JP2002255677A - Small-sized test equipment - Google Patents

Small-sized test equipment

Info

Publication number
JP2002255677A
JP2002255677A JP2001053337A JP2001053337A JP2002255677A JP 2002255677 A JP2002255677 A JP 2002255677A JP 2001053337 A JP2001053337 A JP 2001053337A JP 2001053337 A JP2001053337 A JP 2001053337A JP 2002255677 A JP2002255677 A JP 2002255677A
Authority
JP
Japan
Prior art keywords
temperature
reaction vessel
gas
test apparatus
small
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.)
Granted
Application number
JP2001053337A
Other languages
Japanese (ja)
Other versions
JP4988991B2 (en
Inventor
Makoto Doi
眞 土井
Masaki Ban
昌樹 伴
Kiwamu Shiiba
究 椎葉
Noriko Komine
法子 小峰
Toshinori Kimura
俊範 木村
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nisshin Seifun Group Inc
Original Assignee
Nisshin Seifun Group Inc
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 Nisshin Seifun Group Inc filed Critical Nisshin Seifun Group Inc
Priority to JP2001053337A priority Critical patent/JP4988991B2/en
Publication of JP2002255677A publication Critical patent/JP2002255677A/en
Application granted granted Critical
Publication of JP4988991B2 publication Critical patent/JP4988991B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A40/00Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/10Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
    • Y02A40/20Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/40Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse

Abstract

PROBLEM TO BE SOLVED: To provide small-sized test equipment which can simulates a manuring procedure under various temperature conditions. SOLUTION: In order to ensure the reproducibility of experiment, a reaction vessel 11 is kept under a fixed temperature for a prescribed time in the temperature holding mode and, thereafter, is subjected to pseudo-thermal insulation in the temperature follow-up mode and the temperature of fermenting substance CO is naturally elevated. In such a case, the initial conditions of the fermenting substance CO is allowed to coincide with each other and the experiment having high reproducibility is made possible. Otherwise, as another experiment, the reaction vessel 11 is preliminarily subjected to pseudo-thermal insulation in the temperature follow-up mode, the temperature of the fermenting substance CO is naturally elevated and the temperature hysteresis at that time is stored. Subsequently, by the exchange, etc., of the fermenting substance CO in the reaction vessel 11, the temperature of the reaction vessel 11 is regulated in the temperature forced mode. In such a experiment, the reproducibility of the initial pseudo-thermal insulation test can be confirmed.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】この発明は、植物や家畜糞等
のコンポスト化の過程を試験するための小型試験装置に
関し、例えば大型のコンポスト化プラント等におけるコ
ンポスト化過程を自在にシミュレーションすることがで
きる小型試験装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a small-sized test apparatus for testing the composting process of plants, livestock dung and the like, and can freely simulate the composting process in, for example, a large composting plant. The present invention relates to a small test device.

【0002】[0002]

【従来の技術】大型のコンポスト化プラントにおけるコ
ンポスト化過程をシミュレーションするためには、コン
ポスト原料の中心部分における温度変化等を再現する必
要がある。少量のコンポスト原料により大型のコンポス
ト化装置と同様の発酵過程を再現するためには、その熱
容量の小ささのため、環境より意図しない放熱や吸熱が
起こり、細菌相が変わってしまい再現性に問題があっ
た。これを解決するために、小型の反応容器にコンポス
ト原料を収容し、この反応容器を擬似的に断熱して、反
応容器内におけるコンポスト化の過程を再現する小型試
験装置が存在する。
2. Description of the Related Art In order to simulate the composting process in a large-scale composting plant, it is necessary to reproduce a temperature change or the like in a central portion of a compost material. In order to reproduce the same fermentation process as a large composting device using a small amount of compost raw materials, undesired heat release and endotherm occur from the environment due to the small heat capacity, resulting in a change in bacterial flora and a problem with reproducibility. was there. In order to solve this problem, there is a small-sized test apparatus that accommodates compost raw materials in a small reaction vessel, insulates the reaction vessel in a pseudo manner, and reproduces the composting process in the reaction vessel.

【0003】この種の小型試験装置では、反応容器を温
度調節用の水槽に浸漬する構造を有し、水槽に満たした
水の温度を反応容器内部に設けた温度計の指標値に近づ
ける制御を行う。これにより、反応容器が周囲から擬似
的に断熱され、反応容器では、大型のコンポスト化プラ
ントにおけるコンポスト化過程と同様のコンポスト化過
程が進行するというものである。
[0003] This type of small test apparatus has a structure in which a reaction vessel is immersed in a water tank for temperature control, and controls the temperature of water filled in the water tank to approach an index value of a thermometer provided inside the reaction vessel. Do. Thereby, the reaction vessel is pseudo-insulated from the surroundings, and in the reaction vessel, a composting process similar to the composting process in a large-scale composting plant proceeds.

【0004】[0004]

【発明が解決しようとする課題】しかし、上記小型試験
装置では、熱容量が大きな熱媒体を使用しているため、
擬似断熱効果を達成できるだけであり、コンポスト化プ
ラント等におけるコンポスト化過程を様々な温度条件下
でシミュレーションすることができない。
However, since the above-mentioned small test apparatus uses a heat medium having a large heat capacity,
It can only achieve the pseudo adiabatic effect and cannot simulate the composting process in a composting plant or the like under various temperature conditions.

【0005】また、上記小型試験装置では、擬似断熱の
試験に際して反応容器に供給する空気の状態に配慮がさ
れていないため、空気の供給に起因する外乱の影響を把
握することができない。
Further, in the above-described small-sized test apparatus, since the state of the air supplied to the reaction vessel is not taken into consideration during the pseudo-insulation test, it is impossible to grasp the influence of disturbance due to the supply of air.

【0006】この発明課題は、コンポスト化過程を様々
な温度条件下でシミュレーションすることができる小型
試験装置を提供することである。
An object of the present invention is to provide a compact test apparatus capable of simulating a composting process under various temperature conditions.

【0007】[0007]

【課題を解決するための手段】請求項1記載の小型試験
装置は、発酵体を収容する反応容器と、この反応容器を
気体層を隔てて収容する温度調節用の外側容器とを備え
る小型試験装置であって、反応容器中の発酵体の温度に
従って外側容器の温度を逐次変化させる温度追従手段
と、外側容器の温度を調節することにより、予め指定し
た時刻に反応容器中の発酵体の温度を所定の温度に保持
する温度保持手段とを備えることを特徴とする。
According to the present invention, there is provided a small-sized test apparatus comprising: a reaction vessel for accommodating a fermented body; and a temperature-controlling outer vessel for accommodating the reaction vessel with a gas layer therebetween. A temperature tracking means for sequentially changing the temperature of the outer vessel according to the temperature of the fermentation body in the reaction vessel, and the temperature of the fermentation body in the reaction vessel at a predetermined time by adjusting the temperature of the outer vessel. And temperature maintaining means for maintaining the temperature at a predetermined temperature.

【0008】上記小型試験装置では、温度追従手段が反
応容器中の発酵体の温度に従って外側容器の温度を逐次
変化させるだけでなく、温度保持手段が、外側容器の温
度を調節することにより、予め指定した時刻に反応容器
中の発酵体の温度を所定の温度に保持するので、反応容
器中の発酵体の温度を一定時間だけ所定の温度に保持す
る定値制御試験を行ったり、このような定値制御後に温
度追従手段を利用して擬似断熱試験を行うことができ
る。
[0008] In the above-mentioned small test apparatus, the temperature follow-up means not only changes the temperature of the outer vessel in accordance with the temperature of the fermentation body in the reaction vessel, but also the temperature holding means adjusts the temperature of the outer vessel in advance. Since the temperature of the fermentation body in the reaction vessel is maintained at a predetermined temperature at a specified time, a constant value control test for maintaining the temperature of the fermentation body in the reaction vessel at a predetermined temperature for a certain period of time is performed. After the control, a pseudo adiabatic test can be performed using the temperature following means.

【0009】また、請求項2記載の小型試験装置は、発
酵体を収容する反応容器と、この反応容器を気体層を隔
てて収容する温度調節用の外側容器とを備える小型試験
装置であって、反応容器中の発酵体の温度に従って外側
容器の温度を逐次変化させる温度追従手段と、外側容器
の温度を調節することにより、予め指定した第1時刻か
ら第2時刻の間に、反応容器中の発酵体の温度を第1温
度から第2温度に徐々に変化させる温度強制手段とを備
えることを特徴とする。
A small test apparatus according to a second aspect of the present invention is a small test apparatus comprising a reaction container for accommodating a fermented body and an outer container for temperature control for accommodating the reaction container with a gas layer therebetween. A temperature follower for sequentially changing the temperature of the outer vessel according to the temperature of the fermented body in the reaction vessel; and adjusting the temperature of the outer vessel so that the temperature of the outer vessel is adjusted between the first time and the second time designated in advance. Temperature forcing means for gradually changing the temperature of the fermented body from the first temperature to the second temperature.

【0010】上記小型試験装置では、温度追従手段が反
応容器中の発酵体の温度に従って外側容器の温度を逐次
変化させるだけでなく、温度強制手段が、外側容器の温
度を調節することにより、予め指定した第1時刻から第
2時刻の間に、反応容器中の発酵体の温度を第1温度か
ら第2温度に徐々に変化させるので、反応容器中の発酵
体の温度を第1温度から第2温度に所望の曲線で連続的
に変化させることができる。つまり、温度追従手段を利
用して擬似断熱試験を行った際の温度変化曲線を利用し
て、再現性を試験したり、発酵量や発酵生物を最適化す
る温度パターンを決定することができる。
[0010] In the above-mentioned small test apparatus, the temperature follow-up means not only changes the temperature of the outer vessel in accordance with the temperature of the fermented body in the reaction vessel, but also the temperature forcing means adjusts the temperature of the outer vessel in advance. Since the temperature of the fermentation body in the reaction vessel is gradually changed from the first temperature to the second temperature between the designated first time and the second time, the temperature of the fermentation body in the reaction vessel is changed from the first temperature to the second temperature. The two temperatures can be varied continuously with the desired curve. In other words, the reproducibility can be tested and the temperature pattern for optimizing the fermentation amount and the fermentation organism can be determined by using the temperature change curve obtained by performing the pseudo adiabatic test using the temperature following means.

【0011】また、請求項3記載の小型試験装置は、発
酵体を収容する反応容器と、この反応容器を気体層を隔
てて収容する温度調節用の外側容器とを備える小型試験
装置であって、反応容器中の発酵体の温度に従って外側
容器の温度を逐次変化させる温度追従手段と、反応容器
に気体を供給する気体供給手段と、気体の温度、成分、
及び流量の少なくとも1つを調節する気体供給調節手段
とを備えることを特徴とする。
A small test apparatus according to a third aspect of the present invention is a small test apparatus comprising: a reaction container for accommodating a fermented body; and an outer container for temperature control for accommodating the reaction container with a gas layer therebetween. A temperature following means for sequentially changing the temperature of the outer vessel according to the temperature of the fermented body in the reaction vessel, a gas supply means for supplying a gas to the reaction vessel, a gas temperature, a component,
And gas supply adjusting means for adjusting at least one of the flow rates.

【0012】上記小型試験装置では、温度追従手段が反
応容器中の発酵体の温度に従って外側容器の温度を逐次
変化させる擬似断熱試験に際して、反応容器に供給する
気体の温度、成分、及び流量の少なくとも1つを調節す
ることができるので、反応容器に供給する気体の条件を
様々に変化させて、発酵量や発酵生物を最適化する気体
条件を決定することができる。
[0012] In the above-mentioned small-size test apparatus, at least a temperature, a component, and a flow rate of the gas supplied to the reaction vessel are used in the pseudo adiabatic test in which the temperature following means sequentially changes the temperature of the outer vessel according to the temperature of the fermented body in the reaction vessel. Since one of them can be adjusted, the gas conditions for optimizing the fermentation amount and the fermentation organism can be determined by variously changing the conditions of the gas supplied to the reaction vessel.

【0013】また、請求項4記載の小型試験装置では、
気体供給調節手段を制御して、反応容器中の発酵体の温
度に従って反応容器に供給する気体の温度を逐次変化さ
せる気体温度追従手段を更に備えることを特徴とする。
Further, in the small-sized test apparatus according to the fourth aspect,
The apparatus is further characterized by further comprising a gas temperature follow-up means for controlling the gas supply adjusting means and sequentially changing the temperature of the gas supplied to the reaction vessel in accordance with the temperature of the fermented body in the reaction vessel.

【0014】上記小型試験装置では、擬似断熱試験に際
して、反応容器に供給する気体による熱的外乱を低減し
て、より実際のコンポスト化プラント等に近い条件を設
定することができる。
[0014] In the above-mentioned small test apparatus, in the pseudo adiabatic test, the thermal disturbance due to the gas supplied to the reaction vessel is reduced, so that conditions closer to those of an actual composting plant or the like can be set.

【0015】[0015]

【発明の実施の形態】以下、この発明の実施の形態に係
る小型試験装置について、図面を参照しつつ説明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A small test apparatus according to an embodiment of the present invention will be described below with reference to the drawings.

【0016】図1は、実施形態の小型試験装置の全体構
造を説明するブロック図である。この小型試験装置は、
反応容器11及び外側容器13による二重構造となって
いる試験装置本体10と、試験装置本体10の重量を計
測する電子天秤20と、反応容器11の内部温度を計測
する第1温度計30と、外側容器13の外周に設けたヒ
ータ13aに適宜通電して外側容器13を加熱するヒー
タ駆動装置40と、外側容器13自体の温度を計測する
第2温度計50と、反応容器11に空気等を含むガスを
供給するガス源60と、反応容器11から出るガスを分
析するガス分析装置70と、小型試験装置全体を統括的
に制御する主制御装置90とを備える。なお上記のう
ち、ヒータ駆動装置40と主制御装置90は、温度制御
回路を構成する。
FIG. 1 is a block diagram for explaining the overall structure of the small test apparatus according to the embodiment. This small test device
A test apparatus main body 10 having a double structure including a reaction vessel 11 and an outer vessel 13, an electronic balance 20 for measuring the weight of the test apparatus main body 10, and a first thermometer 30 for measuring the internal temperature of the reaction vessel 11. A heater driving device 40 for heating the outer container 13 by appropriately energizing a heater 13a provided on the outer periphery of the outer container 13, a second thermometer 50 for measuring the temperature of the outer container 13 itself, and air or the like for the reaction container 11. A gas source 60 for supplying a gas containing the gas, a gas analyzer 70 for analyzing the gas flowing out of the reaction vessel 11, and a main controller 90 for controlling the entire small test apparatus as a whole. Among the above, the heater driving device 40 and the main control device 90 constitute a temperature control circuit.

【0017】試験装置本体10は、反応容器11内部に
ふすまや家畜糞といった発酵物質COを収容する。反応
容器11には、下部に入口部19aが設けられており、
ガス源60から酸素、水分等を含む空気であるガスが供
給される。発酵物質COから発生し或いはこれを通過し
たガスは、反応容器11上部の出口部19bを経てガス
分析装置70に導入される。なお、反応容器11は、熱
的な緩衝材として機能する空気層ARを介して外側容器
13に収容される。この場合、反応容器11と外側容器
13の間を空気層ARとしているが、この空間に空気以
外の各種気体を収容しても同様の効果を得ることができ
る。
The test apparatus main body 10 accommodates a fermentation substance CO such as bran or livestock dung inside the reaction vessel 11. The reaction vessel 11 is provided with an inlet portion 19a at a lower portion,
A gas, which is air containing oxygen, moisture, and the like, is supplied from a gas source 60. The gas generated from the fermentation substance CO or passed therethrough is introduced into the gas analyzer 70 via the outlet 19b at the top of the reaction vessel 11. The reaction container 11 is housed in the outer container 13 via an air layer AR functioning as a thermal buffer. In this case, the space between the reaction vessel 11 and the outer vessel 13 is an air layer AR. However, the same effect can be obtained by storing various gases other than air in this space.

【0018】電子天秤20は、試験装置本体10の質量
を計測することができ、反応容器11中における発酵物
質COの質量や、発酵物質COのコンポスト化に伴う質
量変化を精密に逐次検出することができ、その結果をデ
ジタルデータとして主制御装置90に出力する。
The electronic balance 20 can measure the mass of the test apparatus main body 10 and accurately and sequentially detect the mass of the fermentation substance CO in the reaction vessel 11 and the mass change accompanying the composting of the fermentation substance CO. And outputs the result to main controller 90 as digital data.

【0019】第1温度計30は、測温抵抗体等の感熱素
子からなり、温度計駆動装置32に駆動されて反応容器
11の内部、すなわち発酵物質COの温度を精密に逐次
検出することができ、その結果をデジタルデータとして
主制御装置90に出力する。
The first thermometer 30 is composed of a thermosensitive element such as a resistance thermometer, and is driven by a thermometer driving device 32 to accurately and sequentially detect the temperature of the inside of the reaction vessel 11, ie, the temperature of the fermentation substance CO. The result is output to main controller 90 as digital data.

【0020】ヒータ駆動装置40は、外側容器13の外
周に設けたヒータ13aに供給する電力を調節すること
ができ、ヒータ13aによって外側容器13全体を適当
に加熱させることができる。
The heater driving device 40 can adjust the power supplied to the heater 13a provided on the outer periphery of the outer container 13, so that the entire outer container 13 can be appropriately heated by the heater 13a.

【0021】第2温度計50は、測温抵抗体等の感熱素
子からなり、温度計駆動装置52に駆動されて外側容器
13自体、すなわち外側容器13を構成する壁体の温度
を精密に逐次検出することができ、その結果をデジタル
データとして主制御装置90に出力する。
The second thermometer 50 is composed of a thermosensitive element such as a resistance temperature detector, and is driven by a thermometer driving device 52 to accurately and sequentially measure the temperature of the outer container 13 itself, that is, the wall of the outer container 13. The result can be detected, and the result is output to main controller 90 as digital data.

【0022】ガス源60は、図示を省略するが、空気を
圧縮供給するコンプレサと、コンプレサからの空気の供
給量を調節する流量計と、コンプレサからの空気の温度
を調節する温度調節素子とを備える。なお、ガス源60
には、成分添加装置62が接続されており、反応容器1
1の入口部19aに供給する空気に酸素、水蒸気、二酸
化炭素等を適宜添加することができる。
The gas source 60 includes a compressor (not shown) for compressing and supplying air, a flow meter for adjusting the amount of air supplied from the compressor, and a temperature adjusting element for adjusting the temperature of air from the compressor. Prepare. The gas source 60
Is connected to a component addition device 62,
Oxygen, water vapor, carbon dioxide, or the like can be appropriately added to the air supplied to the first inlet portion 19a.

【0023】ガス分析装置70は、図示を省略するが、
アンモニア、水蒸気等のトラップ、酸素センサ等を備
え、反応容器11の出口部19bから排出されるガスの
成分や量を分析することができ、その結果をデジタルデ
ータとして主制御装置90に出力する。
The gas analyzer 70 is not shown, but
It is provided with a trap for ammonia, water vapor, etc., an oxygen sensor, etc., and can analyze the components and the amount of gas discharged from the outlet 19b of the reaction vessel 11, and output the result to the main controller 90 as digital data.

【0024】主制御装置90は、コンピュータ等からな
り、電子天秤20、第1温度計30、第2温度計50、
ガス分析装置70等から計測結果をデジタルデータとし
て受信し、その結果を経時変化として保存したり、統計
的に分析することができる。さらに、主制御装置90
は、第1温度計30や第2温度計50の計測結果をヒー
タ駆動装置40の出力制御に活用することができる。
The main controller 90 comprises a computer or the like, and includes an electronic balance 20, a first thermometer 30, a second thermometer 50,
The measurement result is received as digital data from the gas analyzer 70 or the like, and the result can be stored as a change with time or statistically analyzed. Further, main controller 90
Can use the measurement results of the first thermometer 30 and the second thermometer 50 for output control of the heater driving device 40.

【0025】図2は、試験装置本体10の詳細な構造を
説明する側方断面図である。試験装置本体10は、既述
のように反応容器11を外側容器13に収容した二重槽
となっている。
FIG. 2 is a side sectional view for explaining a detailed structure of the test apparatus main body 10. The test apparatus main body 10 is a double tank containing the reaction container 11 in the outer container 13 as described above.

【0026】内側の反応容器11は、ポリプロピレン等
の樹脂材からなり、下部で窄まった円筒状の形状を有し
ている。反応容器11の下端に設けた空気導用の入口部
19aは、チューブ14に着脱自在に接続されており、
このチューブ14を介して、図1のガス源60からの空
気等が供給される。反応容器11の上部は、アルミニュ
ウムで形成された封止部材15によって蓋がされてお
り、OリングOL1によって反応容器11内の気密性が
保たれている。この封止部材15は、外部容器13と熱
的に結合されており、熱伝導率の高い材料で製作されて
いるため、外部容器13の温度に十分追随する。この封
止部材15には、反応容器11内部の堆肥化空間CSに
延びる第1温度計30が固定されており、堆肥化空間C
Sの温度を計測することができる。また、封止部材15
には、堆肥化空間CSのガスを採取する出口部19bが
形成されており、堆肥化空間CSから排出されたガスを
配管15cを介して図1のガス分析装置70に供給す
る。さらに、封止部材15の中央部には、反応容器11
内の発酵物質を採取、観察等するためのサンプリング窓
15aが設けられている。このサンプリング窓15a
は、蓋部材16によって開閉可能になっており、Oリン
グOL2によって反応容器11内の気密性を保つことが
できる。反応容器11内の底に近い部分には、発酵物質
を収容する堆肥化空間CSの底となる多孔の底板部材1
7が固定されている。底板部材17の下側空間は、ガス
供給ポートGPとなっており、入口部19aから供給さ
れたガスを一旦貯留する。ガス供給ポートGPに供給さ
れたガスは、底板部材17に設けた多数の通気口17a
を介して堆肥化空間CSに供給される。
The inner reaction vessel 11 is made of a resin material such as polypropylene, and has a cylindrical shape narrowed at a lower portion. An inlet 19 a for air conduction provided at the lower end of the reaction vessel 11 is detachably connected to the tube 14.
Air and the like from the gas source 60 in FIG. 1 are supplied through the tube 14. The upper portion of the reaction vessel 11 is covered with a sealing member 15 made of aluminum, and the airtightness in the reaction vessel 11 is maintained by an O-ring OL1. Since the sealing member 15 is thermally coupled to the outer container 13 and is made of a material having a high thermal conductivity, it sufficiently follows the temperature of the outer container 13. A first thermometer 30 extending to the composting space CS inside the reaction vessel 11 is fixed to the sealing member 15, and the first composting space C
The temperature of S can be measured. Also, the sealing member 15
Is formed with an outlet 19b for collecting gas in the composting space CS, and supplies the gas discharged from the composting space CS to the gas analyzer 70 of FIG. 1 through the pipe 15c. Further, the center of the sealing member 15 is provided with the reaction vessel 11.
A sampling window 15a for collecting, observing, and the like the fermentation substance in the inside is provided. This sampling window 15a
Is openable and closable by a lid member 16, and the airtightness in the reaction vessel 11 can be maintained by the O-ring OL2. A portion near the bottom in the reaction vessel 11 has a porous bottom plate member 1 serving as a bottom of the composting space CS for accommodating fermentation substances.
7 is fixed. The lower space of the bottom plate member 17 is a gas supply port GP, and temporarily stores gas supplied from the inlet 19a. The gas supplied to the gas supply port GP is supplied to a large number of vents 17 a provided in the bottom plate member 17.
To the composting space CS.

【0027】外側容器13は、円柱状の内部空間に反応
容器11を空気層ARを介して収容している。外側容器
13の側壁は、ヒータ13aによって全体が被覆されて
いる。外側容器13の本体13bは、アルミニュウム等
の材料からなり、周囲のヒータ13aによって全体がほ
ぼ均一に加熱される。本体13bの側壁内部には、第2
温度計50が埋め込まれており、本体13bの温度を計
測することができる。本体13bの底部には、開口13
cが形成されており、反応容器11下端の突起である入
口部19aが挿入されて外部に露出する。なお、開口1
3cにはOリングOL3が埋め込まれており、外側容器
13の内部空間すなわち空気層ARの気密性を保つ。外
側容器13の上端は、反応容器11の蓋を兼ねる封止部
材15によって封止されている。さらに、反応容器11
全体は、本体13bの下部から延びる支柱18を介して
図1の電子天秤20に固定されている。
The outer vessel 13 contains the reaction vessel 11 in a cylindrical internal space via an air space AR. The entire side wall of the outer container 13 is covered with a heater 13a. The main body 13b of the outer container 13 is made of a material such as aluminum, and is entirely uniformly heated by the surrounding heater 13a. The second inside of the side wall of the main body 13b
The thermometer 50 is embedded, and can measure the temperature of the main body 13b. An opening 13 is provided at the bottom of the main body 13b.
c is formed, and the inlet 19a, which is a projection at the lower end of the reaction vessel 11, is inserted and exposed to the outside. Opening 1
An O-ring OL3 is buried in 3c to maintain the airtightness of the internal space of the outer container 13, that is, the air layer AR. The upper end of the outer container 13 is sealed by a sealing member 15 also serving as a lid of the reaction container 11. Further, the reaction vessel 11
The whole is fixed to the electronic balance 20 of FIG. 1 via a column 18 extending from the lower part of the main body 13b.

【0028】図2の試験装置本体10を簡単化した熱系
として考えると、発熱体である発酵物質を収容する堆肥
化空間CSと、反応容器11と、空気層ARと、外側容
器13の本体13bと、熱源であるヒータ13aとを直
列に接続したものと考えることができる。例えば、堆肥
化空間CSの温度を第1温度計30で計測しつつ、第2
温度計50によって検出した本体13bの温度が第1温
度計30の計測結果と等しくなるようにヒータ13aを
駆動すれば、堆肥化空間CSと本体13bとの温度がほ
ぼ等しくなり、熱的な均衡が保たれるので、堆肥化空間
CSから空気層ARや外側容器13への熱の流出や、外
側容器13から堆肥化空間CSへの熱の流入がほとんど
相殺され、反応容器11が周囲から熱的に孤立する擬似
断熱効果が得られる。この際、空気層ARがバッファと
なって反応容器11が周囲温度の強い作用を受けること
を防止することができる。すなわち、ヒータ13aの制
御遅れやオーバーシュートによる熱の過剰な流入・流出
が適度な時間遅れで作用する。これにより、反応容器1
1の熱的な安定性を高め、擬似断熱効果の精度をより高
めることができる。なお、本体13bの肉厚をある程度
厚くしているので、外側容器13がある程度の熱容量を
持つことになり、ヒータ13aによる不均一な加熱を回
避することができる。また、ヒータ13aと第2温度計
50とを適度に離しているので、外側容器13の本体1
3bの温度をより正確に測定することができる。
Assuming that the test apparatus main body 10 shown in FIG. 2 is a simplified heat system, the composting space CS for accommodating the fermentation substance as a heating element, the reaction vessel 11, the air layer AR, and the main body of the outer vessel 13 It can be considered that the heater 13a and the heater 13a as a heat source are connected in series. For example, while measuring the temperature of the composting space CS with the first thermometer 30, the second
If the heater 13a is driven so that the temperature of the main body 13b detected by the thermometer 50 becomes equal to the measurement result of the first thermometer 30, the temperatures of the composting space CS and the main body 13b become substantially equal, and the thermal balance Is maintained, the outflow of heat from the composting space CS to the air layer AR and the outer container 13 and the inflow of heat from the outer container 13 to the composting space CS are almost offset, and the reaction container 11 is heated from the surroundings. A pseudo adiabatic effect which is isolated in isolation is obtained. At this time, it is possible to prevent the reaction vessel 11 from being strongly affected by the ambient temperature due to the air layer AR serving as a buffer. That is, excessive inflow / outflow of heat due to control delay of the heater 13a or overshoot acts with an appropriate time delay. Thereby, the reaction vessel 1
1 can be improved in thermal stability, and the accuracy of the pseudo adiabatic effect can be further improved. In addition, since the thickness of the main body 13b is increased to some extent, the outer container 13 has a certain heat capacity, and uneven heating by the heater 13a can be avoided. Further, since the heater 13a and the second thermometer 50 are appropriately separated from each other, the main body 1 of the outer container 13 is
The temperature of 3b can be measured more accurately.

【0029】一方、図2の試験装置本体10では、反応
容器11と外側容器13とを分離することができるの
で、反応容器11を熱変形に比較的弱い材料で形成する
ことができる。また、反応容器11に発酵物質を充填し
た状態で別の装置にて事前に殺菌等の熱処理を施した
り、反応容器11を複数準備してこれらを交換しつつコ
ンポスト化の試験を行うことができる。また、試験後に
反応容器11のみを洗浄したり、反応容器11を発酵物
質とともに廃棄することもできる。さらに、反応容器1
1と外側容器13が構造上分離しているので、反応容器
11とヒータ13aも分離され、漏電事故を未然に防止
することができる。なお、反応容器11に収容される発
酵物質は水分を多量に含むものも多く、発酵過程でも水
分を発生するので、反応容器11と不可分にヒータ13
aを設けた場合、漏電防止に配慮する必要が生じる。
On the other hand, in the test apparatus main body 10 shown in FIG. 2, since the reaction vessel 11 and the outer vessel 13 can be separated, the reaction vessel 11 can be formed of a material which is relatively resistant to thermal deformation. In addition, a heat treatment such as sterilization may be performed in advance with another apparatus in a state where the reaction vessel 11 is filled with the fermentation substance, or a test of composting may be performed while preparing a plurality of reaction vessels 11 and exchanging them. . After the test, only the reaction vessel 11 can be washed, or the reaction vessel 11 can be discarded together with the fermentation substance. Further, the reaction vessel 1
Since the first container 1 and the outer container 13 are structurally separated from each other, the reaction container 11 and the heater 13a are also separated from each other, thereby preventing an electric leakage accident. The fermented substance contained in the reaction vessel 11 often contains a large amount of water, and water is also generated during the fermentation process.
When a is provided, it is necessary to take into consideration the prevention of electric leakage.

【0030】特に反応容器11をポリプロピレンで形成
しているので、反応容器11を別のオートクレーブ殺菌
装置で殺菌処理することができ、装置内を無菌状態にし
てから、実験を開始することができる。なお、上記のよ
うなオートクレーブ殺菌が行えない場合、アルコール等
を用いた殺菌が必要になるが、このような殺菌剤は外乱
要素となる可能性がある。また、反応容器11がポリプ
ロピレン製であるので、金属材料で形成した場合のよう
にイオン(例えば銅イオンには殺菌効果があるといわれ
る)の流出がななく、反応系である発酵物質に影響を与
える心配がない。さらに、金属容器と比較して不要な熱
流が発生しにくく、擬似熱系の安定性をより高めること
ができる。
In particular, since the reaction vessel 11 is made of polypropylene, the reaction vessel 11 can be sterilized by another autoclave sterilization apparatus, and the experiment can be started after the inside of the apparatus is sterilized. When the autoclave sterilization as described above cannot be performed, sterilization using alcohol or the like is required, but such a sterilizing agent may be a disturbance factor. In addition, since the reaction vessel 11 is made of polypropylene, there is no outflow of ions (for example, copper ions are said to have a bactericidal effect) unlike the case where the reaction vessel 11 is formed of a metal material, so that the fermentation substance as a reaction system is not affected. Don't worry about giving. Further, unnecessary heat flow is less likely to be generated as compared with the metal container, and the stability of the pseudo heat system can be further improved.

【0031】以下、図1の小型試験装置の動作を説明す
る。まず、反応容器11の温度制御について説明する。
The operation of the small test apparatus shown in FIG. 1 will be described below. First, the temperature control of the reaction vessel 11 will be described.

【0032】反応容器11については、温度追従手段に
よって実現される温度追従モードと、温度保持手段によ
って実現される温度保持モードと、温度強制手段によっ
て実現される温度強制モードとを含む3つのモードで温
度調節が行われる。これらの動作モードは、主制御装置
90にプログラムされており、オペレータの指示に従
い、これらモードを単独で或いは適宜組み合わせて反応
容器11の温度管理を行うことができる。反応容器11
の温度管理に際して、主制御装置90は、第1及び第2
温度計30、50の計測結果に基づいてヒータ駆動装置
40を制御し、ヒータ13aによる外側容器13の加熱
量を制御する。
The reaction vessel 11 has three modes including a temperature following mode realized by the temperature following means, a temperature holding mode realized by the temperature holding means, and a temperature forced mode realized by the temperature forcing means. Temperature control is performed. These operation modes are programmed in the main control device 90, and the temperature of the reaction vessel 11 can be controlled individually or in an appropriate combination according to an instruction of the operator. Reaction vessel 11
When the temperature is controlled, the main controller 90 controls the first and second
The heater driving device 40 is controlled based on the measurement results of the thermometers 30 and 50, and the amount of heating of the outer container 13 by the heater 13a is controlled.

【0033】上記温度制御において、温度追従モードで
は、反応容器11中の発酵物質CO温度計測結果に従っ
て外側容器13の温度を逐次変化させる。具体的には、
ヒータ13aの通電量をPID制御等の手法を利用して
調節し、第2温度計50の計測値を第1温度計30の計
測値(変動する目標値)に一致させる。
In the above temperature control, in the temperature following mode, the temperature of the outer container 13 is sequentially changed according to the result of measuring the temperature of the fermentation substance CO in the reaction container 11. In particular,
The amount of electricity supplied to the heater 13a is adjusted using a technique such as PID control, and the measured value of the second thermometer 50 is made to match the measured value of the first thermometer 30 (a fluctuating target value).

【0034】温度保持モードでは、予め指定した時刻に
反応容器11中の発酵物質COの温度を所望の温度値に
保持する。具体的には、ヒータ13aの通電量をPID
制御等の手法を利用して調節し、第1温度計30の計測
値を一定の目標値に一致させる。この場合、第2温度計
50の計測値は、第1温度計30の計測値よりもある程
度小さくなり、反応容器11で発生した熱が外側容器1
3に流出することになる。
In the temperature keeping mode, the temperature of the fermentation substance CO in the reaction vessel 11 is kept at a desired temperature at a time designated in advance. Specifically, the power supply amount of the heater 13a is determined by PID
Adjustment is performed using a method such as control, and the measurement value of the first thermometer 30 is made to coincide with a constant target value. In this case, the measured value of the second thermometer 50 is somewhat smaller than the measured value of the first thermometer 30, and the heat generated in the reaction vessel 11
3 will flow out.

【0035】温度強制モードでは、予め指定した時刻t
1から時刻t2までの間に、反応容器11中の発酵物質C
Oの温度を温度T1から温度T2に徐々に変化させる。具
体的には、第1温度計30の計測値が所望の曲線を描く
ように、PID制御等の手法を利用してヒータ13aの
通電量を調節する。なお、外側容器13の温度に対応す
る第2温度計50の計測値が所望の曲線を描くようにヒ
ータ13aの通電量を調節することもできる。この場
合、厳密には反応容器11の温度を制御することはでき
ない。
In the temperature forced mode, a time t specified in advance
From time 1 to time t2, fermentation substance C in reaction vessel 11
The temperature of O is gradually changed from the temperature T1 to the temperature T2. Specifically, the energization amount of the heater 13a is adjusted using a technique such as PID control so that the measurement value of the first thermometer 30 draws a desired curve. It should be noted that the amount of electricity supplied to the heater 13a can be adjusted so that the measured value of the second thermometer 50 corresponding to the temperature of the outer container 13 draws a desired curve. In this case, the temperature of the reaction vessel 11 cannot be strictly controlled.

【0036】以上のような温度管理により、図1の小型
試験装置を用いて以下に例示するような各種条件で実験
を行うことができる。
With the above-described temperature control, an experiment can be performed using the small test apparatus of FIG. 1 under various conditions as exemplified below.

【0037】まず、実験の再現性を確保するため、温度
保持モードで反応容器11を一定時間一定の温度に保
ち、その後、温度追従モードで反応容器11を擬似断熱
して発酵物質COの温度を自然に上昇させる。この場
合、サンプルである発酵物質COを一定温度に保った
後、発酵物質COの温度変化に伴って外側容器13の温
度を逐次変化させる。このように、擬似断熱の前工程と
して温度を一定にする定値制御工程を設けることによ
り、発酵物質COの発酵過程における初期条件をほぼ一
致させることができ、再現性の高い実験が可能になる。
First, in order to ensure the reproducibility of the experiment, the reaction vessel 11 is kept at a constant temperature for a certain time in the temperature holding mode, and then the temperature of the fermentation substance CO is reduced by pseudo-insulating the reaction vessel 11 in the temperature following mode. Let it rise naturally. In this case, after keeping the fermentation substance CO as a sample at a constant temperature, the temperature of the outer container 13 is sequentially changed with the temperature change of the fermentation substance CO. As described above, by providing the constant value control step of keeping the temperature constant as a pre-process of the pseudo adiabatic process, the initial conditions in the fermentation process of the fermentation substance CO can be substantially matched, and an experiment with high reproducibility can be performed.

【0038】図3(a)は、上記の温度制御を概念的に
説明するグラフであり、横軸は時間、縦軸は温度を示
す。グラフからも明らかなように、時刻t0まで反応容
器11中の発酵物質COの温度をT0に保持する。その
後、反応容器11を擬似断熱して、反応容器11を自然
な温度上昇に任せる。
FIG. 3A is a graph conceptually illustrating the above-mentioned temperature control. The horizontal axis indicates time, and the vertical axis indicates temperature. As is clear from the graph, the temperature of the fermentation substance CO in the reaction vessel 11 is maintained at T0 until time t0. After that, the reaction vessel 11 is pseudo-insulated to allow the reaction vessel 11 to naturally rise in temperature.

【0039】別の実験として、予め温度追従モードで反
応容器11を擬似断熱して発酵物質COの温度を自然に
上昇させ、その際の温度履歴を記憶しておく。次に、反
応容器11中の発酵物質COを交換するなどして、温度
強制モードで反応容器11の温度を調節する。この場
合、温度追従モードで反応容器11を擬似断熱した際の
温度履歴に一致するように反応容器11の温度を強制的
に変化させる。このような実験では、当初の擬似断熱試
験の再現性を確認することができる。
As another experiment, the temperature of the fermentation substance CO is naturally raised by pseudo-insulating the reaction vessel 11 in the temperature following mode in advance, and the temperature history at that time is stored. Next, the temperature of the reaction vessel 11 is adjusted in the temperature forced mode, for example, by exchanging the fermentation substance CO in the reaction vessel 11. In this case, the temperature of the reaction vessel 11 is forcibly changed so as to match the temperature history when the reaction vessel 11 is pseudo-insulated in the temperature following mode. In such an experiment, the reproducibility of the initial pseudo adiabatic test can be confirmed.

【0040】さらに別の実験として、予め温度追従モー
ドで反応容器11を擬似断熱して発酵物質COの温度を
自然に上昇させ、その際の温度履歴を記憶しておく。こ
のような温度履歴を温度的、時間的に変形した変形パタ
ーンをオペレータ側で設定し、この変形パターンに基づ
いて反応容器11の温度を強制的に調節する。このよう
な実験では、発酵物質COの発酵パターンの最適化や発
酵生成物の最適化を図る各種シミュレーションが可能に
なり、多様な実験結果を収集することが可能になる。
As still another experiment, the temperature of the fermentation substance CO is naturally increased by pseudo-insulating the reaction vessel 11 in the temperature following mode in advance, and the temperature history at that time is stored. An operator sets a deformation pattern obtained by deforming such a temperature history in terms of temperature and time, and forcibly adjusts the temperature of the reaction vessel 11 based on the deformation pattern. In such an experiment, various simulations for optimizing the fermentation pattern of the fermentation substance CO and optimizing the fermentation product can be performed, and various experimental results can be collected.

【0041】図3(b)は、上記の温度制御を概念的に
説明するグラフである。時刻t1に温度T1であった反応
容器11中の発酵物質COの温度を、徐々に上昇させて
時刻t2に温度T2としている。なお、一点鎖線は、予め
行った擬似断熱試験の温度履歴を示しており、実線の変
形パターンでは、擬似断熱の場合の温度変化に対してΔ
Tだけ発酵物質COの温度を上昇させた条件で試験を行
っている。
FIG. 3B is a graph conceptually illustrating the above temperature control. The temperature of the fermentation substance CO in the reaction vessel 11 that was at the temperature T1 at the time t1 is gradually increased to the temperature T2 at the time t2. The dashed line indicates the temperature history of the pseudo adiabatic test performed in advance.
The test is performed under the condition that the temperature of the fermentation substance CO is increased by T.

【0042】さらに別の実験として、実際のコンポスト
化プラントの外界条件等を考慮して任意の温度上昇パタ
ーンを設定し、この温度上昇パターンに基づいて反応容
器11の温度を強制的に調節することもできる。このよ
うな実験では、実プラントの環境条件を考慮したシミュ
レーションが可能になる。
As another experiment, an arbitrary temperature rise pattern is set in consideration of the external conditions of the actual composting plant, and the temperature of the reaction vessel 11 is forcibly adjusted based on the temperature rise pattern. You can also. In such an experiment, a simulation that takes into account the environmental conditions of the actual plant becomes possible.

【0043】以下、反応容器11へのガス供給の制御に
ついて説明する。反応容器11に供給されるガスの温度
や流量は、ガス源60や成分添加装置62の制御によっ
て適宜調節される。例えば、反応容器11に供給する空
気等に含まれる水分量を調節するとともに、ガス分析装
置70で排気ガス中の水分量を計測することにより、発
酵物質COから発生した水分を計測することができる。
同様にして、酸素の吸収量、アンモニアの発生量等を監
視することができる。反応容器11に供給するガスは、
パルス状に増減させることができる。これにより、実際
のコンポスト化プラント等で外気を定期的に供給して換
気を行う場合のシミュレーションが可能になる。
Hereinafter, control of gas supply to the reaction vessel 11 will be described. The temperature and the flow rate of the gas supplied to the reaction vessel 11 are appropriately adjusted by controlling the gas source 60 and the component addition device 62. For example, the moisture generated from the fermentation substance CO can be measured by adjusting the amount of moisture contained in the air or the like supplied to the reaction vessel 11 and measuring the amount of moisture in the exhaust gas by the gas analyzer 70. .
Similarly, the amount of absorbed oxygen, the amount of generated ammonia, and the like can be monitored. The gas supplied to the reaction vessel 11 is
It can be increased or decreased in a pulsed manner. This makes it possible to simulate the case where ventilation is performed by periodically supplying outside air in an actual composting plant or the like.

【0044】反応容器11に供給するガスの温度は、気
体温度追従手段によって実現される気体温度追従モード
と、気体温度保持手段によって実現される気体温度保持
モードと、気体温度強制手段によって実現される気体温
度強制モードとを含む3つのモードで管理される。これ
らの動作モードは、主制御装置90にプログラムされて
おり、オペレータの指示に従い、これらモードを単独で
或いは適宜組み合わせて反応容器11の温度管理を行う
ことができる。
The temperature of the gas supplied to the reaction vessel 11 is realized by a gas temperature tracking mode realized by gas temperature tracking means, a gas temperature holding mode realized by gas temperature holding means, and a gas temperature forcing means. It is managed in three modes including a gas temperature forced mode. These operation modes are programmed in the main control device 90, and the temperature of the reaction vessel 11 can be controlled individually or in an appropriate combination according to an instruction of the operator.

【0045】気体温度追従モードでは、反応容器11中
の発酵物質CO温度計測結果に従って反応容器11に供
給するガスの温度を逐次変化させる。また、気体温度保
持モードでは、予め指定した時刻、期間において反応容
器11に供給するガスの温度を所望の温度値に保持す
る。さらに、気体温度強制モードでは、予め指定した時
刻t1から時刻t2までの間に、反応容器11に供給する
ガスの温度を温度T1から温度T2に徐々に所望の率で変
化させる。
In the gas temperature tracking mode, the temperature of the gas supplied to the reaction vessel 11 is sequentially changed according to the result of measuring the temperature of the fermentation substance CO in the reaction vessel 11. In the gas temperature holding mode, the temperature of the gas supplied to the reaction vessel 11 at a predetermined time and period is held at a desired temperature value. Further, in the gas temperature compulsory mode, the temperature of the gas supplied to the reaction vessel 11 is gradually changed from the temperature T1 to the temperature T2 at a desired rate between the time t1 and the time t2 designated in advance.

【0046】以上の気体温度追従モードでは、熱の漏洩
が無くなり擬似断熱の効果を高めることができる。これ
により、反応容器11内における熱収支を正確に測定す
ることができる。また、気体温度保持モードや気体温度
強制モードでは、供給ガスの温度を一定値にしたり所望
の温度に時事刻々変化させることができるので、実際の
コンポスト化プラント等の外気条件等を考慮して任意の
温度上昇パターンを設定することができる。このような
実験では、実プラント等の環境条件を考慮したシミュレ
ーションが可能になる。
In the above-described gas temperature follow-up mode, the leakage of heat is eliminated, and the effect of pseudo heat insulation can be enhanced. Thereby, the heat balance in the reaction vessel 11 can be accurately measured. In addition, in the gas temperature holding mode or the gas temperature forced mode, the temperature of the supplied gas can be kept constant or changed to a desired temperature every moment. Temperature rise pattern can be set. In such an experiment, a simulation can be performed in consideration of environmental conditions of an actual plant or the like.

【0047】以上、実施の形態に即して本発明を説明し
たが、本発明は上記実施形態に限定されるものではな
い。例えば、外側容器13の温度を調節するため、ヒー
タ13aとともにペルチエ素子やウォータジャケットを
外側容器13の周囲に設けることができる。この場合、
外側容器13のさらに自在な温度調節が可能になり、反
応容器11を自在に温度制御することができる。
Although the present invention has been described with reference to the embodiment, the present invention is not limited to the above embodiment. For example, in order to adjust the temperature of the outer container 13, a Peltier element or a water jacket can be provided around the outer container 13 together with the heater 13a. in this case,
The temperature of the outer vessel 13 can be more freely adjusted, and the temperature of the reaction vessel 11 can be freely controlled.

【0048】[0048]

【発明の効果】請求項1記載の小型試験装置によれば、
温度追従手段が反応容器中の発酵体の温度に従って外側
容器の温度を逐次変化させるだけでなく、温度保持手段
が、外側容器の温度を調節することにより、予め指定し
た時刻に反応容器中の発酵体の温度を所定の温度に保持
するので、反応容器中の発酵体の温度を一定時間だけ所
定の温度に保持する定値制御試験を行ったり、このよう
な定値制御後に温度追従手段を利用して擬似断熱試験を
行うことができる。
According to the small-sized test apparatus according to the first aspect,
The temperature follower not only changes the temperature of the outer container sequentially according to the temperature of the fermented body in the reaction vessel, but also the temperature holding means adjusts the temperature of the outer vessel so that the fermentation in the reaction vessel can be performed at a predetermined time. Since the temperature of the body is maintained at a predetermined temperature, a constant value control test for maintaining the temperature of the fermented body in the reaction vessel at a predetermined temperature for a predetermined time is performed, or the temperature follow-up means is used after such constant value control. A simulated adiabatic test can be performed.

【0049】また、請求項2記載の小型試験装置によれ
ば、温度追従手段が反応容器中の発酵体の温度に従って
外側容器の温度を逐次変化させるだけでなく、温度強制
手段が、外側容器の温度を調節することにより、予め指
定した第1時刻から第2時刻の間に、反応容器中の発酵
体の温度を第1温度から第2温度に徐々に変化させるの
で、反応容器中の発酵体の温度を第1温度から第2温度
に所望の曲線で連続的に変化させることができる。つま
り、温度追従手段を利用して擬似断熱試験を行った際の
温度変化曲線を利用して、再現性を試験したり、発酵量
や発酵生物を最適化する温度パターンを決定することが
できる。
According to the small-sized test apparatus of the second aspect, not only the temperature follow-up means changes the temperature of the outer vessel in accordance with the temperature of the fermented body in the reaction vessel, but also the temperature forcing means comprises By adjusting the temperature, the temperature of the fermented body in the reaction vessel is gradually changed from the first temperature to the second temperature between the first time and the second time specified in advance, so that the fermented body in the reaction vessel is changed. Can be continuously changed from the first temperature to the second temperature with a desired curve. In other words, the reproducibility can be tested and the temperature pattern for optimizing the fermentation amount and the fermentation organism can be determined by using the temperature change curve obtained by performing the pseudo adiabatic test using the temperature following means.

【0050】また、請求項3記載の小型試験装置によれ
ば、温度追従手段が反応容器中の発酵体の温度に従って
外側容器の温度を逐次変化させる擬似断熱試験に際し
て、反応容器に供給する気体の温度、成分、及び流量の
少なくとも1つを調節することができるので、反応容器
に供給する気体の条件を様々に変化させて、発酵量や発
酵生物を最適化する気体条件を決定することができる。
According to the third aspect of the present invention, in the simulated adiabatic test in which the temperature following means sequentially changes the temperature of the outer vessel according to the temperature of the fermentation body in the reaction vessel, Since at least one of the temperature, the component, and the flow rate can be adjusted, the conditions of the gas supplied to the reaction vessel can be variously changed to determine the gas conditions for optimizing the fermentation amount and the fermentation organism. .

【0051】また、請求項4記載の小型試験装置によれ
ば、擬似断熱試験に際して、反応容器に供給する気体に
よる熱的外乱を低減して、より実際のコンポスト化プラ
ント等に近い条件を設定することができる。
According to the small-sized test apparatus of the fourth aspect, in the pseudo adiabatic test, the thermal disturbance due to the gas supplied to the reaction vessel is reduced, and conditions closer to those of an actual composting plant or the like are set. be able to.

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

【図1】この発明の実施の形態に係る小型試験装置の全
体構造を説明する図である。
FIG. 1 is a diagram illustrating an overall structure of a small test apparatus according to an embodiment of the present invention.

【図2】図1の小型試験装置を構成する試験装置本体の
詳細な構造を説明する図である。
FIG. 2 is a diagram illustrating a detailed structure of a test apparatus main body constituting the small test apparatus of FIG.

【図3】図1の小型試験装置を用いた温度制御の例を説
明する図である。
FIG. 3 is a diagram illustrating an example of temperature control using the small test device of FIG. 1;

【符号の説明】[Explanation of symbols]

10 試験装置本体 11 反応容器 13 外側容器 13a ヒータ 13b 本体 15 封止部材 15a サンプリング窓 17 底板部材 19a 入口部 19b 出口部 20 電子天秤 30 第1温度計 32 温度計駆動装置 40 ヒータ駆動装置 50 第2温度計 52 温度計駆動装置 60 ガス源 62 成分添加装置 70 ガス分析装置 90 主制御装置 AR 空気層 CO 発酵物質 DESCRIPTION OF SYMBOLS 10 Test apparatus main body 11 Reaction container 13 Outer container 13a Heater 13b Main body 15 Sealing member 15a Sampling window 17 Bottom plate member 19a Inlet part 19b Outlet part 20 Electronic balance 30 First thermometer 32 Thermometer driving device 40 Heater driving device 50 Second Thermometer 52 Thermometer driving device 60 Gas source 62 Component adding device 70 Gas analyzer 90 Main controller AR Air layer CO Fermentation material

───────────────────────────────────────────────────── フロントページの続き (72)発明者 椎葉 究 茨城県つくば市大久保13番地 日清製粉株 式会社つくば研究所内 (72)発明者 小峰 法子 茨城県つくば市大久保13番地 日清製粉株 式会社つくば研究所内 (72)発明者 木村 俊範 茨城県土浦市永国台2−25 Fターム(参考) 4D004 AA02 BA04 CA19 CA22 CA46 CB04 CB06 CB32 CC02 CC08 DA01 DA02 DA06 DA10 DA11 DA12 4D059 AA01 AA07 BA03 BA56 BK13 CC01 DB02 EA06 EA09 EB06 4H061 AA03 AA10 CC36 CC41 CC47 EE66 GG48 GG70  ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Kaoru Shiiba 13 Okubo, Tsukuba, Ibaraki Nisshin Flour Milling Co., Ltd. Inside the Tsukuba Research Laboratory (72) Inventor Toshinori Kimura 2-25 Ekunokudai, Tsuchiura-shi, Ibaraki Pref. EA09 EB06 4H061 AA03 AA10 CC36 CC41 CC47 EE66 GG48 GG70

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 発酵体を収容する反応容器と、当該反応
容器を気体層を隔てて収容する温度調節用の外側容器と
を備える小型試験装置であって、 前記反応容器中の前記発酵体の温度に従って前記外側容
器の温度を逐次変化させる温度追従手段と、 前記外側容器の温度を調節することにより、予め指定し
た時刻に前記反応容器中の前記発酵体の温度を所定の温
度に保持する温度保持手段とを備えることを特徴とする
小型試験装置。
1. A small-sized test apparatus comprising: a reaction vessel containing a fermented body; and an outer vessel for temperature control containing the reaction vessel separated by a gas layer, wherein the fermentation body in the reaction vessel is A temperature follower for sequentially changing the temperature of the outer container according to a temperature; and a temperature for maintaining the temperature of the fermented body in the reaction container at a predetermined time at a predetermined time by adjusting the temperature of the outer container. A small-sized test apparatus comprising: a holding unit.
【請求項2】 発酵体を収容する反応容器と、当該反応
容器を気体層を隔てて収容する温度調節用の外側容器と
を備える小型試験装置であって、 前記反応容器中の前記発酵体の温度に従って前記外側容
器の温度を逐次変化させる温度追従手段と、 前記外側容器の温度を調節することにより、予め指定し
た第1時刻から第2時刻の間に、前記反応容器中の前記
発酵体の温度を第1温度から第2温度に徐々に変化させ
る温度強制手段とを備えることを特徴とする小型試験装
置。
2. A small-sized test apparatus comprising: a reaction vessel containing a fermented body; and an outer vessel for temperature control containing the reaction vessel separated by a gas layer, wherein the fermentation body in the reaction vessel is provided. A temperature following means for sequentially changing the temperature of the outer container according to the temperature; and adjusting the temperature of the outer container to adjust the temperature of the fermented body in the reaction container between a first time and a second time specified in advance. A small test apparatus comprising: temperature forcing means for gradually changing a temperature from a first temperature to a second temperature.
【請求項3】 発酵体を収容する反応容器と、当該反応
容器を気体層を隔てて収容する温度調節用の外側容器と
を備える小型試験装置であって、 前記反応容器中の前記発酵体の温度に従って前記外側容
器の温度を逐次変化させる温度追従手段と、 前記反応容器に気体を供給する気体供給手段と、 前記気体の温度、成分及び流量の少なくとも1つを調節
する気体供給調節手段とを備えることを特徴とする小型
試験装置。
3. A small-sized test apparatus comprising: a reaction vessel for accommodating a fermented body; and an outer vessel for temperature control for accommodating the reaction vessel with a gas layer therebetween, wherein the fermentation body in the reaction vessel is provided. Temperature following means for sequentially changing the temperature of the outer container according to temperature; gas supply means for supplying a gas to the reaction vessel; and gas supply adjustment means for adjusting at least one of the temperature, component and flow rate of the gas. A small-sized test apparatus comprising:
【請求項4】 前記気体供給調節手段を制御して、前記
反応容器中の前記発酵体の温度に従って前記反応容器に
供給する気体の温度を逐次変化させる気体温度追従手段
を更に備えることを特徴とする請求項3記載の小型試験
装置。
4. The apparatus according to claim 1, further comprising gas temperature tracking means for controlling said gas supply adjusting means to sequentially change the temperature of gas supplied to said reaction vessel in accordance with the temperature of said fermented body in said reaction vessel. The small test apparatus according to claim 3, wherein
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100514011C (en) * 2007-01-30 2009-07-15 中国科学院上海光学精密机械研究所 High-light pulse type pseudo-thermal light source
CN102936160A (en) * 2012-12-10 2013-02-20 东北农业大学 Composting fermentation box of livestock excrement laboratory

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102786363A (en) * 2012-02-21 2012-11-21 天津生态城环保有限公司 Novel kitchen garbage fermentation device and usage method

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JPS56100188A (en) * 1980-01-10 1981-08-11 Hitachi Kiden Kogyo Kk Fermentation device
JPH03199184A (en) * 1989-12-28 1991-08-30 Akira Ito Organic waste fermenting device
JPH07313955A (en) * 1994-05-26 1995-12-05 Sanyo Electric Co Ltd Organic substance treating apparatus
JPH10128303A (en) * 1996-11-06 1998-05-19 Yanmar Agricult Equip Co Ltd Garbage treatment apparatus
JPH10309558A (en) * 1998-06-23 1998-11-24 Matsushita Electric Ind Co Ltd Garbage treating machine
JP2000325930A (en) * 1999-05-25 2000-11-28 S K K:Kk Garbage treatment apparatus for household use
JP2002253201A (en) * 2001-02-28 2002-09-10 Nisshin Seifun Group Inc Small-sized testing device
JP2002255678A (en) * 2001-02-28 2002-09-11 National Agricultural Research Organization Composting laboratory equipment

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS56100188A (en) * 1980-01-10 1981-08-11 Hitachi Kiden Kogyo Kk Fermentation device
JPH03199184A (en) * 1989-12-28 1991-08-30 Akira Ito Organic waste fermenting device
JPH07313955A (en) * 1994-05-26 1995-12-05 Sanyo Electric Co Ltd Organic substance treating apparatus
JPH10128303A (en) * 1996-11-06 1998-05-19 Yanmar Agricult Equip Co Ltd Garbage treatment apparatus
JPH10309558A (en) * 1998-06-23 1998-11-24 Matsushita Electric Ind Co Ltd Garbage treating machine
JP2000325930A (en) * 1999-05-25 2000-11-28 S K K:Kk Garbage treatment apparatus for household use
JP2002253201A (en) * 2001-02-28 2002-09-10 Nisshin Seifun Group Inc Small-sized testing device
JP2002255678A (en) * 2001-02-28 2002-09-11 National Agricultural Research Organization Composting laboratory equipment

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100514011C (en) * 2007-01-30 2009-07-15 中国科学院上海光学精密机械研究所 High-light pulse type pseudo-thermal light source
CN102936160A (en) * 2012-12-10 2013-02-20 东北农业大学 Composting fermentation box of livestock excrement laboratory

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