JPS63126426A - perishable storage equipment - Google Patents
perishable storage equipmentInfo
- Publication number
- JPS63126426A JPS63126426A JP61273362A JP27336286A JPS63126426A JP S63126426 A JPS63126426 A JP S63126426A JP 61273362 A JP61273362 A JP 61273362A JP 27336286 A JP27336286 A JP 27336286A JP S63126426 A JPS63126426 A JP S63126426A
- Authority
- JP
- Japan
- Prior art keywords
- storage
- carbon dioxide
- blower
- gas
- combustion furnace
- 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
Links
Landscapes
- Storage Of Fruits Or Vegetables (AREA)
- Storage Of Harvested Produce (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
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。つまシ、貯蔵庫
内の酸素(o2)濃度を減少せしめ、炭酸ガス(C02
)濃度を増加せしめることて生鮮物の呼吸作用を抑制し
、また微生物による変質1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. It reduces the concentration of oxygen (O2) in the storage room and releases carbon dioxide (C02).
) 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 decomposition and oxidation caused by microorganisms.
以下図面を参照しながら、上述した従来の生鮮物貯蔵装
置の一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′から成る冷却製蓋4′を設けている。6′
はプロパンガスボンベであり、炭素ガス発生装置6′で
前記貯蔵庫1′よシ導入管7′で導入した空気を供して
燃焼させC3H8+60−3CO2+ 4H20+ 6
31−の反応で発生した燃焼排ガスすなわち炭酸ガス(
CO2)を排出管8′で前記貯蔵庫1′に排出している
。9′は炭酸ガス吸着装置で、前記貯蔵庫1′より導入
管10’で導入し、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′
はガスモニターであり貯蔵庫1′内のガス濃度を検知し
て炭酸ガス発生製蓋6′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, which is provided with a cooling lid 4' consisting of an evaporator 2' and a condensing unit 3'. 6′
is a propane gas cylinder, which is combusted by the carbon gas generator 6' using the air introduced from the storage 1' through the inlet pipe 7' to produce C3H8+60-3CO2+ 4H20+ 6
The combustion exhaust gas, that is, carbon dioxide gas (
CO2) is discharged to the storage 1' through a discharge pipe 8'. Reference numeral 9' denotes a carbon dioxide adsorption device, which is introduced from the storage 1' through an inlet pipe 10', adsorbs excess carbon dioxide (Co2), and then returned to the storage 1' through a discharge pipe 11'. 12'
is a gas monitor which detects the gas concentration in the storage chamber 1' and controls the carbon dioxide gas generating lid 6' and the carbon dioxide adsorption device 9' in a timely manner.
発明が解決しようとする問題点
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′から発生するガスの成分としては炭酸ガス(Co
2)以外にエチレンやプロピレン等の青果物の貯蔵に有
害な・ガスが多量に含有されており、そのガスが直接貯
蔵庫1′内に放出されるため、貯蔵物にしばしば悪影響
を与えていた。Problems to be Solved by the Invention However, in the above configuration, carbon dioxide (Co) is a component of the gas generated from the carbon dioxide gas generator 6'.
In addition to 2), it contains large amounts of gases such as ethylene and propylene that are harmful to the storage of fruits and vegetables, and because these gases are directly released into the storage 1', they often have an adverse effect on the stored items.
本発明は、上記問題点に鑑み、貯蔵に有害なガスを全て
除去し得る生鮮物貯蔵装置を提供するものである。In view of the above problems, the present invention provides a fresh food storage device that can remove all gases harmful to storage.
問題点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貯
蔵庫の下流に燃焼炉を、燃焼炉の下流に送風機を送風機
の下流に吸着器を、吸着器の下流に貯蔵庫を配設し、か
つ、貯蔵庫と燃焼炉との間に設けた切替バルブと、燃焼
炉と送風機との間に設けた切替バルブとを接続してなる
ものである。Means for Solving the Problems In order to solve the above problems, the perishables storage device of the present invention includes a combustion furnace downstream of the storage, a blower downstream of the combustion furnace, an adsorption device downstream of the blower, and a downstream of the adsorption device. A storage is disposed in the combustion chamber, and a switching valve is provided between the storage and the combustion furnace, and a switching valve is provided between the combustion furnace and the blower.
作 用
本発明は、上記構成によって燃焼によって発生するガス
をすべて吸着器を通して貯蔵庫に放出している。この吸
着器の中ては、過剰な炭酸ガスCO2を吸着するだけで
なくエチレン等を吸着する吸着材を充填しているため、
貯蔵に有害なガスをすべて除去し得ることになる。Function: According to the present invention, all the gases generated by combustion are discharged into the storage through the adsorber with the above-mentioned configuration. This adsorber is filled with an adsorbent that not only adsorbs excess carbon dioxide gas CO2, but also adsorbs ethylene, etc.
All gases harmful to storage can be removed.
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ファブ冷蔵庫
の如き貯蔵庫であシ、圧縮機2、凝縮器3、蒸発器4、
送風機5.8より成る冷却装置子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(C02)を吸着して除去する炭酸ガス吸着
装置e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及び燃焼ガスの冷却器13で構
成されている。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
シ貯蔵庫1内の空気を燃焼炉12に導き、更に燃焼炉1
2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1eとの間に風
路17を形成した外ケーシング18と、断熱管15内で
固形燃料19を載置する火格子2゜と、燃焼空気を加熱
して固形燃料19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。In FIG. 1, 1 is a storage such as a prefabricated refrigerator for storing perishables, a compressor 2, a condenser 3, an evaporator 4,
A cooling device consisting of a blower 5.8 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 e for adsorbing and removing excess carbon dioxide (CO2) in the 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 connects the combustion furnace 12 and the combustion gas. It is composed of a cooler 13. 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 through the introduction pipe 10 to the combustion furnace 12, and further connects the combustion furnace 1 to the combustion furnace 1.
After the combustion gas generated in step 2 is cooled by a cooler 13, it is led to a carbon dioxide adsorption device 9 through a 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 forming an air passage 17 between the inner casing 1e and the inner casing 1e for supplying secondary combustion air, and a heat insulating pipe 15 inside the outer casing 18. A grate 2° on which solid fuel 19 is placed, and an ignition heater 21 for heating combustion air to combust solid fuel 19.
It is composed of
固形燃料19は、純度の高い炭素であり燃焼によシC+
02十N2−CO2+N2の反応で燃焼ガスは炭酸ガス
(Co2)と窒素(N2)になる。The solid fuel 19 is highly pure carbon and is combustible.
The combustion gas becomes carbon dioxide (Co2) and nitrogen (N2) through the reaction of 020N2-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26
.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30.3
1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25に接続し℃
いる排出管36.37、切替バルブ38を通して排気管
39よシ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. Inlet pipes 24, 25 and exhaust pipes 26 are connected to the two adsorbers 22, 23 so that the combustion gas alternately circulates.
.. 27, and switching valves 28 and 29 for switching the flow. Inside the adsorber 22.23, there is an adsorbent 30.3.
1 is filled with carbon dioxide (CO2), and when the adsorption capacity decreases, the blower 32 switches the outside air to the switching valve 33. Air is blown to the adsorber 22 or 23 through the inlet pipe 34 or 35 connected to the discharge pipe 26, 27,
Desorb the carbon dioxide gas, connect it to the inlet pipe 24 or 25 and keep it at ℃
The exhaust pipe 39 is configured to be exhausted to the atmosphere through the exhaust pipes 36, 37 and the switching valve 38.
例えば、吸着器22が吸着作用、吸着器23が脱着作用
をし5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9、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、切替バルブ29と
貯蔵庫を接続している。41.42は切替バルブであり
各々、貯蔵庫1と燃焼炉12、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、切替バル
ブ41.42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45の信号によって風量は
決定する。46はチャンバーであり、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45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 adsorption and the adsorber 23 is performing desorption, the switching valves 28 and 29 are set in the direction in which the combustion gas flows through the combustion gas inlet pipe 24, adsorber 22, and discharge pipe 26. The switching valves 33 and 38 are opened in the direction in which outside air flows through the inlet pipe 36, adsorber 23, and exhaust pipe 37 by the blower 32, and is exhausted to the atmosphere through the exhaust pipe 39. Ru. The exhaust pipe 4o connects the switching valve 29 and the storage. 41 and 42 are switching valves for the storage 1, the combustion furnace 12, the cooler 13 and the blower 14, respectively.
The switching valves 41 and 42 are connected to each other 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 45 that detects the gas concentration in the storage 1. A chamber 46 is a container provided in the introduction pipe 1o between the storage 1 and the switching valve 41, and is connected to the sampling tube 47 of the gas monitor 45.
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N 27 s % p 0
22’%であシ、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1oより、チャ
ンバー46、切替バルブ41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
に供される。C+02十N2(o2擢。The atmosphere in storage 1 was initially N 27 s % p 0
When the carbon dioxide gas generator 8 is operated at 22'%,
Internal air is introduced into the combustion furnace 12 by the blower 14 from the introduction pipe 1o through the chamber 46 and the switching valve 41, heated by the ignition heater 21, and used for combustion of the solid fuel 19. C+020N2 (o2 擢.
の反応で燃焼ガスは炭酸ガス(C02)と窒素(N2)
になって、冷却器13で冷却した後、連結管11により
、切替バルブ42、送風機14を通過し、更に切替バル
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26、切替バルブ29を通
過して排気管4oにより、貯蔵庫1へ循環する。一定時
間が経過すると、燃焼ガスが循環する吸着器が22から
23に切替わるべく、切替バルブ28.29が切替わり
、切替バルブ28、導入管25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、切替バ
ルブ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22.23が切替
わり、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材30.31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40を
通って貯蔵庫1内に排気され、貯蔵庫1内の炭酸ガス(
Co2)濃度は徐々に増加し始める。76rr+3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%
より減少し続ける。貯蔵庫1内のガス濃度を、酸素(0
2)6%、炭酸ガス(C02)5%。In the reaction, the combustion gas is carbon dioxide (C02) and nitrogen (N2)
After being cooled by the cooler 13, the air passes through the switching valve 42 and the blower 14 through the connecting pipe 11, and further passes through the switching valve 28 and the introduction pipe 24, and enters the adsorber 22. Here, carbon dioxide (Co2) is adsorbed by the adsorbent 3o, and only nitrogen (N2) passes through the exhaust pipe 26 and the switching valve 29 and circulates to the storage 1 through the exhaust pipe 4o. After a certain period of time has elapsed, the switching valves 28 and 29 are switched so that the adsorber in which the combustion gas circulates is switched from 22 to 23, and the combustion gas passes through the switching valve 28 and the introduction pipe 25 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 valve 29, and is circulated to the storage 1 through the exhaust pipe 4o. After a certain period of time has elapsed again, the adsorbers 22 and 23 are switched, and the combustion gas is alternately circulated. During this time, the adsorber 23
.. The adsorbents 30 and 31 filled in the chamber 23 reach the limit of their adsorption capacity for carbon dioxide (CO2), and the carbon dioxide (CO2) in the combustion gas cannot be adsorbed completely, and it passes through the exhaust pipe 40 to the storage chamber. 1, and carbon dioxide gas (
Co2) concentration begins to increase gradually. This is the state of the storage 1, which has a size of 76rr+3, and has been in operation for about 2 hours since the start of operation. During this time, the oxygen (O2) concentration in storage 1 was initially 21%.
continues to decrease. The gas concentration in storage 1 is set to oxygen (0
2) 6%, carbon dioxide gas (C02) 5%.
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6チに達したことを、ガスモニター
46が、チャンバー4θ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(CO2)を吸着していると、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35゜
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(C02)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(CO2)濃度は所定の5%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0これで、貯蔵庫1内が所定
のiス濃度酸素(02)5% 、炭酸fj ス(CO2
) 5 %、窒素(N2)90%となり、貯蔵を開始す
る。酸素(0□)濃度が所定の5%に達したのを検知す
ると同時に切替バルブ41.42が、導入管10、連結
管43、連結管11を連通ずるように切替わる。Assuming that 90% nitrogen (N2) is the predetermined value, when the gas monitor 46 detects by sampling the gas in the chamber 4θ that the carbon dioxide gas in the storage chamber 1 has increased to 6. The blower 32 for desorption of the gas adsorption device 9 is operated, and regeneration of the adsorbent in the adsorption device is started. For example, when the adsorber 22 is adsorbing carbon dioxide (CO2) as combustion gas circulates, the adsorber 23 is moved to the outside air by the blower 32 through the switching valve 33. Carbon dioxide (C02) is desorbed and regenerated by passing through the inlet pipe 35 and the discharge pipe 27 and being blown onto the adsorbent 31. Since this is performed alternately at regular intervals, the carbon dioxide (CO2) concentration in the storage 1 is maintained at a predetermined 5%. On the other hand, oxygen (
02) The concentration continues to decrease as it is being used for combustion during that time, 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 0 Now, the inside of storage 1 is at the predetermined concentrations of oxygen (02) 5% and carbon dioxide fj (CO2).
) 5%, nitrogen (N2) 90%, and storage begins. At the same time as detecting that the oxygen (0□) concentration has reached a predetermined value of 5%, the switching valves 41 and 42 are switched so that the introduction pipe 10, the connecting pipe 43, and the connecting pipe 11 are communicated with each other.
以後、一定時間毎に送風機14を運転し、チャンバー4
6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(Co□)が所定の6%を越えると炭
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45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(Co2
)が吸着材30に吸着されて、更に、排出管26、切替
バルブ29、排気管4o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3
1に送風されることによって炭酸ガス(C02)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。After that, the blower 14 is operated at regular intervals, and the chamber 4 is
By detecting the gas in the storage compartment 1 with the gas monitor 46, if the carbon dioxide (Co□) generated by the respiration of fresh food stored in the storage compartment 1 exceeds a predetermined 6%, the carbon dioxide adsorption device 9 is activated. It works to adsorb carbon dioxide (CO2) until it reaches a predetermined concentration. To explain this operation, when the gas monitor 45 detects that a predetermined concentration has been exceeded,
The blower 14 is operated, and the gas in the storage 1 is transferred to the inlet pipe 10.
.. Excess carbon dioxide (Co2
) is adsorbed by the adsorbent 30 and further circulates to the storage 1 through the exhaust pipe 26, the switching valve 29, and the exhaust pipe 4o. On the other hand, in the adsorber 23, outside air is passed through the switching valve 33, the inlet pipe 36, and the exhaust pipe 27 by the blower 32, and the adsorbent 3
1, carbon dioxide gas (C02) is desorbed and regenerated. 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%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 6%, 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35
、排気管27、切替バルブ29、排気管4゜を通過し、
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 35.
, passes through the exhaust pipe 27, the switching valve 29, and the exhaust pipe 4°,
It is introduced into 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25、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
径路は、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と連通するように、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, the switching valve 41, and the connecting pipe 4.
3. It passes through the switching valve 42, the connecting pipe 11, the switching valve 28, the introduction pipe 25, 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 paths include 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 33 is opened so that the switching valve 28 is communicated with the introduction pipe 24.
is switched so that it communicates with the introduction pipe 34.
以上のように本発明は、貯蔵庫の下流に燃焼炉を、燃焼
炉の下流に送風機を、送風機の下流に吸着器を、吸着器
の下流に貯蔵庫を環状に配設し、かつ貯蔵庫と燃焼炉と
の間に設けた切替バルブと 。As described above, the present invention provides a combustion furnace downstream of a storage, a blower downstream of the combustion furnace, an adsorption device downstream of the blower, a storage storage downstream of the adsorption device, and a storage storage and a combustion furnace. and a switching valve installed between.
燃焼炉と、送風機との間に設けた切替バルブとを接続し
てなるものであるから、燃焼によって発生するガスをす
べて吸着器を通して貯蔵庫に放出しているため、この吸
着器によって過剰な炭酸ガス(CO2)を1吸着するだ
けでなく、エチレン等を吸着する吸着材を充填している
ため、貯蔵に有害なガスをすべて除去することができる
。Since the combustion furnace is connected to a switching valve installed between the blower, all the gas generated by combustion is released into the storage through the adsorber, which removes excess carbon dioxide. Because it is filled with an adsorbent that not only adsorbs CO2 but also adsorbs ethylene, etc., it can remove all gases that are harmful to storage.
発明の効果
以上のように本発明は、貯蔵庫の下流に燃焼炉を、燃焼
炉の下流に送風機を、送風機の下流に吸着器を、吸着器
の下流に貯蔵庫を環状に配設し、かつ貯蔵庫と燃焼炉と
の間に設けた切替バルブと、燃焼炉と、送風機との間に
設けた切替バルブとを接続してなるものであるから、燃
焼によって発生するガスをすべて吸着器を通して貯蔵庫
に放出しているため、この吸着器によって過剰な炭酸ガ
ス(C02)を吸着するだけでなく、エチレン等を吸着
する吸着材を充填しているため、貯蔵に有害なガスをす
べて除去することができる。Effects of the Invention As described above, the present invention provides a combustion furnace downstream of a storage, a blower downstream of the combustion furnace, an adsorption device downstream of the blower, a storage storage downstream of the adsorption device, and a storage storage. The switching valve installed between the combustion furnace and the combustion furnace is connected to the switching valve installed between the combustion furnace and the blower, so all the gas generated by combustion is released into the storage through the adsorber. Therefore, this adsorber not only adsorbs excess carbon dioxide gas (C02), but also contains an adsorbent that adsorbs ethylene and other substances, making it possible to remove all gases that are harmful to storage.
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図は従来の生鮮物貯蔵装置の系統図である。
1・・・・・・貯蔵庫、12・・・・・・燃焼炉、14
・川・・送風機、19・・・・・・固形燃料、22.2
3・・・・・・吸着器、41.42・・・・・・切替バ
ルブ。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, 14
・River...Blower, 19...Solid fuel, 22.2
3...Adsorber, 41.42...Switching valve.
Claims (1)
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、前記燃焼炉から発生するガ
スの過剰な炭酸ガスを吸着すべく吸着材を入れた吸着器
とを備え、前記貯蔵庫の下流に前記燃焼炉を、前記燃焼
炉の下流に前記送風機を、前記送風機の下流に前記吸着
器を、前記吸着器の下流に前記貯蔵庫を配設し、かつ、
前記貯蔵庫と前記燃焼炉との間に設けた切替バルブと、
前記燃焼炉と前記送風機との間に設けた切替バルブとを
接続し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;
This combustion furnace is equipped with a blower that circulates air from the storage to be used for combustion of the fuel, and an absorber containing an adsorbent to adsorb excess carbon dioxide gas generated from the combustion furnace, The combustion furnace is arranged downstream, the blower is arranged downstream of the combustion furnace, the adsorber is arranged downstream of the blower, and the storage is arranged downstream of the adsorber, and
a switching valve provided between the storage and the combustion furnace;
A fresh produce storage device characterized in that a switching valve provided between the combustion furnace and the blower is connected.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61273362A JPS63126426A (en) | 1986-11-17 | 1986-11-17 | perishable storage equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61273362A JPS63126426A (en) | 1986-11-17 | 1986-11-17 | perishable storage equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS63126426A true JPS63126426A (en) | 1988-05-30 |
Family
ID=17526842
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP61273362A Pending JPS63126426A (en) | 1986-11-17 | 1986-11-17 | perishable storage equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS63126426A (en) |
-
1986
- 1986-11-17 JP JP61273362A patent/JPS63126426A/en active Pending
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