JP3027191U - Multipurpose recycling equipment - Google Patents

Multipurpose recycling equipment

Info

Publication number
JP3027191U
JP3027191U JP1996000755U JP75596U JP3027191U JP 3027191 U JP3027191 U JP 3027191U JP 1996000755 U JP1996000755 U JP 1996000755U JP 75596 U JP75596 U JP 75596U JP 3027191 U JP3027191 U JP 3027191U
Authority
JP
Japan
Prior art keywords
furnace
generated
carbonization
waste
waste heat
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.)
Expired - Lifetime
Application number
JP1996000755U
Other languages
Japanese (ja)
Inventor
尾 繁 中
田 大 三 郎 窪
Original Assignee
神戸農林株式会社
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 神戸農林株式会社 filed Critical 神戸農林株式会社
Priority to JP1996000755U priority Critical patent/JP3027191U/en
Application granted granted Critical
Publication of JP3027191U publication Critical patent/JP3027191U/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Carbon And Carbon Compounds (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

(57)【要約】 【課題】 生産性を向上させて経済的効率を上げ得る炭
化炉と、この炭化炉の炭化処理が産業廃棄物などの処理
に応用でき、この炭化処理工程の廃熱利用による多目的
リサイクル装置を提供するものである。 【解決手段】 炭材1又は産業廃棄物2を破砕機3で破
砕した後炭化処理する炭化炉4と、炭化炉4で生ずる排
煙7が煙道管を介して供給され、前記排煙7を完全燃焼
させる燃焼式消煙装置8と、この燃焼式消煙装置8の廃
熱が供給され高含水率廃棄物を乾燥せしめる乾燥炉11
と、乾燥炉11で発生する臭気や悪臭ガスなどの排出ガ
スを燃焼させて消臭する消臭装置16と、消臭装置16
で生ずる廃熱が供給される蒸気発生装置18と、蒸気発
生装置18で発生した水蒸気を用いて粉末活性炭を生成
する賦活装置19とで構成したことを特徴とする。
(57) [Abstract] [Problem] Carbonization furnace that can improve productivity and improve economic efficiency, and carbonization treatment of this carbonization furnace can be applied to treatment of industrial wastes, and waste heat utilization of this carbonization treatment process To provide a multipurpose recycling device. SOLUTION: A carbonization furnace 4 for crushing carbonaceous material 1 or industrial waste 2 by a crusher 3 and then carbonizing it, and flue gas 7 generated in the carbonization furnace 4 are supplied through a flue pipe, and the flue gas 7 -Type smoke eliminator 8 for completely burning air and a drying furnace 11 for drying waste having a high water content by supplying waste heat of the combustion-type smoke eliminator 8
And a deodorizing device 16 for deodorizing by burning exhaust gas such as odor and malodorous gas generated in the drying furnace 11, and a deodorizing device 16
The steam generator 18 to which the waste heat generated in 1 is supplied, and the activating device 19 for generating the powdered activated carbon by using the steam generated in the steam generator 18.

Description

【考案の詳細な説明】[Detailed description of the device]

【0001】[0001]

【考案の属する技術分野】[Technical field to which the device belongs]

この考案は炭化炉を用いた多目的リサイクルプラントシステムに係り、特に、 産業廃棄物や炭材を炭化処理する際発生する有害な煙を利用した多目的リサイク ル装置に関する。 The present invention relates to a multi-purpose recycling plant system using a carbonization furnace, and more particularly to a multi-purpose recycle device that uses harmful smoke generated when carbonizing industrial waste and carbonaceous materials.

【0002】[0002]

【従来の技術】[Prior art]

従来より、主燃料になっている木炭は一般には木炭炭化炉で生成されていた。 この木炭炭化炉は土を盛った土窯や石と粘土を積み重ねた石窯が使用され、この 土窯で木材を焼いて炭化させていた。 また、近年では一部耐火レンガを用いた炭化炉やドラム缶等で炭を焼く炭化処 理技法があった。炭材である木材を窯に入れて炭化させる場合、炭化中に灰化し て炭材への着火促進を施す上げ木を上部に配し、また、下部には炭化中に蒸発す る炭材の含有水分を吸収して窯内部の保温効果を成す敷木を必要としていた。 更に、木炭の炭化過程は煙突から排出される煙の色や臭いによって上げ木の着 火の立ち消えを防ぐために煙道口や通風口の開閉調節を行ったり、収炭量を増や すための追い焼きのタイミングや良質の木炭を得るための窯止めタイミングが重 要な作業であって、この炭焼き作業は豊富な経験によって木炭を生成していた。 Traditionally, the main fuel, charcoal, has generally been produced in a charcoal carbonization furnace. This charcoal carbonization furnace used a clay kiln filled with soil and a stone kiln in which stones and clay were stacked, and wood was burned and carbonized in this kiln. In addition, in recent years, there has been a carbonization treatment technique in which charcoal is burned in a carbonization furnace or a drum that uses some refractory bricks. When wood, which is a carbon material, is put into a kiln and carbonized, a raised tree that is ashed during carbonization to accelerate ignition of the carbon material is placed on the upper part, and a lower part of the carbon material that evaporates during carbonization is placed. It was necessary to have a floor covering that absorbs the water content and keeps the heat inside the kiln. Furthermore, the charcoal carbonization process involves opening and closing the flue vents and vents to prevent the ignition of raised trees from extinguishing due to the color and odor of smoke emitted from the chimney, and additional measures to increase the amount of coal collected. The timing of firing and the timing of kiln stopping to obtain high-quality charcoal are important operations, and this charcoal-burning operation used the wealth of experience to produce charcoal.

【0003】[0003]

【考案が解決しようとする課題】[Problems to be solved by the device]

しかし、上記した従来の木炭の炭化処理作業は、前述のように経験と熟練とが 要求され、しかも、木材から完全な木炭にするには長い時間と日数と手間を必要 とするため木炭のコスト低減が不可能であり、経済的にも採算の合うものではな かった。 また、前記木炭の炭化処理工程で発生する煙や熱はほとんど大気中に放出され 膨大なエネルギー源の再利用が成されていなかった。一部排煙を回収して木酢液 を抽出して殺菌剤等に利用されているが、有害成分と言われるタール分が含まれ ているため、一般的には余り使われていないという状況であった。 この考案は上記した点に鑑みてなされたものであり、その目的とするところは 、木炭製造や炭化処理工程で発生する煙を利用すると共に、煙の消煙の際に発生 する熱などを効率よく利用し、以って生産性と経済性を向上せしめた新規な多目 的リサイクル装置を提供するところにある。 However, the above-mentioned conventional charcoal carbonization work requires experience and skill as described above, and moreover, it takes a long time, days, and troubles to convert the charcoal into a complete charcoal. Reduction was impossible, and it was not economically viable. Moreover, most of the smoke and heat generated in the charcoal carbonization process are released into the atmosphere, and a huge amount of energy source has not been reused. It is used as a germicide, etc. by extracting some flue gas and extracting wood vinegar, but since it contains tar content, which is said to be a harmful component, it is generally rarely used. there were. The present invention has been made in view of the above points, and its purpose is to utilize the smoke generated in the charcoal manufacturing process and the carbonization process, and to efficiently generate the heat generated when the smoke is extinguished. The purpose is to provide a new multi-purpose recycling device that is frequently used, thereby improving productivity and economic efficiency.

【0004】[0004]

【課題を解決するための手段】[Means for Solving the Problems]

上記目的を達成するため、この考案の多目的リサイクル装置は、炭材又は産業 廃棄物を炭化処理する炭化炉と、前記炭化炉で生じ、排出される排煙が煙道管を 介して供給され、前記排煙を完全燃焼させる燃焼式消煙装置と、この燃焼式消煙 装置の廃熱を利用して高含水率廃棄物を乾燥せしめる乾燥炉と、前記乾燥炉で発 生する排出ガスを燃焼させて消臭する消臭装置と、前記消臭装置で生ずる廃熱が 供給される蒸気発生装置と、前記蒸気発生装置で発生した水蒸気を用いて粉末活 性炭を生成する賦活装置とで構成したものである。 In order to achieve the above-mentioned object, the multipurpose recycling apparatus of the present invention comprises a carbonization furnace for carbonizing carbonaceous materials or industrial waste, and the flue gas generated and discharged in the carbonization furnace is supplied through a flue pipe, Combustion type smoke extinguishing device that completely burns the flue gas, drying furnace that uses the waste heat of this combustion type smoke extinguishing device to dry high moisture content waste, and burns the exhaust gas generated in the drying furnace It consists of a deodorizing device that deodorizes by doing so, a steam generating device to which waste heat generated in the deodorizing device is supplied, and an activating device that generates powdered activated carbon using the steam generated in the steam generating device. It was done.

【0005】 この考案によれば、炭材や産業廃棄物を所定の大きさに破砕して炭材篭に入れ て炭化炉の自動点火バーナーで連続炭化処理して活性炭や有機肥料などの炭素系 炭化物を生成する。 一方、前記炭化炉で生ずる煙が煙道管を介して燃焼式消煙装置に供給され、炉 内温度を約1500℃の高温にすることで、前記煙は完全燃焼され無煙となって 排出される。この燃焼式消煙装置で発生する約1000℃の熱は高含水率廃棄物 の乾燥炉に供給され、この乾燥炉内で乾燥された材料は粉砕され選別処理されて 有機肥料や飼料、医薬品などの原料として使用される。According to the present invention, carbonaceous materials and industrial waste are crushed to a predetermined size, placed in a carbonaceous material basket, and continuously carbonized by an automatic ignition burner of a carbonization furnace to activate carbonaceous materials such as activated carbon and organic fertilizer. Generates carbide. On the other hand, the smoke generated in the carbonization furnace is supplied to the combustion type smoke eliminator through the flue pipe, and the temperature inside the furnace is raised to a high temperature of about 1500 ° C, so that the smoke is completely burned and becomes smokeless and discharged. It The heat of about 1000 ℃ generated by this combustion type smoke eliminator is supplied to the drying furnace for high-moisture content waste, and the material dried in this drying furnace is crushed and sorted to treat organic fertilizers, feed, pharmaceuticals, etc. Used as a raw material.

【0006】 更に、乾燥炉で発生する臭気や悪臭ガスなどの排出ガスを消臭装置に供給し、 前記燃焼式消煙装置と同様に排出ガスを完全燃焼させて消臭又は脱臭して無臭無 害にする。 この消臭装置で発生する熱は蒸気発生装置や温水発生装置に供給され、蒸気発 生装置で生成した水蒸気を用いて粉末活性炭を賦活製造することができ、また、 温水発生装置で生成した温水が給湯設備に供給され利用される。 更に、前記水蒸気又は温水が暖房設備供給されて利用される。Further, exhaust gas such as odor or malodorous gas generated in the drying furnace is supplied to the deodorizing device, and the exhaust gas is completely burned to deodorize or deodorize in the same manner as in the combustion-type smoke eliminating device. Do harm The heat generated by this deodorizer is supplied to the steam generator and hot water generator, and the activated carbon powder can be activated and produced using the steam generated by the steam generator, and the hot water generated by the hot water generator can be used. Is supplied to the hot water supply facility for use. Further, the steam or hot water is supplied to a heating facility for use.

【0007】[0007]

【考案の実施の形態】[Embodiment of device]

この考案に係る多目的リサイクル装置の実施例を図1のブロック図に基づいて 説明する。 図において、1は木炭を生成する炭材、2は本考案の炭化炉を利用して炭化処 理を行うための産業廃棄物、3は炭材1や産業廃棄物2を所定サイズに破砕する 破砕機、4は炭化炉、5は炭化炉4で炭素系炭化物となって生成される活性炭、 6は前記同様に炭素系炭化物となって生成される有機肥料である。 An embodiment of the multipurpose recycling apparatus according to the present invention will be described based on the block diagram of FIG. In the figure, 1 is a carbonaceous material for producing charcoal, 2 is an industrial waste for performing a carbonization treatment using the carbonization furnace of the present invention, and 3 is a crushed carbonaceous material 1 or industrial waste 2 into a predetermined size. Crusher, 4 is a carbonization furnace, 5 is activated carbon produced as carbonaceous carbide in the carbonization furnace 4, and 6 is an organic fertilizer produced as carbonaceous carbide as described above.

【0008】 7は炭化炉4の炭化処理工程で生じ、排出される排煙を示し、この排煙7は燃 焼式消煙装置8で完全燃焼される。9は燃焼式消煙装置8で発生し、排出される 廃熱を示し、廃熱9が供給される乾燥炉11では、この廃熱9を利用して水分の 多い高含水率廃棄物10を乾燥せしめる。 そして、乾燥炉11で乾燥せしめた廃棄物10は粉砕機12で粉砕され、選別 機13で選別処理されて有機肥料、飼料又は医薬品14の原料となる。 15は乾燥炉11内で発生し、排出される排出ガスであり、この排出ガス15 は臭気を有する悪臭ガスであって消臭装置16に供給され完全燃焼されて無臭無 害となる。17は消臭装置16で発生し、排出される廃熱であり、この廃熱17 は蒸気発生装置18に導かれ、賦活装置19では蒸気発生装置18で発生した水 蒸気を使って粉末活性炭20の賦活処理を行うようになっている。 又、21は廃熱17によって温水を得る温水発生装置であり、この温水発生装 置21の温水は給湯設備22や暖房設備23に供給される。Reference numeral 7 denotes smoke emitted from the carbonization process of the carbonization furnace 4 and discharged. The smoke 7 is completely combusted by a combustion type smoke eliminating device 8. Reference numeral 9 indicates the waste heat generated and discharged in the combustion type smoke eliminator 8. In the drying furnace 11 to which the waste heat 9 is supplied, the waste heat 9 is used to generate a high water content waste 10 having a high water content. Let it dry. Then, the waste 10 dried in the drying furnace 11 is crushed by the crusher 12 and sorted by the sorter 13 to be a raw material for the organic fertilizer, feed or medicine 14. Reference numeral 15 is an exhaust gas generated and discharged in the drying furnace 11. The exhaust gas 15 is a malodorous gas having an odor and is supplied to the deodorizing device 16 and completely combusted to be odorless and harmless. Reference numeral 17 denotes waste heat generated in the deodorizer 16 and discharged. The waste heat 17 is guided to the steam generator 18, and the activation device 19 uses the water vapor generated in the steam generator 18 to activate the powdered activated carbon 20. The activation process is performed. Reference numeral 21 is a hot water generator that obtains hot water from the waste heat 17, and the hot water of the hot water generator 21 is supplied to the hot water supply equipment 22 and the heating equipment 23.

【0009】 このように構成された本考案のリサイクルプラントシステムの炭化処理は、木 材、竹材等の原料である炭材1や木くず、古タイヤ、脱水汚泥等の産業廃棄物2 が所定の大きさに破砕機3で破砕されて炭化炉4で炭化処理される。 本考案の炭化炉4は以下のように構成されている。 即ち、炭材を入れる篭の実容積を5m3とし、その素材を全てステンレス製に する。この炭材篭を入れる炭化炉4は、鉄製で炉の内面をキャスタブルと耐火モ ルタルで加工し保温と断熱効果を良くする。 次に、原料への着火を早めるため自動点火バーナーで炉の上部面より均一に火 流する構造にした。これに依って、点火から着火までの時間が従来より1/3〜 1/4に短縮される。In the carbonization treatment of the recycling plant system of the present invention configured as described above, the carbonaceous material 1 which is a raw material of wood, bamboo and the like and the industrial waste 2 such as wood waste, old tires, dehydrated sludge and the like have a predetermined size. Furthermore, it is crushed by the crusher 3 and carbonized in the carbonization furnace 4. The carbonization furnace 4 of the present invention is configured as follows. That is, the actual volume of the basket containing the carbonaceous material is set to 5 m 3, and all the materials are made of stainless steel. The carbonization furnace 4 in which this carbon cage is put is made of iron, and the inner surface of the furnace is castable and refractory to improve heat retention and heat insulation. Next, in order to speed up the ignition of the raw materials, an automatic ignition burner was used to create a structure in which the flow was even from the upper surface of the furnace. As a result, the time from ignition to ignition is shortened to 1/3 to 1/4 as compared with the conventional case.

【0010】 更に、炉内温度のコントロールを自動的に行うと共に、煙突の高さを炭材篭の 高さの2倍にすることによって、着火後の自燃効率をアップさせ、炭化物の生産 歩止りを向上させた。 この炭化炉では良質の炭化物を12時間の工程で処理することが出来る。Furthermore, the temperature inside the furnace is automatically controlled, and the height of the chimney is made twice as high as the height of the carbon cage, so that the self-combustion efficiency after ignition is increased and the production yield of carbide is reduced. Improved. In this carbonization furnace, good quality carbide can be processed in a process of 12 hours.

【0011】 このようにして炭化処理された炭素系炭化物は活性炭5や有機肥料6又は土壌 改良剤として利用される。更に、炭化炉4での炭化処理工程において生ずる排煙 7は、燃焼式消煙装置8に供給され無煙になる。 消煙方法は、燃焼式で円筒型の燃焼炉底部に煙導管を連結し、煙は燃焼炉の底 面より流入させる。炉内底部側面に燃料(灯油、重油、廃油)を0.5リットル 程度注入し、炉内中心部に設置した多孔を施したパイプから送風機によって炉内 にエアーを吹き込む、炉内ではエアーの対流作用により燃料は気化し、着火する と完全燃焼の状態になる。その際の炉内温度は1500℃前後で、温度の調整は 送風機の風量及び燃料の注入量で行い、その機能は電気制御によってコントロー ルされる。The carbon-based carbide thus carbonized is used as activated carbon 5, organic fertilizer 6 or a soil conditioner. Further, the flue gas 7 produced in the carbonization process in the carbonization furnace 4 is supplied to the combustion type smoke eliminator 8 and becomes smokeless. As for the smoke elimination method, a smoke conduit is connected to the bottom of a combustion-type cylindrical combustion furnace, and smoke is introduced from the bottom surface of the combustion furnace. About 0.5 liter of fuel (kerosene, heavy oil, waste oil) is injected into the bottom side of the furnace, and air is blown into the furnace by a blower from the perforated pipe installed in the center of the furnace. The fuel is vaporized by the action, and when ignited, it becomes a state of complete combustion. At that time, the temperature inside the furnace is around 1500 ° C, and the temperature is adjusted by the air volume of the blower and the injection amount of fuel, and its function is controlled by electrical control.

【0012】 炉内温度が1500℃前後になるには3分〜5分の時間を要し完全燃焼状態に なったところで、煙を流入させ気化した燃料と混合され更に完全燃焼させる。 従って燃焼炉の排気口では無煙となり透明な気体として排出される。排気口で の温度は約1000℃前後になっている。It takes 3 to 5 minutes for the temperature in the furnace to reach around 1500 ° C., and when a complete combustion state is reached, smoke is introduced and mixed with the vaporized fuel to complete combustion. Therefore, no smoke is emitted at the exhaust port of the combustion furnace and the gas is discharged as a transparent gas. The temperature at the exhaust port is around 1000 ° C.

【0013】 燃焼式消煙装置8から排出される約1000℃の廃熱9は高含水率廃棄物10 が供給される乾燥炉11の熱源として使用される。この乾燥炉11の内部には耐 熱コンベヤー(図示せず)が設置されていて、この耐熱コンベヤーに水分の多い 高含水率廃棄物10を載置させて前記廃熱9を利用して乾燥させる。この乾燥し た高含水率廃棄物10は粉砕機12で粉末状に粉砕され、選別機13で選別処理 されて有機肥料、飼料又は医薬品14等の原料として利用される。The waste heat 9 of about 1000 ° C. discharged from the combustion type smoke eliminator 8 is used as a heat source of the drying furnace 11 to which the high water content waste 10 is supplied. A heat resistant conveyor (not shown) is installed inside the drying furnace 11, and a high moisture content waste 10 having a large amount of water is placed on the heat resistant conveyor and dried using the waste heat 9. . The dried high-moisture content waste 10 is pulverized by a pulverizer 12 into powder, and is sorted by a sorter 13 to be used as a raw material for organic fertilizers, feeds or pharmaceuticals 14.

【0014】 一方、乾燥炉11で発生した排出ガス15は消臭装置16に供給される。乾燥 炉11の排出ガス15は臭気を有する悪臭ガスであるから、この悪臭ガスは燃焼 式消煙装置8と同様に消臭装置16で完全燃焼されて消臭又は脱臭され無臭無害 となる。 また、消臭装置16で廃出される廃熱17は高温であるため、蒸気発生装置1 8や温水発生装置21に供給され、蒸気発生装置18では水蒸気を生成し、この 水蒸気を使って粉末活性炭20生成のために必要な賦活装置19に利用される。 また、廃熱21を利用して温水発生装置21で生成された温水は給湯設備22や 暖房設備23に供給されて利用される。On the other hand, the exhaust gas 15 generated in the drying furnace 11 is supplied to the deodorizing device 16. Since the exhaust gas 15 of the drying furnace 11 is a malodorous gas having an odor, this malodorous gas is completely burned by the deodorizing device 16 like the combustion type smoke eliminating device 8 to be deodorized or deodorized to be harmless and odorless. Further, since the waste heat 17 discharged in the deodorizer 16 is high in temperature, it is supplied to the steam generator 18 and the hot water generator 21, and the steam generator 18 generates steam, which is used to generate powdered activated carbon. 20 is used for the activation device 19 required for generation. The hot water generated by the hot water generator 21 using the waste heat 21 is supplied to the hot water supply equipment 22 and the heating equipment 23 for use.

【0015】[0015]

【考案の効果】[Effect of device]

この考案に係る多目的リサイクル装置は前述のように構成して、炭化処理工程 で発生する排煙の処理工程で発生する廃熱、又、前記廃熱を利用した乾燥炉で発 生する有害排出ガスの処理工程で発生する廃熱をリサイクルして有機肥料や飼料 又は医薬品などの生成原料を作り出したり、更に、粉末活性炭の賦活処理を行う ことができるなど、簡単な構成で多目的なリサイクルシステムを構築することが できる。 The multi-purpose recycling apparatus according to the present invention is configured as described above, and waste heat generated in the process of treating the flue gas generated in the carbonization process, and harmful exhaust gas generated in the drying furnace using the waste heat. Constructing a versatile recycling system with a simple structure, such as recycling the waste heat generated in the treatment process to produce organic fertilizer, feed or pharmaceuticals and other raw materials, and activating powdered activated carbon. can do.

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

【図1】この考案に係る多目的リサイクル装置を示した
ブロック図である。
FIG. 1 is a block diagram showing a multipurpose recycling device according to the present invention.

【符号の説明】[Explanation of symbols]

4 炭化炉 8 燃焼式消煙装置 11 乾燥炉 16 消臭装置 18 蒸気発生装置 19 賦活装置 4 Carbonization furnace 8 Combustion type smoke eliminating device 11 Drying furnace 16 Deodorizing device 18 Steam generating device 19 Activating device

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C10B 53/02 ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI technical display location C10B 53/02

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】 炭材又は産業廃棄物を炭化処理する炭化
炉と、前記炭化炉で生じ、排出される排煙が煙道管を介
して供給され、前記排煙を完全燃焼させる燃焼式消煙装
置と、この燃焼式消煙装置の廃熱を利用して高含水率廃
棄物を乾燥せしめる乾燥炉と、前記乾燥炉で発生する排
出ガスを燃焼させて消臭する消臭装置と、前記消臭装置
で生ずる廃熱が供給される蒸気発生装置と、前記蒸気発
生装置で発生した水蒸気を用いて粉末活性炭を生成する
賦活装置とで構成したことを特徴とする多目的リサイク
ル装置。
1. A carbonization furnace for carbonizing carbonaceous materials or industrial waste, and a flue gas produced in and discharged from the carbonization furnace is supplied through a flue pipe to burn the flue gas completely. A smoke device, a drying furnace for drying high moisture content waste by utilizing waste heat of the combustion type smoke eliminating device, a deodorizing device for deodorizing by burning exhaust gas generated in the drying furnace, A multipurpose recycling apparatus comprising a steam generator to which waste heat generated in a deodorizer is supplied and an activating device that generates powdered activated carbon by using the steam generated in the steam generator.
JP1996000755U 1996-01-25 1996-01-25 Multipurpose recycling equipment Expired - Lifetime JP3027191U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1996000755U JP3027191U (en) 1996-01-25 1996-01-25 Multipurpose recycling equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1996000755U JP3027191U (en) 1996-01-25 1996-01-25 Multipurpose recycling equipment

Publications (1)

Publication Number Publication Date
JP3027191U true JP3027191U (en) 1996-07-30

Family

ID=43162314

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1996000755U Expired - Lifetime JP3027191U (en) 1996-01-25 1996-01-25 Multipurpose recycling equipment

Country Status (1)

Country Link
JP (1) JP3027191U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000024671A1 (en) * 1998-10-28 2000-05-04 Ebara Corporation Waste carbonizing method
US11525167B2 (en) 2017-06-16 2022-12-13 Arcelormittal Operating method of an iron making installation and associated operating installation

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5632036A (en) * 1979-08-22 1981-04-01 Yamaha Motor Co Ltd Combustion chamber for two-stroke-cycle gasoline engine
JPH01312313A (en) * 1988-06-13 1989-12-18 Mitsubishi Heavy Ind Ltd Garbage incineration equipment
JPH06271307A (en) * 1993-03-02 1994-09-27 Marukoshi Eng:Kk Equipment for producing activated carbon from waste polymer
JPH0788457A (en) * 1993-09-20 1995-04-04 Hitachi Ltd System and method for utilizing waste

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5632036A (en) * 1979-08-22 1981-04-01 Yamaha Motor Co Ltd Combustion chamber for two-stroke-cycle gasoline engine
JPH01312313A (en) * 1988-06-13 1989-12-18 Mitsubishi Heavy Ind Ltd Garbage incineration equipment
JPH06271307A (en) * 1993-03-02 1994-09-27 Marukoshi Eng:Kk Equipment for producing activated carbon from waste polymer
JPH0788457A (en) * 1993-09-20 1995-04-04 Hitachi Ltd System and method for utilizing waste

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000024671A1 (en) * 1998-10-28 2000-05-04 Ebara Corporation Waste carbonizing method
US11525167B2 (en) 2017-06-16 2022-12-13 Arcelormittal Operating method of an iron making installation and associated operating installation

Similar Documents

Publication Publication Date Title
EP3012037A1 (en) Production line and method for recycling of charcoal and gas from garbage
WO2017158649A1 (en) Semi-carbonized plant biomass production apparatus
CN102476907A (en) Equipment and method of high-efficiency high-speed environmentally-friendly energy-saving sludge treatment system
CN107162373A (en) A kind of pig manure method of comprehensive utilization based on carbonization pyrolytic technique
CN106424101A (en) Method for harmlessly treating household garbage by carbonization, pyrolysis and gasification
KR101152613B1 (en) System for treating sludge or waste having a by-pass line
KR200380974Y1 (en) Energy saving type sludge carbonization equipment using regenerative heat exchanger
JP2014037955A (en) Device for continuously producing warm water using woodchip biomass as fuel
CN207514918U (en) A kind of rubbish cooperates with incinerating and treating device with semi-dry sludge
JP3858123B2 (en) Treatment method by carbonization of waste
CN203669943U (en) Energy-saving power generation device by using solid wastes
JP3027191U (en) Multipurpose recycling equipment
WO2011027394A1 (en) Waste treatment method
CN204769832U (en) Pyrolysis system is burned in mummification of birds that dies of illness poultry
CN210826081U (en) Double-bed pyrolysis gasification device for municipal domestic waste
JP2008106209A (en) Small carbonization furnace with distributed power generation function
CN104781376A (en) Process and device for production of compacted fertilizer charcoal
JP3479628B2 (en) Carbonization equipment
JP4295942B2 (en) Production facilities for dry fertilizer made from livestock manure
CN207661783U (en) A kind of small-sized rubbish gas charcoal complementation charing combustion furnace
JP7444518B1 (en) Oil palm char production method
US1957364A (en) Carbonizing process and apparatus
JP3545504B2 (en) Method and apparatus for producing solid fuel
CN204111602U (en) A kind of refuse pyrolysis gas prepares unslaked lime system
JP2002303409A (en) Thermal decomposition treating method for poultry manure, and special fertilizer using its residue, and soil improving agent