JPH0348773B2 - - Google Patents
Info
- Publication number
- JPH0348773B2 JPH0348773B2 JP26130786A JP26130786A JPH0348773B2 JP H0348773 B2 JPH0348773 B2 JP H0348773B2 JP 26130786 A JP26130786 A JP 26130786A JP 26130786 A JP26130786 A JP 26130786A JP H0348773 B2 JPH0348773 B2 JP H0348773B2
- Authority
- JP
- Japan
- Prior art keywords
- combustion
- carbon dioxide
- carbon
- fuel
- temperature
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 72
- 238000002485 combustion reaction Methods 0.000 claims description 63
- 239000000446 fuel Substances 0.000 claims description 40
- 229910002092 carbon dioxide Inorganic materials 0.000 claims description 36
- 239000001569 carbon dioxide Substances 0.000 claims description 36
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 34
- 229910052799 carbon Inorganic materials 0.000 claims description 32
- 239000003054 catalyst Substances 0.000 claims description 12
- 238000000746 purification Methods 0.000 claims description 12
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 12
- 229910002091 carbon monoxide Inorganic materials 0.000 description 12
- 239000007789 gas Substances 0.000 description 12
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 11
- 229910052760 oxygen Inorganic materials 0.000 description 11
- 239000001301 oxygen Substances 0.000 description 11
- 238000006243 chemical reaction Methods 0.000 description 9
- 239000000567 combustion gas Substances 0.000 description 5
- 230000007423 decrease Effects 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 230000003247 decreasing effect Effects 0.000 description 2
- 125000004430 oxygen atom Chemical group O* 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 238000004378 air conditioning Methods 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 230000029058 respiratory gaseous exchange Effects 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Landscapes
- Storage Of Fruits Or Vegetables (AREA)
- Storage Of Harvested Produce (AREA)
Description
【発明の詳細な説明】
産業上の利用分野
本発明は、生鮮物の置かれている雰囲気の空気
組成を調節することにより、呼吸作用や微生物、
酸素などの活動を抑制する貯蔵装置として、生鮮
物貯蔵の分野に利用される。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention improves respiration and microorganisms by adjusting the air composition of the atmosphere in which fresh food is placed.
It is used in the field of fresh food storage as a storage device that suppresses the activity of oxygen and other substances.
従来の技術
従来の貯蔵装置は、例えば加藤薫「新しい資源
方式CA貯蔵システムについて」(空気調和と冷凍
1974−7P191)に示されるように、第3図のよう
な構成になつていた。 Conventional technology Conventional storage devices are used, for example, in Kaoru Kato's ``About a new resource-based CA storage system'' (air conditioning and refrigeration).
1974-7P191), the structure was as shown in Figure 3.
すなわち、ボンベ等より供給された燃料と循環
用送風機1により、冷蔵庫2から供給された空気
3が混合し、二酸化炭素発生装置4内で燃焼して
二酸化炭素を発生させる。そして二酸化炭素発生
装置4で発生した二酸化炭素は冷蔵庫2へ供給さ
れるために、冷蔵庫2内の酸素を減少し、二酸化
炭素を増加する。二酸化炭素濃度が設定値になれ
ばスクラバ5を運転し、過剰な二酸化炭素を吸着
する。次に酸素濃度が設定値になれば、二酸化炭
素発生装置4を停止し、酸素補給用送風機6を運
転して、生鮮物の置かれている雰囲気の空気組成
を一定に保つようにして、生鮮物の貯蔵を行うも
のである。 That is, fuel supplied from a cylinder or the like is mixed with air 3 supplied from the refrigerator 2 by the circulation blower 1, and the mixture is combusted in the carbon dioxide generator 4 to generate carbon dioxide. Since the carbon dioxide generated by the carbon dioxide generator 4 is supplied to the refrigerator 2, oxygen in the refrigerator 2 is decreased and carbon dioxide is increased. When the carbon dioxide concentration reaches the set value, the scrubber 5 is operated to adsorb excess carbon dioxide. Next, when the oxygen concentration reaches the set value, the carbon dioxide generator 4 is stopped and the oxygen supply blower 6 is operated to maintain a constant air composition in the atmosphere in which the perishables are placed. It is used to store things.
発明が解決しようとする問題点
しかしこのような構造の生鮮物貯蔵装置の燃料
に石油系のガス燃料を用いると、排気ガス中に多
量の水蒸気を含むために、この水浄気を凝縮させ
るために非常に大きな凝縮器が必要になるという
問題があつた。Problems to be Solved by the Invention However, when petroleum-based gas fuel is used as fuel for a perishables storage device with such a structure, the exhaust gas contains a large amount of water vapor, and this water vapor must be condensed. The problem was that a very large condenser was required.
そこで燃料に炭素燃料を用いると水蒸気の発生
という問題を避けることができる。しかし、燃焼
が経過していくにつれ、冷蔵庫2内の酸素濃度が
低下し、燃焼に使用できる酸素量が減少していく
ために、燃料消費量が減少する。そこで二酸化炭
素発生装置4の下流に空気予熱器を設け、燃焼温
度を低下することなく循環機空気量を増加するこ
とにより、燃料消費量の減少を防いでいる。 Therefore, if carbon fuel is used as fuel, the problem of water vapor generation can be avoided. However, as the combustion progresses, the oxygen concentration within the refrigerator 2 decreases, and the amount of oxygen that can be used for combustion decreases, resulting in a decrease in fuel consumption. Therefore, an air preheater is provided downstream of the carbon dioxide generator 4 to increase the amount of air in the circulator without lowering the combustion temperature, thereby preventing a decrease in fuel consumption.
ところが、この様な燃焼炉では燃焼初期に炭素
燃料の上層部の温度がまだ低いために、燃焼開始
後しばらくの間、燃焼炉からは一酸化炭素を大量
に含んだ低温の燃焼ガスが排出される。このため
に、せつかく二酸化炭素発生装置4の下流に設け
た空気予熱器が能力を十分に発揮できず、燃焼炉
内の温度が安定し、安定した燃焼が行えるまでに
長時間を要するという新たな問題が生じてきた。 However, in such a combustion furnace, the temperature of the upper layer of the carbon fuel is still low at the beginning of combustion, so low-temperature combustion gas containing a large amount of carbon monoxide is discharged from the combustion furnace for a while after combustion starts. Ru. For this reason, the air preheater installed downstream of the carbon dioxide generator 4 cannot fully demonstrate its capacity, and it takes a long time to stabilize the temperature inside the combustion furnace and perform stable combustion. A problem has arisen.
本発明は簡単な構成で、燃焼開始直後から空気
予熱器の能力を最大限に活用し、燃焼炉が短時間
で安定した燃焼を行える生鮮物貯蔵装置を提供す
るものである。 The present invention provides a perishables storage device which has a simple configuration, makes full use of the capacity of the air preheater immediately after the start of combustion, and allows the combustion furnace to perform stable combustion in a short period of time.
問題点を解決するための手段
そこで、本発明は、二酸化炭素発生装置の下流
に浄化用触媒を設け、さらに浄化用触媒の下流に
空気予熱器を設けるものである。Means for Solving the Problems Accordingly, the present invention provides a purification catalyst downstream of the carbon dioxide generator, and further provides an air preheater downstream of the purification catalyst.
作 用 この技術的手段による作用は次のようになる。Effect The effect of this technical means is as follows.
二酸化炭素発生装置の下流に浄化用触媒を設
け、その下流に設けることにより、燃焼炉から供
給される一酸化炭素を大量に含んだ低温の燃焼ガ
スが、浄化用触媒で一酸化炭素が二酸化炭素に変
換する発熱反応により、高温になつて空気予熱器
に供給される。このために空気予熱器の能力を最
大限に引き出すことができ、空気予熱器で熱交換
された高温の燃焼用空気を燃焼炉に供給すること
ができる。この高温の燃焼用空気が炭素燃料の燃
料温度を高め、反応を激しくするために、燃焼炉
内の温度が早く安定し、燃焼が安定する時間を大
幅に短縮することができる。 A purification catalyst is provided downstream of the carbon dioxide generator, and by installing it downstream, the low temperature combustion gas containing a large amount of carbon monoxide supplied from the combustion furnace is converted to carbon monoxide by the purification catalyst. The exothermic reaction converts the air to a high temperature, which is then fed to the air preheater. For this reason, the capacity of the air preheater can be maximized, and high-temperature combustion air that has undergone heat exchange with the air preheater can be supplied to the combustion furnace. This high-temperature combustion air raises the temperature of the carbon fuel and intensifies the reaction, so the temperature inside the combustion furnace stabilizes quickly and the time it takes for combustion to stabilize can be significantly shortened.
実施例
以下、本発明の一実施例を添付図面に基づいて
説明する。Embodiment Hereinafter, an embodiment of the present invention will be described based on the accompanying drawings.
第1図において、二酸化炭素発生装置7の燃焼
炉8を仕切るように火格子9を設け、その上に炭
素燃料10を供給する。また火格子9の下には電
熱ヒータ11が設けてある。始動時に電熱ヒータ
11に通電し、炭素燃料10が燃焼するのに十分
な温度まで加熱した時点で、循環用送風機12を
運転し、燃焼炉8に燃焼用空気を供給する。炭素
燃料10はすでに十分に加熱されているので、空
気が炭素燃料10に接触するや否や燃焼を開始す
る。この時の燃焼量は炭素燃料10の表面積と、
炭素燃料10に供給される酸素量で決定される。 In FIG. 1, a fire grate 9 is provided to partition a combustion furnace 8 of a carbon dioxide generator 7, and a carbon fuel 10 is supplied onto the fire grate 9. Further, an electric heater 11 is provided below the grate 9. At the time of startup, the electric heater 11 is energized, and when the carbon fuel 10 is heated to a temperature sufficient for combustion, the circulation blower 12 is operated to supply combustion air to the combustion furnace 8. Since the carbon fuel 10 is already sufficiently heated, combustion begins as soon as air contacts the carbon fuel 10. The amount of combustion at this time is the surface area of carbon fuel 10,
It is determined by the amount of oxygen supplied to the carbon fuel 10.
二酸化炭素発生装置7で発生した多量の二酸化
炭素を含む高温の排ガスは、浄化用触媒13で浄
化され、空気予熱器14に供給される。この空気
予熱器14において、排ガスは燃焼用空気と熱交
換され、燃焼用空気を予熱したのちに冷却器15
へ供給される。そして冷却器15で冷却された排
ガスはスクラバ16を通つて冷蔵庫17へ供給さ
れる。そしてこのことより酸素濃度が低下した空
気は、再び循環用送風機12により燃焼炉8へ供
給される。このサイクルは冷蔵庫17内の二酸化
炭素濃度が設定値になるまで続けられる。 High-temperature exhaust gas containing a large amount of carbon dioxide generated by the carbon dioxide generator 7 is purified by a purification catalyst 13 and supplied to an air preheater 14 . In this air preheater 14, the exhaust gas is heat exchanged with the combustion air, and after preheating the combustion air, the exhaust gas is heated in the cooler 15.
supplied to The exhaust gas cooled by the cooler 15 is supplied to the refrigerator 17 through the scrubber 16. Then, the air whose oxygen concentration has decreased due to this is supplied to the combustion furnace 8 again by the circulation blower 12. This cycle continues until the carbon dioxide concentration within the refrigerator 17 reaches the set value.
スクラバ16は、たとえば内部に活性炭などを
充填した二酸化炭素吸着層と吸着した二酸化炭素
を脱着する再生装置とバイパス経路とを有するも
のである。冷蔵庫17を設けたガスセンサ(図示
せず)からの信号により、冷蔵庫17内の二酸化
炭素濃度が設定値に達したことを検出すると、ス
クラバ16を運転し、設定値を保つように燃焼に
より発生した過剰な二酸化炭素を吸着し続ける。
冷蔵庫17内のガスセンサからの信号により、冷
蔵庫17内の酸素濃度が設定値に達したことを検
出すると、二酸化炭素発生装置7、循環用送風機
12、スクラバ16を停止する。以後は貯蔵して
いる生鮮物が呼吸することにより消費した酸素
は、酸素供給用送風機18より大気中の酸素を冷
蔵庫17へ供給し、生鮮物が呼吸することにより
発生した二酸化炭素はスクラバ16により吸着す
ることにより、冷蔵庫17内の空気組成を設定値
に保ち続ける。 このような構成の本発明の実施
例の具体的な動作関係について以下に説明する。 The scrubber 16 has, for example, a carbon dioxide adsorption layer filled with activated carbon or the like, a regenerator for desorbing the adsorbed carbon dioxide, and a bypass path. When it is detected by a signal from a gas sensor (not shown) provided in the refrigerator 17 that the concentration of carbon dioxide in the refrigerator 17 has reached the set value, the scrubber 16 is operated to maintain the set value of the carbon dioxide generated by combustion. Continues to adsorb excess carbon dioxide.
When it is detected by the signal from the gas sensor in the refrigerator 17 that the oxygen concentration in the refrigerator 17 has reached a set value, the carbon dioxide generator 7, circulation blower 12, and scrubber 16 are stopped. Thereafter, the oxygen consumed by the stored perishables when they breathe is supplied from the oxygen supply blower 18 to the refrigerator 17, and the carbon dioxide generated when the perishables breathe is removed by the scrubber 16. By adsorption, the air composition within the refrigerator 17 is maintained at the set value. The specific operational relationship of the embodiment of the present invention having such a configuration will be described below.
炭素燃料の燃焼というものは、炭素燃料の表面
に炭素が接触すると、炭素燃料の表面で、炭素原
子が酸素原子と結び付いて一酸化炭素を発生する
反応が起こる。続いて炭素燃料の表面近傍で、一
酸化炭素と酸素原子が結び付いて二酸化炭素を発
生するという反応が気相で起こる。特に後者の反
応は高温の気相で起こるために、この反応が起き
ている燃焼ガスが低温の部分に触れると、二酸化
炭素に変化する反応が止まり、一酸化炭素が発生
する。 In combustion of carbon fuel, when carbon comes into contact with the surface of the carbon fuel, a reaction occurs where carbon atoms combine with oxygen atoms to generate carbon monoxide. Next, near the surface of the carbon fuel, a reaction occurs in the gas phase in which carbon monoxide and oxygen atoms combine to generate carbon dioxide. In particular, the latter reaction occurs in the high-temperature gas phase, so when the combustion gas undergoing this reaction comes into contact with a cold area, the reaction that changes it to carbon dioxide stops, and carbon monoxide is generated.
第2図に予熱開始から燃焼開始直後までの炭素
燃料10の温度変化を示す。この図より、燃焼部
に多量の炭素燃料を供給すると、燃焼部内にある
全ての炭素燃料を燃焼可能な状態まで予熱するの
に、非常に長時間の予熱が必要になることがわか
る。そこで、炭素燃料10の下層の温度が燃焼可
能な温度になつたときに、燃焼用空気を燃焼部に
供給して燃焼を行うようにして燃焼を開始する
と、燃焼炉8の下部の炭素燃料(第2図a)は燃
焼を行うほど温度が高いにもかかわらず、燃焼炉
8の上部の炭素燃料(第2図c)は、中間の炭素
燃料(第2図b)に予熱時の熱量を奪われている
ので、予熱中に熱量の供給が砲どなく、非常に低
温であることがわかる。このために燃焼が開始し
た燃焼炉8下部の炭素燃料(第2図a)の燃焼ガ
スが低温の炭素燃料に触れると、一酸化炭素が二
酸化炭素に変化する反応が停止し、発生する炭素
燃料の燃焼反応のうちで、一酸化炭素が多量に発
生する。特に燃えにくい高温焼結した炭素燃料を
燃料として用いた場合には、焼結していない炭素
燃料よりも、一酸化炭素の発生量はかなり多くな
り、燃焼炉が安定するのに要する時間も長くな
る。一酸化炭素の発生を抑えるためには、なるべ
く早く燃焼炉8上部の炭素燃料の温度を高め、燃
焼を安定させればよい。 FIG. 2 shows the temperature change of the carbon fuel 10 from the start of preheating to immediately after the start of combustion. From this figure, it can be seen that when a large amount of carbon fuel is supplied to the combustion section, a very long period of preheating is required to preheat all the carbon fuel in the combustion section to a combustible state. Therefore, when the temperature of the lower layer of the carbon fuel 10 reaches a combustible temperature, if combustion air is supplied to the combustion section and combustion is started, the carbon fuel ( Although the temperature in Fig. 2 a) is high enough to cause combustion, the carbon fuel in the upper part of the combustion furnace 8 (Fig. 2 c) has a heat value during preheating of the carbon fuel in the middle (Fig. 2 b). As the temperature is being taken away, there is no supply of heat during preheating, and the temperature is extremely low. For this reason, when the combustion gas of the carbon fuel (Fig. 2 a) at the bottom of the combustion furnace 8 where combustion has started comes into contact with the low-temperature carbon fuel, the reaction in which carbon monoxide changes to carbon dioxide stops, and the carbon fuel generated During the combustion reaction, a large amount of carbon monoxide is generated. In particular, when high-temperature sintered carbon fuel, which is less flammable, is used as fuel, the amount of carbon monoxide produced is considerably higher than that of unsintered carbon fuel, and the time required for the combustion furnace to stabilize is longer. Become. In order to suppress the generation of carbon monoxide, the temperature of the carbon fuel in the upper part of the combustion furnace 8 should be raised as quickly as possible to stabilize combustion.
そこで本発明では、二酸化炭素発生装置7の下
流に浄化用触媒13を設け、その下流に空気予熱
器14を設けることにより、燃焼炉8から供給さ
れる一酸化炭素を大量に含んだ低温の燃焼ガス
が、浄化用触媒13で一酸化炭素が二酸化炭素に
変換する発熱反応により、高温になつて空気予熱
器14に供給される。このために空気予熱器14
に供給される燃焼ガスは、従来の装置に比べては
るかに高温になつているので、空気予熱器14の
能力を最大限に引き出すことができ、燃焼用空気
を空気予熱器14で高温に熱交換して燃焼炉8に
供給することができる。この高温の燃焼用空気が
炭素燃料10の燃焼反応を激しくするために、燃
焼炉8上部の炭素燃料が短時間で高温になり、燃
焼炉8内の温度が早く安定し、燃焼が安定する時
間を大幅に短縮することができる。 Therefore, in the present invention, by providing a purification catalyst 13 downstream of the carbon dioxide generator 7 and an air preheater 14 downstream thereof, low-temperature combustion containing a large amount of carbon monoxide supplied from the combustion furnace 8 is achieved. The gas is heated to a high temperature by an exothermic reaction in which carbon monoxide is converted to carbon dioxide in the purification catalyst 13 and then supplied to the air preheater 14 . For this purpose, the air preheater 14
Since the combustion gas supplied to the combustion chamber is at a much higher temperature than that of conventional devices, the capacity of the air preheater 14 can be maximized, and the combustion air is heated to a high temperature by the air preheater 14. It can be replaced and supplied to the combustion furnace 8. Since this high-temperature combustion air intensifies the combustion reaction of the carbon fuel 10, the carbon fuel in the upper part of the combustion furnace 8 becomes high temperature in a short period of time, and the temperature inside the combustion furnace 8 quickly stabilizes, resulting in stable combustion. can be significantly shortened.
特に、燃えにくい高温焼結した炭素燃料を燃料
として用いた場合には、焼結していない炭素燃料
を燃料として用いた場合より以上に、燃焼炉での
燃焼が安定する時間を大幅に短縮することができ
る。 In particular, when high-temperature sintered carbon fuel, which is difficult to burn, is used as fuel, the time required for combustion to stabilize in the combustion furnace is significantly shorter than when unsintered carbon fuel is used as fuel. be able to.
発明の効果
本発明は、二酸化炭素発生装置の下流に浄化用
触媒を設け、さらに浄化用触媒の下流に前記二酸
化炭素発生装置からの排ガスと燃焼用空気を熱交
換する空気予熱器を設けることにより、燃焼開始
直後から空気予熱器の能力を最大限に活用し、燃
焼炉での燃焼が安定する時間を大幅に短縮するこ
とができる。Effects of the Invention The present invention provides a purification catalyst downstream of a carbon dioxide generator, and further provides an air preheater downstream of the purification catalyst for exchanging heat between exhaust gas from the carbon dioxide generator and combustion air. , the ability of the air preheater can be fully utilized immediately after the start of combustion, greatly shortening the time it takes for combustion to stabilize in the combustion furnace.
第1図は本発明の一実施例の生鮮物貯蔵装置の
概略図、第2図は炭素燃料の温度の時間特性図、
第3図は従来の生鮮物貯蔵装置の概略図である。
7……二酸化炭素発生装置、8……燃焼炉、1
3……浄化用触媒、14……空気予熱器。
FIG. 1 is a schematic diagram of a perishables storage device according to an embodiment of the present invention, FIG. 2 is a time characteristic diagram of the temperature of carbon fuel,
FIG. 3 is a schematic diagram of a conventional fresh produce storage device. 7... Carbon dioxide generator, 8... Combustion furnace, 1
3... Purification catalyst, 14... Air preheater.
Claims (1)
燃焼することにより二酸化炭素を前記冷蔵庫に供
給する二酸化炭素発生装置と、燃焼用空気として
前記冷蔵庫内の空気を循環して前記二酸化炭素発
生装置に供給する循環用送風機とを有し、前記二
酸化炭素発生装置の下流に浄化用触媒を設け、前
記浄化用触媒の下流に前記二酸化炭素発生装置か
らの排ガスと燃焼用空気を熱交換する空気予熱器
を設けたことを特徴とする生鮮物貯蔵装置。1. A refrigerator, a carbon dioxide generator that supplies carbon dioxide to the refrigerator by burning carbon fuel in a combustion section provided inside the refrigerator, and a carbon dioxide generator that circulates air within the refrigerator as combustion air. A purification catalyst is provided downstream of the carbon dioxide generator, and air preheating is provided downstream of the purification catalyst to exchange heat between exhaust gas from the carbon dioxide generator and combustion air. A fresh food storage device characterized by being equipped with a container.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61261307A JPS63112919A (en) | 1986-10-31 | 1986-10-31 | perishable storage equipment |
| KR1019870012146A KR900003723B1 (en) | 1986-10-31 | 1987-10-30 | Apparatus for preservation of fishes |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61261307A JPS63112919A (en) | 1986-10-31 | 1986-10-31 | perishable storage equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63112919A JPS63112919A (en) | 1988-05-18 |
| JPH0348773B2 true JPH0348773B2 (en) | 1991-07-25 |
Family
ID=17359972
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP61261307A Granted JPS63112919A (en) | 1986-10-31 | 1986-10-31 | perishable storage equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS63112919A (en) |
-
1986
- 1986-10-31 JP JP61261307A patent/JPS63112919A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS63112919A (en) | 1988-05-18 |
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