JPH04277072A - Method and apparatus for treating garbage - Google Patents

Method and apparatus for treating garbage

Info

Publication number
JPH04277072A
JPH04277072A JP3065388A JP6538891A JPH04277072A JP H04277072 A JPH04277072 A JP H04277072A JP 3065388 A JP3065388 A JP 3065388A JP 6538891 A JP6538891 A JP 6538891A JP H04277072 A JPH04277072 A JP H04277072A
Authority
JP
Japan
Prior art keywords
kitchen waste
carbonization
intermediate product
desired shape
molding
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
JP3065388A
Other languages
Japanese (ja)
Inventor
Yasunobu Kawachi
河内 康伸
Takao Takahashi
孝夫 高橋
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.)
Shibaura Machine Co Ltd
Original Assignee
Toshiba Machine Co Ltd
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 Toshiba Machine Co Ltd filed Critical Toshiba Machine Co Ltd
Priority to JP3065388A priority Critical patent/JPH04277072A/en
Publication of JPH04277072A publication Critical patent/JPH04277072A/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
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel
    • 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)
  • Glanulating (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)

Abstract

PURPOSE:To treat garbage so as to utilize the same as fuel, an adsorbent or a desiccant by converting the garbage to activated carbon like carbide uniform in quality and easy to handle. CONSTITUTION:Garbage is kneaded, heated and pressed by a molding apparatus 10 such as an extruder to be extruded from a die 19. The extruded intermediate product is cut by a cutter 20 to be molded into pellets. The intermediate product thus molded into a desired shape is, if necessary, dried according to its water content by dryer 30 to be introduced into the dry distillation pipe 43 of a dry distillation apparatus 40 and moisture or volatile gas is discharged to obtain porous activated carbon like carbide.

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、残飯を主とした厨芥の
処理に係り、特に厨芥を有用な製品とする処理方法およ
び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 the processing of kitchen waste, mainly leftover food, and particularly to a processing method and apparatus for turning kitchen waste into a useful product.

【0002】0002

【従来の技術】従来、厨芥は腐敗や悪臭の発生を押える
ため、好気性菌等によって短期間のうちに醗酵させ、さ
らには乾燥させて飼料,肥料ならびに燃料として利用す
ることが行われているが、醗酵には2ないし数日間を要
する。
[Prior Art] Conventionally, in order to prevent spoilage and the generation of bad odors, kitchen waste has been fermented by aerobic bacteria in a short period of time, and then dried to be used as feed, fertilizer, and fuel. However, fermentation takes two to several days.

【0003】0003

【発明が解決しようとする課題】上記のような厨芥の処
理は、十分な減容を達成できず、多くの費用と日数を要
すると共に、処理によって得られる生成物は変質のおそ
れがあると共に品質の一様性や需給のバランスに問題が
あり、資源のリサイクルという社会の期待に十分応えて
いない。
[Problems to be Solved by the Invention] The processing of kitchen waste as described above does not achieve sufficient volume reduction, requires a lot of cost and time, and the product obtained by the processing may deteriorate in quality and have poor quality. There are problems with the uniformity of resources and the balance between supply and demand, and society's expectations for resource recycling are not fully met.

【0004】本発明は、厨芥を衛生的で変質することも
なく、かつ品質が一様で取扱いが容易な製品に変換し、
減容効果を高められると共に、燃料、汚水処理用の吸着
剤ならびに乾燥剤として利用することのできる厨芥の処
理方法および装置を提供することを目的としている。
[0004] The present invention converts kitchen waste into products that are hygienic, do not deteriorate, have uniform quality, and are easy to handle.
It is an object of the present invention to provide a method and apparatus for treating kitchen waste that can enhance the volume reduction effect and can be used as a fuel, an adsorbent for sewage treatment, and a desiccant.

【0005】[0005]

【課題を解決するための手段】上記目的を達成するため
の本発明による厨芥の処理方法は、厨芥を混練,加熱な
らびに加圧して所望の形状に成形し、これを乾留して炭
化させるものである。なお、水分が多い厨芥は成形時に
脱水を行い、また乾留の前に乾燥を行うことが好ましい
[Means for Solving the Problems] The method for processing kitchen waste according to the present invention to achieve the above object is to knead, heat and pressurize kitchen waste to form it into a desired shape, and then carbonize it by carbonizing it. be. Note that it is preferable that kitchen waste containing a large amount of water be dehydrated during molding and dried before carbonization.

【0006】また、上記目的を達成するための本発明に
よる厨芥の処理装置は、厨芥を受入れて混練,加熱なら
びに加圧して所望の形状に成形する成形装置と、この成
形装置によって所望の形状に成形された厨芥の中間生成
物を乾留により炭化する乾留装置とからなるものである
[0006] In order to achieve the above object, the kitchen waste processing apparatus according to the present invention also includes a molding device that receives kitchen waste, kneads it, heats it, pressurizes it, and molds it into a desired shape; It consists of a carbonization device that carbonizes the intermediate product of molded kitchen waste by carbonization.

【0007】なお、成形装置と乾留装置との間に乾燥器
を介在させ、また成形装置を1ないし2軸押出機とし、
さらにまた乾留装置の熱源を処理される厨芥の吸収帯域
にある電磁波としてもよい。
[0007] Furthermore, a dryer is interposed between the molding device and the carbonization device, and the molding device is a single or twin screw extruder,
Furthermore, the heat source of the carbonization apparatus may be an electromagnetic wave in the absorption band of the kitchen waste to be processed.

【0008】[0008]

【作用】厨芥を、例えば押出機のような成形装置により
混練,加熱ならびに加圧して厨芥中のでんぷん質をバイ
ンダとしてペレットのような所望の形状に成形して中間
生成物を作る。次に、これを好ましくは乾燥器で乾燥さ
せてから乾留装置に入れ、無酸素雰囲気内で加熱し、水
分はもちろんメタンやアンモニアなどの揮発性ガスを放
出させると共に熱分解して炭化する。炭化された製品は
多孔質体であり、燃料として利用できるほか、汚水処理
用の吸着剤および乾燥剤としても利用できる。
[Operation] Kitchen waste is kneaded, heated, and pressurized using a molding device such as an extruder, and the starch in the kitchen waste is used as a binder to form a desired shape such as a pellet to produce an intermediate product. Next, this is preferably dried in a drier, then placed in a carbonization apparatus and heated in an oxygen-free atmosphere to release not only moisture but also volatile gases such as methane and ammonia, as well as being thermally decomposed and carbonized. The carbonized product is porous and can be used as a fuel, as well as an adsorbent and desiccant for wastewater treatment.

【0009】[0009]

【実施例】以下本発明の実施例について図1を参照して
説明する。成形装置10には、1ないし2軸スクリュ式
の押出機を用いている。11はスクリュで、モータ12
により歯車伝達機構13を介して回転されるようになっ
ている。シリンダ14の元部にはホッパ15が設けられ
、ホッパ15内には矢印Aで示すように投入された厨芥
を破砕してシリンダ14内へ供給するための破砕器16
が設けられている。シリンダ14の途中には、脱気口1
7,18が設けられている。なお、シリンダ14のホッ
パ15に比較的近い位置に多数のスリットからなるスク
リーン状の脱水口を設けてもよい。シリンダ14の先端
にはダイス19が取付けられている。ダイス19は所望
の断面形状の図示しない開口を有している。ダイス19
の出口側には切断装置20が取付けられて、ダイス19
から押出された中間生成物を所望の長さに切断して所望
の形状(以下ペレットという)に成形するようになって
いる。
Embodiments An embodiment of the present invention will be described below with reference to FIG. The molding device 10 uses a single or twin screw type extruder. 11 is a screw, motor 12
It is designed to be rotated via a gear transmission mechanism 13. A hopper 15 is provided at the base of the cylinder 14, and a crusher 16 is provided in the hopper 15 for crushing the kitchen waste thrown in as shown by arrow A and supplying it into the cylinder 14.
is provided. There is a deaeration port 1 in the middle of the cylinder 14.
7 and 18 are provided. Note that a screen-shaped dewatering port made of a large number of slits may be provided in a position relatively close to the hopper 15 of the cylinder 14. A die 19 is attached to the tip of the cylinder 14. The die 19 has an opening (not shown) with a desired cross-sectional shape. Dice 19
A cutting device 20 is attached to the exit side of the die 19.
The intermediate product extruded from the pellets is cut into desired lengths and molded into desired shapes (hereinafter referred to as pellets).

【0010】30は乾燥器であり、切断装置20でペレ
ットにされた中間生成物を矢印Bで示すようにホッパ3
1から受入れる。乾燥器30は、外筒32と内筒33の
二重管構造をし、内筒33内にスクリュ34が回転自在
に設けられている。スクリュ34はモータ35によって
回転を与えられ、ホッパ31から受入れた中間生成物を
図において右から左へ搬送するようになっている。外筒
32と内筒33の間には給気口36から熱風が供給され
、内筒33の左端に設けた通気口37aから内筒33内
へも熱風を流入させるようになっている。内筒33の右
端には熱風排出用の通気口37bが設けられ、外筒32
の右端には排気口38が開口されている。また、内外筒
32,33の左端には乾燥された中間生成物の排出口3
9が開口されている。
Reference numeral 30 denotes a dryer, in which the intermediate product pelletized by the cutting device 20 is transferred to the hopper 3 as shown by arrow B.
Accept from 1. The dryer 30 has a double pipe structure including an outer cylinder 32 and an inner cylinder 33, and a screw 34 is rotatably provided in the inner cylinder 33. The screw 34 is rotated by a motor 35 and conveys the intermediate product received from the hopper 31 from right to left in the figure. Hot air is supplied between the outer cylinder 32 and the inner cylinder 33 from an air supply port 36, and the hot air is also made to flow into the inner cylinder 33 from a vent 37a provided at the left end of the inner cylinder 33. A vent 37b for discharging hot air is provided at the right end of the inner cylinder 33, and the outer cylinder 32
An exhaust port 38 is opened at the right end. In addition, a discharge port 3 for dried intermediate products is provided at the left end of the inner and outer cylinders 32 and 33.
9 is open.

【0011】排出口39の下方には、乾留装置40のホ
ッパ41が開口している。乾留装置40は、耐熱構造の
炉体42と、その中に設置された乾留管43からなり、
乾留管43内にはモータ44によって回転されるスクリ
ュ45が設けられている。ホッパ41はロータリバルブ
46を介して乾留管43の元部に接続されており、ロー
タリバルブ46は乾留管43の内部と外部とをしゃ断し
つつホッパ41に投入された中間生成物を乾留管43内
へ投入するようになっている。乾留管43の先端部には
排出管47が接続され、排出管47の先端はロータリバ
ルブ46と同様のロータリバルブ48を介して外部に開
口されるようになっている。49は製品受である。なお
、ロータリバルブ46,48は、交互に開閉する2段シ
ャッタ式のバルブでもよく、以下これらを単にバルブと
いう。
A hopper 41 of a carbonization device 40 is opened below the discharge port 39. The carbonization apparatus 40 consists of a furnace body 42 having a heat-resistant structure and a carbonization tube 43 installed therein.
A screw 45 rotated by a motor 44 is provided inside the carbonization tube 43 . The hopper 41 is connected to the base of the carbonization tube 43 via a rotary valve 46, and the rotary valve 46 shuts off the inside and outside of the carbonization tube 43 and transfers the intermediate product input into the hopper 41 to the carbonization tube 43. It is designed to be inserted inside. A discharge pipe 47 is connected to the distal end of the carbonization pipe 43, and the distal end of the discharge pipe 47 is opened to the outside via a rotary valve 48 similar to the rotary valve 46. 49 is a product receiver. Note that the rotary valves 46 and 48 may be two-stage shutter type valves that open and close alternately, and will hereinafter be simply referred to as valves.

【0012】炉体42の下部には、運転の初期に用いら
れるほか乾留管43からの後述する揮発性ガスに対して
補助的に用いられることもある燃料供給部50および空
気取入部51に接続されたバーナ52が設けられ、炉体
42内で燃料を燃焼させ、乾留管43を加熱するように
なっている。乾留管43には内部で発生した水蒸気や揮
発性ガスを排出するためのガス排出管53が接続され、
揮発性ガスなどをバーナ52の近くに導入し、加熱用の
燃料として利用するようになっている。また、炉体42
の廃熱ガスは排煙管54により乾燥器30の給気口32
へ導入されるようになっている。
The lower part of the furnace body 42 is connected to a fuel supply section 50 and an air intake section 51, which are used in the initial stage of operation and are sometimes used auxiliary for volatile gases from the carbonization tube 43, which will be described later. A burner 52 is provided to combust fuel within the furnace body 42 and heat the carbonization tube 43. A gas discharge pipe 53 is connected to the carbonization pipe 43 for discharging water vapor and volatile gas generated inside.
Volatile gas or the like is introduced near the burner 52 and used as heating fuel. In addition, the furnace body 42
The waste heat gas is sent to the air supply port 32 of the dryer 30 through the flue gas pipe 54.
It is now being introduced to

【0013】次いで本装置の作用について説明する。矢
印Aで示すように、必要に応じて切断故紙,おがくず,
もみがら,発泡スチロール等の含水率調整用または混練
処理性改善用などの添加材と共に厨芥をホッパ15に投
入する。投入された厨芥は破砕器16によって所定の小
塊に裁断され、シリンダ14内に送り込まれ、スクリュ
11によって混練,加圧されると共に、この混練,加圧
によって発熱し、さらにはシリンダ14の周囲に設けた
図示しないヒータによって積極的に加熱されて昇温し、
脱気口17,18から蒸発水分が排出される。こうして
混練,加熱ならびに加圧された厨芥は、ダイス19から
例えば直径10mm程度の円形断面のような所望の断面
形状で押出される。押出された厨芥はその中に含まれて
いるでんぷん質がバインダの役目を果たして賦形される
Next, the operation of this device will be explained. As shown by arrow A, cut waste paper, sawdust,
Kitchen waste is fed into the hopper 15 together with additives such as rice husks and expanded polystyrene for adjusting the moisture content or improving kneading processability. The thrown kitchen waste is cut into predetermined small pieces by the crusher 16, fed into the cylinder 14, kneaded and pressurized by the screw 11, and generates heat due to this kneading and pressurization, and furthermore, the surroundings of the cylinder 14. The temperature is increased by being actively heated by a heater (not shown) installed in the
Evaporated water is discharged from the deaeration ports 17 and 18. The thus kneaded, heated, and pressurized kitchen waste is extruded from the die 19 in a desired cross-sectional shape, such as a circular cross-section with a diameter of about 10 mm. The extruded kitchen waste is shaped with the starch contained therein acting as a binder.

【0014】ダイス19から押出された厨芥は、急激な
圧力低下と温度変化によって膨化し、発泡して多孔質の
中間生成物を形成すると共に、切断装置20によって例
えば10mm程度の所望の長さに切断されてペレットに
成形される。
The kitchen waste extruded from the die 19 expands and foams due to the rapid pressure drop and temperature change to form a porous intermediate product, and is cut into a desired length of, for example, about 10 mm by the cutting device 20. It is cut and formed into pellets.

【0015】上記成形装置10でペレットにされた厨芥
の中間生成物は、含水率を20%程度にするため、矢印
Bで示すように、ホッパ31によって乾燥器30内に導
入され、給気口39から供給される熱風により乾燥され
つつ、内筒33内をスクリュ34によって右から左へ進
み、矢印Cで示すように、排出口39から乾留装置40
のホッパ41へ投入される。なお、成形装置10で成形
された中間生成物の含水率が比較的低い場合は、乾燥器
30による乾燥を省略して成形後直接乾留装置40のホ
ッパ41へ導入してもよい。
The intermediate product of kitchen waste pelletized by the molding device 10 is introduced into the dryer 30 by a hopper 31 as shown by arrow B in order to have a moisture content of about 20%. While being dried by hot air supplied from 39, the inner cylinder 33 is moved from right to left by the screw 34, and as shown by arrow C, it is passed through the carbonization device 40 from the discharge port 39.
The liquid is thrown into the hopper 41 of Note that when the moisture content of the intermediate product molded in the molding device 10 is relatively low, drying in the dryer 30 may be omitted and the product may be directly introduced into the hopper 41 of the carbonization device 40 after molding.

【0016】ホッパ40へ投入された中間生成物は、バ
ルブ46を介して乾留管43内へ導入される。乾留装置
40の炉体42はバーナ52による燃料と乾留管43内
からガス排出管53により導入された揮発性ガスの燃焼
によって乾留管43を加熱しており、乾留管43内に投
入された中間生成物をスクリュ45で送りながら加熱す
る。乾留管43内はバルブ46,48によって外気から
略しゃ断された状態にあるために略無酸素雰囲気であり
、中間生成物は燃焼することなく、水分はもちろんメタ
ンやアンモニア等の揮発性ガスを放出させると共に熱分
解して炭化され、活性炭状の多孔質の炭化物となる。 炭化物となった厨芥すなわち製品は排出管47からバル
ブ48を介して、矢印Dで示すように、製品受49に投
入される。
The intermediate product charged into the hopper 40 is introduced into the carbonization tube 43 via the valve 46. The furnace body 42 of the carbonization apparatus 40 heats the carbonization tube 43 by combustion of fuel by the burner 52 and volatile gas introduced from the carbonization tube 43 through the gas exhaust pipe 53. The product is heated while being fed by the screw 45. The inside of the carbonization tube 43 is substantially cut off from the outside air by the valves 46 and 48, so there is a substantially oxygen-free atmosphere, and the intermediate products do not burn, releasing moisture as well as volatile gases such as methane and ammonia. At the same time, it is thermally decomposed and carbonized to become a porous carbide like activated carbon. The charred kitchen waste, that is, the product, is fed from the discharge pipe 47 via the valve 48 into the product receiver 49 as shown by arrow D.

【0017】前述した実施例は、成形装置10に1台の
押出機を用いて厨芥を混練,加熱ならびに加圧して膨化
したペレット状の中間生成物を成形して、乾燥器30を
介してまたは直接乾留装置40へ導く例を示したが、特
に含水率を低下させるため、複数の押出機をカスケード
状に結合して多段に押出処理するようにしてもよく、ま
た乾燥器30および乾留管43もそれぞれ所定温度でま
たは温度を変えてカスケード状に多段に設けてもよい。
In the above-mentioned embodiment, one extruder is used in the molding device 10 to knead kitchen waste, heat and pressurize it to form a swollen pellet-like intermediate product. Although an example has been shown in which the process is carried out directly to the carbonization apparatus 40, in order to particularly reduce the water content, a plurality of extruders may be connected in a cascade to carry out the extrusion process in multiple stages. They may also be provided in multiple stages in a cascade shape, each at a predetermined temperature or at different temperatures.

【0018】また、前述した実施例は、乾留装置40の
熱源として乾留中に中間生成物から発生する揮発性ガス
と補助燃料を用いた例を示したが、乾留管43を鋼等の
導電性の物質で作成し、中間生成物の吸収帯域にある電
磁波を乾留管43へ導入して加熱するようにしてもよい
。この場合、上記揮発性ガスは乾燥器30の熱源として
使用することが好ましい。
Further, in the above-mentioned embodiment, volatile gas generated from intermediate products during carbonization and auxiliary fuel were used as the heat source of the carbonization apparatus 40, but the carbonization tube 43 was made of conductive material such as steel. It is also possible to heat the carbonization tube 43 by introducing electromagnetic waves in the absorption band of the intermediate product into the carbonization tube 43. In this case, the volatile gas is preferably used as a heat source for the dryer 30.

【0019】実験例 (1)厨芥の成分(重量%) 米飯          50 惣菜(揚物)  30 野菜屑        20 (2)含水率  58重量% (3)成形 上記厨芥を細かく裁断した後、押出機により混練し、直
径10mmの棒状にした後、長さ10mmに切断してペ
レットに賦形した。 (4)乾燥 上記ペレットの表面が乾くまで、熱風乾燥した。 (5)乾留 上記の乾燥ペレットを乾留管内に入れ、ほぼ密閉状態で
、まず105℃に加熱して10〜20分その温度に保っ
た後、10〜30分掛けて450〜600℃に加熱し、
その温度に10分保持した後、250℃まで降温させて
取出した。 (6)出来上がった炭化物 出来上がった炭化物は、当初の厨芥量に対し十分減容さ
れると共に重量は約5%に減少し、コークス状の多孔質
体であった。また、燃焼させたところ炎,煙は生じなか
った。
Experimental Example (1) Ingredients of kitchen waste (wt%): Rice 50 Deli (fried food) 30 Vegetable scraps 20 (2) Moisture content 58% by weight (3) Molding After cutting the kitchen waste into pieces, the above kitchen waste was kneaded using an extruder. It was made into a rod shape with a diameter of 10 mm, and then cut into a length of 10 mm and shaped into pellets. (4) Drying The above pellets were dried with hot air until the surface was dry. (5) Carbonization The above dried pellets are placed in a carbonization tube, and in an almost airtight state, first heated to 105℃, kept at that temperature for 10 to 20 minutes, and then heated to 450 to 600℃ over 10 to 30 minutes. ,
After maintaining the temperature for 10 minutes, the temperature was lowered to 250°C and taken out. (6) Finished carbide The finished carbide was a coke-like porous material, which was sufficiently reduced in volume and weight to about 5% of the original amount of kitchen waste. Also, when it was burned, no flame or smoke was produced.

【0020】[0020]

【発明の効果】以上述べたように本発明によれば、厨芥
を衛生的で変質することもなく、かつ品質が一様で取扱
いが容易な活性炭状の炭化物に変換するため、減容効果
を高められると共に、燃料,汚水処理用の吸着剤ならび
に乾燥剤として利用することができる効果がえられる。
[Effects of the Invention] As described above, according to the present invention, kitchen waste is converted into activated carbon-like charcoal which is hygienic and does not deteriorate in quality, has uniform quality, and is easy to handle. In addition, it can be used as a fuel, an adsorbent for sewage treatment, and a desiccant.

【図面の簡単な説明】[Brief explanation of the drawing]

【図1】本発明の一実施例を示す概要構成図である。FIG. 1 is a schematic configuration diagram showing one embodiment of the present invention.

【符号の説明】[Explanation of symbols]

10  成形装置 11  スクリュ 14  シリンダ 16  破砕器 17  脱気口 18  脱気口 19  ダイス 20  切断装置 30  乾燥器 32  外筒 33  内筒 34  スクリュ 36  給気口 38  排気口 40  乾留装置 42  炉体 43  乾留管 45  スクリュ 46  バルブ 48  バルブ 52  バーナ 10 Molding equipment 11 Screw 14 Cylinder 16 Crusher 17 Deaeration port 18 Deaeration port 19 Dice 20 Cutting device 30 Dryer 32 Outer cylinder 33 Inner cylinder 34 Screw 36 Air supply port 38 Exhaust port 40 Carbonization equipment 42 Furnace body 43 Carbonization tube 45 Screw 46 Valve 48 Valve 52 Burner

Claims (7)

【特許請求の範囲】[Claims] 【請求項1】  厨芥を混練,加熱ならびに加圧して所
望の形状に成形し、これを乾留して炭化させることから
なる厨芥の処理方法。
1. A method for processing kitchen waste, which comprises kneading, heating and pressurizing kitchen waste to form it into a desired shape, and carbonizing it by carbonization.
【請求項2】  厨芥を混練,加熱ならびに脱水して所
望の形状に成形し、これを乾留して炭化させることから
なる厨芥の処理方法。
2. A method for treating kitchen waste, which comprises kneading, heating and dehydrating kitchen waste to form it into a desired shape, and carbonizing it by carbonization.
【請求項3】  乾留の前工程として乾燥を行うことを
特徴とする請求項1または2記載の厨芥の処理方法。
3. The method for treating kitchen waste according to claim 1 or 2, wherein drying is performed as a step before carbonization.
【請求項4】  厨芥を受入れて混練,加熱ならびに加
圧して所望の形状に成形する成形装置と、同成形装置に
よって所望の形状に成形された厨芥の中間生成物を乾留
により炭化する乾留装置とからなる厨芥の処理装置。
4. A molding device that receives kitchen waste, kneads it, heats it, and pressurizes it to form it into a desired shape; and a carbonization device that carbonizes the intermediate product of the kitchen waste formed into the desired shape by the molding device. Kitchen waste processing equipment consisting of:
【請求項5】  成形装置と乾留装置の間に中間生成物
の乾燥器を介在させたことを特徴とする請求項4記載の
厨芥の処理装置。
5. The kitchen waste processing device according to claim 4, further comprising an intermediate product dryer interposed between the molding device and the carbonization device.
【請求項6】  成形装置が1ないし2軸押出機を有す
ることを特徴とする請求項4または5記載の厨芥の処理
装置。
6. The kitchen waste processing apparatus according to claim 4, wherein the molding apparatus has a one or twin screw extruder.
【請求項7】  乾留装置の熱源が処理される厨芥の吸
収帯域にある電磁波であることを特徴とする請求項4,
5または6記載の厨芥の処理装置。
7. Claim 4, characterized in that the heat source of the carbonization apparatus is an electromagnetic wave in the absorption band of the kitchen waste to be treated.
6. The kitchen waste processing device according to 5 or 6.
JP3065388A 1991-03-06 1991-03-06 Method and apparatus for treating garbage Pending JPH04277072A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3065388A JPH04277072A (en) 1991-03-06 1991-03-06 Method and apparatus for treating garbage

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3065388A JPH04277072A (en) 1991-03-06 1991-03-06 Method and apparatus for treating garbage

Publications (1)

Publication Number Publication Date
JPH04277072A true JPH04277072A (en) 1992-10-02

Family

ID=13285558

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3065388A Pending JPH04277072A (en) 1991-03-06 1991-03-06 Method and apparatus for treating garbage

Country Status (1)

Country Link
JP (1) JPH04277072A (en)

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06154728A (en) * 1992-11-18 1994-06-03 Shigeru Nakao Carbonization treatment of organic waste
JPH078936A (en) * 1993-04-13 1995-01-13 Nakayasu:Kk Method and apparatus for carbonizing organic waste
KR20010027512A (en) * 1999-09-14 2001-04-06 노현수 crusher of refuse
JP2001288474A (en) * 2000-04-06 2001-10-16 Iwasaki Kazuko Dry distillation method and combustion method of urban waste
KR20020083060A (en) * 2001-04-25 2002-11-01 박양균 dry devive for sludge and food garbage
US7252691B2 (en) 2001-03-06 2007-08-07 John Philipson Conversion of municipal solid waste to high fuel value
JP2010534121A (en) * 2007-07-25 2010-11-04 リアン,チーフイ Processing method to thoroughly recycle solid waste
CN102776006A (en) * 2012-08-17 2012-11-14 江西鹏源环保科技发展有限公司 Device for destructive distillation and drying of biomass
CN106312081A (en) * 2016-11-09 2017-01-11 昆山聚贝机械设计有限公司 Mixed metal granulator
CN107234120A (en) * 2016-03-29 2017-10-10 北京三聚环保新材料股份有限公司 A kind of moulding process of house refuse and the garbage-molding material as made from the technique
CN108745200A (en) * 2018-05-03 2018-11-06 南安市创培电子科技有限公司 A kind of broken comminutor of the chemical industry material with vent gas treatment

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06154728A (en) * 1992-11-18 1994-06-03 Shigeru Nakao Carbonization treatment of organic waste
JPH078936A (en) * 1993-04-13 1995-01-13 Nakayasu:Kk Method and apparatus for carbonizing organic waste
KR20010027512A (en) * 1999-09-14 2001-04-06 노현수 crusher of refuse
JP2001288474A (en) * 2000-04-06 2001-10-16 Iwasaki Kazuko Dry distillation method and combustion method of urban waste
US7252691B2 (en) 2001-03-06 2007-08-07 John Philipson Conversion of municipal solid waste to high fuel value
KR20020083060A (en) * 2001-04-25 2002-11-01 박양균 dry devive for sludge and food garbage
JP2010534121A (en) * 2007-07-25 2010-11-04 リアン,チーフイ Processing method to thoroughly recycle solid waste
CN102776006A (en) * 2012-08-17 2012-11-14 江西鹏源环保科技发展有限公司 Device for destructive distillation and drying of biomass
CN107234120A (en) * 2016-03-29 2017-10-10 北京三聚环保新材料股份有限公司 A kind of moulding process of house refuse and the garbage-molding material as made from the technique
CN106312081A (en) * 2016-11-09 2017-01-11 昆山聚贝机械设计有限公司 Mixed metal granulator
CN108745200A (en) * 2018-05-03 2018-11-06 南安市创培电子科技有限公司 A kind of broken comminutor of the chemical industry material with vent gas treatment

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