JP2002113447A - Biodegradation processing device and biodegradation processing method - Google Patents
Biodegradation processing device and biodegradation processing methodInfo
- Publication number
- JP2002113447A JP2002113447A JP2000306185A JP2000306185A JP2002113447A JP 2002113447 A JP2002113447 A JP 2002113447A JP 2000306185 A JP2000306185 A JP 2000306185A JP 2000306185 A JP2000306185 A JP 2000306185A JP 2002113447 A JP2002113447 A JP 2002113447A
- Authority
- JP
- Japan
- Prior art keywords
- biodegradation
- stirring chamber
- temperature
- processing
- bacteria
- 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
Landscapes
- Processing Of Solid Wastes (AREA)
- Accessories For Mixers (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】この発明は、特に、生分解菌
として超好熱菌(超高温菌)を利用した高速分解消滅処
理を主眼とする生分解処理装置及び生分解処理方法に関
するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a biodegradation processing apparatus and a biodegradation processing method, which mainly focuses on high-speed decontamination treatment using hyperthermophiles (ultrathermophiles) as biodegradable bacteria. .
【0002】[0002]
【従来の技術及び発明が解決しようとする課題】従来、
高速分解消滅処理を主眼とする場合、生分解処理容器内
を高温に維持する必要がある。本発明は、種々の手段を
採用して、生分解処理容器内の高温状態を確実に保持し
て生分解菌を増殖させながら生分解処理を効率良く行う
ことを目的にしている。2. Description of the Related Art
When the main purpose is the high-speed disintegration treatment, it is necessary to maintain the inside of the biodegradation treatment container at a high temperature. SUMMARY OF THE INVENTION An object of the present invention is to efficiently carry out a biodegradation process while maintaining a high temperature state in a biodegradation treatment container and growing biodegradable bacteria by employing various means.
【0003】[0003]
【課題を解決するための手段及び発明の効果】後記実施
形態の図面(図1、図3及び図4(a)に示す第一実施
形態、図2、図3及び図4(b)に示す第二実施形態)
の符号を援用して本発明を説明する。Means for Solving the Problems and Effects of the Invention A drawing of a later-described embodiment (first embodiment shown in FIGS. 1, 3 and 4 (a), and FIGS. 2, 3 and 4 (b)) Second embodiment)
The present invention will be described with reference to the reference numerals.
【0004】* 請求項1の発明 この発明にかかる生分解処理装置(1)は、下記のよう
に構成されている。生分解処理容器(2)内に設けた攪
拌室(7)に攪拌機構(8)を備えている。この生分解
処理容器(2)にはこの攪拌室(7)に連通する処理物
供給部(14)と熱風供給部(15)と排気部(16)
とを設けている。この生分解処理容器(2)の外壁
(4,5,6)の一部または全部に設けた断熱材(2
5)によりこの攪拌室(7)を囲っている。* The invention of claim 1 The biodegradation treatment apparatus (1) according to the present invention is configured as follows. A stirring mechanism (8) is provided in a stirring chamber (7) provided in the biodegradation container (2). The biodegradation processing container (2) has a processing material supply unit (14), a hot air supply unit (15), and an exhaust unit (16) communicating with the stirring chamber (7).
Are provided. A heat insulating material (2) provided on part or all of the outer wall (4, 5, 6) of the biodegradation container (2)
The stirring chamber (7) is surrounded by 5).
【0005】生分解処理装置(1)において、生分解菌
として超好熱菌(超高温菌)を利用した高速分解消滅処
理を主眼とする場合、生分解処理容器(2)内を高温に
維持するため、攪拌機構(8)を設けて攪拌室(7)を
攪拌可能にし、熱風供給部(15)を設けて攪拌室
(7)に熱風を供給可能にし、排気部(16)を設けて
攪拌室(7)から水蒸気等を排気可能にしている。この
ような構造だけでも攪拌室(7)で高温を維持する上で
は有効であるが、さらに攪拌室(7)を高温状態で保持
するために攪拌室(7)の熱を生分解処理容器(2)の
外側に逃がさない目的で、断熱材(25)を利用した。
そのため、攪拌室(7)の高温状態をより一層確実に保
持することができる。従って、生分解菌を増殖させなが
ら生分解処理を効率良く行うことができる。[0005] In the biodegradation treatment apparatus (1), when the main object is a high-speed decontamination treatment using a hyperthermophilic bacterium (ultrathermophile) as a biodegradation bacterium, the inside of the biodegradation treatment vessel (2) is maintained at a high temperature. Therefore, a stirring mechanism (8) is provided so that the stirring chamber (7) can be stirred, a hot air supply section (15) is provided, hot air can be supplied to the stirring chamber (7), and an exhaust section (16) is provided. Steam and the like can be exhausted from the stirring chamber (7). Although such a structure alone is effective in maintaining a high temperature in the stirring chamber (7), the heat of the stirring chamber (7) is further reduced in order to maintain the stirring chamber (7) at a high temperature. In order not to escape to the outside of 2), a heat insulating material (25) was used.
Therefore, the high temperature state of the stirring chamber (7) can be more reliably maintained. Therefore, the biodegradation can be efficiently performed while the biodegradable bacteria are growing.
【0006】* 請求項2の発明 この発明は、請求項1の発明を前提として下記のように
構成されている。前記排気部(16)は前記攪拌室
(7)からの排気量を調節し得る排気量調節手段(2
2)を有している。この攪拌室(7)内の温度に応じて
この排気量調節手段(22)を動作し得る駆動手段(2
3,24)を設けている。* Invention of Claim 2 The present invention is configured as follows on the premise of the invention of Claim 1. The exhaust part (16) is an exhaust amount adjusting means (2) capable of adjusting an exhaust amount from the stirring chamber (7).
2). A driving means (2) capable of operating the exhaust amount adjusting means (22) according to the temperature in the stirring chamber (7).
3, 24) are provided.
【0007】この発明では、攪拌室(7)内の温度に応
じて攪拌室(7)からの水蒸気等の排気量を調節し得る
ので、請求項1の発明の効果に加えて、攪拌室(7)の
高温状態をより一層確実に保持し、生分解菌を増殖させ
ながら生分解処理を効率良く行うことができる。In the present invention, the amount of exhaust of water vapor or the like from the stirring chamber (7) can be adjusted according to the temperature in the stirring chamber (7). The high temperature state of 7) can be maintained more reliably, and the biodegradation can be efficiently performed while growing the biodegradable bacteria.
【0008】* 請求項3の発明 この発明は、請求項2の発明を前提として下記のように
構成されている。前記駆動手段は、前記攪拌室(7)に
設けた温度センサ(24)と、この温度センサ(24)
からの検知温度に応じて前記排気量調節手段(22)を
開閉動作し得る制御部(23)とを備えている。この発
明では、請求項2の発明の効果に加えて、攪拌室(7)
の高温状態の維持管理を容易に行うことができる。* Invention of Claim 3 The present invention is configured as follows on the premise of the invention of Claim 2. The driving means includes a temperature sensor (24) provided in the stirring chamber (7), and the temperature sensor (24)
And a control unit (23) capable of opening and closing the displacement adjusting means (22) in accordance with the temperature detected from the air conditioner. According to this invention, in addition to the effect of the invention of claim 2, the stirring chamber (7)
Can be easily maintained in a high temperature state.
【0009】* 請求項4の発明 この発明は、請求項3の発明を前提として下記のように
構成されている。前記制御部(23)は、前記温度セン
サ(24)からの検知温度が所定値以上になった場合
に、前記排気量調節手段(22)を開動作させる。この
発明では、請求項3の発明の効果に加えて、攪拌室
(7)の高温状態の維持管理をより一層容易に行うこと
ができる。* Invention of Claim 4 The present invention is configured as follows on the premise of the invention of Claim 3. The control section (23) opens the displacement control means (22) when the temperature detected by the temperature sensor (24) becomes equal to or higher than a predetermined value. According to this invention, in addition to the effect of the third aspect of the invention, the high temperature state of the stirring chamber (7) can be maintained and managed more easily.
【0010】* 請求項5の発明 この発明は、下記のように構成されている。請求項1か
ら請求項4のうちいずれかの請求項の発明にかかる生分
解処理装置(1)を有機性廃棄物回収自動車(28)の
車台(28a)に設置した。この発明では、請求項1か
ら請求項4のうちいずれかの請求項の発明の効果を有機
性廃棄物回収自動車(28)で有効に発揮して廃棄物処
理を促進することができる。* The invention of claim 5 The present invention is configured as follows. The biodegradation treatment device (1) according to any one of claims 1 to 4 is installed on a chassis (28a) of an organic waste collection vehicle (28). In this invention, the effects of the invention of any one of claims 1 to 4 can be effectively exhibited in the organic waste collection vehicle (28) to promote waste treatment.
【0011】* 請求項6の発明 この発明にかかる生分解処理方法は、下記のように構成
されている。生分解処理容器(2)内の攪拌室(7)に
処理物として生分解菌と菌宿体とを供給した状態で、こ
の処理物を攪拌する処理と、この攪拌室(7)に所定温
度の熱風を供給する処理と、この攪拌室(7)内の温度
が所定値以上になった場合にこの攪拌室(7)内の水蒸
気等を排気する処理とを互いに組み合わせてこの生分解
菌を増殖させながら生分解処理を行なう。* The invention of claim 6 The biodegradation treatment method according to the present invention is configured as follows. In a state where the biodegradable bacteria and the bacterial host are supplied to the stirring chamber (7) in the biodegradation processing container (2) as the processed material, the processed material is stirred, and the stirring chamber (7) is heated to a predetermined temperature. The process of supplying hot air and the process of exhausting water vapor or the like in the stirring chamber (7) when the temperature in the stirring chamber (7) becomes equal to or higher than a predetermined value are combined with each other to remove the biodegradable bacteria. Perform biodegradation while growing.
【0012】生分解処理方法において、生分解菌として
超好熱菌(超高温菌)を利用した高速分解消滅処理を主
眼とする場合、生分解処理容器(2)内を高温に維持す
るため、攪拌室(7)を攪拌し、攪拌室(7)に熱風を
供給し、攪拌室(7)から水蒸気等を排気し、攪拌室
(7)の高温状態を確実に保持して生分解菌を増殖させ
ながら生分解処理を効率良く行うことができる。In the biodegradation treatment method, when the main purpose is a high-speed elimination treatment using a hyperthermophilic bacterium (ultrathermophile) as a biodegradable bacterium, the inside of the biodegradation treatment container (2) is maintained at a high temperature. The stirring chamber (7) is stirred, hot air is supplied to the stirring chamber (7), steam and the like are exhausted from the stirring chamber (7), and the high temperature state of the stirring chamber (7) is reliably maintained to remove biodegradable bacteria. Biodegradation can be performed efficiently while growing.
【0013】* 請求項7の発明 この発明においては、請求項6の発明にかかる菌宿体が
粉末活性炭を含む。この発明では、この粉末活性炭によ
り、磁場の安定効果や消臭効果が生じるとともに、粉末
のため処理物への付着くい込みが良くなるなどの特色を
有し、生分解菌の増殖効果を高めたり生分解処理を効率
良く行うことができる。* Invention of Claim 7 In this invention, the fungal harbor according to the invention of Claim 6 contains powdered activated carbon. According to the present invention, the activated carbon powder has characteristics such as a magnetic field stabilizing effect and a deodorizing effect, and the powder has characteristics such as better adhesion to a treated material. The decomposition process can be performed efficiently.
【0014】[0014]
【発明の実施の形態】まず、本発明の第一実施形態にか
かる縦型生分解処理装置を図1、図3及び図4(a)を
参照して説明する。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS First, a vertical biodegradation processing apparatus according to a first embodiment of the present invention will be described with reference to FIGS. 1, 3 and 4 (a).
【0015】この縦型生分解処理装置1は回収自動車2
8の車台28aに設置されている。この縦型生分解処理
装置1において、生分解処理容器2は、周壁4と底壁5
とを有する容器本体3と、この容器本体3の上端部を閉
塞する蓋壁6とを備えている。この容器本体3と蓋壁6
とで囲まれた攪拌室7内には攪拌機構8が設置されてい
る。この攪拌機構8においては、生分解処理容器2の外
側に設置された駆動装置9により回転し得る回転軸10
が底壁5で回転可能に支持されて蓋壁6へ向けて鉛直に
延設され、この回転軸10に複数の回転羽根11が片持
梁状に取り付けられている。この各回転羽根11は、回
転軸10の回転中心線10aの方向へ並べられていると
ともに回転軸10の回転方向へ互いに所定角度ずつずら
して配置され、回転中心線10aに対し直交する半径方
向へ回転軸10から延びる腕板12と、この腕板12の
先端部に対し周壁4の付近で取着された羽根板13とを
有している。This vertical biodegradation treatment apparatus 1 is a collection vehicle 2
8 undercarriage 28a. In this vertical biodegradation processing apparatus 1, the biodegradation processing container 2 includes a peripheral wall 4 and a bottom wall 5.
And a lid wall 6 for closing the upper end of the container body 3. The container body 3 and the lid wall 6
A stirring mechanism 8 is installed in the stirring chamber 7 surrounded by. In the stirring mechanism 8, a rotating shaft 10 that can be rotated by a driving device 9 installed outside the biodegradation processing container 2.
Is rotatably supported by the bottom wall 5 and extends vertically toward the lid wall 6. A plurality of rotating blades 11 are attached to the rotating shaft 10 in a cantilever manner. The rotating blades 11 are arranged in the direction of the rotation center line 10a of the rotation shaft 10 and are arranged to be shifted from each other by a predetermined angle in the rotation direction of the rotation shaft 10, and are arranged in a radial direction orthogonal to the rotation center line 10a. The arm plate 12 includes an arm plate 12 extending from the rotation shaft 10, and a blade plate 13 attached to a distal end portion of the arm plate 12 near the peripheral wall 4.
【0016】前記生分解処理容器2の蓋壁6には処理物
供給部14と熱風供給部15と排気部16とが取り付け
られている。この処理物供給部14は開閉可能な投入口
17を有し、この投入口17が前記生分解処理容器2内
の攪拌室7に連通している。この熱風供給部15はこの
攪拌室7に連通する給気口18を有し、この生分解処理
容器2の外側に設置された加熱送風装置19にこの給気
口18が接続されている。この排気部16はこの攪拌室
7に連通する排気口20を有し、この生分解処理容器2
の外側に設置された脱臭装置21にこの排気口20が接
続されている。この排気口20内には攪拌室7からの排
気量を調節し得る排気量調節手段として開閉窓付きファ
ン22が取り付けられている。図示しないが、この開閉
窓付きファン22においては、回転に伴い窓が開き、回
転の停止に伴い窓が閉じるようになっている。A treated material supply unit 14, a hot air supply unit 15, and an exhaust unit 16 are attached to the lid wall 6 of the biodegradation container 2. The treated product supply unit 14 has an opening 17 that can be opened and closed, and the inlet 17 communicates with the stirring chamber 7 in the biodegradation processing container 2. The hot air supply unit 15 has an air supply port 18 communicating with the stirring chamber 7, and the air supply port 18 is connected to a heating air blower 19 installed outside the biodegradation treatment container 2. The exhaust part 16 has an exhaust port 20 communicating with the stirring chamber 7, and
The exhaust port 20 is connected to a deodorizing device 21 installed outside the device. A fan 22 with an opening / closing window is mounted in the exhaust port 20 as an exhaust amount adjusting means capable of adjusting the amount of exhaust from the stirring chamber 7. Although not shown, in the fan 22 with an opening / closing window, the window is opened as the rotation is performed, and the window is closed as the rotation is stopped.
【0017】前記開閉窓付きファン22は、駆動手段と
して前記生分解処理容器2の外側に設置されたコントロ
ーラ23(制御部)に接続されている。この生分解処理
容器2内の攪拌室7には駆動手段としての温度センサ2
4が前記排気口20の付近で取り付けられて前記コント
ローラ23に接続されている。The fan 22 with an opening / closing window is connected as a driving means to a controller 23 (control unit) installed outside the biodegradation container 2. The stirring chamber 7 in the biodegradation container 2 has a temperature sensor 2 as a driving means.
4 is attached near the exhaust port 20 and connected to the controller 23.
【0018】図3に示すように、前記生分解処理容器2
の外壁をなす周壁4と底壁5と蓋壁6とにはそれぞれ断
熱材25(保温材)が内外両壁部26,27間に挟着さ
れている。なお、底壁5では断熱材25を省略してもよ
い。この断熱材25としては、鉱物質のものや動植物質
のものや金属質のものなど、既存のものから適宜選択し
て採用すればよいが、本実施形態ではガラス繊維を利用
している。As shown in FIG. 3, the biodegradation vessel 2
A heat insulating material 25 (heat insulating material) is sandwiched between the inner and outer wall portions 26 and 27 on the peripheral wall 4, the bottom wall 5, and the lid wall 6, which form the outer walls. Note that the heat insulating material 25 may be omitted from the bottom wall 5. The heat insulating material 25 may be appropriately selected from existing materials such as mineral materials, animal and plant materials, and metallic materials. In this embodiment, glass fibers are used.
【0019】前記生分解処理容器2内の攪拌室7には処
理物供給部14の投入口17から処理物として生分解菌
(生分解微生物)と菌宿体とを供給する。この生分解菌
としては、高速分解消滅処理を主眼とする場合、超好熱
菌(超高温菌)を利用する。この菌宿体としては、生分
解菌の増殖を主眼とする場合、生ごみやもみがらやコー
ヒー粕や茶粕やハーブのほか、微粉末活性炭も利用され
る。また、有機性廃棄物処理では、この菌宿体としてこ
れらに有機性廃棄物を加える。A biodegradable bacterium (biodegradable microorganism) and a bacterium are supplied to the agitation chamber 7 in the biodegradation processing container 2 from the inlet 17 of the processed material supply unit 14 as a processed material. As the biodegradable bacterium, a hyperthermophilic bacterium (ultrathermophilic bacterium) is used when the main object is a high-speed disintegration treatment. In the case where the main purpose is to grow biodegradable bacteria, fine powdered activated carbon is used in addition to garbage, rice husk, coffee grounds, tea grounds and herbs. In the organic waste treatment, an organic waste is added to these as a fungus host.
【0020】前記攪拌室7で各回転羽根11が2.0〜
2.5回/secの回転数で回転してその腕板12及び
羽根板13により前記生分解菌と菌宿体とを攪拌する。
この攪拌を行いながら、前記熱風供給部15の給気口1
8から、400℃〜500℃の範囲の温度、好ましくは
約450℃の乾燥熱風を、攪拌室7の内容積1m3 あた
り0.1〜2.0m3 /minの供給量で攪拌室7に供
給する。この乾燥熱風がマンガン鉱石や石炭石やコバル
ト鉱石や活性炭等の混合資材を通過すると、分解菌の活
性を高めることができる。この攪拌室7において、前記
コントローラ23は、温度センサ24からの検知温度が
100℃未満になった場合に前記開閉窓付きファン22
の回転を停止させ、この検知温度が100℃以上になっ
た場合に前記開閉窓付きファン22を回転させる。この
開閉窓付きファン22が回転して開くと、この攪拌室7
内の水蒸気等が排気部16の排気口20から脱臭装置2
1を経て排気される。そのため、この攪拌室7は約10
0℃の温度に設定され易くなる。また、この温度センサ
24の検知温度は各種条件に応じて70℃〜120℃の
範囲の温度に設定してもよく、その設定に伴い攪拌室7
は約70℃〜約120℃の範囲の温度に設定され易くな
る。In the stirring chamber 7, each of the rotating blades 11
The biodegradable bacterium and the bacterium are stirred by the arm plate 12 and the wing plate 13 while rotating at a rotation speed of 2.5 times / sec.
While performing this stirring, the air supply port 1 of the hot air supply unit 15
8 to 400 ° C. to 500 ° C., preferably about 450 ° C., into the stirring chamber 7 at a supply rate of 0.1 to 2.0 m 3 / min per 1 m 3 of the internal volume of the stirring chamber 7. Supply. When the dry hot air passes through a mixed material such as manganese ore, coal stone, cobalt ore, and activated carbon, the activity of the decomposing bacteria can be increased. In the stirring chamber 7, the controller 23 operates the fan 22 with the opening / closing window when the temperature detected by the temperature sensor 24 becomes less than 100 ° C.
Is stopped, and when the detected temperature becomes 100 ° C. or higher, the fan 22 with the opening / closing window is rotated. When the fan 22 with the opening / closing window rotates and opens, the stirring chamber 7 is opened.
The water vapor and the like in the inside of the deodorizing device 2
It is exhausted through 1. Therefore, the stirring chamber 7 has a capacity of about 10
The temperature is easily set to 0 ° C. The temperature detected by the temperature sensor 24 may be set to a temperature in the range of 70 ° C. to 120 ° C. according to various conditions.
Tends to be set to a temperature in the range of about 70C to about 120C.
【0021】図2、図3及び図4(b)に示す本発明の
第二実施形態にかかる横型生分解処理装置1は、前述し
た第一実施形態にかかる縦型生分解処理装置1と比較し
て、攪拌機構8の回転軸10を水平に延設した点で異な
り、他は第一実施形態と同様である。この場合、生分解
処理容器2を各回転羽根11に対して逆の方向へ回転可
能に設けてもよい。The horizontal biodegradation processing apparatus 1 according to the second embodiment of the present invention shown in FIGS. 2, 3 and 4 (b) is compared with the vertical biodegradation processing apparatus 1 according to the first embodiment described above. The difference is that the rotating shaft 10 of the stirring mechanism 8 extends horizontally, and the other points are the same as in the first embodiment. In this case, the biodegradation processing container 2 may be provided so as to be rotatable in the opposite direction with respect to each rotating blade 11.
【図1】 第一実施形態にかかる縦型生分解処理装置を
回収自動車の車台に載せて概略的に示す断面図である。FIG. 1 is a cross-sectional view schematically showing a vertical biodegradation processing apparatus according to a first embodiment mounted on a chassis of a recovery automobile.
【図2】 第二実施形態にかかる横型生分解処理装置を
回収自動車の車台に載せて概略的に示す断面図である。FIG. 2 is a cross-sectional view schematically showing a horizontal biodegradation processing apparatus according to a second embodiment mounted on a chassis of a recovery automobile.
【図3】 この縦型生分解処理装置及び横型生分解処理
装置において生分解処理容器の外壁を示す部分拡大断面
図である。FIG. 3 is a partially enlarged cross-sectional view showing an outer wall of a biodegradation processing container in the vertical biodegradation processing apparatus and the horizontal biodegradation processing apparatus.
【図4】 (a)は図1のXーX線断面図であり、
(b)は図2のYーY線断面図である。FIG. 4A is a sectional view taken along line XX of FIG.
FIG. 3B is a sectional view taken along line YY of FIG. 2.
1…生分解処理装置、2…生分解処理容器、4…周壁
(外壁)、5…底壁(外壁)、6…蓋壁(外壁)、7…
攪拌室、8…攪拌機構、14…処理物供給部、15…熱
風供給部、16…排気部、22…開閉窓付きファン(排
気量調節手段)、23…制御部としてのコントローラ
(駆動手段)、24…温度センサ(駆動手段)、25…
断熱材、28a…車台。DESCRIPTION OF SYMBOLS 1 ... Biodegradation processing apparatus, 2 ... Biodegradation processing container, 4 ... Peripheral wall (outer wall), 5 ... Bottom wall (outer wall), 6 ... Lid wall (outer wall), 7 ...
Stirring chamber, 8: Stirring mechanism, 14: Processed material supply unit, 15: Hot air supply unit, 16: Exhaust unit, 22: Fan with opening / closing window (exhaust amount adjusting unit), 23: Controller (drive unit) as control unit , 24 ... temperature sensor (drive means), 25 ...
Insulation material, 28a ... chassis.
Claims (7)
機構を備え、この生分解処理容器にはこの攪拌室に連通
する処理物供給部と熱風供給部と排気部とを設け、この
生分解処理容器の外壁の一部または全部に設けた断熱材
によりこの攪拌室を囲ったことを特徴とする生分解処理
装置。1. A stirrer is provided in a stirring chamber provided in a biodegradation processing container, and a processing material supply unit, a hot air supply unit, and an exhaust unit which communicate with the stirring chamber are provided in the biodegradation processing container. A biodegradation treatment apparatus, wherein the stirring chamber is surrounded by a heat insulating material provided on part or all of the outer wall of the biodegradation treatment container.
調節し得る排気量調節手段を有し、この攪拌室内の温度
に応じてこの排気量調節手段を動作し得る駆動手段を設
けたことを特徴とする請求項1に記載の生分解処理装
置。2. The exhaust unit has an exhaust amount adjusting unit capable of adjusting an exhaust amount from the stirring chamber, and a driving unit capable of operating the exhaust amount adjusting unit in accordance with the temperature in the stirring chamber. The biodegradation processing apparatus according to claim 1, wherein:
度センサと、この温度センサからの検知温度に応じて前
記排気量調節手段を開閉動作し得る制御部とを備えてい
ることを特徴とする請求項2に記載の生分解処理装置。3. The driving unit includes a temperature sensor provided in the stirring chamber, and a control unit that can open and close the exhaust amount adjusting unit in accordance with a temperature detected by the temperature sensor. The biodegradation treatment apparatus according to claim 2, wherein
知温度が所定値以上になった場合に、前記排気量調節手
段を開動作させることを特徴とする請求項3に記載の生
分解処理装置。4. The biodegradation process according to claim 3, wherein the control unit opens the displacement control means when the temperature detected by the temperature sensor becomes equal to or higher than a predetermined value. apparatus.
請求項に記載の生分解処理装置を有機性廃棄物回収自動
車の車台に設置したことを特徴とする生分解処理装置。5. A biodegradation processing apparatus, wherein the biodegradation processing apparatus according to any one of claims 1 to 4 is installed in a chassis of an organic waste recovery automobile.
て生分解菌と菌宿体とを供給した状態で、この処理物を
攪拌する処理と、この攪拌室に所定温度の熱風を供給す
る処理と、この攪拌室内の温度が所定値以上になった場
合にこの攪拌室内の水蒸気等を排気する処理とを互いに
組み合わせてこの生分解菌を増殖させながら生分解処理
を行なうことを特徴とする生分解処理方法。6. A process for agitating a processed product in a state where biodegradable bacteria and a bacterial host are supplied as a processed product to a stirring chamber in a biodegradation processing container, and supplying hot air at a predetermined temperature to the stirring chamber. And performing a biodegradation process while multiplying the biodegradable bacteria by combining the process of exhausting water vapor and the like in the stirring chamber when the temperature in the stirring chamber becomes a predetermined value or more. Biodegradation treatment method.
徴とする請求項6に記載の生分解処理方法。7. The biodegradation treatment method according to claim 6, wherein the fungal host contains powdered activated carbon.
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JP2000306185A JP2002113447A (en) | 2000-10-05 | 2000-10-05 | Biodegradation processing device and biodegradation processing method |
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Cited By (6)
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CN102950142A (en) * | 2012-11-20 | 2013-03-06 | 邝生林 | Full-automatic animal carcass harmless treatment device |
CN103223415A (en) * | 2013-04-28 | 2013-07-31 | 北京津同利亚科技发展有限公司 | Heat transfer oil heating tank apparatus of vehicle-mounted moveable animal carcass harmless treatment apparatus |
CN103230925A (en) * | 2013-04-28 | 2013-08-07 | 北京津同利亚科技发展有限公司 | Heat conduction oil heating device of vehicle-mounted mobile-type animal carcass innocent treatment device |
CN103350095A (en) * | 2013-04-25 | 2013-10-16 | 北京津同利亚科技发展有限公司 | Vehicle-mounted moveable full-automatic animal carcass harmless treatment apparatus |
KR101425210B1 (en) * | 2013-05-03 | 2014-08-01 | 주식회사 피티케이 | Powder feeding apparatus of high speed granulator |
CN106269778A (en) * | 2015-05-26 | 2017-01-04 | 浙江布莱蒙农业科技股份有限公司 | Portable dead poultry treating stations |
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Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
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CN102950142A (en) * | 2012-11-20 | 2013-03-06 | 邝生林 | Full-automatic animal carcass harmless treatment device |
CN103350095A (en) * | 2013-04-25 | 2013-10-16 | 北京津同利亚科技发展有限公司 | Vehicle-mounted moveable full-automatic animal carcass harmless treatment apparatus |
CN103223415A (en) * | 2013-04-28 | 2013-07-31 | 北京津同利亚科技发展有限公司 | Heat transfer oil heating tank apparatus of vehicle-mounted moveable animal carcass harmless treatment apparatus |
CN103230925A (en) * | 2013-04-28 | 2013-08-07 | 北京津同利亚科技发展有限公司 | Heat conduction oil heating device of vehicle-mounted mobile-type animal carcass innocent treatment device |
KR101425210B1 (en) * | 2013-05-03 | 2014-08-01 | 주식회사 피티케이 | Powder feeding apparatus of high speed granulator |
CN106269778A (en) * | 2015-05-26 | 2017-01-04 | 浙江布莱蒙农业科技股份有限公司 | Portable dead poultry treating stations |
CN106269778B (en) * | 2015-05-26 | 2019-01-01 | 浙江布莱蒙农业科技股份有限公司 | Mobile death poultry treating stations |
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