JPS62198328A - Apparatus for storing perishables - Google Patents

Apparatus for storing perishables

Info

Publication number
JPS62198328A
JPS62198328A JP3992286A JP3992286A JPS62198328A JP S62198328 A JPS62198328 A JP S62198328A JP 3992286 A JP3992286 A JP 3992286A JP 3992286 A JP3992286 A JP 3992286A JP S62198328 A JPS62198328 A JP S62198328A
Authority
JP
Japan
Prior art keywords
storage
carbon dioxide
gas
adsorption device
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.)
Pending
Application number
JP3992286A
Other languages
Japanese (ja)
Inventor
純 武田
啓人 中間
武 清水
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 JP3992286A priority Critical patent/JPS62198328A/en
Publication of JPS62198328A publication Critical patent/JPS62198328A/en
Pending legal-status Critical Current

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  • 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。つまり、貯蔵庫
内の酸素(02)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 (以下、CA
貯蔵と称す)。
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 (02) 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 prevent chemical reactions such as decomposition and oxidation caused by microorganisms (hereinafter referred to as CA).
storage).

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′から成る冷却装置4′を設けている。5′
はプロパンガスボンベであり、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
燃焼させC3H8+60 →3CO+4H20+531
 、lalの反応で発生し2       ま た炭酸ガス(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
)全吸着した後排出管11で貯蔵庫1′に戻している。
FIG. 3 shows a system diagram of a conventional fresh food storage device. Reference numeral 1' denotes a storage, and a cooling device 4' consisting of an evaporator 2' and a condensing unit 3' is provided. 5′
is a propane gas cylinder, which is combusted by the carbon dioxide generator 6' using air introduced from the storage 1' through the introduction pipe 7' to produce C3H8+60 →3CO+4H20+531
, lal2 and carbon dioxide (CO2) is discharged into the storage 1' through a discharge pipe 8'. Reference numeral 9' denotes a carbon dioxide gas adsorption device, which is introduced from the storage 1' through an inlet pipe 10 to absorb excess carbon dioxide (Co2).
) After all the adsorption is carried out, it is returned to the storage 1' through the discharge pipe 11.

12′はガスモニターであり貯蔵H1′内のガス濃度を
検知して炭酸ガス発生装置6′及び廃酸ガス吸着装置9
′を適時コントロールしている。
12' is a gas monitor which detects the gas concentration in the storage H1' and connects the carbon dioxide gas generator 6' and the waste acid gas adsorption device 9.
′ is controlled in a timely manner.

以上のように構成された生鮮物貯蔵装置について以下そ
の動作について説明する。
The operation of the fresh produce storage device configured as above will be described below.

まずガスモニター12′の炭酸ガス(CO2)、酸R(
02)+lI!eCO2;s%、02;5%  K設定
しておく。貯蔵庫1′内の雰囲気は最初N2;79%、
02;21%であり、炭酸ガス発生装置6′が運転され
ると庫内空気は送風機(図示せず)によって導入管7′
より導入され、プロパンガスボンベ5′から供給された
ガスと混合され燃焼に供される。燃焼によって発生した
炭酸ガス(Co2)を排出管8′より貯蔵庫1′内へ循
、環させる。
First, the gas monitor 12' shows carbon dioxide gas (CO2), acid R (
02)+lI! Set eCO2; s%, 02; 5% K. The atmosphere inside storage 1' was initially N2; 79%;
02: 21%, and when the carbon dioxide gas generator 6' is operated, the air inside the refrigerator is transferred to the inlet pipe 7' by a blower (not shown).
The gas is introduced from the propane gas cylinder 5', mixed with gas supplied from the propane gas cylinder 5', and subjected to combustion. Carbon dioxide (Co2) generated by combustion is circulated into the storage 1' through the exhaust pipe 8'.

これによって貯蔵庫1′内ガス組成は、酸素(02)濃
度が低下し炭酸ガス(Co2)濃度が増加してくる、炭
酸ガス(CO2)濃度が6%に達したことをガスモニタ
ー12′が検知して炭酸ガス吸着装置9′全運転させ、
送風機(図示せず)によって導入管i o’より貯蔵庫
1′内のガスー炭酸ガス吸着装置9′に導入し過剰の炭
酸ガス(Co2)’を吸着し、排出管11′で貯蔵庫1
′内へ循環させる。
As a result, the gas composition in the storage chamber 1' is such that the oxygen (02) concentration decreases and the carbon dioxide (Co2) concentration increases.The gas monitor 12' detects that the carbon dioxide (CO2) concentration has reached 6%. and fully operate the carbon dioxide adsorption device 9′.
A blower (not shown) introduces the gas through the inlet pipe i o' into the gas-carbon dioxide adsorption device 9' in the storage 1', adsorbs excess carbon dioxide (Co2)', and removes it from the storage 1 through the discharge pipe 11'.
’.

一方酸素(o2)濃度はその間にも燃焼に供せられてい
るため徐々に減少し初期02 ; 21%からo2;6
チまで減少する。これをガスモニター12′が検知し炭
酸ガス発生装置6′を停止させる。貯蔵庫1′内のガス
組成がN2;90チ、 Co2; sチ。
On the other hand, the oxygen (O2) concentration gradually decreases because it is being used for combustion during that time, from the initial 02:21% to O2:6.
decreases to . The gas monitor 12' detects this and stops the carbon dioxide gas generator 6'. The gas composition in the storage chamber 1' is N2; 90 cm, Co2; s.

0□; 6%の所定の値に到達すれば炭酸ガス吸着装置
9′が停止し所定の貯蔵条件に到達する。
0□; When the predetermined value of 6% is reached, the carbon dioxide adsorption device 9' is stopped and the predetermined storage condition is reached.

ところで、上記動作の中で、炭酸ガス吸着装置9′によ
って吸着された貯蔵庫1′内の過剰の炭酸ガスは、貯蔵
庫1′外に排出されるため、その分、貯蔵庫1′内の圧
力が大気圧よりも負圧になる。
By the way, during the above operation, the excess carbon dioxide in the storage 1' that has been adsorbed by the carbon dioxide adsorption device 9' is discharged outside the storage 1', so the pressure inside the storage 1' increases accordingly. The pressure becomes more negative than atmospheric pressure.

これを解消するために貯蔵庫1′内外の圧力を均一に保
つ圧力調整弁(図示せず)より外気の空気が貯蔵庫1′
内に補充される。ところが、当然補充される空気には2
1%の酸素分が含まれているため、これをまた燃焼によ
って炭酸ガス化し、再び炭酸ガス吸着装置9′によって
吸着し、貯蔵庫1′外に放出される。一方この時、補充
される空気の79%は窒素であり、この分で貯蔵庫1′
内の負圧の解消に当てられるがまた十分ではないので、
再び外気の空気が貯蔵庫1′内に補充されるという動作
が連続的に繰返される。
To solve this problem, outside air is supplied to the storage 1' from a pressure regulating valve (not shown) that maintains uniform pressure inside and outside the storage 1'.
will be replenished within. However, the air that is naturally replenished has 2
Since it contains 1% oxygen, it is also converted into carbon dioxide by combustion, adsorbed again by the carbon dioxide adsorption device 9', and discharged outside the storage 1'. On the other hand, at this time, 79% of the air replenished is nitrogen, and this amount makes up 1' of the storage space.
Although it is used to relieve the negative pressure inside, it is not enough,
The operation of replenishing the storage chamber 1' with outside air is repeated continuously.

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、貯蔵庫1′内の負
圧を解消するために補充される空気に含まれる酸素分を
燃焼によって炭酸ガス化し、それを炭酸ガス吸着装置9
′によって吸着し、貯蔵庫1′外に排出しているため、
どうしても貯蔵庫1′内を所定のガス濃度にするのに時
間ががかり、従って、貯蔵庫1′内の生鮮物の呼吸作用
の抑制も遅れるため、その間の鮮度の劣下が大きかった
。ちなみに、第4図に示す如く10坪の貯蔵庫内のガ。
Problems to be Solved by the Invention However, in the above configuration, the oxygen contained in the air that is replenished in order to eliminate the negative pressure in the storage chamber 1' is converted into carbon dioxide by combustion, and the carbon dioxide gas is converted into carbon dioxide gas by the carbon dioxide adsorption device. 9
′ is adsorbed and discharged outside the storage 1′,
It takes time to bring the inside of the storage 1' to a predetermined gas concentration, and as a result, there is a delay in suppressing the respiration of the fresh food in the storage 1', resulting in a significant deterioration in freshness during that time. By the way, as shown in Figure 4, there are moths in a 10 tsubo storage room.

ス濃度をCO26% ; 02 s%;N29o%にす
るのに要する時間は、20時間も要していた。
It took as long as 20 hours to reduce the gas concentration to 6% CO2; 02 s%; 90% N2.

本発明は、上記問題点に鑑み、短時間で所定のガス濃度
に到達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 reach a predetermined gas concentration in a short time.

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
、貯蔵庫内へ窒素ガスを導入する手段を備えたものであ
る。
Means for Solving the Problems In order to solve the above problems, the fresh produce storage apparatus of the present invention is provided with means for introducing nitrogen gas into the storage.

作  用 本発明は、上記した構成によって、炭酸ガス吸着装置に
よって吸着された貯蔵庫内の過剰の炭酸ガスを貯蔵庫外
に排出することによって生じた貯蔵庫内外の圧力差を解
消するために、炭酸ガスを排出すると同時に、排出する
炭酸ガスと同量の窒素ガスを貯蔵庫内に補充することに
より、外気の空気を導入する必要がなく従って燃焼によ
って低減させる酸素量は貯蔵庫内の酸素だけであるので
、短時間で貯蔵庫内を所定のガス濃度に到達できるため
、生鮮物の呼吸作用の抑制も早急にでき鮮度の劣化を防
止できるものである。
Effects The present invention has the above-described configuration, in order to eliminate the pressure difference between the inside and outside of the storage, which is caused by discharging the excess carbon dioxide in the storage, which has been adsorbed by the carbon dioxide adsorption device, to the outside of the storage. By replenishing the storage with the same amount of nitrogen gas as the carbon dioxide gas to be discharged at the same time as the carbon dioxide being discharged, there is no need to introduce outside air, and the amount of oxygen reduced by combustion is only the oxygen in the storage. Since it is possible to reach a predetermined gas concentration in the storage in a short period of time, the respiration effect of fresh food can be quickly suppressed and deterioration of freshness can be prevented.

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、第1
図、第2図で説明する。
Example ・The following is a first example of a fresh food storage device according to an example of the present invention.
This will be explained with reference to FIG.

図において1は生鮮物を貯蔵するプレファプ冷蔵庫の如
き貯蔵庫であり、圧縮機2.凝縮器3゜蒸発器4.送風
機6.6よ構成る冷却装置7を上部に載架・している。
In the figure, 1 is a storage such as a pre-fabricated refrigerator for storing perishables, and a compressor 2. Condenser 3° Evaporator 4. A cooling device 7 comprising a blower 6.6 is mounted on the top.

上記貯蔵庫1には、庫内に炭酸ガス(C02)を充填す
るための炭酸ガス発生装置8.庫内の過剰の炭酸ガス(
C02)を吸着して一定濃度に保つ炭酸ガス吸着装置9
がそれぞれ接続されている。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10と、燃焼ガスを貯蔵
庫1内に排出する排出管11との間に構成され、送風機
12.パルプ13.燃焼炉14.燃焼排ガスの冷却器1
5で構成されている。送風機12は、導入管10より貯
蔵庫1内の空気を燃焼炉14に導き燃焼炉14での燃焼
排ガスを冷却器16で冷却した後、排出管11より貯蔵
庫1内へ循環させるものである。また燃焼炉14は内面
にセラミック管16を備えた内ケーシング17と燃焼二
次空気を供給するために内ケーシング17との間ニ風路
18を形成した外ケーシング19と、セラミック管16
内で固形燃料2oを載置する火格子21と、送風機12
からの空気を加熱して固形燃料20を燃焼させるための
着火用ヒータ22よシ構成されている。固形燃料20は
炭の如き炭素純度の高いものであシ、燃焼によりC+0
2十N2→Co2+N2の反応で燃焼排ガスは炭酸ガス
(co2)と窒素(N2)のみとなって貯蔵庫1内に導
入されるものである。23は燃焼補助用の空気を外気よ
り導入するためのパルプである。
The storage 1 includes a carbon dioxide gas generating device 8 for filling the interior of the storage with carbon dioxide (C02). Excess carbon dioxide gas in the refrigerator (
Carbon dioxide adsorption device 9 that adsorbs C02) and maintains it at a constant concentration
are connected to each other. The carbon dioxide generator 8 is constructed between an inlet pipe 10 that introduces air into the storage 1 and an exhaust pipe 11 that discharges combustion gas into the storage 1, and includes a blower 12. Pulp 13. Combustion furnace 14. Combustion exhaust gas cooler 1
It consists of 5. The blower 12 guides the air inside the storage 1 to the combustion furnace 14 through the introduction pipe 10, cools the combustion exhaust gas in the combustion furnace 14 with the cooler 16, and then circulates it into the storage 1 through the discharge pipe 11. The combustion furnace 14 also includes an inner casing 17 having a ceramic tube 16 on its inner surface, an outer casing 19 forming an air passage 18 between the inner casing 17 for supplying secondary combustion air, and a ceramic tube 16.
A grate 21 on which solid fuel 2o is placed, and a blower 12
The ignition heater 22 is configured to heat the air from the engine and combust the solid fuel 20. The solid fuel 20 is one with high carbon purity, such as charcoal, and is C+0 by combustion.
Due to the reaction of 20N2→Co2+N2, the combustion exhaust gas becomes only carbon dioxide (CO2) and nitrogen (N2) and is introduced into the storage 1. 23 is a pulp for introducing air for combustion assistance from the outside air.

一方、炭酸ガス吸着装置9は貯蔵庫1内のガス組成が炭
酸ガス発生装置8によって、N2;79%。
On the other hand, in the carbon dioxide adsorption device 9, the gas composition in the storage 1 is N2: 79% due to the carbon dioxide gas generation device 8.

CO□;16%、02;15チになった時、所定の値。When CO□: 16%, 02: 15%, a predetermined value is set.

例えば、N2;90%、Co2;5%、02;5%にす
べく過剰の炭酸ガス(C02)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24.25に
対し、貯蔵庫1内のガスを交互に循環させるよう導入管
26.排出管2了、送風機2 B * ハル7”29〜
36で構成されている。吸着器24.25内には、吸着
材37.38が充填されており、炭酸ガス(C02)を
吸着し、また、吸着能力が低下すると、送風機39の吐
出側に設けたヒータ4oを加熱し、熱風をパルプ33 
、35を介して吸着器24.25に導かれる導入管41
により送風し、炭酸ガスを脱着し、パルプ34゜36を
介して大気に導かれる排出管42より大気に排出される
よう構成している。例えば、吸着器24が吸着作用、吸
着器26が脱着作用をしている時は、パルプ29,30
,33.34が開、パルプ31.32,35.36が閉
となっており、送風機28によって炭酸ガス(Co2)
過剰の貯蔵庫1内のガスを、吸着器24の吸着材37に
通して炭酸ガスの吸着をさせ再び貯蔵庫1に戻し、一方
、送風機39によってヒータ4oで加熱された外気を、
吸着器26の吸着材38に通して炭酸ガスの脱着を行う
ものである。43は貯蔵庫1内のガス濃度を検知するガ
スモニターであり、貯蔵庫1内のガス濃度によって炭酸
ガス発生装置8及び炭酸ガス吸着装置9の運転のコント
ロールを行う。
For example, it is for adsorbing excess carbon dioxide gas (C02) to make it N2: 90%, Co2: 5%, and 02: 5%, and discharging it outside the storage 1. An inlet pipe 26. is used to alternately circulate the gas in the storage 1 to the two adsorbers 24.25. Discharge pipe 2 completed, blower 2 B * Hull 7” 29~
It consists of 36 pieces. The adsorber 24.25 is filled with adsorbent material 37.38, which adsorbs carbon dioxide gas (C02), and when the adsorption capacity decreases, it heats the heater 4o provided on the discharge side of the blower 39. , pulp hot air 33
, 35 to the adsorber 24.25.
The structure is such that air is blown, carbon dioxide is desorbed, and the carbon dioxide gas is discharged to the atmosphere through an exhaust pipe 42 which is led to the atmosphere via pulps 34 and 36. For example, when the adsorber 24 is performing adsorption and the adsorber 26 is performing desorption, the pulp 29, 30
, 33, 34 are open, pulp 31, 32, 35, 36 are closed, and carbon dioxide gas (Co2) is generated by the blower 28.
The excess gas in the storage 1 is passed through the adsorbent 37 of the adsorber 24 to adsorb carbon dioxide gas and returned to the storage 1 again, while the outside air heated by the heater 4o by the blower 39 is
Carbon dioxide is desorbed by passing it through the adsorbent 38 of the adsorber 26. 43 is a gas monitor that detects the gas concentration in the storage 1, and controls the operation of the carbon dioxide gas generator 8 and the carbon dioxide adsorption device 9 according to the gas concentration in the storage 1.

44は、窒素ガスボンベであり、ボンベ内の窒素ガスは
送気管46によって貯蔵庫1内に導かれている。46は
、送気管45に設けられたパルプであり、ガスモニター
43の信号により開閉動作を行うべく構成しである。
44 is a nitrogen gas cylinder, and the nitrogen gas in the cylinder is guided into the storage 1 through an air pipe 46. Reference numeral 46 denotes a pulp provided in the air supply pipe 45, and is configured to open and close in response to a signal from the gas monitor 43.

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。
The operation of the fresh food storage apparatus constructed as above will be explained with reference to FIGS. 1 and 2.

貯蔵庫1内の雰囲気は最初N2;79%、02;21チ
となっておシ、炭酸ガス発生装置8が運転されると庫内
空気は送風機12によって導入管1゜より導入されパル
プ13を通過して燃焼炉14へ導入され、着火用ヒiり
22により加熱され固形燃料20の燃焼に供される。C
+02十N2→CO2+N2の反応で排ガスは炭酸ガス
(CO2)と窒素(N2)のみとなって冷却器15で冷
却した後排出管11より貯蔵庫1内へ循環させる。貯蔵
庫1内のガス組成は、酸素(0゜)濃度が低下し炭酸ガ
ス(CO2)a度が増加してぐる。2時間30分を経i
すると、N2;79%、Co2;s%、02;1et%
となり、所定のriを、N2;90%、co。;5チ。
Initially, the atmosphere in the storage warehouse 1 is N2: 79%, 02: 21%, and when the carbon dioxide gas generator 8 is operated, the air inside the warehouse is introduced from the introduction pipe 1° by the blower 12 and passes through the pulp 13. The solid fuel 20 is then introduced into the combustion furnace 14, heated by the ignition torch 22, and used for combustion of the solid fuel 20. C
Due to the reaction +020N2→CO2+N2, the exhaust gas becomes only carbon dioxide (CO2) and nitrogen (N2), which are cooled by the cooler 15 and then circulated into the storage 1 through the discharge pipe 11. The gas composition in the storage 1 is such that the oxygen (0°) concentration decreases and the carbon dioxide (CO2) a degree increases. After 2 hours and 30 minutes i
Then, N2; 79%, Co2; s%, 02; 1et%
Then, the predetermined ri is N2; 90%, co. ;5 chi.

o2;6%とすると、炭酸ガス(CO2)が所定の6チ
に達したことをガスモニター43が検知し、炭酸ガス吸
着装置9が運転される。そして、貯蔵庫1内のガスを送
風機28で導入管26よシ吸着器24に導入され、吸着
材37によって炭酸ガスだけ吸着され窒素だけが排出管
27より貯蔵庫1内に戻される。吸着器24.25は交
互に吸着作用。
o2: 6%, the gas monitor 43 detects that carbon dioxide (CO2) has reached a predetermined level of 6%, and the carbon dioxide adsorption device 9 is operated. Then, the gas in the storage 1 is introduced into the adsorption device 24 through the introduction pipe 26 by the blower 28, only carbon dioxide gas is adsorbed by the adsorbent 37, and only nitrogen is returned into the storage 1 through the discharge pipe 27. Adsorbers 24 and 25 alternately perform adsorption action.

脱着作用を繰返し連続的にどちらかの吸着器で炭酸ガス
を吸着する。従って貯蔵庫1内の炭酸ガス濃度は5%を
維持するが、貯蔵庫1内の過剰の炭酸ガスは吸着器24
.26で吸着され、貯蔵庫1外に排出管42より排出さ
れるため、貯蔵庫1内はその外大気圧より負圧となる。
The desorption action is repeated and carbon dioxide gas is adsorbed continuously by either adsorber. Therefore, the carbon dioxide concentration in the storage 1 is maintained at 5%, but the excess carbon dioxide in the storage 1 is removed by the adsorber 24.
.. 26 and discharged outside the storage 1 through the discharge pipe 42, the pressure inside the storage 1 becomes more negative than the outside atmospheric pressure.

これを解消するため、貯蔵庫1内の炭酸ガス濃度が5チ
を越えて、炭酸ガス吸着装置9が運転されると同時にガ
スモニター43からの信号によりパルプ46が閉から開
となり、窒素ボンベ44から送気管45を通って貯蔵庫
1内に窒素ガスが導入される。導入される量は、炭酸ガ
ス吸着装置9で排出される過剰の炭酸ガス量と同等量に
調整されている。一方酸素(02)濃度はその間にも燃
焼に供せられているため減少し、16時間後に所定の6
%に達する。これをガスモニター43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。
To solve this problem, when the carbon dioxide concentration in the storage 1 exceeds 5% and the carbon dioxide adsorption device 9 is operated, the pulp 46 is switched from closed to open by a signal from the gas monitor 43, and the nitrogen cylinder 44 is opened. Nitrogen gas is introduced into the storage 1 through the air pipe 45 . The amount introduced is adjusted to be equivalent to the amount of excess carbon dioxide discharged by the carbon dioxide adsorption device 9. On the other hand, the concentration of oxygen (02) decreases because it is being used for combustion during that time, and after 16 hours, the concentration of oxygen (02) decreases.
reach %. The gas monitor 43 detects this and stops the carbon dioxide gas generator 8 and carbon dioxide adsorption device 9.

それと同時にパルプ46が開から閉に切替わり、窒素ボ
ンベ44からの窒素ガスの送気を停止する。
At the same time, the pulp 46 is switched from open to closed, and the supply of nitrogen gas from the nitrogen cylinder 44 is stopped.

これで貯蔵庫1内がガス濃度N2;90%、C02;5
%、02;5%となり、所定の貯蔵条件に到達する。以
後、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(C02)が所定の値6チを越える
とガスモニター43が検知し、炭酸ガス吸着装置9を働
かせ、炭酸ガスを所定の値になるまで吸着し排出する。
Now the gas concentration inside storage 1 is N2; 90%, C02; 5
%, 02; 5%, reaching the predetermined storage conditions. Thereafter, when the carbon dioxide gas (C02) generated by the respiration of fresh food stored in the storage room 1 exceeds a predetermined value of 6, the gas monitor 43 detects this and activates the carbon dioxide adsorption device 9 to remove carbon dioxide gas. It is adsorbed and discharged until it reaches a predetermined value.

それと同時にパルプ46も閉から開となり、排出した分
の窒素を貯蔵庫1内に補充し、貯蔵庫1内の圧力が負圧
にならないようにする。
At the same time, the pulp 46 is also changed from closed to open, and the discharged nitrogen is replenished into the storage 1 to prevent the pressure inside the storage 1 from becoming a negative pressure.

発明の効果 以上のように本発明は、炭酸ガス発生装置と、炭酸ガス
吸着装置と、貯蔵庫内へ窒素ガスを導入する手段を設け
ることにより、炭酸ガス吸着装置によって吸着された貯
蔵庫内の過剰の炭酸ガスを貯蔵庫外に排出することによ
って生じた貯蔵庫内外の圧力差を解消するために、炭酸
ガスを排出すると同時に、         、排出す
る炭酸ガスと同量の窒素ガスを貯蔵庫内に補充すること
により、外気の空気を導入する必要がなく、従って燃焼
によって低減させる酸素量は貯蔵庫内の酸素だけである
ので、短時間で、貯蔵庫内を所定のガス濃度に到達し得
るため、生鮮物の呼吸作用の抑制も早急にでき鮮度の劣
化を防止できるものである。
Effects of the Invention As described above, the present invention provides a carbon dioxide gas generation device, a carbon dioxide adsorption device, and a means for introducing nitrogen gas into the storage, thereby reducing the amount of excess gas in the storage that has been adsorbed by the carbon dioxide adsorption device. In order to eliminate the pressure difference between the inside and outside of the storage chamber caused by discharging carbon dioxide gas outside the storage chamber, at the same time as the carbon dioxide gas is discharged, the same amount of nitrogen gas as the discharged carbon dioxide gas is replenished into the storage chamber. There is no need to introduce outside air, and the amount of oxygen that is reduced by combustion is only the oxygen in the storage, so the predetermined gas concentration can be reached within the storage in a short period of time, which reduces the respiration of fresh produce. This can also be quickly controlled to prevent deterioration of freshness.

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

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
造図、第2図は同第1図の貯蔵庫内のガス成分の変化図
、第3図は従来の生鮮物貯蔵装置の系統図、第4図は貯
蔵庫内のガス成分の変化図である。 1・・・・・・貯蔵庫、8・・・・・・炭酸ガス発生装
置、9・・・・・・炭酸ガス吸着装置、12・・・・・
・送風機、14・・・・・・燃焼炉、2o・・・・・・
燃料、24.25・・・・・・吸着器、28・・・・・
・送風機、37.38・・・・・・吸着材、44・・;
・・・窒素ボンベ。 第2図 第3図
Fig. 1 is a structural diagram of a fresh produce storage device according to an embodiment of the present invention, Fig. 2 is a diagram of changes in gas components in the storage chamber shown in Fig. 1, and Fig. 3 is a system diagram of a conventional fresh produce storage device. , FIG. 4 is a diagram showing changes in gas components in the storage. 1... Storage, 8... Carbon dioxide gas generator, 9... Carbon dioxide adsorption device, 12...
・Blower, 14... Combustion furnace, 2o...
Fuel, 24.25...Adsorber, 28...
・Blower, 37.38...Adsorbent, 44...;
...Nitrogen cylinder. Figure 2 Figure 3

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、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より成る炭酸ガス発生装置と、前
記貯蔵庫内の炭酸ガスを吸着すべく吸着材を入れた吸着
器、この吸着器に前記貯蔵庫内のガスを循環せしめる送
風機より成る炭酸ガス吸着装置と、前記貯蔵庫内へ窒素
ガスを導入する手段を備えたことを特徴とする生鮮物貯
蔵装置。
A carbon dioxide fuel cell system consisting of a storage for storing perishables, a combustion furnace for burning carbon-containing fuel to introduce carbon dioxide gas into the storage, and a blower for circulating air from the storage to the combustion furnace for combustion of the fuel. A carbon dioxide adsorption device includes a gas generator, an adsorbent containing an adsorbent to adsorb carbon dioxide in the storage, a blower that circulates gas in the storage through the adsorption device, and a carbon dioxide adsorption device that supplies nitrogen gas into the storage. A fresh produce storage device characterized by comprising means for introducing.
JP3992286A 1986-02-25 1986-02-25 Apparatus for storing perishables Pending JPS62198328A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3992286A JPS62198328A (en) 1986-02-25 1986-02-25 Apparatus for storing perishables

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3992286A JPS62198328A (en) 1986-02-25 1986-02-25 Apparatus for storing perishables

Publications (1)

Publication Number Publication Date
JPS62198328A true JPS62198328A (en) 1987-09-02

Family

ID=12566425

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3992286A Pending JPS62198328A (en) 1986-02-25 1986-02-25 Apparatus for storing perishables

Country Status (1)

Country Link
JP (1) JPS62198328A (en)

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