JP4599187B2 - Organic waste transport device - Google Patents

Organic waste transport device Download PDF

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JP4599187B2
JP4599187B2 JP2005047401A JP2005047401A JP4599187B2 JP 4599187 B2 JP4599187 B2 JP 4599187B2 JP 2005047401 A JP2005047401 A JP 2005047401A JP 2005047401 A JP2005047401 A JP 2005047401A JP 4599187 B2 JP4599187 B2 JP 4599187B2
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organic waste
pipe
receiving
garbage
transport
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JP2006231164A (en
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和敬 竹内
勝也 三石
正登 渡辺
勝啓 伊藤
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Mitsui Engineering and Shipbuilding Co Ltd
Mitsui E&S Holdings Co Ltd
Mitsui Zosen Environment Engineering Corp
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Mitsui Engineering and Shipbuilding Co Ltd
Mitsui E&S Holdings Co Ltd
Mitsui Zosen Environment Engineering Corp
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Description

本発明は有機性廃棄物の搬送装置に関し、詳しくは、受入ホッパー或いはピット内の生ゴミを残さず搬出し、生ゴミの腐敗、悪臭、蛆・はえ等の発生、危険性ガスの発生を防止し、安全及び衛生的な運転を確保することができる有機性廃棄物の搬送装置に関する。   The present invention relates to an organic waste transport device, and more particularly, it carries out garbage without leaving garbage in a receiving hopper or pit, and generates decay, bad odor, soot and fly, and generation of dangerous gas. The present invention relates to an organic waste transport device that can prevent and ensure safe and sanitary operation.

家庭やホテル、レストラン等の厨房等から発生する生ゴミ等の有機性廃棄物(以下、必要により、「生ゴミ等」という)は、ビニール袋などの樹脂製袋に入れられた状態で排出されることが多く、腐敗性が高い特性があり、既に腐敗していたりするものも混じっている。   Organic waste such as garbage (hereinafter referred to as “garbage etc.” if necessary) generated from kitchens at home, hotels, restaurants, etc., is discharged in plastic bags and other plastic bags. It often has a characteristic of high perishability, and some are already corrupt.

上記の生ゴミ等は、ゴミ処理施設に塵芥車で運ばれ、ゴミピットに投入され、その後、クレーンバケットで所定のゴミホッパーに投入する方式が最も一般的に採用されている。   The above-mentioned method is most generally employed in which the above garbage is transported to a garbage disposal facility by a garbage truck, put into a garbage pit, and then put into a predetermined garbage hopper by a crane bucket.

しかし、クレーンバケットでは掴みきれないゴミがピットに残る。従って、生ゴミ等の場合、残った生ゴミが腐敗し、悪臭、蛆・はえ等の発生、更に危険性ガスの発生が懸念される。   However, garbage that cannot be grasped by the crane bucket remains in the pit. Therefore, in the case of raw garbage, the remaining raw garbage is rotted, and there is a concern about generation of bad odor, soot and fly, and generation of dangerous gas.

また、切出し装置付きホッパーに生ゴミを投入し、切出し装置、粗粉砕機からチューブコンベアを通し、生ゴミを湿式破砕選別装置に送ることは可能であるが、チューブ中のチェーンにビニール袋が絡まる、或いは残飯類が餅のようにチェーンに固着し、最終的には搬送できなくなる問題があり、更に残飯類が腐敗する問題がある。   It is also possible to feed garbage into a hopper equipped with a cutting device, pass the tube conveyor from the cutting device and coarse pulverizer, and send the garbage to the wet crushing and sorting device. Alternatively, there is a problem that the leftovers stick to the chain like a bowl and eventually cannot be conveyed, and there is another problem that the leftovers rot.

更に、切出し装置付きホッパーに生ゴミを投入し、切出し装置、粗粉砕機からフライトコンベアを通し、生ゴミを湿式破砕選別装置に送ることは可能であるが、トラフ中のチェーンにビニール袋が絡まったり、或いは残飯類が餅のようにチェーンに固着し、搬送できなくなる問題や水分が送れない問題がある。
特開2004−66051 ポンプ輸送
Furthermore, it is possible to feed garbage into a hopper equipped with a cutting device and send it to the wet crushing and sorting device through the flight conveyor from the cutting device and coarse pulverizer, but a plastic bag is entangled in the chain in the trough. There is a problem that the leftovers are stuck to the chain like a bowl and cannot be transported or moisture cannot be sent.
JP-A-2004-66051 Pump transportation

そこで、本発明は、受入ホッパー或いはピット内の生ゴミを残さず搬出し、生ゴミの腐敗、悪臭、蛆・はえ等の発生、危険性ガスの発生を防止し、安全及び衛生的な運転を確保することができる有機性廃棄物の搬送装置を提供することを課題とする。   Therefore, the present invention carries out garbage without leaving garbage in the receiving hopper or pit, prevents garbage from being spoiled, foul odor, generation of soot and fly, generation of dangerous gas, and safe and sanitary operation. It is an object of the present invention to provide an organic waste transport device capable of ensuring the above.

また、本発明の他の課題は、以下の記載によって明らかとなる。   Other problems of the present invention will become apparent from the following description.

上記課題は、以下の各発明によって解決される。   The above problems are solved by the following inventions.

(請求項1)
生ゴミ等の有機性廃棄物を受け入れる受入手段と、該受入手段から送られる生ゴミ等の有機性廃棄物を破砕する破砕手段と、前記破砕手段で破砕された有機性廃棄物を受け入れる投入手段と、該投入手段内に水又は温水を供給する水供給装置とを備え、かつ該破砕手段と該投入手段は負圧になるように構成され、該投入手段から含水率70%以上90%以下の有機性廃棄物を受け入れると共に負圧下で空気輸送する輸送配管を有することを特徴とする有機性廃棄物の搬送装置。
(Claim 1)
Accepting means for receiving organic waste such as garbage, crushing means for crushing organic waste such as garbage sent from the receiving means, and input means for receiving organic waste crushed by the crushing means And a water supply device for supplying water or hot water into the charging means, and the crushing means and the charging means are configured to have a negative pressure, and the moisture content from the charging means is 70% to 90%. An organic waste transport apparatus comprising a transport pipe that accepts organic waste and pneumatically transports it under negative pressure.

(請求項2)
前記投入ホッパー内から前記輸送配管に供給する廃棄物供給装置を有することを特徴とする請求項1記載の有機性廃棄物の搬送装置。
(Claim 2)
The apparatus for transporting organic waste according to claim 1, further comprising a waste supply device that supplies the transport pipe from the inside of the charging hopper.

(請求項3)
前記投入ホッパーが、前記有機性廃棄物を計量する計量機を備えることを特徴とする請求項2記載の有機性廃棄物の搬送装置。
(Claim 3)
The said waste hopper is equipped with the weighing machine which measures the said organic waste, The conveying apparatus of the organic waste of Claim 2 characterized by the above-mentioned.

(請求項4)
前記輸送配管の途中に、該輸送配管によって輸送される有機性廃棄物を受け入れると共に有機性廃棄物が除外された空気を排出する受タンクを有し、該受タンクはスラリー化槽に接続されていることを特徴とする請求項1〜3の何れかに記載の有機性廃棄物の搬送装置。
(Claim 4)
In the middle of the transportation pipe, it has a receiving tank for receiving the organic waste transported by the transportation pipe and discharging the air from which the organic waste has been excluded, and the receiving tank is connected to the slurrying tank. The organic waste transport apparatus according to claim 1, wherein the transport apparatus is an organic waste transport apparatus.

(請求項5)
前記受タンクが、前記有機性廃棄物を計量する計量機を備えることを特徴とする請求項4記載の有機性廃棄物の搬送装置。
(Claim 5)
The said waste tank is equipped with the weighing machine which measures the said organic waste, The conveying apparatus of the organic waste of Claim 4 characterized by the above-mentioned.

(請求項6)
前記受タンクから排出された空気を輸送する空気配管に、気水分離手段を備えることを特徴とする請求項4又は5記載の有機性廃棄物の搬送装置。
(Claim 6)
6. The apparatus for transporting organic waste according to claim 4, wherein the air pipe for transporting the air discharged from the receiving tank is provided with a steam / water separation means.

(請求項7)
前記輸送配管を負圧状態にする吸引手段を備え、該吸引手段の吸込側に前記輸送配管が連結されていることを特徴とする請求項1〜6の何れかに記載の有機性廃棄物の搬送装置。
(Claim 7)
The organic waste according to any one of claims 1 to 6, further comprising suction means for bringing the transport pipe into a negative pressure state, wherein the transport pipe is connected to a suction side of the suction means. Conveying device.

(請求項8)
前記吸引手段の吐出側の配管が、前記輸送配管の前記有機性廃棄物の受入部位に連結されていることを特徴とする請求項7記載の有機性廃棄物の搬送装置。
(Claim 8)
8. The organic waste transporting apparatus according to claim 7, wherein a pipe on the discharge side of the suction means is connected to a site for receiving the organic waste of the transport pipe.

本発明によると、受入ホッパー或いはピット内の生ゴミを残さず搬出し、生ゴミの腐敗、悪臭、蛆・はえ等の発生、危険性ガスの発生を防止し、安全及び衛生的な運転を確保することができる有機性廃棄物の搬送装置を提供することができる。   According to the present invention, the garbage in the receiving hopper or pit is carried out without leaving any garbage, and the garbage is prevented from being spoiled, foul odors, generation of soot and fly, and the generation of hazardous gas, and safe and hygienic operation is achieved. It is possible to provide an organic waste transport device that can be secured.

以下、本発明の実施の形態について図面に基づいて説明する。   Hereinafter, embodiments of the present invention will be described with reference to the drawings.

図1は、本発明の実施形態を示す説明図である。図1において、1は生ゴミ等の有機性廃棄物を受け入れる受入手段である。受入手段1には、例えば塵芥車100等によって所定量の生ゴミ等の有機性廃棄物が搬入される。搬入は定期的でも不定期的でもよい。   FIG. 1 is an explanatory diagram showing an embodiment of the present invention. In FIG. 1, reference numeral 1 denotes a receiving means for receiving organic waste such as garbage. A predetermined amount of organic waste such as garbage is carried into the receiving means 1 by, for example, a garbage truck 100 or the like. Carry-in can be regular or irregular.

受入手段1は、金属製又は樹脂製の受入ホッパー101や図示しないコンクリート製の受入ピットによって構成される。受入ホッパー或いは受入ピットの形状は、円錐台又は角錐台構造にして底部中心に受け入れた生ゴミ等の有機性廃棄物が集まる構成にすることがその後の搬出を容易にする上で好ましい。   The receiving means 1 includes a metal or resin receiving hopper 101 and a concrete receiving pit (not shown). The shape of the receiving hopper or the receiving pit is preferably a truncated cone or truncated pyramid structure so that organic waste such as raw garbage received at the center of the bottom gathers in order to facilitate subsequent carry-out.

有機性廃棄物には、生ゴミ以外に、樹脂製袋(例えばビニール袋、ポリ袋など)、樹脂製トレー、樹脂片(ビニール片、フィルム片)などを含み、かかる有機性廃棄物に混入する物質としては、卵の殻、重い金属、貝殻、小石等がある。   Organic waste includes resin bags (for example, plastic bags, plastic bags, etc.), resin trays, resin pieces (vinyl pieces, film pieces), etc., in addition to garbage, and is mixed into such organic waste. Substances include egg shells, heavy metals, shells, pebbles and the like.

受入手段1の底部には、切出し装置102が設けられ、切出し装置102としては、例えばスクリューコンベアを好ましく用いることができる。かかる切出し装置102により、受入手段1内の生ゴミ等は所定量ずつ下方に搬出され、全量抜き出される。従って、生ゴミの腐敗、危険性ガスの発生を防ぐことができる。   A cutting device 102 is provided at the bottom of the receiving means 1. As the cutting device 102, for example, a screw conveyor can be preferably used. By this cutting device 102, garbage etc. in the receiving means 1 are carried downward by a predetermined amount and extracted in its entirety. Therefore, it is possible to prevent garbage from being spoiled and generation of dangerous gas.

2は受入手段1から送られる生ゴミ等の有機性廃棄物を破砕する破砕手段であり、該破砕手段2には破砕機が用いられ、該破砕機によって生ゴミ袋を破砕することにより空気輸送を可能にした。また破砕機によって同時に生ゴミを粗粉砕することにより空気輸送をより容易にした。   Reference numeral 2 denotes a crushing means for crushing organic waste such as garbage sent from the receiving means 1. A crusher is used for the crushing means 2, and pneumatic transportation is performed by crushing the garbage bag by the crusher. Made possible. Also, pneumatic transportation was made easier by roughly crushing raw garbage simultaneously with a crusher.

3は前記破砕手段で破砕された有機性廃棄物を受け入れる投入手段であり、投入手段は、投入ホッパー300を備え、該投入ホッパー300には水供給装置301が設けてある。   Reference numeral 3 denotes an input unit that receives the organic waste crushed by the crushing unit. The input unit includes an input hopper 300, and the input hopper 300 is provided with a water supply device 301.

かかる水供給装置301は、破砕手段2で破砕された生ゴミ等に水又は温水を供給して含水率70%以上90%以下の有機性廃棄物を結果として生成する。   Such a water supply device 301 supplies water or warm water to the raw garbage etc. crushed by the crushing means 2 to produce organic waste having a water content of 70% or more and 90% or less as a result.

水供給装置301は、温水供給配管302と、温水制御弁303と、水供給配管304と、水制御弁305を備えている。温水制御弁303と水制御弁305を設けると、水供給装置301から供給される水の水温、水量が調整可能となる。水供給装置301から供給される水配管の先端にはスプレーノズル306を設けると洗浄効果を向上させる上で好ましい。   The water supply device 301 includes a hot water supply pipe 302, a hot water control valve 303, a water supply pipe 304, and a water control valve 305. When the hot water control valve 303 and the water control valve 305 are provided, the temperature and amount of water supplied from the water supply device 301 can be adjusted. A spray nozzle 306 is preferably provided at the front end of the water pipe supplied from the water supply device 301 in order to improve the cleaning effect.

水供給装置301から水を投入ホッパー300内に供給できる構成にすると、生ゴミ等の水分は70%以上90%以下、好ましくは80%以上90%以下の含水率となる。   When water is supplied from the water supply device 301 into the charging hopper 300, the moisture content of raw garbage becomes 70% or more and 90% or less, preferably 80% or more and 90% or less.

かかる含水率であると、投入ホッパー300内部に樹脂製袋、樹脂片、残飯類等が残らないようにすることができることは勿論のこと、輸送配管の閉塞を防ぐことができる。   With such a moisture content, it is possible to prevent resin bags, resin pieces, leftovers, etc. from remaining in the charging hopper 300, and it is possible to prevent clogging of the transportation piping.

生ゴミ等の水分は以下の算出式によって算出する。   The water content of raw garbage is calculated by the following formula.

含水率(%)=(生ゴミ等中の水分重量/生ゴミ等の全重量)×100   Moisture content (%) = (weight of water in garbage / total weight of garbage) × 100

含水率が70%未満であると、輸送配管の閉塞が生じる問題があり、90%を越えると水分が多すぎて搬送障害が生じる。   If the water content is less than 70%, there is a problem that the transportation piping is blocked, and if it exceeds 90%, there is too much moisture, resulting in a conveyance failure.

本発明の好ましい実施の形態としては、生ゴミの量を計量し、後段の発酵に最適なスラリー濃度を確保するために、投入ホッパー300に計量機307を設け、生ゴミを計量する。計量機307は、投入ホッパー300ではなく、受入ホッパー101に設けることもでき、投入ホッパー300と受入ホッパー101の両方に設けてもよい。   As a preferred embodiment of the present invention, in order to measure the amount of raw garbage and to secure an optimum slurry concentration for subsequent fermentation, the input hopper 300 is provided with a weighing machine 307 to measure the raw garbage. The weighing machine 307 can be provided not in the charging hopper 300 but in the receiving hopper 101, and may be provided in both the charging hopper 300 and the receiving hopper 101.

投入ホッパー300の底部には生ゴミ等の輸送配管4に供給する廃棄物供給装置308を設けてある。309は廃棄物供給装置308の排出管310に設けられた遮断弁である。   At the bottom of the charging hopper 300, a waste supply device 308 is provided for supplying the transportation piping 4 for raw garbage and the like. Reference numeral 309 denotes a shutoff valve provided in the discharge pipe 310 of the waste supply device 308.

廃棄物供給装置308の排出管310は、輸送配管4に接続されており、水供給手段3から高含水有機性廃棄物を輸送配管4に供給可能となっている。   The discharge pipe 310 of the waste supply device 308 is connected to the transport pipe 4, so that high water content organic waste can be supplied from the water supply means 3 to the transport pipe 4.

輸送配管4は吸引手段の一例である吸引ブロア400の吸込側に連結されている。かかる構成により、輸送配管4内の生ゴミ等は負圧下で空気輸送される。   The transport pipe 4 is connected to a suction side of a suction blower 400 which is an example of a suction unit. With this configuration, garbage etc. in the transport pipe 4 is pneumatically transported under a negative pressure.

輸送配管4の径は、10t/hrの生ゴミ等(含水率85%)を輸送する際に、50mmφ〜80mmφの範囲である。好ましくは約75mmφ程度であり、かかる小径の配管であっても閉塞せずに輸送可能である。   The diameter of the transport pipe 4 is in the range of 50 mmφ to 80 mmφ when transporting garbage such as 10 t / hr (water content 85%). Preferably, the diameter is about 75 mmφ, and even such a small-diameter pipe can be transported without being blocked.

吸引ブロア400の吐出側の吐出配管401は、輸送配管4に前生ゴミ等を受け入れる受入部位402に連結されている。従って、輸送配管4と、吸引ブロア400、吐出配管401は、循環系を構成している。400Aは吸引安全弁である。   A discharge pipe 401 on the discharge side of the suction blower 400 is connected to a receiving part 402 that receives pre-grown garbage or the like in the transport pipe 4. Accordingly, the transport pipe 4, the suction blower 400, and the discharge pipe 401 constitute a circulation system. 400A is a suction safety valve.

輸送配管4の途中には、輸送配管4によって輸送される生ゴミ等を受け入れる受タンク403が設けられている。受タンク403は生ゴミ等を受け入れた後、輸送空気と分離し、輸送空気は輸送配管4に戻されて吸引ブロア400に吸引される。403Aはダンパーである。   In the middle of the transport pipe 4, a receiving tank 403 that receives raw garbage transported by the transport pipe 4 is provided. The receiving tank 403 receives raw garbage and the like and then separates it from the transport air. The transport air is returned to the transport pipe 4 and sucked into the suction blower 400. 403A is a damper.

受タンク403の下部にはスラリー化槽404が接続されている。スラリー化槽404は、モータ405によって回転する攪拌機406を備えており、攪拌機406の先端には裁断刃407を備えている。   A slurrying tank 404 is connected to the lower part of the receiving tank 403. The slurrying tank 404 includes a stirrer 406 that is rotated by a motor 405, and a cutting blade 407 is provided at the tip of the stirrer 406.

スラリー化槽404に導入された生ゴミ等は、更に細かくスラリー化すると同時に、重い金属、貝の殻、紛れ込んだ小石等の挟雑物は分離され、抜き出される。   The garbage etc. introduced into the slurrying tank 404 is further slurried and at the same time, heavy metals, shells of shells, and mixed objects such as pebbles are separated and extracted.

次にスラリー化槽404で生成されたスラリーは、水頭差を利用し自然流下で(水頭差を利用できない場合はスラリーポンプ408を用いて)、分別槽409に送られる。   Next, the slurry generated in the slurrying tank 404 is sent to the separation tank 409 under a natural flow using the water head difference (when the water head difference cannot be used, using the slurry pump 408).

分別槽409は例えばスクリーンによって構成され、ビニール袋、砂状になった卵の殻等を分離する。   The separation tank 409 is constituted by a screen, for example, and separates a plastic bag, a sand-like egg shell, and the like.

次に分別処理されたスラリーは、一時図示しない貯留槽を経て、発酵槽410に送られ、発酵処理される。   Next, the separated slurry is temporarily sent to a fermenter 410 through a storage tank (not shown) and subjected to a fermentation process.

一方、受タンク403で分離された輸送空気は吸引ブロア400に至る過程で、気水分離手段である気水分離装置403Bにより、水分が分離される。気水分離装置403Bの構成は特に限定されないが、例えば、マルチサイクロン、慣性集塵機などを採用できる。   On the other hand, the transported air separated in the receiving tank 403 is separated in the process of reaching the suction blower 400 by the steam / water separator 403B, which is a steam / water separator. Although the structure of the steam separator 403B is not specifically limited, For example, a multi cyclone, an inertia dust collector, etc. are employable.

輸送配管4あるいは吐出配管401には、圧力調整装置411を設けることもでき、図1に示す例では、吐出配管401に設けている。412は圧力指示制御計である。圧力調整装置411で抜き出された空気は必要により脱臭装置413で脱臭することも好ましいことである。   The transport pipe 4 or the discharge pipe 401 can be provided with a pressure adjusting device 411. In the example shown in FIG. Reference numeral 412 denotes a pressure indicating controller. It is also preferable that the air extracted by the pressure adjusting device 411 is deodorized by the deodorizing device 413 if necessary.

以上の設備において、生ゴミ等の搬送は吸引ブロアによる負圧下で行われる。輸送配管4(あるいは吐出配管401)における好ましい圧力状態を例示すると、受入部位402では−10mmAq程度、吸引ブロア400の部位で−400mmAq程度が好ましい。   In the above equipment, the conveyance of garbage etc. is performed under a negative pressure by a suction blower. For example, a preferable pressure state in the transport pipe 4 (or the discharge pipe 401) is preferably about −10 mmAq at the receiving part 402 and about −400 mmAq at the part of the suction blower 400.

本発明では、切出し装置102以降、破砕機、投入ホッパーなどは全て負圧になるように構成されるので、付着物や残留物は全て水供給装置から送られる水との協働作用で除去され、輸送配管で搬送される。従って、生ゴミの腐敗、危険性ガスの発生を防ぐ上でも更に効果的である。   In the present invention, since the crushing device and the charging hopper are all configured to have a negative pressure after the cutting device 102, all the deposits and residues are removed by the cooperative action with the water fed from the water supply device. , Transported by transport piping. Therefore, it is further effective in preventing the decay of raw garbage and the generation of hazardous gas.

以上、本発明の好ましい実施形態について説明したが、本発明の実施の形態は上記に限定されず、例えば図2に示すように、計量機414を受タンク403に設けることも好ましい。また水供給手段3側と受タンク403の両方に計量機を設けることもできる。   The preferred embodiment of the present invention has been described above. However, the embodiment of the present invention is not limited to the above, and it is also preferable to provide a weighing machine 414 in the receiving tank 403, for example, as shown in FIG. A metering device can be provided on both the water supply means 3 side and the receiving tank 403.

また輸送配管4の特に曲がり部位(エルボなど)には、エアー供給管を配置することも好ましい。即ち、図3に示すように、エルボ1とエルボ2が存在する場合、エルボ1の前段の圧力計P、後段の圧力計Pで各々の圧力を計測し、差圧が所定値以上になったら、生ゴミ等の供給を停止し、空気吸入管420から空気を供給する。 Moreover, it is also preferable to arrange an air supply pipe at a bent part (elbow or the like) of the transport pipe 4. That is, as shown in FIG. 3, when the elbow 1 and the elbow 2 are present, the respective pressures are measured by the pressure gauge P 0 at the front stage and the pressure gauge P 1 at the rear stage of the elbow 1 so that the differential pressure becomes a predetermined value or more. When this happens, the supply of garbage and the like is stopped, and air is supplied from the air suction pipe 420.

空気の配管に対する供給する方向は、図4に示すように接線方向に供給する。このような方向に供給すると、生ゴミ等を低圧力で搬送助長できてこのましい。   The air is supplied to the pipe in the tangential direction as shown in FIG. If it supplies in such a direction, it will be good to encourage conveyance of garbage etc. with low pressure.

またエルボ2の前段の圧力計P、後段の圧力計Pでおのおの圧力を計測し、差圧が所定値以上になったら、生ゴミ等の供給を停止し、空気吸入管421から空気を供給する。 Also, each pressure is measured with the pressure gauge P 1 at the front of the elbow 2 and the pressure gauge P 2 at the rear, and when the differential pressure exceeds a predetermined value, the supply of garbage etc. is stopped and the air is sucked from the air suction pipe 421. Supply.

空気の配管に対する供給する方向は、図4に示すように接線方向に供給することが好ましい。   As shown in FIG. 4, it is preferable to supply the air to the piping in the tangential direction.

なお、図3に示す態様において、供給する流体を空気に代えて、水や不活性ガスを供給することもできる。   In the embodiment shown in FIG. 3, water or inert gas can be supplied instead of air to be supplied.

本発明の実施形態を示す説明図Explanatory drawing which shows embodiment of this invention 本発明の他の実施形態を示す説明図Explanatory drawing which shows other embodiment of this invention. 本発明の他の実施形態を示す説明図Explanatory drawing which shows other embodiment of this invention. 図3の要部断面説明図3 is a cross-sectional explanatory diagram of the main part of FIG.

符号の説明Explanation of symbols

1:受入手段
100:塵芥車
101:受入ホッパー
102:切出し装置
2:破砕手段
3:投入手段
300:投入ホッパー
301:水供給装置
302:温水供給配管
303:温水制御弁
304:水供給配管
305:水制御弁
306:スプレーノズル
307:計量機
308:廃棄物供給装置
309:遮断弁
310:排出管
4:輸送配管
400:吸引ブロア
401:吐出配管
402:受入部位
403:受タンク
403A:ダンパー
403B:気水分離装置
404:スラリー化槽
405:モータ
406:攪拌機
407:裁断刃
408:スラリーポンプ
409:分別槽
410:発酵槽
411:圧力調整装置
412:圧力指示制御計
413:脱臭装置
414:計量機
420:空気吸入管
421:空気吸入管
1: Receiving means 100: Dust truck 101: Receiving hopper 102: Cutting device 2: Crushing means 3: Loading means 300: Loading hopper 301: Water supply device 302: Hot water supply pipe 303: Hot water control valve 304: Water supply pipe 305: Water control valve 306: Spray nozzle 307: Metering device 308: Waste supply device 309: Shut-off valve 310: Discharge pipe 4: Transport pipe 400: Suction blower 401: Discharge pipe 402: Receiving part 403: Receiving tank 403A: Damper 403B: Gas-water separator 404: Slurry tank 405: Motor 406: Stirrer 407: Cutting blade 408: Slurry pump 409: Separation tank 410: Fermenter 411: Pressure regulator 412: Pressure indicating controller 413: Deodorizer 414: Meter 420: Air suction pipe 421: Air suction pipe

Claims (8)

生ゴミ等の有機性廃棄物を受け入れる受入手段と、該受入手段から送られる生ゴミ等の有機性廃棄物を破砕する破砕手段と、前記破砕手段で破砕された有機性廃棄物を受け入れる投入手段と、該投入手段内に水又は温水を供給する水供給装置とを備え、かつ該破砕手段と該投入手段は負圧になるように構成され、該投入手段から含水率70%以上90%以下の有機性廃棄物を受け入れると共に負圧下で空気輸送する輸送配管を有することを特徴とする有機性廃棄物の搬送装置。   Accepting means for receiving organic waste such as garbage, crushing means for crushing organic waste such as garbage sent from the receiving means, and input means for accepting organic waste crushed by the crushing means And a water supply device for supplying water or hot water into the charging means, and the crushing means and the charging means are configured to have a negative pressure, and the moisture content from the charging means is 70% to 90%. An organic waste transport apparatus comprising a transport pipe that accepts organic waste and pneumatically transports it under negative pressure. 前記投入手段は、投入ホッパーを備えると共に、該投入ホッパー内から前記輸送配管に供給する廃棄物供給装置を備えることを特徴とする請求項1記載の有機性廃棄物の搬送装置。   2. The organic waste transporting apparatus according to claim 1, wherein the charging unit includes a charging hopper and a waste supply device that supplies the charging pipe from the charging hopper to the transport pipe. 前記投入ホッパーが、前記有機性廃棄物を計量する計量機を備えることを特徴とする請求項2記載の有機性廃棄物の搬送装置。The said waste hopper is equipped with the weighing machine which measures the said organic waste, The conveying apparatus of the organic waste of Claim 2 characterized by the above-mentioned. 前記輸送配管の途中に、該輸送配管によって輸送される有機性廃棄物を受け入れると共に有機性廃棄物が除外された空気を排出する受タンクを有し、該受タンクはスラリー化槽に接続されていることを特徴とする請求項1〜3の何れかに記載の有機性廃棄物の搬送装置。In the middle of the transportation pipe, it has a receiving tank for receiving the organic waste transported by the transportation pipe and discharging the air from which the organic waste has been excluded, and the receiving tank is connected to the slurrying tank. The organic waste transport apparatus according to claim 1, wherein the transport apparatus is an organic waste transport apparatus. 前記受タンクが、前記有機性廃棄物を計量する計量機を備えることを特徴とする請求項4記載の有機性廃棄物の搬送装置。 The said waste tank is equipped with the weighing machine which measures the said organic waste, The conveying apparatus of the organic waste of Claim 4 characterized by the above-mentioned. 前記受タンクから排出された空気を輸送する空気配管に、気水分離手段を備えることを特徴とする請求項4又は5記載の有機性廃棄物の搬送装置。6. The apparatus for transporting organic waste according to claim 4, wherein the air pipe for transporting the air discharged from the receiving tank is provided with a steam / water separation means. 前記輸送配管を負圧状態にする吸引手段を備え、該吸引手段の吸込側に前記輸送配管が連結されていることを特徴とする請求項1〜6の何れかに記載の有機性廃棄物の搬送装置。The organic waste according to any one of claims 1 to 6, further comprising suction means for bringing the transport pipe into a negative pressure state, wherein the transport pipe is connected to a suction side of the suction means. Conveying device. 前記吸引手段の吐出側の配管が、前記輸送配管の前記有機性廃棄物の受入部位に連結されていることを特徴とする請求項7記載の有機性廃棄物の搬送装置。8. The organic waste transporting apparatus according to claim 7, wherein a pipe on the discharge side of the suction means is connected to a site for receiving the organic waste of the transport pipe.
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JPS61114903A (en) * 1984-11-06 1986-06-02 三菱重工業株式会社 Dust vacuum transporter

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61114903A (en) * 1984-11-06 1986-06-02 三菱重工業株式会社 Dust vacuum transporter

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