JP2001246352A - Garbage treating apparatus - Google Patents
Garbage treating apparatusInfo
- Publication number
- JP2001246352A JP2001246352A JP2000063695A JP2000063695A JP2001246352A JP 2001246352 A JP2001246352 A JP 2001246352A JP 2000063695 A JP2000063695 A JP 2000063695A JP 2000063695 A JP2000063695 A JP 2000063695A JP 2001246352 A JP2001246352 A JP 2001246352A
- Authority
- JP
- Japan
- Prior art keywords
- decomposition tank
- air
- inlet line
- line
- garbage
- 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
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M29/00—Means for introduction, extraction or recirculation of materials, e.g. pumps
- C12M29/20—Degassing; Venting; Bubble traps
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M27/00—Means for mixing, agitating or circulating fluids in the vessel
- C12M27/02—Stirrer or mobile mixing elements
- C12M27/06—Stirrer or mobile mixing elements with horizontal or inclined stirrer shaft or axis
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M29/00—Means for introduction, extraction or recirculation of materials, e.g. pumps
- C12M29/06—Nozzles; Sprayers; Spargers; Diffusers
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M29/00—Means for introduction, extraction or recirculation of materials, e.g. pumps
- C12M29/26—Conditioning fluids entering or exiting the reaction vessel
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M41/00—Means for regulation, monitoring, measurement or control, e.g. flow regulation
- C12M41/30—Means for regulation, monitoring, measurement or control, e.g. flow regulation of concentration
- C12M41/34—Means for regulation, monitoring, measurement or control, e.g. flow regulation of concentration of gas
Abstract
Description
【０００１】[0001]
【発明の属する技術分野】本発明は微生物により生ごみ
を処理する生ごみ処理装置に係り、とりわけ分解槽内へ
の給気量を容易かつ簡単に測定することができる生ごみ
処理装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a garbage disposal apparatus for treating garbage with microorganisms, and more particularly to a garbage disposal apparatus capable of easily and easily measuring the amount of air supplied to a decomposition tank.
【０００２】[0002]
【従来の技術】生ごみ処理装置は、微生物が内蔵された
媒体を収納するとともに投入された生ごみを微生物によ
り分解する分解槽と、分解槽の入口側および出口側に各
々設けられた給気用の入口ラインおよび排気用の出口ラ
インとを備えている。2. Description of the Related Art A garbage disposal apparatus includes a decomposition tank for storing a medium containing microorganisms therein and decomposing the inputted garbage by microorganisms, and an air supply provided on an inlet side and an outlet side of the decomposition tank, respectively. And an outlet line for exhaust.
【０００３】また入口ラインには、加熱装置が設置さ
れ、さらに入口ラインまたは出口ラインにファンとダン
パが設置されている。このため入口ラインから分解槽内
にファンにより空気を送ることができ、かつ分解槽内へ
送られる空気を加熱装置で加熱して分解槽内を一定温度
に保っている。[0003] A heating device is installed at the entrance line, and a fan and a damper are installed at the entrance line or the exit line. For this reason, air can be sent from the inlet line into the decomposition tank by a fan, and the air sent into the decomposition tank is heated by a heating device to maintain the inside of the decomposition tank at a constant temperature.
【０００４】[0004]
【発明が解決しようとする課題】上述のように入口ライ
ンまたは出口ラインのいずれかにファンとダンパが設け
られているが、従来の装置では風量計を設定していない
ため分解槽内への風量を十分把握することはできない。As described above, a fan and a damper are provided at either the inlet line or the outlet line. However, in the conventional apparatus, since the air flow meter is not set, the air flow into the decomposition tank is not provided. Cannot be grasped enough.
【０００５】このような場合、加熱装置が風量計を兼ね
備えていれば、分解槽内への空気の風量を正確に把握す
ることができ、かつ生ごみ処理装置の全体システムを簡
略化することができて都合が良い。In such a case, if the heating device also has an air flow meter, it is possible to accurately grasp the air flow into the decomposition tank and to simplify the entire system of the garbage disposal device. Convenient and convenient.
【０００６】本発明はこのような点を考慮してなされた
ものであり、分解槽内への空気風量を把握することがで
き、かつ全体システムを簡略化することができる生ごみ
処理装置を提供することを目的とする。The present invention has been made in view of the above points, and provides a garbage disposal apparatus capable of grasping the amount of air flow into the decomposition tank and simplifying the entire system. The purpose is to do.
【０００７】[0007]
【課題を解決するための手段】本発明は、微生物が内蔵
された媒体を収納するとともに、投入された生ごみを微
生物により分解する分解槽と、分解槽の入口側に設けら
れた給気用の入口ラインと、分解槽の出口側に設けられ
た排気用の出口ラインと、入口ラインに設けられた加熱
装置と、入口ラインまたは出口ラインのいずれかに設け
られたファンとを備え、加熱装置は熱線式風量計を有す
ることを特徴とする生ごみ処理装置である。SUMMARY OF THE INVENTION The present invention provides a decomposition tank for storing a medium containing microorganisms therein and decomposing the inputted garbage by the microorganisms, and an air supply provided at the inlet side of the decomposition tank. An inlet line, an exhaust outlet line provided on the outlet side of the decomposition tank, a heating device provided on the inlet line, and a fan provided on either the inlet line or the outlet line, Is a garbage processing apparatus having a hot wire anemometer.
【０００８】本発明は、微生物が内蔵された媒体を収納
するとともに、投入された生ごみを微生物により分解す
る分解槽と、分解槽の入口側に設けられた給気用の入口
ラインと、分解槽の出口側に設けられた排気用の出口ラ
インと、入口ラインに設けられた加熱装置と、入口ライ
ンまたは出口ラインのいずれかに設けられたファンとを
備え、入口ラインのうち加熱装置の上流側および下流側
に、第１温度検知器と第２温度検知器を各々設け、第１
温度検知器と第２温度検知器からの温度信号と、加熱装
置からの加熱量信号とに基づいて、風量を求める制御装
置を設けたことを特徴とする生ごみ処理装置である。The present invention provides a decomposition tank for storing a medium containing microorganisms therein and decomposing the inputted garbage by the microorganisms, an inlet line for air supply provided on the inlet side of the decomposition tank, An outlet line for exhaust provided on the outlet side of the tank, a heating device provided on the inlet line, and a fan provided on either the inlet line or the outlet line, the upstream of the heating device in the inlet line A first temperature detector and a second temperature detector are provided on the
A garbage processing apparatus characterized by including a control device for obtaining an air volume based on temperature signals from a temperature detector and a second temperature detector and a heating amount signal from a heating device.
【０００９】本発明によれば、熱線式風量計により分解
槽内へ給気される空気を加熱することができるととも
に、この熱線式風量計により分解槽内へ給気される空気
の風量を正確に把握することができる。また第１温度検
知器と第２温度検知器からの信号と、加熱装置からの加
熱量信号とに基づいて、制御装置により風量を求めるこ
とができる。According to the present invention, it is possible to heat the air supplied into the decomposition tank by the hot wire type air flow meter, and to accurately measure the air volume of the air supplied into the decomposition bath by the hot wire type air flow meter. Can be grasped. Further, the control device can determine the air volume based on the signals from the first temperature detector and the second temperature detector and the heating amount signal from the heating device.
【００１０】[0010]
【発明の実施の形態】以下、図面を参照して本発明の実
施の形態について説明する。図１および図２は本発明に
よる生ごみ処理装置の一実施の形態を示す図である。Embodiments of the present invention will be described below with reference to the drawings. 1 and 2 are diagrams showing an embodiment of a garbage processing apparatus according to the present invention.
【００１１】図１および図２に示すように、生ごみ処理
装置は微生物が内蔵された媒体２を収納するとともに、
投入口１ａから投入された生ごみ８を微生物により分解
する分解槽１と、分解槽１の入口側に設けられた給気用
の入口ライン１１と、分解槽１の出口側に設けられた排
気用の出口ライン１２とを備えている。As shown in FIGS. 1 and 2, the garbage disposal apparatus stores a medium 2 containing microorganisms,
Decomposition tank 1 for decomposing garbage 8 supplied from input port 1 a by microorganisms, inlet line 11 for air supply provided on the inlet side of decomposition tank 1, and exhaust gas provided on the outlet side of decomposition tank 1 And an outlet line 12.
【００１２】また入口ライン１１には風量調整装置とし
てのダンパ６と、熱線式風量計４が順次設けられてい
る。このうち熱線式風量計４は加熱装置としての加熱素
子４ａと、加熱素子４ａに接続された測定回路５とを有
し、さらに測定回路５は電源５ａと、可変抵抗５ｂと、
ブリッジ平衡用可変抵抗５ｃと、検流計５ｄと、電流計
５ｅとからなっている。The inlet line 11 is provided with a damper 6 as an air flow adjusting device and a hot wire air flow meter 4 in order. Among them, the hot wire anemometer 4 has a heating element 4a as a heating device, and a measuring circuit 5 connected to the heating element 4a. The measuring circuit 5 further includes a power supply 5a, a variable resistor 5b,
It comprises a bridge balancing variable resistor 5c, a galvanometer 5d, and an ammeter 5e.
【００１３】また熱線式風量計４において、測定回路５
により加熱される加熱素子４ａの抵抗と風速との関係が
予め求められている。すなわち加熱素子４ａは、加熱素
子４ａから放熱される熱量に応じて、その抵抗が変化す
るため、加熱素子４ａの温度を一定に保つ場合、変化し
た加熱素子４ａの抵抗値に応じて電流値が変化する。こ
のため加熱素子４ａを流れる電流値を測定回路５の検流
計５ｄおよび電流計５ｅで読み取ることにより、入口ラ
イン１１内を流れる空気量を求めることができる。In the hot wire type air flow meter 4, a measuring circuit 5
The relationship between the resistance of the heating element 4a heated by the above and the wind speed is determined in advance. That is, since the resistance of the heating element 4a changes according to the amount of heat radiated from the heating element 4a, when the temperature of the heating element 4a is kept constant, the current value is changed according to the changed resistance value of the heating element 4a. Change. Therefore, by reading the value of the current flowing through the heating element 4a with the galvanometer 5d and the ammeter 5e of the measurement circuit 5, the amount of air flowing through the inlet line 11 can be obtained.
【００１４】また出口ライン１２には、駆動部７ａを有
するファン７が設置され、このファン７により入口ライ
ン１１を通って空気を分解槽１内に送ることができ、分
解槽１内の空気は出口ライン１２を通って外方へ排気さ
れる。The outlet line 12 is provided with a fan 7 having a driving portion 7a, and the fan 7 can send air through the inlet line 11 into the decomposition tank 1, and the air in the decomposition tank 1 The air is exhausted outward through the outlet line 12.
【００１５】さらに分解槽１内には媒体２の温度を測定
する温度計１３が設置され、また出口ライン１２には出
口ライン１２を通る排気中の発生蒸気量を測定する発生
蒸気量計１４が設けられている。Further, a thermometer 13 for measuring the temperature of the medium 2 is provided in the decomposition tank 1, and a generated steam meter 14 for measuring the generated steam in the exhaust gas passing through the outlet line 12 is provided at the outlet line 12. Is provided.
【００１６】また図１に示すように、測定回路５、温度
計１３および発生蒸気量計１４は各々制御装置１０に接
続され、この制御装置１０によりダンパ６および測定回
路５が調整される。As shown in FIG. 1, the measuring circuit 5, the thermometer 13 and the generated steam meter 14 are each connected to a control device 10, which adjusts the damper 6 and the measuring circuit 5.
【００１７】なお、分解槽１内に収納された媒体２とし
ては、微生物を内蔵したおがくず等が考えられる。The medium 2 accommodated in the decomposition tank 1 may be sawdust containing microorganisms.
【００１８】また媒体２に生ごみ８を投入し、媒体２を
分解槽１内に設置された攪拌機３により攪拌することに
よって、生ごみを微生物により分解処理して水、二酸化
炭素、アンモニア、酢酸、およびラク酸等が生成され
る。分解槽１内で発生した水、二酸化炭素等は、水蒸気
および二酸化炭素ガス等となって出口ライン１２から排
気される。Further, the garbage 8 is put into the medium 2, and the medium 2 is stirred by the stirrer 3 installed in the decomposition tank 1, whereby the garbage is decomposed by microorganisms, and water, carbon dioxide, ammonia, acetic acid is removed. , And lacnic acid are produced. Water, carbon dioxide, and the like generated in the decomposition tank 1 are exhausted from the outlet line 12 as steam, carbon dioxide gas, and the like.
【００１９】次にこのような構成からなる本実施の形態
の作用について説明する。Next, the operation of the present embodiment having the above configuration will be described.
【００２０】まず分解槽１内に投入口１ａから生ごみ８
が投入される。次にファン７により、空気が入口ライン
１１へ送られ、入口ライン１１に送られた空気はダンパ
６を通り、熱線式風量計４の加熱素子４ａにより加熱さ
れて分解槽１内へ給気される。First, garbage 8 is introduced into the decomposition tank 1 from the input port 1a.
Is input. Next, air is sent to the inlet line 11 by the fan 7, and the air sent to the inlet line 11 passes through the damper 6, is heated by the heating element 4 a of the hot-wire anemometer 4, and is supplied into the decomposition tank 1. You.
【００２１】分解槽１内では、投入された生ごみ８が上
述のように、媒体２内の微生物により分解処理され、水
蒸気および二酸化炭素ガス等を生成する。これらの水蒸
気および二酸化炭素ガス等は、分解槽１から出口ライン
１２を経て外方へ排出される。In the decomposition tank 1, the introduced garbage 8 is decomposed by the microorganisms in the medium 2 as described above to generate steam, carbon dioxide gas and the like. These water vapor and carbon dioxide gas are discharged from the decomposition tank 1 to the outside via the outlet line 12.
【００２２】この間、測定回路５の検流計５ｄおよび電
流計５ｅで測定された電流値に基づいて、入口ライン１
１内を流れる空気の風量が定まり、測定回路５から風量
信号が制御装置１０へ送られる。同時に温度計１３およ
び発生蒸気量計１４により媒体２の温度および出口ライ
ン１２内の発生蒸気量が測定され、温度計１３および発
生蒸気量計１４からの温度信号および蒸気量信号は、各
々制御装置１０へ送られる。In the meantime, based on the current values measured by the galvanometer 5d and the ammeter 5e of the measuring circuit 5, the inlet line 1
The air volume of the air flowing inside 1 is determined, and an air volume signal is sent from the measurement circuit 5 to the control device 10. At the same time, the temperature of the medium 2 and the amount of generated steam in the outlet line 12 are measured by the thermometer 13 and the generated steam amount meter 14, and the temperature signal and the steam amount signal from the thermometer 13 and the generated steam amount meter 14 are controlled by the control device, respectively. Sent to 10.
【００２３】制御装置１０は、分解槽１内において適切
な生ごみ分解処理を行なうため、分解槽１内の媒体２の
温度および発生蒸気量が所望の値となるよう、熱線式風
量計４の測定回路５を制御して熱線式風量計４の加熱素
子４ａの温度を所定の値に定める。The control device 10 controls the hot wire anemometer 4 so that the temperature of the medium 2 and the amount of generated steam in the decomposition tank 1 become desired values in order to perform appropriate garbage decomposition processing in the decomposition tank 1. By controlling the measuring circuit 5, the temperature of the heating element 4a of the hot wire anemometer 4 is set to a predetermined value.
【００２４】同時に制御装置１０は、分解槽１内の給気
量を所望の値に定めるよう、熱線式風量計４からの風量
信号に基づいてダンパ６を調整し、分解槽１内の風量を
制御する。なお、ファン７の駆動部７ａにインバータを
用い、駆動部７ａを回転数制御可能としておくことによ
り、制御装置１０によって分解槽１内の給気量が所望の
値となるようファン７の回転数を制御してもよい。この
場合、インバータを用いた駆動部７ａが風量調整装置と
なる。At the same time, the control device 10 adjusts the damper 6 based on the air flow signal from the hot wire type air flow meter 4 so that the air supply amount in the decomposition tank 1 is set to a desired value, and adjusts the air flow in the decomposition tank 1. Control. In addition, by using an inverter as the drive unit 7a of the fan 7 and controlling the rotation speed of the drive unit 7a, the control unit 10 controls the rotation speed of the fan 7 so that the supply air amount in the decomposition tank 1 becomes a desired value. May be controlled. In this case, the driving unit 7a using the inverter serves as an air volume adjusting device.
【００２５】このように本実施の形態によれば、熱線式
風量計４により、分解槽１への給気される空気を加熱す
るとともに風量を求めることができるので、加熱装置と
風量計を別個に設ける必要はなく、全体システムを簡略
化することができる。また、制御装置１０により熱線式
風量計４を制御することにより、分解槽１内で所望の分
解条件を得ることができる。As described above, according to the present embodiment, the hot wire anemometer 4 can heat the air supplied to the decomposition tank 1 and determine the air volume, so that the heating device and the air volume meter are separately provided. Need not be provided, and the overall system can be simplified. Further, by controlling the hot-wire anemometer 4 by the control device 10, desired decomposition conditions can be obtained in the decomposition tank 1.
【００２６】なお、上記実施の形態において、熱線式風
量計４により風量を求めた例について示したが、これに
限らず熱線式風量計４を加熱装置としてのみ用い、熱線
式風量計４の上流側と下流側に、第１温度検知器１５ａ
と第２温度検知器１５ｂを各々設置してもよい（図１の
２点鎖線）。In the above-described embodiment, an example in which the air volume is obtained by the hot wire anemometer 4 has been described. However, the present invention is not limited to this, and the hot wire anemometer 4 is used only as a heating device, The first temperature detector 15a
And the second temperature detector 15b may be provided (two-dot chain line in FIG. 1).
【００２７】この場合、熱線式風量計４からの加熱量信
号と、第１温度検知器１５ａおよび第２温度検知器１５
ｂからの信号とが制御装置１０へ入力される。制御装置
１０は熱線式風量計４からの加熱量信号と、第１温度検
知器１５ａおよび第２温度検知器１５ｂからの信号に基
づいて、入口ライン１１内を流れる空気の風量を求め
る。In this case, the heating amount signal from the hot wire type air flow meter 4 and the first temperature detector 15a and the second temperature detector 15
b is input to the control device 10. The control device 10 obtains the air volume of the air flowing through the inlet line 11 based on the heating amount signal from the hot wire type air flow meter 4 and the signals from the first temperature detector 15a and the second temperature detector 15b.
【００２８】[0028]
【発明の効果】以上のように本発明によれば、熱線式風
量計により、分解槽内へ給気される空気を加熱すること
ができるとともに、空気の風量を把握することができ
る。また第１温度検知器と第２温度検知器からの信号
と、加熱装置からの加熱量信号とに基づいて、制御装置
により風量を求めることができる。このため生ごみ処理
装置の全体システムを簡略化することができる。As described above, according to the present invention, the air supplied into the decomposition tank can be heated by the hot wire type air flow meter, and the air flow rate can be grasped. Further, the control device can determine the air volume based on the signals from the first temperature detector and the second temperature detector and the heating amount signal from the heating device. For this reason, the whole system of the garbage processing apparatus can be simplified.
【図１】本発明による生ごみ処理装置の一実施の形態を
示す概略図FIG. 1 is a schematic diagram showing an embodiment of a garbage processing apparatus according to the present invention.
【図２】熱線式風量計の測定回路を示す図FIG. 2 is a diagram showing a measurement circuit of a hot-wire anemometer;
１ 分解槽 ２ 媒体 ４ 熱線式風量計 ５ 測定回路 ６ ダンパ ７ ファン ８ 生ごみ １０ 制御装置 DESCRIPTION OF SYMBOLS 1 Decomposition tank 2 Medium 4 Hot wire type air flow meter 5 Measurement circuit 6 Damper 7 Fan 8 Garbage 10 Control device
───────────────────────────────────────────────────── フロントページの続き Ｆターム(参考） 4B029 AA03 AA13 BB01 CC05 EA10 EA12 EA14 4D004 AA03 AC04 CA19 CA22 CB04 CB28 CB36 CC02 CC07 CC08 DA01 DA02 DA06 DA12 ──────────────────────────────────────────────────続 き Continued on the front page F term (reference) 4B029 AA03 AA13 BB01 CC05 EA10 EA12 EA14 4D004 AA03 AC04 CA19 CA22 CB04 CB28 CB36 CC02 CC07 CC08 DA01 DA02 DA06 DA12
Claims (4)
に、投入された生ごみを微生物により分解する分解槽
と、 分解槽の入口側に設けられた給気用の入口ラインと、 分解槽の出口側に設けられた排気用の出口ラインと、 入口ラインに設けられた加熱装置と、 入口ラインまたは出口ラインのいずれかに設けられたフ
ァンとを備え、 加熱装置は熱線式風量計を有することを特徴とする生ご
み処理装置。1. A decomposition tank for storing a medium containing microorganisms therein and decomposing the inputted garbage by microorganisms, an inlet line for air supply provided at an inlet side of the decomposition tank, An outlet line for exhaust provided on the outlet side, a heating device provided on the inlet line, and a fan provided on either the inlet line or the outlet line, the heating device having a hot wire anemometer A garbage disposal device characterized by the following.
設け、 熱線式風量計からの風量信号に基づいて、風量調整装置
を制御する制御装置を設けたことを特徴とする請求項１
記載の生ごみ処理装置。2. The apparatus according to claim 1, further comprising an air volume adjusting device for controlling an air volume in the decomposing tank, and a control device for controlling the air volume adjusting device based on an air volume signal from a hot wire anemometer.
A garbage disposal device as described.
設け、 分解槽内に媒体の温度を測定する温度計を設けるととも
に、出口ラインに発生蒸気量計を設け、 熱線式風量計からの風量信号、温度計からの温度信号お
よび発生蒸気量計からの蒸気量信号に基づいて、風量調
整装置を制御する制御装置を設けたことを特徴とする請
求項１記載の生ごみ処理装置。3. An air flow adjusting device for controlling the air flow in the decomposition tank, a thermometer for measuring the temperature of the medium in the decomposition tank, a generated steam flow meter in the outlet line, and a hot wire air flow meter. 2. The garbage processing apparatus according to claim 1, further comprising a control device for controlling the air volume adjusting device based on the air volume signal, the temperature signal from the thermometer, and the steam volume signal from the generated steam volume meter.
に、投入された生ごみを微生物により分解する分解槽
と、 分解槽の入口側に設けられた給気用の入口ラインと、 分解槽の出口側に設けられた排気用の出口ラインと、 入口ラインに設けられた加熱装置と、 入口ラインまたは出口ラインのいずれかに設けられたフ
ァンとを備え、 入口ラインのうち加熱装置の上流側および下流側に、第
１温度検知器と第２温度検知器を各々設け、 第１温度検知器と第２温度検知器からの温度信号と、加
熱装置からの加熱量信号とに基づいて、風量を求める制
御装置を設けたことを特徴とする生ごみ処理装置。4. A decomposition tank for accommodating a medium containing microorganisms therein and decomposing inputted garbage by microorganisms, an inlet line for air supply provided on an inlet side of the decomposition tank, An outlet line for exhaust provided on the outlet side, a heating device provided on the inlet line, and a fan provided on either the inlet line or the outlet line, On the downstream side, a first temperature detector and a second temperature detector are provided, respectively. Based on a temperature signal from the first temperature detector and the second temperature detector, and a heating amount signal from the heating device, an air volume is determined. A garbage disposal device provided with a required control device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2000063695A JP2001246352A (en) | 2000-03-08 | 2000-03-08 | Garbage treating apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2000063695A JP2001246352A (en) | 2000-03-08 | 2000-03-08 | Garbage treating apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JP2001246352A true JP2001246352A (en) | 2001-09-11 |
Family
ID=18583523
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2000063695A Pending JP2001246352A (en) | 2000-03-08 | 2000-03-08 | Garbage treating apparatus |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2001246352A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US8877285B2 (en) | 2011-11-22 | 2014-11-04 | Ford Global Technologies, Llc | Process for repairing a cylinder running surface by means of plasma spraying processes |
| US9079213B2 (en) | 2012-06-29 | 2015-07-14 | Ford Global Technologies, Llc | Method of determining coating uniformity of a coated surface |
| DE102015222479A1 (en) | 2015-11-13 | 2017-05-18 | Henkel Ag & Co. Kgaa | Gelled hair fixative |
-
2000
- 2000-03-08 JP JP2000063695A patent/JP2001246352A/en active Pending
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US8877285B2 (en) | 2011-11-22 | 2014-11-04 | Ford Global Technologies, Llc | Process for repairing a cylinder running surface by means of plasma spraying processes |
| US9079213B2 (en) | 2012-06-29 | 2015-07-14 | Ford Global Technologies, Llc | Method of determining coating uniformity of a coated surface |
| DE102015222479A1 (en) | 2015-11-13 | 2017-05-18 | Henkel Ag & Co. Kgaa | Gelled hair fixative |
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