JPH1085712A - Vacuum carrying and drying device for garbage - Google Patents

Vacuum carrying and drying device for garbage

Info

Publication number
JPH1085712A
JPH1085712A JP8239265A JP23926596A JPH1085712A JP H1085712 A JPH1085712 A JP H1085712A JP 8239265 A JP8239265 A JP 8239265A JP 23926596 A JP23926596 A JP 23926596A JP H1085712 A JPH1085712 A JP H1085712A
Authority
JP
Japan
Prior art keywords
vacuum
garbage
dryer
drying apparatus
drying
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
JP8239265A
Other languages
Japanese (ja)
Other versions
JP3209322B2 (en
Inventor
Toshiyuki Hino
俊之 日野
Nagao Yokota
長雄 横田
Nobuyuki Tani
信幸 谷
Yasunori Ito
康則 伊藤
Hideo Iwaki
秀夫 岩城
Susumu Sato
佐藤  進
Takahiro Sato
隆裕 佐藤
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.)
Kajima Corp
Original Assignee
Kajima Corp
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 Kajima Corp filed Critical Kajima Corp
Priority to JP23926596A priority Critical patent/JP3209322B2/en
Publication of JPH1085712A publication Critical patent/JPH1085712A/en
Application granted granted Critical
Publication of JP3209322B2 publication Critical patent/JP3209322B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

Landscapes

  • Processing Of Solid Wastes (AREA)
  • Drying Of Solid Materials (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a vacuum carrying and drying device for garbage combining the carrying and drying operation of gargage rationally. SOLUTION: Discharge outlets of crushers 1 for turning garbage into slurry are connected with piping 4, and the lower end of the piping is connected with a vacuum drier 6 with a drier inlet valve 5. Garbage slurry discharged out of the crushers 1 by the negative pressure of the vacuum drier 6 is sucked into the vacuum drier 6 and carried. The water content in the vaccum drier 6 is evaporated under the pressure reduced by a compressor 7 to dry the garbage in the vacuum drier 6. Preferably a plurality of crushers 1 with crusher outlet valves 3 on their discharge outlets are connected with the upstream side of the drier inlet valve 5 of the piping 4.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は生ごみの真空搬送乾燥装
置に関し、とくにスラリー状の生ごみを真空により搬送
及び乾燥する搬送乾燥装置に関する。本発明による生ご
みの真空搬送乾燥装置は、とくにショッピングセンター
のレストラン等における厨芥処理、集合住宅における各
戸の厨芥処理、給食センター等における生ごみの集中処
理、食品工場等における生ごみの集中処理、汚泥の搬送
とその乾燥、し尿の搬送と乾燥処理などに適する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a vacuum conveying and drying apparatus for garbage, and more particularly to a conveying and drying apparatus for conveying and drying slurry-like garbage by vacuum. Vacuum conveying and drying apparatus for garbage according to the present invention, especially garbage processing in restaurants and the like of shopping centers, garbage processing of each house in apartment houses, intensive processing of garbage in food service centers and the like, intensive processing of garbage in food factories, Suitable for transporting and drying sludge, transporting and drying human waste.

【0002】[0002]

【従来の技術】都市化の進展に伴い、厨芥等の生ごみの
処理が問題化している。生ごみは、まず非衛生的である
ため人手による取扱や処理が好まれず、また生ごみは腐
敗し易いので、一日以上貯蔵するには冷蔵庫による低温
貯蔵が必要とされる。実際に、輸送時には腐敗汚水によ
る臭気や、周囲汚損等の問題を生じ、さらに焼却処理時
には水分が多いために多量の石油等の助燃材を必要とす
る。
2. Description of the Related Art With the progress of urbanization, disposal of garbage such as kitchen garbage has become a problem. Since garbage is unsanitary and is not favored for manual handling and disposal, and garbage is easily rotted, it is necessary to store it in a refrigerator at a low temperature for storage for more than one day. Actually, problems such as odor due to putrefactive sewage and contamination of surroundings occur during transportation, and a large amount of moisture is required during incineration treatment, so that a large amount of an auxiliary material such as petroleum is required.

【0003】下水道の完備した米国等では、家庭の台所
にディスポーザ(生ごみ粉砕器)が設備され、生ごみを
破砕して下水に流して処理している。我が国ではディス
ポーザの使用は禁止されているが、これは下水処理の負
荷が極端に増加するものと見込まれるためである。ただ
し、排水処理施設の完備した建物では、我が国でも生ご
み粉砕器と配管輸送が図3及び図4に示すような方式で
使われることがある。
[0003] In the United States and other countries equipped with a sewage system, a disposer (garbage crusher) is installed in a home kitchen, and garbage is crushed and discharged into sewage for treatment. The use of disposers is banned in Japan, because the burden of sewage treatment is expected to increase significantly. However, in a building equipped with a wastewater treatment facility, garbage crushers and pipe transportation may be used in Japan as shown in Figs. 3 and 4.

【0004】図3(A)は、自然流下式を示し、ディスポ
ーザ30及びシンク31からの流出物を上下方向の配管によ
り固液分離器32へ流下させ、その固液分離器32において
雑排水と固形の厨芥とに分離する。図3(B)は、ポンプ
圧送式であって、ディスポーザ30からの流出物を破砕圧
送装置33により配管を介して固液分離器32へ送出し、水
と固形物とに分離する。図3(C)は、ポンプ圧送循環式
であって、ディスポーザ30からの流出物をポンプ34によ
り配管を介してウォータープレス35へ送って固形厨芥を
分離すると共に、雑排水の全部又は一部を補給水槽36の
水に代えて又はこの水に加えてポンプPによりディスポ
ーザ30へ戻し、循環使用する。図4(A)は、真空搬送式
であって、投入口41に投入された生ごみは真空ポンプ39
の運転により配管内を流下し、気液分離装置38を経由す
る。ここで気体は真空ポンプ39により排出され、残った
液状物を固液分離器32へ送出し、水と固形物とに分離す
る。図4(B)の方式では、各ディスポーザ30に小型貯留
タンク29を設けてディスポーザ30の流出物を短期的にこ
こに蓄える。配管内は常時真空ポンプ39により真空を保
持しており、開閉弁40の開により厨芥を気液分離装置38
へ移送する。
FIG. 3 (A) shows a natural flow type in which the effluent from the disposer 30 and the sink 31 is caused to flow down to a solid-liquid separator 32 through a vertical pipe, and the solid-liquid separator 32 removes miscellaneous wastewater. Separate into solid kitchen waste. FIG. 3 (B) shows a pump pressure feeding system in which the effluent from the disposer 30 is sent to a solid-liquid separator 32 via a pipe by a crushing / pressure feeding device 33 to be separated into water and solid matter. FIG. 3 (C) shows a pump-feeding circulation type in which the effluent from the disposer 30 is sent to a water press 35 via a pipe by a pump 34 to separate solid kitchen garbage, and all or part of the gray water is discharged. Instead of or in addition to the water in the makeup water tank 36, the water is returned to the disposer 30 by the pump P and used for circulation. FIG. 4A shows a vacuum transfer type, in which garbage put into the inlet 41 is supplied by a vacuum pump 39.
With the operation, the gas flows down in the pipe and passes through the gas-liquid separator 38. Here, the gas is discharged by the vacuum pump 39, and the remaining liquid is sent to the solid-liquid separator 32, where it is separated into water and solids. In the system shown in FIG. 4B, a small storage tank 29 is provided in each disposer 30, and the effluent from the disposer 30 is stored here for a short time. The vacuum is constantly maintained in the piping by a vacuum pump 39, and the kitchen waste is separated by a gas-liquid separation device 38 by opening an on-off valve 40.
Transfer to

【0005】[0005]

【発明が解決しようとする課題】しかし、図3及び図4
の方式は、生ごみを中央へ搬送して固液分離するもの
の、そのようにして固液分離した後の固形厨芥はやはり
生ごみであって腐敗し易いため、冷蔵保存の必要があ
り、分離された雑排水も有機物等を濃厚に含んでおり十
分な排水処理を必要とする。即ち、従来の生ごみの配管
輸送方式は、単に配管輸送を提供するのみであって生ご
み自体の腐敗防止やスラリー化用の水分についての排水
処理の問題を殆ど解決していない。
However, FIG. 3 and FIG.
In this method, garbage is conveyed to the center for solid-liquid separation, but solid kitchen waste after solid-liquid separation is still garbage and easily rots. Drained wastewater also contains rich organic matter and requires sufficient wastewater treatment. In other words, the conventional garbage pipe transport system merely provides pipe transport, and hardly solves the problems of decay of the garbage itself and wastewater treatment of water for slurrying.

【0006】従って、本発明の目的は、生ごみの輸送と
乾燥処理とを合理的に組合わせて行なう方式の生ごみの
真空搬送乾燥装置を提供するにある。
SUMMARY OF THE INVENTION Accordingly, an object of the present invention is to provide a vacuum transporting and drying apparatus for garbage in which garbage is transported and dried in a reasonable combination.

【0007】[0007]

【課題を解決するための手段】図1の実施例において、
本発明の生ごみの真空搬送乾燥装置は、生ごみスラリー
化用の粉砕器1、及び配管4でその粉砕器1の吐出口と
連通した乾燥機入口弁5付き真空乾燥機6を備えてなる
ものである。好ましくは、粉砕器弁3が吐出口に設けら
れた複数の粉砕器1を配管4の乾燥器入口弁5の上流側
に接続する。
In the embodiment shown in FIG.
The garbage vacuum transport drying apparatus of the present invention comprises a crusher 1 for making garbage slurry, and a vacuum dryer 6 with a dryer inlet valve 5 communicating with a discharge port of the crusher 1 through a pipe 4. Things. Preferably, the plurality of pulverizers 1 provided with the pulverizer valves 3 at the discharge ports are connected to the pipe 4 on the upstream side of the dryer inlet valve 5.

【0008】[0008]

【発明の実施の形態】図1の実施例においては、粉砕器
1は生ごみを水栓(図省略)からの水と混合・粉砕して
生ごみスラリーとして吐き出す。真空乾燥機6は真空圧
を発生し、乾燥機入口弁5を開いている時は、配管4に
その真空を及ぼし、粉砕機1で粉砕された生ごみスラリ
ーを圧力差により配管4を介して真空乾燥機6へ吸引す
ることにより、粉砕器1から真空乾燥機6への生ごみ輸
送を行う。ここで乾燥機入口弁5を閉じ、真空乾燥機6
の真空を維持すれば、水分は蒸発し生ごみの固形分のみ
が乾燥ごみとして残る。図示例ではこの乾燥ごみが乾燥
ごみ排出口14から抜出される。こうして、生ごみの乾燥
処理が行われ、大幅な減量がなされる。
DESCRIPTION OF THE PREFERRED EMBODIMENTS In the embodiment of FIG. 1, a crusher 1 mixes and crushes garbage with water from a faucet (not shown) and discharges the garbage as a garbage slurry. The vacuum dryer 6 generates a vacuum pressure, applies the vacuum to the pipe 4 when the dryer inlet valve 5 is open, and causes the garbage slurry pulverized by the pulverizer 1 to pass through the pipe 4 by a pressure difference. By sucking into the vacuum dryer 6, garbage is transported from the crusher 1 to the vacuum dryer 6. Here, the dryer inlet valve 5 is closed and the vacuum dryer 6
If the vacuum is maintained, the water evaporates and only the solid matter of the garbage remains as dry garbage. In the illustrated example, the dried waste is extracted from the dried waste outlet 14. In this way, the garbage is dried, and the weight is significantly reduced.

【0009】図1の実施例では、真空乾燥機6内の空気
及び真空蒸発した水蒸気を圧縮機7により抜出して圧縮
し、高温となった水蒸気を凝縮機8で凝縮させて真空乾
燥機6の外へ抜出している。乾燥生ごみは軽量化されて
取扱が容易であり、コンポスト材料や燃料(RDF)等
として広くリサイクル用に利用できる。真空乾燥機6か
ら抜出した水は蒸留水であって原則的に排水処理は不要
であり、再利用も可能である。
In the embodiment of FIG. 1, the air in the vacuum dryer 6 and the vapor evaporated in a vacuum are extracted and compressed by a compressor 7, and the high-temperature steam is condensed by a condenser 8 and Pulled out. Dried garbage is light in weight and easy to handle, and can be widely used for recycling as compost material, fuel (RDF), and the like. The water extracted from the vacuum dryer 6 is distilled water, and does not require wastewater treatment in principle, and can be reused.

【0010】従って、本発明の目的である「生ごみの輸
送と乾燥処理とを合理的に組合わせた生ごみの真空搬送
乾燥装置」の提供が達成される。
[0010] Accordingly, the object of the present invention is to provide a "garbage vacuum transfer and drying apparatus which rationally combines garbage transport and drying treatment".

【0011】[0011]

【実施例】図1の実施例では、粉砕器弁3が吐出口に設
けられた複数の粉砕器1を、例えば複数戸の台所へ戸別
に設ける。また、各粉砕器1と粉砕器弁3との間に短期
貯留容器2を設けている。真空乾燥機6を集中処理装置
として、建物の特定の場所、例えば廃棄物処理室に設け
る。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS In the embodiment shown in FIG. 1, a plurality of pulverizers 1 provided with a pulverizer valve 3 at a discharge port are provided, for example, in a plurality of kitchens. Further, a short-term storage container 2 is provided between each crusher 1 and the crusher valve 3. The vacuum dryer 6 is provided as a centralized processing device at a specific place in a building, for example, a waste treatment room.

【0012】各粉砕器1を配管4により真空乾燥機6へ
結合する。配管4は鋼管、銅管、塩ビ管等であり、真空
乾燥機6側の端部に乾燥器入口弁5が設けられている。
図示例の複数の粉砕器1を横に連通する部分の配管4の
両端には、配管掃除用の空気吸込み口があり、それぞれ
開閉弁10を介して消音器11が取付けられている。この生
ごみの真空搬送乾燥装置の実施例の動作を搬送運転と乾
燥運転とに分けて説明する。
Each crusher 1 is connected to a vacuum dryer 6 by a pipe 4. The pipe 4 is a steel pipe, a copper pipe, a PVC pipe, or the like, and a dryer inlet valve 5 is provided at an end on the vacuum dryer 6 side.
At both ends of the pipe 4 at the portion where the plurality of crushers 1 of the illustrated example communicate laterally, air suction ports for pipe cleaning are provided, and silencers 11 are attached via opening / closing valves 10 respectively. The operation of this embodiment of the vacuum transfer and drying apparatus for garbage will be described separately for a transfer operation and a drying operation.

【0013】[搬送運転]生ごみは、粉砕器1によって
細粒化され同時に水と混合されてスラリー状とされ、短
期貯留容器2に貯留される。一方、真空乾燥機6は、真
空容器6aとこれに接続された圧縮機7又は真空ポンプ16
(図2)とを有し、その圧縮機7又は真空ポンプ16によ
って真空容器6aは常時例えば0.5気圧程度の負圧に保た
れ、乾燥機入口弁5は開放状態に保たれる。
[Transportation Operation] The garbage is pulverized by a pulverizer 1 and simultaneously mixed with water to form a slurry, which is stored in a short-term storage container 2. On the other hand, the vacuum dryer 6 includes a vacuum vessel 6a and a compressor 7 or a vacuum pump 16 connected thereto.
(FIG. 2), the vacuum vessel 6a is always kept at a negative pressure of, for example, about 0.5 atm by the compressor 7 or the vacuum pump 16, and the dryer inlet valve 5 is kept open.

【0014】短期貯留容器2に所定量の生ごみスラリー
が貯留された時に粉砕器弁3を開ければ、その生ごみス
ラリーは圧力差により真空乾燥機6へ吸込まれて輸送さ
れ、その中に貯留される。自動化のために、短期貯留容
器2の中に例えば水位センサー等の生ごみスラリー量検
出手段(図示せず)を設け、粉砕器弁3を電動弁として
前記スラリー量検出手段の出力により粉砕器弁3が自動
的に開かれるようにしてもよい。
If a crusher valve 3 is opened when a predetermined amount of garbage slurry is stored in the short-term storage container 2, the garbage slurry is sucked into the vacuum dryer 6 by a pressure difference and transported, and is stored therein. Is done. For automation, a garbage slurry amount detecting means (not shown) such as a water level sensor is provided in the short-term storage container 2, and the crusher valve 3 is used as an electric valve and the crusher valve is output by the slurry amount detecting means. 3 may be automatically opened.

【0015】[乾燥運転]生ごみスラリーを貯留後の真
空乾燥機6では、例えば電熱ヒータ(図省略)等により
予熱した後に圧縮機7を運転し、水分を真空蒸発(例え
ば90゜C、70kPa)させる。ただし、予熱法は本発明の主
目的ではない。発生した水蒸気は、圧縮機7で圧縮さ
れ、真空容器6aの外周に設けた凝縮器8で凝縮される
(例えば110゜C、140kPa)。この際の凝縮潜熱で、真空
容器内の廃棄物を加熱する。凝縮後の温水は、スチーム
トラップ9から排出される。この際、乾燥機入口弁5は
閉じておく。
[Drying operation] In the vacuum dryer 6 after storing the garbage slurry, the compressor 7 is operated after preheating by, for example, an electric heater (not shown) or the like, and the moisture is vacuum evaporated (for example, 90 ° C, 70 kPa). ). However, the preheating method is not the main object of the present invention. The generated steam is compressed by the compressor 7 and condensed by the condenser 8 provided on the outer periphery of the vacuum vessel 6a (for example, 110 ° C., 140 kPa). The waste in the vacuum vessel is heated by the latent heat of condensation at this time. The hot water after the condensation is discharged from the steam trap 9. At this time, the dryer inlet valve 5 is closed.

【0016】図1の実施例の真空乾燥機6は、モータ12
により駆動される回転羽根13からなる攪拌器を有し、生
ごみスラリーの水分蒸発の促進を図る。乾燥運転を夜間
に行うことにより、搬送運転と乾燥運転とが重なるのを
避けることができる。しかし、乾燥運転中であっても搬
送運転をすることは可能である。生ごみと共に吸込まれ
た空気は、凝縮器8内で凝縮しないので、抽気弁(図示
せず)を設けて排出する。
The vacuum dryer 6 of the embodiment shown in FIG.
And a stirrer composed of rotating blades 13 driven by the garbage to promote the evaporation of water from the garbage slurry. By performing the drying operation at night, the transport operation and the drying operation can be prevented from overlapping. However, it is possible to perform the transport operation even during the drying operation. Since the air sucked in with the garbage does not condense in the condenser 8, the air is exhausted by providing a bleed valve (not shown).

【0017】規模の大きな設備では、真空乾燥機6を複
数台設置し、配管4の中間部に切替弁(図示せず)を設
けて、搬送運転モードの真空乾燥機6と乾燥運転モード
の真空乾燥機6とを並列にして同時運転することも可能
である。真空乾燥機6としては、水蒸気再圧縮式真空乾
燥機(特願平7-282750号参照)又はそれと同等のエネル
ギー消費量の少ないものが望ましいが、これらのものに
限定されない。例えば図2のように、真空容器6a内部を
凝縮器8を介して外側の真空ポンプ16で減圧することも
可能である。図2の実施例では、配管により真空容器6a
へ供給され、その真空容器6aはボイラー22によって加熱
される。凝縮器8で凝縮した水分は、レシーバタンク23
に集められ、気液分離を受けた後抜出しポンプP2により
外部へ送出される。真空ポンプ16によって引出された空
気は気液分離器24を介して外部へ排出される。凝縮器8
を冷却するため、冷却塔25で放熱する冷却装置が設けら
れている。
In a large-scale facility, a plurality of vacuum dryers 6 are provided, and a switching valve (not shown) is provided at an intermediate portion of the pipe 4, so that the vacuum dryer 6 in the transport operation mode and the vacuum dryer in the drying operation mode are provided. It is also possible to operate the dryer 6 in parallel and operate simultaneously. The vacuum dryer 6 is desirably a steam recompression vacuum dryer (see Japanese Patent Application No. 7-282750) or a device with low energy consumption equivalent thereto, but is not limited thereto. For example, as shown in FIG. 2, the pressure inside the vacuum vessel 6a can be reduced by the outer vacuum pump 16 via the condenser 8. In the embodiment shown in FIG.
And the vacuum vessel 6a is heated by the boiler 22. The water condensed in the condenser 8 is transferred to the receiver tank 23
After being subjected to gas-liquid separation, it is sent to the outside by a withdrawal pump P2. The air drawn by the vacuum pump 16 is discharged to the outside via the gas-liquid separator 24. Condenser 8
A cooling device that radiates heat in the cooling tower 25 is provided to cool the cooling tower.

【0018】[0018]

【発明の効果】以上説明したように本発明の生ごみの真
空搬送乾燥装置は、生ごみスラリーの搬送及び乾燥を真
空乾燥機によって行うので、次の顕著な効果を奏する。 (イ)生ごみの搬送と乾燥処理とを、一台の生ごみの真空
搬送乾燥装置により合理的に組合わせて効率よく行なう
ことができる。 (ロ)生ごみを真空吸引で搬送するので、自然流下やポン
プ圧送に比して搬送水の使用量が少なくてよい。 (ハ)真空処理のため臭気対策が容易であり、例えば圧縮
機の吐出側に脱臭器を設けることにより対処できる。
As described above, the vacuum transport and drying apparatus for garbage according to the present invention has the following remarkable effects because the garbage slurry is transported and dried by the vacuum dryer. (A) The transfer and drying of garbage can be rationally and efficiently performed by a single vacuum transfer and drying apparatus for garbage. (B) Since garbage is transported by vacuum suction, the amount of transport water used may be smaller than that of natural flow or pumping. (C) Odor countermeasures are easy because of the vacuum treatment, and can be dealt with, for example, by providing a deodorizer on the discharge side of the compressor.

【0019】(ニ)真空乾燥機から抜出される水は蒸留水
であり、原則的に排水処理は不要である。 (ホ)乾燥後の生ごみは、コンポスト化や燃料化等により
広くリサイクル過程に組込むことができ、取扱いが容易
である。 (ヘ)水蒸気再圧縮式真空乾燥機(特願平7-282750号参
照)等の高エネルギー効率の真空乾燥機を使えば、社会
的・地球環境的に望ましい廃棄物処理方法を実現するこ
とができる。 (ト)固液分離器が不要である。
(D) The water extracted from the vacuum dryer is distilled water, and wastewater treatment is basically unnecessary. (E) The garbage after drying can be widely incorporated into the recycling process by composting or fueling, and is easy to handle. (F) A high energy-efficiency vacuum dryer such as a steam recompression vacuum dryer (see Japanese Patent Application No. 7-282750) can realize a socially and environmentally desirable waste treatment method. it can. (G) No solid-liquid separator is required.

【0020】(チ)乾燥後の生ごみは腐敗し難いので、冷
蔵庫で保存する必要がない。 (リ)乾燥後のごみは水分がなくなり減量化(乾燥前の1/
4〜1/10)されているため、外部委託費をその分だけ節
約できる。 (ヌ)真空乾燥機はある程度の容積をもっているので、蓄
圧作用を期待することができる。即ち、圧縮機(又は真
空ポンプ)が小型でも、十分長い時間に亘り真空吸引力
を発生できる。 (ル)いわゆる生ごみ以外にも、スラリー化可能なもの、
例えば汚泥やし尿等の輸送と乾燥処理に利用することが
できる。
(H) Since the garbage after drying is hard to perish, it is not necessary to store it in a refrigerator. (I) Waste after drying has lost moisture and is reduced in weight (1/1 before drying)
4 to 1/10), so the outsourcing costs can be saved accordingly. (V) Since the vacuum dryer has a certain volume, a pressure accumulation function can be expected. That is, even if the compressor (or the vacuum pump) is small, the vacuum suction force can be generated for a sufficiently long time. (R) In addition to so-called garbage, those that can be slurried,
For example, it can be used for transporting sludge and human waste and drying.

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

【図1】は本発明の一実施例の構成を示す説明図であ
る。
FIG. 1 is an explanatory diagram showing a configuration of an embodiment of the present invention.

【図2】は他の実施例を示す説明図である。FIG. 2 is an explanatory view showing another embodiment.

【図3】は従来のスラリー輸送の自然流下及び圧送方式
を示す説明図である。
FIG. 3 is an explanatory diagram showing a conventional natural flow and slurry feeding method of slurry transportation.

【図4】は従来のスラリー輸送の真空方式を示す説明図
である。
FIG. 4 is an explanatory view showing a conventional vacuum system for slurry transportation.

【符号の説明】[Explanation of symbols]

1…粉砕器 2…短期貯留容器 3…粉砕器弁 4…配管 5…乾燥機入口弁 6…真空乾燥機 7…圧縮機 8…凝縮器 9…スチームトラップ 10…開閉弁 11…消音器 12…モータ 13…回転羽根 14…乾燥ごみ排出口 16…真空ポンプ 22…ボイラー 23…レシーバタンク 24…分離器 25…冷却塔 29…小型貯留タンク 30…ディスポーザ 31…シンク 32…固液分離器 33…破砕圧送装置 34…ポンプ 35…ウォータープレス 36…補給水槽 38…気液分離装置 39…真空ポンプ 40…開閉弁 41…投入口。 DESCRIPTION OF SYMBOLS 1 ... Pulverizer 2 ... Short-term storage container 3 ... Pulverizer valve 4 ... Piping 5 ... Dryer inlet valve 6 ... Vacuum dryer 7 ... Compressor 8 ... Condenser 9 ... Steam trap 10 ... On-off valve 11 ... Muffler 12 ... Motor 13 ... Rotating blade 14 ... Dry waste outlet 16 ... Vacuum pump 22 ... Boiler 23 ... Receiver tank 24 ... Separator 25 ... Cooling tower 29 ... Small storage tank 30 ... Disposer 31 ... Sink 32 ... Solid-liquid separator 33 ... Crushing Pumping device 34 ... Pump 35 ... Water press 36 ... Replenishing water tank 38 ... Gas-liquid separator 39 ... Vacuum pump 40 ... On-off valve 41 ... Inlet.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 伊藤 康則 東京都港区元赤坂一丁目2番7号 鹿島建 設株式会社内 (72)発明者 岩城 秀夫 東京都港区元赤坂一丁目2番7号 鹿島建 設株式会社内 (72)発明者 佐藤 進 東京都調布市飛田給二丁目19番1号 鹿島 建設株式会社技術研究所内 (72)発明者 佐藤 隆裕 東京都調布市飛田給二丁目19番1号 鹿島 建設株式会社技術研究所内 ────────────────────────────────────────────────── ─── Continuing on the front page (72) Inventor Yasunori Ito 1-2-7 Moto-Akasaka, Minato-ku, Tokyo Kashima Construction Co., Ltd. (72) Inventor Hideo Iwaki 1-2-7 Moto-Akasaka, Minato-ku, Tokyo No. Kashima Construction Co., Ltd. (72) Inventor Susumu Sato 2-191-1, Tobita-Shi, Chofu-shi, Tokyo Kashima Construction Co., Ltd. Kashima Construction Co., Ltd.

Claims (7)

【特許請求の範囲】[Claims] 【請求項1】生ごみスラリー化用粉砕器、及び配管で前
記粉砕器の吐出口と連通した乾燥機入口弁付き真空乾燥
機を備えてなる生ごみの真空搬送乾燥装置。
An apparatus for vacuum conveying and drying garbage, comprising: a crusher for making garbage slurry; and a vacuum dryer with a dryer inlet valve connected to a discharge port of the crusher by piping.
【請求項2】請求項1の真空搬送乾燥装置において、粉
砕器弁が前記吐出口に設けられた複数の前記スラリー化
用粉砕器を前記配管の乾燥機入口弁の上流側に接続して
なる生ごみの真空搬送乾燥装置。
2. A vacuum conveying and drying apparatus according to claim 1, wherein a plurality of said pulverizers provided at said discharge port are connected to a plurality of said pulverizers upstream of a dryer inlet valve of said pipe. Vacuum transfer drying equipment for garbage.
【請求項3】請求項2の真空搬送乾燥装置において、各
前記粉砕器の前記吐出口と粉砕器弁との間に短期貯留容
器を設けてなる生ごみの真空搬送乾燥装置。
3. The vacuum transfer drying apparatus for garbage according to claim 2, wherein a short-term storage container is provided between said discharge port of each of said pulverizers and a pulverizer valve.
【請求項4】請求項1から3までの何れかの真空搬送乾
燥装置において、前記真空乾燥機に、前記乾燥機入口弁
へ接続した真空容器、該真空容器の気体を引抜き圧縮す
る圧縮機、及び該圧縮機の吐出口に接続した凝縮器を設
けてなる生ごみの真空搬送乾燥装置。
4. The vacuum transfer drying apparatus according to claim 1, wherein the vacuum dryer has a vacuum vessel connected to the dryer inlet valve, a compressor for drawing and compressing the gas in the vacuum vessel, And a vacuum transfer and drying apparatus for garbage provided with a condenser connected to a discharge port of the compressor.
【請求項5】請求項1から3までの何れかの真空搬送乾
燥装置において、前記真空乾燥機に、前記乾燥機入口弁
へ接続した真空容器、及び凝縮器を介して該真空容器の
気体を引抜く真空ポンプを設けてなる生ごみの真空搬送
乾燥装置。
5. The vacuum transfer drying apparatus according to claim 1, wherein the gas in the vacuum vessel is supplied to the vacuum dryer through a vacuum vessel connected to the dryer inlet valve and a condenser. Vacuum transfer and drying device for garbage provided with a vacuum pump to pull out.
【請求項6】請求項4又は5の真空搬送乾燥装置におい
て、前記凝縮器を真空容器の周壁に取付け、前記凝縮器
からの放熱により真空容器を加熱してなる生ごみの真空
搬送乾燥装置。
6. The vacuum transfer drying apparatus for garbage according to claim 4, wherein said condenser is mounted on a peripheral wall of a vacuum vessel, and said vacuum vessel is heated by radiating heat from said condenser.
【請求項7】請求項4、5又は6の真空搬送乾燥装置に
おいて、前記真空容器の内部に攪拌手段を設けてなる生
ごみの真空搬送乾燥装置。
7. The vacuum transport drying apparatus for garbage according to claim 4, wherein a stirring means is provided inside said vacuum vessel.
JP23926596A 1996-09-10 1996-09-10 Vacuum transfer drying equipment for garbage Expired - Fee Related JP3209322B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP23926596A JP3209322B2 (en) 1996-09-10 1996-09-10 Vacuum transfer drying equipment for garbage

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP23926596A JP3209322B2 (en) 1996-09-10 1996-09-10 Vacuum transfer drying equipment for garbage

Publications (2)

Publication Number Publication Date
JPH1085712A true JPH1085712A (en) 1998-04-07
JP3209322B2 JP3209322B2 (en) 2001-09-17

Family

ID=17042200

Family Applications (1)

Application Number Title Priority Date Filing Date
JP23926596A Expired - Fee Related JP3209322B2 (en) 1996-09-10 1996-09-10 Vacuum transfer drying equipment for garbage

Country Status (1)

Country Link
JP (1) JP3209322B2 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007271222A (en) * 2006-03-31 2007-10-18 Osaka Gas Co Ltd Vacuum drying device
JP2007271225A (en) * 2006-03-31 2007-10-18 Osaka Gas Co Ltd Vacuum drying device
US8365433B2 (en) 2007-03-23 2013-02-05 Kunitomo Kankyo Plant Co., Ltd. Apparatus and method for treating organic waste and organic material obtained by the treatment method
CN109570193A (en) * 2018-11-26 2019-04-05 山东大学 Kitchen garbage vacuum collecting is crushed specification processing system and method

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007271222A (en) * 2006-03-31 2007-10-18 Osaka Gas Co Ltd Vacuum drying device
JP2007271225A (en) * 2006-03-31 2007-10-18 Osaka Gas Co Ltd Vacuum drying device
US8365433B2 (en) 2007-03-23 2013-02-05 Kunitomo Kankyo Plant Co., Ltd. Apparatus and method for treating organic waste and organic material obtained by the treatment method
CN109570193A (en) * 2018-11-26 2019-04-05 山东大学 Kitchen garbage vacuum collecting is crushed specification processing system and method

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