JP3826560B2 - Refrigeration unit with freshness maintaining device - Google Patents

Refrigeration unit with freshness maintaining device Download PDF

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Publication number
JP3826560B2
JP3826560B2 JP10439398A JP10439398A JP3826560B2 JP 3826560 B2 JP3826560 B2 JP 3826560B2 JP 10439398 A JP10439398 A JP 10439398A JP 10439398 A JP10439398 A JP 10439398A JP 3826560 B2 JP3826560 B2 JP 3826560B2
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Japan
Prior art keywords
refrigerant
passage
freshness
ethylene
catalyst
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JP10439398A
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JPH11294936A (en
Inventor
晃一 達
伸浩 柳沢
尚孝 山本
誠一路 木藤
宗侯 長谷川
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Isuzu Motors Ltd
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Isuzu Motors Ltd
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Description

【0001】
【発明の属する技術分野】
本発明はエチレンガス分解機構を有する鮮度保持装置を備えた冷蔵装置に関する。
【0002】
【従来の技術】
鮮度保持装置において、青果物,花き等の鮮度を保持するために、鮮度の劣化に関与しているエチレンガスを分解除去する触媒を用いていた。
エチレンガス除去に用いられている触媒は数種類の触媒があるが、いずれの触媒においてもエチレンガスの吸着、分解反応を利用している。
これらの装置は冷凍車等の低温環境に設置した場合、エチレン吸着効率は良いがエチレンの分解反応、および分解物の脱離においては低温のため効率が悪かった。
【0003】
そこで、エチレンの分解反応効率を向上させるため、特開平8−5228号公報に、空気の流下方向に直角にエチレン除去脱臭シートと加熱ヒータを備えたエチレン除去脱臭装置が開示されている。
また、特開平5−277326号公報には、ダクトを流下する空気中のエチレンを吸着する吸着材と、その上流側に配設する温度制御装置とを備え、吸着材を冷却、または加熱することにより吸着材のエチレン吸着量を増減させる雰囲気制御装置が開示されている。
【0004】
【発明が解決しようとする課題】
しかし、上記開示されている装置は、触媒を加熱させるための加熱手段を新たに配設しており、装置全体を大型化すると共に、エネルギーコストを増加させていた。
そこで、この発明はエチレンガス吸着効率、およびエチレンガスの分解効率がよく、かつ装置の小型化を達成できる鮮度保持装置を提供するものである。
【0005】
【課題を解決するための手段】
本発明の鮮度保持装置付きの冷蔵装置は、コンプレッサーとコンデンサーとエバポレータとの間に配設する冷媒の通路に冷媒を循環させて、高温高圧から低温低圧に換える冷凍サイクルを構成すると共に、コンプレッサーから流出する高温高圧冷媒の通路に、鮮度保持装置に連絡する冷媒の循環通路を形成する構成を具備する。
鮮度保持装置に連絡する冷媒の循環通路は、通路の開閉手段を備え、エチレン吸着分解触媒の上流側を通過する構成を有する。
【0006】
【発明の実施の形態】
本発明の鮮度保持装置付き冷蔵装置の実施の形態を図面を参照して説明する。
図1は鮮度保持装置付きの冷蔵装置の機構説明図、図2は鮮度保持装置の斜視図である。
【0007】
冷蔵装置1は冷媒を圧縮するコンプレッサー10と、圧縮された冷媒を凝縮するコンデンサー20と、コンデンサー20からの冷媒を蒸発させるエバポレータ30を有する。
コンプレッサー10から流出するガス冷媒は、第1の冷媒通路15からコンデンサ20に流入し液化される。コンデンサ20から流出する液体冷媒は第2の冷媒通路25から、エバポレータ30に流入し周囲の熱を奪ってガス化される。ガス冷媒は第3の冷媒通路35を通ってコンプレッサー10に流入し圧縮されて第1の冷媒通路15から、循環される。
【0008】
第1の冷媒通路15には通路切換器50を介して鮮度保持装置40に通づる第4の冷媒通路45を配設する。
第4の冷媒通路45は第1の冷媒通路15から冷媒が鮮度保持装置40に流入する流入側通路45Aと、鮮度保持装置40から流出する冷媒を第1の冷媒通路15に戻す流出側通路45Bを有する。
冷媒は第1の通路15の分岐点17から流入側通路45Aを通って鮮度保持装置40に流入し、流出側通路45Bを通って、分岐点19から第1の冷媒通路15に流入し循環するように配設されている。
【0009】
通路切換器50は流入側通路45Aの第1の冷媒通路15近辺に配設する第1のバルブ51、流出側通路45Bの第1の冷媒通路15近辺に配設する第2のバルブ53と、第1の冷媒通路15の分岐点17と分岐点19との間の第1の通路15に配設する第3のバルブ55を備えている。各バルブ51,53,55は開閉制御装置60により開閉が制御されている。
【0010】
鮮度保持装置40はエチレンを除去、分解する触媒を内在させる触媒部41を有している。
触媒部41の触媒は、エチレンを吸着する吸着剤としての活性炭と、エチレンの分解触媒としての白金、パラジウム、酸化チタン等を練り込んで混合したものを用いている。
なお、エチレンの分解は、分解触媒による酸化反応で炭酸ガスと水に分解されるが、分解反応を活性化させてより分解を促進させるために、オゾンを付与させることもある。
【0011】
触媒部41の表面にはその全面に第4の冷媒通路45を延設した冷媒細管部450を配設する。
冷媒細管部450は、例えば図2に示すように、第4の冷媒通路45を形成する配管サイズよりその管径を細くした細径管を蛇行させて触媒部41の配設部分の全面を被覆するように配設する。冷媒細管部450は鮮度保持装置40の触媒部41に対して風流入側に配置する。
【0012】
通路切換器50の制御装置60は、第1のバルブ51,第2のバルブ53、第3のバルブ55の開閉を制御している。
例えば、第1のバルブ51と第2のバルブ53を解放し、第3のバルブ55を閉鎖する。この状態で、コンプレッサー10から流出した冷媒は第1の冷媒通路15から第4の冷媒通路45に流入し、流入側通路45Aから鮮度保持装置40の細管部450を通って、流出側通路45Bから第1の冷媒通路15に循環し、コンデンサー20に流入する。
このとき、コンプレッサー10で圧縮された冷媒は高温高圧となっているので、高温の冷媒は第4の冷媒通路45から触媒部41の全面を通って、低温の触媒部41の触媒を温め、流出側通路45Bから第1の冷媒通路15に戻る。
一定時間経過すると、第3のバルブ55を開き、第1と第2のバルブ51,53を閉鎖する。
この状態でコンプレッサー10からの圧縮された高温の冷媒は第1の冷媒通路15を通ってコンデンサー20に流入し、通常の冷媒の循環を実行する。
【0013】
この冷蔵装置1は、鮮度保持装置40を冷雰囲気中に設置しているので、矢印方向からの空気に含まれるエチレンを触媒部41で効率良く吸着する。
そして、制御装置60は一定時間毎に圧縮された高温の冷媒を鮮度保持装置40の触媒部41に循環させる。鮮度保持装置40の触媒部41は触媒温度が上昇し、エチレンの分解、および分解物の離脱が促進される。細管部450による温度の上昇は矢印方向に流れる風により触媒部41の内部に進行し、触媒部41全体の温度上昇を促しエチレンの分解、離脱をさらに進行させる。
【0014】
このように、制御装置60の通路切換器50の一連のバルブ開閉制御により、鮮度保持装置40の触媒の表面温度が一定間隔で低温、高温を繰返し、効率的にエチレンの吸着、分解を実行し、エチレン除去能力を向上させる。
なお、この実施の形態では制御装置はバルブの開閉を時間によって制御する例を説明したが、温度、濃度等による制御としても同様の効果を達成する。
【0015】
(実施例)
次に、鮮度保持装置40を備えた冷蔵装置をコンテナに配設する実施例を説明する(図3参照)。
冷蔵コンテナ100には、冷蔵装置1と鮮度保持装置40を配設している。
冷蔵装置1はコンテナ100の外部に配設するコンプレッサー10と、コンテナ100内に配設するコンデンサー20とエバポレータ30等を装備している。
エバポレータ30は冷蔵コンテナ10内の空気を取り入れて除湿と冷却を達成して、乾燥した冷気を放出する。
【0016】
鮮度保持装置40はエバポレータ30の上流側に配設される。
鮮度保持装置40は流入するコンテナ100内の空気のエチレンガスを吸着し、分解して、コンテナ内のエチレンガスを除去する。
鮮度保持装置40は冷蔵装置1の冷媒通路15から分岐する第4の冷媒通路45で冷蔵装置1の冷媒循環系に連絡している。
【0017】
第4の冷媒通路45が切換器50により第1の冷媒通路15に連絡したとき、コンプレッサー10から流出する高温に圧縮された冷媒は、第4の冷媒通路45から鮮度保持装置40内に流入し、鮮度保持装置40内に収容されている触媒を加熱させ、触媒に吸着しているエチレンの分解を促進させる。
また、この状態で一定時間経過すると切換器50が切り替わり、コンプレッサー10からの冷媒は鮮度保持装置40を経由せずにコンデンサー20に流入する。この間、鮮度保持装置40の触媒は冷雰囲気中で冷され、エチレンの吸着を実行する。
【0018】
【発明の効果】
本発明の鮮度保持装置付きの冷蔵装置は、触媒の加熱、冷却が達成されエチレンガス吸着効率、およびエチレンガスの分解効率がよい。さらに、加熱装置等の特別な装置を配設する必要がなく、装置の小型化を達成できる。
【図面の簡単な説明】
【図1】本発明に係る鮮度保持装置付きの冷蔵装置の構成説明図。
【図2】鮮度保持装置の斜視図。
【図3】冷蔵コンテナに配設される鮮度保持装置付き冷蔵装置の概略図。
【符号の説明】
10 コンプレッサー
15 第1の冷媒通路
20 コンデンサー
25 第2の冷媒通路
30 エバポレータ
35 第3の冷媒通路
40 鮮度保持装置
41 触媒部
50 切換装置
51,53,55 バルブ
60 制御装置
450 細管部
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a refrigeration apparatus including a freshness maintaining apparatus having an ethylene gas decomposition mechanism.
[0002]
[Prior art]
In order to maintain the freshness of fruits and vegetables, etc. in the freshness maintaining device, a catalyst that decomposes and removes ethylene gas involved in the deterioration of freshness has been used.
There are several types of catalysts used for removing ethylene gas, and any of these catalysts utilizes ethylene gas adsorption and decomposition reactions.
When these devices are installed in a low-temperature environment such as a refrigerator, the ethylene adsorption efficiency is good, but the ethylene decomposition reaction and the decomposition product desorption are inefficient due to the low temperature.
[0003]
In order to improve the decomposition reaction efficiency of ethylene, Japanese Patent Application Laid-Open No. 8-5228 discloses an ethylene removal and deodorization apparatus provided with an ethylene removal and deodorization sheet and a heater perpendicular to the air flow direction.
Japanese Patent Application Laid-Open No. 5-277326 includes an adsorbent that adsorbs ethylene in the air flowing down the duct and a temperature control device disposed upstream thereof, and cools or heats the adsorbent. Discloses an atmosphere control device for increasing or decreasing the ethylene adsorption amount of the adsorbent.
[0004]
[Problems to be solved by the invention]
However, the above-disclosed apparatus is newly provided with heating means for heating the catalyst, increasing the size of the entire apparatus and increasing the energy cost.
Accordingly, the present invention provides a freshness maintaining device that has good ethylene gas adsorption efficiency and ethylene gas decomposition efficiency, and can achieve downsizing of the device.
[0005]
[Means for Solving the Problems]
The refrigeration apparatus with a freshness maintaining device of the present invention constitutes a refrigeration cycle in which a refrigerant is circulated through a refrigerant passage disposed between a compressor, a condenser, and an evaporator to change from a high temperature and a high pressure to a low temperature and a low pressure. A configuration is provided in which a refrigerant circulation passage communicating with the freshness maintaining device is formed in the passage of the high-temperature and high-pressure refrigerant flowing out.
The refrigerant circulation passage communicating with the freshness maintaining device includes a passage opening / closing means, and has a configuration passing through the upstream side of the ethylene adsorption / decomposition catalyst.
[0006]
DETAILED DESCRIPTION OF THE INVENTION
An embodiment of a refrigeration apparatus with a freshness maintaining apparatus of the present invention will be described with reference to the drawings.
FIG. 1 is a mechanism explanatory view of a refrigeration apparatus with a freshness holding device, and FIG. 2 is a perspective view of the freshness holding device.
[0007]
The refrigeration apparatus 1 includes a compressor 10 that compresses a refrigerant, a condenser 20 that condenses the compressed refrigerant, and an evaporator 30 that evaporates the refrigerant from the condenser 20.
The gas refrigerant flowing out of the compressor 10 flows into the condenser 20 from the first refrigerant passage 15 and is liquefied. The liquid refrigerant flowing out of the condenser 20 flows into the evaporator 30 from the second refrigerant passage 25, takes away the surrounding heat, and is gasified. The gas refrigerant flows into the compressor 10 through the third refrigerant passage 35, is compressed, and is circulated from the first refrigerant passage 15.
[0008]
The first refrigerant passage 15 is provided with a fourth refrigerant passage 45 that communicates with the freshness maintaining device 40 via a passage switch 50.
The fourth refrigerant passage 45 includes an inflow side passage 45A through which the refrigerant flows from the first refrigerant passage 15 into the freshness maintaining device 40, and an outflow side passage 45B through which the refrigerant flowing out from the freshness holding device 40 is returned to the first refrigerant passage 15. Have
The refrigerant flows from the branch point 17 of the first passage 15 through the inflow side passage 45A into the freshness maintaining device 40, passes through the outflow side passage 45B, flows from the branch point 19 into the first refrigerant passage 15 and circulates. It is arranged like this.
[0009]
The passage switch 50 includes a first valve 51 disposed in the vicinity of the first refrigerant passage 15 of the inflow side passage 45A, a second valve 53 disposed in the vicinity of the first refrigerant passage 15 of the outflow side passage 45B, A third valve 55 disposed in the first passage 15 between the branch point 17 and the branch point 19 of the first refrigerant passage 15 is provided. Each valve 51, 53, 55 is controlled to be opened and closed by an opening / closing control device 60.
[0010]
The freshness maintaining device 40 has a catalyst unit 41 that contains a catalyst for removing and decomposing ethylene.
As the catalyst of the catalyst part 41, activated carbon as an adsorbent that adsorbs ethylene and platinum, palladium, titanium oxide or the like as an ethylene decomposition catalyst are kneaded and mixed.
In addition, although ethylene is decomposed into carbon dioxide gas and water by an oxidation reaction by a decomposition catalyst, ozone may be applied in order to activate the decomposition reaction and further promote decomposition.
[0011]
On the surface of the catalyst portion 41, a refrigerant thin tube portion 450 having a fourth refrigerant passage 45 extending over the entire surface is disposed.
For example, as shown in FIG. 2, the refrigerant thin tube portion 450 covers the entire surface of the portion where the catalyst portion 41 is disposed by meandering a thin tube whose diameter is smaller than the pipe size forming the fourth refrigerant passage 45. It arrange | positions so that it may do. The refrigerant thin tube portion 450 is disposed on the wind inflow side with respect to the catalyst portion 41 of the freshness maintaining device 40.
[0012]
The control device 60 of the passage switch 50 controls the opening / closing of the first valve 51, the second valve 53, and the third valve 55.
For example, the first valve 51 and the second valve 53 are released, and the third valve 55 is closed. In this state, the refrigerant that has flowed out of the compressor 10 flows from the first refrigerant passage 15 into the fourth refrigerant passage 45, passes through the narrow tube portion 450 of the freshness maintaining device 40 from the inflow side passage 45A, and from the outflow side passage 45B. It circulates in the first refrigerant passage 15 and flows into the condenser 20.
At this time, since the refrigerant compressed by the compressor 10 has a high temperature and high pressure, the high temperature refrigerant passes through the entire surface of the catalyst portion 41 from the fourth refrigerant passage 45 to warm the catalyst of the low temperature catalyst portion 41 and flows out. The side passage 45B returns to the first refrigerant passage 15.
When a certain time has elapsed, the third valve 55 is opened, and the first and second valves 51 and 53 are closed.
In this state, the compressed high-temperature refrigerant from the compressor 10 flows into the condenser 20 through the first refrigerant passage 15 and executes normal refrigerant circulation.
[0013]
Since the refrigeration apparatus 1 has the freshness maintaining apparatus 40 installed in a cold atmosphere, the catalyst part 41 efficiently adsorbs ethylene contained in the air from the direction of the arrow.
And the control apparatus 60 circulates the high temperature refrigerant | coolant compressed for every fixed time to the catalyst part 41 of the freshness holding apparatus 40. FIG. The catalyst temperature of the catalyst unit 41 of the freshness maintaining device 40 is increased, and the decomposition of ethylene and the separation of decomposition products are promoted. The temperature rise by the narrow tube portion 450 proceeds to the inside of the catalyst portion 41 by the wind flowing in the direction of the arrow, and the temperature rise of the entire catalyst portion 41 is promoted to further promote the decomposition and separation of ethylene.
[0014]
As described above, by the series of valve opening / closing control of the passage switch 50 of the control device 60, the surface temperature of the catalyst of the freshness maintaining device 40 repeatedly repeats the low temperature and the high temperature at regular intervals, thereby efficiently performing the adsorption and decomposition of ethylene. , Improve ethylene removal ability.
In this embodiment, the example in which the control device controls the opening / closing of the valve according to time has been described. However, the same effect can be achieved by controlling the temperature, the concentration, and the like.
[0015]
(Example)
Next, the Example which arrange | positions the refrigeration apparatus provided with the freshness holding | maintenance apparatus 40 in a container is described (refer FIG. 3).
In the refrigerated container 100, the refrigeration apparatus 1 and the freshness maintaining apparatus 40 are disposed.
The refrigerator 1 is equipped with a compressor 10 disposed outside the container 100, a condenser 20 disposed within the container 100, an evaporator 30, and the like.
The evaporator 30 takes in the air in the refrigerated container 10 to achieve dehumidification and cooling, and releases dry cold air.
[0016]
The freshness maintaining device 40 is disposed on the upstream side of the evaporator 30.
The freshness maintaining device 40 adsorbs and decomposes the ethylene gas in the air flowing into the container 100 to remove the ethylene gas in the container.
The freshness maintaining device 40 communicates with the refrigerant circulation system of the refrigeration apparatus 1 through a fourth refrigerant passage 45 branched from the refrigerant passage 15 of the refrigeration apparatus 1.
[0017]
When the fourth refrigerant passage 45 communicates with the first refrigerant passage 15 by the switch 50, the refrigerant compressed to a high temperature flowing out from the compressor 10 flows into the freshness maintaining device 40 from the fourth refrigerant passage 45. Then, the catalyst accommodated in the freshness maintaining device 40 is heated to promote the decomposition of ethylene adsorbed on the catalyst.
In addition, when a certain time elapses in this state, the switch 50 is switched, and the refrigerant from the compressor 10 flows into the condenser 20 without passing through the freshness maintaining device 40. During this time, the catalyst of the freshness maintaining device 40 is cooled in a cold atmosphere, and ethylene is adsorbed.
[0018]
【The invention's effect】
The refrigeration apparatus with the freshness maintaining apparatus of the present invention achieves heating and cooling of the catalyst, and has good ethylene gas adsorption efficiency and ethylene gas decomposition efficiency. Furthermore, it is not necessary to provide a special device such as a heating device, and the size of the device can be reduced.
[Brief description of the drawings]
FIG. 1 is a configuration explanatory view of a refrigeration apparatus with a freshness maintaining apparatus according to the present invention.
FIG. 2 is a perspective view of a freshness holding device.
FIG. 3 is a schematic view of a refrigeration apparatus with a freshness maintaining apparatus disposed in a refrigerated container.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 10 Compressor 15 1st refrigerant path 20 Condenser 25 2nd refrigerant path 30 Evaporator 35 3rd refrigerant path 40 Freshness maintenance apparatus 41 Catalyst part 50 Switching apparatus 51, 53, 55 Valve 60 Control apparatus 450 Narrow pipe part

Claims (3)

コンプレッサーと、コンデンサーと、エバポレータと、コンプレッサーとコンデンサーとエバポレータとを連絡する冷媒の冷媒通路とを有する冷蔵装置と、空気中のエチレンガスを吸着分解するエチレン吸着分解触媒を有する鮮度保持装置とを備え、コンプレッサーとコンデンサーを連絡する冷媒通路は、鮮度保持装置に連絡する冷媒の循環通路を形成してなる鮮度保持装置付き冷蔵装置。 A refrigeration apparatus having a compressor, a condenser, an evaporator, a refrigerant passage for refrigerant connecting the compressor, the condenser and the evaporator, and a freshness maintaining apparatus having an ethylene adsorption / decomposition catalyst for adsorbing and decomposing ethylene gas in the air. The refrigerant passage connecting the compressor and the condenser forms a refrigerant circulation passage communicating with the freshness maintaining device. 鮮度保持装置に連絡する冷媒の循環通路は、通路の開閉手段を備えてなる請求項1記載の鮮度保持装置付き冷蔵装置。 The refrigerating apparatus with a freshness-keeping device according to claim 1, wherein the refrigerant circulation passage communicating with the freshness-keeping device comprises passage opening / closing means . 鮮度保持装置に連絡する冷媒の循環通路はエチレン吸着分解触媒の上流側を通過するように配設されてなる請求項1記載の鮮度保持装置付き冷蔵装置。Circulating passage ethylene adsorptive decomposition arranged by comprising Claim 1 Symbol placement freshness retaining device with refrigeration apparatus to pass through the upstream side of the catalyst of the refrigerant to contact freshness retaining device.
JP10439398A 1998-04-15 1998-04-15 Refrigeration unit with freshness maintaining device Expired - Lifetime JP3826560B2 (en)

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JP10439398A JP3826560B2 (en) 1998-04-15 1998-04-15 Refrigeration unit with freshness maintaining device

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JP3826560B2 true JP3826560B2 (en) 2006-09-27

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JP5936758B1 (en) * 2015-08-28 2016-06-22 日立アプライアンス株式会社 refrigerator
JP2017072306A (en) * 2015-10-07 2017-04-13 日立アプライアンス株式会社 refrigerator

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