JP2000044372A - Composting facility of circulated air-conditioning type - Google Patents
Composting facility of circulated air-conditioning typeInfo
- Publication number
- JP2000044372A JP2000044372A JP24770898A JP24770898A JP2000044372A JP 2000044372 A JP2000044372 A JP 2000044372A JP 24770898 A JP24770898 A JP 24770898A JP 24770898 A JP24770898 A JP 24770898A JP 2000044372 A JP2000044372 A JP 2000044372A
- Authority
- JP
- Japan
- Prior art keywords
- air
- fermentation
- composting
- section
- facility
- 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
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
- Y02W10/37—Wastewater or sewage treatment systems using renewable energies using solar energy
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/40—Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse
Landscapes
- Processing Of Solid Wastes (AREA)
- Treatment Of Sludge (AREA)
- Fertilizers (AREA)
Abstract
(57)【要約】
【目的】 汚泥等の堆肥化を安定した高い効率で行うこ
とができる、省エネルギー型、環境保全型の堆肥化施設
を提供するにある。
【構成】 汚泥等を堆肥化する施設において、連続する
一次発酵工程1と二次発酵工程2及び乾燥工程3を保温
材4で囲い、乾燥工程3の端に吹き出し部5、反対側の
一次発酵工程1の端に吸い込み部6、及び吸い込み部6
と吹き出し部5とを連通するダクト7の経路中に空気調
和装置を設け、吸い込み部6から吹き出し部5へ向かう
ダクト7内と、吹き出し部5から吸い込み部6へ向かう
囲い4内に循環した空気の流れを形成する送風機11を
設けたことを特徴とする。
(57) [Summary] [Objective] An object of the present invention is to provide an energy-saving and environmentally-friendly composting facility capable of stably and efficiently composting sludge and the like. [Constitution] In a facility for composting sludge, etc., a continuous primary fermentation step 1, a secondary fermentation step 2, and a drying step 3 are surrounded by a heat insulating material 4, and a blowing section 5 is provided at an end of the drying step 3, and a primary fermentation on the opposite side. At the end of step 1, a suction unit 6 and a suction unit 6
An air conditioner is provided in a path of a duct 7 that communicates with the air outlet 5, and air circulated in the duct 7 from the suction unit 6 to the air outlet 5 and in the enclosure 4 from the air outlet 5 to the air inlet 6. Characterized in that a blower 11 for forming a flow is provided.
Description
【0001】[0001]
【産業上の利用分野】下水の汚泥等の堆肥化施設に関す
る。The present invention relates to a facility for composting sewage sludge.
【0002】[0002]
【従来の技術】従来の技術として、汚泥堆肥化施設の代
表例を図3に示す。一次発酵槽41へ投入された被堆肥
化物15は一次発酵処理後、二次発酵槽42、乾燥機4
3の順にベルトコンベヤー44等により移送され、それ
ぞれの処理が行われる。一次、二次の発酵槽41、42
では発酵に必要な酸素を供給するための給気45と悪臭
の槽外への発散を抑制するための排気46を、乾燥機4
3では乾燥に必要な熱風の送気47と発生ガスの排気4
8を行っている。このような施設では、以下の問題点が
ある。 一次、二次の発酵槽41、42は外気温度の影響を
受け易く、外気温度によっては堆肥化の効率が悪くな
る。特に冬期は発酵に長時間を要し、発酵できない場合
もある。 発酵によって発生した水蒸気が槽内で飽和状態とな
って、結露し、被堆肥化物15の水分蒸発を妨げてい
る。 一次、二次の発酵槽41、42と乾燥機43及び各
工程間の被堆肥化物の移動中が悪臭の発生源となり、作
業環境や周辺環境の悪化の原因となっている。悪臭対策
を行う場合、各発生源に排気や脱臭の設備を設置するこ
とが必要となり、設備が大型化して、費用がかさむ。 燃料49使用の乾燥機43からの発生ガスの排気4
8は、大気汚染や地球温暖化の原因となる。2. Description of the Related Art As a conventional technique, a typical example of a sludge composting facility is shown in FIG. The compost 15 put into the primary fermenter 41 is subjected to the primary fermentation treatment, and then the secondary fermenter 42 and the dryer 4
They are transported by the belt conveyor 44 and the like in the order of 3, and each processing is performed. Primary and secondary fermenters 41, 42
In the dryer 4, an air supply 45 for supplying oxygen necessary for fermentation and an exhaust 46 for suppressing the emission of offensive odor to the outside of the tank are provided.
In 3, hot air supply 47 required for drying and generated gas exhaust 4
8 has been done. Such a facility has the following problems. The primary and secondary fermenters 41 and 42 are easily affected by the outside air temperature, and the efficiency of composting is reduced depending on the outside air temperature. Especially in the winter season, fermentation takes a long time and fermentation may not be possible. The water vapor generated by the fermentation becomes saturated in the tank and forms dew, thereby preventing water evaporation of the compost 15. The primary and secondary fermenters 41 and 42, the dryer 43, and the movement of the compost between the respective steps are sources of foul odors and cause deterioration of the working environment and the surrounding environment. When taking countermeasures against odors, it is necessary to install exhaust and deodorizing equipment at each generation source, which increases the size of the equipment and increases costs. Emission of generated gas 4 from dryer 43 using fuel 49
No. 8 causes air pollution and global warming.
【0003】[0003]
【発明が解決しようとする課題】本発明は上述の問題点
に鑑みてなされたものであり、目的とするところは、以
下の効果を達成し、以て、汚泥等の堆肥化を安定した高
い効率で行うことができる、省エネルギー型、環境保全
型の堆肥化施設を提供するにある。 発酵槽内の空気調和を行い、温度、湿度、酸素濃度
等を調整し、微生物の反応に適した環境条件に整えるこ
とによって、発酵を促進させ、発酵期間の短縮や水分蒸
発の効率化を図る。 発酵熱や乾燥後の排熱の外気への放出を抑え、熱回
収し、有効利用を図る。 上記で堆肥化の効率を高めることによって、悪臭
の発生源となる発酵槽と乾燥機等のコンパクト化、及び
排気、脱臭設備の小型化を図り、悪臭の周辺環境への発
散を抑制することを容易とする。 乾燥には、大気汚染や地球温暖化の原因となる燃料
による熱風は用いず、乾燥効率の高い乾・温風を使用す
る。 発酵温度が十分に上がらない場合であっても、堆肥
中の病原菌や寄生虫卵あるいは雑草の種子を確実に死滅
又は不活性化させることができるものとする。SUMMARY OF THE INVENTION The present invention has been made in view of the above-mentioned problems, and has as its object to achieve the following effects, thereby achieving a stable high composting of sludge and the like. An object of the present invention is to provide an energy-saving and environmentally-friendly composting facility that can be performed efficiently. Air conditioning in the fermenter, adjusting temperature, humidity, oxygen concentration, etc., and setting environmental conditions suitable for microbial reactions to promote fermentation, shorten fermentation period, and improve water evaporation efficiency . It suppresses the release of fermentation heat and waste heat after drying to the outside air, recovers heat, and aims for effective utilization. By increasing the efficiency of composting above, the fermenters and dryers, which are the sources of offensive odors, will be made more compact, and the exhaust and deodorizing equipment will be made smaller, thereby suppressing the emission of offensive odors to the surrounding environment. Be easy. For drying, hot air from fuel that causes air pollution and global warming is not used, but dry and warm air with high drying efficiency is used. Even when the fermentation temperature does not rise sufficiently, pathogenic bacteria, parasite eggs or weed seeds in the compost can be reliably killed or inactivated.
【0004】[0004]
【課題を解決するための手段】本発明は、上述の目的を
達成するため、次の構成をそなえる。すなわち、汚泥等
を堆肥化する施設において、連続する一次発酵工程1と
二次発酵工程2及び乾燥工程3を保温材4で囲い、乾燥
工程3の端に吹き出し部5、反対側の一次発酵工程1の
端に吸い込み部6、及び吸い込み部6と吹き出し部5と
を連通する循環空気用ダクト7経路中に熱交換器8、冷
却コイル9、加熱コイル10等の空気調和装置を設け、
吸い込み部6から吹き出し部5へ向かう循環空気用ダク
ト7内と、吹き出し部5から吸い込み部6へ向かう囲い
4内に循環した空気の流れを形成する循環空気用送風機
11を設けたことを特徴とする。The present invention has the following configuration to achieve the above object. That is, in a facility for composting sludge or the like, a continuous primary fermentation step 1, a secondary fermentation step 2, and a drying step 3 are surrounded by a heat insulating material 4, and a blowing section 5 is provided at an end of the drying step 3, and a primary fermentation step on the opposite side. At one end, an air conditioner such as a heat exchanger 8, a cooling coil 9, and a heating coil 10 is provided in a path of a suction section 6 and a duct 7 for circulating air that communicates the suction section 6 and the blowing section 5,
A circulating air blower 11 for forming a flow of air circulating in a duct 7 for circulating air from the suction section 6 to the blowing section 5 and in the enclosure 4 from the blowing section 5 to the suction section 6 is provided. I do.
【0005】[0005]
【作用】次に作用について述べる。 循環空気用送風機11によって一次発酵工程1の端
の吸い込み部6から吸い込まれた循環空気は、熱交換器
8で熱回収、冷却コイル9で冷却除湿、加熱コイル10
で加熱され、乾・温風となって乾燥工程3の端の吹き出
し部5より吹き出し、乾燥工程3の水分蒸発を促進す
る。 乾燥工程3で減温、加湿された循環空気は、二次と
一次の発酵のそれぞれの微生物反応に適した温、湿度と
なり、二次、一次の順に流れ、それぞれの発酵を促進す
る。 給気用の送風機12の吸い込みによって熱交換器8
に入った外気は、加温された後、発酵に必要な酸素を供
給するため、給気用ダクト13を経て床面に設けた給気
部14より一次と二次の発酵工程1、2全域に給気され
る。 一次と二次の発酵工程1、2及び乾燥工程3を保温
材4で囲うことにより、発酵熱や乾燥後の排熱の外気へ
の放出を抑え、囲い4内での有効利用を図る、とともに
悪臭の周辺環境への発散を抑制する。 発酵温度が十分に上がらない場合、加熱コイル10
の温度調整で、循環空気の温度を上げることで、被堆肥
化物中の病原菌や寄生虫卵あるいは雑草の種子を確実に
死滅又は不活性化させる。Next, the operation will be described. The circulating air sucked from the suction section 6 at the end of the primary fermentation step 1 by the circulating air blower 11 recovers heat in the heat exchanger 8, cools and dehumidifies in the cooling coil 9, and cools the heating coil 10.
, And is blown out from the blowing section 5 at the end of the drying step 3 to promote evaporation of water in the drying step 3. The circulating air whose temperature has been reduced and humidified in the drying step 3 has a temperature and humidity suitable for each of the microbial reactions of the secondary and primary fermentation, flows in the order of secondary and primary, and promotes each fermentation. The heat exchanger 8 is sucked by the air supply blower 12.
The outside air that has entered is heated and then supplied to the floor via an air supply duct 13 to supply oxygen necessary for fermentation. Is supplied with air. By surrounding the primary and secondary fermentation steps 1, 2 and the drying step 3 with the heat insulating material 4, the release of fermentation heat and exhaust heat after drying to the outside air is suppressed, and the effective use in the enclosure 4 is achieved. Suppresses the release of offensive odors to the surrounding environment. If the fermentation temperature does not rise sufficiently,
By raising the temperature of the circulating air by adjusting the temperature, the pathogens, parasite eggs or weed seeds in the compost can be reliably killed or inactivated.
【0006】[0006]
【実施例】本発明の好適な実施例を2例挙げ、図面に基
づいて説明する。 (1)第1実施例 図1は本発明に係わる循環空気調和型堆肥化施設の実施
例を示す説明図である。投入口16より投入された被堆
肥化物15は、一次発酵工程1、二次発酵工程2、乾燥
工程3の順に処理が行われ、堆肥化された製品は排出口
17より搬出される。この3つの工程全体は保温材4で
囲われ、それぞれの工程の境は開閉式の整流板18、1
9で仕切られている。20は切り返し機で3つの工程を
走査し、被堆肥化物15の移動と攪拌を行う。次にこの
実施例の作用について説明する。 循環空気用送風機11によって一次発酵工程1の端
の吸い込み部6から吸い込まれた循環空気は、熱交換器
8で熱回収、冷却塔21を用いた冷却コイル9で冷却除
湿、太陽熱集熱器22と補助熱源23を用いた加熱コイ
ル10で加熱され、乾・温風となって乾燥工程3の端の
吹き出し部5より吹き出し、乾燥工程3の水分蒸発を促
進する。 乾燥工程3で減温、加湿された循環空気は、二次と
一次の発酵のそれぞれの微生物反応に適した温、湿度と
なり、二次、一次の順に流れ、それぞれの発酵を促進す
る。なお、3つの工程の境の整流板18、19は、囲い
4の中の循環空気の流れを抑制し、各工程に適した環境
条件を形成する、とともに囲い4の中の循環空気の流れ
を整える役割を担う。 給気用の送風機12の吸い込みによって熱交換器8
に入った外気は、加温された後、発酵に必要な酸素を供
給するため、給気用ダクト13を経て床面に設けた給気
部14より一次と二次の発酵工程1、2全域に給気され
る。 流量調整ダンパ24の開閉で循環空気の吹き出し量
を吸い込み量よりも少なくし、囲い4内の負圧化を図
り、悪臭の囲い4外への発散を抑える。吸い込み量から
吹き出し量を差し引いた分は、流量調整ダンパ24から
排気用ダクト25を経て、脱臭塔26で処理された後、
大気へ排出される。 (2)第2実施例 一次発酵工程に投入する被堆肥化物の含水率が高く、又
変動する場合は、前工程で含水率の調整を行うことが必
要となる。第2実施例は、第1実施例を応用したもの
で、従来、発酵の前工程で行っている混合を一次発酵工
程の上部で行い、この混合場所に乾・温風の循環空気の
一部を送り、混合しながら被堆肥化物の乾燥を行い、含
水率を調整するものである。図2は第2実施例を示す説
明図である。31は攪拌式の混合機、32は混合機に設
けた吹き出し部、33は吸い込み部である。循環空気用
送風機11の風量を上げ、流量調整ダンパ34によっ
て、加熱コイル35、吹き出し部32、混合機31内、
吸い込み部33の順に流れる循環空気の量を調整する。
吸い込み部33に吸い込まれた循環空気は、連通口37
を通って、一次発酵工程1の吸い込み部6より吸い込ま
れる。混合機31は密閉構造であり、機内は負圧化さ
れ、悪臭の発散は抑制される。混合機の投入口38より
投入された被堆肥化物15は、攪拌によって副資材と混
合されながら乾燥された後、投入口16より一次発酵工
程1に投入される。被堆肥化物15の含水率の調整は、
加熱コイル35の温度と混合機31内を流れる循環空気
量及び乾燥時間によって行う。DESCRIPTION OF THE PREFERRED EMBODIMENTS Two preferred embodiments of the present invention will be described with reference to the drawings. (1) First Embodiment FIG. 1 is an explanatory diagram showing an embodiment of a circulating air-conditioning type composting facility according to the present invention. The compost 15 input from the input port 16 is processed in the order of the primary fermentation step 1, the secondary fermentation step 2, and the drying step 3, and the composted product is discharged from the discharge port 17. The entire three processes are surrounded by a heat insulating material 4, and the boundaries between the processes are opened and closed rectifying plates 18, 1 and 2.
It is divided by nine. Reference numeral 20 denotes a turning machine which scans three steps to move and agitate the compost 15. Next, the operation of this embodiment will be described. The circulating air sucked from the suction part 6 at the end of the primary fermentation step 1 by the circulating air blower 11 recovers heat in the heat exchanger 8, cools and dehumidifies in the cooling coil 9 using the cooling tower 21, and collects the solar heat collector 22. Is heated by the heating coil 10 using the auxiliary heat source 23, and is dried and becomes hot air, and is blown out from the blowing portion 5 at the end of the drying step 3, thereby promoting the evaporation of water in the drying step 3. The circulating air whose temperature has been reduced and humidified in the drying step 3 has a temperature and humidity suitable for each of the microbial reactions of the secondary and primary fermentation, flows in the order of secondary and primary, and promotes each fermentation. In addition, the rectifying plates 18 and 19 at the boundary of the three processes suppress the flow of the circulating air in the enclosure 4 to form environmental conditions suitable for each process, and reduce the flow of the circulating air in the enclosure 4. Takes the role of trimming. The heat exchanger 8 is sucked by the air supply blower 12.
The outside air that has entered is heated and then supplied to the floor via an air supply duct 13 to supply oxygen necessary for fermentation. Is supplied with air. By opening and closing the flow control damper 24, the amount of circulating air blown out is made smaller than the amount of suction, thereby reducing the pressure inside the enclosure 4 and suppressing the emission of offensive odors outside the enclosure 4. The amount obtained by subtracting the blowing amount from the suction amount is processed by the deodorization tower 26 from the flow control damper 24 through the exhaust duct 25,
Released to the atmosphere. (2) Second Example If the water content of the compost to be fed into the primary fermentation step is high and fluctuates, it is necessary to adjust the water content in the previous step. The second embodiment is an application of the first embodiment. Conventionally, the mixing performed in the previous step of fermentation is performed at the upper part of the primary fermentation step, and a part of the circulating air of dry and warm air is placed in the mixing place. To dry the compost while mixing and adjust the water content. FIG. 2 is an explanatory diagram showing the second embodiment. 31 is a stirring type mixer, 32 is a blowing section provided in the mixer, and 33 is a suction section. The air volume of the circulating air blower 11 is increased, and the heating coil 35, the blowing unit 32, the inside of the mixer 31,
The amount of circulating air flowing in the order of the suction unit 33 is adjusted.
The circulating air sucked into the suction part 33 is connected to the communication port 37.
Through the suction section 6 of the primary fermentation step 1. The mixer 31 has a hermetic structure, the inside of the mixer is made negative pressure, and emission of offensive odor is suppressed. The compost 15 input from the input port 38 of the mixer is dried while being mixed with the auxiliary material by stirring, and then input into the primary fermentation step 1 from the input port 16. Adjustment of the water content of the compost 15
This is performed based on the temperature of the heating coil 35, the amount of circulating air flowing in the mixer 31, and the drying time.
【0007】[0007]
【発明の効果】下水の汚泥等の堆肥化を本発明によって
行えば、以下のような顕著な効果を奏する。 発酵槽内の空気調和を行い、温度、湿度、酸素濃度
等を調整し、微生物の反応に適した環境条件に整えるこ
とによって、発酵を促進させ、発酵期間の短縮や水分蒸
発の効率化を図ることができる。 外気の温度、湿度の影響を受けることなく、安定し
た高い効率で堆肥化を行うことができる。 上記によって発酵槽を小さくすることで、また、
一次と二次の発酵及び乾燥の3つの工程を同一箇所で連
続して行うことで、施設のコンパクト化を図ることが可
能となり、これによって、設置の際、用地面積が少な
い、施設の設置費用が安価、施設の運転管理がし易い等
の利点がある。 排気、脱臭設備の小型化が図られ、悪臭の周辺環境
への発散を容易に抑えることができ、悪臭対策の経費が
少なくて良い。 発酵熱や乾燥後の排熱の熱回収、有効利用で省エネ
ルギー型である。 乾燥の熱源は、大気汚染や地球温暖化の原因となる
燃料を用いず、太陽熱を用いた乾燥効率の高い乾・温風
を使用し、環境保全型である。 循環空気の乾・温風は、従来の乾燥機の熱風と異な
り、高熱で発酵菌を死滅又は弱体化させることがない。
したがって、種菌としてできあがった堆肥を返送するこ
とにより菌の能力を高めることができる。よって、高価
な種菌を購入する必要がない。 発酵温度が上がらない場合であっても、補助熱源を
使い循環空気の温度を上げることで、被堆肥化物中の病
原菌や寄生虫卵あるいは雑草の種子を確実に死滅又は不
活性化させることができ、安全性が高い。 以上の効果により、下水の汚泥等の堆肥化を安定した高
い効率で行うことができる、省エネルギー型、環境保全
型の堆肥化施設を提供することが可能となる。以上、本
発明について好適な実施例を挙げて説明したが、本発明
はこの実施例に限定されるものではない。例えば、ここ
での実施例は横形の施設であるが、従来の立形の多段パ
ドルや多段落し戸の発酵槽にも設置することができ、こ
の場合、上段が一次発酵工程、中段が二次発酵工程、下
段が乾燥工程となり、吹き出し部は床面、吸い込み部は
天井に設けることになる。また、ここでの実施例は空気
調和の熱源に太陽熱を用いているが、ゴミ焼却炉の排熱
も利用することができる。その他発明の精神を逸脱しな
い範囲内で多くの改変を施し得る。According to the present invention, composting of sewage sludge and the like has the following remarkable effects. Air conditioning in the fermenter, adjusting temperature, humidity, oxygen concentration, etc., and setting environmental conditions suitable for microbial reactions to promote fermentation, shorten fermentation period, and improve water evaporation efficiency be able to. Composting can be performed stably with high efficiency without being affected by the temperature and humidity of the outside air. By making the fermenter smaller by the above,
By performing the three steps of primary and secondary fermentation and drying continuously at the same location, it is possible to reduce the size of the facility, thereby reducing the site area and setting up the facility. However, there are advantages such as low cost and easy operation management of facilities. The exhaust and deodorizing equipment can be reduced in size, the odor can be easily diffused into the surrounding environment, and the cost of odor control can be reduced. It is an energy-saving type with effective use and heat recovery of fermentation heat and waste heat after drying. The heat source for drying is an environmental conservation type that uses dry and warm air with high drying efficiency using solar heat without using fuel that causes air pollution and global warming. The dry and warm air of the circulating air is different from the hot air of a conventional dryer, and does not kill or weaken the fermentation bacteria due to high heat.
Therefore, by returning the compost completed as a seed fungus, the ability of the fungus can be enhanced. Therefore, there is no need to purchase expensive inoculum. Even if the fermentation temperature does not rise, by raising the temperature of the circulating air using an auxiliary heat source, it is possible to reliably kill or inactivate pathogens, parasite eggs, or weed seeds in the compost to be composted. High safety. With the above effects, it is possible to provide an energy-saving and environment-conserving composting facility that can stably and efficiently compost sewage sludge and the like. Although the present invention has been described with reference to the preferred embodiments, the present invention is not limited to these embodiments. For example, although the embodiment here is a horizontal facility, it can also be installed in a conventional vertical multi-stage paddle or multi-stage door fermenter, in which case the upper stage is the primary fermentation step and the middle stage is the second stage. The next fermentation step and the lower step are the drying step, and the blowing part is provided on the floor and the suction part is provided on the ceiling. Further, in this embodiment, solar heat is used as a heat source for air conditioning, but exhaust heat of a garbage incinerator can also be used. Many other modifications can be made without departing from the spirit of the invention.
【図1】第1実施例を示す説明図である。FIG. 1 is an explanatory diagram showing a first embodiment.
【図2】第2実施例を示す説明図である。FIG. 2 is an explanatory diagram showing a second embodiment.
【図3】従来の技術を示す説明図である。FIG. 3 is an explanatory diagram showing a conventional technique.
1・・・一次発酵工程 2・・・二次発酵工程 3・・・乾燥工程 4・・・保温材の囲い 5・・・吹き出し部 6・・・吸い込み部 7・・・循環空気用ダクト 8・・・熱交換器 9・・・冷却コイル 10・・・加熱コイル 11・・・循環空気用送風機 12・・・給気用送風
機 13・・・給気用ダクト 14・・・給気部 15・・・被堆肥化物 16・・・投入口 17・・・排出口 18・・・整流板
(a) 19・・・整流板(b) 20・・・切り返し機 21・・・冷却塔 22・・・太陽熱集熱
器 23・・・補助熱源 24・・・流量調整ダ
ンパ 25・・・排気用ダクト 26・・・脱臭塔 31・・・混合機 32・・・吹き出し部 33・・・吸い込み部 34・・・流量調整ダ
ンパ 35・・・加熱コイル 36・・・補助熱源 37・・・連通口 38・・・混合機の投
入口 41・・・一次発酵槽 42・・・二次発酵槽 43・・・乾燥機 44・・・ベルトコン
ベヤー 45・・・給気 46・・・排気 47・・・熱風の送気 48・・・発生ガスの
排気 49・・・燃料DESCRIPTION OF SYMBOLS 1 ... Primary fermentation process 2 ... Secondary fermentation process 3 ... Drying process 4 ... Enclosure of heat insulating material 5 ... Blow-out part 6 ... Suction part 7 ... Circulation air duct 8 ... heat exchanger 9 ... cooling coil 10 ... heating coil 11 ... blower for circulating air 12 ... blower for air supply 13 ... duct for air supply 14 ... air supply section 15 ... compostable material 16 ... inlet 17 ... outlet 18 ... rectifier plate (a) 19 ... rectifier plate (b) 20 ... turning machine 21 ... cooling tower 22. ..Solar heat collector 23 ... Auxiliary heat source 24 ... Flow rate adjustment damper 25 ... Exhaust duct 26 ... Deodorization tower 31 ... Mixer 32 ... Blow-out part 33 ... Suction part 34 ... Flow adjustment damper 35 ... Heating coil 36 ... Auxiliary heat source 37 ... Communication port 8 ... Inlet of mixer 41 ... Primary fermenter 42 ... Secondary fermenter 43 ... Dryer 44 ... Belt conveyor 45 ... Air supply 46 ... Exhaust 47 ...・ Air supply of hot air 48 ・ ・ ・ Exhaust of generated gas 49 ・ ・ ・ Fuel
Claims (1)
る一次発酵工程と二次発酵工程及び乾燥工程を保温材で
囲い、乾燥工程の端に吹き出し部、反対側の一次発酵工
程の端に吸い込み部、及び吸い込み部と吹き出し部とを
連通するダクト経路中に空気調和装置を設け、吸い込み
部から吹き出し部へ向かうダクト内と、吹き出し部から
吸い込み部へ向かう囲い内に循環した空気の流れを形成
する送風機を設けたことを特徴とする。In a facility for composting sludge, etc., a continuous primary fermentation step, a secondary fermentation step, and a drying step are surrounded by a heat insulating material, and a blowing section is provided at an end of the drying step, and an end of the primary fermentation step on the opposite side. An air conditioner is provided in a duct path that communicates the suction section and the suction section and the blowout section, and a flow of air circulated in a duct from the suction section to the blowout section and in an enclosure from the blowout section to the suction section. A fan to be formed is provided.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24770898A JP2000044372A (en) | 1998-07-29 | 1998-07-29 | Composting facility of circulated air-conditioning type |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24770898A JP2000044372A (en) | 1998-07-29 | 1998-07-29 | Composting facility of circulated air-conditioning type |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JP2000044372A true JP2000044372A (en) | 2000-02-15 |
Family
ID=17167490
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP24770898A Pending JP2000044372A (en) | 1998-07-29 | 1998-07-29 | Composting facility of circulated air-conditioning type |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2000044372A (en) |
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1998
- 1998-07-29 JP JP24770898A patent/JP2000044372A/en active Pending
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