JPH02203717A - Apparatus for storing perishables - Google Patents

Apparatus for storing perishables

Info

Publication number
JPH02203717A
JPH02203717A JP1025045A JP2504589A JPH02203717A JP H02203717 A JPH02203717 A JP H02203717A JP 1025045 A JP1025045 A JP 1025045A JP 2504589 A JP2504589 A JP 2504589A JP H02203717 A JPH02203717 A JP H02203717A
Authority
JP
Japan
Prior art keywords
combustion
storage
carbon dioxide
gas
preheater
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
JP1025045A
Other languages
Japanese (ja)
Inventor
Jun Takeda
純 武田
Takeshi Shimizu
武 清水
Junichi Nagai
純一 永井
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
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 filed Critical Matsushita Refrigeration Co
Priority to JP1025045A priority Critical patent/JPH02203717A/en
Publication of JPH02203717A publication Critical patent/JPH02203717A/en
Pending legal-status Critical Current

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

Abstract

PURPOSE:To shorten the time of electrical conduction to heated parts, such as heater, required for combustion and reduce power consumption by providing a preheater for preheating air fed to combustion of a fuel in a combustion furnace at a specific position. CONSTITUTION:A preheater 12' for preheating air fed to combustion of a fuel 19 in a combustion furnace 12 is provided so as to contact the upper part of the combustion furnace. Air circulated from a storage chamber 1 is subjected to heat exchange with high-temperature combustion gases and preheated in the preheater and simultaneously preheated with heat conduction from the combustion furnace. Thereby, the time of electrical conduction to an ignition heater 21 used for combustion may be short.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、野菜、果実等の生鮮物を生産地あるいは流通
段階等において長期間の貯蔵を可能とする生鮮物貯蔵装
置に関する。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a fresh produce storage device that allows fresh produce such as vegetables and fruits to be stored for a long period of time at the production site or at the distribution stage.

従来の技術 生鮮物を貯蔵する手段としては冷蔵貯蔵が一般的である
が、これに加えてより長期にわたる貯蔵手段として、貯
蔵庫内の空気成分を変える貯蔵がある。つまり、貯蔵庫
内の酸素(o2)濃度を減少せしめ、炭酸ガス(Co2
)濃度を増加せしめることで生鮮物の呼吸作用を抑制し
、また微生物による変質2分解や酸化等の化学反応も防
止することができることが知られている。
BACKGROUND OF THE INVENTION Refrigerated storage is a common means of storing perishables, but in addition to this, a longer term storage method involves changing the air composition within the storage room. In other words, the concentration of oxygen (O2) in the storage chamber is reduced, and the concentration of carbon dioxide (Co2) is reduced.
) It is known that by increasing the concentration, it is possible to suppress the respiration of fresh foods and also to prevent chemical reactions such as alteration and decomposition by microorganisms and oxidation.

以下図面を参照しながら、上述した従来の生鮮物貯蔵装
置の、−例について説明する。
An example of the above-mentioned conventional fresh food storage device will be described below with reference to the drawings.

第3図は従来の生鮮物貯蔵装置の系統図を示すものであ
る。1′は貯蔵庫であり、蒸発器2′、コンデンシング
ユニット3′から成る冷却袋@4′を設けている。6′
はプロパンガスボンベであシ、炭酸ガス発生装置6′で
前記貯蔵庫1′より導入管7′で導入した空気を供して
酸化触媒を媒体として燃焼させC3H8+502−+3
co2−1−4H20+531 ’do反応で発生した
燃焼排ガスすなわち炭酸ガス(CO2)過剰の炭酸ガス
(CO2)を吸着した後、排出管11′で貯蔵庫1′に
戻している。12′はガスモニタ−であり貯蔵庫1′内
のガス濃度を検知して炭酸ガス発生装置8′及び炭酸ガ
ス吸着装置9′を適時コントロールしている。
FIG. 3 shows a system diagram of a conventional fresh food storage device. Reference numeral 1' denotes a storage, and a cooling bag @4' consisting of an evaporator 2' and a condensing unit 3' is provided. 6'
is a propane gas cylinder, and the carbon dioxide gas generator 6' is supplied with air introduced from the storage 1' through the inlet pipe 7', and the oxidation catalyst is used as a medium to combust C3H8+502-+3.
CO2-1-4H20+531 ' After adsorbing excess carbon dioxide gas (CO2), that is, combustion exhaust gas generated in the do reaction, it is returned to the storage 1' through a discharge pipe 11'. A gas monitor 12' detects the gas concentration in the storage 1' and controls the carbon dioxide gas generator 8' and the carbon dioxide adsorption device 9' in a timely manner.

発明が解決しようとする課題 しかしながら上記のような構成では、炭酸ガス発生装置
6′でプロパンガスを貯蔵庫1′よシ導入した空気で燃
焼させるために酸化触媒を電気ヒータで常時加熱する必
要があった。そのため電気代が高く、また電気ヒータを
常時通電するため、耐久性に問題があった。
Problems to be Solved by the Invention However, with the above configuration, it is necessary to constantly heat the oxidation catalyst with an electric heater in order to burn propane gas in the carbon dioxide generator 6' with air introduced from the storage 1'. Ta. As a result, electricity costs were high, and since the electric heater was constantly energized, there were problems with durability.

本発明は上記課題に鑑み、燃焼の省電力化とヒータ等の
加熱部品の耐久性の向上を図った生鮮物貯蔵装置を提供
するものである。
In view of the above-mentioned problems, the present invention provides a fresh produce storage device that saves power during combustion and improves the durability of heating components such as heaters.

課題を解決するための手段 上記問題点を解決するため本発明の生鮮物貯蔵装置は、
燃焼炉の燃料の燃焼に供する空気を予熱する予熱器を備
え、予熱器と燃焼炉が少なくとも一面を接して設けたも
のである。
Means for Solving the Problems In order to solve the above-mentioned problems, the perishables storage device of the present invention has the following features:
The combustion furnace is equipped with a preheater for preheating the air used for combustion of fuel in the combustion furnace, and the preheater and the combustion furnace are provided in contact with each other on at least one side.

作  用 本発明は上記した構成によって貯蔵庫より循環した温度
の低い空気を予熱器で予熱し、かつ、予熱器と燃焼炉が
少なくとも一面を接して設けているため、燃焼炉からの
熱伝導による受熱によって予熱器の予熱効果を高めて、
燃焼炉の燃料の燃焼に供するものであるから燃焼に必要
なヒータ等の加熱部品の通電時間を短かくできるため、
省電力化と、耐久性の向上が図れることとなる。
Effect The present invention has the above-described configuration in which the low-temperature air circulated from the storage is preheated by the preheater, and the preheater and the combustion furnace are provided in contact with each other on at least one side, so that the heat is not received by heat conduction from the combustion furnace. By increasing the preheating effect of the preheater,
Since it is used for burning fuel in a combustion furnace, it is possible to shorten the energization time of heating parts such as heaters necessary for combustion.
This results in power savings and improved durability.

実施例 以下本発明の一実施例の生鮮物貯蔵装置について図面を
参照しながら説明する。
EXAMPLE Hereinafter, a fresh food storage apparatus according to an embodiment of the present invention will be described with reference to the drawings.

第1図は、本発明の実施例における生鮮物貯蔵装置の構
成を示すものである。
FIG. 1 shows the configuration of a fresh produce storage device in an embodiment of the present invention.

第1図において1は生鮮物を貯蔵するプレ7アブ冷蔵庫
の如き貯蔵庫であり、圧縮機2、慶縮器3、蒸発器4、
送風機5.6より成る冷却装置7を上部に載架している
。前記貯蔵庫1には、庫内に炭酸ガス(CO2)を充填
するための炭酸ガス発生装置8と、燃焼ガスの中の過剰
な炭酸ガス(CO2)を吸着して除去する炭酸ガス吸着
装置9が接続されている。炭酸ガス発生装置8は、貯蔵
庫1内の空気を導入する導入管1oと、ここで発生した
燃焼ガスを炭酸ガス吸着装置9に導く連結管11との間
に配置され、燃焼炉12及び燃焼炉12上部に接して設
けた燃焼に供する空気を燃焼ガスと熱交換し予熱する予
熱器12′と燃焼ガスの冷却器13で構成されている。
In Fig. 1, 1 is a storage such as a pre-7 refrigerator for storing perishables, and includes a compressor 2, a condenser 3, an evaporator 4,
A cooling device 7 consisting of a blower 5.6 is mounted on the top. The storage 1 includes a carbon dioxide gas generator 8 for filling the interior with carbon dioxide (CO2), and a carbon dioxide adsorption device 9 for adsorbing and removing excess carbon dioxide (CO2) from combustion gas. It is connected. The carbon dioxide gas generator 8 is disposed between an introduction pipe 1o that introduces air in the storage 1 and a connecting pipe 11 that leads the combustion gas generated here to the carbon dioxide adsorption device 9, and is arranged between a combustion furnace 12 and a combustion furnace. It consists of a preheater 12', which is provided in contact with the upper part of the combustion gas, and which exchanges heat with the combustion gas to preheat the air used for combustion, and a combustion gas cooler 13.

14は送風機であり冷却器13と炭酸ガス吸着装置9と
の間の連結管11に設け、導入管10より貯蔵庫1内の
空気を燃焼炉12に導き、更に燃焼炉12で発生した燃
焼ガスを冷却器13で冷却した後、連結管11により炭
酸ガス吸着装置9に導く。燃焼炉12は、内面に断熱管
16を備えた内ケーシング16と、燃焼2次空気を供給
するために内ケーシング16との間に風路17を形成し
た外ケーシング18と、断熱管16内で固形燃料19を
載置する火格子2oと、燃焼空気を加熱して固形燃料1
9を燃焼させるための着火用ヒータ21より構成されて
いる。固形燃料19は、純度の高い炭素であり燃焼によ
りC+o2+N2→Co2+N2 の反応で燃焼ガスは
炭酸ガス(Co2)と窒素(N2)になる。
Reference numeral 14 denotes a blower, which is installed in the connecting pipe 11 between the cooler 13 and the carbon dioxide adsorption device 9, guides the air in the storage 1 to the combustion furnace 12 through the introduction pipe 10, and also directs the combustion gas generated in the combustion furnace 12. After being cooled by the cooler 13, it is led to the carbon dioxide adsorption device 9 through the connecting pipe 11. The combustion furnace 12 includes an inner casing 16 having a heat insulating pipe 16 on its inner surface, an outer casing 18 having an air passage 17 formed between the inner casing 16 and the inner casing 16 for supplying secondary combustion air, and a heat insulating pipe 16 inside the heat insulating pipe 16. A grate 2o on which solid fuel 19 is placed, and a solid fuel 1 that heats combustion air.
It is composed of an ignition heater 21 for combusting the fuel. The solid fuel 19 is highly pure carbon, and upon combustion, the combustion gas becomes carbon dioxide (Co2) and nitrogen (N2) through a reaction of C+O2+N2→Co2+N2.

一方炭酸ガス吸着装置9は、燃焼ガスの中の過剰な炭酸
ガス(Co2)を吸着し、貯蔵庫1外に排出するための
ものである。2基の吸着器22 、23に対し、燃焼ガ
スが交互に循環するように導入管24.25、排出管2
6,27、及び流れを切替る切替バルブ28.29で構
成されている。吸着器22.23内には、吸着材30.
31が充填されており、炭酸ガス(CO2)を吸着し吸
着能力が低下すると、送風機32によって外気を切替バ
ルブ33.排出管26.27に接続している導入管34
あるいは35を通して吸着器22あるいは23に送風し
、炭酸ガスを脱着し、導入管24あるいは26に接続し
ている排出管36.37、切替バルブ38を通して排気
管39より大気に排気されるよう構成している。
On the other hand, the carbon dioxide adsorption device 9 is for adsorbing excess carbon dioxide (Co2) in the combustion gas and discharging it to the outside of the storage 1. An inlet pipe 24, 25 and an exhaust pipe 2 are connected to the two adsorbers 22 and 23 so that the combustion gas alternately circulates.
6, 27, and switching valves 28 and 29 for switching the flow. Inside the adsorber 22.23, an adsorbent 30.
31 is filled with carbon dioxide gas (CO2), and when the adsorption capacity decreases, the blower 32 switches the outside air to the switching valve 33. Inlet pipe 34 connected to outlet pipe 26.27
Alternatively, the configuration is such that air is blown to the adsorber 22 or 23 through 35, desorbs carbon dioxide gas, and is exhausted to the atmosphere from an exhaust pipe 39 through an exhaust pipe 36, 37 connected to the inlet pipe 24 or 26, and a switching valve 38. ing.

例えば、吸着器22が吸着作用、吸着器23が脱着作用
をしている時は、切替バルブ28.29は、燃焼ガス導
入管24、吸着器22、排出管26を通過して流れる方
向に開いており、また、切替バルブ33.38は、外気
が送風機32によって、導入管36、吸着器23、排出
管37を通過して流れる方向に開いて、排気管39よシ
大気に排気される。排気管4oは、切替パルプ29と貯
蔵庫を接続している。41は導入管10に設は一方を大
気に開放している切替パルプである。42は切替パルプ
であり、冷却器13と送風機14との間に設けられ、か
つ連結管43によって、導入管1゜と切替パルプ42は
接続されている。44は送風機14の風量を制御するコ
ントローラーであり、貯蔵庫1内のガス濃度を検知する
ガスモニター46の信号によって風量は決定する。46
はチャンバーであシ、貯蔵庫1と切替バルブ41の間の
導入管1oに設けられた容器であり、ガスモニター46
のサンプリングチューブ47を接続している。
For example, when the adsorber 22 is performing an adsorption function and the adsorber 23 is performing a desorption function, the switching valves 28 and 29 are opened in the direction in which the combustion gas flows through the combustion gas inlet pipe 24, adsorber 22, and discharge pipe 26. Furthermore, the switching valves 33 and 38 are opened in the direction in which outside air flows through the inlet pipe 36, the adsorber 23, and the exhaust pipe 37 by the blower 32, and is exhausted to the atmosphere through the exhaust pipe 39. The exhaust pipe 4o connects the switching pulp 29 and the storage. Reference numeral 41 is a switching pulp installed in the introduction pipe 10 and having one side open to the atmosphere. A switching pulp 42 is provided between the cooler 13 and the blower 14, and the introduction pipe 1° and the switching pulp 42 are connected by a connecting pipe 43. 44 is a controller that controls the air volume of the blower 14, and the air volume is determined by a signal from a gas monitor 46 that detects the gas concentration in the storage 1. 46
is a chamber, which is a container provided in the introduction pipe 1o between the storage 1 and the switching valve 41, and a gas monitor 46.
A sampling tube 47 is connected thereto.

以上のように構成された生鮮物貯蔵装置について、第1
図、第2図を用いてその動作を説明する。
Regarding the fresh food storage device configured as described above, the first
The operation will be explained using FIG.

貯蔵庫1内の雰囲気は、最初N279%、0221’%
であり、炭酸ガス発生装置8が運転されると、庫内空気
は、送風機14によって導入管10よυ、チャンバー4
6、切替パルプ41を通って予熱器12′の管外側に導
入され風路17を通って燃焼炉12へ導入され、着火用
ヒータ21で加熱され固形燃料19の燃焼ニ供すレル。
The atmosphere inside storage 1 was initially N279%, 0221'%.
When the carbon dioxide gas generator 8 is operated, the air inside the refrigerator is transferred to the inlet pipe 10 and the chamber 4 by the blower 14.
6. A barrel that is introduced to the outside of the tube of the preheater 12' through the switching pulp 41, is introduced into the combustion furnace 12 through the air passage 17, is heated by the ignition heater 21, and is used for combustion of the solid fuel 19.

C+ 02 + N 2 →CO2” N 2の反応で
燃焼ガスは炭酸ガス(Co□)と窒素(N2)になって
、予熱器12′の管内側を通シ冷却器13で冷却した後
、連結管11により、切替パルプ42、送風機14を通
過し、更に切替パルプブ28、導入管24を通過して吸
着器22に入る。ここで炭酸ガス(Co2)は、吸着材
3oによって吸着され窒素(N2)だけが、排出管2θ
、切替パルプ29を通過して排気管4oにより、貯蔵庫
1へ循環する。
C+ 02 + N 2 →CO2" The combustion gas becomes carbon dioxide (Co□) and nitrogen (N2) through the reaction of N2, and after cooling the inside of the tube of the preheater 12' in the condenser cooler 13, it is connected. Through the pipe 11, it passes through the switching pulp 42 and the blower 14, and further passes through the switching pulp 28 and the introduction pipe 24 to enter the adsorber 22. Here, carbon dioxide (Co2) is adsorbed by the adsorbent 3o and becomes nitrogen (N2). ) is the only discharge pipe 2θ
, the pulp passes through the switching pulp 29 and is circulated to the storage 1 through the exhaust pipe 4o.

一定時間が経過すると、燃焼ガスが循環する吸着器が2
2から23に切替わるべく、切替バ1Lty”28 。
After a certain period of time, the adsorber in which combustion gas circulates
To switch from 2 to 23, press the switch bar 1Lty"28.

29が切替わシ、切替パルプ28、導入管26を通過し
て吸着器23に入る。ここで再び炭酸ガス(C02)は
、吸着材31によって吸着され窒素(N2)だけが排出
管27、切替パルプ29を通過して排気管4oにより貯
蔵庫1へ循環する。再び一定時間が経過すると吸着器2
2.23が切替わ夛、交互に燃焼ガスが循環する。この
間に吸着器23.23の中に充填された吸着剤30.3
1は、炭酸ガス(Co2)の吸着能力の限界に達し燃焼
ガスの中の炭酸ガス(C02)は吸着しきれなくなり、
排気管4oを通って貯蔵庫1内に排気され、貯蔵庫1内
の炭酸ガス(C02)濃度は徐4に増加し始める。ys
、7の大きさの貯蔵庫1で運転開始後約2時間の状態で
ある。この間にも、貯蔵庫1内の酸素(o2)濃度は最
初21チより減少し続ける。貯蔵庫1内のガス濃度を、
酸素(o2)6%、炭酸ガス(Co  )5チ、窒素(
N2)90%を所定の値とすると、貯蔵庫1内の炭酸ガ
スが増加して5%に達したことを、ガスモニター46が
、チャンバー46内のガスサンプリングを行うことによ
って検知すると、炭酸ガス吸着装置9の脱着用の送風機
32が運転され、吸着器内の吸着材の再生が開始される
。例えば、吸着器22が、燃焼ガスが循環して炭酸ガス
(C02)を吸着していると、吸着器23は、送風機3
2によって外気が切替パルプ33゜導入管36.排出管
27を通過し、吸着材31に送風されることによって炭
酸ガス(Co2)が脱着され再生される。これが一定時
間毎に交互に行われるため、貯蔵庫1内の炭酸ガス(C
o2)濃度は所定の6sを維持する。一方酸素(02)
濃度は、その間も燃焼に供せられているため、減少し続
け、10時間後に所定の6%に達し、これをガスモニタ
ー46が検知し、炭酸ガス発生装置8及び炭酸ガス吸着
装置9を停止させる。これで、貯蔵庫1内が所定のガス
濃度酸素(02)6%、炭酸ガス(Co2)5チ、窒素
(N2)90%となシ、貯蔵を開始する。
29 is switched, passes through the switching pulp 28 and the introduction pipe 26, and enters the adsorber 23. Here, carbon dioxide (C02) is again adsorbed by the adsorbent 31, and only nitrogen (N2) passes through the exhaust pipe 27 and the switching pulp 29, and is circulated to the storage 1 through the exhaust pipe 4o. After a certain period of time has passed again, the adsorber 2
2.23 switches and the combustion gas alternately circulates. During this time, the adsorbent 30.3 filled in the adsorber 23.23
1 reaches the limit of carbon dioxide gas (Co2) adsorption capacity, and carbon dioxide gas (C02) in the combustion gas can no longer be adsorbed.
The gas is exhausted into the storage 1 through the exhaust pipe 4o, and the carbon dioxide (C02) concentration within the storage 1 begins to gradually increase. ys
This is the state of the storage 1, which has a size of . During this time, the oxygen (O2) concentration in the storage 1 continues to decrease from the initial 21°. The gas concentration in storage 1 is
Oxygen (O2) 6%, carbon dioxide gas (Co) 5%, nitrogen (
N2) If 90% is the predetermined value, when the gas monitor 46 detects by sampling the gas in the chamber 46 that the carbon dioxide in the storage 1 has increased to 5%, the carbon dioxide adsorbs. The blower 32 for desorption of the device 9 is operated, and regeneration of the adsorbent in the adsorber is started. For example, when the adsorber 22 is adsorbing carbon dioxide (C02) as combustion gas circulates, the adsorber 23 is adsorbed by the blower 3.
2, outside air is switched to pulp 33° introduction pipe 36. Carbon dioxide (Co2) is desorbed and regenerated by passing through the exhaust pipe 27 and being blown onto the adsorbent 31. This is done alternately at regular intervals, so carbon dioxide (C
o2) Maintain the concentration at the predetermined 6s. On the other hand, oxygen (02)
During that time, the concentration continues to decrease as it is being used for combustion, and reaches the predetermined 6% after 10 hours, which is detected by the gas monitor 46, and the carbon dioxide gas generator 8 and carbon dioxide adsorption device 9 are stopped. let Now, the storage begins when the gas concentration in the storage 1 reaches the predetermined gas concentrations of 6% oxygen (02), 5% carbon dioxide (Co2), and 90% nitrogen (N2).

酸素(02)濃度が所定の6チに達したのを検知すると
同時に切替パルプ41.42が、導入管10、連結管4
3、連結管11を連通ずるように切替わる。以後、一定
時間毎に送風機14を運転し、チャンバー46内のガス
をガスモニター46で検知することによって、貯蔵庫1
内に貯蔵している生鮮物の呼吸作用によって発生する炭
酸ガス(Co2)75衝定の6%横えると炭酸ガス吸着
装置9が働き、所定の濃度になるまで炭酸ガス(Co2
)を吸着する。この動作を説明すると、ガスモニター4
6が所定の濃度を越えたことを検知すると、送風機14
が運転され、貯蔵庫1内のガスが導入管10.切替バル
ブ41、連結管43、切替バルブ42、送風機14、連
結管11、切替バルブ28、導入管24を通過して吸着
器22に導入され、過剰の炭酸ガス(C02)が吸着材
3oに吸着されて、更に、排出管26、切替バルブ29
、排気管40を通過して貯蔵庫1に循環する。一方吸着
器23は、送風機32によって外気が切替バルブ33、
導入管36、排気管27を通過し、吸着材31に送風さ
れることによって炭酸ガス(Co2)が脱着され再生さ
れる。これが一定時間毎に交互に付われるため、貯蔵庫
1内の炭酸ガス(CO2)濃度は、所定の濃度にもどる
At the same time as detecting that the oxygen (02) concentration has reached the predetermined level, the switching pulps 41 and 42 switch the inlet pipe 10 and connecting pipe 4
3. The connecting pipe 11 is switched so as to be in communication with each other. Thereafter, by operating the blower 14 at regular intervals and detecting the gas in the chamber 46 with the gas monitor 46, the storage 1
When 6% of the carbon dioxide (Co2) 75 produced by the respiration of fresh food stored in the storage compartment is stored, the carbon dioxide adsorption device 9 works and absorbs carbon dioxide (Co2) until a predetermined concentration is reached.
). To explain this operation, gas monitor 4
6 exceeds a predetermined concentration, the blower 14
is operated, and the gas in the storage 1 is transferred to the inlet pipe 10. It passes through the switching valve 41, the connecting pipe 43, the switching valve 42, the blower 14, the connecting pipe 11, the switching valve 28, and the introduction pipe 24, and is introduced into the adsorber 22, and excess carbon dioxide (C02) is adsorbed by the adsorbent 3o. Furthermore, a discharge pipe 26 and a switching valve 29 are provided.
, passes through the exhaust pipe 40 and circulates to the storage 1. On the other hand, the adsorber 23 receives outside air by a blower 32 through a switching valve 33 ,
Carbon dioxide (Co2) is desorbed and regenerated by passing through the introduction pipe 36 and the exhaust pipe 27 and being blown onto the adsorbent 31. Since this is applied alternately at regular intervals, the carbon dioxide (CO2) concentration in the storage 1 returns to the predetermined concentration.

また、生鮮物の呼吸作用によって不足してくる酸素(0
2)が所定の6チ以下になると、送風機32によって外
気が貯蔵庫1に導入され補給される。
In addition, oxygen (0
2) becomes less than a predetermined value of 6 inches, outside air is introduced into the storage 1 by the blower 32 and replenished.

導入経路は、送風機32、切替バルブ33、導入管36
、排気管27、切替バルブ29、排気管40桶過し、貯
蔵庫1に導入される。
The introduction route includes a blower 32, a switching valve 33, and an introduction pipe 36.
, the exhaust pipe 27, the switching valve 29, and the exhaust pipe 40, and are introduced into the storage 1.

次に貯蔵を終了し、貯蔵庫1内の生鮮物を取出すために
貯蔵庫1内のガスを換気する動作を説明する。
Next, the operation of ventilating the gas in the storage 1 in order to finish storage and take out the perishables in the storage 1 will be explained.

制御盤(図示せず)に設けた換気スイッチ(図示せず)
をONにすることによって送風機14が運転され、貯蔵
庫1内のガスを導入管10.切替バルブ41、連結管4
3、切替バルブ42、連結管11、切替バルブ28、導
入管26、排出管37を通過して大気に放出される。同
時に、送風機32で外気を貯蔵庫1内に導入する。その
経路は、送風機32、切替バルブ33、導入管34、排
出管26、切替バルブ29、排気管40である。貯蔵庫
1内のガスが外気と同等になったことをガスモニター4
6で検知して、送風機14.32を停止し、切替バルブ
28を導入管24と連通ずるように、切替バルブ33を
導入管34と連通ずるように切替える。
Ventilation switch (not shown) on control panel (not shown)
The blower 14 is operated by turning on the gas in the storage 1 through the inlet pipe 10. Switching valve 41, connecting pipe 4
3. It passes through the switching valve 42, the connecting pipe 11, the switching valve 28, the introduction pipe 26, and the discharge pipe 37, and is released into the atmosphere. At the same time, outside air is introduced into the storage 1 by the blower 32. The path includes the blower 32, the switching valve 33, the inlet pipe 34, the discharge pipe 26, the switching valve 29, and the exhaust pipe 40. Gas monitor 4 confirms that the gas in storage 1 has become equal to the outside air.
6, the blowers 14 and 32 are stopped, and the switching valve 28 is switched to communicate with the inlet pipe 24, and the switching valve 33 is switched to communicate with the inlet pipe 34.

以上のように本発明は、燃焼炉の燃料の燃焼に供する空
気を予熱する予熱器を設け、かつ、この予熱器を燃焼炉
の上部に接するように設けることによシ、貯蔵庫より循
環した低温の空気を、予熱器で高温の燃焼ガスと熱交換
して予熱すると同時に、燃焼炉からの熱伝導によって予
熱するため、燃焼させるだめの着火用ヒータ21の通電
時間を短かくできるため、省電力化と、着火用ヒータ2
1の耐久性の向上を図ることができる。
As described above, the present invention provides a preheater for preheating the air used for combustion of fuel in the combustion furnace, and by providing this preheater in contact with the upper part of the combustion furnace, the low temperature air circulated from the storage Since the air is preheated by heat exchange with high-temperature combustion gas in the preheater and at the same time by heat conduction from the combustion furnace, the energization time of the ignition heater 21 for combustion can be shortened, which saves power. and ignition heater 2
The durability of No. 1 can be improved.

発明の効果 以上のように本発明は、燃焼炉の燃料の燃焼に供する空
気を予熱する予熱器を備え、予熱器と燃焼炉が少なくと
も一面を接して設けることにより、貯蔵庫より循環した
低温の空気を、予熱器で高温の燃焼ガスと熱交換して予
熱すると同時に、燃焼炉からの熱伝導によって予熱する
ため、燃焼させるための着火用ヒータの通電時間を短か
くできるため省電力化と着火用ヒータの耐久性の向上を
図ることができる。
Effects of the Invention As described above, the present invention includes a preheater for preheating the air used for combustion of fuel in a combustion furnace, and by providing the preheater and the combustion furnace in contact with each other on at least one side, the low temperature air circulated from the storage is heated. is preheated by heat exchange with high-temperature combustion gas in the preheater, and at the same time by heat conduction from the combustion furnace, it is possible to shorten the energization time of the ignition heater for combustion, resulting in power savings and ignition. It is possible to improve the durability of the heater.

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

第1図は本発明の一実施例における生鮮物貯蔵装置の構
成図、第2図は同装置による庫内ガス成分の変化図、第
3図は従来の生鮮物収蔵装置の系統図である。 1・・・・・・貯蔵庫、12・・・・・・燃焼炉、12
′・・・・・・予熱器、14・・・・・・送風機、19
・・・・・・固形燃料、22゜23・・・・・・吸着器
FIG. 1 is a block diagram of a fresh food storage device according to an embodiment of the present invention, FIG. 2 is a diagram of changes in gas components in the refrigerator according to the same device, and FIG. 3 is a system diagram of a conventional fresh food storage device. 1...Storage, 12...Combustion furnace, 12
'...Preheater, 14...Blower, 19
...Solid fuel, 22゜23...Adsorber.

Claims (1)

【特許請求の範囲】[Claims] 生鮮物を貯蔵する貯蔵庫と、この貯蔵庫内へ炭酸ガスを
導入すべく炭素を含有する燃料を燃焼させる燃焼炉と、
この燃焼炉に前記燃料の燃焼に供する空気を前記貯蔵庫
より循環せしめる送風機と、前記燃焼炉の燃料の燃焼に
供する空気を予熱する予熱器とを備え、前記予熱器と前
記燃焼炉が少なくとも一面を接して設けたことを特徴と
する生鮮物貯蔵装置。
a storage for storing perishables; a combustion furnace for burning carbon-containing fuel to introduce carbon dioxide gas into the storage;
The combustion furnace includes a blower that circulates air from the storage to be used for combustion of the fuel, and a preheater that preheats the air that is used for combustion of the fuel in the combustion furnace, and the preheater and the combustion furnace cover at least one side. A fresh food storage device characterized in that the devices are installed adjacent to each other.
JP1025045A 1989-02-03 1989-02-03 Apparatus for storing perishables Pending JPH02203717A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1025045A JPH02203717A (en) 1989-02-03 1989-02-03 Apparatus for storing perishables

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1025045A JPH02203717A (en) 1989-02-03 1989-02-03 Apparatus for storing perishables

Publications (1)

Publication Number Publication Date
JPH02203717A true JPH02203717A (en) 1990-08-13

Family

ID=12154947

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1025045A Pending JPH02203717A (en) 1989-02-03 1989-02-03 Apparatus for storing perishables

Country Status (1)

Country Link
JP (1) JPH02203717A (en)

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