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JPH0348774B2 - - Google Patents
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JPH0348774B2 - - Google Patents

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Publication number
JPH0348774B2
JPH0348774B2 JP26131086A JP26131086A JPH0348774B2 JP H0348774 B2 JPH0348774 B2 JP H0348774B2 JP 26131086 A JP26131086 A JP 26131086A JP 26131086 A JP26131086 A JP 26131086A JP H0348774 B2 JPH0348774 B2 JP H0348774B2
Authority
JP
Japan
Prior art keywords
refrigerator
carbon dioxide
combustion
scrubber
air
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
JP26131086A
Other languages
Japanese (ja)
Other versions
JPS63112922A (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 JP61261310A priority Critical patent/JPS63112922A/en
Priority to US07/113,766 priority patent/US4754611A/en
Priority to KR1019870012146A priority patent/KR900003723B1/en
Publication of JPS63112922A publication Critical patent/JPS63112922A/en
Publication of JPH0348774B2 publication Critical patent/JPH0348774B2/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
1674−7 P191)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).
1674-7 P191), 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 a 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。しかし冷蔵庫
内の酸素濃度が低い状態からの再着火を行う場
合、酸素濃度が正常な場合と同程度の燃焼量で燃
焼を行おうとすると、循環空気量が非常に大きく
なる。したがつて、せつかく予熱により炭素燃料
を燃焼可能な温度まで加熱しても、循環空気によ
り炭素燃料が冷却されて燃焼を開始することがで
きないという問題が生じてきた。
Therefore, if carbon fuel is used as fuel, the problem of water vapor generation can be avoided. However, when re-igniting the refrigerator from a state where the oxygen concentration is low, the amount of circulating air becomes extremely large if you try to perform combustion with the same amount of combustion as when the oxygen concentration is normal. Therefore, even if the carbon fuel is heated to a combustible temperature through preheating, a problem has arisen in that the carbon fuel is cooled by the circulating air and cannot start combustion.

本発明は簡単な構成で、冷蔵庫内の酸素濃度が
低くても再着火することができる生鮮物貯蔵装置
を提供するものである。
The present invention provides a fresh food storage device that has a simple configuration and can re-ignite even if the oxygen concentration inside the refrigerator is low.

問題点を解決するための手段 そこで、本発明は、冷蔵庫と二酸化炭素発生装
置を接続し、二酸化炭素発生装置の下流に浄化用
触媒、空気予熱器、冷却器、循環用送風機、スク
ラバの順で配置し、スクラバと冷蔵庫を接続し、
冷蔵庫と二酸化炭素発生装置間の経路に吸入口を
設け、循環用送風機とスクラバ間に排出口を設
け、さらに冷蔵庫内に酸素濃度検出器を設け、冷
蔵庫の酸素濃度が所定値以下であれば、始動時に
冷蔵庫と二酸化炭素発生装置間の経路に設けた開
閉部と、冷蔵庫とスクラバ間の経路に設けた開閉
部を閉じ、吸入口と排出口を開けて燃焼を行い、
燃焼部の温度が所定の温度になつたときに、吸入
口と排出口を閉じ、前記2つの開閉部を開けるも
のである。
Means for Solving the Problems Therefore, the present invention connects a refrigerator and a carbon dioxide generator, and installs a purification catalyst, an air preheater, a cooler, a circulating blower, and a scrubber in the order downstream of the carbon dioxide generator. Place and connect the scrubber and refrigerator,
An inlet is provided in the path between the refrigerator and the carbon dioxide generator, an outlet is provided between the circulation blower and the scrubber, and an oxygen concentration detector is installed inside the refrigerator.If the oxygen concentration in the refrigerator is below a predetermined value, At startup, the opening/closing part installed in the path between the refrigerator and the carbon dioxide generator and the opening/closing part installed in the path between the refrigerator and the scrubber are closed, and the intake and exhaust ports are opened to perform combustion.
When the temperature of the combustion section reaches a predetermined temperature, the inlet and outlet are closed and the two opening/closing sections are opened.

作 用 この技術的手段による作用は次のようになる。Effect The effect of this technical means is as follows.

冷蔵庫内の酸素濃度が低い状態から生鮮物貯蔵
装置の運転を行う場合には、冷蔵庫内に設けた酸
素濃度検出器からの信号により、始動時に冷蔵庫
と二酸化炭素発生装置間の経路に設けた開閉部
と、冷蔵庫のスクラバ間の経路に設けた開閉部を
閉じ、吸入口と排出口を開けて燃焼を行う。この
時、燃焼に用いられる空気は大気中の酸素濃度が
21%のものであるので、燃焼用空気が予熱されて
高温の炭素燃料に接触するや否や燃焼を開始す
る。燃焼炉内の温度や燃料の温度が十分に上昇し
てから、吸入口と排出口を閉じ、前記2つの開閉
部を開けることにより、冷蔵庫内の低酸素濃度の
空気を燃焼炉に供給する。ここで燃焼炉および炭
素燃料の温度は、酸素濃度21%燃焼により十分に
高温になつているので、燃焼用空気による炭素燃
料の温度低下を最小限に防ぐことができ、低酸素
濃度下での再着火を行うことができるものであ
る。
When operating a perishables storage device in a state where the oxygen concentration inside the refrigerator is low, a signal from an oxygen concentration detector installed inside the refrigerator is used to open and close the path between the refrigerator and the carbon dioxide generator at the time of startup. Close the opening and closing section provided in the path between the refrigerator scrubber and the refrigerator scrubber, and open the inlet and outlet to perform combustion. At this time, the air used for combustion has a concentration of oxygen in the atmosphere.
21%, combustion begins as soon as the combustion air is preheated and contacts the hot carbon fuel. After the temperature inside the combustion furnace and the temperature of the fuel have risen sufficiently, the intake port and the exhaust port are closed and the two opening/closing portions are opened, thereby supplying air with a low oxygen concentration inside the refrigerator to the combustion furnace. Here, the temperature of the combustion furnace and the carbon fuel are sufficiently high due to combustion with an oxygen concentration of 21%, so it is possible to minimize the temperature drop of the carbon fuel due to the combustion air, and it is possible to prevent the temperature of the carbon fuel from decreasing due to combustion air. It can be re-ignited.

実施例 以下、本発明の一実施例を添付図面に基づいて
説明する。
Embodiment Hereinafter, an embodiment of the present invention will be described based on 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に通電し、炭素燃料10が燃焼するのに十分
な温度まで加熱した時点で、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はすでに十分に加熱されているので、空
気が炭素燃料10に接触するや否や燃焼を開始す
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 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 when the carbon fuel 10 is heated to a temperature sufficient for combustion, the circulation blower 12 is operated to supply combustion air to the combustion furnace 8. Since the carbon fuel 10 is already sufficiently heated, combustion begins as soon as air contacts the carbon fuel 10. The amount of combustion at this time is the surface area of carbon fuel 10,
It is determined by 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
炭素を含む高温の排ガスは、浄化用触媒13で浄
化され、空気予熱器14に供給される。この空気
予熱器14において、排ガスは燃焼用空気と熱交
換され、燃焼用空気を予熱したのちに冷却器15
へ供給される。そして冷却器15で冷却された排
ガスはスクラバ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。
High-temperature exhaust gas containing a large amount of carbon dioxide generated by the carbon dioxide generator 7 is purified by a purification catalyst 13 and supplied to an air preheater 14 . In this air preheater 14, the exhaust gas is heat exchanged with the combustion air, and after preheating the combustion air, the exhaust gas is heated in the cooler 15.
supplied to The exhaust gas cooled by the cooler 15 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.

スクラバ16は、たとえば内部に活性炭などを
充填した二酸化炭素吸着層と吸着した二酸化炭素
を脱着する再生装置とバイパス経路とを有するも
のである。冷蔵庫17に設けたガスセンサ(図示
せず)からの信号により、冷蔵庫17内の二酸化
炭素濃度が設定値に達したことを検出すると、ス
クラバ16を運転し、設定値を保つように燃焼に
より発生した過剰な二酸化炭素を吸着し続ける。
冷蔵庫17内の酸素濃度検出器21からの信号に
より、冷蔵庫17内の酸素濃度が設定値に達した
ことを検出すると、二酸化炭素発生装置7、循環
用送風機12、スクラバ16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。
The scrubber 16 has, for example, a carbon dioxide adsorption layer filled with activated carbon or the like, a regenerator for desorbing the adsorbed carbon dioxide, and a bypass path. When it is detected by a signal from a gas sensor (not shown) provided in the refrigerator 17 that the carbon dioxide concentration in the refrigerator 17 has reached the set value, the scrubber 16 is operated to maintain the set value. Continues to adsorb excess carbon dioxide.
When it is detected by the signal from the oxygen concentration detector 21 in the refrigerator 17 that the oxygen concentration in the refrigerator 17 has reached a set value, the carbon dioxide generator 7, circulation blower 12, and scrubber 16 are 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.

炭素燃料の燃焼というものは、炭素燃料の表面
に酸素が接触すると、炭素燃料の表面で、炭素原
子が酸素原子と結び付いて一酸化炭素を発生する
反応が起こる。続いて炭素燃料の表面近傍で、一
酸化炭素と酸素原子が結び付いて二酸化炭素を発
生するという反応が気相で起こる。したがつて炭
素燃料の燃焼は、炭素燃料の表面積と酸素濃度に
依存するところが大きい。このために冷蔵庫17
内の空気を循環して燃焼する場合、燃焼の経過と
ともに冷蔵庫17内の酸素濃度が低下していくの
で、燃焼の経過とともに燃料消費量が低下する。
In combustion of carbon fuel, when oxygen comes into contact with the surface of the carbon fuel, a reaction occurs where carbon atoms combine with oxygen atoms to generate carbon monoxide. Next, near the surface of the carbon fuel, a reaction occurs in the gas phase in which carbon monoxide and oxygen atoms combine to generate carbon dioxide. Therefore, the combustion of carbon fuel largely depends on the surface area and oxygen concentration of the carbon fuel. For this reason refrigerator 17
When the air inside the refrigerator 17 is circulated for combustion, the oxygen concentration inside the refrigerator 17 decreases as the combustion progresses, so the amount of fuel consumed decreases as the combustion progresses.

そこで、以下に述べる方法で燃料消費量の減少
を防いでいる。すなわち、冷蔵庫17内の酸素濃
度の減少に合せて、炭素燃料10に供給する空気
量を増加すると、炭素燃料10に供給される酸素
量が増え、燃焼に使用できる酸素量が増加するこ
とになるので、燃料消費量が増加する。
Therefore, the method described below is used to prevent a decrease in fuel consumption. That is, if the amount of air supplied to the carbon fuel 10 is increased in accordance with the decrease in the oxygen concentration in the refrigerator 17, the amount of oxygen supplied to the carbon fuel 10 will increase, and the amount of oxygen that can be used for combustion will increase. Therefore, fuel consumption increases.

冷蔵庫17内の酸素濃度があまり小さくないと
きは、増加する空気量がそれほど多くないので問
題がないが、冷蔵庫17内の酸素濃度が小さくな
ると増加する空気量が非常に多くなる。したがつ
て、冷蔵庫17内酸素濃度が低い状態から、燃焼
炉8を再着火し、生鮮物貯蔵装置を運転する場合
には、予熱時にせつかく炭素燃料10を燃焼可能
な温度まで昇温しても、始動時に燃焼炉8に流入
する空気量が多いために、送風開始とともに炭素
燃料10の温度が低下するために燃焼を開始しな
い可能性がある。
When the oxygen concentration inside the refrigerator 17 is not very small, there is no problem because the increased amount of air is not so large, but when the oxygen concentration inside the refrigerator 17 becomes small, the increased amount of air becomes very large. Therefore, when re-igniting the combustion furnace 8 and operating the perishables storage device from a state where the oxygen concentration inside the refrigerator 17 is low, it is necessary to raise the temperature of the carbon fuel 10 to a temperature at which it can be combusted during preheating. However, since the amount of air flowing into the combustion furnace 8 at the time of startup is large, the temperature of the carbon fuel 10 decreases with the start of air blowing, so there is a possibility that combustion will not start.

そこで本発明では、冷蔵庫17と二酸化炭素発
生装置7を接続し、二酸化炭素発生装置7の下流
に浄化用触媒13、空気予熱器14、冷却器1
5、循環用送風機12、スクラバ16の順で配置
し、スクラバ16と冷蔵庫17を接続し、冷蔵庫
17と二酸化炭素発生装置7間の経路に吸入口1
9を設け、循環用送風機12とスクラバ16間に
排出口20を設け、さらに冷蔵庫17内に酸素濃
度検出器21を設け、冷蔵庫17の酸素濃度が設
定値以下であれば、始動時に冷蔵庫17と二酸化
炭素発生装置7間の経路に設けた開閉部22と、
冷蔵庫17とスクラバ16間の経路に設けた開閉
部23を閉じ、吸入口19と排出口20を開けて
燃焼を行い、燃焼炉8の温度が所定の温度になつ
たときに、吸入口19と排出口20を閉じ、前記
2つの開閉部22,23を開けるようにしてあ
る。
Therefore, in the present invention, the refrigerator 17 and the carbon dioxide generator 7 are connected, and the purification catalyst 13, the air preheater 14, and the cooler 1 are downstream of the carbon dioxide generator 7.
5. Arrange the circulation blower 12 and the scrubber 16 in this order, connect the scrubber 16 and the refrigerator 17, and install the inlet 1 in the path between the refrigerator 17 and the carbon dioxide generator 7.
9, a discharge port 20 is provided between the circulation blower 12 and the scrubber 16, and an oxygen concentration detector 21 is provided in the refrigerator 17, so that if the oxygen concentration in the refrigerator 17 is below the set value, the refrigerator 17 and An opening/closing part 22 provided in the path between the carbon dioxide generators 7;
The opening/closing part 23 provided in the path between the refrigerator 17 and the scrubber 16 is closed, the inlet 19 and the outlet 20 are opened to perform combustion, and when the temperature of the combustion furnace 8 reaches a predetermined temperature, the inlet 19 and the outlet 20 are opened. The discharge port 20 is closed and the two opening/closing parts 22 and 23 are opened.

したがつて、冷蔵庫17内の酸素濃度が低い状
態から生鮮物貯蔵装置の運転を行う場合には、冷
蔵庫17内に設けた酸素濃度検出器21からの信
号により、始動時に冷蔵庫17と二酸化炭素発生
装置7間の経路に設けた開閉部22と、冷蔵庫と
スクラバ間の経路に設けた開閉部23を閉じ、吸
入口19に設けた吸入弁25と排出口20に設け
た排出弁24を開ける。このことにより、循環用
送風機12は吸入口19より大気から正常空気を
取り込んで二酸化炭素発生装置7に供給し、燃焼
炉8で発生した燃焼ガスを排出口20から大気に
放出する。この時、燃焼に用いられる空気は大気
中の酸素濃度が21%のものであるので、燃焼用空
気が予熱されて高温の炭素燃料10に接触するや
否や燃焼を開始する。また冷蔵庫17は2つの開
閉部22,23を閉じることにより循環経路と遮
断されているので、冷蔵庫17内に大気から酸素
濃度21%の正常空気が侵入することもなく、せつ
かく酸素濃度を下げた冷蔵庫17内の空気組成を
変えることなく、大気の正常空気を用いて燃焼す
ることができる。
Therefore, when operating the perishables storage device in a state where the oxygen concentration inside the refrigerator 17 is low, the signal from the oxygen concentration detector 21 provided inside the refrigerator 17 is used to detect whether the refrigerator 17 and carbon dioxide are being generated at the time of startup. The opening/closing part 22 provided in the path between the devices 7 and the opening/closing part 23 provided in the path between the refrigerator and the scrubber are closed, and the suction valve 25 provided in the suction port 19 and the discharge valve 24 provided in the discharge port 20 are opened. As a result, the circulation blower 12 takes in normal air from the atmosphere through the intake port 19 and supplies it to the carbon dioxide generator 7, and discharges the combustion gas generated in the combustion furnace 8 to the atmosphere through the exhaust port 20. At this time, since the air used for combustion has an atmospheric oxygen concentration of 21%, combustion starts as soon as the combustion air is preheated and comes into contact with the high-temperature carbon fuel 10. In addition, since the refrigerator 17 is isolated from the circulation path by closing the two opening/closing parts 22 and 23, normal air with an oxygen concentration of 21% does not enter the refrigerator 17 from the atmosphere, reducing the oxygen concentration. Combustion can be performed using normal atmospheric air without changing the air composition inside the refrigerator 17.

また、排出口20は冷却器15より下流に設け
ることにより、排出口20に設けてある排出弁2
4は耐熱性の材料を用いる必要がなく、非常に安
価な弁を用いることができる。さらに排出口20
はスクラバ16より上流にあるので、燃焼開始初
期に断熱材に含まれていた水分が蒸発することに
より発生する水蒸気は、スクラバ16に送られず
に大気へ放出される。このためにスクラバ16に
充填されている活性炭は水分被毒を受けないの
で、循環サイクルの運転モードに入つても、スク
ラバ16の能力が低下するということはない。
Further, by providing the discharge port 20 downstream from the cooler 15, the discharge valve 2 provided at the discharge port 20
4 does not require the use of heat-resistant materials, and a very inexpensive valve can be used. Furthermore, the discharge port 20
is located upstream of the scrubber 16, so water vapor generated by evaporation of moisture contained in the heat insulating material at the beginning of combustion is not sent to the scrubber 16 but is released into the atmosphere. For this reason, the activated carbon filled in the scrubber 16 is not poisoned by water, so the performance of the scrubber 16 will not be reduced even if it enters the circulation cycle operation mode.

加えて、吸入口19は空気予熱器14より上流
に設けることにより、空気予熱器14の空運転を
防ぐことができ、空気予熱器14の寿命を向上す
ることができる。
In addition, by providing the suction port 19 upstream of the air preheater 14, the air preheater 14 can be prevented from running idle, and the life of the air preheater 14 can be improved.

そして燃焼炉8内の温度や炭素燃料10の温度
が十分に上昇してから、吸入口19の吸入弁25
と排出口20の排出弁24を閉じ、循環経路に設
けた2つの開閉部22,23を開けることによ
り、今度は冷蔵庫17内の低酸素濃度の空気を燃
焼炉8に供給する。ここで燃焼炉8および炭素燃
料10の温度は、大気の酸素濃度21%の空気を用
いた燃焼により十分に高温になつているので、燃
焼用空気による炭素燃料10の温度低下を最小限
に防ぐことができ、低酸素濃度下での再着火を行
うことができる。
After the temperature inside the combustion furnace 8 and the temperature of the carbon fuel 10 rise sufficiently, the intake valve 25 of the intake port 19
By closing the discharge valve 24 of the discharge port 20 and opening the two opening/closing parts 22 and 23 provided in the circulation path, the low oxygen concentration air in the refrigerator 17 is then supplied to the combustion furnace 8. Here, the temperatures of the combustion furnace 8 and the carbon fuel 10 are sufficiently high due to combustion using air with an atmospheric oxygen concentration of 21%, so that the temperature drop of the carbon fuel 10 due to the combustion air is minimized. It is possible to carry out re-ignition under low oxygen concentration.

これまでの説明は循環経路の切り替えを燃焼炉
8の温度が所定の温度になつたときに行うという
ことで述べてきたが、循環経路の切り替えを所定
時間経過後すなわち燃焼炉8での燃焼が安定する
のに必要な時間経過後に行つても、同様の効果が
ある。
The explanation so far has been that the circulation path is switched when the temperature of the combustion furnace 8 reaches a predetermined temperature, but the circulation path is switched after a predetermined period of time has elapsed, that is, the combustion in the combustion furnace 8 is started. The same effect can be obtained even if the treatment is performed after the time required for stabilization has elapsed.

発明の効果 本発明は、冷蔵庫と二酸化炭素発生装置を接続
し、二酸化炭素発生装置の下流に浄化用触媒、空
気予熱器、冷却器、循環用送風機、スクラバの順
で配置し、スクラバと冷蔵庫を接続し、冷蔵庫と
二酸化炭素発生装置間の経路に吸入口を設け、循
環用送風機とスクラバ間に排出口を設け、さらに
冷蔵庫内に酸素濃度検出器を設け、冷蔵庫の酸素
濃度が設定値以下であれば、始動時に冷蔵庫と二
酸化炭素発生装置間の経路に設けた開閉部と、冷
蔵庫とスクラバ間の経路に設けた開閉部を閉じ、
吸入口と排出口を開けて燃焼を行い、燃焼部の温
度が所定の温度になつたときに、吸入口と排出口
を閉じ、前記2つの開閉部を開けることにより、
冷蔵庫内の酸素濃度が抵くても再着火することが
できるものである。
Effects of the Invention The present invention connects a refrigerator and a carbon dioxide generator, and arranges a purification catalyst, an air preheater, a cooler, a circulation blower, and a scrubber downstream of the carbon dioxide generator in this order, and connects the scrubber and the refrigerator. An inlet is installed in the path between the refrigerator and the carbon dioxide generator, an outlet is installed between the circulation blower and the scrubber, and an oxygen concentration detector is installed inside the refrigerator to detect when the oxygen concentration in the refrigerator is below the set value. If there is, close the opening/closing part installed in the path between the refrigerator and the carbon dioxide generator and the opening/closing part installed in the path between the refrigerator and the scrubber at startup.
By opening the inlet and outlet to perform combustion, and when the temperature of the combustion part reaches a predetermined temperature, closing the inlet and outlet and opening the two opening/closing parts,
Even if the oxygen concentration inside the refrigerator is low, it can be re-ignited.

【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図は従来例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、12……循環用送
風機、13……浄化用触媒、14……空気予熱
器、15……冷却器、16……スクラバ、17…
…冷蔵庫、19……吸入口、20……排出口、2
1……酸素濃度検出器。
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, 12... Circulating blower, 13... Purification catalyst, 14... Air preheater, 15... Cooler, 16... Scrubber, 17...
... Refrigerator, 19... Inlet, 20... Outlet, 2
1...Oxygen concentration detector.

Claims (1)

【特許請求の範囲】[Claims] 1 冷蔵庫と、炭素燃料を内部に設けた燃焼部で
燃焼することにより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を接続し、前記二酸化
炭素発生装置の下流に浄化用触媒を設け、前記浄
化用触媒の下流に前記二酸化炭素発生装置からの
排ガスと燃焼用空気を熱交換する空気予熱器を設
け、前記空気予熱器の下流に冷却器を設け、前記
冷却器の下流に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
る循環用送風機を設け、前記循環用送風機の下流
に前記冷蔵庫の二酸化炭素濃度を設定値に保つス
クラバを設け、前記スクラバと前記冷蔵庫を接続
し、前記冷蔵庫と前記二酸化炭素発生装置間の経
路に吸入口を設け、前記循環用送風機と前記スク
ラバ間に排出口を設け、さらに前記冷蔵庫内に酸
素濃度検出器を設け、前記冷蔵庫の酸素濃度が所
定値以下であれば、始動時に前記冷蔵庫と二酸化
炭素発生装置間の経路に設けた開閉部と、前記冷
蔵庫と前記スクラバ間の経路に設けた開閉部を閉
じ、前記吸入口と前記排出口を開けて燃焼を行
い、前記燃焼部の温度が所定の温度になつたとき
もしくは所定時間経過後に、前記吸入口と前記排
出口を閉じ、前記2つの開閉部を開けることを特
徴とする生鮮物貯蔵装置。
1. A refrigerator is connected to a carbon dioxide generator that supplies carbon dioxide to the refrigerator by burning carbon fuel in a combustion section provided inside, and a purification catalyst is provided downstream of the carbon dioxide generator, and the purification An air preheater for exchanging heat between exhaust gas from the carbon dioxide generating device and combustion air is provided downstream of the carbon dioxide generator, a cooler is provided downstream of the air preheater, and downstream of the cooler the air is heated as combustion air. A circulation blower is provided to circulate air in the refrigerator and supply it to the carbon dioxide generating device, and a scrubber is provided downstream of the circulation blower to keep the carbon dioxide concentration in the refrigerator at a set value, and the scrubber and the refrigerator are connected to each other. an inlet is provided in the path between the refrigerator and the carbon dioxide generator, an outlet is provided between the circulation blower and the scrubber, an oxygen concentration detector is provided in the refrigerator, and oxygen concentration in the refrigerator is If the concentration is below a predetermined value, at startup, the opening/closing part provided in the path between the refrigerator and the carbon dioxide generator and the opening/closing part provided in the path between the refrigerator and the scrubber are closed, and the opening/closing part provided in the path between the refrigerator and the scrubber is closed. The fresh food is characterized in that combustion is performed with an outlet open, and when the temperature of the combustion section reaches a predetermined temperature or after a predetermined time has elapsed, the intake port and the discharge port are closed, and the two opening/closing sections are opened. Object storage device.
JP61261310A 1986-10-31 1986-10-31 perishable storage equipment Granted JPS63112922A (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
JP61261310A JPS63112922A (en) 1986-10-31 1986-10-31 perishable storage equipment
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
JP61261310A JPS63112922A (en) 1986-10-31 1986-10-31 perishable storage equipment

Publications (2)

Publication Number Publication Date
JPS63112922A JPS63112922A (en) 1988-05-18
JPH0348774B2 true JPH0348774B2 (en) 1991-07-25

Family

ID=17360015

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61261310A Granted JPS63112922A (en) 1986-10-31 1986-10-31 perishable storage equipment

Country Status (1)

Country Link
JP (1) JPS63112922A (en)

Also Published As

Publication number Publication date
JPS63112922A (en) 1988-05-18

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