JPH0378550B2 - - Google Patents
Info
- Publication number
- JPH0378550B2 JPH0378550B2 JP62121962A JP12196287A JPH0378550B2 JP H0378550 B2 JPH0378550 B2 JP H0378550B2 JP 62121962 A JP62121962 A JP 62121962A JP 12196287 A JP12196287 A JP 12196287A JP H0378550 B2 JPH0378550 B2 JP H0378550B2
- Authority
- JP
- Japan
- Prior art keywords
- hot gas
- hydrogen storage
- cooler
- coil
- refrigerant
- 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
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
- F25B47/00—Arrangements for preventing or removing deposits or corrosion, not provided for in another subclass
- F25B47/02—Defrosting cycles
- F25B47/022—Defrosting cycles hot gas defrosting
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C11/00—Use of gas-solvents or gas-sorbents in vessels
- F17C11/005—Use of gas-solvents or gas-sorbents in vessels for hydrogen
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/32—Hydrogen storage
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P90/00—Enabling technologies with a potential contribution to greenhouse gas [GHG] emissions mitigation
- Y02P90/45—Hydrogen technologies in production processes
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Filling Or Discharging Of Gas Storage Vessels (AREA)
- Compression-Type Refrigeration Machines With Reversible Cycles (AREA)
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、ホツトガス方式により冷却器の除霜
を行なうホツトガス除霜装置の改良に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to an improvement of a hot gas defrosting device that defrosts a cooler using a hot gas method.
ホツトガス方式により除霜を行なう冷却装置で
は、除霜時にホツトガスを冷却器に通し、その熱
で冷却器の霜を溶かす。この除霜の際、ガスは凝
縮して液化するので、この凝縮した液冷媒を蒸発
させて圧縮機に吸入させることが必要となる。
In a cooling device that defrosts using a hot gas method, hot gas is passed through the cooler during defrosting, and the heat is used to melt the frost in the cooler. During defrosting, the gas condenses and becomes liquefied, so it is necessary to evaporate the condensed liquid refrigerant and draw it into the compressor.
従来、除霜の際に液化した凝縮冷媒を蒸発させ
るには第2図に示すタンク方式が知られている。
同図で、圧縮機31、凝縮機32、膨張弁33お
よび冷却器34を直列に接続した冷凍回路が構成
されており、圧縮機31から出た吐出配管35
が、タンク36内のコイル37に接続されて、タ
ンク36内の水またはブラインの加温が行なわれ
る。また凝縮器32の手前に設けられデフロスト
時に閉成される開閉弁38の入口側配管部と冷却
器34のに入口配管部とが、デフロスト時に開成
される開閉弁39を中途部に設けた分岐配管40
により接続されている。また冷却器34を出た配
管は、冷却運転時に開成される開閉弁41を通り
圧縮機31の吸入配管42に接続されているとと
もに、デフロスト時に開成される開閉弁43を経
由してタンク36内のコイル44を通つて吸入配
管42に接続されている。 Conventionally, a tank system shown in FIG. 2 has been known for evaporating condensed refrigerant that is liquefied during defrosting.
In the figure, a refrigeration circuit is configured in which a compressor 31, a condenser 32, an expansion valve 33, and a cooler 34 are connected in series, and a discharge pipe 35 coming out of the compressor 31 is configured.
is connected to a coil 37 in tank 36 to heat the water or brine in tank 36. In addition, the inlet piping part of the on-off valve 38 which is provided before the condenser 32 and is closed during defrosting, and the inlet piping part of the cooler 34 are connected to a branch where an on-off valve 39, which is opened during defrosting, is provided in the middle. Piping 40
connected by. The pipe exiting the cooler 34 is connected to the suction pipe 42 of the compressor 31 through an on-off valve 41 that is opened during cooling operation, and is connected to the intake pipe 42 of the compressor 31 through an on-off valve 43 that is opened during defrosting. The suction pipe 42 is connected to the suction pipe 42 through the coil 44 .
このように構成されていることで、デフロスト
時に冷却器34で凝縮した液冷媒は、タンク36
内のコイル44を通過する際に水たはブラインに
よつて加温されてガス化される。なお、冷却運転
時は実線で示す矢印の経由を通つて冷媒が流れ、
除霜時には破線で示す矢印の経路を通つて冷媒が
流れる。 With this configuration, the liquid refrigerant condensed in the cooler 34 during defrosting is transferred to the tank 36.
The water or brine is heated and gasified as it passes through the coil 44 inside. In addition, during cooling operation, the refrigerant flows through the arrow shown by the solid line.
During defrosting, the refrigerant flows through the path indicated by the dashed arrow.
また水またはブラインの熱容量を利用して凝縮
液冷媒の蒸発を行なうタンク方式の他に、デフロ
スト時に冷却器から出る凝縮液冷媒を熱交換器の
コイルに通すとともに、この熱交換器の他方のコ
イルに冷却水を通し、交換熱を大気に放出するこ
とで、凝縮液冷媒の蒸発を行なう熱交換方式など
がある。 In addition to the tank method, which uses the heat capacity of water or brine to evaporate condensed refrigerant, the condensed refrigerant discharged from the cooler during defrosting is passed through a coil of a heat exchanger, and the other coil of this heat exchanger is There is a heat exchange method in which the condensed refrigerant is evaporated by passing cooling water through the refrigerant and releasing the exchanged heat to the atmosphere.
ところで、上述のタンク方式により凝縮液冷媒
の蒸発を行なう場合では、滞留水によつて水槽が
腐食されるという問題がある。
However, when the condensed liquid refrigerant is evaporated using the tank method described above, there is a problem in that the water tank is corroded by the accumulated water.
また上述の熱交換方式では、冷却水温度が低い
場合、効率よく凝縮液冷媒の蒸発を行なえないと
いう問題がある。 Furthermore, the above-described heat exchange method has a problem in that the condensed liquid refrigerant cannot be efficiently evaporated when the cooling water temperature is low.
そこで本発明は、このような従来の問題点を解
決するために提案されたものであり、従来のタン
ク方式のように滞留水によつて水槽が腐食するよ
うなことはなく、また凝縮液冷媒をガス化するの
に充分な熱量が得られるホツトガス除霜装置を提
供することを目的とする。 Therefore, the present invention was proposed to solve these conventional problems, and unlike the conventional tank system, the water tank does not corrode due to accumulated water, and the condensate refrigerant An object of the present invention is to provide a hot gas defrosting device that can obtain sufficient heat to gasify.
この目的を達成するために本発明のホツトガス
除霜装置は、熱平衡圧力の異なる水素吸蔵合金を
それぞれ個別に封入した容器を設け、これら容器
間をを配管で連結し、熱平衡圧力の低い水素吸蔵
合金を封入した容器に第1、第2の熱交換コイル
を設け、冷却運転時に上記第1の熱交換コイルに
圧縮機から吐出されるホツトガス冷媒を通し、冷
却器の除霜時には上記第1の熱交換コイルへのホ
ツトガス冷媒の供給を停止して、冷却器にホツト
ガス冷媒を通すとともに、上記第2の熱交換コイ
ルに冷却器の除霜後の凝縮液冷媒を通すことを特
徴とする構成となつている。
In order to achieve this object, the hot gas defrosting device of the present invention is provided with containers in which hydrogen storage alloys with different thermal equilibrium pressures are individually sealed, and these containers are connected by piping, and hydrogen storage alloys with low thermal equilibrium pressures are installed. A first and second heat exchange coil is provided in a container enclosing a hot gas refrigerant, and during cooling operation, the hot gas refrigerant discharged from the compressor is passed through the first heat exchange coil, and when the cooler is defrosted, the first heat exchanger is passed through the first heat exchange coil. The configuration is characterized in that the supply of hot gas refrigerant to the exchange coil is stopped, the hot gas refrigerant is passed through the cooler, and the condensed liquid refrigerant after defrosting of the cooler is passed through the second heat exchange coil. ing.
上述の本発明では、冷却運転時にホツトガス冷
媒が第1の熱交換コイルに通されることで、低圧
側の水素吸蔵合金が加熱されて圧力が上昇し、こ
の合金から水素ガスが放出されて、他方の容器内
の水素吸蔵合金に吸収される。
In the above-described present invention, when the hot gas refrigerant is passed through the first heat exchange coil during cooling operation, the hydrogen storage alloy on the low pressure side is heated and the pressure increases, and hydrogen gas is released from this alloy. It is absorbed by the hydrogen storage alloy in the other container.
また除霜時には、第1の熱交換コイルへのホツ
トガス冷媒の供給が停止されて、同じ容器内の第
2の熱交換コイルに除霜後の凝縮液冷媒が通され
るので、この容器内の水素吸蔵合金が冷却されて
圧力が低下する。これにより他方の容器内に封入
された高圧側の水素吸蔵合金から水素ガスが放出
され、低圧側の水素吸蔵合金に水素ガスか吸収さ
れる。このときの水素ガス吸収による低圧側合金
の発熱によつて、凝縮液冷媒のガス化が行なわれ
る。 Also, during defrosting, the supply of hot gas refrigerant to the first heat exchange coil is stopped and the condensed liquid refrigerant after defrost is passed through the second heat exchange coil in the same container, so that The hydrogen storage alloy is cooled and the pressure decreases. As a result, hydrogen gas is released from the hydrogen storage alloy on the high pressure side sealed in the other container, and the hydrogen gas is absorbed by the hydrogen storage alloy on the low pressure side. At this time, the condensed liquid refrigerant is gasified by heat generation in the low-pressure side alloy due to absorption of hydrogen gas.
以下、本発明の実施例を図面に基づき詳細に説
明する。
Hereinafter, embodiments of the present invention will be described in detail based on the drawings.
第1図は、本発明に係るホツトガス除霜装置の
構成を示している。 FIG. 1 shows the configuration of a hot gas defrosting device according to the present invention.
同図で、ガス冷媒を圧縮する圧縮機1から出る
吐出配管2には、3方切換弁3に続いて、開閉弁
4が設けられ、さらに凝縮器5が接続され、膨張
弁6に続いて冷却器7接続されている。なお、凝
縮器5の冷却コイル5aには冷却水が通される。
上記3方切換弁3の圧縮機1側のポートを第1ポ
ート3aとし、開閉弁4側を第2ポート3bとす
れば、第3ポート3cは、低圧側の粒状の水素吸
蔵合金8を吸容した容器9内に、この水素吸蔵合
金8に埋もれて設けた第1の熱交換コイル10の
一端に接続されており、このコイル10の他端に
接続される配管は開閉弁4の入口側に接続される
配管と合流している。また上記開閉弁4の入口側
配管には、中途部に開閉弁11を設けた分岐配管
12の一端が接続されており、この分岐配管12
の他端は膨張弁6と冷却器7円を結ぶ配管に接続
されている。 In the same figure, a discharge pipe 2 coming out of a compressor 1 that compresses gas refrigerant is provided with an on-off valve 4 following a three-way switching valve 3, and further connected with a condenser 5, followed by an expansion valve 6. Cooler 7 is connected. Note that cooling water is passed through the cooling coil 5a of the condenser 5.
If the port on the compressor 1 side of the three-way switching valve 3 is the first port 3a, and the on-off valve 4 side is the second port 3b, the third port 3c absorbs the granular hydrogen storage alloy 8 on the low pressure side. It is connected to one end of a first heat exchange coil 10 that is buried in the hydrogen storage alloy 8 in the container 9 containing the hydrogen, and the piping connected to the other end of the coil 10 is connected to the inlet side of the on-off valve 4. It merges with the piping connected to. Further, one end of a branch pipe 12 having an on-off valve 11 in the middle is connected to the inlet side pipe of the on-off valve 4.
The other end is connected to a pipe connecting the expansion valve 6 and the cooler 7.
また冷却器7内の冷却コイル7aの他端と圧縮
機1は、中途部にサクシヨン主弁13を設けた吸
入配管14によつて接続されており、このサクシ
ヨン主弁13には上記容器9内に水素吸蔵合金8
に埋もれて設けた第2の熱交換コイル15が並列
に接続されている。なお、、コイル15の入口側
は、開閉弁20が設けられている。 The other end of the cooling coil 7a in the cooler 7 and the compressor 1 are connected by a suction pipe 14 having a suction main valve 13 in the middle. Hydrogen storage alloy 8
A second heat exchange coil 15, which is embedded in the heat exchanger coil 15, is connected in parallel. Note that an on-off valve 20 is provided on the inlet side of the coil 15.
また容器9とは別に、容器9内の水素吸蔵合金
8とは熱平衡圧力の異なる高圧側の粒状の水素吸
蔵合金16を収容した容器17が設けられてお
り、容器9と容器17間は配管18により接続さ
れている。ここで、水素吸蔵合金8,16には、
たとえばランタンニツケル合金等が用いられ、合
金の割合比を変ることにより、水素ガスとの反応
温度を変えている。またこの容器17内には、冷
却水が流れる冷却コイル19が粒状の水素吸蔵合
金16に埋もれて配されている。 In addition to the container 9, a container 17 containing a granular hydrogen storage alloy 16 on the high pressure side having a different thermal equilibrium pressure from the hydrogen storage alloy 8 in the container 9 is provided. connected by. Here, the hydrogen storage alloys 8 and 16 include:
For example, a lanthanum nickel alloy is used, and by changing the proportion of the alloy, the reaction temperature with hydrogen gas is changed. Further, within this container 17, a cooling coil 19 through which cooling water flows is disposed so as to be buried in the granular hydrogen storage alloy 16.
このように構成されるホツトガス除霜装置で
は、冷却装置の冷却運転時に、3方切換弁3が第
1ポート3aと第3ポート3cが結ばれるよに切
換えられ、開閉弁11,20が閉成され、開閉弁
4およびサクシヨン主弁13が開成される。これ
により冷却運転時には、圧縮機1から吐出される
ホツトガス冷媒が3方切換弁3を通り容器9内の
コイル10に流されて、低圧側の水素吸蔵合金8
が加熱される。水素吸蔵合金8が加熱されると圧
力が上がり合金8に吸蔵されていた水素ガスが放
出される。放出された水素ガスは、配管18を通
り容器17に移動し、水素吸蔵合金16と反応し
合金16に吸収される。このとき、水素吸蔵合金
16が反応熱により発熱するので、冷却コイル1
9によつて合金16を冷却する。図中、実線の矢
印で示す方法が、冷却運転時の冷媒の流れ方向と
なつている。 In the hot gas defrosting device configured as described above, during cooling operation of the cooling device, the three-way switching valve 3 is switched so that the first port 3a and the third port 3c are connected, and the on-off valves 11 and 20 are closed and closed. Then, the on-off valve 4 and suction main valve 13 are opened. As a result, during cooling operation, the hot gas refrigerant discharged from the compressor 1 passes through the three-way switching valve 3 and flows into the coil 10 in the container 9, and the hydrogen storage alloy 8 on the low pressure side
is heated. When the hydrogen storage alloy 8 is heated, the pressure increases and the hydrogen gas stored in the alloy 8 is released. The released hydrogen gas moves to the container 17 through the pipe 18, reacts with the hydrogen storage alloy 16, and is absorbed by the alloy 16. At this time, the hydrogen storage alloy 16 generates heat due to the heat of reaction, so the cooling coil 1
9 to cool the alloy 16. In the figure, the direction indicated by the solid arrow is the flow direction of the refrigerant during cooling operation.
一方、冷却器7の除霜時には、3方切換弁3が
第1ポート3aと第2ポート3bが結ばれるよう
に切換えられ、開閉弁4およびサクシヨン主弁1
3が閉成され、開閉弁11,20が開成される。
これにより、図中破線の矢印で示すように圧縮機
1から吐出されるホツトガス冷媒は、容器9内の
コイル10を通られず分岐配管12を通つて冷却
器7に供給され、冷却器7の除霜が行なわれる。
このとき、ホツトガス冷媒は冷却器7の冷却コイ
ル7aを通過することで凝縮されて液化する。冷
却器7の出た凝縮液冷媒は、容器9内のコイル1
5に通されることで、低圧側の水素吸蔵合金8の
冷却が行なわれる。冷却されて水素吸吸蔵合金8
の圧力が低下することで、今度は水素ガスが高圧
側の水素吸蔵合金16から放出されて、低圧側の
水素吸蔵合金8側に移動し、合金8に吸収され
る。このとき低圧側の水素吸蔵合金8は、水素ガ
スの吸収反応で発熱し、この発熱によつてコイル
15に通される凝縮液冷媒の蒸発が促進される。
ガス化した冷媒は圧縮機1に送られる。この際、
高圧側の水素吸蔵合金16は、水素ガスの放出反
応で吸熱するので、冷却コイル19に通される冷
却水によつて大気の熱を補うようにする。 On the other hand, when defrosting the cooler 7, the three-way switching valve 3 is switched so that the first port 3a and the second port 3b are connected, and the on-off valve 4 and the suction main valve 1 are switched.
3 is closed, and the on-off valves 11 and 20 are opened.
As a result, the hot gas refrigerant discharged from the compressor 1 is supplied to the cooler 7 through the branch pipe 12 without passing through the coil 10 in the container 9, as shown by the broken line arrow in the figure. Defrosting is performed.
At this time, the hot gas refrigerant passes through the cooling coil 7a of the cooler 7 and is condensed and liquefied. The condensed refrigerant discharged from the cooler 7 is transferred to the coil 1 in the container 9.
5, the hydrogen storage alloy 8 on the low pressure side is cooled. Cooled hydrogen storage alloy 8
As the pressure decreases, hydrogen gas is released from the hydrogen storage alloy 16 on the high pressure side, moves to the hydrogen storage alloy 8 side on the low pressure side, and is absorbed by the alloy 8. At this time, the hydrogen storage alloy 8 on the low pressure side generates heat due to the hydrogen gas absorption reaction, and this heat generation promotes evaporation of the condensed liquid refrigerant passed through the coil 15.
The gasified refrigerant is sent to the compressor 1. On this occasion,
Since the hydrogen storage alloy 16 on the high pressure side absorbs heat due to the hydrogen gas release reaction, the heat of the atmosphere is supplemented by the cooling water passed through the cooling coil 19.
ここで、コイル15に通される凝縮液冷媒の液
量が増れば、低圧側の水素吸蔵合金8の温度が下
がり圧力も低下するので、高圧側の水素吸蔵合金
16からの移動水素ガス量が増加し、合金8での
水素ガス吸収によるる発熱が増大する。これによ
り、コイル15に通される凝縮液冷媒量と水素吸
蔵合金8での水素ガス吸収による発生熱とのバラ
ンスがとれ、液冷媒の蒸発が一定条件で行われる
ようになる。 Here, if the amount of condensed refrigerant passed through the coil 15 increases, the temperature of the hydrogen storage alloy 8 on the low pressure side decreases and the pressure also decreases, so the amount of hydrogen gas transferred from the hydrogen storage alloy 16 on the high pressure side increases, and heat generation due to absorption of hydrogen gas in alloy 8 increases. Thereby, the amount of condensed refrigerant passed through the coil 15 and the heat generated by hydrogen gas absorption in the hydrogen storage alloy 8 are balanced, and the liquid refrigerant is evaporated under constant conditions.
以上説明したように本発明では、熱平衡圧力の
異なる2種類の水素吸蔵合金をそれぞれ容器に封
入し、水素吸蔵合金の水素ガス吸入時の発生熱を
利用し、除霜後の凝縮液冷媒の蒸発を行なうよう
にしているので、従来のタンク方式のように水槽
が滞留水によつて腐食するような不具合はない。
As explained above, in the present invention, two types of hydrogen storage alloys with different thermal equilibrium pressures are each sealed in a container, and the heat generated when the hydrogen storage alloy sucks hydrogen gas is used to evaporate the condensed liquid refrigerant after defrosting. Therefore, unlike conventional tank systems, there is no problem of corrosion of the water tank due to accumulated water.
また本発明によれば、縮液冷媒を蒸発するため
の充分な熱量が得られるので、液冷媒を効率よく
ガス化できる。たとえば従来のタンク方式のもの
と比較した場合、水を使用するタンク方式では、
温度差を50℃とすると容積当りの蓄熱量は50kca
l/であるが、水素吸蔵合金(2つの容器を使用
する場合)では70〜100kcal/の蓄熱量が得られ
る。 Further, according to the present invention, sufficient heat for evaporating the condensed liquid refrigerant can be obtained, so that the liquid refrigerant can be efficiently gasified. For example, when compared to a conventional tank system, a tank system that uses water has
If the temperature difference is 50℃, the amount of heat storage per volume is 50kca
1/1, but with a hydrogen storage alloy (when two containers are used), a heat storage amount of 70 to 100 kcal/ is obtained.
第1図は本発明に係るホツトガス除霜装置の構
成図、第2図は従来の除霜装置の構成図である。
図中、1……圧縮機、2……吐出配管、3……
3方切換弁、4,11,20……開閉弁、5……
凝縮器、6……膨張弁、7……冷却器、7a……
冷却コイル、8,16……水素吸蔵合金、9,1
7……容器、10,15……熱交換コイル、12
……分岐配管、13……サクシヨン主弁、14…
…吸入配管、18……配管、19……冷却コイ
ル。
FIG. 1 is a configuration diagram of a hot gas defrosting device according to the present invention, and FIG. 2 is a configuration diagram of a conventional defrosting device. In the figure, 1...compressor, 2...discharge piping, 3...
3-way switching valve, 4, 11, 20... Open/close valve, 5...
Condenser, 6... Expansion valve, 7... Cooler, 7a...
Cooling coil, 8, 16...Hydrogen storage alloy, 9, 1
7... Container, 10, 15... Heat exchange coil, 12
...Branch piping, 13...Suction main valve, 14...
...Suction piping, 18...Piping, 19...Cooling coil.
Claims (1)
個別に封入した容器を設け、これら容器間を配管
で連結し、熱平衡圧力の低い水素吸蔵合金を封入
した容器に第1、第2の熱交換コイルを設け、冷
却運転時に上記第1の熱交換コイルに圧縮機から
吐出されるホツトガス冷媒を通し、冷却器の除霜
時には上記第1の熱交換コイルへのホツトガス冷
媒の供給を停止して、冷却器にホツトガス冷媒を
通すとともに、上記第2の熱交換コイルに冷却器
の除霜後の凝縮液冷媒を通すことを特徴とするホ
ツトガス除霜装置。1. Providing containers in which hydrogen storage alloys with different thermal equilibrium pressures are individually sealed, and connecting these containers with piping, and providing first and second heat exchange coils in the containers in which hydrogen storage alloys with low thermal equilibrium pressures are sealed. During the cooling operation, the hot gas refrigerant discharged from the compressor is passed through the first heat exchange coil, and when the cooler is defrosted, the supply of the hot gas refrigerant to the first heat exchange coil is stopped and the hot gas refrigerant is passed through the cooler. A hot gas defrosting device characterized in that a hot gas refrigerant is passed through the hot gas refrigerant, and condensed liquid refrigerant after defrosting of the cooler is passed through the second heat exchange coil.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62121962A JPS63289400A (en) | 1987-05-19 | 1987-05-19 | Hot gas defrosting device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62121962A JPS63289400A (en) | 1987-05-19 | 1987-05-19 | Hot gas defrosting device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63289400A JPS63289400A (en) | 1988-11-25 |
| JPH0378550B2 true JPH0378550B2 (en) | 1991-12-16 |
Family
ID=14824204
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62121962A Granted JPS63289400A (en) | 1987-05-19 | 1987-05-19 | Hot gas defrosting device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS63289400A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006234328A (en) * | 2005-02-25 | 2006-09-07 | Hoshizaki Electric Co Ltd | Ice making machine |
-
1987
- 1987-05-19 JP JP62121962A patent/JPS63289400A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS63289400A (en) | 1988-11-25 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US4646539A (en) | Transport refrigeration system with thermal storage sink | |
| AU2012215130A1 (en) | Flash defrost system | |
| JP5904628B2 (en) | Refrigeration cycle with refrigerant pipe for defrost operation | |
| JPH0378550B2 (en) | ||
| JPH09119725A (en) | Dual freezer | |
| JP2548269Y2 (en) | Gasoline cooling system | |
| JPH0820139B2 (en) | Heat storage type heat pump device | |
| JPS5875675A (en) | Air-cooling or refrigerating device utilizing solar heat | |
| JPH051966U (en) | Refrigeration equipment | |
| JP2940839B2 (en) | Air conditioning | |
| JPH0737867B2 (en) | Defroster for dual cryogenic refrigerator | |
| JPS645732Y2 (en) | ||
| JPH01169283A (en) | Refrigerating cycle | |
| JP2940838B2 (en) | Air conditioning | |
| JPS62773A (en) | Heat accumulation type refrigerator | |
| JPS6143194Y2 (en) | ||
| JPS5842839Y2 (en) | Defrost device for refrigeration cycle | |
| JPH09119726A (en) | Dual freezer | |
| JP2876893B2 (en) | Absorption type ice cold storage device | |
| JPH0445749B2 (en) | ||
| KR950004396Y1 (en) | Arrangement for vaporising residuum of liquid refrigerant | |
| JPS6243249Y2 (en) | ||
| JPS61184366A (en) | Heat pump type hot-water supply device | |
| JPH0459546B2 (en) | ||
| JPH0571858B2 (en) |