JPS61289879A - Apparatus for controlling aging temperature of fermentation tank - Google Patents

Apparatus for controlling aging temperature of fermentation tank

Info

Publication number
JPS61289879A
JPS61289879A JP60131301A JP13130185A JPS61289879A JP S61289879 A JPS61289879 A JP S61289879A JP 60131301 A JP60131301 A JP 60131301A JP 13130185 A JP13130185 A JP 13130185A JP S61289879 A JPS61289879 A JP S61289879A
Authority
JP
Japan
Prior art keywords
temperature
heat medium
heat
tank
medium
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
Application number
JP60131301A
Other languages
Japanese (ja)
Inventor
Izumi Azuma
東 泉
Akio Adachi
昭夫 安達
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.)
Fuji Electric Co Ltd
Original Assignee
Fuji Electric Co Ltd
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 Fuji Electric Co Ltd filed Critical Fuji Electric Co Ltd
Priority to JP60131301A priority Critical patent/JPS61289879A/en
Publication of JPS61289879A publication Critical patent/JPS61289879A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To keep the aging temperature of a raw material to the optimum fermentation temperature all the year round, by uniformly heating or cooling the raw material charged in the fermentation tank according to the variation of ambient temperature condition. CONSTITUTION:Plural heat-exchange pipes 3 are inserted separately in the raw material 2 charged in the fermentation tank 1. When the aging temperature of the raw material 2 becomes higher than the optimum temperature, the freezing machine 11 of the medium-cooling apparatus 4 is operated, the thermal medium in the tank 9 is cooled by the evaporator 12, the temperature of the medium is detected by the temperature sensor 14 and adjusted with the temperature controller 15 and the medium is supplied through the medium-circulation 6 to the pipe 3 with the circulation pump 5 to effect the uniform cooling of the raw material 2. When the aging temperature is lower than a preset level, the electric heater 10 of the apparatus 4 is electrified to heat the medium, and the heated medium is supplied through the pump 5 and the channel 6 to the pipe 3 to effect the uniform heating of the raw material 2.

Description

【発明の詳細な説明】[Detailed description of the invention] 【発明の属する技術分野】[Technical field to which the invention pertains]

この発明は、例えば味噌の製造に使用する醸造タンクを
対象に、該タンク内に仕込んだ味噌の原料の均温加熱な
いし均温冷却を行い、年間を通じて醸造の際の熟成温度
を適正温度に調整維持するようにした醸造タンクの熟成
温度調整装置に関する。
This invention targets a brewing tank used for the production of miso, for example, and uniformly heats or cools the miso raw materials charged in the tank to adjust the ripening temperature during brewing to an appropriate temperature throughout the year. This invention relates to a fermentation temperature adjustment device for a brewing tank.

【従来技術とその問題点】[Prior art and its problems]

頭記した味噌に対象に醸造を行う場合に、味噌の品質は
その熟成温度に大きく左右されことが知られている。一
般に味噌の醗酵は30℃前後で程よく進行し、熟成温度
がこの温度よりも低いと味噌の熟成が遅れて熟成効率が
低くなる。また温度が高過ぎると味噌に変色、変味が生
じて品質のよい味噌が作れない。一方、味噌は40〜5
0%の水分を含む中間水分食品であってその性状として
熱伝導性が低く、このために原料を醸造タンク内に仕込
んで味噌の醸造を行う場合にはその熟成温度の管理面で
様々な障害が生じる。すなわち大形の醸造タンク内に味
噌の原料を仕込んだ状態では、タンク内の中心部はタン
クの周壁に接する周辺部に比べて熱の応答性が悪く、し
たがってこのままでは醗酵熱の蓄積によりタンク内の中
心部が周辺部に比べて温度が異常に高くなり、中心部で
熟成が過度となって味噌にいわゆる悲境り現象は発」−
する。 特に間近では味噌の低食塩化が進み、また醸造の際に酵
母培養液を添加したりする傾向があり、このために酵母
の醗酵が旺盛となって醗酵熱の発〈[聞が大きく、醸造
中の半成味噌の温度」1昇に与える影響も大である。こ
のように味噌を製造する際には、その醸造工程における
熟成温度が品質管理の上で極めて重要な意味をもってい
る。 かかる点、従来における味噌の醸造工程では醸造タンク
を据(−Jけた部屋の室内空気調和によるQi純な方法
で醸造中の味噌の熟成温度管理を行っているのが現状で
ある。しかt7てごのような室内の空気調和方式では、
前述のように味噌の熱伝導性が低いためにタンク内の温
度分布に大幅なばらつきが生じ、特にタンク内の中心部
では醗酵熱の蓄積による温度」1昇が過度になっていわ
ゆる悲境Lj現象の発生が道側〕られない。このために
味噌の悲境は防止策として、一部ではタンクの芯を抜い
た1’−−ナラ形の醸造タンクの使用も試みられている
が、この方式でも大形の醸造タンクではタンク内の温度
分布にばらつきを無くずことができず充分な成yが4η
られていない。 また別な手段として熱運搬性能に優れた特性を示すし−
1、パイプを使用し、このヒートバ・イブを醸造タンク
の中心部にに方から原寧1内に挿入t7てこの部分の過
度な発生熱を列部に放熱さゼる方法も一部で試験的に試
みらねでいる。このヒートパイプの採用によれば、特に
タンク内の過剰熱の除熱に優れた効果を発揮して味噌の
芯焼り現象を防止できる。しかして冬期のように周囲温
度の低い什態に番、t、ヒートパイプはそのままでは役
に立たない。すなわち先述のように味噌の熟成温度は3
01前後がi!!温であることから、周囲温度の低い冬
期には逆に醸造中の味噌の温度を適正温度まで高める必
要がある。しかしてタンク内に長尺のヒートパイプを突
き立てて使用Jる状態では、ヒートパイプブのウィック
による毛細管力には限界があり、ヒートパイプの1−、
@部へ外部から熱を加えても作動液がパイプ内の底部に
寝込んだままとなってヒートパイプの機能が働かず醸造
タンク内の加熱作用を充分に発1ボできない。一方、冬
期における醸造タンクの加熱手段としてタンクの外周に
熱媒パイプを壱装し1.、′、の熱媒バイブに湯等の高
温熱媒を供給して加熱する方法が考えられるが、この方
法でも味噌自Iの熱伝導性が低いためにタンク内全域で
均温加熱することができず、μm成温度の適温維持に充
分な効果が発揮できない。
When brewing the above-mentioned miso, it is known that the quality of the miso is greatly influenced by its maturing temperature. Generally, the fermentation of miso proceeds moderately at around 30°C, and if the ripening temperature is lower than this temperature, the ripening of miso will be delayed and the ripening efficiency will be low. Also, if the temperature is too high, the miso will change color and taste, making it impossible to produce high-quality miso. On the other hand, miso is 40-5
It is an intermediate-moisture food containing 0% water and has low thermal conductivity.For this reason, when miso is brewed by putting raw materials into a brewing tank, there are various problems in managing the ripening temperature. occurs. In other words, when miso raw materials are placed in a large brewing tank, the center of the tank has poor heat response compared to the peripheral area that touches the tank's peripheral wall, and if left as it is, fermentation heat will accumulate inside the tank. The temperature in the center of the miso becomes abnormally high compared to the surrounding area, causing excessive ripening in the center and causing the so-called doomsday phenomenon in miso.
do. In particular, in recent years, miso has become increasingly low in sodium chloride, and there is also a tendency to add yeast culture liquid during brewing, which has led to active yeast fermentation and the production of fermentation heat. It also has a great effect on raising the temperature of the semi-finished miso inside. When producing miso in this way, the aging temperature during the brewing process has an extremely important meaning in terms of quality control. In view of this, in the conventional miso brewing process, the temperature at which the miso is ripened during brewing is controlled using a simple method of indoor air conditioning in a room with a brewing tank installed. In an indoor air conditioning system like this,
As mentioned above, due to the low thermal conductivity of miso, there is a large variation in the temperature distribution inside the tank, and especially in the center of the tank, the temperature increases by 1 due to the accumulation of fermentation heat, resulting in the so-called disaster Lj. The occurrence of the phenomenon cannot be detected on the road side. For this reason, as a preventive measure against miso miso, some attempts have been made to use a 1'--oak-shaped brewing tank with the tank core removed, but even with this method, large-sized brewing tanks do not require much space inside the tank. It is not possible to eliminate variations in the temperature distribution of
It has not been done. As another means, it exhibits excellent properties in heat transport performance.
1. Using a pipe, insert this Heatba-Eve into the center of the brewing tank from the direction into the 1st part of the brewing tank. A method was also tested in which the excessive heat generated at the lever part was radiated to the row part. I'm not really trying. By employing this heat pipe, it is particularly effective in removing excess heat within the tank, thereby preventing the core burning phenomenon of miso. However, when the ambient temperature is low, such as during the winter, the heat pipe is of no use as it is. In other words, as mentioned earlier, the ripening temperature of miso is 3.
Around 01 is i! ! Since the temperature is high, in winter when the ambient temperature is low, it is necessary to raise the temperature of miso during brewing to an appropriate temperature. However, when using a long heat pipe stuck inside a tank, there is a limit to the capillary force due to the heat pipe's wick, and the heat pipe's 1-
Even if heat is applied from the outside to the @ part, the working fluid remains at the bottom of the pipe, and the heat pipe function does not work, making it impossible to generate sufficient heating within the brewing tank. On the other hand, as a heating means for the brewing tank in winter, a heating medium pipe is installed around the outer circumference of the tank.1. A possible method is to supply a high temperature heat medium such as hot water to the heat medium vibrator of ,', but even with this method, it is difficult to uniformly heat the entire area inside the tank due to the low thermal conductivity of Misoji I. Therefore, a sufficient effect cannot be exhibited in maintaining the appropriate μm formation temperature.

【発明の目的】[Purpose of the invention]

この発明は上記の点にかんがみなされたものであり、例
えば前記した味噌の醸造を対象にその醸造タンク内にイ
]込んだ原料を周囲温度条件の変動に対応して均温加熱
ないし均温冷却し、原料の熟成温度を年間を通じて適正
な醗酵温度に維持できるようにL7た醸造タンクの熟成
温度調整装置を従供することを目的とする。
This invention has been made in consideration of the above points, and is intended for example for the above-mentioned miso brewing, and is capable of uniformly heating or uniformly cooling raw materials placed in a brewing tank in response to fluctuations in ambient temperature conditions. The purpose of the present invention is to provide a fermentation temperature adjustment device for a L7 brewing tank so that the fermentation temperature of raw materials can be maintained at an appropriate fermentation temperature throughout the year.

【発明の要点】[Key points of the invention]

上記目的を達成するために、この発明は#造タンクに対
し該タンクに仕込んだ原料内に分散して外部より挿入し
た複数本の熱交換パイプと、外部に装置の熱媒加熱/冷
却装置と、前記熱交換パイプと熱媒加熱/冷却装置との
間に配管した熱媒循環回路と、および熱媒循環回路に介
装した熱媒循環ポンプとを装備してなり、周囲温度条件
に対応する熱媒加熱/7;i却装置の加熱ないし冷却手
段の運転選択により温度1iJ整された熱媒を熱媒循環
回路を通じて熱交換バイブに循環供給し、醸造タンク内
における原料熟成温度の適温調整を行うように構成した
ものである。
In order to achieve the above object, the present invention includes a plurality of heat exchange pipes inserted from the outside and dispersed within the raw material charged in the tank, and a heat medium heating/cooling device of the device externally. , equipped with a heat medium circulation circuit piped between the heat exchange pipe and the heat medium heating/cooling device, and a heat medium circulation pump interposed in the heat medium circulation circuit, and adapted to the ambient temperature conditions. Heating medium heating/7: The heating medium whose temperature has been adjusted to 1 iJ by the operation selection of the heating or cooling means of the cooling device is circulated and supplied to the heat exchanger vibrator through the heating medium circulation circuit, and the appropriate temperature adjustment of the raw material ripening temperature in the brewing tank is carried out. It is configured to do so.

【発明の実施例】[Embodiments of the invention]

第1図はこの発明の実晦例による温度調整装置の系統図
、第2図および第3図はそれぞれ第1図における熱交換
パイプの異なる実施例の構成図である。まず第1図にお
いて、1は醸造タンク、2は該タンク内いのち仕込んだ
味噌の原料である。 かかる醸造タンク1に対して、この発明により前記醸造
タンク1内に仕込んだ原料2に中に多数の熱交換バイブ
3が分散して外部より差込み配備されており、この熱交
換パイプ3と符号4で示す熱媒加熱/冷却装置との間を
結んで熱媒循環ポンプ5を介装した熱媒循環回路6が構
成されている。 なお7.8は各熱交換パイプ3と接続した熱媒の入ロヘ
ソダ管および出[1ヘツダ管である。一方、前記した熱
交換パイプ3は、例えば第2図に示すようなU字管形の
金属性パイプ、あるいは第3図に示すような内管旧と久
管32からなる二重金属管が採用される。また熱媒加熱
/冷却装W4は熱媒タンク9、該熱媒タンク内で熱媒に
浸漬して配備された熱媒加熱手段としての電熱ヒータ1
0、熱媒冷却手段とし7ての冷凍la]+の蒸発!1i
12、熱媒攪拌機13、および温度センサ14を装備の
温度制御器15等を備えて構成されている。 次に上記構成ににる醸造タンク1に対する熟成温度の温
度調整動作を説明する。ます列気温度の低い冬期を除き
、醸造タンクl内にお番ノる原料2の熟成温度が醗酵熱
の蓄積によって適正な熟成温度以トに高くなる状態では
、熱媒加熱/冷却装置4におLJる冷凍機11を選択し
て運転し、その蒸発器12を通じて熱媒タンク9内の熱
媒を冷却する。 この場合に熱媒温度は温度センサ14で検出され、その
温度検出値を基に温度制御器I5により冷凍機11を運
転制御することにより熱媒温度が、所望の冷却温度とな
るように温度iN整される。一方、熱媒攪拌機13によ
り熱媒タンク9内で攪拌された熱媒は熱媒循環ポンプ5
により矢印のように熱媒循環回路6を通じて各熱交換パ
イプ3へ循環供給され、この過程で醸造タンク1内のほ
ぼ全域を均温冷却して醗酵熱による余分な熱を奪って系
外に除熱する。しかもこの場合に複数本の熱交換パイプ
3が醸造タンクl内で原料2と直接接触するように分散
して挿入配備されており、これにより夏期等の周囲温度
が高い場合にも醸造タンクl内の全域で原料2の熟成温
度を適正な醗酵温度に維持できるようになる。なお付近
で低温お地下水等が豊富に得られるならば、前記した冷
凍機IIを水冷却器に置き換えて実施することもできる
。 一方、冬期のように周囲温度が低く醸造中の熟成温度を
適正な醗酵温度まで高める必要のある場合には、前記と
は逆に熱媒加熱/冷却装置4の電   1熱ヒータ10
を選択してこれに通電して熱媒を適正醗酵温度に対応す
る30℃程度に加温し、この状態で熱媒を各熱交換パイ
プ3へ供給する。これ番こより醸造タンク1内の全域で
原料2の熟成温度を適正な醗酵温度に均温加熱して醸造
を進行させることができる。 なお上記実施例は味噌の醸造への適用に付いて述べたが
、その用途は味噌のめに限定されるものではなく、他の
製品の醸造を行う場合にも同様に実施適用が可能である
FIG. 1 is a system diagram of a temperature regulating device according to an embodiment of the present invention, and FIGS. 2 and 3 are configuration diagrams of different embodiments of the heat exchange pipe in FIG. 1, respectively. First, in FIG. 1, 1 is a brewing tank, and 2 is the raw material for miso that is stored inside the tank. According to the present invention, a large number of heat exchange vibrators 3 are inserted into the brewing tank 1 from the outside and inserted into the raw material 2 charged in the brewing tank 1, and the heat exchange pipes 3 and 4 are connected to each other. A heat medium circulation circuit 6 in which a heat medium circulation pump 5 is interposed is connected to the heat medium heating/cooling device shown in . Note that 7.8 is a heat medium inlet header pipe and an outlet header pipe connected to each heat exchange pipe 3. On the other hand, the heat exchange pipe 3 described above may be, for example, a U-shaped metal pipe as shown in FIG. 2, or a double metal pipe consisting of an inner tube and a long tube as shown in FIG. Ru. The heat medium heating/cooling device W4 includes a heat medium tank 9, and an electric heater 1 as a heat medium heating means provided immersed in the heat medium in the heat medium tank.
0, refrigeration la] + evaporation as a heat medium cooling means 7! 1i
12, a heat medium stirrer 13, a temperature controller 15 equipped with a temperature sensor 14, and the like. Next, the temperature adjustment operation of the ripening temperature for the brewing tank 1 having the above configuration will be explained. Except for the winter season when the air temperature is low, when the ripening temperature of the raw material 2 in the brewing tank 1 becomes higher than the appropriate ripening temperature due to the accumulation of fermentation heat, the heat medium heating/cooling device 4 The LJ refrigerator 11 is selected and operated, and the heat medium in the heat medium tank 9 is cooled through its evaporator 12. In this case, the heating medium temperature is detected by the temperature sensor 14, and the temperature controller I5 controls the operation of the refrigerator 11 based on the detected temperature value, so that the heating medium temperature reaches the desired cooling temperature (iN). It will be arranged. On the other hand, the heat medium stirred in the heat medium tank 9 by the heat medium stirrer 13 is transferred to the heat medium circulation pump 5.
As shown by the arrow, the heat medium is circulated and supplied to each heat exchange pipe 3 through the heat medium circulation circuit 6, and in this process, almost the entire area inside the brewing tank 1 is uniformly cooled, removing excess heat due to fermentation heat and removing it from the system. heat. Moreover, in this case, a plurality of heat exchange pipes 3 are inserted and arranged in a distributed manner so as to be in direct contact with the raw material 2 inside the brewing tank 1, so that even when the ambient temperature is high such as in the summer, the heat exchange pipes 3 can be inserted into the brewing tank 1. It becomes possible to maintain the ripening temperature of raw material 2 at an appropriate fermentation temperature over the entire range of . Note that if low-temperature ground water or the like is available in abundance in the vicinity, the above-mentioned refrigerator II can be replaced with a water cooler. On the other hand, when the ambient temperature is low and it is necessary to raise the ripening temperature during brewing to the appropriate fermentation temperature, such as in winter, the electric heater 10 of the heat medium heating/cooling device 4 should be
is selected and energized to heat the heat medium to about 30° C. corresponding to the appropriate fermentation temperature, and in this state the heat medium is supplied to each heat exchange pipe 3. From this point on, the fermentation temperature of the raw material 2 can be uniformly heated to a proper fermentation temperature throughout the entire region inside the brewing tank 1, and brewing can proceed. Although the above embodiments have been described with reference to the application to the brewing of miso, the application is not limited to miso noodles, and can be similarly applied to the brewing of other products. .

【発明の効果】【Effect of the invention】

以−り述べたようにこの発明によれば、醸造タンクに対
し該タンクに仕込んだ原料内に分散して外部より挿入し
た複数本の熱交換パイプと、外部に設置の熱媒加熱/冷
却v装置と、前記熱交換パイプと熱媒加熱/冷却装置と
の間に配管した熱媒循環回路と、および熱媒循環回路に
介装した熱媒循環ポンプとを装備してなり、周囲温度条
件に対応する熱媒加熱/冷却装置の加熱ないし冷却手段
の運転選択により温度調整された熱媒を熱媒循環回路を
通じて熱交換パイプに循環供給し、醸造タンク内におけ
る原料熟成温度の適温調整を行うように構成したことに
より、年間を通じての周囲温度の変動に対応して醸造タ
ンク内の全域で原料を均温加熱、均温冷却し、その熟成
温度を適正な醗酵温度に釘醋整維持することができる。
As described above, according to the present invention, a plurality of heat exchange pipes are inserted into the brewing tank from the outside and dispersed within the raw materials charged in the tank, and a heat medium heating/cooling pipe installed externally is connected to the brewing tank. The apparatus is equipped with a heat medium circulation circuit piped between the heat exchange pipe and the heat medium heating/cooling device, and a heat medium circulation pump interposed in the heat medium circulation circuit, and is equipped with The heating medium whose temperature has been adjusted by selecting the operation of the heating or cooling means of the corresponding heating medium heating/cooling device is circulated and supplied to the heat exchange pipe through the heating medium circulation circuit, and the temperature for ripening the raw material in the brewing tank is adjusted to an appropriate temperature. With this configuration, it is possible to uniformly heat and uniformly cool the raw materials throughout the entire area within the brewing tank in response to fluctuations in ambient temperature throughout the year, and to maintain the ripening temperature at the appropriate fermentation temperature. can.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図はこの発明の実施例による熟成温度調整装置の系
統図、第2図および第3図はそれぞれ第1図における熱
交換パイプの異なる実施例の構成図である。図において
、 1:醸造タンク、2;原料、3:熱交換パイプ、4:熱
媒加熱/冷却装置、5:熱媒循環ポンプ、6:熱媒循環
回路、IO:熱媒加熱手段としての電熱ヒータ、11:
熱媒冷却手段としての冷凍機。
FIG. 1 is a system diagram of a ripening temperature adjusting device according to an embodiment of the present invention, and FIGS. 2 and 3 are configuration diagrams of different embodiments of the heat exchange pipe in FIG. 1, respectively. In the figure, 1: Brewing tank, 2: Raw material, 3: Heat exchange pipe, 4: Heat medium heating/cooling device, 5: Heat medium circulation pump, 6: Heat medium circulation circuit, IO: Electric heat as heat medium heating means. Heater, 11:
Refrigerator as a heat medium cooling means.

Claims (1)

【特許請求の範囲】[Claims] 1)醸造タンクに対し該タンクに仕込んだ原料内に分散
して外部より挿入した複数本の熱交換パイプと、外部に
設置の熱媒加熱/冷却装置と、前記熱交換パイプと熱媒
加熱/冷却装置との間に配管した熱媒循環回路と、およ
び熱媒循環回路に介装した熱媒循環ポンプとを装備して
なり、周囲温度条件に対応する熱媒加熱/冷却装置の加
熱ないし冷却手段の運転選択により温度調整された熱媒
を熱媒循環回路を通じて熱交換パイプに循環供給し、醸
造タンク内における原料熟成温度の適温調整を行うこと
を特徴とする醸造タンクの熟成温度調整装置。
1) A plurality of heat exchange pipes inserted into the brewing tank from the outside and dispersed within the raw materials charged in the tank, a heat medium heating/cooling device installed externally, and the heat exchange pipes and the heat medium heating/cooling device installed externally. Equipped with a heat medium circulation circuit piped between the heat medium circulation circuit and the cooling device, and a heat medium circulation pump installed in the heat medium circulation circuit, the heat medium heating/cooling device can be heated or cooled according to ambient temperature conditions. A fermentation temperature adjustment device for a brewing tank, characterized in that a heat medium whose temperature has been adjusted by selecting an operation of a means is circulated and supplied to a heat exchange pipe through a heat medium circulation circuit to appropriately adjust the temperature for ripening raw materials in a brewing tank.
JP60131301A 1985-06-17 1985-06-17 Apparatus for controlling aging temperature of fermentation tank Pending JPS61289879A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60131301A JPS61289879A (en) 1985-06-17 1985-06-17 Apparatus for controlling aging temperature of fermentation tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60131301A JPS61289879A (en) 1985-06-17 1985-06-17 Apparatus for controlling aging temperature of fermentation tank

Publications (1)

Publication Number Publication Date
JPS61289879A true JPS61289879A (en) 1986-12-19

Family

ID=15054759

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60131301A Pending JPS61289879A (en) 1985-06-17 1985-06-17 Apparatus for controlling aging temperature of fermentation tank

Country Status (1)

Country Link
JP (1) JPS61289879A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006134451A1 (en) * 2005-06-14 2006-12-21 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Fermentation unit with liquid nitrogen cooling
JP2007500502A (en) * 2003-07-31 2007-01-18 プロフィタ・ビオロギッシャー・プフランツェンシュッツ・ゲゼルシャフト・ミト・ベシュレンクテル・ハフツング Solid fermenter

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5087588A (en) * 1973-12-06 1975-07-14
JPS5176479A (en) * 1974-12-24 1976-07-02 Toyo Engineering Corp TADANKOTAI BAIYOSO

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5087588A (en) * 1973-12-06 1975-07-14
JPS5176479A (en) * 1974-12-24 1976-07-02 Toyo Engineering Corp TADANKOTAI BAIYOSO

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007500502A (en) * 2003-07-31 2007-01-18 プロフィタ・ビオロギッシャー・プフランツェンシュッツ・ゲゼルシャフト・ミト・ベシュレンクテル・ハフツング Solid fermenter
JP4663640B2 (en) * 2003-07-31 2011-04-06 プロフィタ・ビオロギッシャー・プフランツェンシュッツ・ゲゼルシャフト・ミト・ベシュレンクテル・ハフツング Solid fermenter
WO2006134451A1 (en) * 2005-06-14 2006-12-21 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Fermentation unit with liquid nitrogen cooling
US7704732B2 (en) 2005-06-14 2010-04-27 American Air Liquide, Inc. Fermentation unit with liquid nitrogen cooling

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