JPH10332178A - Heat storage type low-temperature air supply system - Google Patents

Heat storage type low-temperature air supply system

Info

Publication number
JPH10332178A
JPH10332178A JP13988397A JP13988397A JPH10332178A JP H10332178 A JPH10332178 A JP H10332178A JP 13988397 A JP13988397 A JP 13988397A JP 13988397 A JP13988397 A JP 13988397A JP H10332178 A JPH10332178 A JP H10332178A
Authority
JP
Japan
Prior art keywords
ice
heat storage
air
low
heat
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.)
Withdrawn
Application number
JP13988397A
Other languages
Japanese (ja)
Inventor
Seiji Shibuya
誠司 澁谷
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP13988397A priority Critical patent/JPH10332178A/en
Publication of JPH10332178A publication Critical patent/JPH10332178A/en
Withdrawn legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To widely utilize a system, for example, for an amusement facility requiring a low-temperature storage and a low-temperature atmosphere for storing, for example, vegetables and fruits in an aircraft that is being parked at an airport, by supplying an ice slurry to an air heat exchanger, and performing heat exchange with air and then supplying low-temperature air. SOLUTION: A freeze 5 is operated by utilizing inexpensive power at night time, and cold water that is pumped up from a heat storage bath 7 by a cold water pump 12 is cooled to overcooled state by an evaporator 6. The overcooled water 13 is guided to the heat storage bath 7, the overcooled state is canceled in the heat storage bath 7, and ice in sherbet state with a large heat storage density is generated and heat is stored. Preferably, the ratio of ice is approximately 60%. An ice-unloading device 2 mixes sherbet-shaped ice 8 being stored with cold water when low-temperature air needs to be supplied and manufactures an ice slurry 9. The ratio of the ice 9 in the ice slurry 9 is adjusted to approximately 1.5, thus supplying low-temperature air at approximately 3 deg.C.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、蓄熱式低温空気供
給システムに関する。例えば、空港における駐機中の航
空機内を冷却するための航空機冷却装置、野菜又は果物
等を保存する低温倉庫、低温雰囲気を必要とするアミュ
ーズメント施設等に広く利用できる。
[0001] The present invention relates to a regenerative cold air supply system. For example, the present invention can be widely used in an aircraft cooling device for cooling an aircraft parked at an airport, a low-temperature warehouse for storing vegetables or fruits, and an amusement facility requiring a low-temperature atmosphere.

【0002】[0002]

【従来の技術】従来の蓄熱式低温空気供給システムの一
例を図2に示す。このシステムでは、夜間の安価な電力
を利用し、冷凍機21を使用して直接蒸発コイル22で
蓄熱槽31内の低温潜熱蓄熱物質23を−10℃程度ま
で冷却して潜熱を蓄える。そして、低温空気が必要な時
に、潜熱を蓄えた低温潜熱蓄熱物質23を蓄熱槽31よ
り汲み出し、低温潜熱物質ポンプ24にてブライン熱交
換器25へ送り、ブライン熱交換器25でブライン(不
凍液)と熱交換して−2℃程度の低温ブラインを製造
し、ブラインポンプ26を備えたブライン循環回路28
にて空気熱交換器27へ送給する。更に、この低温ブラ
インを空気熱交換器27にて空気と交換することにより
低温空気29を供給する。
2. Description of the Related Art FIG. 2 shows an example of a conventional regenerative cold air supply system. In this system, low-temperature latent heat storage material 23 in heat storage tank 31 is cooled to about −10 ° C. by direct evaporation coil 22 using refrigerator 21 to store latent heat using inexpensive power at night. Then, when low-temperature air is required, the low-temperature latent heat storage material 23 storing the latent heat is pumped out of the heat storage tank 31, sent to the brine heat exchanger 25 by the low-temperature latent heat substance pump 24, and brine (antifreeze) is used by the brine heat exchanger 25. Heat is exchanged to produce a low temperature brine of about -2 ° C., and a brine circulation circuit 28 having a brine pump 26.
To the air heat exchanger 27. Further, the low-temperature brine is exchanged with air in the air heat exchanger 27 to supply low-temperature air 29.

【0003】また他の従来の蓄熱式低温空気供給システ
ムを図3に示す。このシステムでは、夜間の安価な電力
を利用し、冷凍機41を使用してブラインを−15℃程
度まで蒸発器42で冷却し、そのブラインにより蓄熱槽
43内に充填されたカプセル44内の低温潜熱蓄熱物質
45としての氷を−10℃程度まで冷却して潜熱を蓄え
る。そして、低温空気が必要な時に、ブラインを蓄熱槽
43に供給し、潜熱を蓄えた低温潜熱蓄熱物質45と熱
交換させて−2℃程度の低温ブラインを製造し、ブライ
ンポンプ47を備えたブライン循環回路49にて空気熱
交換器48へ送給する。更に、この低温ブラインを、空
気熱交換器48にて空気と熱交換することにより低温空
気50を供給する。
FIG. 3 shows another conventional regenerative cold air supply system. In this system, the brine is cooled to about −15 ° C. by an evaporator 42 using a refrigerator 41 by using inexpensive electric power at night, and the brine cools a capsule 44 filled in a heat storage tank 43 by the brine. Ice as the latent heat storage material 45 is cooled to about −10 ° C. to store the latent heat. Then, when low-temperature air is required, the brine is supplied to the heat storage tank 43 and exchanged heat with the low-temperature latent heat storage material 45 storing the latent heat to produce a low-temperature brine of about −2 ° C. The air is supplied to the air heat exchanger 48 in the circulation circuit 49. Further, the low-temperature brine is heat-exchanged with air in the air heat exchanger 48 to supply low-temperature air 50.

【0004】[0004]

【発明が解決しようとする課題】[Problems to be solved by the invention]

(1)従来の蓄熱式低温空気供給システムでは夜間に蓄
熱する場合、冷凍機21,41で低温潜熱蓄熱物質2
3,45を−10℃程度まで冷却する必要があるため、
冷凍機21,41の冷媒蒸発温度を低くする必要があ
り、冷凍機21,41の入力に対する蓄熱量の比すなわ
ち成績係数が低い。 (2)低温潜熱蓄熱物質23から冷熱を取り出す時にブ
ラインを使用する必要があり、その管理に注意が必要で
ある。 (3)低温潜熱蓄熱物質23は一般に蓄熱密度が小さ
く、蓄熱槽31の容量が大きくなる。また、潜熱蓄熱物
質23とブラインの熱交換器25が必要であり、それぞ
れにポンプ24,26を必要とする。よってシステムと
しての設置スペースが広くなる。 (4)低温潜熱蓄熱物質45をカプセル44内に封入す
る方法では、蓄熱時及び放熱時において熱抵抗が大きい
という不都合がある。
(1) In the conventional regenerative low-temperature air supply system, when storing heat at night, low-temperature latent heat storage material 2 is stored in refrigerators 21 and 41.
Since it is necessary to cool 3,45 to about -10 ° C,
It is necessary to lower the refrigerant evaporation temperature of the refrigerators 21 and 41, and the ratio of the heat storage amount to the input of the refrigerators 21 and 41, that is, the coefficient of performance is low. (2) When extracting cold from the low-temperature latent heat storage material 23, it is necessary to use brine, and care must be taken in its management. (3) The low-temperature latent heat storage material 23 generally has a low heat storage density, and the capacity of the heat storage tank 31 increases. Further, a latent heat storage material 23 and a brine heat exchanger 25 are required, and pumps 24 and 26 are required respectively. Therefore, the installation space as a system is widened. (4) The method of encapsulating the low-temperature latent heat storage material 45 in the capsule 44 has a disadvantage that the thermal resistance is large during heat storage and heat release.

【0005】[0005]

【課題を解決するための手段】[Means for Solving the Problems]

(1)蓄熱槽の冷水を直接冷凍機の蒸発器で冷却し、過
冷却状態のまま蓄熱槽に移送し、蓄熱槽で過冷却状態を
解除しシャーベット状の氷を生成し蓄熱する。 (2)低温空気の供給が必要な時、蓄熱槽のシャーベッ
ト状の氷を氷払出装置により冷水と混合して氷スラリー
を製造する。 (3)氷スラリーを空気熱交換器に供給し、空気と熱交
換させて低温空気を供給する。
(1) The cold water in the heat storage tank is directly cooled by the evaporator of the refrigerator, transferred to the heat storage tank in a supercooled state, released from the supercooled state in the heat storage tank, and sherbet-like ice is generated and stored. (2) When the supply of low-temperature air is required, the sherbet-like ice in the heat storage tank is mixed with cold water by an ice dispenser to produce an ice slurry. (3) The ice slurry is supplied to an air heat exchanger and exchanged with air to supply low-temperature air.

【0006】〔作用〕 (1)蓄熱槽の冷水を直接冷凍機の蒸発器で過冷却状態
に冷却する。このとき、冷水を−10℃まで冷却する必
要が無く、冷媒の蒸発温度が高くできる。 (2)蓄熱時に蓄熱材の冷水との間の熱抵抗が増加しな
いため、連続して一定の蓄熱が可能である。 (3)過冷却水は蓄熱槽内で過冷却を解除され、蓄熱密
度の大きいシャーベット状の氷として蓄熱される。 (4)蓄熱槽より氷を払い出して氷スラリーを製造する
とき、氷の割合を高くすることにより、熱輸送密度を大
きくでき、単位輸送熱量当たりの配管断面積を小さくで
き、配管口径を小さくして配管設備費が低減できる。 (5)空気熱交換器へ供給される氷スラリーの温度は0
℃であり、空気熱交換器を介して、3℃程度の低温空気
が供給される。
[Operation] (1) The cold water in the heat storage tank is directly cooled to a supercooled state by the evaporator of the refrigerator. At this time, there is no need to cool the cold water to −10 ° C., and the evaporation temperature of the refrigerant can be increased. (2) Since the thermal resistance between the heat storage material and the cold water does not increase during heat storage, constant heat storage is possible continuously. (3) The supercooled water is released from the supercooling in the heat storage tank, and is stored as sherbet-like ice having a large heat storage density. (4) When dispensing ice from the heat storage tank to produce an ice slurry, by increasing the percentage of ice, the heat transfer density can be increased, the pipe cross-sectional area per unit heat transfer can be reduced, and the pipe diameter can be reduced. Piping equipment costs can be reduced. (5) The temperature of the ice slurry supplied to the air heat exchanger is zero.
° C, and low-temperature air of about 3 ° C is supplied via an air heat exchanger.

【0007】[0007]

【発明の実施の形態】本発明の一実施例に係る蓄熱式低
温空気供給システムを図1に示す。本実施例の蓄熱式低
温空気供給システムは、蓄熱槽7の冷水を直接冷凍機5
の蒸発器6で冷却し、過冷却状態のまま蓄熱槽7に移送
し、蓄熱槽7で過冷却状態を解除してシャーベット状の
氷8を生成し蓄熱する過冷却式氷蓄熱装置1と、蓄熱槽
7から氷8を冷水中に払い出して氷スラリー9を製造す
る氷払出装置2と、氷スラリー9と空気を熱交換し低温
冷風を供給する空気熱交換器3と、氷払出装置2と空気
熱交換器3とを結び氷スラリーを循環させる氷スラリー
循環回路4よりなる。
FIG. 1 shows a regenerative low-temperature air supply system according to an embodiment of the present invention. The regenerative low-temperature air supply system of the present embodiment uses the cold water in the heat storage tank
A supercooling type ice heat storage device 1 that cools in an evaporator 6, transfers the supercooled state to a heat storage tank 7 in a supercooled state, releases the supercooled state in the heat storage tank 7, generates sherbet-like ice 8, and stores heat. An ice dispensing device 2 for dispensing ice 8 from the heat storage tank 7 into cold water to produce an ice slurry 9; an air heat exchanger 3 for exchanging heat between the ice slurry 9 and air and supplying low-temperature cold air; An ice slurry circulation circuit 4 connects the air heat exchanger 3 and circulates the ice slurry.

【0008】過冷却式氷蓄熱装置1では、夜間の安価な
電力を利用して、冷凍機5を運転し、蓄熱槽7から冷水
ポンプ12にて汲み上げられた冷水を蒸発器6で過冷却
状態まで冷却する。このとき、冷水を−10℃まで冷却
する必要が無く、冷媒の蒸発温度が高くできる。冷却さ
れた過冷却水13は、蓄熱槽7に導かれ、蓄熱槽7内で
過冷却状態を解除し、蓄熱密度の大きいシャーベット状
の氷8を生成し蓄熱する。氷の比率は、6割程度が良
い。ここで、蓄熱時に蓄熱材の冷水13との間の熱抵抗
が増加しないため、連続して一定の蓄熱が可能である。
In the supercooled ice heat storage device 1, the refrigerator 5 is operated by using inexpensive electric power at night, and the cold water pumped from the heat storage tank 7 by the cold water pump 12 is supercooled by the evaporator 6. Cool down to At this time, there is no need to cool the cold water to −10 ° C., and the evaporation temperature of the refrigerant can be increased. The cooled supercooled water 13 is guided to the heat storage tank 7, releases the supercooled state in the heat storage tank 7, and generates sherbet-like ice 8 having a large heat storage density to store heat. The ratio of ice is preferably about 60%. Here, since the thermal resistance between the heat storage material and the cold water 13 during heat storage does not increase, constant heat storage is possible continuously.

【0009】氷払出装置2は、低温空気の供給が必要な
とき、蓄えられたシャーベット状の水8を冷水と混合し
て氷スラリ−9を製造する。氷スラリ−9における氷の
割合は1.5割程度まで調整される。蓄熱槽7より氷8
を払い出して氷スラリー9を製造するとき、氷の割合を
高くすることにより、熱輸送密度を大きくでき、単位輸
送熱量当たりの配管断面積を小さくでき、配管口径を小
さくして配管設備費が低減できる。
When the supply of low-temperature air is required, the ice dispenser 2 mixes the stored sherbet-like water 8 with cold water to produce an ice slurry 9. The ratio of ice in the ice slurry 9 is adjusted to about 1.5%. Ice 8 from thermal storage tank 7
When the ice slurry 9 is manufactured by dispensing water, the ratio of ice can be increased to increase the heat transport density, reduce the pipe cross-sectional area per unit heat transported, reduce the pipe diameter, and reduce piping equipment costs. it can.

【0010】氷スラリー循環回路4は、調整された氷ス
ラリー9を氷スラリーポンプ10により空気熱交換器3
へ供給し、更に、空気熱交換器3で熱交換して昇温した
氷スラリー9を蓄熱槽7または氷払出装置2へ戻す回路
である。空気熱交換器3へ供給される氷スラリー9の温
度は0℃である。空気熱交換器3は、送風機14により
供給された空気と氷スラリー9とを熱交換し、3℃程度
の低温空気11を航空機15へ供給し、駐機中の航空機
15内の機内を冷却する機器である。
The ice slurry circulation circuit 4 supplies the adjusted ice slurry 9 to the air heat exchanger 3 by an ice slurry pump 10.
This is a circuit for returning the ice slurry 9 heated by the heat exchange in the air heat exchanger 3 to the heat storage tank 7 or the ice discharging device 2. The temperature of the ice slurry 9 supplied to the air heat exchanger 3 is 0 ° C. The air heat exchanger 3 exchanges heat between the air supplied by the blower 14 and the ice slurry 9, supplies low-temperature air 11 of about 3 ° C. to the aircraft 15, and cools the inside of the aircraft 15 while parked. Equipment.

【0011】本実施例では、冷凍機5の凝縮器16は空
冷式となっているが、水冷式であってもかまわない。ま
た、空気熱交換器3の入口は航空機冷却後の空気であっ
てもかまわない。また、氷スラリー9の供給量が多く、
夜間蓄熱製造した氷だけでは対応できない場合、冷凍機
5を追い掛けて運転し、氷を製造して対応することも可
能である。
In the present embodiment, the condenser 16 of the refrigerator 5 is of an air-cooled type, but may be of a water-cooled type. Further, the inlet of the air heat exchanger 3 may be air after cooling the aircraft. Also, the supply amount of the ice slurry 9 is large,
When it is not possible to cope with only the ice produced by night-time heat storage, it is also possible to operate by chasing the refrigerator 5 to produce the ice.

【0012】[0012]

【発明の効果】以上、実施例に基づいて具体的に説明し
たように、本発明の蓄熱式低温空気供給システムによれ
ば、以下の効果を奏する。 (1)蓄熱槽の冷水を直接冷却する蒸発器を用いるた
め、冷媒の蒸発温度を高くでき、冷凍機の成績係数が高
く省エネルギーである。 (2)過冷却状態の冷水を解除してシャーベット状の氷
を生成する過冷却式氷蓄熱装置を用いるため、蓄熱時に
蓄熱材の冷水との間の熱抵抗が増加せず、連続して一定
の蓄熱が可能である。 (3)シャーベット状の氷として蓄熱する蓄熱槽を用い
るため、蓄熱密度が大きく、また、蓄熱材と空気熱交換
器への熱輸送媒体が同一であるため、熱交換器が別個に
不要であり、ポンプも1台でよく、よって省スペースと
なる。 (4)氷払出装置と熱交換器との間を氷スラリー循環回
路で結び、氷スラリーを循環させるため、氷スラリーの
氷の割合を高くすることにより、熱輸送密度を大きくで
き、また、単位輸送熱量当たりの配管断面積を小さくで
き、これにより、配管口径を小さくして配管設備費が低
減できる。 (5)温度が0℃である氷スラリーと熱交換して、3℃
程度の低温空気を供給できる空気熱交換器を用いるた
め、例えば、空港における駐機中の航空機内、野菜、果
物等を保存する低温倉庫、低温雰囲気を必要とするアミ
ューズメント施設等に広く利用可能である。 (6)水以外の蓄熱材、熱輸送媒体を使用しないため、
その材料費が安価であり、管理が容易である。
As described above, according to the embodiment, the regenerative low-temperature air supply system of the present invention has the following effects. (1) Since an evaporator for directly cooling the cold water in the heat storage tank is used, the evaporation temperature of the refrigerant can be increased, and the coefficient of performance of the refrigerator is high and energy is saved. (2) Since the supercooled ice heat storage device that releases the supercooled cold water to generate sherbet-like ice is used, the thermal resistance between the heat storage material and the cold water does not increase during heat storage, and is continuously constant. Heat storage is possible. (3) Since a heat storage tank for storing heat as sherbet-shaped ice is used, the heat storage density is high, and since the heat storage medium and the heat transport medium to the air heat exchanger are the same, a separate heat exchanger is not required. , Only one pump is required, which saves space. (4) Since the ice dispenser and the heat exchanger are connected by an ice slurry circulation circuit to circulate the ice slurry, the heat transport density can be increased by increasing the proportion of ice in the ice slurry, and the unit can be increased. The cross-sectional area of the pipe per heat transfer can be reduced, thereby reducing the pipe diameter and reducing the cost of piping equipment. (5) heat exchange with an ice slurry having a temperature of 0 ° C. and 3 ° C.
Because it uses an air heat exchanger that can supply air at a low temperature, it can be widely used in aircraft parked at airports, low-temperature warehouses for storing vegetables, fruits, etc., and amusement facilities that require a low-temperature atmosphere. is there. (6) Because heat storage materials and heat transport media other than water are not used,
The material cost is low and management is easy.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明の一実施例に係る蓄熱式低温空気供給シ
ステムの概略説明図である。
FIG. 1 is a schematic explanatory view of a regenerative low-temperature air supply system according to one embodiment of the present invention.

【図2】従来の蓄熱式低温空気供給システムに係る概略
説明図である。
FIG. 2 is a schematic explanatory diagram relating to a conventional regenerative low-temperature air supply system.

【図3】従来の蓄熱式低温空気供給システムに係る概略
説明図である。
FIG. 3 is a schematic explanatory diagram relating to a conventional regenerative low-temperature air supply system.

【符号の説明】[Explanation of symbols]

1 過冷却氷蓄熱装置 2 氷払出装置 3 空気熱交換器 4 氷スラリー循環回路 5 冷凍機 6 蒸発器 7 蓄熱槽 8 氷 9 氷スラリー 10 氷スラリーポンプ 11 低温空気 12 冷水ポンプ 13 冷水(過冷却水) 14 送風機 15 航空機 16 凝縮器 REFERENCE SIGNS LIST 1 supercooled ice heat storage device 2 ice dispenser 3 air heat exchanger 4 ice slurry circulation circuit 5 refrigerator 6 evaporator 7 heat storage tank 8 ice 9 ice slurry 10 ice slurry pump 11 low temperature air 12 cold water pump 13 cold water (supercooled water ) 14 Blower 15 Aircraft 16 Condenser

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 蓄熱槽の冷水を直接冷凍機の蒸発器で冷
却し、過冷却状態のまま蓄熱槽に移送し、該蓄熱槽で過
冷却状態を解除してシャーベット状の氷を生成し蓄熱す
る過冷却式氷蓄熱装置と、前記蓄熱槽から氷を冷水中に
払い出して氷スラリーを製造する氷払出装置と、氷スラ
リーと空気を熱交換し低温冷風を供給する空気熱交換器
と、前記氷払出装置と前記空気熱交換器とを結び氷スラ
リーを循環させる氷スラリー循環回路よりなることを特
徴とする蓄熱式低温空気供給システム。
1. Cold water in a heat storage tank is directly cooled by an evaporator of a refrigerator, transferred to a heat storage tank in a supercooled state, and released from the supercooled state in the heat storage tank to generate sherbet-like ice. A supercooled ice heat storage device, an ice discharge device that discharges ice from the heat storage tank into cold water to produce an ice slurry, an air heat exchanger that exchanges heat between the ice slurry and air to supply low-temperature cold air, A regenerative low-temperature air supply system comprising an ice slurry circulation circuit that connects an ice dispenser and the air heat exchanger and circulates ice slurry.
JP13988397A 1997-05-29 1997-05-29 Heat storage type low-temperature air supply system Withdrawn JPH10332178A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13988397A JPH10332178A (en) 1997-05-29 1997-05-29 Heat storage type low-temperature air supply system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13988397A JPH10332178A (en) 1997-05-29 1997-05-29 Heat storage type low-temperature air supply system

Publications (1)

Publication Number Publication Date
JPH10332178A true JPH10332178A (en) 1998-12-15

Family

ID=15255812

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13988397A Withdrawn JPH10332178A (en) 1997-05-29 1997-05-29 Heat storage type low-temperature air supply system

Country Status (1)

Country Link
JP (1) JPH10332178A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108131761A (en) * 2017-12-27 2018-06-08 深圳市海吉源科技有限公司 Cold-storage groove liquid level is less than the simple chilled water storage system of refrigerating plant room
CN109049622A (en) * 2018-08-28 2018-12-21 扬中市惠丰包装有限公司 A kind of cooling constant temperature drainage trough of plastic material molding
WO2019051604A1 (en) * 2017-09-15 2019-03-21 Einhorn Mordechai Heat exchange systems and methods

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2019051604A1 (en) * 2017-09-15 2019-03-21 Einhorn Mordechai Heat exchange systems and methods
CN108131761A (en) * 2017-12-27 2018-06-08 深圳市海吉源科技有限公司 Cold-storage groove liquid level is less than the simple chilled water storage system of refrigerating plant room
CN109049622A (en) * 2018-08-28 2018-12-21 扬中市惠丰包装有限公司 A kind of cooling constant temperature drainage trough of plastic material molding
CN109049622B (en) * 2018-08-28 2020-10-23 扬中市惠丰包装有限公司 Plastic material shaping cooling constant temperature drainage groove

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