JPS6337864B2 - - Google Patents
Info
- Publication number
- JPS6337864B2 JPS6337864B2 JP56011706A JP1170681A JPS6337864B2 JP S6337864 B2 JPS6337864 B2 JP S6337864B2 JP 56011706 A JP56011706 A JP 56011706A JP 1170681 A JP1170681 A JP 1170681A JP S6337864 B2 JPS6337864 B2 JP S6337864B2
- Authority
- JP
- Japan
- Prior art keywords
- cooler
- compressor
- temperature
- dehumidifying
- air
- 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
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2400/00—Component parts or details not otherwise provided for in this subclass
- F25B2400/07—Details of compressors or related parts
- F25B2400/075—Details of compressors or related parts with parallel compressors
Landscapes
- Devices That Are Associated With Refrigeration Equipment (AREA)
Description
【発明の詳細な説明】
本発明は、運転効率の高い制御方式を行なう二
温度蒸発冷凍装置の運転方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method of operating a two-temperature evaporative refrigeration system that implements a control system with high operating efficiency.
従来、二温度蒸発冷凍サイクルとしては、第1
図のように圧縮機1、凝縮器2、第1減圧器3、
および第1冷却器4を順次連結し、さらに第2減
圧器5を介して、蒸発温度の低い第2冷却器6を
接続した冷凍サイクル7が一般的である。この冷
凍サイクルを庫内温度0〜2℃の冷蔵オープンシ
ヨーケースに適用した場合の一例を第2図に示
す。図に示す二温度冷蔵オープンシヨーケース
は、前面に開口を有する断熱箱体11、その内側
に風路12を形成して貯蔵品を収納する内ケース
17が設置され、さらに該風路12内には庫内送
風機14、蒸発温度の高い除湿冷却器Bおよび蒸
発温度の低い主冷却器Aがそれぞれ取付られ、該
風路12の前面上部には冷気の吹出口15が、下
部には吸込口16が設けられエアカーテンを形成
している。 Conventionally, in a two-temperature evaporative refrigeration cycle, the first
As shown in the figure, a compressor 1, a condenser 2, a first pressure reducer 3,
A refrigeration cycle 7 in which a first cooler 4 and a first cooler 4 are sequentially connected, and a second cooler 6 having a low evaporation temperature is further connected via a second pressure reducer 5 is common. FIG. 2 shows an example in which this refrigeration cycle is applied to a refrigerated open case with an internal temperature of 0 to 2°C. The two-temperature refrigerated open storage case shown in the figure includes an insulating box 11 having an opening on the front, an inner case 17 that forms an air passage 12 inside the box and stores stored items, and further includes an inner case 17 inside which forms an air passage 12 to store stored items. An internal air blower 14, a dehumidifying cooler B with a high evaporation temperature, and a main cooler A with a low evaporation temperature are installed respectively, and a cold air outlet 15 is installed at the upper front of the air passage 12, and an inlet 16 is installed at the lower part. are installed to form an air curtain.
除湿冷却器Bは第1図の冷凍サイクル7の第1
冷却器4に対応し、冷却器表面温度は0℃近辺
(0℃以上)に設定される。また、主冷却器Aは
第2冷却器6に対応しており、冷却器表面温度は
概略−10℃〜−15℃程度に設定される。 The dehumidifying cooler B is the first refrigeration cycle 7 in FIG.
Corresponding to the cooler 4, the cooler surface temperature is set to around 0°C (0°C or higher). Further, the main cooler A corresponds to the second cooler 6, and the cooler surface temperature is set to approximately -10°C to -15°C.
ここで、庫内送風機14によつて吸込まれた高
温多湿の空気は、冷却器表面温度が0℃近辺(0
℃以上)に設定されている除湿冷却器Bによつて
水の形で除湿される。除湿され、水分の少なくな
つた空気はさらに主冷却器Aによつて所定の温度
(概略−5℃程度)まで冷却された後、シヨーケ
ース上部の冷気吹出口15より庫内13に吹き出
され、庫内を必要温度(0〜2℃)に冷却する。
庫内を冷却した空気は一部外気を吸込み、再び吸
込口16より吸込まれ、以下同様の循環を繰返
す。また吹出口15より吹き出された冷気は前面
開口部にエアカーテンを形成し外気が庫内13へ
侵入するのを防止している。本例のように二温度
蒸発冷蔵シヨーケースは徐湿冷却器Bの除斜作用
により主冷却器Aへの着霜量が軽減し、除霜回数
を少なくできるため、除霜に伴う庫内温度の上昇
による貯蔵品の損傷を小さくできるという効果が
ある。しかし、本例の如く従来の二温度蒸発冷蔵
オープンシヨーケースでは、除湿冷却器Bの表面
温度を常に0℃以上を保つように、例えば冷凍サ
イクルにおいて蒸発圧力調整弁(図示せず)のよ
うな機構を用いて常に一定に保つため庫内温度が
低い場合や、周囲空気温度が低い場合のように吸
込空気温度が0℃近くまで低下する場合には、除
湿冷却器Bと空気温度との差が非常に小さくなつ
て交換熱量が減る結果、除湿冷却器Bの除湿作用
が激減し、主冷却器Aへの着霜量が増えるという
欠点があつた。また、上記蒸発圧力調整弁のよう
な蒸発圧力を調整する機構を設けないような場合
には、吸込空気温度が高い通常の運転では除湿冷
却器Bの表面温度は略0℃に設定され空気中の水
分は結露し水の形で除湿されるが、庫内温度が低
い場合や周囲空気温度が低い場合のように吸込空
気温度が低い場合には、除湿冷却器Bの蒸発温度
が低下するため除湿冷却器の表面温度が0℃以下
となり、水分の一部分は冷却器表面へ凍結した
り、着霜し、冷却器の目づまりを生じ蒸発圧力が
低下して運転効率が悪くなるという欠点があつ
た。さらに別の従来例として上記除湿冷却器Bお
よび主冷却器Aを第3図のように、圧縮機21,
21′、凝縮器22,22′、減圧器23,23′、
冷却器24,24′にて形成されるそれぞれ独立
した二つの冷凍サイクル25,25′で構成した
場合には、蒸発温度が高い除湿冷却器Bを接続し
た冷凍サイクル25の方が成績係数が高いので、
冷凍システム全体として運転効率が高くなる。し
かし、この場合も冷凍負荷が減つた場合には除湿
冷却器Bの表面温度を略0℃に設定することが困
難となり、第1図の従来例と同様、除湿冷却器B
に着霜を生じるので結局除湿冷却器Bの蒸発温度
が低下し、効率の良い運転を長時間維持するのが
困難となるばかりでなく、蒸発温度の高い冷却器
の運転範囲が狭いという欠点があつた。 Here, the hot and humid air sucked in by the internal blower 14 has a surface temperature of the cooler near 0°C (0°C).
Dehumidification is carried out in the form of water by dehumidifying cooler B, which is set at a temperature of at least 10°C. The dehumidified air with reduced moisture is further cooled to a predetermined temperature (approximately -5°C) by the main cooler A, and then blown into the refrigerator interior 13 from the cold air outlet 15 at the top of the show case. Cool the inside to the required temperature (0-2°C).
The air that has cooled the inside of the refrigerator partially draws in outside air, is sucked in again through the suction port 16, and the same circulation is repeated thereafter. Further, the cold air blown out from the outlet 15 forms an air curtain at the front opening to prevent outside air from entering the inside 13 of the refrigerator. In a two-temperature evaporative refrigerating case like this one, the amount of frost on the main cooler A is reduced by the deskewing action of the dehumidifying cooler B, and the number of times of defrosting can be reduced. This has the effect of reducing damage to stored goods due to rising. However, in the conventional two-temperature evaporative refrigeration open case like this example, in order to keep the surface temperature of the dehumidifying cooler B always above 0°C, for example, an evaporative pressure regulating valve (not shown) is installed in the refrigeration cycle. When the temperature inside the refrigerator is low because it is kept constant using a mechanism, or when the ambient air temperature is low and the intake air temperature drops to nearly 0℃, the difference between the dehumidifying cooler B and the air temperature. As a result, the dehumidifying effect of the dehumidifying cooler B is drastically reduced and the amount of frost formed on the main cooler A is increased. In addition, if a mechanism for adjusting the evaporation pressure such as the above-mentioned evaporation pressure adjustment valve is not provided, the surface temperature of the dehumidifying cooler B is set to approximately 0°C during normal operation when the intake air temperature is high, and the air Moisture is condensed and dehumidified in the form of water, but when the intake air temperature is low, such as when the internal temperature is low or the ambient air temperature is low, the evaporation temperature of dehumidifying cooler B decreases. When the surface temperature of the dehumidifying cooler drops below 0°C, some of the water freezes or forms frost on the surface of the cooler, clogging the cooler, lowering the evaporation pressure, and reducing operating efficiency. . As another conventional example, the dehumidifying cooler B and the main cooler A are combined with a compressor 21, as shown in FIG.
21', condenser 22, 22', pressure reducer 23, 23',
When configured with two independent refrigeration cycles 25 and 25' formed by coolers 24 and 24', the coefficient of performance of the refrigeration cycle 25 connected to dehumidifying cooler B, which has a higher evaporation temperature, is higher. So,
The operating efficiency of the entire refrigeration system is increased. However, in this case as well, when the refrigeration load decreases, it becomes difficult to set the surface temperature of dehumidifying cooler B to approximately 0°C, and as in the conventional example shown in Fig. 1, dehumidifying cooler B
As frost forms on the dehumidifying cooler B, the evaporation temperature of the dehumidifying cooler B eventually decreases, which not only makes it difficult to maintain efficient operation for a long time, but also has the drawback that the operating range of the cooler with a high evaporating temperature is narrow. It was hot.
本発明は上記欠点を除去するためになされたも
ので、上述の従来例のように、周囲条件や庫内温
度条件など運転条件によつて蒸発温度の高い除湿
冷却に着霜を生じるような場合でも、除湿性能を
維持して主冷却器への着霜を軽減するとともに、
蒸発温度が高い側の冷却器の運転比率および熱交
換比率を高め運転効率の高い二温度蒸発冷凍装置
の運転方法を提供することを目的とする。 The present invention has been made in order to eliminate the above-mentioned drawbacks, and when frost formation occurs in dehumidifying cooling with a high evaporation temperature depending on operating conditions such as ambient conditions and internal temperature conditions, as in the above-mentioned conventional example, However, while maintaining dehumidification performance and reducing frost formation on the main cooler,
It is an object of the present invention to provide a method of operating a two-temperature evaporative refrigeration system with high operating efficiency by increasing the operating ratio and heat exchange ratio of the cooler on the side where the evaporation temperature is higher.
以下本発明の一実施例を第4図にもとづき説明
する。図において、第1圧縮機31、凝縮器3
2、第1電磁弁33、第1減圧器34、第1冷却
器35をそれぞれ環状に接続して主冷媒回路を形
成するとともに、凝縮器32の出口側を分岐し
て、第2電磁弁37、第2減圧器38、第2冷却
器39、第2圧縮機36を直列に接続し、さらに
第2圧縮機36の吐出側を第1圧縮機31の吐出
側経路に連結して副冷媒回路を形成してなり、第
2冷却器39の蒸発温度は第1冷却器35の蒸発
温度より高く設定して冷凍運転を行なう。 An embodiment of the present invention will be described below based on FIG. 4. In the figure, a first compressor 31, a condenser 3
2. The first solenoid valve 33, the first pressure reducer 34, and the first cooler 35 are connected in a ring to form a main refrigerant circuit, and the outlet side of the condenser 32 is branched to form a second solenoid valve 37. , the second pressure reducer 38, the second cooler 39, and the second compressor 36 are connected in series, and the discharge side of the second compressor 36 is further connected to the discharge side path of the first compressor 31 to form an auxiliary refrigerant circuit. The evaporation temperature of the second cooler 39 is set higher than the evaporation temperature of the first cooler 35 to perform the freezing operation.
また、第2圧縮機36は強制的に間欠運転が行
なわれ、第1圧縮機31は冷凍負荷に応じて断続
運転を行なう。 Further, the second compressor 36 is forced to operate intermittently, and the first compressor 31 operates intermittently depending on the refrigeration load.
上記実施例の冷凍サイクルを第2図の冷蔵シヨ
ーケースに適用した場合について説明する。第2
図において、除湿冷却器Bは冷凍装置40の第2
冷却器39に対応し、主冷却器Aは冷凍サイクル
40の第1冷却器35に対応する。庫内送風機1
4によつて吸込まれた高温多湿の空気は、蒸発温
度が0℃以下を含む0℃近辺に設定された除湿冷
却器Bによつて、水の形、あるいは霜となつて除
湿される。これにより主冷却器Aの着霜量が軽減
し、除霜回数を少なくできるため、除霜に伴う庫
内温度の変動を小さくできる。 A case where the refrigeration cycle of the above embodiment is applied to the refrigerating case shown in FIG. 2 will be explained. Second
In the figure, the dehumidifying cooler B is the second
The main cooler A corresponds to the cooler 39 and the first cooler 35 of the refrigeration cycle 40 . Internal blower 1
The hot and humid air sucked in by the air filter 4 is dehumidified in the form of water or frost by the dehumidifying cooler B whose evaporation temperature is set at around 0° C., including 0° C. or lower. As a result, the amount of frost on the main cooler A is reduced, and the number of times of defrosting can be reduced, so that fluctuations in temperature inside the refrigerator due to defrosting can be reduced.
さらに本実施例では、第2圧縮機36を強制的
に間欠運転させるため、以下に述べるように、除
湿冷却器Bの霜が付着したときおこる蒸発温度の
低下や通風抵抗の増加による運転効率の低下をも
防止することができる。 Furthermore, in this embodiment, since the second compressor 36 is forced to operate intermittently, as described below, the operating efficiency is reduced due to a decrease in evaporation temperature and an increase in ventilation resistance that occur when frost forms on the dehumidifying cooler B. It is also possible to prevent the decrease.
例えば、一定時間(例えば30分間)運転後、タ
イマ(図示せず)等の動作指令により第2圧縮機
36の運転を停止すると除湿冷却器B39の冷却
作用が停止し、主冷却器A35のみでは冷凍能力
が不足するため、吸込空気温度が0℃以上に上昇
してきて、除湿冷却器Bの表面に付着した霜は融
ける。一定時間(例えば3分間)停止後、再び第
2圧縮機36の運転を再開し、以後上記運転を繰
返すことにより、除湿冷却器Bへの着霜量の増加
が防止されるので、周囲空気温度が低い場合や庫
内温度が低い場合のように吸込空気温度が0℃近
辺まで低下する場合でも除湿冷却器Bによる効率
良い除湿運転が長時間行なえるとともに着霜の増
加による蒸発圧力の長時間、低下を防止し、第2
圧縮機36の運転効率の低下を防ぐことができ
る。また、除湿冷却器Bの運転範囲が、除湿冷却
器Bの表面に水分が着霜する低蒸発温度領域まで
拡大できるため、全交換熱量に対する除湿冷却器
Bの熱交換比率を大きく設定できる。また蒸発温
度が低く成績係数の悪い第1圧縮機31は負荷に
応じて断続運転する一方、蒸発温度が高く成績係
数の良い第2圧縮機36の運転範囲をより低負荷
領域まで広げ、第2圧縮機の運転比率を拡大でき
るため、冷凍装置の運転効率が高まるという効果
もある。 For example, if the operation of the second compressor 36 is stopped by an operation command from a timer (not shown) or the like after operation for a certain period of time (for example, 30 minutes), the cooling action of the dehumidifying cooler B39 will stop, and the main cooler A35 alone will not work. Since the refrigerating capacity is insufficient, the temperature of the intake air rises to 0° C. or higher, and the frost adhering to the surface of the dehumidifying cooler B melts. After stopping for a certain period of time (for example, 3 minutes), the operation of the second compressor 36 is restarted, and by repeating the above operation, an increase in the amount of frost formed on the dehumidifying cooler B is prevented, so that the ambient air temperature Even when the intake air temperature drops to around 0℃, such as when the temperature is low or the internal temperature is low, dehumidifying cooler B can perform efficient dehumidification for a long time, and the evaporation pressure can be maintained for a long time due to increased frost formation. , prevent the decline, and the second
A decrease in the operating efficiency of the compressor 36 can be prevented. Further, since the operating range of the dehumidifying cooler B can be expanded to a low evaporation temperature region where moisture forms frost on the surface of the dehumidifying cooler B, the heat exchange ratio of the dehumidifying cooler B to the total amount of heat exchanged can be set to be large. In addition, the first compressor 31, which has a low evaporation temperature and a poor coefficient of performance, operates intermittently depending on the load, while the operating range of the second compressor 36, which has a high evaporation temperature and a good coefficient of performance, is expanded to a lower load region. Since the operating ratio of the compressor can be expanded, there is also the effect of increasing the operating efficiency of the refrigeration system.
さらに凝縮器32を共通にして冷凍サイクルを
形成しているので、第1圧縮機31が停止すると
凝縮器32を通過する冷媒量が第1圧縮機31か
らの吐出分だけ減少するので、凝縮圧力、すなわ
ち吐出圧力が低下して第2圧縮機36の成績係数
を向上し、冷凍装置全体としての運転効率をより
向上させることができる。本実施例では、タイマ
等により一定周期の間欠運転を行つているが、除
湿センサ、温度センサ等、検知要素により間欠運
転を行つてもよい。 Furthermore, since the condenser 32 is used in common to form the refrigeration cycle, when the first compressor 31 stops, the amount of refrigerant passing through the condenser 32 decreases by the amount discharged from the first compressor 31, so the condensing pressure That is, the discharge pressure is reduced, the coefficient of performance of the second compressor 36 is improved, and the operating efficiency of the refrigeration system as a whole can be further improved. In this embodiment, intermittent operation is performed at a fixed period using a timer or the like, but intermittent operation may be performed using a detection element such as a dehumidification sensor or a temperature sensor.
なお、本発明は除湿冷却器Bの表面温度が0℃
以上で着霜が起こらないように設定されている場
合についても、低負荷時の凝縮器の有効性、第2
冷却器の蒸発温度が高いことによる運転効率の向
上、および2冷却器の並列接続による圧力損失の
低減等の効果が得られる。また、除湿冷却器Bの
表面温度が0℃以下で、吸込口温度も常に0℃以
下となるような場合にも、間欠的に除湿冷却器B
の運転を止め、除湿冷却器Bの前後をダンパーで
遮断し、ヒータ等で除霜するとともに、その間除
湿冷却器Bをバイパスして冷気を主冷却器Aに導
びくように形成すれば、同様の効果が得られる。 In addition, in the present invention, the surface temperature of the dehumidifying cooler B is 0°C.
Even when the settings above are set to prevent frost formation, the effectiveness of the condenser at low load, the second
Effects such as improved operating efficiency due to the high evaporation temperature of the cooler and reduction in pressure loss due to the parallel connection of the two coolers can be obtained. In addition, even if the surface temperature of dehumidifying cooler B is below 0°C and the inlet temperature is always below 0°C, dehumidifying cooler B may be
The same effect can be obtained by stopping the operation of the dehumidifying cooler B, blocking the front and rear of the dehumidifying cooler B with a damper, defrosting it with a heater, etc., and bypassing the dehumidifying cooler B in the meantime and guiding the cold air to the main cooler A. The effect of this can be obtained.
以上説明したように、本発明によれば、蒸発温
度の異る2台の冷却器、および2台の圧縮機を有
する冷凍サイクルを凝縮器を共通にして二温度蒸
発冷凍装置の運転方法として蒸発温度の高い第2
圧縮機は一定時間ごとに運転を停止する強制間欠
運転とし、第1圧縮機は冷凍負荷に応じて断続運
転させることにより、蒸発温度が高い側の冷却器
で水として除湿される場合だけでなく、着霜を生
じるような運転条件においても高い運転効率が得
られるという効果を有する。 As explained above, according to the present invention, a refrigeration cycle having two coolers with different evaporation temperatures and two compressors can be combined with a common condenser to achieve evaporation. 2nd place with higher temperature
The compressor is forced to operate intermittently, with operation stopped at regular intervals, and the first compressor is operated intermittently depending on the refrigeration load, so that the compressor is not only dehumidified as water in the cooler with a higher evaporation temperature. This has the effect that high operating efficiency can be obtained even under operating conditions that cause frost formation.
第1図および第3図は従来の二温度蒸発冷凍サ
イクルの構成図、第2図は二温度蒸発冷蔵シヨー
ケースの断面構造図、第4図は本発明の一実施例
を示す冷凍サイクル構成図である。
31……第1圧縮機、32……凝縮器、33…
…第1電磁弁、34……第1減圧器、35……第
1冷却器、36……第2圧縮機、37……第2電
磁弁、38……第2減圧器、39……第2冷却
器、40……冷凍サイクル、A……主冷却器、B
……除湿冷却器。
Figures 1 and 3 are block diagrams of a conventional two-temperature evaporative refrigeration cycle, Figure 2 is a cross-sectional structural diagram of a two-temperature evaporative refrigeration case, and Figure 4 is a block diagram of a refrigeration cycle showing an embodiment of the present invention. be. 31...first compressor, 32...condenser, 33...
...first solenoid valve, 34...first pressure reducer, 35...first cooler, 36...second compressor, 37...second solenoid valve, 38...second pressure reducer, 39...th 2 cooler, 40... Refrigeration cycle, A... Main cooler, B
...Dehumidifying cooler.
Claims (1)
低い第1冷却器を有し、第1圧縮機、凝縮器、第
1減圧機、第1冷却器を環状に接続する主冷媒回
路と、凝縮器の出口側経路を分岐し、第2減圧
器、第2冷却器、第2圧縮機を直列に接続し、さ
らに第2圧縮機の吐出側を第1圧縮機の吐出側経
路に連結する副冷媒回路を備えた二温度蒸発式冷
凍装置の運転において、第2圧縮機はタイマによ
り一定時間ごとに運転を停止する制御間欠運転を
行ない、第1圧縮機は冷却空間が所望する温度に
なるように冷却空間に設けられたサーモスタツト
により冷凍負荷に応じて断続運転を行なうことを
特徴とする冷凍装置の運転方法。1 A main refrigerant circuit that has a second cooler with a high evaporation temperature and a first cooler with a low evaporation temperature, and connects the first compressor, the condenser, the first pressure reducer, and the first cooler in an annular manner; The secondary compressor branches the outlet side path of the compressor, connects the second pressure reducer, second cooler, and second compressor in series, and further connects the discharge side of the second compressor to the discharge side path of the first compressor. In the operation of a two-temperature evaporative refrigeration system equipped with a refrigerant circuit, the second compressor performs a controlled intermittent operation in which the operation is stopped at fixed intervals using a timer, and the first compressor operates so that the cooling space reaches the desired temperature. 1. A method of operating a refrigeration system, characterized in that a thermostat provided in a cooling space performs intermittent operation according to the refrigeration load.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1170681A JPS57127756A (en) | 1981-01-30 | 1981-01-30 | Refrigerating plant |
| US06/341,328 US4474026A (en) | 1981-01-30 | 1982-01-21 | Refrigerating apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1170681A JPS57127756A (en) | 1981-01-30 | 1981-01-30 | Refrigerating plant |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS57127756A JPS57127756A (en) | 1982-08-09 |
| JPS6337864B2 true JPS6337864B2 (en) | 1988-07-27 |
Family
ID=11785482
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1170681A Granted JPS57127756A (en) | 1981-01-30 | 1981-01-30 | Refrigerating plant |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS57127756A (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| SE439831C (en) * | 1984-03-21 | 1987-01-26 | Olson Hans E E | PROCEDURE AND DEVICE FOR DEFROSTING MULTIPLE EVENTS |
| JP6699254B2 (en) * | 2016-03-10 | 2020-05-27 | 富士電機株式会社 | Cooling system |
| JP2021016518A (en) * | 2019-07-19 | 2021-02-15 | 富士電機株式会社 | Showcase |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5551262A (en) * | 1978-10-07 | 1980-04-14 | Fuji Electric Co Ltd | Condensing unit for refrigeration equipment |
-
1981
- 1981-01-30 JP JP1170681A patent/JPS57127756A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS57127756A (en) | 1982-08-09 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US5509272A (en) | Apparatus for dehumidifying air in an air-conditioned environment with climate control system | |
| US4197716A (en) | Refrigeration system with auxiliary heat exchanger for supplying heat during defrost cycle and for subcooling the refrigerant during a refrigeration cycle | |
| US2468626A (en) | Refrigerating apparatus | |
| CN107228522B (en) | Control method of air-cooled refrigerator | |
| JPH0124543Y2 (en) | ||
| JP3049425B2 (en) | Refrigerator with two evaporators | |
| JPS6337864B2 (en) | ||
| US2169900A (en) | Air conditioning system | |
| JP2002195726A5 (en) | ||
| US5069040A (en) | Coil bypass arrangement | |
| JPH06273011A (en) | Cool air drier | |
| JPS5888580A (en) | Cooling device | |
| JP2013122333A (en) | Container refrigeration apparatus | |
| JPS5941753A (en) | Cooling device | |
| JP4286106B2 (en) | Freezer refrigerator | |
| JPH08254372A (en) | Air conditioner | |
| USRE20477E (en) | Refrigerating apparatus | |
| JPS5842842Y2 (en) | Two-stage compression refrigeration equipment | |
| JPS6015100Y2 (en) | Refrigerated open case | |
| JPS5835986Y2 (en) | Refrigerated open case | |
| JPH0311661Y2 (en) | ||
| JP3495956B2 (en) | refrigerator | |
| JPS6142067Y2 (en) | ||
| JPS6215745Y2 (en) | ||
| JPS63290381A (en) | Operation controller for open showcase |