水蒸気及び廃ガスを前記燃焼ガスに
より燃焼させるもので、従来分離されていた熱源と廃ガ
ス処理設備とを兼ねた装置である。燃焼ガスは、例えば
撹拌混合機又はホッパを加熱するスチームの代用とし
て、断熱ジャケットの空間や直接撹拌混合又はホッパ内
へ導く。
[0011] A gas processing section comprising a boiler supplies a combustion gas as a heating medium necessary for a stirring mixer (dehydration processing) or a hopper (preliminary processing), and also supplies steam and waste discharged from the stirring mixer or hopper. It is a device that burns gas with the combustion gas and combines a heat source and a waste gas treatment facility that have been conventionally separated. The combustion gases are introduced into the space of the heat insulating jacket or directly into the stirring mixer or hopper, for example as a substitute for a stirring mixer or steam for heating the hopper.

【0012】[0012]

【発明の実施の形態】以下、本発明の実施形態につき、
図を参照しながら説明する。図1は本発明の処理車1に
おける各部の積載形態の一例を示す斜視図であり、図2
は主に原料の処理の流れを示す各部の構成図である。図
1に見られるように、本発明の処理車1は、荷台2に原
料ホッパ3、移送経路となる送りスクリュー4、4連装
の密閉経路5,5,5,5からなる撹拌混合機6とガス処
理部7、そして原料ホッパ3及び撹拌混合機6へ加熱媒
体である熱風を供給するボイラー8を積載し、ゴミ回収
車同様に市街地等を廻って原料となる生ゴミ、厨芥等を
回収し、走行中又は所定地点で再生処理を施すようにな
っている。
BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, embodiments of the present invention will be described.
This will be described with reference to the drawings. FIG. 1 is a perspective view showing an example of a loading form of each part in the processing vehicle 1 of the present invention.
3 is a configuration diagram of each section mainly showing a flow of processing of a raw material. As shown in FIG. 1, the processing vehicle 1 of the present invention includes a raw material hopper 3 on a loading platform 2, a feed screw 4 serving as a transfer path, and a stirring mixer 6 including four closed paths 5, 5, 5, 5. A boiler 8 that supplies hot air as a heating medium to the gas processing unit 7, the raw material hopper 3 and the stirring and mixing machine 6 is loaded, and raw garbage and kitchen garbage, etc., which become raw materials, are collected around a city or the like like a garbage truck. The reproduction process is performed during traveling or at a predetermined point.

【0013】原料ホッパ3は、図2に見られるように、
ホッパ入口9とホッパ出口10とを備えた容器11内に2重
構造のリボンスクリュー12を架設した構造となってい
る。リボンスクリュー12には原料切断用の切断刃13を取
り付けてあり、投入された原料を粗砕し、混練すること
ができる。また、ボイラー8(図1参照)から供給される
熱風により、原料中の一定程度以上の水分を蒸散させた
り、必要に応じて油分又は水分を補充して原料中の油分
調整をすることもできる。蒸散した水分はガス処理部7
(図1参照)へ送られる。
The raw material hopper 3 is, as shown in FIG.
A double-structured ribbon screw 12 is provided in a container 11 having a hopper inlet 9 and a hopper outlet 10. A cutting blade 13 for cutting the raw material is attached to the ribbon screw 12, so that the input raw material can be roughly crushed and kneaded. Further, the hot air supplied from the boiler 8 (see FIG. 1) can evaporate a certain amount or more of water in the raw material, or can adjust the oil content in the raw material by replenishing oil or water as needed. . The evaporated water is supplied to the gas treatment unit 7
(See FIG. 1).

【0014】送りスクリュー4は、スクリュー入口14と
スクリュー出口15とを備えた円筒16内に、前半が等ピッ
チ、後半は原料の送り方向にピッチが徐々に狭まってい
くスクリュー軸17を内蔵している。原料はスクリュー軸
17によって圧搾されながら送られ、スクリュー出口15近
傍に配したカッタ18によって一定長さに切断され、更に
オリフィス板19(図3:図2中A−A断面図)からペレッ
ト状に分断されて排出される。このように、油分調整を
終え、混練された原料をペレット状に分断することで、
撹拌混合機6(図1参照)での脱水処理を効率よく実施で
きる。
The feed screw 4 incorporates a screw shaft 17 having a uniform pitch in the first half and a gradually narrowing pitch in the feed direction of the raw material in the second half in a cylinder 16 having a screw inlet 14 and a screw outlet 15. I have. Raw material is screw shaft
It is sent while being squeezed by 17, cut into a certain length by a cutter 18 arranged near the screw outlet 15, and further separated into pellets from an orifice plate 19 (FIG. 3: AA sectional view in FIG. 2) and discharged. Is done. Thus, by adjusting the oil content and kneading the raw material into pellets,
The dewatering process in the stirring mixer 6 (see FIG. 1) can be performed efficiently.

【0015】図4は本例の撹拌混合機6を構成する密閉
経路5の構造を示す原料の送り方向断面図、図5は図4
中B−B断面図である。撹拌混合機6は、図4に見られ
るように、撹拌機入口20と撹拌機出口21とを備えた断面
略小判状(図5参照)の密閉経路5内に、投擲ブロック22
を備えた円盤23を等間隔で取り付けた撹拌軸24を下方に
偏心して内蔵した構造で、熱風を用いた「炒め」処理によ
り原料を脱水処理しながら移送していく。なお、図4
中、実線矢印が熱風、破線矢印が蒸散する水蒸気及び廃
ガス、そして白抜き太矢印が原料の移送方向を表してい
る。
FIG. 4 is a sectional view in the feed direction of the raw material showing the structure of the closed passage 5 constituting the stirring mixer 6 of the present embodiment, and FIG.
It is middle BB sectional drawing. As shown in FIG. 4, the stirring mixer 6 is provided with a throw block 22 in a substantially oval cross section (see FIG. 5) having a stirrer inlet 20 and a stirrer outlet 21.
A stirrer shaft 24 having discs 23 provided at equal intervals and having a built-in structure is eccentrically mounted downward, and the material is transferred while being dehydrated by a "stir-fry" process using hot air. FIG.
The middle and solid arrows indicate hot air, the broken arrows indicate water vapor and waste gas evaporating, and the thick arrows indicate the direction of material transfer.

【0016】図4及び図5に見られるように、投擲ブロ
ック22は撹拌軸24に一体となった円盤23の外周に120度
の間隔をもって3枚ずつ取り付けてあり、それぞれに原
料を撹拌機出口21へ向けて押し出す傾斜面25と原料を原
料の送り直角方向へ跳ね上げる投擲面26とを備え、更に
前記傾斜面25及び投擲面26にわたって原料を裁断刃27を
設けている。この投擲ブロック22は撹拌軸24と共に回転
し、密閉経路5内に閉じ込めた原料を傾斜面25で押しな
がら一方向へ移送しつつ、密閉経路5の内壁面に向けて
投擲面26で原料を跳ね上げ、かつ裁断刃27で原料を切り
分けながら撹拌する。原料は、前記撹拌運動を受けなが
ら熱風により脱水される。原料の投擲方向に当たる密閉
経路5の内壁面には、原料の散乱手段として粉砕刃28を
取り付けている。散乱手段は、このほか原料の送り方向
の軸をもった回転体であってもよい。
As can be seen in FIGS. 4 and 5, three throwing blocks 22 are attached to the outer periphery of a disk 23 integrated with a stirring shaft 24 at intervals of 120 degrees, and the raw materials are respectively supplied to the outlet of the stirrer. An inclined surface 25 for extruding the raw material toward 21 and a throwing surface 26 for jumping up the raw material in a direction perpendicular to the feed direction of the raw material are provided. Further, a cutting blade 27 for cutting the raw material over the inclined surface 25 and the throwing surface 26 is provided. The throw block 22 rotates together with the stirring shaft 24, and pushes the raw material confined in the closed passage 5 in one direction while pushing the raw material on the inclined surface 25, and bounces the raw material toward the inner wall surface of the closed passage 5. Then, the raw material is stirred while being cut by the cutting blade 27. The raw material is dehydrated by hot air while undergoing the stirring movement. A crushing blade 28 is attached to the inner wall surface of the closed path 5 corresponding to the raw material throwing direction as a raw material scattering means. The scattering means may be a rotating body having an axis in the feed direction of the raw material.

【0017】本例の撹拌混合機6は、原料の移送方向に
登り勾配をもった密閉経路5,5,5,5を4連装して脱
水処理に必要な経路長を確保している。加えて、各密閉
経路5が登り勾配をもっているため、投擲ブロック22の
傾斜面25に押される原料は移送方向へ進むものと逆に戻
されるものに分けられ、全体としてゆっくりと時間を掛
けて密閉経路5内を進むことになる。これにより、本例
の撹拌混合機6では、各密閉経路5の合計長に比べて比
較的長い時間を掛けて原料が移送され、十分な脱水処理
を施すことができる。このため、例えば4連装の密閉経
路5,5,5,5のうち、前3連装で脱水処理をし、最後
の密閉経路5においては原料を加熱せず、撹拌により解
しながら冷却するといった後処理もすることができる。
また、本例のように密閉経路5を傾斜させると、装置の
設置面積を低減させることにも役立つ。なお、設置面積
の低減のため、原料を巡回させるループ型の密閉経路か
らなる撹拌混合機を用いてもよい。
The stirring and mixing machine 6 of this embodiment is provided with four closed paths 5, 5, 5, 5 having an ascending gradient in the direction in which the raw materials are transferred, to secure the path length required for the dehydration treatment. In addition, since each closed path 5 has an ascending slope, the raw material pushed on the inclined surface 25 of the throwing block 22 is divided into one that moves in the transfer direction and one that is returned in the reverse direction. The vehicle will travel in route 5. Thereby, in the stirring mixer 6 of the present example, the raw material is transferred over a relatively long time as compared with the total length of each closed path 5, and a sufficient dehydration treatment can be performed. For this reason, for example, of the four closed paths 5, 5, 5, 5, the dehydration process is performed in the first three paths, and in the last closed path 5, the raw material is not heated, but is cooled while being released by stirring. Processing can also be performed.
Further, when the closed path 5 is inclined as in this example, it is useful to reduce the installation area of the apparatus. In addition, in order to reduce the installation area, a stirring mixer having a loop-type closed path for circulating the raw material may be used.

【0018】原料の脱水処理のための熱は、上記熱風を
直接密閉経路5へ吹き込ませるだけでなく、様々な手段
で加えることができる。例えば、図6(図4相当)に見ら
れるように、密閉経路5の外壁面に対して隙間29をもっ
た断熱ジャケット30を被覆して、この隙間29に高温の水
蒸気を流通させて密閉経路5自体を加熱する手段のほ
か、電磁波を用いた加熱手段等を挙げることができる。
The heat for dehydrating the raw material can be applied not only by blowing the hot air directly into the closed passage 5 but also by various means. For example, as shown in FIG. 6 (corresponding to FIG. 4), the outer wall surface of the closed passage 5 is covered with a heat insulating jacket 30 having a gap 29, and high-temperature steam is circulated through the gap 29 to close the closed passage 5. In addition to the means for heating 5 itself, heating means using electromagnetic waves can be used.

【0019】図7はエジェクター32からなるガス処理部
7の断面図、図8はボイラー8を兼ねたガス処理部7の
部分断面図である。荷台2という極めて狭い設置面積の
関係から、地上設置型の設備のような複数の機器からな
るガス処理部は使用できないため、本発明は基本的に単
一の装置構成により水蒸気及び廃ガスを処理する。しか
も、ボイラー8を兼ねたガス処理部7は、水蒸気及び廃
ガスを燃焼して異物を焼却処分すると共に、燃焼ガスを
原料ホッパ3又は撹拌混合機6へ加熱媒体として供給す
ることができ、更に設置スペースを削減することができ
る利点がある。
FIG. 7 is a cross-sectional view of the gas processing section 7 including the ejector 32, and FIG. 8 is a partial cross-sectional view of the gas processing section 7 serving also as the boiler 8. Due to the extremely small installation area of the loading bed 2, a gas processing unit composed of a plurality of devices such as ground-based equipment cannot be used. Therefore, the present invention basically treats steam and waste gas with a single device configuration. I do. Moreover, the gas processing unit 7 serving also as the boiler 8 can burn the steam and the waste gas to incinerate the foreign matter and supply the combustion gas to the raw material hopper 3 or the stirring mixer 6 as a heating medium. There is an advantage that the installation space can be reduced.

【0020】エジェクター32からなるガス処理部7は、
図7に見られるように、負圧下の密閉水槽33内へポンプ
40により駆動するエジェクター32が水蒸気及び廃ガスを
水底に向けて放出し、負圧により低温に維持された密閉
水槽33内の迂回路34を経る過程で液化すると共に、迂回
路34を異物のフィルタとして除去し、液化した水蒸気の
みを排水する。密閉水槽33の負圧は、脇に付設したポン
プ41により駆動する副エジェクター35により密閉水槽33
内の空気を吸引することで実現する。従来、水蒸気及び
廃ガスを液化する場合には、エジェクターからなる液化
装置に加えて冷却を担うコンデンサを用いていたのに対
し、本発明ではエジェクター32を用いた密閉水槽33のみ
で冷却、液化を担う点が異なる。この小さくまとめられ
たガス処理部7は、本発明の処理車の実現に大きく寄与
している。
The gas processing section 7 composed of the ejector 32
As can be seen in FIG. 7, pump into closed water tank 33 under negative pressure.
An ejector 32 driven by 40 discharges water vapor and waste gas toward the bottom of the water, liquefies in a process of passing through a bypass 34 in a closed water tank 33 maintained at a low temperature by negative pressure, and filters the bypass 34 for foreign matter. And only the liquefied steam is drained. The negative pressure of the closed water tank 33 is controlled by a sub-ejector 35 driven by a pump 41 attached to the side.
It is realized by sucking the air inside. Conventionally, when liquefying water vapor and waste gas, a condenser for cooling is used in addition to a liquefaction device including an ejector, whereas in the present invention, cooling and liquefaction are performed only in a closed water tank 33 using an ejector 32. They are different. This small gas processing unit 7 greatly contributes to the realization of the processing vehicle of the present invention.

【0021】ボイラー8を兼ねたガス処理部7は、図8
に見られるように、原料ホッパ3又は撹拌混合機6へ供
給する加熱媒体としての燃焼ガスを生成する際、水蒸気
又は廃ガスを燃やして異物を焼却、除去する。水蒸気及
び廃ガスは、ファン42により強制的にボイラー8の最下
層に送り込まれ、第1フィルタ36を通して大きな異物を
除去し、燃焼室37においてバーナー38により焼却し、更
に第2フィルタ39を通して燃焼ガスの一部をファン43に
より強制的に原料ホッパ3又は撹拌混合機6へ送り出
し、残りを大気中へ排気する。ガス処理部7がボイラー
8を兼ねることにより、更に設置スペースの削減に寄与
することができる。
The gas processing unit 7 also serving as the boiler 8 is provided in FIG.
As can be seen from the above, when generating a combustion gas as a heating medium to be supplied to the raw material hopper 3 or the stirring mixer 6, the steam or the waste gas is burned to incinerate and remove foreign matter. The steam and the waste gas are forcibly sent to the lowermost layer of the boiler 8 by the fan 42, remove large foreign substances through the first filter 36, incinerate by the burner 38 in the combustion chamber 37, and further pass through the second filter 39 to the combustion gas. Is forcibly sent to the raw material hopper 3 or the stirring mixer 6 by the fan 43, and the rest is exhausted to the atmosphere. Since the gas processing unit 7 also serves as the boiler 8, it can further contribute to a reduction in installation space.

【0022】[0022]

【発明の効果】本発明の処理車により、各別に専用の再
生処理設備を設けることのできない比較的小さな工場や
ホテル等から出される生ゴミ、塵芥等の有機廃棄物を回
収し、容易に再生処理を施すことができる。再生した原
料は、肥料や飼料として利用でき、しかも処理車が運搬
手段としても機能するので、コストも抑えることができ
る。将来的には、一般家庭から出される生ゴミの回収を
本発明の処理車で実施して、現在のように回収して焼却
又は埋立処分するだけでなく、回収しながら再生処理を
施し、有益な資源として再利用を図ることで、回収コス
トを低減させることにも貢献できるようになる。
According to the treatment vehicle of the present invention, organic wastes such as garbage and garbage discharged from relatively small factories and hotels, for which a dedicated regeneration treatment facility cannot be separately provided, are collected and easily recycled. Processing can be performed. Recycled raw materials can be used as fertilizer and feed, and the processing vehicle also functions as a transportation means, so that costs can be reduced. In the future, garbage from general households will be collected by the treatment vehicle of the present invention, and not only will it be collected and incinerated or landfilled as it is now, but it will also be useful to perform recycling while collecting it. By reusing it as a valuable resource, it will also be possible to contribute to reducing collection costs.

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

【図1】本発明の処理車における各部の積載形態の一例
を示す斜視図である。
FIG. 1 is a perspective view showing an example of a loading form of each part in a processing vehicle of the present invention.

【図2】同処理車の主に原料の処理の流れを示す各部の
構成図である。
FIG. 2 is a configuration diagram of each part showing a flow of processing of a raw material mainly in the processing vehicle.

【図3】図2中A−A断面図である。FIG. 3 is a sectional view taken along line AA in FIG. 2;

【図4】本例の撹拌混合機の構造を示す原料の送り方向
断面図である。
FIG. 4 is a sectional view in the feed direction of the raw material, showing the structure of the stirring mixer of the present example.

【図5】図4中B−B断面図である。FIG. 5 is a sectional view taken along line BB in FIG. 4;

【図6】密閉経路外壁面に対して断熱ジャケットを被覆
した撹拌混合機の図4相当図である。
FIG. 6 is a diagram corresponding to FIG. 4 of the stirring mixer in which the heat insulating jacket is coated on the outer wall surface of the closed path.

【図7】エジェクターからなるガス処理部の断面図であ
る。
FIG. 7 is a cross-sectional view of a gas processing unit including an ejector.

【図8】ボイラーを兼ねたガス処理部の部分断面図であ
る。
FIG. 8 is a partial cross-sectional view of a gas processing unit serving also as a boiler.

【符号の説明】[Explanation of symbols]

1 処理車 3 原料ホッパ 4 送りスクリュー 5 密閉経路 6 撹拌混合機 7 ガス処理部 8 ボイラー DESCRIPTION OF SYMBOLS 1 Processing car 3 Material hopper 4 Feed screw 5 Sealed path 6 Stirring mixer 7 Gas processing part 8 Boiler

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI B65F 3/22 B09B 3/00 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 6 Identification code FI B65F 3/22 B09B 3/00

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 有機物又は有機廃棄物等の原料を脱水処
理する再生処理装置を搭載した車両であって、再生処理
装置が、投入した原料の油分調整を図りながら粉砕又は
混練する原料ホッパと、該原料ホッパから原料を受け取
り送り出す移送経路と、移送経路から受け取った原料を
加熱手段又は保温手段を有する密閉経路内に閉じ込めて
一方向へ移送しつつ該移送方向の略直角方向へ原料を跳
ね上げて撹拌又は粉砕しながら該原料を脱水処理する撹
拌混合機と、原料ホッパ又は撹拌混合機から放出される
水蒸気及び廃ガスを処理するガス処理部とからなること
を特徴とする有機廃棄物再生処理車。
1. A vehicle equipped with a regeneration processing device for dehydrating a raw material such as organic matter or organic waste, wherein the regeneration processing device crushes or kneads while adjusting the oil content of the input raw material, A transfer path for receiving and sending the raw material from the raw material hopper, and a raw material received from the transfer path is confined in a closed path having a heating means or a heat retaining means, and is transferred in one direction while jumping the raw material in a direction substantially perpendicular to the transfer direction. Organic waste recycling processing, comprising: a stirring mixer for dehydrating the raw material while stirring or pulverizing the raw material; and a gas processing unit for processing steam and waste gas discharged from the raw material hopper or the mixing mixer. car.
【請求項2】 移送部が原料を圧縮しながら移送する送
りスクリューであって、スクリュー入口からスクリュー
出口へ至る経路にピッチを徐々に狭めていくスクリュー
と、前記スクリュー出口近傍には前記スクリューを省い
てカッタを取り付け、スクリュー出口に圧縮した原料を
細長く押し出すオリフィス状の多孔板を配した構成から
なることを特徴とする請求項1記載の有機廃棄物再生処
理車。
2. A feed screw for transferring a raw material while compressing the feed, wherein the screw gradually narrows a pitch in a path from a screw inlet to a screw outlet, and the screw is omitted near the screw outlet. The organic waste recycling vehicle according to claim 1, wherein a cutter is attached, and an orifice-shaped perforated plate is provided at a screw outlet to extrude the compressed raw material into an elongated shape.
【請求項3】 撹拌混合機が一定長の密閉経路を複数連
結して長尺の処理経路を構成してなり、各密閉経路は撹
拌機入口から撹拌機出口へ向けて登り勾配を有している
ことを特徴とする請求項1記載の有機廃棄物再生処理
車。
3. A stirring mixer comprises a plurality of closed paths having a predetermined length connected to form a long processing path, and each closed path has an ascending gradient from an inlet of the stirrer to an outlet of the stirrer. The vehicle for recycling organic waste according to claim 1, wherein:
【請求項4】 ガス処理部が負圧下の密閉水槽内へ導い
た水蒸気及び廃ガスを冷却により液化するエジェクター
であって、水蒸気及び廃ガスを水底へ向けて放出し、水
槽内の迂回壁を廻って水面へ向けて上昇させる過程で水
蒸気を液化して、廃ガスから異物を除去することを特徴
とする請求項1記載の有機廃棄物再生処理車。
4. An ejector for liquefying water vapor and waste gas introduced into a closed water tank under a negative pressure by cooling by a gas treatment unit, wherein the ejector discharges the water vapor and waste gas toward the bottom of the water to form a bypass wall in the water tank. The organic waste recycling vehicle according to claim 1, wherein the steam is liquefied in the process of moving toward the water surface to remove foreign matter from the waste gas.
【請求項5】 ガス処理部が水蒸気及び廃ガスを燃やし
て燃焼ガスを生成するボイラーであって、燃焼ガスを大
気中へ放出すると共に、該燃焼ガスの一部を原料ホッパ
又は撹拌混合機へ供給し加熱媒体として利用することを
特徴とする請求項1記載の有機廃棄物再生処理車。
5. A boiler in which a gas processing section burns water vapor and waste gas to generate a combustion gas, discharges the combustion gas into the atmosphere, and transfers a part of the combustion gas to a raw material hopper or a stirring mixer. The vehicle according to claim 1, wherein the vehicle is supplied and used as a heating medium.
JP8285239A 1996-10-28 1996-10-28 Organic waste recycling vehicle Pending JPH10129805A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8285239A JPH10129805A (en) 1996-10-28 1996-10-28 Organic waste recycling vehicle

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8285239A JPH10129805A (en) 1996-10-28 1996-10-28 Organic waste recycling vehicle

Publications (1)

Publication Number Publication Date
JPH10129805A true JPH10129805A (en) 1998-05-19

Family

ID=17688924

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8285239A Pending JPH10129805A (en) 1996-10-28 1996-10-28 Organic waste recycling vehicle

Country Status (1)

Country Link
JP (1) JPH10129805A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH11268801A (en) * 1998-03-23 1999-10-05 Tokusho Sangyo Kk Organic waste collecting transport vehicle
WO2006011727A1 (en) * 2004-07-27 2006-02-02 Jong-Wan Im Special vehicle for instantly processing organic wastes and thereafter instantly producing organic lime manure
JP2006231712A (en) * 2005-02-25 2006-09-07 Marumi:Kk Pelletizer
JP2007021410A (en) * 2005-07-19 2007-02-01 Kunitomo Kankyo Plant:Kk Apparatus and method for treating organic waste
WO2007033425A1 (en) * 2005-09-23 2007-03-29 Cassa Pty Ltd Mobile recycling and bio-fuel production system for animal waste
KR100863154B1 (en) 2008-04-18 2008-10-13 주식회사 삼영필텍 Mobile purification system of waste oil
JP2011092938A (en) * 2010-12-16 2011-05-12 Kunitomo Kankyo Plant:Kk Apparatus for treating organic waste
KR101370569B1 (en) * 2011-02-16 2014-03-06 조영두 Moving apparatus for highly pathogenic waste treatment

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH11268801A (en) * 1998-03-23 1999-10-05 Tokusho Sangyo Kk Organic waste collecting transport vehicle
WO2006011727A1 (en) * 2004-07-27 2006-02-02 Jong-Wan Im Special vehicle for instantly processing organic wastes and thereafter instantly producing organic lime manure
CN100460364C (en) * 2004-07-27 2009-02-11 林锺完 Special vehicle for instantly processing organic wastes and thereafter instantly producing organic lime manure
JP2006231712A (en) * 2005-02-25 2006-09-07 Marumi:Kk Pelletizer
JP2007021410A (en) * 2005-07-19 2007-02-01 Kunitomo Kankyo Plant:Kk Apparatus and method for treating organic waste
JP4692994B2 (en) * 2005-07-19 2011-06-01 有限会社国友環境プラント Organic waste treatment methods
WO2007033425A1 (en) * 2005-09-23 2007-03-29 Cassa Pty Ltd Mobile recycling and bio-fuel production system for animal waste
KR100863154B1 (en) 2008-04-18 2008-10-13 주식회사 삼영필텍 Mobile purification system of waste oil
JP2011092938A (en) * 2010-12-16 2011-05-12 Kunitomo Kankyo Plant:Kk Apparatus for treating organic waste
KR101370569B1 (en) * 2011-02-16 2014-03-06 조영두 Moving apparatus for highly pathogenic waste treatment

Similar Documents

Publication Publication Date Title
CA1290937C (en) Process and device for conditioning bulk material
US4829678A (en) Sludge treatment process
KR101729994B1 (en) Low-temperature dry apparatus for sludge using heat transfer media and dry method thereof
JPH10129805A (en) Organic waste recycling vehicle
JPS6243651B2 (en)
JP2002018397A (en) Wet garbage dewatering and drying device
US4217222A (en) Apparatus for processing municipal solid waste and sewage sludge
KR20150064895A (en) System for disposing of waste of food
JP2000065476A (en) Drying treatment method and device for wet waste
JP2905203B1 (en) On-board drying device for sewage sludge and method of using the same
JP2004216332A (en) Treatment method and treatment system for waste
JP3949632B2 (en) Drying equipment
JP3709521B2 (en) Organic waste treatment equipment
JPH105799A (en) Sludge treatment and device therefor
JPH1071400A (en) Process and apparatus for sludge treatment
EP0926230B1 (en) Rendering apparatus and method
KR200362533Y1 (en) processing device for waste food
KR100319410B1 (en) System and method for treating organic waste matter have in water
JP2000192063A (en) Method and apparatus for mixing and drying wet waste
KR20020023357A (en) Manufacturing Apparatus and Method of Heating Fuel Using Food Garbage
JPH0978076A (en) Apparatus for manufacturing solid fuel
KR20000008142A (en) Food garbage solidification device
JP3642633B2 (en) Fish meal manufacturing method and equipment
KR100311659B1 (en) device for disposing food garbage
JP2000034112A (en) Activated carbon for dioxin adsorption, its production, apparatus and dioxin adsorption treatment