JPS63126424A - Apparatus for storing perishables - Google Patents
Apparatus for storing perishablesInfo
- Publication number
- JPS63126424A JPS63126424A JP61273360A JP27336086A JPS63126424A JP S63126424 A JPS63126424 A JP S63126424A JP 61273360 A JP61273360 A JP 61273360A JP 27336086 A JP27336086 A JP 27336086A JP S63126424 A JPS63126424 A JP S63126424A
- Authority
- JP
- Japan
- Prior art keywords
- storage
- blower
- gas
- carbon dioxide
- 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
Links
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 85
- 238000003860 storage Methods 0.000 claims description 71
- 229910002092 carbon dioxide Inorganic materials 0.000 claims description 45
- 238000002485 combustion reaction Methods 0.000 claims description 23
- 239000001569 carbon dioxide Substances 0.000 claims description 18
- 238000001816 cooling Methods 0.000 claims description 11
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 9
- 239000000446 fuel Substances 0.000 claims description 7
- 229910052799 carbon Inorganic materials 0.000 claims description 5
- 230000003750 conditioning effect Effects 0.000 claims 1
- 239000007789 gas Substances 0.000 description 25
- 239000003463 adsorbent Substances 0.000 description 18
- 239000000567 combustion gas Substances 0.000 description 18
- 238000001179 sorption measurement Methods 0.000 description 16
- 230000007423 decrease Effects 0.000 description 6
- 239000004449 solid propellant Substances 0.000 description 5
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 230000007774 longterm Effects 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 230000008929 regeneration Effects 0.000 description 3
- 238000011069 regeneration method Methods 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 2
- 238000007664 blowing Methods 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000003795 desorption Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 235000013305 food Nutrition 0.000 description 2
- 230000001172 regenerating effect Effects 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 230000029058 respiratory gaseous exchange Effects 0.000 description 2
- 239000006096 absorbing agent Substances 0.000 description 1
- 239000003575 carbonaceous material Substances 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 235000012055 fruits and vegetables Nutrition 0.000 description 1
- 239000002828 fuel tank Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
Landscapes
- Storage Of Harvested Produce (AREA)
- Storage Of Fruits Or Vegetables (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CA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9分解や酸化等の化学的反応も防
止することができることが知られている。そしてこのC
A貯蔵方式としては例えば特公昭80−12004号公
報に示される如く、炭素を含む燃料を燃焼装置で燃焼さ
せ、燃焼排ガスを貯蔵庫内へ導入することによシ、庫内
の酸素濃度を減少させるガス発生装置と、庫内の雰囲気
を所定の値にするCo2吸収塔(ガス調整装置)とを構
成してなるものである。BACKGROUND OF THE INVENTION Refrigerated storage is a common means of storing perishables, but in addition to this, there is CA storage, which changes the air composition within the storage, as a longer-term storage means. In other words, by reducing the oxygen 02 concentration and increasing the carbon dioxide concentration in the storage, it is possible to suppress the respiration of fresh produce and also to prevent chemical reactions such as alteration9 decomposition and oxidation caused by microorganisms. It has been known. And this C
As shown in Japanese Patent Publication No. 80-12004, the A storage method reduces the oxygen concentration in the storage by burning fuel containing carbon in a combustion device and introducing the combustion exhaust gas into the storage. It consists of a gas generator and a Co2 absorption tower (gas adjustment device) that adjusts the atmosphere inside the refrigerator to a predetermined value.
一方、かかる生鮮物貯蔵装置(CA貯蔵装@)において
は通常冷却装置によって冷気を庫内に循環させて生鮮物
を冷却と雰囲気調整とで長時間保存を可能としているが
、このためには、生鮮物の入庫後直ちに所定の雰囲気に
調整することは言うまでもなく、生鮮物が常に安定した
冷却条件下におかれることが望ましい。On the other hand, in such perishables storage equipment (CA storage equipment@), the perishables can be stored for a long time by using a cooling device to circulate cold air inside the storage and by controlling the atmosphere. Needless to say, the atmosphere must be adjusted to a predetermined level immediately after the fresh produce is stored, and it is desirable that the fresh produce is always kept under stable cooling conditions.
発明が解決しようとする問題点
上述の如き生鮮物貯蔵装置において、庫内の雰囲気調整
時、例えばCO2濃度が5%で所定の値とな9.02濃
度を6チになるまで減少させる時は、庫内の空気を燃焼
炉へ送り、燃焼炉により空気中の02 をCo2 に変
化させ、この燃焼ガスをガス調整装置の2つの炭酸ガス
吸着器の一方に導入し、内部に充填した活性炭等の吸着
材で燃焼ガス中のCO2を吸着し、この空気を庫内にも
どし、他方には、送風機により室内の空気を送り込み吸
着材に吸着したCO2を取り除く吸着材の再生を例えば
吸着6外脱着6分等の時間切りかえで行っていた。Problems to be Solved by the Invention In the above-mentioned fresh food storage apparatus, when adjusting the atmosphere inside the chamber, for example, when the CO2 concentration reaches a predetermined value at 5%, and when reducing the CO2 concentration from 9.02 to 6. , the air inside the warehouse is sent to the combustion furnace, where the 02 in the air is changed into Co2, and this combustion gas is introduced into one of the two carbon dioxide adsorbers of the gas adjustment device, and activated carbon etc. The adsorbent adsorbs CO2 in the combustion gas and returns this air to the inside of the chamber. On the other hand, a blower sends indoor air to remove CO2 adsorbed on the adsorbent. For example, adsorption 6 external desorption is used to regenerate the adsorbent. The sessions were held at different times, such as 6 minutes.
ところが、吸着材の送風による再生時において、流入シ
2.貯蔵庫内の02 濃度の減少速度がおそくな、ると
いう問題点があった。However, when regenerating the adsorbent by blowing air, the inflow 2. There was a problem in that the rate of decrease in the 02 concentration in the storage was slow.
そこで本発明は、上記問題点に鑑み、貯蔵庫内をすばや
く所定雰囲気に調整できる生鮮物貯蔵装置を提供するも
のである。SUMMARY OF THE INVENTION In view of the above-mentioned problems, the present invention provides a fresh produce storage device that can quickly adjust the inside of a storage to a predetermined atmosphere.
問題点を解決するための手段 したがって本発明は生鮮物を貯蔵する貯蔵庫と。Means to solve problems Therefore, the present invention relates to a storage for storing perishables.
この貯蔵庫内を冷却する冷却装置と、前記貯蔵庫内へ炭
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装置とより成る炭酸ガス
発生装置と、前記貯蔵庫内の雰囲気を所定の値に調整す
る複数個の吸着器と、この吸着器を再生せしめる送風装
置とより成るガス調整装置と、前記貯蔵庫の炭酸ガス濃
度に応じて、吸着器を切り替える制御装置とより成るも
のである。A cooling device that cools the inside of the storage, a combustion furnace that burns fuel containing carbon to introduce carbon dioxide gas into the storage, and a blower that circulates air from the storage to be used for combustion of the fuel in the combustion furnace. a gas regulating device consisting of a plurality of adsorbers that adjust the atmosphere in the storage to a predetermined value, a blower device that regenerates the adsorbers, and a carbon dioxide gas generator in the storage. It consists of a control device that switches adsorbers depending on the concentration.
作用
本発明は、前記した構成によって、吸着器の切り替えを
制御することができるため%02の庫内流入量を減少さ
せることができるので、貯蔵庫内をすばやく所定の雰囲
気に調整できるものである。Effects According to the present invention, with the above-described configuration, the switching of adsorbers can be controlled, so that the amount of inflow into the storage can be reduced by %02, so that the inside of the storage can be quickly adjusted to a predetermined atmosphere.
実施例
以下本発明の一実施例について1図面に基づき説明する
。EXAMPLE Hereinafter, an example of the present invention will be described based on one drawing.
図において、1は生鮮物を貯蔵するプレハブ冷蔵庫の如
き貯蔵庫″′Cあり、圧縮機2.凝縮器3゜漏扁1−号
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。送風機5は凝縮器3を冷却し、送風機6は
蒸発器4による冷気を庫内に強制循環するものである。In the figure, 1 is a storage unit such as a prefabricated refrigerator for storing perishables, and a cooling device 7 consisting of a compressor 2, a condenser 3, a No. 1 evaporator 4, and a blower 5 and 6 is mounted on the top. The air blower 5 cools the condenser 3, and the air blower 6 forcibly circulates cold air from the evaporator 4 into the warehouse.
上記貯蔵庫1には庫内に炭酸ガスC02を導入するため
の炭酸ガス発生装置8.庫内の雰囲気を一定の状態に保
つガス調整装置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1Qと
、バルブ11.12の開閉により、燃焼ガスをあるいは
定常状態時には貯蔵庫1内ガスを導入しガス調整装置9
内に送る排出管Bとの間に構成され、バルブ14.送風
装置16(例えばシロッコファン)、燃焼炉1eで構成
されている。The storage 1 has a carbon dioxide gas generating device 8 for introducing carbon dioxide gas C02 into the storage. A gas regulating device 9 that maintains the atmosphere inside the refrigerator in a constant state is connected to each of them. The carbon dioxide gas generator 8 introduces combustion gas or, in a steady state, gas from the storage 1 by opening and closing an inlet pipe 1Q that introduces air from the storage 1 and valves 11 and 12, and a gas regulator 9.
A valve 14. It is composed of an air blower 16 (for example, a sirocco fan) and a combustion furnace 1e.
送風装置15は、導入管10より庫1内の空気を燃焼炉
16に送り、バルブ11.12の開閉によシ燃焼炉16
での燃焼ガス及び貯蔵庫1内のガスをガス調整装置9へ
導入させるものである。又燃焼炉16は内面にセラミッ
ク管1アを備えたケーシング18と、このケーシング1
8内で固形燃料19を載置するロスドル兼カバー20と
送風装置16からの空気を加温して固形燃料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。The blower device 15 sends the air inside the warehouse 1 to the combustion furnace 16 through the introduction pipe 10, and blows the air into the combustion furnace 16 by opening and closing the valves 11 and 12.
The combustion gas in the storage room 1 and the gas in the storage 1 are introduced into the gas adjustment device 9. The combustion furnace 16 also includes a casing 18 equipped with a ceramic tube 1a on the inner surface, and a
The fuel tank 8 is comprised of a lid and cover 20 on which the solid fuel 19 is placed, and an ignition heater 21 for heating the air from the blower 16 and combusting the solid fuel 19.
固形燃料19は炭の如き炭素純度の高いものであり、燃
焼によりCO2を燃焼ガスとして発生する。The solid fuel 19 is a high-purity carbon material such as charcoal, and when it is combusted, CO2 is generated as a combustion gas.
っまりC+o2→CQ2の反応で燃焼ガスはN2 とC
O2となる。The combustion gas is N2 and C due to the reaction of C+O2→CQ2.
It becomes O2.
22は、導入管10からのo2!1度が極度に低い時、
固形燃料19の燃焼を継続させるべく外気を導入するた
めのバルブ、23は排出管Bを冷却するための熱交換器
である。22, when the o2!1 degree from the introduction pipe 10 is extremely low,
A valve 23 is a heat exchanger for cooling the exhaust pipe B, and a valve 23 is for introducing outside air to continue combustion of the solid fuel 19.
一方、ガス調整装置9は、2基の吸着器24゜26と、
燃焼ガスをガス調整装置9に送る導入管26、庫1内へ
送る排出管27、送風機28、吸着器24.25の再生
用の送風機29、ノ(ルブ3o〜37にて構成されてお
り、吸着器24.25には活性炭よりなる吸着材38.
39が充填されている。4oは貯蔵庫1のCo2 濃度
を測定するCO2濃度計41よりの信号によりバルブ3
0〜37の開閉を行う制御装置、42は同信号により送
風機29の制御を行う送風機制御装置である。On the other hand, the gas adjustment device 9 includes two adsorbers 24 and 26,
It is composed of an inlet pipe 26 that sends combustion gas to the gas adjustment device 9, an exhaust pipe 27 that sends it into the warehouse 1, a blower 28, a blower 29 for regenerating the adsorber 24, 25, and no(lubes 3o to 37). The adsorber 24.25 has an adsorbent 38. made of activated carbon.
39 is filled. 4o is a valve 3 that is activated by a signal from a CO2 concentration meter 41 that measures the CO2 concentration in the storage chamber 1.
A control device 42 controls the blower 29 using the same signal.
以上の様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 described above will be explained with reference to FIGS. 1 and 2.
冷却装置7で任意の温度に冷却された(例えばAT=2
°C)貯蔵庫1内に、青果物を入庫すると。Cooled to an arbitrary temperature by the cooling device 7 (for example, AT=2
°C) When fruits and vegetables are stored in storage 1.
貯蔵庫1内の雰囲気は外気雰囲気(N2=79%。The atmosphere inside storage 1 is outside air (N2 = 79%).
02=21%)で第2図のA点となっている。ここでC
A雰囲気(例えばN2=90%、CC2=s%。02=21%), which is point A in Figure 2. Here C
A atmosphere (for example, N2 = 90%, CC2 = s%.
o2=5%)第2図で0点にすべく、炭酸ガス発生装置
8を作動さす。すると貯蔵1庫内空気は、導入管10.
バルブ14.送風装置16を介して燃焼炉16に導入さ
れ燃焼に供される。固形燃料19の燃焼による燃焼ガス
、つまりN2 とCo2のガスは、まず吸着器24、
排出管27を通り貯蔵庫1内へ導入され、徐々にC2が
減少する。この時。o2=5%) The carbon dioxide gas generator 8 is activated in order to make the point 0 in FIG. Then, the air inside the storage 1 is transferred to the inlet pipe 10.
Valve 14. The air is introduced into the combustion furnace 16 via the blower 16 and subjected to combustion. The combustion gases resulting from the combustion of the solid fuel 19, that is, the gases of N2 and Co2, first pass through the adsorber 24,
C2 is introduced into the storage 1 through the discharge pipe 27, and C2 gradually decreases. At this time.
吸着塔24を燃焼ガスが通過しているので、ノ(ルブ3
0,33.36.36は開いた状態にあり、バルブ31
.32,34,37は閉じた状態にある。この時、吸着
器24.25の再生用送風機29はまだ停止している。Since the combustion gas is passing through the adsorption tower 24, the
0,33.36.36 are in open state, valve 31
.. 32, 34, and 37 are in a closed state. At this time, the regeneration blower 29 of the adsorber 24, 25 is still stopped.
又、燃焼ガスは、吸着器24を通るために、燃焼カスニ
含すれるCO2,No、、So! etc、吸着材38
に吸着されるが、CC2は濃度が高いためしばらくする
とCo2 の吸着限界に達し、C02が吸着器24より
リークしてくる様になり、貯蔵庫1内のCo2濃度は上
昇してくる。Also, since the combustion gas passes through the adsorber 24, the combustion gas contains CO2, No, So! etc., adsorbent 38
However, since the concentration of CC2 is high, the adsorption limit for Co2 is reached after a while, and CO2 begins to leak from the adsorber 24, and the Co2 concentration in the storage 1 increases.
燃焼炉1eで発生したCo2は吸着材38にその吸着能
力分だけ吸着された後、庫内にCo2が流入するので、
例えば庫内雰囲気が(’2=80%。After the Co2 generated in the combustion furnace 1e is adsorbed by the adsorbent 38 according to its adsorption capacity, the Co2 flows into the warehouse.
For example, the atmosphere inside the refrigerator is ('2 = 80%.
Q=16%、C02=6%)の第2図B点に到達すると
C02濃度計41が貯蔵庫1内のCO2濃度を検知し、
CA雰囲気(N2=90%、o2=5%、CC2=s%
)に制御すべく送風機制御装置42.バルブ制御装置4
oに信号が送られ吸着材38に吸着したC02を取り除
くべく送風機29が作動し、又燃焼炉1eで発生するC
o2を吸着するため、バルブ30〜3了が作動し、燃焼
ガスは吸着器24を通る状態から吸着器25を通る状態
に変わる。When reaching point B in Figure 2 (Q = 16%, CO2 = 6%), the CO2 concentration meter 41 detects the CO2 concentration in the storage 1,
CA atmosphere (N2=90%, O2=5%, CC2=s%
) to control the blower control device 42. Valve control device 4
o, the blower 29 operates to remove the CO2 adsorbed on the adsorbent 38, and also removes the C02 generated in the combustion furnace 1e.
In order to adsorb o2, the valves 30 to 3 are operated, and the combustion gas changes from passing through the adsorber 24 to passing through the adsorber 25.
この時、送風機29は貯蔵庫1内がCA雰囲気(N2=
90%、02=6%、 CC2=ts% )第2 図C
点K 到達するため運転が行われ、バルブ30〜3アの
開閉状態により吸着器24.25中の吸着材38.39
に吸着しているCO2の脱着を交互に行う。又バルブ3
0〜37の開閉は、貯蔵庫1内のCO2!1度により行
われる。つまり、貯蔵庫1内のCO2濃度がまず6チに
なるまでは燃焼ガスは吸着器24を通り、6チ以上にな
るとバルブ制御装置40によりバルブ31.32,34
,37が開、30,33゜35.36が閉となり、燃焼
ガスは吸着器26を通り、送風機29により吸着器24
は再生される。At this time, the blower 29 causes the inside of the storage 1 to have a CA atmosphere (N2=
90%, 02=6%, CC2=ts%) Figure 2 C
Operation is performed to reach point K, and the adsorbent 38.39 in the adsorber 24.25 is
Desorption of CO2 adsorbed on the air is performed alternately. Also valve 3
The opening/closing of 0 to 37 is performed by CO2!1 degrees in the storage 1. In other words, the combustion gas first passes through the adsorber 24 until the CO2 concentration in the storage 1 reaches 6 degrees, and when it reaches 6 degrees or more, the valve controller 40 controls the valves 31, 32, 34.
, 37 are open, and 30, 33° and 35.36 are closed, and the combustion gas passes through the adsorber 26 and is sent to the adsorber 24 by the blower 29.
is played.
この状態になると、貯蔵庫1内のCo2 は、燃焼によ
って生じたC02 と共に吸着器25に吸着されること
になり、貯蔵庫1内のCO2濃度は減少してくる。しか
しある程度吸着器26がCC2を吸着するとCo2 の
吸着限界に達し、CO2がリークしてくるので、貯蔵庫
1内のCO□濃度は徐々に増加してくる。ここで貯蔵庫
1内のCO2濃度が5%以上になると、バルブ制御装置
40により、バルブ30,33.35.36は開、バル
ブ31.32,34,37は閉となり燃焼ガスは吸着器
24を通り、吸着器25は送風機29により再生される
。In this state, the CO2 in the storage 1 will be adsorbed by the adsorber 25 together with the CO2 generated by combustion, and the CO2 concentration in the storage 1 will decrease. However, when the adsorber 26 adsorbs CC2 to a certain extent, the adsorption limit for Co2 is reached and CO2 begins to leak, so that the CO□ concentration in the storage 1 gradually increases. When the CO2 concentration in the storage 1 becomes 5% or more, the valve control device 40 opens the valves 30, 33, 35, and 36, and closes the valves 31, 32, 34, and 37, and the combustion gas flows into the adsorber 24. As usual, the adsorber 25 is regenerated by the blower 29.
つまり、上記した様に、貯蔵庫内がCA雰囲気(N2=
90%、o2=6%、C02=6%)Kなる一1f貯蔵
庫1内のCO2濃度により、吸着24.25の切替えが
行われ、燃焼ガスが通っていない方は常に再生用送風機
29によりCo2 の脱着が行われることになる。In other words, as mentioned above, the inside of the storage is CA atmosphere (N2=
90%, O2 = 6%, CO2 = 6%) The adsorption 24.25 is switched depending on the CO2 concentration in the 1st floor storage room 1, and the one through which combustion gas is not passing is always CO2 by the regeneration blower 29. will be attached and detached.
ここで、吸着器24.25の送風による再生時において
、吸着材3B 、39に02が吸着し、燃焼ガス中のC
o2吸着時に吸着材38.39に吸着したC2が脱離し
貯蔵庫1内に流入するが、吸着材38.39はその吸着
限界までCo2 を吸着するため、吸着器24.2’5
の切り替え時間は例えば吸着材38.39を各30に9
を入れた場合は約20分となり長くなるため、吸着器2
4.25の切り替えによる庫内への02流入量は、吸着
材38.39の長期信頼性を考慮し、切り替え時間をタ
イマーにより5分とした場合に比較して大幅に減少する
。Here, during regeneration by air blowing from the adsorbers 24 and 25, 02 is adsorbed to the adsorbents 3B and 39, and the carbon in the combustion gas is
During o2 adsorption, C2 adsorbed on the adsorbent 38.39 is desorbed and flows into the storage 1, but since the adsorbent 38.39 adsorbs Co2 up to its adsorption limit, the adsorbent 24.2'5
For example, the switching time for the adsorbent is 38.39 to 30.
If the absorber 2 is used, it will take about 20 minutes, so
The amount of 02 flowing into the warehouse due to the switching of 4.25 is significantly reduced compared to the case where the switching time is set to 5 minutes by a timer, considering the long-term reliability of the adsorbent 38.39.
つまり、貯蔵庫1内Co2濃度により、バルブ30〜3
7の開閉を行うと、吸着材38,39のCO2吸着能力
に応じて開閉時間が決定されるので、始めから吸着材3
5.39の長期信頼性を考慮して吸着器24.25の切
り替え時間を決定するのに比較して、切り替え時間が長
くとれ、又Co の吸着によるo2の貯蔵庫1内流入
量はバルブ3o〜37の開閉直後がたいへん多くしだい
に減少する傾向があるので、燃焼ガス中のCQ2吸着に
よる貯蔵庫1内への0□流入量は少なくなり、貯蔵庫1
内をすばやく所定雰囲気に調整することができる。In other words, depending on the Co2 concentration in the storage 1, the valves 30 to 3
When opening and closing 7, the opening and closing time is determined according to the CO2 adsorption capacity of the adsorbents 38 and 39, so the adsorbent 3
Compared to determining the switching time of the adsorbers 24 and 25 by considering the long-term reliability of 5.39, the switching time can be longer, and the amount of O2 flowing into the storage 1 due to the adsorption of Co is determined by the valves 3o to 3o. Since the amount of CQ2 flowing into the storage 1 due to CQ2 adsorption in the combustion gas decreases, the amount of CQ2 flowing into the storage 1 decreases.
The interior can be quickly adjusted to the desired atmosphere.
発明の効果
生鮮物を貯蔵する貯蔵庫と、この貯蔵庫内を冷却する冷
却装置と、前記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
送風装置とより成る炭酸ガス発生装置と、前記貯蔵庫内
の雰囲気を所定の値に調整する複数個の吸着器と、この
吸着器を再生せしめる送風装置とより成るガス調整装置
と、前記貯蔵庫の炭酸ガス濃度に応じて、吸着器を切り
替える制御装置とより成る生鮮物貯蔵装置であるため、
前記吸着器の炭酸ガス吸着能力により吸着器の切り替え
時間が決定されるので、始めから吸着器中の吸着材の長
期信頼性を考慮して切り替え時間を決定するのに比較し
て切り替え時間が長くとれ、又炭酸ガス吸着時における
酸素の貯蔵庫内への流入量は、吸着器の切り替え直後が
たいへん多くしだいに減少する傾向にあるため、酸素の
貯蔵庫内への流入量は少なくなり、貯蔵庫内をすばやく
所定の雰囲気に調整することができる効果が得られる。Effects of the Invention A storage for storing perishables, a cooling device for cooling the inside of the storage, a combustion furnace for burning fuel containing carbon to introduce carbon dioxide gas into the storage, and a combustion furnace for injecting the fuel into the storage. A carbon dioxide gas generator comprising a blower that circulates air for combustion from the storage, a plurality of adsorbers that adjust the atmosphere in the storage to a predetermined value, and a blower that regenerates the adsorbers. This is a fresh produce storage device consisting of a gas adjustment device consisting of a gas regulator, and a control device that switches the adsorber according to the carbon dioxide concentration in the storage.
Since the adsorber switching time is determined by the carbon dioxide adsorption capacity of the adsorber, the switching time is longer than if the switching time was determined by considering the long-term reliability of the adsorbent in the adsorber from the beginning. The amount of oxygen flowing into the storage during absorption and adsorption of carbon dioxide tends to be very high immediately after switching the adsorber, and then gradually decreases. The effect is that the atmosphere can be quickly adjusted to a predetermined atmosphere.
第1図は本発明の一実施例である生鮮物貯蔵装置の構成
図、第2図は、同装置の空気雰囲気及び装置作動図であ
る。
1・・・・・・貯蔵庫、7・・・・・・冷却装置、8・
・・・・・炭酸ガス発生装置%9・・・・・・ガス調整
装置215・・・・・・送風装置、1e・・・・・・燃
焼炉、24.25・・・・・・吸着器、29・・・・・
・送風装置、40・・・・・・吸着器を切り替える制御
装置。
代理人の氏名 弁理士 中 尾 敏 男 ほか1名/−
FLa、’1
7− 玲即躾!
8− 炭酸ガス発生装置
9− ガス調!E装置
15− 送息躾I
/6−j!!、+1ア
24.25−吸着器
6−送IL代置
荀−吸着5ヒWり臂λる利岬Ft置
第1図FIG. 1 is a block diagram of a fresh produce storage device according to an embodiment of the present invention, and FIG. 2 is a diagram showing the air atmosphere and operation of the device. 1...Storage, 7...Cooling device, 8.
...Carbon dioxide generator %9...Gas regulator 215...Blower, 1e...Combustion furnace, 24.25...Adsorption Vessel, 29...
・Blower device, 40... Control device for switching the adsorption device. Name of agent: Patent attorney Toshio Nakao and 1 other person/-
FLa, '1 7- Rei Immediate Discipline! 8- Carbon dioxide generator 9- Gas tone! E device 15- Breathing training I /6-j! ! ,+1A 24.25-Adsorber 6-Transfer IL substitution station-Adsorption 5 HiW arm λru Cape Ft location Fig. 1
Claims (1)
却装置と、前記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
送風装置とより成る炭酸ガス発生装置と、前記貯蔵庫内
の雰囲気を所定の値に調整する複数個の吸着器と、この
吸着器を再生せしめる送風装置とより成るガス調整装置
と、前記貯蔵庫の炭酸ガス濃度に応じて、吸着器を切り
替える制御装置とより成る生鮮物貯蔵装置。A storage for storing perishables, a cooling device for cooling the inside of the storage, a combustion furnace for burning fuel containing carbon to introduce carbon dioxide into the storage, and a combustion furnace for burning the fuel. A gas conditioning device comprising a carbon dioxide gas generation device comprising a blower device that circulates air from the storage, a plurality of adsorbers that adjust the atmosphere in the storage to a predetermined value, and a blower device that regenerates the adsorbers. A fresh produce storage device comprising: a device; and a control device that switches adsorbers depending on the carbon dioxide concentration in the storage.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61273360A JPS63126424A (en) | 1986-11-17 | 1986-11-17 | Apparatus for storing perishables |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61273360A JPS63126424A (en) | 1986-11-17 | 1986-11-17 | Apparatus for storing perishables |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS63126424A true JPS63126424A (en) | 1988-05-30 |
Family
ID=17526813
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP61273360A Pending JPS63126424A (en) | 1986-11-17 | 1986-11-17 | Apparatus for storing perishables |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS63126424A (en) |
-
1986
- 1986-11-17 JP JP61273360A patent/JPS63126424A/en active Pending
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