JP2795070B2 - Ice making equipment - Google Patents

Ice making equipment

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Publication number
JP2795070B2
JP2795070B2 JP4173995A JP17399592A JP2795070B2 JP 2795070 B2 JP2795070 B2 JP 2795070B2 JP 4173995 A JP4173995 A JP 4173995A JP 17399592 A JP17399592 A JP 17399592A JP 2795070 B2 JP2795070 B2 JP 2795070B2
Authority
JP
Japan
Prior art keywords
temperature
capacity
cold storage
storage material
cooling
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
Application number
JP4173995A
Other languages
Japanese (ja)
Other versions
JPH0618066A (en
Inventor
恭伸 奥村
伸二 松浦
弘二 松岡
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.)
Daikin Industries Ltd
Original Assignee
Daikin Kogyo Co 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 Daikin Kogyo Co Ltd filed Critical Daikin Kogyo Co Ltd
Priority to JP4173995A priority Critical patent/JP2795070B2/en
Publication of JPH0618066A publication Critical patent/JPH0618066A/en
Application granted granted Critical
Publication of JP2795070B2 publication Critical patent/JP2795070B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Description

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

【0001】[0001]

【産業上の利用分野】本発明は、空気調和装置等に使用
する製氷装置に係り、とくに管路の凍結防止対策に関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an ice making device used for an air conditioner or the like, and more particularly to a measure for preventing freezing of a pipeline.

【0002】[0002]

【従来の技術】この種の製氷装置は、特開平4−386
7号公報に開示されているように、蓄氷槽と過冷却生成
冷却器と過冷却解消部とを循環路により順次接続して水
または水溶液である蓄冷材の循環可能な閉回路を形成
し、過冷却生成冷却器で蓄冷材を過冷却し、蓄冷材の過
冷却状態を循環路内の過冷却解消部で解消してスラリー
状の氷化物を生成し、スラリー状の氷化物が混在する蓄
冷材を蓄氷槽まで流通して蓄氷槽に貯溜している。
2. Description of the Related Art This type of ice making apparatus is disclosed in Japanese Patent Application Laid-Open No. 4-386.
As disclosed in Japanese Patent Application Publication No. 7, the ice storage tank, the supercool generation / cooler, and the supercool elimination unit are sequentially connected by a circulation path to form a closed circuit capable of circulating a cold storage material such as water or an aqueous solution. Supercooling the regenerator material with a supercooling generation cooler, eliminating the supercooling state of the regenerator material in the supercooling elimination section in the circulation path to generate slurry-like iced matter, and slurry-like iced matter is mixed Cold storage material is distributed to the ice storage tank and stored in the ice storage tank.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、上記製
氷装置では、過冷却生成冷却器の具体的な運転手段は記
載されておらず、単に凝固点Tg より低い低温度で蓄冷
材を過冷却するだけでは、冷却温度Tの過冷却度(Tg
−T)が小さい場合には生成した氷化物は管路を閉塞し
やすいという問題がある。
However, in the above ice making apparatus, no specific operation means of the supercooling-generating cooler is described, and merely supercooling the cold storage material at a low temperature lower than the freezing point Tg is not described. , Supercooling degree of cooling temperature T (Tg
When -T) is small, there is a problem that the generated frost tends to block the pipeline.

【0004】すなわち、蓄冷材の凝固点温度より低温度
であるが過冷却度が小さい温度範囲(凍結発生温度帯)
では、過冷却度が小さいために過冷却状態の解消後に生
成するスラリー状の氷化物は柔らかく、水中に浮遊して
いる。そして、過冷却中の蓄冷材の温度低下速度が小さ
く上記凍結発生温度帯をゆっくり通過すると、上記の氷
化物が多量に生成され、氷化物が混在する蓄冷材は非常
に粘性が大きくなる。このため、過冷却解消部やその下
流側の循環路に氷化物が滞留して管路を閉塞する可能性
があり、管路閉塞防止のために製氷装置の発停回数が増
加して安定した連続運転ができないおそれがある。
That is, a temperature range in which the temperature is lower than the freezing point temperature of the cold storage material but the degree of supercooling is small (freezing occurrence temperature zone).
In this case, since the degree of subcooling is small, the slurry-like iced matter generated after the supercooled state is eliminated is soft and floats in water. When the temperature of the cold storage material during supercooling decreases slowly and passes slowly through the freezing temperature zone, a large amount of the above-mentioned iced material is generated, and the cold storage material containing the iced material has a very high viscosity. For this reason, there is a possibility that icy substances may stay in the subcooling elimination part and the circulation path downstream thereof and block the pipeline, and the number of times of starting and stopping the ice making device is increased to prevent the pipeline from being blocked, thereby stabilizing. Continuous operation may not be possible.

【0005】本発明は、かかる点に鑑みてなされたもの
であって、冷却手段の過冷却度が小さい領域における管
路の閉塞を防止することを目的としている。
[0005] The present invention has been made in view of the above, and an object of the present invention is to prevent blockage of a pipeline in a region where the degree of supercooling of a cooling means is small.

【0006】[0006]

【課題を解決するための手段】上記目的を達成するため
に、請求項1に係る発明が講じた手段は、冷却手段にお
ける出口温度が凍結発生温度帯に入ると出口温度を凝固
点温度近傍に維持する能力低下手段と、所定状態になる
と冷却手段の冷却能力を復帰する能力復帰手段とを設け
るものである。
Means for Solving the Problems In order to achieve the above object, the means according to the first aspect of the present invention is to maintain the outlet temperature near the freezing point temperature when the outlet temperature in the cooling means enters the freezing temperature range. And a capacity return means for returning the cooling capacity of the cooling means when a predetermined state is reached.

【0007】具体的には、請求項1に係る発明が講じた
手段は、図1(実線のみ)に示すように、スラリー状に
氷化された蓄冷材(W)を貯溜する蓄氷槽(21)と、
蓄冷材(W)を過冷却する冷却能力可変の冷却手段(2
5)とが順に蓄冷材(W)の循環可能に接続され、過冷
却された蓄冷材(W)の過冷却状態を解消して生成した
氷化物を上記蓄氷槽(21)に貯溜する製氷装置を前提
としている。
Specifically, as shown in FIG. 1 (only the solid line), the means adopted by the invention according to claim 1 is an ice storage tank (W) for storing a cold storage material (W) iced into a slurry. 21),
Cooling means (2) with a variable cooling capacity for supercooling the cold storage material (W)
5) are sequentially connected so that the cold storage material (W) can be circulated, and store iced products generated by eliminating the supercooled state of the supercooled cold storage material (W) in the ice storage tank (21). The device is assumed.

【0008】そして、上記冷却手段(25)を所定の冷
却能力に制御する能力制御手段(73)が設けられた構
成としている。
[0008] A capacity control means (73) for controlling the cooling means (25) to a predetermined cooling capacity is provided.

【0009】さらに、上記冷却手段(25)における蓄
冷材(W)の出口温度T2 を検出する出口温度検出手段
(Th1)が設けられた構成としている。
Further, an outlet temperature detecting means (Th1) for detecting an outlet temperature T2 of the cold storage material (W) in the cooling means (25) is provided.

【0010】その上、該出口温度検出手段(Th1)の温
度信号を受け、上記蓄冷材(W)の出口温度T2 が、蓄
冷材(W)の凝固点温度T0 に基づいて設定された所定
の設定温度範囲(K)に入ると、上記蓄冷材(W)の出
口温度T2 を上昇させることなく凝固点温度T0または
凝固点温度T0 近傍の所定値に維持するように、上記冷
却手段(25)の冷却能力を低下させる能力低下手段
(75)が設けられた構成としている。
In addition, upon receiving the temperature signal from the outlet temperature detecting means (Th1), the outlet temperature T2 of the cold storage material (W) is set at a predetermined value set based on the freezing point temperature T0 of the cold storage material (W). When the temperature falls into the temperature range (K), the cooling means (25) is maintained at the freezing point temperature T0 or at a predetermined value near the freezing point temperature T0 without increasing the outlet temperature T2 of the cold storage material (W). ) Is provided with a capacity reduction means (75) for reducing the cooling capacity.

【0011】さらにその上、該能力低下手段(75)に
よる冷却手段(25)の能力低下後に、所定状態になる
と、蓄冷材(W)を急速冷却して該蓄冷材(W)の出口
温度T2 が上記凝固点温度T0 または上記所定値から上
記設定温度範囲(K)よりも低い温度に速やかに移行す
るように上記冷却手段(25)の冷却能力を復帰させる
復帰信号を上記能力制御手段(73)に出力する能力復
帰手段(77)が設けられた構成としている。
In addition, when the cooling means (75) is reduced in capacity by the capacity reducing means (75) and enters a predetermined state, the cold storage material (W) is rapidly cooled and the outlet of the cold storage material (W) is discharged.
The temperature T2 is higher than the freezing point temperature T0 or the predetermined value.
Quickly transition to a temperature lower than the set temperature range (K)
As described above, a capacity return means (77) for outputting a return signal for returning the cooling capacity of the cooling means (25) to the capacity control means (73) is provided.

【0012】特に、請求項2に係る発明が講じた手段
は、能力復帰手段を、所定時間経過すると、冷却手段の
冷却能力を復帰させるように構成するものである。
[0012] In particular , according to a second aspect of the present invention, the capacity restoring means is configured to return the cooling capacity of the cooling means after a lapse of a predetermined time.

【0013】具体的には、請求項2に係る発明が講じた
手段は、図1(実線のみ)に示すように、請求項1に係
る発明の能力復帰手段(77)に代え、能力低下手段
(75)による冷却手段(25)の能力低下後に、所定
時間が経過すると、蓄冷材(W)を急速冷却して該蓄冷
材(W)の出口温度T2 が上記凝固点温度T0 または上
記所定値から上記設定温度範囲(K)よりも低い温度に
速やかに移行するように上記冷却手段の冷却能力を復帰
させる復帰信号を上記能力制御手段(73)に出力する
能力復帰手段(77)が設けられた構成としている。
Specifically, as shown in FIG. 1 (only the solid line), the means taken by the invention according to claim 2 replaces the capacity return means (77) according to the invention according to claim 1, and replaces the capacity reduction means. When a predetermined time has elapsed after the capacity of the cooling means (25) is reduced by (75), the cool storage material (W) is rapidly cooled to
The outlet temperature T2 of the material (W) is equal to or higher than the freezing point temperature T0.
From the specified value to a temperature lower than the set temperature range (K)
A capacity return means (77) for outputting a return signal for returning the cooling capacity of the cooling means to the capacity control means (73) so as to make a quick transition is provided.

【0014】また、請求項3に係る発明が講じた手段
は、能力復帰手段を、蓄冷材の入口温度が凝固点温度T
0 より高い所定の低温温度に達すると、冷却手段の冷却
能力を復帰させるように構成するものである。
Further, a means adopted by the invention according to claim 3 is that a capacity return means is provided, wherein the inlet temperature of the cold storage material is set to the freezing point temperature T.
When a predetermined low temperature higher than 0 is reached, the cooling capacity of the cooling means is restored.

【0015】具体的には、請求項3に係る発明が講じた
手段は、図1に示すように、請求項1に係る発明の製氷
装置に加えて、上記冷却手段(25)における蓄冷材
(W)の入口温度T1 を検出する入口温度検出手段(T
h2)が設けられた構成としている。
Specifically, as shown in FIG. 1, the means adopted by the invention according to claim 3 is, in addition to the ice making device according to the invention according to claim 1, a cold storage material (25) in the cooling means (25). W) Inlet temperature detecting means (T) for detecting the inlet temperature T1
h2).

【0016】さらに、請求項1に係る発明の能力復帰手
段(77)に代え、能力低下手段(75)による冷却手
段(25)の能力低下後に、上記入口温度検出手段(T
h2)の温度信号を受けて上記蓄冷材(W)の入口温度が
凝固点温度T0 より高い所定の低温温度T3 に達する
と、蓄冷材(W)を急速冷却して該蓄冷材(W)の出口
温度T2 が上記凝固点温度T0 または上記所定値から上
記設定温度範囲(K)よりも低い温度に速やかに移行す
るように上記冷却手段(25)の冷却能力を復帰させる
復帰信号を上記能力制御手段(73)に出力する能力復
帰手段(77)が設けられた構成としている。
Further, instead of the capacity return means (77) according to the first aspect of the present invention, after the capacity of the cooling means (25) is reduced by the capacity reduction means (75), the inlet temperature detection means (T
When the temperature of the cold storage material (W) reaches a predetermined low temperature T3 higher than the freezing point temperature T0 in response to the temperature signal of h2), the cold storage material (W) is rapidly cooled to exit the cold storage material (W).
The temperature T2 is higher than the freezing point temperature T0 or the predetermined value.
Quickly transition to a temperature lower than the set temperature range (K)
As described above, a capacity return means (77) for outputting a return signal for returning the cooling capacity of the cooling means (25) to the capacity control means (73) is provided.

【0017】さらに、請求項4に係る発明が講じた手段
は、能力復帰手段を、蓄冷材の入口温度が低能力運転開
始時の出口温度と上記凍結発生下限温度との間の温度差
分だけ低下すると、冷却手段の冷却能力を復帰させるよ
うに構成するものである。
The invention according to claim 4 is characterized in that the capacity return means reduces the temperature of the cold storage material by the temperature difference between the outlet temperature at the start of low capacity operation and the above-mentioned freezing occurrence lower limit temperature. Then, the cooling capacity of the cooling means is restored.

【0018】具体的には、請求項4に係る発明が講じた
手段は、図1に示すように、請求項3に係る発明と同様
の入口温度検出手段(Th2)を備える一方、請求項3に
係る発明の能力復帰手段(77)に代え、能力低下手段
(75)による冷却手段(25)の能力低下後に、上記
入口温度検出手段(Th2)の温度信号を受けて上記蓄冷
材(W)の入口温度T1 が上記能力低下手段(75)に
よる低能力運転開始時の出口温度T2 と上記凍結発生下
限温度Tf との間の温度差△T分だけ低能力運転開始時
より低下すると、上記冷却手段(25)の冷却能力を復
帰させる復帰信号を上記能力制御手段(73)に出力す
る能力復帰手段(77)が設けられた構成としている。
Specifically, as shown in FIG. 1, the means adopted by the invention according to claim 4 includes an inlet temperature detecting means (Th2) similar to the invention according to claim 3, while In place of the capacity return means (77) of the invention according to the invention, after the performance of the cooling means (25) is reduced by the capacity reducing means (75), the cold storage material (W) is received by receiving a temperature signal from the inlet temperature detecting means (Th2). When the inlet temperature T1 of the cooling water is lowered by a temperature difference ΔT between the outlet temperature T2 at the start of the low-capacity operation by the above-mentioned capacity lowering means (75) and the freezing occurrence lower limit temperature Tf from the start of the low-capacity operation, A capacity return means (77) for outputting a return signal for returning the cooling capacity of the means (25) to the capacity control means (73) is provided.

【0019】[0019]

【作用】上記の構成により、請求項1に係る発明では、
蓄氷槽(21)から流通する蓄冷材(W)が冷却手段
(25)で過冷却され、該蓄冷材(W)の過冷却状態が
解消されて生成した氷化物が上記蓄氷槽(21)に貯溜
される。
According to the first aspect of the present invention,
The cold storage material (W) flowing from the ice storage tank (21) is subcooled by the cooling means (25), and the supercooled state of the cold storage material (W) is eliminated, and the iced product generated is stored in the ice storage tank (21). ).

【0020】製氷開始当初等において、蓄冷材(W)の
出口温度T2 が設定温度範囲(K)に入ると、出口温度
検出手段(Th1)の温度信号を能力低下手段(75)が
受け、上記蓄冷材(W)の出口温度T2 が、蓄冷材
(W)の出口温度T2 が凝固点温度T0 または凝固点温
度T0 を維持するように冷却手段(25)の冷却能力を
低下させる。したがって、蓄冷材(W)は過冷却されな
いので管路の閉塞が防止されると共に、蓄氷槽(21)
の蓄冷材(W)が凝固点温度T0 または凝固点温度T0
近傍まで冷却され、冷却手段(25)における入口温度
T1 が低下することになる。
When the outlet temperature T2 of the cold storage material (W) falls within the set temperature range (K) at the beginning of ice making or the like, the temperature decreasing means (75) receives the temperature signal of the outlet temperature detecting means (Th1), and The outlet temperature T2 of the cold storage material (W) reduces the cooling capacity of the cooling means (25) so that the outlet temperature T2 of the cold storage material (W) maintains the freezing point temperature T0 or the freezing point temperature T0. Accordingly, since the cold storage material (W) is not supercooled, blockage of the pipeline is prevented, and the ice storage tank (21)
Is the freezing point temperature T0 or the freezing point temperature T0
As a result, the inlet temperature T1 in the cooling means (25) decreases.

【0021】そして、冷却手段(25)の能力低下後
に、蓄冷材(W)が所定状態、例えば、定常能力の通常
運転に復帰して蓄冷材(W)を冷却しても管路閉塞が生
じない過冷却状態になると、能力復帰手段(77)が冷
却手段(25)の冷却能力を復帰させる。能力低下手段
(75)による低能力運転中に入口温度T1 が所定状態
にまで低下しているので、冷却能力復帰直後の出口温度
T2 は管路閉塞が生じないような大きな過冷却度の温度
になる。
After the capacity of the cooling means (25) is reduced, even if the cold storage material (W) returns to a predetermined state, for example, normal operation with a steady capacity and cools the cold storage material (W), the pipeline blockage occurs. If there is no supercooling state, the capacity returning means (77) returns the cooling capacity of the cooling means (25). Since the inlet temperature T1 has dropped to a predetermined state during the low-capacity operation by the capacity reducing means (75), the outlet temperature T2 immediately after the return of the cooling capacity is set to a temperature with a large degree of supercooling such that the pipe line is not blocked. Become.

【0022】とくに、請求項2に係る発明では、所定時
間経過すると、能力復帰手段(77)が請求項1の所定
状態になったと判断して冷却手段(25)の冷却能力を
復帰させるので、能力復帰が簡単に行われる。
In particular, according to the second aspect of the present invention, after a lapse of a predetermined time, the capacity return means (77) determines that the predetermined state of the first aspect has been attained and returns the cooling capacity of the cooling means (25). Capability is easily restored.

【0023】また、請求項3に係る発明では、蓄冷材
(W)の入口温度T1 が凝固点温度T0 より高い所定の
低温温度T3 に達すると、能力復帰手段(77)が冷却
手段(25)の冷却能力を復帰させるので、該所定低温
温度T3 を、例えば、冷却能力復帰後の冷却によって出
口温度T2 が凍結発生下限温度Tf より低下するような
入口温度T1 に設定すれば、出口温度T2 は凍結発生温
度帯(K)を速やかに通過して、確実に管路の閉塞を防
止しながら冷却手段(25)の能力復帰がなされる。
According to the third aspect of the present invention, when the inlet temperature T1 of the cold storage material (W) reaches a predetermined low temperature T3 higher than the freezing point temperature T0, the capacity return means (77) turns on the cooling means (25). Since the cooling capacity is restored, if the predetermined low temperature T3 is set to, for example, an inlet temperature T1 at which the outlet temperature T2 becomes lower than the freezing occurrence lower limit temperature Tf by cooling after the cooling capacity is restored, the outlet temperature T2 becomes frozen. The cooling means (25) is returned to capacity while quickly passing through the generated temperature zone (K) and reliably preventing blockage of the pipeline.

【0024】さらに、請求項4に係る発明では、蓄冷材
(W)の入口温度T1 が低能力運転開始時の出口温度T
2 と凍結発生下限温度Tf との間の温度差△T分だけ低
下すると、冷却手段(25)の冷却能力を復帰させるの
で、必要な温度低下分だけ冷却能力が低下し、必要以上
に能力を低下させた低能力運転が起こらない。
Further, in the invention according to claim 4, the inlet temperature T1 of the cold storage material (W) is lower than the outlet temperature T at the start of the low capacity operation.
If the temperature difference ΔT between the temperature 2 and the freezing occurrence lower limit temperature Tf is reduced by ΔT, the cooling capacity of the cooling means (25) is restored, so that the cooling capacity is reduced by the necessary temperature reduction and the capacity is increased more than necessary. Reduced low capacity driving does not occur.

【0025】[0025]

【発明の効果】以上のように、請求項1に係る発明によ
れば、蓄冷材の出口温度T2 の過冷却度が小さい製氷開
始当初において、能力低下手段(75)により蓄冷材
(W)が凝固点温度T0 または凝固点温度T0 近傍の温
度で冷却されることにより、管路の閉塞を防止しながら
入口温度T1 を低下することができる。このため、冷却
手段(25)の冷却能力復帰直後より管路閉塞が発生す
るおそれのある危険状態を越えた過冷却状態に移行する
ことができ、安定した製氷運転を連続して行うことがで
きる。
As described above, according to the first aspect of the present invention, at the beginning of ice making when the supercooling degree of the outlet temperature T2 of the cold storage material is small, the cold storage material (W) is reduced by the capacity reducing means (75). By cooling at the freezing point temperature T0 or at a temperature close to the freezing point temperature T0, the inlet temperature T1 can be reduced while preventing the blockage of the pipeline. Therefore, immediately after the return of the cooling capacity of the cooling means (25), it is possible to shift to a supercooling state that exceeds a dangerous state in which a pipe blockage may occur, and it is possible to continuously perform a stable ice making operation. .

【0026】また、請求項2に係る発明によれば、能力
復帰手段(77)が所定時間経過すれば冷却手段(2
5)の冷媒能力を復帰させるので、簡単に管路の閉塞を
防止しながら定常運転に移行することができる。
Further, according to the second aspect of the present invention, the cooling means (2) is activated when the capacity return means (77) elapses a predetermined time.
Since the refrigerant capacity of 5) is restored, it is possible to easily shift to the steady operation while preventing blockage of the pipeline.

【0027】また、請求項3に係る発明によれば、蓄冷
材(W)の入口温度T1 が凝固点温度T0 より高い所定
の低温温度T3 に達すると、能力復帰手段(77)が冷
却手段(25)の冷却能力を復帰させるので、確実に管
路の凍結を防止しつつ冷却手段(25)の能力復帰を行
うことができる。
According to the third aspect of the present invention, when the inlet temperature T1 of the cold storage material (W) reaches the predetermined low temperature T3 higher than the freezing point temperature T0, the capacity return means (77) turns the cooling means (25). Since the cooling capacity of the cooling means (25) can be surely prevented, the cooling means (25) can be restored in capacity while preventing freezing of the pipeline.

【0028】さらに、請求項4に係る発明によれば、蓄
冷材(W)の入口温度T1 が低能力運転開始時の出口温
度T2 と凍結発生下限温度Tf との間の温度差分だけ低
下すると、冷却手段(25)の冷却能力を復帰させるの
で、冷却能力低下量が機種の違い等による流量差の影響
を受けることがなく、必要以上に能力を低下させた低能
力運転の実行を防止することができる。
Further, according to the invention of claim 4, when the inlet temperature T1 of the cold storage material (W) decreases by the temperature difference between the outlet temperature T2 at the start of the low capacity operation and the freezing occurrence lower limit temperature Tf, Since the cooling capacity of the cooling means (25) is restored, the cooling capacity reduction amount is not affected by a flow rate difference due to a difference in model, etc., and execution of a low capacity operation in which the capacity is reduced more than necessary is prevented. Can be.

【0029】[0029]

【実施例】以下、本発明の実施例を図面に基づき説明す
る。
Embodiments of the present invention will be described below with reference to the drawings.

【0030】図2および図3は請求項1および2に係る
発明の第1実施例を示す。図2は、本実施例の製氷装置
(Y)を備えた空気調和装置の全体構成を示し、室外ユ
ニット(X)に対して、複数の室内ユニット(A),
(A),…が接続されたいわゆるマルチ形空気調和装置
である。
FIGS. 2 and 3 show a first embodiment of the present invention. FIG. 2 shows the overall configuration of an air conditioner provided with the ice making device (Y) of the present embodiment, wherein a plurality of indoor units (A),
(A), ... is what is called a multi-type air conditioner connected.

【0031】上記室外ユニット(X)においては、
(1)は第1圧縮機、(11)は第2圧縮機、(2)は
図中実線と図中破線との2方向に切り換わる四路切換
弁、(3)は冷房運転時には凝縮器として暖房運転時に
は蒸発器として機能する熱源側空気熱交換器としての室
外熱交換器、(4)は通常冷房運転時には冷媒流量調節
弁として機能し、暖房運転時と蓄熱冷房運転時とには冷
媒圧力を減圧する高熱源側減圧機構として機能する室外
電動膨脹弁である。
In the outdoor unit (X),
(1) is a first compressor, (11) is a second compressor, (2) is a four-way switching valve that switches in two directions, a solid line and a broken line in the figure, and (3) is a condenser during cooling operation. An outdoor heat exchanger as a heat source side air heat exchanger that functions as an evaporator during a heating operation, and (4) functions as a refrigerant flow rate control valve during a normal cooling operation, and a refrigerant flows during a heating operation and a regenerative cooling operation. This is an outdoor electric expansion valve that functions as a high heat source side pressure reducing mechanism that reduces the pressure.

【0032】一方、各室内ユニット(A),(A),…
は、同一構成のものが並列に接続されており、(6)は
冷房運転時には利用側減圧機構として機能し、暖房運転
時には冷媒流量調整弁として機能する室内電動膨脹弁、
(7)は冷房運転時には蒸発器として、暖房運転時には
凝縮器として機能する利用側熱交換器としての室内熱交
換器である。
On the other hand, each of the indoor units (A), (A),.
Are electrically connected in parallel, and (6) is an indoor electric expansion valve that functions as a use side pressure reducing mechanism during cooling operation and functions as a refrigerant flow control valve during heating operation.
(7) is an indoor heat exchanger as a use side heat exchanger that functions as an evaporator during a cooling operation and as a condenser during a heating operation.

【0033】そして、上記第1圧縮機(1)と、四路切
換弁(2)と、室外熱交換器(3)と、室外電動膨脹弁
(4)とが順次接続された高熱源側回路(B)と、室外
電動膨脹弁(4)側より各室内ユニットの(A),
(A),…の室内電動膨脹弁(6),(6),…と室内
熱交換器(7),(7),…とが順次接続された利用側
回路(C)とが形成され、高熱源側回路(B)の室外電
動膨脹弁(4)側と利用側回路(C)の室内電動膨脹弁
(6),(6),…側とが接続部(g)において接続さ
れる一方、利用側回路(C)の室内熱交換器(7),
(7),…側は四路切換弁(2)に接続されて、冷媒が
可逆循環して室外空気との熱交換によって得た熱を室内
空気に放出するヒートポンプ作用を有する主冷媒回路
(E)が形成されている。
A high heat source side circuit in which the first compressor (1), the four-way switching valve (2), the outdoor heat exchanger (3), and the outdoor electric expansion valve (4) are sequentially connected. (B) and (A) and (A) of each indoor unit from the outdoor electric expansion valve (4) side.
The indoor electric expansion valves (6), (6),... Of (A), and the indoor heat exchangers (7), (7),. The outdoor electric expansion valve (4) side of the high heat source side circuit (B) and the indoor electric expansion valves (6), (6),... Side of the utilization side circuit (C) are connected at the connection part (g). , The indoor heat exchanger (7) of the use side circuit (C),
The (7),... Sides are connected to the four-way switching valve (2), and the main refrigerant circuit (E) has a heat pump function of releasing the heat obtained by reversible circulation of the refrigerant and heat exchange with the outdoor air to the indoor air. ) Is formed.

【0034】また、主冷媒回路(E)には、高熱源側回
路(B)に対して並列に低熱源側回路(H)が接続さ
れ、つまり、低熱源側回路(H)は、一端が第1圧縮機
(1)の吸込側に、他端が上記接続部(g)に接続され
ている。低熱源側回路(H)には、第1圧縮機(1)側
より第2圧縮機(11)と、低熱源側熱交換器(13)
と、蓄熱冷房運転時に流量調整をする低熱源側電動膨脹
弁(14)とが順次接続されている。第1圧縮機(1)
の吐出側と第2圧縮機(11)の吐出側との間には、第
1圧縮機(1)から第2圧縮機(11)への冷媒の流入
を阻止する逆止弁(17)と、ピークカット用電磁弁
(19)とが並列に接続されている。また、上記空気調
和装置には、冷媒との熱交換により冷熱を蓄熱する蓄熱
運転と、この蓄熱を利用して冷房を行う蓄熱冷房運転と
を行うための製氷装置(Y)が配置されている。
A low heat source side circuit (H) is connected to the main refrigerant circuit (E) in parallel with the high heat source side circuit (B). That is, the low heat source side circuit (H) has one end. The other end is connected to the suction portion of the first compressor (1) and to the connection portion (g). The low heat source side circuit (H) includes a second compressor (11) from the first compressor (1) side and a low heat source side heat exchanger (13).
And a low heat source side electric expansion valve (14) for adjusting the flow rate during the heat storage cooling operation. First compressor (1)
A check valve (17) between the discharge side of the first compressor and the discharge side of the second compressor (11) for preventing refrigerant from flowing from the first compressor (1) to the second compressor (11); , And a peak cut solenoid valve (19) are connected in parallel. Further, the air conditioner is provided with an ice making device (Y) for performing a heat storage operation for storing cold heat by exchanging heat with a refrigerant and a heat storage cooling operation for performing cooling using the heat storage. .

【0035】該製氷装置(Y)は、スラリー状に氷化さ
れた蓄冷材(W)を貯溜して冷熱を蓄熱する蓄氷槽(2
1)と、ポンプ(23)と、冷媒との熱交換によって蓄
冷材(W)を過冷却する冷却手段としての過冷却生成熱
交換器(25)と、蓄冷材(W)の過冷却状態を解消す
る過冷却解消部(27)とが循環路(29)によって蓄
冷材(W)の循環可能に順次接続されて閉回路に形成さ
れている。蓄冷材(W)としては、水または水溶液が用
いられる。
The ice making device (Y) stores the cold storage material (W) iced in a slurry state and stores cold heat therein.
1), a pump (23), a supercooling-generating heat exchanger (25) as a cooling means for supercooling the cold storage material (W) by heat exchange with a refrigerant, and a supercooling state of the cold storage material (W). The subcooling elimination part (27) to be eliminated is sequentially connected to the regenerative material (W) by a circulation path (29) so as to allow the regenerative material (W) to circulate, thereby forming a closed circuit. Water or an aqueous solution is used as the cold storage material (W).

【0036】また、過冷却生成熱交換器(25)と過冷
却解消部(27)との間の製氷装置(Y)には、過冷却
解消部(27)における過冷却状態の解消によって生成
した氷化物が循環路(29)の管壁に付着して凍結が発
生した場合に過冷却生成熱交換器(25)への凍結進展
を防止するための凍結進展防止部(31)が介設されて
いる。
The ice making device (Y) between the subcooling generation heat exchanger (25) and the subcooling elimination section (27) is generated by eliminating the supercooling state in the supercooling elimination section (27). A freezing prevention unit (31) is provided to prevent freezing from propagating to the supercooling generation heat exchanger (25) when the freezing occurs due to the adhesion of the frost to the pipe wall of the circulation path (29). ing.

【0037】また、ポンプ(23)と過冷却生成熱交換
器(25)との間の製氷装置(Y)には、上記低熱源側
熱交換器(13)が介設されている。該低熱源側熱交換
器(13)は、蓄熱運転時には蓄冷材(W)を予熱する
凝縮器として機能し、蓄熱冷房運転時には冷媒と蓄冷材
(W)との熱交換により冷熱を回収する凝縮器として機
能するように構成されている。
The low heat source side heat exchanger (13) is provided in the ice making device (Y) between the pump (23) and the supercooling generation heat exchanger (25). The low heat source side heat exchanger (13) functions as a condenser for preheating the cold storage material (W) during the heat storage operation, and condensing for recovering cold heat by exchanging heat between the refrigerant and the cold storage material (W) during the heat storage cooling operation. It is configured to function as a vessel.

【0038】また、上記製氷装置(Y)の過冷却生成熱
交換器(25)への冷熱の供給を目的として、主冷媒回
路(E)には過冷却生成回路(F)が接続されている。
該過冷却生成回路(F)は、流入端(33a)が主冷媒
回路(E)の接続部(g)に接続され、低熱源側回路
(H)との共通管路(35)を経て分岐部(37)で低
熱源側回路(H)と分岐して流出端(33b)が両圧縮
機(1),(11)の吸込側に接続されている。過冷却
生成回路(F)には、接続部(g)側より蓄熱運転時に
減圧機構として機能する水側電動膨脹弁(39)と、過
冷却生成熱交換器(25)とが順次介設されている。
Further, a supercooling generation circuit (F) is connected to the main refrigerant circuit (E) for the purpose of supplying cold heat to the supercooling generation heat exchanger (25) of the ice making device (Y). .
The subcooling generation circuit (F) has an inflow end (33a) connected to the connection part (g) of the main refrigerant circuit (E), and branches via a common conduit (35) with the low heat source side circuit (H). The branch (37) branches off from the low heat source side circuit (H) and the outlet end (33b) is connected to the suction side of both compressors (1) and (11). In the supercool generation circuit (F), a water-side electric expansion valve (39) functioning as a pressure reducing mechanism during the heat storage operation from the connection part (g) side, and a supercool generation heat exchanger (25) are sequentially provided. ing.

【0039】過冷却生成熱交換器(25)は、満液式で
あって、液冷媒の液面を調整して冷却能力が制御される
ようになっている。
The supercooling-generating heat exchanger (25) is of a liquid full type, and the cooling capacity is controlled by adjusting the liquid level of the liquid refrigerant.

【0040】また、凍結進展防止部(31)への暖熱の
供給を目的として、第2圧縮機(11)の吐出側に流入
端(41a)が、過冷却生成回路(F)の水側電動膨脹
弁(39)より上流側に流出端(41b)がそれぞれ接
続されて第1バイパス路(41)が形成され、該第1バ
イパス路(41)には流入端(41a)側より凍結進展
防止部(31)と冷媒冷却用電動膨脹弁(43)とが介
設されている。
Further, for the purpose of supplying warming heat to the freezing progress preventing section (31), an inflow end (41a) is provided at the discharge side of the second compressor (11), and the water side of the subcooling generation circuit (F). Outflow ends (41b) are respectively connected to the upstream side of the electric expansion valve (39) to form a first bypass passage (41), and the first bypass passage (41) freezes from the inflow end (41a) side. The prevention part (31) and the refrigerant cooling electric expansion valve (43) are interposed.

【0041】さらに、過冷却解消部(27)への冷熱の
供給を目的として、第1バイパス路(41)の冷媒冷却
用電動膨脹弁(43)より下流側に流入端(45a)
が、過冷却生成回路(F)の過冷却生成熱交換器(2
5)より下流側に流出端(45b)がそれぞれ接続され
て第2バイパス路(45)が形成され、該第2バイパス
路(45)には過冷却解消部(27)が介設されてい
る。
Further, for the purpose of supplying cold heat to the subcooling elimination section (27), the inflow end (45a) of the first bypass passage (41) is located downstream of the refrigerant cooling electric expansion valve (43).
Is the supercooling generation heat exchanger (2) of the supercooling generation circuit (F).
5) The outflow ends (45b) are connected to the downstream side, respectively, to form a second bypass passage (45), and a subcooling eliminating section (27) is interposed in the second bypass passage (45). .

【0042】さらに、室外熱交換器(3)より下流側の
高熱源側回路(B)には、室外電動膨脹弁(4)と、フ
ラッシュガスをガス抜きする気液分離器(61)とが順
次介設されている。室外電動膨脹弁(4)は、蓄熱冷房
運転時において、室外熱交換器(3)の流量調整弁とし
てのみ機能して、室外熱交換器(3)の過冷却制御をす
るように構成されている。
Further, in the high heat source side circuit (B) downstream of the outdoor heat exchanger (3), an outdoor electric expansion valve (4) and a gas-liquid separator (61) for degassing flash gas are provided. It is interposed sequentially. The outdoor electric expansion valve (4) is configured to function only as a flow control valve of the outdoor heat exchanger (3) and perform supercooling control of the outdoor heat exchanger (3) during the heat storage cooling operation. I have.

【0043】該気液分離器(61)は、室外熱交換器
(3)からの凝縮冷媒をガス冷媒と液冷媒とに分離し、
該気液分離器(61)のガス流出口(63)に一端が接
続されたガス通路(65)の他端が過冷却生成回路
(F)を介して両圧縮機(1),(11)の吸込側に接
続されて、気液分離器(61)が分離したガス冷媒をガ
ス通路(65)が高熱源側回路(B)よりガス抜きする
ようになっている。ガス通路(65)には、開閉弁(6
6)と、流量調整機構としての第1キャピラリーチュー
ブ(67)とが介設されている。
The gas-liquid separator (61) separates the condensed refrigerant from the outdoor heat exchanger (3) into a gas refrigerant and a liquid refrigerant,
The other end of the gas passage (65), one end of which is connected to the gas outlet (63) of the gas-liquid separator (61), is connected to both compressors (1), (11) via a subcooling generation circuit (F). The gas passage (65) vents the gas refrigerant separated by the gas-liquid separator (61) from the high heat source side circuit (B). The gas passage (65) has an on-off valve (6
6) and a first capillary tube (67) as a flow rate adjusting mechanism are interposed.

【0044】そして、各種運転モードに応じて、上記各
弁の切り換えあるいは開度の調節を行い、冷媒の循環経
路を切り換えるように構成されている。次に、上記空気
調和装置の各運転モードにおける回路構成と冷媒の循環
動作について説明する。図2に示すように、通常冷房運
転時には、四路切換弁(2)を実線側に切り換え、低熱
源側電動膨脹弁(14)と、水側電動膨脹弁(39)
と、冷媒冷却用電動膨脹弁(43)と、ピークカット用
電磁弁(19)とを閉制御する一方、室外電動膨脹弁
(4)と、室内電動膨脹弁(6),(6),…とを開制
御して、冷媒が主冷媒回路(E)のみを流れる運転制御
状態にする。第1圧縮機(1)および第2圧縮機(1
1)の吐出冷媒は、室外熱交換器(3)で凝縮し、室内
電動膨脹弁(6),(6),…で減圧された後、室内熱
交換器(7),(7),…で蒸発して両圧縮機(1),
(11)に戻る。
The valves are switched or their openings are adjusted in accordance with the various operation modes to switch the refrigerant circulation path. Next, a circuit configuration and a refrigerant circulation operation in each operation mode of the air conditioner will be described. As shown in FIG. 2, during the normal cooling operation, the four-way switching valve (2) is switched to the solid line side, and the low heat source side electric expansion valve (14) and the water side electric expansion valve (39).
, The refrigerant cooling electric expansion valve (43) and the peak cut solenoid valve (19) are closed, while the outdoor electric expansion valve (4) and the indoor electric expansion valves (6), (6),. Are controlled to be in an operation control state in which the refrigerant flows only through the main refrigerant circuit (E). The first compressor (1) and the second compressor (1
The refrigerant discharged in 1) is condensed in the outdoor heat exchanger (3) and decompressed by the indoor electric expansion valves (6), (6),..., And then the indoor heat exchangers (7), (7),. Evaporates at both compressors (1),
Return to (11).

【0045】暖房運転時には、四路切換弁(2)を破線
側に切り換え、低熱源電動膨脹弁(14)と、水側電動
膨脹弁(39)と、冷媒冷却用電動膨脹弁(43)と、
ピークカット用電磁弁(19)とを閉制御する一方、室
外電動膨脹弁(4)と、室内電動膨脹弁(6),
(6),…とを開制御して、冷媒が主冷媒回路(E)の
みを流れる運転制御状態にする。両圧縮機(1),(1
1)の吐出冷媒は、室内熱交換器(7),(7),…で
凝縮し、室外電動膨脹弁(4)で減圧された後、室外熱
交換器(3)で蒸発して両圧縮機(1),(11)に戻
る。
During the heating operation, the four-way switching valve (2) is switched to the broken line side, and the low heat source electric expansion valve (14), the water-side electric expansion valve (39), and the refrigerant cooling electric expansion valve (43) are used. ,
While closing the peak cut solenoid valve (19), the outdoor electric expansion valve (4), the indoor electric expansion valve (6),
(6), ... are controlled to be in an operation control state in which the refrigerant flows only through the main refrigerant circuit (E). Both compressors (1), (1
The refrigerant discharged in 1) is condensed in the indoor heat exchangers (7), (7),..., Decompressed by the outdoor electric expansion valve (4), and then evaporated in the outdoor heat exchanger (3) to compress both refrigerants. Return to machines (1) and (11).

【0046】蓄熱運転時には、四路切換弁(2)を実線
側に切り換え、室外電動膨脹弁(4)と、低熱源側電動
膨脹弁(14)と、水側電動膨脹弁(39)と、冷媒冷
却用電動膨脹弁(43)とを開制御する一方、室内電動
膨脹弁(6),(6),…と、ピークカット用電磁弁
(19)とを閉制御して、高熱源側回路(B)と、低熱
源側回路(H)と、過冷却生成回路(F)と、第1バイ
パス路(41)と、第2バイパス路(45)とが冷媒の
流通可能な状態になる一方、利用側回路(C)への冷媒
の流通が遮断される運転制御状態にする。第1圧縮機
(1)の吐出冷媒は、室外熱交換器(3)で凝縮し、過
冷却生成回路(F)に流れ、水側電動膨脹弁(39)で
減圧された後過冷却生成熱交換器(25)で蒸発し、高
熱源側回路(B)に再び流入して第1圧縮機(1)に戻
る。
During the heat storage operation, the four-way switching valve (2) is switched to the solid line side, and the outdoor electric expansion valve (4), the low heat source side electric expansion valve (14), the water side electric expansion valve (39), While the refrigerant cooling electric expansion valve (43) is controlled to be open, the indoor electric expansion valves (6), (6),... And the peak cut solenoid valve (19) are controlled to be closed, so that the high heat source side circuit is controlled. (B), the low heat source side circuit (H), the subcooling generation circuit (F), the first bypass path (41), and the second bypass path (45) while the refrigerant is in a state where it can be circulated. Then, the operation control state is set in which the circulation of the refrigerant to the use side circuit (C) is interrupted. Refrigerant discharged from the first compressor (1) is condensed in the outdoor heat exchanger (3), flows into the supercooling generation circuit (F), is depressurized by the water-side electric expansion valve (39), and is then cooled by the supercooling heat. It evaporates in the exchanger (25), flows again into the high heat source side circuit (B), and returns to the first compressor (1).

【0047】一方、第2圧縮機(11)の吐出冷媒は、
第1バイパス路(41)と低熱源側回路(H)とに分岐
する。第1バイパス路(41)に流れた冷媒は、凍結進
展防止部(31)で凝縮し、冷媒冷却用電動膨脹弁(4
3)で減圧されて冷媒温度が0℃より低温に冷却された
後、一部が第2バイパス路(45)に分岐して過冷却解
消部(27)で蒸発して過冷却生成回路(F)を経て第
2圧縮機(11)に戻る。冷媒の残部はそのまま第1バ
イパス路(41)を流れて過冷却生成回路(F)に合流
し、過冷却解消部(27)を経て第2圧縮機(11)に
戻る。
On the other hand, the refrigerant discharged from the second compressor (11)
It branches to a first bypass path (41) and a low heat source side circuit (H). The refrigerant flowing into the first bypass passage (41) is condensed in the freeze-prevention preventing section (31), and the refrigerant-cooled electric expansion valve (4) is condensed.
After the pressure is reduced in 3) and the refrigerant temperature is cooled to a temperature lower than 0 ° C., a part thereof branches to the second bypass passage (45) and evaporates in the subcooling elimination section (27) to evaporate. ), And returns to the second compressor (11). The remainder of the refrigerant flows through the first bypass path (41) as it is, joins the supercool generation circuit (F), and returns to the second compressor (11) via the supercool elimination section (27).

【0048】また、低熱源側回路(H)に流れた冷媒
は、低熱源側熱交換器(13)で凝縮し、分岐部(3
7)で高熱源側回路(B)からの液冷媒と合流して過冷
却生成回路(F)に流れ、過冷却生成熱交換器(25)
を経て第2圧縮機(11)に戻る。
The refrigerant flowing to the low heat source side circuit (H) is condensed in the low heat source side heat exchanger (13) and is condensed in the branch (3).
In 7), the liquid refrigerant from the high heat source side circuit (B) is combined with the liquid refrigerant and flows into the supercool generation circuit (F), where the supercool generation heat exchanger (25)
And returns to the second compressor (11).

【0049】上記冷媒流通状態において、冷媒は、低熱
源側熱交換器(13)で蓄冷材(W)を予熱して蓄冷材
(W)中に氷化物が混在している場合には該氷化物を融
解し、過冷却生成熱交換器(25)で循環路(29)を
流通する蓄冷材(W)を過冷却し、凍結進展防止部(3
1)で循環路(29)の管壁を加温して凍結の進展を防
止し、過冷却解消部(27)で蓄冷材(W)の過冷却状
態を解消して氷化を開始させてスラリー状の氷化物を生
成する。そして、氷化物は蓄氷槽(21)に貯溜されて
冷熱が蓄えられる。
In the above-described refrigerant flowing state, the refrigerant preheats the cold storage material (W) in the low heat source side heat exchanger (13). The supercooled material (W) flowing through the circulation path (29) is supercooled by the supercooling generation heat exchanger (25),
In 1), the pipe wall of the circulation path (29) is heated to prevent the progress of freezing, and the supercooling elimination section (27) eliminates the supercooled state of the cold storage material (W) to start icing. Produces slurry ice. The iced material is stored in an ice storage tank (21) to store cold heat.

【0050】蓄熱冷房運転時には、四路切換弁(2)が
実線側に切り換えられ、水側電動膨脹弁(39)と、冷
媒冷却用電動膨脹弁(43)と、ピークカット用電磁弁
(19)とを閉制御する一方、室外電動膨脹弁(4)
と、室内電動膨脹弁(6),(6),…と、低熱源側電
動膨脹弁(14)とを開制御して、冷媒が高熱源側回路
(B)と低熱源側回路(H)とに分流する冷媒が利用側
回路(C)に合流して流れる運転制御状態にする。高熱
源側回路(B)における第1圧縮機(1)の吐出冷媒
は、室外熱交換器(3)で凝縮され、室外電動膨脹弁
(4)で低熱源側回路(H)の液管圧力にまで減圧され
る一方、低熱源側回路(H)における第2圧縮機(1
1)の吐出冷媒は、低熱源側熱交換器(13)で凝縮さ
れ、両凝縮冷媒は主冷媒回路(E)の接続部(g)で合
流して利用側回路(C)に流れ、室内電動膨脹弁
(6),(6),…で減圧され、室内熱交換器(7),
(7),…で蒸発した後高熱源側回路(B)に流入し、
両圧縮機(1),(11)に戻る。
During the heat storage cooling operation, the four-way switching valve (2) is switched to the solid line side, and the water-side electric expansion valve (39), the refrigerant cooling electric expansion valve (43), and the peak cut solenoid valve (19) are used. ) And the outdoor electric expansion valve (4)
, And the indoor electric expansion valves (6), (6),... And the low heat source side electric expansion valve (14) are controlled to open so that refrigerant flows into the high heat source side circuit (B) and the low heat source side circuit (H). The operation control state is such that the refrigerant diverted to and flows into the utilization side circuit (C). Refrigerant discharged from the first compressor (1) in the high heat source side circuit (B) is condensed in the outdoor heat exchanger (3), and the liquid pressure of the low heat source side circuit (H) is passed through the outdoor electric expansion valve (4). , And the second compressor (1) in the low heat source side circuit (H).
The discharged refrigerant of 1) is condensed in the low heat source side heat exchanger (13), and both condensed refrigerants join at the connection part (g) of the main refrigerant circuit (E) and flow to the utilization side circuit (C), and are indoors. The pressure is reduced by the electric expansion valves (6), (6), ..., and the indoor heat exchanger (7),
After evaporating in (7), ..., it flows into the high heat source side circuit (B),
Return to both compressors (1) and (11).

【0051】そして、蓄熱冷房運転時において、室外電
動膨脹弁(4)の減圧によって下流側の高熱源側回路
(B)で発生したフラッシュガスは気液分離器(61)
で液冷媒より分離される。一方、開閉弁(66)を開制
御して、ガス通路(65)を冷媒流通可能にする。フラ
ッシュガスは、ガス通路(65)によって低圧の両圧縮
機(1),(11)の吸込側にガス抜きされ、キャピラ
リーチューブ(67)のガス抜き量に対応する乾き度に
まで高熱源側回路(B)の液管圧力が低下し、低熱源側
熱交換器(13)の凝縮温度と第2圧縮機入力とは低い
値に保持される。
During the heat storage / cooling operation, the flash gas generated in the downstream high heat source side circuit (B) due to the pressure reduction of the outdoor electric expansion valve (4) is supplied to the gas-liquid separator (61).
Is separated from the liquid refrigerant. On the other hand, the on-off valve (66) is controlled to open so that the refrigerant can flow through the gas passage (65). The flash gas is vented to the suction side of the low-pressure compressors (1) and (11) by the gas passage (65), and the high heat source side circuit is dried to a dryness corresponding to the gas venting amount of the capillary tube (67). The liquid pipe pressure in (B) decreases, and the condensing temperature of the low heat source side heat exchanger (13) and the input of the second compressor are kept at low values.

【0052】さらに、上記蓄熱冷房運転の一態様とし
て、電力使用量がピークに達する日中においては、蓄熱
だけを利用する蓄熱専用冷房運転を行う。つまり、上記
蓄熱冷房運転時の回路切換動作において、室外電動膨脹
弁(4)を閉制御して高熱源側回路(B)を遮断する一
方、ピークカット用電磁弁(19)を開制御して第1圧
縮機(1)からの冷媒を低熱源側回路(H)に流通させ
る運転制御状態にする。両圧縮機(1),(11)の吐
出冷媒は、低熱源側熱交換器(13)だけで凝縮される
ので、日中の圧縮機の容量を減少することができ、電力
使用量の低減と安定した冷房運転が可能になる。
Further, as one mode of the heat storage cooling operation, during the daytime when the electric power consumption reaches a peak, a heat storage only cooling operation using only heat storage is performed. That is, in the circuit switching operation at the time of the heat storage cooling operation, the outdoor electric expansion valve (4) is controlled to be closed to cut off the high heat source side circuit (B), and the peak cut solenoid valve (19) is controlled to be opened. An operation control state is set in which the refrigerant from the first compressor (1) flows through the low heat source side circuit (H). Since the refrigerant discharged from both compressors (1) and (11) is condensed only in the low heat source side heat exchanger (13), the capacity of the compressor during the day can be reduced, and the power consumption is reduced. And stable cooling operation becomes possible.

【0053】次に、本発明の特徴として、過冷却生成熱
交換器(25)の出口配管には、蓄冷材(W)の出口温
度T2 を検出する出口温度検出手段としての出口温度セ
ンサ(Th1)が配設されている。また、図示しないが、
入口側のディストリビュータからの分岐管に、蓄冷材
(W)の入口温度T1 を検出する入口温度検出手段とし
ての入口温度センサ(Th2)が配設されている。
Next, as a feature of the present invention, an outlet temperature sensor (Th1) serving as an outlet temperature detecting means for detecting an outlet temperature T2 of the cold storage material (W) is provided at the outlet pipe of the supercooling / generation heat exchanger (25). ) Are arranged. Although not shown,
An inlet temperature sensor (Th2) as inlet temperature detecting means for detecting the inlet temperature T1 of the cold storage material (W) is provided in a branch pipe from the inlet side distributor.

【0054】上記出口温度センサ(Th1)と入口温度セ
ンサ(Th2)とはコントローラ(G)に接続され、該コ
ントローラ(G)には能力制御手段(73)と、能力低
下手段(75)と、能力復帰手段(77)とが内蔵され
ている。能力制御手段(73)は、過冷却生成熱交換器
(25)を所定の冷却能力に制御するように構成されて
いる。
The outlet temperature sensor (Th1) and the inlet temperature sensor (Th2) are connected to a controller (G). The controller (G) has a capacity control means (73), a capacity reduction means (75), A capacity return means (77) is built in. The capacity control means (73) is configured to control the supercooling generation heat exchanger (25) to a predetermined cooling capacity.

【0055】能力低下手段(75)は、出口温度センサ
(Th1)の温度信号を受け、上記蓄冷材(W)の出口温
度T2 が、蓄冷材(W)の凝固点温度T0 に基づいて設
定された所定の設定温度範囲に入ると、蓄冷材(W)の
出口温度T2 が凝固点温度T0 を維持するように過冷却
生成熱交換器(25)の冷却能力を低下させるように構
成されている。
The capacity reducing means (75) receives the temperature signal from the outlet temperature sensor (Th1), and sets the outlet temperature T2 of the cold storage material (W) based on the freezing point temperature T0 of the cold storage material (W). When the temperature falls within a predetermined set temperature range, the cooling capacity of the supercooling heat exchanger (25) is reduced so that the outlet temperature T2 of the cold storage material (W) maintains the freezing point temperature T0.

【0056】上記設定温度範囲としては、該蓄冷材
(W)の凝固点温度T0 より低温で該凝固点温度T0 よ
り低い所定の凍結発生下限温度Tf (例えば、−1℃)
以上の温度範囲の凍結発生温度帯(K)に設定されてい
る。
The above-mentioned set temperature range is a predetermined freezing limit lower temperature Tf lower than the freezing point temperature T0 of the cold storage material (W) and lower than the freezing point temperature T0 (for example, -1 ° C.).
It is set in the freezing occurrence temperature zone (K) in the above temperature range.

【0057】さらに、能力復帰手段(77)は、能力低
下手段(75)による過冷却生成熱交換器(25)の能
力低下後に、所定状態になると過冷却生成熱交換器(2
5)の冷却能力を復帰させる復帰信号を能力制御手段
(73)に出力するように構成されている。蓄冷材
(W)の所定状態としては、定常能力の通常運転に復帰
して蓄冷材(W)を冷却しても管路閉塞が生じない過冷
却状態に設定されている。
Further, the capacity return means (77), when the capacity of the supercooling heat exchanger (25) is reduced by the capacity reducing means (75), when the supercooling heat exchanger (2) enters a predetermined state,
It is configured to output a return signal for returning the cooling capacity of 5) to the capacity control means (73). The predetermined state of the cold storage material (W) is set to a supercooled state in which even when the cold storage material (W) is cooled by returning to the normal operation of the steady capacity and the cold storage material (W) is not blocked.

【0058】そして、請求項2に係る発明の特徴とし
て、能力復帰手段(77)は、所定時間(例えば、10
分間)が経過すると上記所定状態になったと判別して復
帰信号を能力制御手段(73)に出力するように構成さ
れている。
As a feature of the invention according to claim 2, the ability return means (77) is provided for a predetermined time (for example, 10 minutes).
After the elapse of (minutes), it is determined that the above-mentioned predetermined state has been reached, and a return signal is output to the capability control means (73).

【0059】次に、上記過冷却生成熱交換器(25)の
作動について説明する。蓄氷槽(21)から流通する蓄
冷材(W)が過冷却生成熱交換器(25)で過冷却さ
れ、該蓄冷材(W)の過冷却状態を解消して生成した氷
化物を上記蓄氷槽(21)に貯溜される。
Next, the operation of the supercooling heat exchanger (25) will be described. The cold storage material (W) flowing from the ice storage tank (21) is supercooled by the supercooling generation heat exchanger (25), and the supercooled state of the cold storage material (W) is eliminated, and the generated icing material is stored in the supercooling material (W). It is stored in an ice tank (21).

【0060】過冷却生成熱交換器(25)の冷却能力は
能力制御手段(73)によって能力制御され、過冷却生
成熱交換器(25)における蓄冷材(W)の出口温度T
2 は、蓄冷材(W)の凝固点温度T0 と該凝固点温度T
0 より低い所定の凍結発生下限温度Tf との間の凍結発
生温度帯(K)より低温の所定値に保持される。蓄熱運
転開始当初のいわゆるプルダウン運転時においては、図
3に示すように、過冷却生成熱交換器(25)における
蓄冷材(W)の入口温度T1 と出口温度T2 とは所定温
度差(例えば、3℃)を保って低下していく。
The cooling capacity of the supercool generation heat exchanger (25) is controlled by the capacity control means (73), and the outlet temperature T of the cold storage material (W) in the supercool generation heat exchanger (25).
2 is the freezing point temperature T0 of the cold storage material (W) and the freezing point temperature T
The temperature is kept at a predetermined value lower than the freezing occurrence temperature zone (K) between the predetermined freezing occurrence lower limit temperature Tf lower than 0. At the time of the so-called pull-down operation at the beginning of the heat storage operation, as shown in FIG. 3, a predetermined temperature difference between the inlet temperature T1 and the outlet temperature T2 of the cold storage material (W) in the supercooling heat exchanger (25) (for example, (3 ° C).

【0061】そして、蓄冷材(W)の出口温度T2 が凍
結発生温度帯(K)に入ると、出口温度センサ(Th1)
の温度信号を能力低下手段(75)が受け、上記蓄冷材
(W)の出口温度T2 が凝固点温度T0 を維持するよう
に過冷却生成熱交換器(25)の冷却能力を低下させ
る。したがって、蓄冷材(W)は過冷却されないので管
路の閉塞が防止されると共に、蓄氷槽(21)の蓄冷材
(W)が凝固点温度T0近傍まで冷却され、過冷却生成
熱交換器(25)における入口温度T1 が低下すること
になる。
When the outlet temperature T2 of the cold storage material (W) enters the freezing occurrence temperature zone (K), the outlet temperature sensor (Th1)
Is received by the capacity reducing means (75), and the cooling capacity of the supercooling heat exchanger (25) is reduced so that the outlet temperature T2 of the cold storage material (W) maintains the freezing point temperature T0. Therefore, since the regenerator material (W) is not supercooled, the blockage of the pipeline is prevented, and the regenerator material (W) in the ice storage tank (21) is cooled to near the freezing point temperature T0, and the supercooling heat exchanger ( The inlet temperature T1 in 25) will decrease.

【0062】そして、過冷却生成熱交換器(25)の能
力低下後に、所定時間が経過すると上記所定状態になっ
たと判断し、能力復帰手段(77)が過冷却生成熱交換
器(25)の冷却能力を復帰させる。能力低下手段(7
5)による低能力運転中に入口温度T1 が所定状態にま
で低下しているので、冷却能力復帰直後の出口温度T2
は管路閉塞が生じないような大きな過冷却度の温度にな
る。
After a predetermined time elapses after the performance of the supercooling generation heat exchanger (25) is reduced, it is determined that the above-mentioned predetermined state has been attained, and the capacity return means (77) is operated by the supercooling generation heat exchanger (25). Restore cooling capacity. Capability reduction means (7
Since the inlet temperature T1 has dropped to the predetermined state during the low capacity operation according to 5), the outlet temperature T2 immediately after the cooling capacity is restored.
Becomes a temperature with a large degree of supercooling so as not to block the pipeline.

【0063】本実施例によれば、蓄冷材の出口温度T2
の過冷却度が小さい製氷開始当初において、能力低下手
段(75)により蓄冷材(W)が凝固点温度T0 で冷却
されることにより、管路の閉塞を防止しながら入口温度
T1 を低下することができる。このため、過冷却生成熱
交換器(25)の冷却能力復帰直後より管路閉塞が発生
するおそれのある危険状態を越えた過冷却状態に移行す
ることができ、安定した製氷運転を連続して行うことが
できる。
According to this embodiment, the outlet temperature T2 of the cold storage material
At the beginning of ice making with a small degree of supercooling, the cold storage material (W) is cooled at the freezing point temperature T0 by the capacity reducing means (75), so that the inlet temperature T1 can be reduced while preventing the pipeline from being blocked. it can. For this reason, immediately after the return of the cooling capacity of the supercooling-generation heat exchanger (25), it is possible to shift to a supercooling state that exceeds a dangerous state in which a pipe blockage may occur, and to continuously perform a stable ice making operation. It can be carried out.

【0064】また、能力復帰手段(77)が所定時間経
過すれば過冷却生成熱交換器(25)の冷媒能力を復帰
させるので、簡単に管路の閉塞を防止しながら定常運転
に移行することができる。
Since the capacity return means (77) returns the refrigerant capacity of the supercooling / generation heat exchanger (25) after a lapse of a predetermined time, it is possible to easily shift to the steady operation while preventing the blockage of the pipeline. Can be.

【0065】次に、図2および図4は請求項1および3
に係る発明の第2実施例を示す。本実施例は、所定時間
の経過後一律に冷却能力を復帰する前実施例の能力復帰
手段(77)に代え、蓄冷材(W)の入口温度T1 が凝
固点温度T0 より高い所定の低温温度T3 に達すると、
過冷却生成熱交換器(25)の冷却能力を復帰させる能
力復帰手段(77)を設けている。
Next, FIG. 2 and FIG.
2 shows a second embodiment of the present invention. In this embodiment, instead of the capacity return means (77) of the previous embodiment which uniformly returns the cooling capacity after a predetermined time has elapsed, a predetermined low temperature T3 in which the inlet temperature T1 of the cold storage material (W) is higher than the freezing point temperature T0. Reaches
A capacity return means (77) for returning the cooling capacity of the supercooling generation heat exchanger (25) is provided.

【0066】具体的には、能力復帰手段(77)は、能
力低下手段(75)による過冷却生成熱交換器(25)
の能力低下後に、上記入口温度センサ(Th2)の温度信
号を受けて上記蓄冷材(W)の入口温度T1 が凝固点温
度T0 より高い所定の低温温度に達すると、上記過冷却
生成熱交換器(25)の冷却能力を復帰させる復帰信号
を上記能力制御手段(73)に出力するように構成され
ている。
Specifically, the capacity return means (77) is provided with a supercooling-generating heat exchanger (25) by the capacity reducing means (75).
When the inlet temperature T1 of the cold storage material (W) reaches a predetermined low temperature higher than the freezing point temperature T0 upon receiving a temperature signal from the inlet temperature sensor (Th2) after the capacity of the supercooling heat exchanger (Th2) is reduced. It is configured to output a return signal for returning the cooling capacity of 25) to the capacity control means (73).

【0067】本実施例では、図4に示すように、蓄冷材
(W)の入口温度T1 が凝固点温度T0 より高い所定の
低温温度T3 に達すると、能力復帰手段(77)が過冷
却生成熱交換器(25)の冷却能力を復帰させる。した
がって、該所定低温温度T3を、例えば、冷却能力復帰
後の冷却によって出口温度T2 が凍結発生下限温度Tf
より低下するような入口温度T1 に設定すれば、出口温
度T2 は凍結発生温度帯(K)を速やかに通過して、確
実に管路の閉塞が防止されと共に、過冷却生成熱交換器
(25)の能力復帰が行われる。
In this embodiment, as shown in FIG. 4, when the inlet temperature T1 of the cold storage material (W) reaches a predetermined low temperature T3 higher than the freezing point temperature T0, the capacity return means (77) causes the supercooling heat The cooling capacity of the exchanger (25) is restored. Accordingly, the predetermined low temperature T3 is reduced, for example, by the cooling after the cooling capacity is restored, the outlet temperature T2 becomes the freezing occurrence lower limit temperature Tf.
If the inlet temperature T1 is set to a lower temperature, the outlet temperature T2 quickly passes through the freezing occurrence temperature zone (K), thereby reliably preventing the clogging of the pipeline and the supercooling heat exchanger (25). ) Is performed.

【0068】本実施例によれば、蓄冷材(W)の入口温
度T1 が凝固点温度T0 より高い所定の低温温度T3 に
達すると、能力復帰手段(77)が過冷却生成熱交換器
(25)の冷却能力を復帰させるので、確実に管路の凍
結が防止されと共に、過冷却生成熱交換器(25)の能
力復帰を行うことができる。
According to the present embodiment, when the inlet temperature T1 of the cold storage material (W) reaches the predetermined low temperature T3 higher than the freezing point temperature T0, the capacity return means (77) operates the supercooling heat exchanger (25). Since the cooling capacity of the supercooling-generating heat exchanger (25) can be surely prevented, freezing of the pipeline can be prevented and the capacity of the supercooling-generation heat exchanger (25) can be restored.

【0069】次に、図2、図5および図6は請求項1お
よび4に係る発明の第3実施例を示す。本実施例では、
能力復帰手段(77)は、蓄冷材の入口温度T1 が所定
の低温温度に達すると過冷却生成熱交換器(25)の冷
却能力を復帰させる前実施例に代え、能力低下手段(7
5)による過冷却生成熱交換器(25)の能力低下後
に、入口温度センサ(Th2)の温度信号を受けて蓄冷材
(W)の入口温度T1 が能力低下手段(75)による低
能力運転開始時の出口温度T2 と凍結発生下限温度Tf
との間の温度差分だけ低能力運転開始時より低下する
と、過冷却生成熱交換器(25)の冷却能力を復帰させ
る復帰信号を能力制御手段(73)に出力するように構
成されている。
Next, FIGS. 2, 5 and 6 show a third embodiment of the present invention. In this embodiment,
The capacity return means (77) replaces the previous embodiment in which the cooling capacity of the supercooling generation heat exchanger (25) is returned when the inlet temperature T1 of the cold storage material reaches a predetermined low temperature, instead of the capacity reduction means (7).
After the capacity reduction of the supercooling-generation heat exchanger (25) due to 5), the temperature signal of the inlet temperature sensor (Th2) is received and the inlet temperature T1 of the cold storage material (W) is reduced to a low capacity operation by the capacity reducing means (75). Outlet temperature T2 and freezing occurrence lower limit temperature Tf
When the temperature is lower than the low-capacity operation start by the temperature difference between the sub-cooling generation heat exchanger (25) and the cooling power of the supercooling heat exchanger (25), a return signal is returned to the capacity control means (73).

【0070】本実施例の過冷却生成熱交換器(25)の
作動を図5の作動温度特性図と図6のフローチャート図
とに基づいて説明する。
The operation of the supercool generation heat exchanger (25) of this embodiment will be described with reference to the operating temperature characteristic diagram of FIG. 5 and the flowchart of FIG.

【0071】まず、ステップS1で蓄冷材(W)の出口
温度T2 が凝固点温度T0 より低いか否か判別し、蓄冷
材(W)の出口温度T2 が凝固点温度T0 以上の時には
判別を繰り返す。蓄冷材(W)の出口温度T2 が凝固点
温度T0 より低い時にはステップS2に移り、出口温度
T2 が凍結発生下限温度Tf より低いか否かを判別し、
出口温度T2 が凍結発生下限温度Tf より低い時には能
力制御手段(73)が過冷却生成熱交換器(25)に定
常能力の通常運転をさせる。
First, in step S1, it is determined whether or not the outlet temperature T2 of the cold storage material (W) is lower than the freezing point temperature T0. If the outlet temperature T2 of the cold storage material (W) is higher than the freezing point temperature T0, the determination is repeated. When the outlet temperature T2 of the cold storage material (W) is lower than the freezing point temperature T0, the process proceeds to step S2, and it is determined whether or not the outlet temperature T2 is lower than the freezing occurrence lower limit temperature Tf.
When the outlet temperature T2 is lower than the freezing occurrence lower limit temperature Tf, the capacity control means (73) causes the supercooling generation heat exchanger (25) to perform a normal operation of a steady capacity.

【0072】一方、出口温度T2 が凍結発生下限温度T
f 以上の時には、出口温度T2 が凍結発生温度帯(K)
に入ったと判別してステップS3に移り、低能力運転を
開始する時のために基準入口温度T1sを読み込む共に、
出口温度T2 と上記凍結発生下限温度Tf との間の温度
差△Tを算出する。
On the other hand, when the outlet temperature T2 is lower than the freezing occurrence lower limit temperature T
f or more, the outlet temperature T2 becomes the freezing occurrence temperature zone (K)
The process proceeds to step S3 when it is determined that the vehicle has entered the low-capacity operation, and the reference inlet temperature T1s is read in order to start the low-capacity operation.
A temperature difference ΔT between the outlet temperature T2 and the above-mentioned freezing occurrence lower limit temperature Tf is calculated.

【0073】次に、ステップS4に移り、入口温度T1
が、上記基準入口温度T1sより上記温度差△T分だけ低
下したか否かを判別する。入口温度T1 が温度差△T分
までは低下していない時には、出口温度T2 が凍結発生
温度帯(K)にあると判別してステップS5に移り、能
力低下手段(75)が過冷却生成熱交換器(25)に冷
却能力の低い低能力運転をさせる。該低能力運転中にス
テップS6に移り、所定時間毎に入口温度T1 を検出し
て、入口温度T1 が温度差△T分だけ低下するまでステ
ップS4〜S6の動作を繰り返す。
Next, the process proceeds to step S4, where the inlet temperature T1
Is lower than the reference inlet temperature T1s by the temperature difference ΔT. If the inlet temperature T1 has not dropped to the temperature difference ΔT, it is determined that the outlet temperature T2 is in the freezing occurrence temperature zone (K), and the process proceeds to step S5, where the capacity reduction means (75) sets the supercooling heat The exchanger (25) is operated at a low capacity with a low cooling capacity. During the low capacity operation, the process proceeds to step S6, where the inlet temperature T1 is detected at predetermined time intervals, and the operations of steps S4 to S6 are repeated until the inlet temperature T1 decreases by the temperature difference ΔT.

【0074】その後、入口温度T1 が基準入口温度T1s
より温度差△T分だけ低下すると、ステップS7に移
り、能力復帰手段(77)が作動して過冷却生成熱交換
器(25)の冷却能力を復帰させる復帰信号を上記能力
制御手段(73)に出力し、過冷却生成熱交換器(2
5)を数分間通常運転させる。この後、ステップS8に
移り、該数分間の通常運転によって出口温度T2 が凍結
発生下限温度Tf より低下したか否かを判別する。出口
温度T2 が凍結発生下限温度Tf より高い時には、出口
温度T2 が凍結発生温度帯(K)にあると判別してステ
ップS3〜ステップS8を繰り返す。出口温度T2 が凍
結発生下限温度Tf より低下した時には、十分過冷却度
は大きくなり、管路凍結発生のおそれのある危険状態は
脱したと判別して通常運転を行う。
Thereafter, the inlet temperature T1 is changed to the reference inlet temperature T1s.
When the temperature difference is further decreased by ΔT, the process proceeds to step S7, in which the capacity return means (77) operates to send a return signal for returning the cooling capacity of the supercooling generation heat exchanger (25) to the capacity control means (73). To the supercooled heat exchanger (2
5) Allow normal operation for several minutes. Thereafter, the process proceeds to step S8, where it is determined whether or not the outlet temperature T2 has dropped below the freezing occurrence lower limit temperature Tf by the normal operation for several minutes. When the outlet temperature T2 is higher than the freezing occurrence lower limit temperature Tf, it is determined that the outlet temperature T2 is in the freezing occurrence temperature zone (K), and Steps S3 to S8 are repeated. When the outlet temperature T2 falls below the freezing occurrence lower limit temperature Tf, the degree of supercooling becomes sufficiently large, and it is determined that the danger state in which the line freezing may occur has been eliminated, and normal operation is performed.

【0075】本実施例では、蓄冷材(W)の入口温度T
1 が低能力運転開始時の出口温度T2 と凍結発生下限温
度Tf との間の温度差分だけ低下すると、過冷却生成熱
交換器(25)の冷却能力を復帰させるので、必要な温
度低下分だけ冷却能力が低下し、必要以上に能力を低下
させた低能力運転が起こらない。
In this embodiment, the inlet temperature T of the cold storage material (W)
When 1 decreases by the temperature difference between the outlet temperature T2 at the start of the low capacity operation and the freezing occurrence lower limit temperature Tf, the cooling capacity of the supercooling heat exchanger (25) is restored. The cooling capacity is reduced, and low-capacity operation in which the capacity is reduced more than necessary does not occur.

【0076】本実施例によれば、蓄冷材(W)の入口温
度T1 が低能力運転開始時の出口温度T2 と凍結発生下
限温度Tf との間の温度差分だけ低下すると、過冷却生
成熱交換器(25)の冷却能力を復帰させるので、冷却
能力低下量が機種の違い等による流量差の影響を受ける
ことがなく、必要以上に能力を低下させた低能力運転の
実行を防止することができる。
According to this embodiment, when the inlet temperature T1 of the cold storage material (W) decreases by the temperature difference between the outlet temperature T2 at the start of the low-capacity operation and the freezing occurrence lower limit temperature Tf, the supercooling heat exchange occurs. Since the cooling capacity of the cooling unit (25) is restored, the cooling capacity reduction amount is not affected by the flow rate difference due to the difference in the model, and the execution of the low capacity operation in which the capacity is reduced more than necessary can be prevented. it can.

【0077】なお、上記実施例において、能力低下手段
(75)が維持しようとする所定温度は、凝固点温度T
0 だけに限らず、凝固点温度T0 近傍の温度であっても
よい。
In the above embodiment, the predetermined temperature which the capacity reducing means (75) is to maintain is the freezing point temperature T
The temperature is not limited to 0 and may be a temperature near the freezing point temperature T0.

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

【図1】請求項1〜4の構成を示すブロック図である。FIG. 1 is a block diagram showing a configuration according to claims 1 to 4;

【図2】本発明の第1実施例ないし第3実施例の空気調
和装置の配管系統の回路図である。
FIG. 2 is a circuit diagram of a piping system of the air conditioner according to the first to third embodiments of the present invention.

【図3】本発明の第1実施例の過冷却生成熱交換器の作
動温度を示す特性図である。
FIG. 3 is a characteristic diagram showing an operating temperature of the supercooling-generation heat exchanger according to the first embodiment of the present invention.

【図4】本発明の第2実施例の図3相当図である。FIG. 4 is a view corresponding to FIG. 3 of a second embodiment of the present invention.

【図5】本発明の第3実施例の図3相当図である。FIG. 5 is a view corresponding to FIG. 3 of a third embodiment of the present invention.

【図6】本発明の第3実施例の運転制御を示すフローチ
ャート図である。
FIG. 6 is a flowchart illustrating operation control according to a third embodiment of the present invention.

【符号の説明】[Explanation of symbols]

21 蓄氷槽 25 過冷却生成熱交換器(冷却手段) 73 能力制御手段 75 能力低下手段 77 能力復帰手段 W 蓄冷材 K 凍結発生温度帯 Th1 出口温度センサ(出口温度検出手段) Th2 入口温度センサ(入口温度検出手段) 21 ice storage tank 25 supercooling generation heat exchanger (cooling means) 73 capacity control means 75 capacity reduction means 77 capacity return means W cold storage material K freezing occurrence temperature zone Th1 outlet temperature sensor (outlet temperature detecting means) Th2 inlet temperature sensor ( Inlet temperature detection means)

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 平3−271671(JP,A) 特開 平3−102130(JP,A) (58)調査した分野(Int.Cl.6,DB名) F24F 5/00 102────────────────────────────────────────────────── ─── Continuation of the front page (56) References JP-A-3-271671 (JP, A) JP-A-3-102130 (JP, A) (58) Fields investigated (Int.Cl. 6 , DB name) F24F 5/00 102

Claims (4)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 スラリー状に氷化された蓄冷材(W)を
貯溜する蓄氷槽(21)と、蓄冷材(W)を過冷却する
冷却能力可変の冷却手段(25)とが順に蓄冷材(W)
の循環可能に接続され、過冷却された蓄冷材(W)の過
冷却状態を解消して生成した氷化物を上記蓄氷槽(2
1)に貯溜する製氷装置において、 上記冷却手段(25)を所定の冷却能力に制御する能力
制御手段(73)と、 上記冷却手段(25)における蓄冷材(W)の出口温度
T2 を検出する出口温度検出手段(Th1)と、 該出口温度検出手段(Th1)の温度信号を受け、上記蓄
冷材(W)の出口温度T2 が、蓄冷材(W)の凝固点温
度T0 に基づいて設定された所定の設定温度範囲(K)
に入ると、上記蓄冷材(W)の出口温度T2 を上昇させ
ることなく凝固点温度T0または凝固点温度T0 近傍の
所定値に維持するように、上記冷却手段(25)の冷却
能力を低下させる能力低下手段(75)と、 該能力低下手段(75)による冷却手段(25)の能力
低下後に、所定状態になると、蓄冷材(W)を急速冷却
して該蓄冷材(W)の出口温度T2 が上記凝固点温度T
0 または上記所定値から上記設定温度範囲(K)よりも
低い温度に速やかに移行するように上記冷却手段(2
5)の冷却能力を復帰させる復帰信号を上記能力制御手
段(73)に出力する能力復帰手段(77)とを備えた
ことを特徴とする製氷装置。
1. An ice storage tank (21) for storing a cold storage material (W) iced in a slurry state, and a cooling means (25) having a variable cooling capacity for supercooling the cold storage material (W). Wood (W)
The chilled material (W) which is connected in a circulable manner and which is formed by eliminating the supercooled state of the supercooled cold storage material (W) is stored in the ice storage tank (2).
In the ice making device stored in 1), a capacity control means (73) for controlling the cooling means (25) to a predetermined cooling capacity and an outlet temperature T2 of the cold storage material (W) in the cooling means (25) are detected. Upon receiving the temperature signals from the outlet temperature detecting means (Th1) and the outlet temperature detecting means (Th1), the outlet temperature T2 of the cold storage material (W) is set based on the freezing point temperature T0 of the cold storage material (W). Predetermined set temperature range (K)
, The outlet temperature T2 of the cold storage material (W) is increased.
Cooling means (75) for reducing the cooling capacity of the cooling means (25) so as to maintain the freezing point temperature T0 or a predetermined value near the freezing point temperature T0 without cooling; When a predetermined state is reached after the capacity reduction of (25), the cold storage material (W) is rapidly cooled.
Then, the outlet temperature T2 of the cold storage material (W) is set to the above freezing point temperature T.
0 or from the above-mentioned predetermined value to the above-mentioned set temperature range (K)
The cooling means (2) so as to quickly shift to a low temperature.
An ice making device comprising: a capacity return means (77) for outputting a return signal for returning the cooling capacity of 5) to the capacity control means (73).
【請求項2】 スラリー状に氷化された蓄冷材(W)を
貯溜する蓄氷槽(21)と、蓄冷材(W)を過冷却する
冷却能力可変の冷却手段(25)とが順に蓄冷材(W)
の循環可能に接続され、過冷却された蓄冷材(W)の過
冷却状態を解消して生成した氷化物を上記蓄氷槽(2
1)に貯溜する製氷装置において、 上記冷却手段(25)を所定の冷却能力に制御する能力
制御手段(73)と、 上記冷却手段(25)における蓄冷材(W)の出口温度
T2 を検出する出口温度検出手段(Th1)と、 該出口温度検出手段(Th1)の温度信号を受け、上記蓄
冷材(W)の出口温度T2 が、蓄冷材(W)の凝固点温
度T0 に基づいて設定された所定の設定温度範囲(K)
に入ると、上記蓄冷材(W)の出口温度T2 を上昇させ
ることなく凝固点温度T0または凝固点温度T0 近傍の
所定値に維持するように、上記冷却手段(25)の冷却
能力を低下させる能力低下手段(75)と、 該能力低下手段(75)による冷却手段(25)の能力
低下後に、所定時間が経過すると、蓄冷材(W)を急速
冷却して該蓄冷材(W)の出口温度T2 が上記凝固点温
度T0 または上記所定値から上記設定温度範囲(K)よ
りも低い温度に速やかに移行するように上記冷却手段
(25)の冷却能力を復帰させる復帰信号を上記能力制
御手段(73)に出力する能力復帰手段(77)とを備
えたことを特徴とする製氷装置。
2. An ice storage tank (21) for storing a cold storage material (W) iced into a slurry and a cooling means (25) having a variable cooling capacity for supercooling the cold storage material (W). Wood (W)
The chilled material (W) which is connected in a circulable manner and which is formed by eliminating the supercooled state of the supercooled cold storage material (W) is stored in the ice storage tank (2).
In the ice making device stored in 1), a capacity control means (73) for controlling the cooling means (25) to a predetermined cooling capacity and an outlet temperature T2 of the cold storage material (W) in the cooling means (25) are detected. Upon receiving the temperature signals from the outlet temperature detecting means (Th1) and the outlet temperature detecting means (Th1), the outlet temperature T2 of the cold storage material (W) is set based on the freezing point temperature T0 of the cold storage material (W). Predetermined set temperature range (K)
, The outlet temperature T2 of the cold storage material (W) is increased.
Cooling means (75) for reducing the cooling capacity of the cooling means (25) so as to maintain the freezing point temperature T0 or a predetermined value near the freezing point temperature T0 without cooling; After a predetermined time elapses after the capacity reduction of (25), the cold storage material (W) is rapidly discharged.
After cooling, the outlet temperature T2 of the cold storage material (W) is set to the above freezing point temperature.
Degree T0 or from the above-mentioned predetermined value to the above-mentioned set temperature range (K)
A capacity return means (77) for outputting to the capacity control means (73) a return signal for returning the cooling capacity of the cooling means (25) so as to quickly shift to a lower temperature. Ice making equipment.
【請求項3】 スラリー状に氷化された蓄冷材(W)を
貯溜する蓄氷槽(21)と、蓄冷材(W)を過冷却する
冷却能力可変の冷却手段(25)とが順に蓄冷材(W)
の循環可能に接続され、過冷却された蓄冷材(W)の過
冷却状態を解消して生成した氷化物を上記蓄氷槽(2
1)に貯溜する製氷装置において、 上記冷却手段(25)を所定の冷却能力に制御する能力
制御手段(73)と、 上記冷却手段(25)における蓄冷材(W)の出口温度
T2 を検出する出口温度検出手段(Th1)と、 上記冷却手段(25)における蓄冷材(W)の入口温度
T1 を検出する入口温度検出手段(Th2)と、 該出口温度検出手段(Th1)の温度信号を受け、上記蓄
冷材(W)の出口温度T2 が、蓄冷材(W)の凝固点温
度T0 に基づいて設定された所定の設定温度範囲(K)
に入ると、上記蓄冷材(W)の出口温度T2 を上昇させ
ることなく凝固点温度T0または凝固点温度T0 近傍の
所定値に維持するように上記冷却手段(25)の冷却能
力を低下させる能力低下手段(75)と、 該能力低下手段(75)による冷却手段(25)の能力
低下後に、上記入口温度検出手段(Th2)の温度信号を
受けて上記蓄冷材(W)の入口温度が凝固点温度T0 よ
り高い所定の低温温度T3 に達すると、蓄冷材(W)を
急速冷却して該蓄冷材(W)の出口温度T2 が上記凝固
点温度T0 または上記所定値から上記設定温度範囲
(K)よりも低い温度に速やかに移行するように上記冷
却手段(25)の冷却能力を復帰させる復帰信号を上記
能力制御手段(73)に出力する能力復帰手段(77)
とを備えたことを特徴とする製氷装置。
3. An ice storage tank (21) for storing a cold storage material (W) iced into a slurry and a cooling means (25) having a variable cooling capacity for supercooling the cold storage material (W) are sequentially stored in a cold storage. Wood (W)
The chilled material (W) which is connected in a circulable manner and which is formed by eliminating the supercooled state of the supercooled cold storage material (W) is stored in the ice storage tank (2).
In the ice making device stored in 1), a capacity control means (73) for controlling the cooling means (25) to a predetermined cooling capacity and an outlet temperature T2 of the cold storage material (W) in the cooling means (25) are detected. An outlet temperature detecting means (Th1), an inlet temperature detecting means (Th2) for detecting an inlet temperature T1 of the cold storage material (W) in the cooling means (25), and a temperature signal from the outlet temperature detecting means (Th1). The outlet temperature T2 of the cold storage material (W) is a predetermined temperature range (K) set based on the freezing point temperature T0 of the cold storage material (W).
, The outlet temperature T2 of the cold storage material (W) is increased.
A cooling means (75) for reducing the cooling capacity of the cooling means (25) so as to maintain the freezing point temperature T0 or a predetermined value near the freezing point temperature T0 without cooling; When the temperature of the cold storage material (W) reaches a predetermined low temperature T3 higher than the freezing point temperature T0 upon receiving a temperature signal from the inlet temperature detecting means (Th2) after the capacity reduction of 25), the cold storage material (W) To
After rapid cooling, the outlet temperature T2 of the cold storage material (W) is solidified as described above.
The set temperature range from the point temperature T0 or the specified value
A capacity return means (77) for outputting a return signal for returning the cooling capacity of the cooling means (25) to the capacity control means (73) so as to quickly shift to a temperature lower than (K ).
An ice making device comprising:
【請求項4】 スラリー状に氷化された蓄冷材(W)を
貯溜する蓄氷槽(21)と、蓄冷材(W)を過冷却する
冷却能力可変の冷却手段(25)とが順に蓄冷材(W)
の循環可能に接続され、過冷却された蓄冷材(W)の過
冷却状態を解消して生成した氷化物を上記蓄氷槽(2
1)に貯溜する製氷装置において、 上記冷却手段(25)を所定の冷却能力に制御する能力
制御手段(73)と、 上記冷却手段(25)における蓄冷材(W)の出口温度
T2 を検出する出口温度検出手段(Th1)と、 上記冷却手段(25)における蓄冷材(W)の入口温度
T1 を検出する入口温度検出手段(Th2)と、 該出口温度検出手段(Th1)の温度信号を受け、上記蓄
冷材(W)の出口温度T2 が、蓄冷材(W)の凝固点温
度T0 に基づいて設定された所定の設定温度範囲(K)
に入ると、上記蓄冷材(W)の出口温度T2 が凝固点温
度T0 または凝固点温度T0 近傍の所定値を維持するよ
うに上記冷却手段(25)の冷却能力を低下させる能力
低下手段(75)と、 該能力低下手段(75)による冷却手段(25)の能力
低下後に、上記入口温度検出手段(Th2)の温度信号を
受けて上記蓄冷材(W)の入口温度T1 が上記能力低下
手段(75)による低能力運転開始時の出口温度T2 と
上記凍結発生下限温度Tf との間の温度差△T分だけ低
能力運転開始時より低下すると、上記冷却手段(25)
の冷却能力を復帰させる復帰信号を上記能力制御手段
(73)に出力する能力復帰手段(77)とを備えたこ
とを特徴とする製氷装置。
4. An ice storage tank (21) for storing a cold storage material (W) iced into a slurry, and a cooling means (25) having a variable cooling capacity for supercooling the cold storage material (W). Wood (W)
The chilled material (W) which is connected in a circulable manner and which is formed by eliminating the supercooled state of the supercooled cold storage material (W) is stored in the ice storage tank (2).
In the ice making device stored in 1), a capacity control means (73) for controlling the cooling means (25) to a predetermined cooling capacity and an outlet temperature T2 of the cold storage material (W) in the cooling means (25) are detected. An outlet temperature detecting means (Th1), an inlet temperature detecting means (Th2) for detecting an inlet temperature T1 of the cold storage material (W) in the cooling means (25), and a temperature signal from the outlet temperature detecting means (Th1). The outlet temperature T2 of the cold storage material (W) is a predetermined temperature range (K) set based on the freezing point temperature T0 of the cold storage material (W).
, The outlet temperature T2 of the cold storage material (W) becomes the freezing point temperature.
A capacity reducing means (75) for reducing the cooling capacity of the cooling means (25) so as to maintain a predetermined value near the temperature T0 or the freezing point temperature T0; and a capacity of the cooling means (25) by the capacity reducing means (75). After the temperature is lowered, the temperature signal of the inlet temperature detecting means (Th2) is received, and the inlet temperature T1 of the cold storage material (W) is reduced by the outlet temperature T2 at the start of the low capacity operation by the capacity reducing means (75) and the freezing occurrence lower limit. When the temperature difference from the temperature Tf is lower than that at the start of the low capacity operation by the temperature difference ΔT, the cooling means (25)
An ice making device, comprising: a capacity return means (77) for outputting a return signal for returning the cooling capacity to the capacity control means (73).
JP4173995A 1992-07-01 1992-07-01 Ice making equipment Expired - Lifetime JP2795070B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4173995A JP2795070B2 (en) 1992-07-01 1992-07-01 Ice making equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4173995A JP2795070B2 (en) 1992-07-01 1992-07-01 Ice making equipment

Publications (2)

Publication Number Publication Date
JPH0618066A JPH0618066A (en) 1994-01-25
JP2795070B2 true JP2795070B2 (en) 1998-09-10

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ID=15970812

Family Applications (1)

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Country Link
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5019355B2 (en) * 2006-11-28 2012-09-05 学校法人玉川学園 Tube wall temperature control method for floating crystal manufacturing machine in heat storage system and cooling system using eutectic point of multicomponent mixed solution
JP2009168445A (en) * 2009-05-01 2009-07-30 Takasago Thermal Eng Co Ltd Ice thermal storage method
JP2015068620A (en) * 2013-09-30 2015-04-13 ダイキン工業株式会社 Air conditioner

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0617757B2 (en) * 1989-09-14 1994-03-09 清水建設株式会社 Freezing detection method for low temperature cold water production equipment
JPH07113498B2 (en) * 1990-03-20 1995-12-06 高砂熱学工業株式会社 Control method of heat pump device for supercooled water production

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