JPH08132008A - Organic waste carbonizing treatment device - Google Patents

Organic waste carbonizing treatment device

Info

Publication number
JPH08132008A
JPH08132008A JP6300252A JP30025294A JPH08132008A JP H08132008 A JPH08132008 A JP H08132008A JP 6300252 A JP6300252 A JP 6300252A JP 30025294 A JP30025294 A JP 30025294A JP H08132008 A JPH08132008 A JP H08132008A
Authority
JP
Japan
Prior art keywords
organic waste
processing container
compressor
nitrogen gas
temperature
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
JP6300252A
Other languages
Japanese (ja)
Other versions
JP2736750B2 (en
Inventor
Masashige Nishi
正成 西
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 JP6300252A priority Critical patent/JP2736750B2/en
Publication of JPH08132008A publication Critical patent/JPH08132008A/en
Application granted granted Critical
Publication of JP2736750B2 publication Critical patent/JP2736750B2/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
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A40/00Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/10Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
    • Y02A40/20Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses

Abstract

PURPOSE: To provide an organic waste carbonizing treatment device in which since water contained in organic waste is evaporated and also carbonized to sharply reduce weight thereof, disposal thereof is easy, and which is widely applied to organic waste which has been hard to decompose and ferment and is also used in facilities in a city area because it generates no malodor. CONSTITUTION: In a treating vessel 1 for housing thermophile which absorb a nitrogen content and generate heat by itself and organic waste such as garbage 10 to be treated, an agitating device 2 is installed, and also a compressor 4 for feeding gaseous nitrogen into the treating vessel is installed. A controller tar controlling the compressor 4 to adjust the feed quantity of gaseous nitrogen, and also a temperature sensor connected to the controller are installed in the treating vessel 1.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は生ごみなど水分含有量の
多い有機廃棄物を光熱菌により炭化する装置に関するも
のである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a device for carbonizing organic waste having a high water content such as garbage by photothermal bacteria.

【0002】[0002]

【従来の技術】近年、ホテルやレストラン、あるいは給
食センターの厨房や食品加工工場から出る生ごみは腐敗
し易いため、悪臭や蝿などの虫が発生して不衛生であ
り、その処分は焼却や埋め立てにより行なわれている。
しかしながら、野菜や肉、魚などの調理の際に出る廃棄
物や食べ残しなどの生ごみは水分含有率が高いため、単
独では焼却できず、また埋め立て処分場も不足している
ことから、生ごみを排出する施設で各自で処分すること
が望ましい。
2. Description of the Related Art In recent years, since kitchen garbage and food processing plants in hotels, restaurants, and food service centers are easily decomposed, bad odors and insects such as flies are generated, which is unsanitary. It is done by landfill.
However, wastes such as vegetables, meat, and fish that are produced during cooking and food waste such as leftover foods cannot be incinerated alone because of high water content, and landfill disposal sites are insufficient. It is desirable to dispose of the waste yourself at the facility that discharges it.

【0003】このため大量に生ごみが排出される施設で
使用できる処理装置が種々開発されており、例えば生ご
みを発酵分解して堆肥を作る装置が最も普及している。
この発酵分解方式は、微生物を利用して生ごみを発酵さ
せて堆肥化するもので、土壤改良剤として有効利用でき
るが、分解に長時間かかり、減容量が少なく、悪臭の発
生などの問題があり、しかも製造された堆肥を製品とし
て販売するための梱包や、保管、輸送など煩雑な手間が
係る上、販売するルートの確立が難しいなどの問題があ
った。特に豆腐の製造工場から出るオカラはレシチンを
含むため分解発酵しにくく堆肥化するのが困難であり、
現状では大部分が埋め立て処分されている。
For this reason, various treatment apparatuses have been developed that can be used in facilities that discharge a large amount of food waste, and, for example, an apparatus for fermenting and decomposing food waste to produce compost is the most popular.
This fermentation decomposition method uses microorganisms to ferment food waste and compost it, and it can be effectively used as a soil improvement agent, but it takes a long time to decompose, there is little volume reduction, and there are problems such as the generation of foul odors. In addition, there is a problem in that it is difficult to establish a sales route due to complicated labor such as packing, storage and transportation for selling the manufactured compost as a product. In particular, the okara from the tofu manufacturing plant contains lecithin and is difficult to decompose and ferment, making it difficult to compost,
Currently, most of the landfill is landfilled.

【0004】[0004]

【発明が解決しようとする課題】本発明は上記問題点を
除去し、有機廃棄物の水分を蒸発させると共に炭化させ
て大幅に減量できるので、処分も容易で、従来、分解発
酵しにくかった有機廃棄物にも広く適用することがで
き、しかも悪臭の発生もないので市街地にある施設でも
使用できる有機廃棄物炭化処理装置を提供するものであ
る。
SUMMARY OF THE INVENTION The present invention eliminates the above-mentioned problems, and can evaporate the water content of an organic waste and carbonize it to a great extent to reduce the volume significantly. The present invention provides an organic waste carbonization treatment apparatus that can be widely applied to wastes and does not generate a foul odor and can be used even in facilities in urban areas.

【0005】[0005]

【課題を解決するための手段】本発明の請求項1記載の
有機廃棄物炭化処理装置は、窒素分を吸収して自力発熱
する光熱菌と、処理される有機廃棄物とを入れる処理容
器内に、攪拌装置を設けると共に、窒素ガスを処理容器
内に供給するコンプレッサーを設け、このコンプレッサ
ーを制御して窒素ガス供給量を調整する制御装置を設け
ると共に、この制御装置に接続された温度センサーを前
記処理容器に設けたことを特徴とするものである。更に
請求項2記載の発明は、窒素ガスを処理容器内に供給す
るガス供給管にヒーターを取付けたことを特徴とするも
のである。
The apparatus for carbonizing organic waste according to claim 1 of the present invention is provided with a photothermia which absorbs nitrogen and generates heat by itself, and an organic waste to be treated. In addition to the stirrer, a compressor for supplying nitrogen gas into the processing container is provided, and a controller for controlling the compressor to adjust the nitrogen gas supply amount is provided, and a temperature sensor connected to the controller is provided. It is provided in the processing container. Furthermore, the invention according to claim 2 is characterized in that a heater is attached to a gas supply pipe for supplying nitrogen gas into the processing container.

【0006】[0006]

【作用】本発明の炭化処理装置により有機廃棄物を炭化
処理する場合、先ず処理容器内に窒素分を吸収して自力
発熱する光熱菌を混ぜた菌床を入れる。次に制御装置の
温度設定を行なってから処理容器内に生ごみや食品廃棄
物などの有機廃棄物を投入する。この後、攪拌装置を運
転して光熱菌を混ぜた菌床と有機廃棄物を撹拌しながら
同時にコンプレッサーを運転し、ここから窒素ガスを含
んでいる空気をヒーターで加熱しながら有機廃棄物に供
給する。
When the organic waste is carbonized by the carbonization apparatus of the present invention, first, a bed of a mixture of photothermal bacteria which absorbs nitrogen and self-heats is put in a processing container. Next, after setting the temperature of the control device, organic waste such as food waste and food waste is put into the processing container. After this, the agitator is operated to agitate the fungal bed mixed with photothermia and the organic waste, and at the same time the compressor is operated to supply the nitrogen-containing air to the organic waste while heating it with a heater. To do.

【0007】このように加熱した空気を供給しながら攪
拌装置で有機廃棄物を撹拌すると、ここに含まれる光熱
菌は空気の4分の3を占める窒素ガスを吸収して自力発
熱して温度が上昇してくると水蒸気やガスが多量に蒸発
し、蒸発した水蒸気やガスは外部に排出される。更に温
度が上昇して90℃を越えると炭化が始まる。この後、更
に温度が上昇して、設定した温度になると温度センサー
がこれを検知して、その測定信号を制御装置に出力し、
ここから停止信号がコンプレッサーに出力されて停止
し、空気の供給が遮断される。このように空気の供給が
停止すると、窒素ガスの供給がなくなるので光熱菌の発
熱が少なくなり処理容器内の温度が低下してくる。温度
が所定の温度まで低下したらこれを温度センサーで検知
して、再びコンプレッサーを運転して窒素ガスを供給し
始めると光熱菌の発熱が活発になって再び温度が上昇し
て、有機廃棄物は全て炭化して大幅に減量することがで
きる。
When the organic waste is stirred by the stirrer while supplying the heated air as described above, the photothermia contained therein absorbs the nitrogen gas which occupies three-fourths of the air and generates heat by itself to raise the temperature. As it rises, a large amount of water vapor and gas evaporate, and the vaporized water vapor and gas are discharged to the outside. When the temperature rises further and exceeds 90 ° C, carbonization begins. After this, the temperature further rises, and when the temperature reaches the set temperature, the temperature sensor detects this and outputs the measurement signal to the control device,
From here, a stop signal is output to the compressor to stop and the air supply is cut off. When the supply of air is stopped in this way, the supply of nitrogen gas is stopped, so that the heat generated by photothermia is reduced and the temperature in the processing container is lowered. When the temperature drops to the specified temperature, this is detected by the temperature sensor, and when the compressor is operated again to start supplying nitrogen gas, the heat of photothermia becomes active and the temperature rises again. All can be carbonized to significantly reduce the amount.

【0008】[0008]

【実施例】以下本発明の一実施例を図1ないし図3を参
照して詳細に説明する。図において1は処理容器、2は
処理容器1内に設けた攪拌装置、3は処理容器1内に設
けた窒素ガス噴出ノズル、4は窒素ガスを供給するコン
プレッサーである。前記処理容器1は断熱材5で形成さ
れ、キャップ部14の中央に排気管6が取付けられてい
る。また処理容器1の横には図2に示すようにリフト装
置7が設けられ、このリフト装置7は、上下方向に設け
たチエーンコンベアー8に、複数個のバケット9…を所
定の間隔で取付け、リフト装置7の底部側に生ごみ10を
貯めるストック部11が設けられ、ここに投入蓋12が取付
けられている。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described in detail below with reference to FIGS. In the figure, 1 is a processing container, 2 is a stirrer provided in the processing container 1, 3 is a nitrogen gas ejection nozzle provided in the processing container 1, and 4 is a compressor for supplying nitrogen gas. The processing container 1 is formed of a heat insulating material 5, and an exhaust pipe 6 is attached to the center of the cap portion 14. As shown in FIG. 2, a lift device 7 is provided beside the processing container 1, and the lift device 7 is provided with a plurality of buckets 9 ... A stock portion 11 for storing food waste 10 is provided on the bottom side of the lift device 7, and a loading lid 12 is attached to the stock portion 11.

【0009】またリフト装置7の上部には投入シュータ
ー13が設けられ、この投入シューター13はキャップ部14
を斜めに貫通して、バケット9で搬送されてきた生ごみ
10を処理容器1内に投入するようになっている。なお15
は投入シューター11に開閉自在に設けられた遮蔽板であ
る。またリフト装置7と反対側の処理容器1の側壁には
取出蓋16が取付けられ、この外側に排出シューター17が
設けられている。
Further, a throwing shooter 13 is provided above the lift device 7, and the throwing shooter 13 has a cap portion 14
Garbage that has been conveyed in a bucket 9 by diagonally penetrating the
10 is put into the processing container 1. 15
Is a shielding plate provided on the input shooter 11 so as to be openable and closable. A take-out lid 16 is attached to the side wall of the processing container 1 on the side opposite to the lift device 7, and a discharge shooter 17 is provided outside this.

【0010】また前記攪拌装置2は図1に示すように、
処理容器1の中央部にシャフト20が立設され、この外周
に複数枚の撹拌羽根21…が取付けられている。またシャ
フト20の下部側は処理容器1の底面を貫通して基台22に
支持されている。23はモーターで、これは減速器24に接
続され、ここに取付けたチェーンホイール25と前記シャ
フト20に取付けたチェーンホイール26とがチェーン27で
連結されている。
As shown in FIG. 1, the stirring device 2 is
A shaft 20 is erected at the center of the processing container 1, and a plurality of stirring blades 21 ... Are attached to the outer periphery of the shaft 20. The lower side of the shaft 20 penetrates the bottom surface of the processing container 1 and is supported by the base 22. Reference numeral 23 denotes a motor, which is connected to a speed reducer 24, and a chain wheel 25 attached here and a chain wheel 26 attached to the shaft 20 are connected by a chain 27.

【0011】また基台22に取付けられたコンプレッサー
4には窒素ガス供給管28が接続され、この先端は処理容
器1の底部側に導かれ、この先端部が窒素ガス噴出ノズ
ル3となっている。また窒素ガス供給管28の中間には棒
状ヒーター29が設けられている。更に処理容器1内の上
部には図2に示すように内部の温度を測定する温度セン
サー30が取付けられ、これは図示しない制御装置を介し
て前記コンプレッサー4に接続され、コンプレッサー4
の運転を制御して窒素ガスの供給量を調整するようにな
っている。
Further, a nitrogen gas supply pipe 28 is connected to the compressor 4 attached to the base 22, the tip of which is guided to the bottom side of the processing container 1, and this tip serves as the nitrogen gas ejection nozzle 3. . A rod-shaped heater 29 is provided in the middle of the nitrogen gas supply pipe 28. Further, as shown in FIG. 2, a temperature sensor 30 for measuring the internal temperature is attached to the upper portion of the processing container 1, which is connected to the compressor 4 via a control device (not shown).
The operation of is controlled to adjust the supply amount of nitrogen gas.

【0012】次に上記構造の有機廃棄物炭化処理装置に
より生ごみ10を処理する方法について説明する。先ず処
理容器1内に窒素分を吸収して自力発熱する光熱菌を混
ぜた菌床31を入れる。次に図示しない制御装置の温度設
定を行なう。この制御装置では例えば処理容器1内の最
高温度を 100℃に設定すると、内部温度がこれに達する
とコンプレッサー4が停止し、これより10℃マイナスの
90℃になると再びコンプレッサー4の運転が再開される
ようになっている。この後、図2に示すように投入蓋12
を開けてここから生ごみ10をストック部11に投入して、
リフト装置7のチエーンコンベアー8を運転すると、こ
こに取付けたバケット9が回転して、生ごみ10を順次掬
い上げて上方に搬送し、上部で反転して投入シューター
13に落下させ、ここから処理容器1内に投入される。
Next, a method of treating the food waste 10 by the organic waste carbonization treatment apparatus having the above structure will be described. First, a bacterium bed 31 mixed with photothermal bacteria that absorb nitrogen and generate heat by itself is placed in the processing container 1. Next, the temperature of the control device (not shown) is set. In this controller, for example, if the maximum temperature inside the processing container 1 is set to 100 ° C, the compressor 4 will stop when the internal temperature reaches this,
When the temperature reaches 90 ° C, the operation of the compressor 4 is restarted again. After this, as shown in FIG.
Open and put the garbage 10 into the stock section 11 from here,
When the chain conveyor 8 of the lift device 7 is operated, the bucket 9 attached here rotates, and the garbage 10 is sequentially picked up and conveyed to the upper side, and inverted at the upper part to throw in the shooter.
It is dropped into 13 and is put into the processing container 1 from here.

【0013】一方、図1に示すようにモーター23を回転
させて、これを減速器24で減速し、この回転力をチェー
ンホイール25からチェーン27を介してチェーンホイール
26に伝達してシャフト20を回転させると、攪拌装置2の
撹拌羽根21が回転して光熱菌を混ぜた菌床31と生ごみ10
が撹拌される。また同時にコンプレッサー4を運転し
て、ここから窒素ガスを含んでいる空気を窒素ガス供給
管28に供給し、中間に設けた棒状ヒーター29で空気を約
50℃程度に加熱して窒素ガス噴出ノズル3から生ごみ10
内に噴出させる。
On the other hand, as shown in FIG. 1, the motor 23 is rotated, and the motor 23 is decelerated by the speed reducer 24. This rotational force is transmitted from the chain wheel 25 to the chain 27 through the chain wheel.
When the shaft 20 is transmitted to 26, the stirring blade 21 of the stirring device 2 is rotated and the fungal bed 31 mixed with photothermia and the garbage 10
Is stirred. At the same time, the compressor 4 is operated to supply the air containing the nitrogen gas to the nitrogen gas supply pipe 28, and the rod-shaped heater 29 provided in the middle supplies about the air.
Heat it to about 50 ℃ and remove the garbage 10 from the nitrogen gas jet nozzle 3.
Inject it inside.

【0014】このように加熱した空気を供給しながら攪
拌装置2で生ごみ10を撹拌すると、ここに含まれる光熱
菌は空気の4分の3を占める窒素ガスの窒素分を吸収し
て自力発熱してくる。光熱菌は数百℃の温度まで上昇し
ても繁殖し続けることができるもので、生ごみ10が40℃
程度に上昇すると雑菌が死滅し、70℃を越えると生ごみ
10に含まれる水蒸気やガスが多量に蒸発し、蒸発した水
蒸気やガスはキャップ部14に設けた排気管6を通って外
部に排出され、更に90℃を越えると炭化が始まる。
When the food waste 10 is stirred by the stirrer 2 while supplying the heated air as described above, the photothermia contained therein absorbs the nitrogen content of nitrogen gas which occupies three-fourths of the air and heats itself. Come on. Photothermophiles can continue to reproduce even if the temperature rises to several hundreds of degrees Celsius.
When it rises to a certain degree, various bacteria die, and when it exceeds 70 ℃, it becomes garbage.
A large amount of water vapor and gas contained in 10 are evaporated, and the vaporized water vapor and gas are discharged to the outside through the exhaust pipe 6 provided in the cap portion 14, and carbonization starts when the temperature exceeds 90 ° C.

【0015】この後、更に温度が上昇して、設定した 1
00℃になるとこれを温度センサー30が検知して、その測
定信号が制御装置に出力され、ここから停止信号がコン
プレッサー4に出力されて停止し、空気の供給が遮断さ
れる。このように空気の供給が停止すると、窒素ガスの
供給がなくなるので光熱菌の発熱が少なくなり処理容器
1内の温度が次第に低下してくる。温度が90℃まで低下
したらこれを温度センサー30で検知して、再びコンプレ
ッサー4を運転して窒素ガスを供給し始めると光熱菌の
発熱が活発になって温度が上昇していく。
After this, the temperature was further raised and the
When the temperature reaches 00 ° C., the temperature sensor 30 detects this, and the measurement signal is output to the control device. From this, a stop signal is output to the compressor 4 to stop and the air supply is cut off. When the supply of air is stopped in this way, the supply of nitrogen gas is stopped, and the heat generation of photothermia is reduced, and the temperature inside the processing container 1 is gradually decreased. When the temperature drops to 90 ° C., this is detected by the temperature sensor 30, and when the compressor 4 is operated again to start supplying nitrogen gas, the heat of photothermia becomes active and the temperature rises.

【0016】この状態をグラフで示すと図3のようにな
り、処理容器1内の温度が90〜 100℃の範囲に調整され
て、生ごみ10の水分の蒸発と炭化が進行して軽石状にな
っていく。生ごみ10は通常水分の含有量が90%以上あ
り、この水分を除去して更に炭化させるので、最終状態
では投入量の5%以下に大幅に減容することができる。
また運転を停止して数日間経てから、再び生ごみ10を投
入して装置を運転しても、炭化した菌床31には光熱菌が
残っているので再び処理することができる。また炭化し
て減容するので、長期間連続的に運転しても、処理容器
1内の菌床31は余り増加せず、炭化した菌床31の排出
は、毎日1トンの生ごみ10を処理しても1週間に1回程
度で十分である。
A graph of this state is shown in FIG. 3, in which the temperature in the processing container 1 is adjusted within the range of 90 to 100 ° C., and evaporation and carbonization of water in the garbage 10 progresses to form a pumice stone. Will become. The raw garbage 10 usually has a water content of 90% or more, and since this water is removed and further carbonized, the volume can be greatly reduced to 5% or less of the input amount in the final state.
Further, even after several days have passed since the operation was stopped, even if the garbage 10 is put into the apparatus again to operate the apparatus, photothermophilia remain in the carbonized bed 31, so that it can be processed again. In addition, since the volume is reduced by carbonization, even if it is continuously operated for a long period of time, the bacterial bed 31 in the processing container 1 does not increase so much, and the carbonized bacterial bed 31 is discharged by 1 ton of garbage 10 per day. Even if it is treated, about once a week is enough.

【0017】炭化した菌床31が増加したときには、図2
に示す取出蓋16を開いて、攪拌装置2を回転させれば、
軽石状の炭化物は脆く崩れて強制的に排出され、排出シ
ューター17を通して図示しない袋などに詰める。このよ
うにして得られた軽石状の炭化物は土壤改良材として有
効であるが、廃棄処分にしてもその容積が少ないので処
分が容易である。
When the carbonized bacterial bed 31 is increased, FIG.
By opening the take-out lid 16 shown in and rotating the stirring device 2,
The pumice-like carbide is brittle and collapses and is forcibly discharged, and is packed into a bag or the like not shown through the discharge shooter 17. The pumice-like carbide obtained in this way is effective as a soil improvement material, but it is easy to dispose because it has a small volume even if it is disposed of.

【0018】なお実験によると、豆腐の製造によって排
出される堆肥化が難しかったオカラ1トンを処理容器1
に投入し、攪拌装置2の回転数を毎分1.5回とし、設
定温度を 100℃に設定して、コンプレッサー4からの空
気供給量を制御して図3に示すように温度調整しながら
処理したところ、6時間でオカラを完全に炭化処理する
ことができ、その炭化物の量は約30Kgであった。
According to the experiment, 1 ton of okara, which was difficult to be composted by the production of tofu, was treated in the processing container 1.
While controlling the rotation speed of the agitator 2 to 1.5 times per minute, setting the set temperature to 100 ° C., controlling the air supply amount from the compressor 4 and adjusting the temperature as shown in FIG. When treated, the okara could be completely carbonized in 6 hours, and the amount of the charcoal was about 30 kg.

【0019】また生ごみ10が自力発熱する光熱菌により
加熱されて発生した水蒸気やガスを排出する排気管6の
先端を、図4に示すように水槽32に通して、水蒸気やガ
スを水冷して液化し、この凝縮液33を捕集すると、ここ
にはアミノ酸やキト酸が多量に含まれており、これは肥
料や殺虫剤としても有効利用することができる。
Further, as shown in FIG. 4, the tip of the exhaust pipe 6 for discharging the water vapor and gas generated by heating the garbage 10 by the photothermia that self-heats is passed through the water tank 32 to cool the water vapor and gas. It is liquefied and collected, and when this condensate 33 is collected, it contains a large amount of amino acids and chito acids, which can be effectively used as fertilizers and insecticides.

【0020】なお上記実施例では、コンプレッサー4を
1台設置した場合について示したが、2台設けて制御装
置により1台をオンオフさせて制御する方法でも良い。
また上記実施例では処理容器1の横にリフト装置7を設
けた場合について示したが、小形の場合には、キャップ
部14を開けてここから直接、生ごみ10を投入する構造で
も良い。また上記実施例では処理容器1内の設定温度を
100℃に設定した場合について示したが、その処理量や
処理時間に応じて任意に設定することができ、処理量が
多く短時間に処理する場合には例えば 150℃程度に設定
すると良い。また炭化する有機廃棄物としては生ごみ10
に限らず、下水処理場から排出される脱水処理ケーキも
同様に処理することができる。
In the above embodiment, the case where one compressor 4 is installed has been described, but a method in which two compressors are provided and one controller is turned on and off by the control device may be used.
Further, in the above embodiment, the case where the lift device 7 is provided beside the processing container 1 has been shown, but in the case of a small size, the structure may be such that the cap portion 14 is opened and the raw garbage 10 is thrown directly from there. In the above embodiment, the set temperature in the processing container 1 is
Although the case of setting the temperature to 100 ° C. is shown, it can be set arbitrarily according to the processing amount and the processing time, and when the processing amount is large and the processing is performed in a short time, it may be set to about 150 ° C., for example. Garbage is 10 as carbonized organic waste.
However, the dehydrated cake discharged from the sewage treatment plant can be treated in the same manner.

【0021】[0021]

【発明の効果】以上説明した如く本発明に係る有機廃棄
物炭化処理装置によれば、窒素分を吸収して自力発熱す
る光熱菌を使用して有機廃棄物を加熱して、水分を蒸発
させると共に炭化させて大幅に減容できるので、処分も
容易で、従来、分解発酵しにくかった有機廃棄物にも広
く適用でき、しかも悪臭の発生もないので市街地にある
施設でも使用することができる。また炭化した有機廃棄
物は土壤改良剤としても利用できる上、加熱時に発生し
た水蒸気を凝縮した液体は、肥料や殺虫剤としても効果
があるなど種々の効果を有するものである。
As described above, according to the apparatus for carbonizing organic waste according to the present invention, the organic waste is heated by using photothermal bacteria that absorb nitrogen and generate heat by itself to evaporate water. Since it can be carbonized and greatly reduced in volume, it can be easily disposed of, can be widely applied to organic waste that has been difficult to decompose and ferment in the past, and since it does not generate a bad odor, it can be used in facilities in urban areas. Further, the carbonized organic waste can be used as a soil improving agent, and the liquid obtained by condensing steam generated during heating has various effects such as being effective as a fertilizer or an insecticide.

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

【図1】本発明の一実施例による有機廃棄物炭化処理装
置の縦断正面図である。
FIG. 1 is a vertical sectional front view of an organic waste carbonization treatment apparatus according to an embodiment of the present invention.

【図2】図1に示す有機廃棄物炭化処理装置の縦断側面
図である。
FIG. 2 is a vertical sectional side view of the organic waste carbonization treatment apparatus shown in FIG.

【図3】処理容器内の温度制御状態を示す説明図であ
る。
FIG. 3 is an explanatory diagram showing a temperature control state in a processing container.

【図4】排気管から排出される水蒸気やガスを凝縮する
装置を示す断面図である。
FIG. 4 is a cross-sectional view showing an apparatus for condensing water vapor or gas discharged from an exhaust pipe.

【符合の説明】[Description of sign]

1 処理容器 2 攪拌装置 3 窒素ガス噴出ノズル 4 コンプレッサー 5 断熱材 6 排気管 7 リフト装置 8 チエーンコンベアー 9 バケット 10 生ごみ 11 ストック部 14 キャップ部 16 取出蓋 20 シャフト 21 撹拌羽根 22 基台 23 モーター 24 減速器 28 窒素ガス供給管 29 ヒーター 30 温度センサー 31 菌床 32 水槽 33 凝縮液 1 Processing Container 2 Stirrer 3 Nitrogen Gas Jet Nozzle 4 Compressor 5 Insulation 6 Exhaust Pipe 7 Lifting Device 8 Chain Conveyor 9 Bucket 10 Garbage 11 Stock Part 14 Cap Part 16 Extraction Lid 20 Shaft 21 Stirring Blade 22 Base 23 Motor 24 Speed reducer 28 Nitrogen gas supply pipe 29 Heater 30 Temperature sensor 31 Bacteria bed 32 Water tank 33 Condensate

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 窒素分を吸収して自力発熱する光熱菌
と、処理される有機廃棄物とを入れる処理容器内に、攪
拌装置を設けると共に、窒素ガスを処理容器内に供給す
るコンプレッサーを設け、このコンプレッサーを制御し
て窒素ガス供給量を調整する制御装置を設けると共に、
この制御装置に接続された温度センサーを前記処理容器
に設けたことを特徴とする有機廃棄物炭化処理装置。
1. A stirrer is provided in a processing container for containing photothermia that absorbs nitrogen content and generates heat by itself and an organic waste to be processed, and a compressor for supplying nitrogen gas into the processing container is provided. , With a control device that controls this compressor to adjust the nitrogen gas supply amount,
An organic waste carbonization treatment device, wherein a temperature sensor connected to this control device is provided in the treatment container.
【請求項2】 窒素ガスを処理容器内に供給するガス
供給管にヒーターを取付けたことを特徴とする請求項1
記載の有機廃棄物炭化処理装置。
2. A heater is attached to a gas supply pipe for supplying nitrogen gas into the processing container.
The organic waste carbonization treatment device described.
JP6300252A 1994-11-09 1994-11-09 Organic waste carbonization method and apparatus Expired - Fee Related JP2736750B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6300252A JP2736750B2 (en) 1994-11-09 1994-11-09 Organic waste carbonization method and apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6300252A JP2736750B2 (en) 1994-11-09 1994-11-09 Organic waste carbonization method and apparatus

Publications (2)

Publication Number Publication Date
JPH08132008A true JPH08132008A (en) 1996-05-28
JP2736750B2 JP2736750B2 (en) 1998-04-02

Family

ID=17882550

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6300252A Expired - Fee Related JP2736750B2 (en) 1994-11-09 1994-11-09 Organic waste carbonization method and apparatus

Country Status (1)

Country Link
JP (1) JP2736750B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102430558A (en) * 2011-09-22 2012-05-02 宁波乐士实业有限公司 Kitchen garbage microbiological processing machine
WO2017195407A1 (en) * 2016-05-11 2017-11-16 克守 谷黒 Method for ultra-low-temperature carbonization treatment of biomass material, and method for producing carbide

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5039283A (en) * 1973-07-11 1975-04-11
JPH03237081A (en) * 1990-02-14 1991-10-22 Koichi Hashimoto Production of compost and equipment
JPH0691242A (en) * 1992-04-08 1994-04-05 Gist Brocades Nv Method of treating organic waste

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5039283A (en) * 1973-07-11 1975-04-11
JPH03237081A (en) * 1990-02-14 1991-10-22 Koichi Hashimoto Production of compost and equipment
JPH0691242A (en) * 1992-04-08 1994-04-05 Gist Brocades Nv Method of treating organic waste

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102430558A (en) * 2011-09-22 2012-05-02 宁波乐士实业有限公司 Kitchen garbage microbiological processing machine
WO2017195407A1 (en) * 2016-05-11 2017-11-16 克守 谷黒 Method for ultra-low-temperature carbonization treatment of biomass material, and method for producing carbide
JPWO2017195407A1 (en) * 2016-05-11 2018-06-07 克守 谷黒 Method for carbonizing biomass material and method for producing carbide
CN109153050A (en) * 2016-05-11 2019-01-04 谷黑克守 The ultralow temperature carbonization treatment method of biological material and the manufacturing method of carbide
EP3446798A4 (en) * 2016-05-11 2019-04-17 Katsumori Taniguro Method for ultra-low-temperature carbonization treatment of biomass material, and method for producing carbide
US11542436B2 (en) 2016-05-11 2023-01-03 Katsumori Taniguro Biomass treatment method

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