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JPH0571212B2 - - Google Patents
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JPH0571212B2 - - Google Patents

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Publication number
JPH0571212B2
JPH0571212B2 JP26459386A JP26459386A JPH0571212B2 JP H0571212 B2 JPH0571212 B2 JP H0571212B2 JP 26459386 A JP26459386 A JP 26459386A JP 26459386 A JP26459386 A JP 26459386A JP H0571212 B2 JPH0571212 B2 JP H0571212B2
Authority
JP
Japan
Prior art keywords
carbon dioxide
carbon
heater
temperature
combustion
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.)
Expired - Lifetime
Application number
JP26459386A
Other languages
Japanese (ja)
Other versions
JPS63116623A (en
Inventor
Masato Hosaka
Atsushi Nishino
Jiro Suzuki
Jun Takeda
Takeshi Shimizu
Hiroshi Hamamoto
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Refrigeration Co
Matsushita Electric Industrial 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 Matsushita Refrigeration Co, Matsushita Electric Industrial Co Ltd filed Critical Matsushita Refrigeration Co
Priority to JP61264593A priority Critical patent/JPS63116623A/en
Priority to US07/113,766 priority patent/US4754611A/en
Priority to KR1019870012146A priority patent/KR900003723B1/en
Publication of JPS63116623A publication Critical patent/JPS63116623A/en
Publication of JPH0571212B2 publication Critical patent/JPH0571212B2/ja
Granted legal-status Critical Current

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  • Storage Of Harvested Produce (AREA)
  • Storage Of Fruits Or Vegetables (AREA)

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、生鮮物の置かれている雰囲気の空気
組成を調節することにより、呼吸作用や微生物、
酵素などの活動を抑制する貯蔵装置として、生鮮
物貯蔵の分野に利用される。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention improves respiration and microorganisms by adjusting the air composition of the atmosphere in which fresh food is placed.
It is used in the field of fresh food storage as a storage device that suppresses enzyme activity.

従来の技術 従来の貯蔵装置は、例えば加藤薫「新しい資源
方式CA貯蔵システムについて」(空気調和と冷凍
1974−7P191)に示されるように、第2図のよう
な構成になつていた。
Conventional technology Conventional storage devices are used, for example, in Kaoru Kato's ``About a new resource-based CA storage system'' (air conditioning and refrigeration).
1974-7P191), the structure was as shown in Figure 2.

すなわち、ボンベ等より供給された燃料と循環
用送風機1により、冷蔵庫2から供給された空気
3が混合し、二酸化炭素発生装置4内で燃焼して
二酸化炭素を発生させる。そして二酸化炭素発生
装置4で発生した二酸化炭素は冷蔵庫2へ供給さ
れるために、冷蔵庫2内の酸素を減少し、二酸化
炭素を増加する。二酸化炭素濃度が設定値になれ
ばスクラバ5を運転し、過剰な二酸化炭素を吸着
する。次に酸素濃度が設定値になれば、二酸化炭
素発生装置4を停止し、酸素補給用送風機6を運
転して、生鮮物の置かれている雰囲気の空気組成
を一定に保つようにして、生鮮物の貯蔵を行うも
のである。
That is, fuel supplied from a cylinder or the like is mixed with air 3 supplied from the refrigerator 2 by the circulation blower 1, and the mixture is combusted in the carbon dioxide generator 4 to generate carbon dioxide. Since the carbon dioxide generated by the carbon dioxide generator 4 is supplied to the refrigerator 2, oxygen in the refrigerator 2 is decreased and carbon dioxide is increased. When the carbon dioxide concentration reaches the set value, the scrubber 5 is operated to adsorb excess carbon dioxide. Next, when the oxygen concentration reaches the set value, the carbon dioxide generator 4 is stopped and the oxygen supply blower 6 is operated to maintain a constant air composition in the atmosphere in which the perishables are placed. It is used to store things.

発明が解決しようとする問題点 しかしこのような構造の生鮮物貯蔵装置の燃料
に石油系のガス燃料を用いると、排気ガス中に多
量の水蒸気を含むために、この水蒸気を凝縮させ
るために非常に大きな凝縮器が必要になるという
問題があつた。
Problems to be Solved by the Invention However, when petroleum-based gas fuel is used as fuel for a perishables storage device having such a structure, the exhaust gas contains a large amount of water vapor, so it takes a very long time to condense this water vapor. The problem was that a large condenser was required.

そこで燃料に炭素燃料を用いると水蒸気の発生
という問題を避けることができる。しかし、この
様な燃焼炉では燃焼初期に炭素燃料の上層部の温
度がまだ低いために、燃焼開始後しばらくの間、
燃焼炉からは一酸化炭素を大量に含んだ低温の燃
焼ガスが排出される。このために、二酸化炭素発
生装置の下流に設けた空気予熱器が能力を十分に
発揮できず、燃焼炉内の温度が安定し、安定した
燃焼が行えるまでに長時間を要するという新たな
問題が生じてきた。
Therefore, if carbon fuel is used as fuel, the problem of water vapor generation can be avoided. However, in such a combustion furnace, the temperature of the upper layer of carbon fuel is still low at the beginning of combustion, so for a while after combustion starts,
The combustion furnace emits low-temperature combustion gas containing a large amount of carbon monoxide. As a result, the air preheater installed downstream of the carbon dioxide generator cannot reach its full potential, creating a new problem in that it takes a long time for the temperature inside the combustion furnace to stabilize and stable combustion to occur. It has arisen.

本発明は簡単な構成で、始動直後から空気予熱
器の能力を最大限に活用し、燃焼炉が短時間で安
定した燃焼を行える生鮮物貯蔵装置を提供するも
のである。
The present invention provides a perishables storage device which has a simple configuration, makes full use of the capacity of the air preheater immediately after startup, and allows the combustion furnace to perform stable combustion in a short period of time.

問題点を解決するための手段 そこで、本発明は始動時にヒータに通電すると
ともに、循環用送風機を運転するものである。
Means for Solving the Problems Accordingly, the present invention energizes the heater and operates the circulation blower at the time of startup.

作 用 この技術的手段による作用は次のようになる。
二酸化炭素発生装置に炭素燃料を加熱するヒータ
を設け、始動時にヒータに通電するとともに、循
環用送風機を運転することにより、ヒータが送風
により冷却され、ヒータの通電率が上昇する。こ
のために、燃焼炉内に供給される熱量が増加し、
また送風により熱伝導が促進されて、燃焼炉内の
温度が無風時に比べて早く安定する。したがつて
炭素燃料が燃焼可能な温度レベルに達したとき
に、炭素燃料の上層部と下層部での温度差が余り
なく、燃焼を開始しても燃焼炉からは一酸化炭素
を大量に含んだ燃焼ガスが排出されない。このた
めに、二酸化炭素発生装置の下流に設けた空気予
熱器は高温の燃焼ガスが送られるために、空気予
熱器が能力を十分に発揮でき、燃焼炉内の温度が
安定し、燃焼が安定する時間を大幅に短縮するこ
とができる。
Effect The effect of this technical means is as follows.
The carbon dioxide generator is provided with a heater that heats carbon fuel, and when the heater is started, the heater is energized and a circulation blower is operated, whereby the heater is cooled by the air flow and the energization rate of the heater increases. For this reason, the amount of heat supplied into the combustion furnace increases,
Additionally, the blowing of air promotes heat conduction, and the temperature inside the combustion furnace stabilizes faster than when there is no wind. Therefore, when the carbon fuel reaches a temperature level where it can be combusted, there is not much difference in temperature between the upper and lower parts of the carbon fuel, and even if combustion starts, the combustion furnace will contain a large amount of carbon monoxide. No combustion gas is emitted. For this reason, the air preheater installed downstream of the carbon dioxide generator receives high-temperature combustion gas, which allows the air preheater to fully demonstrate its capacity, stabilizes the temperature inside the combustion furnace, and stabilizes combustion. The time required to do so can be significantly reduced.

実施例 以下、本発明の一実施例を添付図面を基づいて
説明する。
Embodiment An embodiment of the present invention will be described below with reference to the accompanying drawings.

第1図において、二酸化炭素発生装置7の燃焼
炉8を仕切るように火格子9を設け、その上に炭
素燃料10を供給する。また火格子9の下には電
熱ヒータ11が設けてある。始動時に電熱ヒータ
11に通電すると同時に、循環用送風機12を運
転し、燃焼炉8に燃焼用空気を供給する。炭素燃
料10が燃焼可能な温度まで上昇すると、炭素燃
料10は燃焼を開始する。この時の燃焼量は炭素
燃料10の表面積と、炭素燃料10に供給される
酸素量で決定される。
In FIG. 1, a fire grate 9 is provided so as to partition a combustion furnace 8 of a carbon dioxide generator 7, and a carbon fuel 10 is supplied onto the fire grate 9. Further, an electric heater 11 is provided below the grate 9. At the time of startup, the electric heater 11 is energized and at the same time the circulation blower 12 is operated to supply combustion air to the combustion furnace 8. When the temperature of the carbon fuel 10 rises to a point where it can be combusted, the carbon fuel 10 starts to burn. The amount of combustion at this time is determined by the surface area of the carbon fuel 10 and the amount of oxygen supplied to the carbon fuel 10.

二酸化炭素発生装置7で発生した多量の二酸化
炭素を含む排気ガスは、浄化用触媒13で浄化さ
れる。浄化用触媒13にはヒータ(図示せず)が
設けてあり、浄化用触媒13の温度が活性温度よ
り低い場合には、ヒータで浄化用触媒13を加熱
する構造になつている。浄化用触媒13で浄化さ
れた排気ガスは空気予熱器14で燃焼用空気を予
熱したのちに、冷却器15で冷却され、スクラバ
16を通つて冷蔵庫17へ供給される。そしてこ
のことより酸素濃度が低下した空気は、再び循環
用送風機12により燃焼炉8へ供給される。この
サイクルは冷蔵庫17内の二酸化炭素濃度が設定
値になるまで続けられる。
Exhaust gas containing a large amount of carbon dioxide generated by the carbon dioxide generator 7 is purified by the purification catalyst 13. The purification catalyst 13 is provided with a heater (not shown), and when the temperature of the purification catalyst 13 is lower than the activation temperature, the purification catalyst 13 is heated by the heater. The exhaust gas purified by the purification catalyst 13 preheats combustion air in the air preheater 14, is cooled in the cooler 15, and is supplied to the refrigerator 17 through the scrubber 16. Then, the air whose oxygen concentration has decreased due to this is supplied to the combustion furnace 8 again by the circulation blower 12. This cycle continues until the carbon dioxide concentration within the refrigerator 17 reaches the set value.

冷蔵庫17内の二酸化炭素濃度が設定値になる
と、スクラバ16が吸脱着運転して、設定値以上
の過剰な二酸化炭素を吸着し、冷蔵庫17内の二
酸化炭素濃度が設定値になるように調節してい
る。
When the carbon dioxide concentration in the refrigerator 17 reaches the set value, the scrubber 16 operates to adsorb and desorb excess carbon dioxide exceeding the set value, and adjusts the carbon dioxide concentration in the refrigerator 17 to the set value. ing.

冷蔵庫17内の酸素濃度が設定値になると、二
酸化炭素発生装置7を停止する。以後は貯蔵して
いる生鮮物が呼吸することにより消費した酸素
は、酸素供給用送風機18より大気中の酸素を冷
蔵庫17へ供給し、生鮮物が呼吸することにより
発生した二酸化炭素はスクラバ16により吸着す
ることにより、冷蔵庫17内の空気組成を設定値
に保ち続ける。
When the oxygen concentration in the refrigerator 17 reaches the set value, the carbon dioxide generator 7 is stopped. Thereafter, the oxygen consumed by the stored perishables when they breathe is supplied from the oxygen supply blower 18 to the refrigerator 17, and the carbon dioxide generated when the perishables breathe is removed by the scrubber 16. By adsorption, the air composition within the refrigerator 17 is maintained at the set value.

このような構成の本発明の実施例の具体的な動
作関係について以下に説明する。
The specific operational relationship of the embodiment of the present invention having such a configuration will be described below.

一般に電熱ヒータ11はヒータ線の断線を防ぐ
ために、ヒータの温度により通電量を制御すると
いうコントロールを行つている。一方ヒータの温
度は、ヒータの通電量と放熱量により決められ
る。したがつて、ヒータの温度を一定にコントロ
ールすると、ヒータの放熱条件により、ヒータの
通電量が大きく変わることになる。
Generally, the electric heater 11 is controlled by controlling the amount of current supplied depending on the temperature of the heater in order to prevent disconnection of the heater wire. On the other hand, the temperature of the heater is determined by the amount of current supplied to the heater and the amount of heat released. Therefore, if the temperature of the heater is controlled to be constant, the amount of current applied to the heater will vary greatly depending on the heat dissipation conditions of the heater.

始動時に循環用送風機12を停止して炭素燃料
10を予熱すると、電熱ヒータ11の放熱は輻射
と雰囲気の自然対流によるので、比較的通電量が
少ない段階でヒータの温度が設定値になつてしま
う。炭素燃料10の昇温は主として電熱ヒータ1
1からの輻射によつて行われるために、炭素燃料
10の下層から燃焼可能な温度になる。炭素燃料
10の下層から上層への熱の移動は、熱伝導によ
り行われるが、炭素燃料10内をながれる空気が
ヒータ加熱による自然対流によるものだけでは、
燃焼炉8上部の炭素燃料10が燃焼可能温度にな
るには非常に長時間を要する。したがつて、燃焼
炉8下部の炭素燃料10の温度が燃焼可能な温度
になつたときに、燃焼用空気を燃焼炉8に供給し
て燃焼を行うようにすると、燃焼炉8下部の炭素
燃料10の燃焼ガスが低温の燃焼炉8上部の炭素
燃料10に触れるときに、一酸素炭素が二酸化炭
素に変化する反応が停止し、一酸化炭素が多量に
発生する。特に高温焼結した炭素燃料を燃料とし
て用いた場合には、焼結していない炭素燃料より
も、一酸化炭素の発生量はかなり多くなり、燃焼
炉8が安定するのに要する時間も長くなる。
When the circulation blower 12 is stopped at startup to preheat the carbon fuel 10, the heat dissipation of the electric heater 11 is due to radiation and natural convection of the atmosphere, so the temperature of the heater reaches the set value at a stage where the amount of electricity is relatively small. . The temperature of the carbon fuel 10 is mainly raised by the electric heater 1.
Since this is done by radiation from the carbon fuel 10, the lower layer of the carbon fuel 10 reaches a temperature at which it can be combusted. Heat transfer from the lower layer to the upper layer of the carbon fuel 10 is performed by thermal conduction, but if the air flowing inside the carbon fuel 10 is only due to natural convection due to heater heating,
It takes a very long time for the carbon fuel 10 in the upper part of the combustion furnace 8 to reach a combustible temperature. Therefore, when the temperature of the carbon fuel 10 at the lower part of the combustion furnace 8 reaches a combustible temperature, if combustion air is supplied to the combustion furnace 8 for combustion, the carbon fuel at the lower part of the combustion furnace 8 When the combustion gas 10 comes into contact with the carbon fuel 10 in the upper part of the low-temperature combustion furnace 8, the reaction in which monoxide carbon changes into carbon dioxide stops, and a large amount of carbon monoxide is generated. In particular, when high-temperature sintered carbon fuel is used as a fuel, the amount of carbon monoxide generated is considerably greater than that of unsintered carbon fuel, and the time required for the combustion furnace 8 to stabilize is also longer. .

そこで本発明では、始動時に電熱ヒータ11に
通電するとともに、循環用送風機12を運転す
る。このことにより、電熱ヒータ11に予熱時か
ら強制的に空気を流すことにより、電熱ヒータ1
1の温度を下げるので、無風時に比べて通電量が
多くなる。そして炭素燃料10への熱量の供給
は、電熱ヒータ11からの輻射と、電熱ヒータ1
1により加熱された高温の循環空気の熱伝導によ
つて行われるために、無風時と比べて、高温の循
環空気の熱伝導による分が多く炭素燃料10に供
給されることになる。このために炭素燃料10の
昇温は、無風時に比べて一段と早くなる。そして
炭素燃料10が燃焼可能温度になつたときに燃焼
を開始する。また、炭素燃料10内をヒータ加熱
による高温の空気が流れるために、無風時の自然
対流だけの時とは異なり、燃焼炉8上部の炭素燃
料10への熱の伝導が促進される。
Therefore, in the present invention, at the time of starting, the electric heater 11 is energized and the circulation blower 12 is operated. As a result, by forcing air to flow through the electric heater 11 from the time of preheating, the electric heater 1
Since the temperature of 1 is lowered, the amount of electricity is increased compared to when there is no wind. The amount of heat is supplied to the carbon fuel 10 by radiation from the electric heater 11 and from the electric heater 1.
Since this is carried out by heat conduction of the high temperature circulating air heated by 1, a larger amount of the heat conduction of the high temperature circulating air is supplied to the carbon fuel 10 than when there is no wind. For this reason, the temperature of the carbon fuel 10 rises much faster than when there is no wind. Then, when the carbon fuel 10 reaches a combustible temperature, combustion starts. Furthermore, since high-temperature air heated by the heater flows through the carbon fuel 10, heat conduction to the carbon fuel 10 in the upper part of the combustion furnace 8 is promoted, unlike when there is only natural convection when there is no wind.

また、始動直後は電熱ヒータ11の温度が低い
ために、電熱ヒータ11に電熱ヒータ11の温度
を検出する温度検出部19を設け、温度検出部1
9の出力値が一定になるように、循環用送風機1
2の送風量を増加するように運転すれば、常時電
熱ヒータ11からの輻射量が一定になるために、
さらに効果的な加熱をすることができる。
In addition, since the temperature of the electric heater 11 is low immediately after starting, the electric heater 11 is provided with a temperature detection section 19 that detects the temperature of the electric heater 11.
Circulating blower 1 is installed so that the output value of 9 is constant.
If the operation is performed so as to increase the amount of air blown in step 2, the amount of radiation from the electric heater 11 will always be constant, so
More effective heating can be achieved.

加えて、無風時では予熱時に空気予熱器14の
効果は殆どないが、本発明では燃焼を開始する以
前でも、炭素燃料10内を流れた後の空気が空気
予熱器14で熱交換されて、再び燃焼炉8にフイ
ードバツクされるので、非常に効率的に炭素燃料
10を加熱することができる。
In addition, when there is no wind, the air preheater 14 has almost no effect during preheating, but in the present invention, even before starting combustion, the air that has flowed through the carbon fuel 10 is heat exchanged with the air preheater 14. Since the carbon fuel 10 is fed back to the combustion furnace 8 again, the carbon fuel 10 can be heated very efficiently.

一方、始動時から循環用送風機12を運転する
ことにより、浄化用触媒13にも空気が循環する
ことになるので、浄化用触媒13のヒータの通電
率も増加することができる。これにより、従来の
無風予熱に比べて、浄化用触媒13の昇温を一段
と早くすることができ、浄化用触媒13の触媒能
を十分に発揮することができる。さらに、浄化用
触媒13で加えられた熱も空気予熱器14で熱交
換されて、再び燃焼炉8にフイードバツクされる
ので、非常に効率的に炭素燃料10を加熱するこ
とができる。
On the other hand, by operating the circulation blower 12 from the time of startup, air is also circulated to the purification catalyst 13, so that the energization rate of the heater of the purification catalyst 13 can also be increased. As a result, the temperature of the purification catalyst 13 can be raised much faster than the conventional windless preheating, and the catalytic performance of the purification catalyst 13 can be fully exhibited. Further, since the heat added by the purification catalyst 13 is also exchanged with the air preheater 14 and fed back to the combustion furnace 8, the carbon fuel 10 can be heated very efficiently.

以上のことにより、燃焼炉8上部の炭素燃料1
0が比較的早く昇温し、燃焼開始後に燃焼炉8下
部の炭素燃料10の燃焼ガスが、燃焼炉8上部の
炭素燃料10に触るときに発生する一酸化炭素の
量を大幅に減少することができる。このために短
時間で空気予熱器14に高温の燃焼ガスを供給す
るようになるので、空気予熱器14が能力を十分
に発揮でき、燃焼炉8内の温度が安定し、燃焼が
安定する時間を大幅に短縮することができる。
As a result of the above, the carbon fuel 1 in the upper part of the combustion furnace 8
0 rises in temperature relatively quickly and significantly reduces the amount of carbon monoxide generated when the combustion gas of the carbon fuel 10 in the lower part of the combustion furnace 8 touches the carbon fuel 10 in the upper part of the combustion furnace 8 after combustion starts. I can do it. For this reason, high-temperature combustion gas is supplied to the air preheater 14 in a short time, so the air preheater 14 can fully demonstrate its capacity, the temperature inside the combustion furnace 8 is stabilized, and combustion is stabilized. can be significantly shortened.

発明の効果 本発明は、二酸化炭素発生装置に炭素燃料を加
熱するヒータを設け、始動時にヒータに通電する
とともに、循環用送風機を運転することにより、
空気予熱器が能力を十分に発揮でき、燃焼炉内の
温度が安定し、燃焼が安定する時間を大幅に短縮
することができる。
Effects of the Invention The present invention provides a carbon dioxide generator with a heater that heats carbon fuel, energizes the heater at the time of startup, and operates a circulation blower.
The air preheater can fully demonstrate its capacity, the temperature inside the combustion furnace is stabilized, and the time required for combustion to become stable can be significantly shortened.

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

第1図は本発明の一実施例の生鮮物貯蔵装置の
概略図、第2図は従来の生鮮物貯蔵装置の概略図
である。 7……二酸化炭素発生装置、8……燃焼炉、1
1……電熱ヒータ、12……循環用送風機、14
……空気予熱器。
FIG. 1 is a schematic diagram of a fresh produce storage device according to an embodiment of the present invention, and FIG. 2 is a schematic diagram of a conventional fresh produce storage device. 7... Carbon dioxide generator, 8... Combustion furnace, 1
1... Electric heater, 12... Circulation blower, 14
...Air preheater.

Claims (1)

【特許請求の範囲】[Claims] 1 冷蔵庫と、燃焼部内部に設けた炭素燃料を燃
焼することにより発生した二酸化炭素を前記冷蔵
庫に供給する二酸化炭素発生装置と、燃焼用空気
として前記冷蔵庫内の空気を循環して前記二酸化
炭素発生装置に供給する循環用送風機と、前記二
酸化炭素発生装置の下流に設けた浄化用触媒と、
前記浄化用触媒の下流に設けた前記二酸化炭素発
生装置の排ガスと熱交換して燃焼用空気を予熱す
る空気予熱器を有し、前記二酸化炭素発生装置内
に前記炭素燃料を加熱するヒータを設け、始動時
に前記ヒータに通電し、前記炭素燃料が着火温度
に達する前に前記循環用送風機を運転することを
特徴とする生鮮物貯蔵装置。
1. A refrigerator, a carbon dioxide generating device that supplies carbon dioxide generated by burning carbon fuel provided inside a combustion section to the refrigerator, and generates the carbon dioxide by circulating air in the refrigerator as combustion air. a circulation blower that supplies the device; a purification catalyst provided downstream of the carbon dioxide generator;
an air preheater that preheats combustion air by exchanging heat with the exhaust gas of the carbon dioxide generator provided downstream of the purification catalyst; and a heater that heats the carbon fuel in the carbon dioxide generator. . A fresh produce storage device, characterized in that the heater is energized at startup, and the circulation blower is operated before the carbon fuel reaches an ignition temperature.
JP61264593A 1986-10-31 1986-11-06 Apparatus for storing perishables Granted JPS63116623A (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
JP61264593A JPS63116623A (en) 1986-11-06 1986-11-06 Apparatus for storing perishables
US07/113,766 US4754611A (en) 1986-10-31 1987-10-28 Controlled atmosphere storage system
KR1019870012146A KR900003723B1 (en) 1986-10-31 1987-10-30 Apparatus for preservation of fishes

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61264593A JPS63116623A (en) 1986-11-06 1986-11-06 Apparatus for storing perishables

Publications (2)

Publication Number Publication Date
JPS63116623A JPS63116623A (en) 1988-05-20
JPH0571212B2 true JPH0571212B2 (en) 1993-10-06

Family

ID=17405456

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61264593A Granted JPS63116623A (en) 1986-10-31 1986-11-06 Apparatus for storing perishables

Country Status (1)

Country Link
JP (1) JPS63116623A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012246795A (en) * 2011-05-25 2012-12-13 Toyota Motor Corp Power supply control device for vehicle

Also Published As

Publication number Publication date
JPS63116623A (en) 1988-05-20

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