JPH0849937A - Regenerative air-conditioner - Google Patents

Regenerative air-conditioner

Info

Publication number
JPH0849937A
JPH0849937A JP18228094A JP18228094A JPH0849937A JP H0849937 A JPH0849937 A JP H0849937A JP 18228094 A JP18228094 A JP 18228094A JP 18228094 A JP18228094 A JP 18228094A JP H0849937 A JPH0849937 A JP H0849937A
Authority
JP
Japan
Prior art keywords
heat storage
refrigerant
storage tank
heat
heat exchange
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.)
Pending
Application number
JP18228094A
Other languages
Japanese (ja)
Inventor
Tetsuei Kuramoto
哲英 倉本
Shigeo Aoyama
繁男 青山
Kazuhiko Machida
和彦 町田
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Refrigeration Co
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 Matsushita Refrigeration Co filed Critical Matsushita Refrigeration Co
Priority to JP18228094A priority Critical patent/JPH0849937A/en
Publication of JPH0849937A publication Critical patent/JPH0849937A/en
Pending legal-status Critical Current

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  • Compression-Type Refrigeration Machines With Reversible Cycles (AREA)

Abstract

PURPOSE:To obtain an air-conditioner which takes out effectively the quantity of heat stored in a heat storage tank in a daytime cooling operation. CONSTITUTION:In a regenerative air-conditioner comprising a primary-side refrigerating cycle and a secondary-side refrigerating cycle, a first control device CNT1 which makes a second flow regulating valve RV2 fully open when the quantity of heat stored in a heat storage tank STR becomes a prescribed value or below in a daytime cooling operation and in a heat storage tank operation mode for a relatively small indoor load, and executes the operation in the heat storage tank operation mode until the temperature of water of the heat storage tank becomes a specific value or above, is provided. Even in the case when the quantity of heat stored in the heat storage tank STR decreases, it is possible to take out effectively the quantity of the heat stored and to prevent a shortage of a cooling capacity for the indoor load, according to this constitution.

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、空気を熱源とする空気
調和機において、夜間電力を利用するための蓄熱機能、
及びその制御機能を備えた蓄熱式空気調和機に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an air conditioner using air as a heat source, and has a heat storage function for utilizing nighttime electric power.
And a heat storage type air conditioner having a control function thereof.

【0002】[0002]

【従来の技術】蓄熱式空気調和機については、既にさま
ざまな開発がなされており、例えば、特開平1−186
507号公報に示されているような蓄熱式空気調和機が
ある。
2. Description of the Related Art A heat storage type air conditioner has already been variously developed, for example, Japanese Patent Laid-Open No. 1-186.
There is a heat storage type air conditioner as disclosed in Japanese Patent No. 507.

【0003】その基本的な技術について以下述べる。図
5に示すように、室外ユニットは、圧縮機2,四方弁
3,室外側熱交換器4,冷暖房用減圧装置5,第1補助
熱交換器14aを環状に順次接続して熱源側冷凍サイク
ルを形成し、一方、第1補助熱交換器14aと熱交換す
るように一体に形成されている第2補助熱交換器14
b,冷媒量調整タンク10,冷媒搬送ポンプPM,利用
側熱交換器15a,15bを環状に順次接続して利用側
冷凍サイクルを形成している。
The basic technique will be described below. As shown in FIG. 5, in the outdoor unit, the compressor 2, the four-way valve 3, the outdoor heat exchanger 4, the cooling and heating decompression device 5, and the first auxiliary heat exchanger 14a are sequentially connected in an annular shape to form a heat source side refrigeration cycle. The second auxiliary heat exchanger 14 that is integrally formed so as to exchange heat with the first auxiliary heat exchanger 14a.
b, the refrigerant adjustment tank 10, the refrigerant transfer pump PM, and the use side heat exchangers 15a and 15b are sequentially connected in an annular shape to form a use side refrigeration cycle.

【0004】更に、熱源側冷凍サイクルにおける第1補
助熱交換器14aに対して並列に設置した蓄熱用熱交換
器13aと、利用側冷凍サイクルにおける第2補助熱交
換器14bに対して並列に設置した放熱用熱交換器13
bと、蓄熱材である水16を有する蓄熱槽STRを設置
している。
Further, the heat storage heat exchanger 13a installed in parallel to the first auxiliary heat exchanger 14a in the heat source side refrigeration cycle and the second auxiliary heat exchanger 14b in the user side refrigeration cycle are installed in parallel. Heat exchanger 13 for heat radiation
b, and the heat storage tank STR which has the water 16 which is a heat storage material is installed.

【0005】そして、熱源側冷凍サイクルにおいて、第
1補助熱交換器14aと蓄熱用熱交換器13aとの回路
の切り替えは三方切替弁17a,17bにより行い、利
用側冷凍サイクルにおいて、第2補助熱交換器14bと
放熱用熱交換器13bとの回路の切り替えは三方流量弁
18a,18bにより行う。
In the heat source side refrigeration cycle, the three-way switching valves 17a and 17b are used to switch the circuit between the first auxiliary heat exchanger 14a and the heat storage heat exchanger 13a, and the second auxiliary heat exchanger is used in the user side refrigeration cycle. Switching of the circuit between the exchanger 14b and the heat radiation heat exchanger 13b is performed by the three-way flow valves 18a and 18b.

【0006】以上のように構成された蓄熱式空気調和機
について、その動作を説明する。まず、夜間運転は、熱
源側冷凍サイクルのみの運転であり、熱源側冷凍サイク
ルにおいて四方弁3によって製氷運転、及び蓄熱(温
水)運転に切り替えられ、製氷運転時は図中の実線矢印
の方向に冷媒が流れて冷房サイクルが形成され、室外側
熱交換器4を凝縮器、蓄熱槽内の蓄熱用熱交換器13a
を蒸発器として作用させて、蓄熱槽内の蓄熱用熱交換器
13aの周囲に氷として蓄冷される。
The operation of the heat storage type air conditioner configured as described above will be described. First, the night operation is an operation of only the heat source side refrigeration cycle, and in the heat source side refrigeration cycle, it is switched to the ice making operation and the heat storage (hot water) operation by the four-way valve 3, and during the ice making operation, in the direction of the solid line arrow in the figure. The refrigerant flows to form a cooling cycle, the outdoor heat exchanger 4 is a condenser, and the heat storage heat exchanger 13a in the heat storage tank is formed.
To act as an evaporator, and is stored as ice around the heat storage heat exchanger 13a in the heat storage tank.

【0007】また、蓄熱運転時には図中の破線方向に冷
媒が流れて暖房サイクルが形成され、室外側熱交換器4
を蒸発器、蓄熱槽内の蓄熱用熱交換器13aを凝縮器と
して作用させて、蓄熱槽内の蓄熱用熱交換器13aを介
して蓄熱槽STR内に温水として蓄熱される。この場
合、第1補助熱交換器14aは使用されない。
Further, during the heat storage operation, the refrigerant flows in the direction of the broken line in the figure to form a heating cycle, and the outdoor heat exchanger 4
Is operated as an evaporator and the heat storage heat exchanger 13a in the heat storage tank acts as a condenser, and heat is stored as hot water in the heat storage tank STR via the heat storage heat exchanger 13a in the heat storage tank. In this case, the first auxiliary heat exchanger 14a is not used.

【0008】この場合、熱源側冷凍サイクルと利用側冷
凍サイクルが分離されていて、両サイクル内の冷媒が混
合することがないため、適正冷媒封入量を維持でき、か
つ、熱源側冷凍サイクルの配管長が短くて済むため、圧
縮機2内の冷凍機油が流出しても戻り易く、圧縮機2の
信頼性を高めることができる。
In this case, since the heat source side refrigeration cycle and the use side refrigeration cycle are separated and the refrigerants in both cycles do not mix, an appropriate amount of refrigerant to be filled can be maintained and the piping of the heat source side refrigeration cycle can be maintained. Since the length is short, even if the refrigerating machine oil in the compressor 2 flows out, it is easy to return and the reliability of the compressor 2 can be improved.

【0009】一方、昼間運転は熱源側冷凍サイクル、及
び利用側冷凍サイクルの両方を運転させる。
On the other hand, during the daytime operation, both the heat source side refrigeration cycle and the use side refrigeration cycle are operated.

【0010】特に、利用側での熱負荷が1日のうちで比
較的大きい、いわゆるピーク負荷時の場合、三方切替弁
17a,17bの切り替えにより第1補助熱交換器14
aが熱源側冷凍サイクルに連通され、また、利用側冷凍
サイクルにおいては、三方流量弁18a,18bにより
第2補助熱交換器14b、及び放熱用熱交換器13bへ
流入する冷媒量が分配されている。
Particularly, when the heat load on the user side is relatively large during one day, that is, at the time of so-called peak load, the first auxiliary heat exchanger 14 is switched by switching the three-way switching valves 17a and 17b.
a is communicated with the heat source side refrigeration cycle, and in the use side refrigeration cycle, the three-way flow valves 18a and 18b distribute the amount of refrigerant flowing into the second auxiliary heat exchanger 14b and the heat radiation heat exchanger 13b. There is.

【0011】夜間に蓄熱槽STR内の蓄熱材に蓄えられ
冷熱、あるいは、温熱を蓄熱槽内の放熱用熱交換器13
bを介して、利用側冷凍サイクル内の冷媒と熱交換し、
かつ熱源側冷凍サイクルの運転により冷却、あるいは加
熱された冷媒が第2補助熱交換器14bを介して、利用
側冷凍サイクル内の冷媒と熱交換する。
At night, the heat exchanger 13 for radiating cold or hot heat stored in the heat storage material in the heat storage tank STR in the heat storage tank
heat is exchanged with the refrigerant in the use side refrigeration cycle via b,
Moreover, the refrigerant cooled or heated by the operation of the heat source side refrigeration cycle exchanges heat with the refrigerant in the utilization side refrigeration cycle via the second auxiliary heat exchanger 14b.

【0012】それら二つの熱交換器で熱交換された冷媒
を冷媒搬送ポンプPMにて各室内ユニット12の利用側
熱交換器15へ搬送して室内空気と熱交換することによ
り、各室内の冷房、あるいは、暖房を行なう。
The refrigerant heat-exchanged by the two heat exchangers is conveyed by the refrigerant conveyance pump PM to the use side heat exchanger 15 of each indoor unit 12 and exchanges heat with the indoor air, thereby cooling each room. Or, perform heating.

【0013】従って、この場合、熱源側冷凍サイクルに
おける冷房、あるいは暖房能力は、熱源側冷凍サイクル
の能力と、蓄熱槽STRの放熱用熱交換器13bでの放
熱能力とのほぼ和となり、冷房、あるいは暖房能力が増
大する。
Therefore, in this case, the cooling or heating capacity in the heat source side refrigerating cycle becomes almost the sum of the capacity of the heat source side refrigerating cycle and the heat radiating capacity in the heat radiating heat exchanger 13b of the heat storage tank STR, and Or the heating capacity increases.

【0014】以上のように、夜間の余剰電力エネルギー
を熱に変換して蓄熱しておき、昼間にその電力を利用す
ることにより、昼間の高負荷時刻における電力ピークを
抑え、電力利用の平準化が図れる。
As described above, the surplus power energy at night is converted to heat and stored, and the power is used during the daytime to suppress the power peak at the time of high load during the daytime, and to level the power usage. Can be achieved.

【0015】[0015]

【発明が解決しようとする課題】しかしながら、前述の
従来例では、室内の冷房負荷が比較的小さく、利用側
(2次側)冷凍サイクルの蓄熱槽STRのみを作用させ
る場合、蓄熱槽STR内の蓄熱量の減少に伴って水温が
上昇すると、蓄熱槽STRの放熱用熱交換器13bの管
内側冷媒と管外側の水との温度差が小さくなって蓄熱槽
STRにおける熱交換量が低下し、蓄熱槽出口の冷媒過
冷却度を保持できなくなってしまう。
However, in the above-mentioned conventional example, when the indoor cooling load is relatively small and only the heat storage tank STR of the utilization side (secondary side) refrigeration cycle is operated, the inside of the heat storage tank STR is When the water temperature rises along with the decrease in the heat storage amount, the temperature difference between the refrigerant inside the pipe and the water outside the pipe of the heat radiating heat exchanger 13b of the heat storage tank STR decreases, and the heat exchange amount in the heat storage tank STR decreases. The refrigerant supercooling degree at the outlet of the heat storage tank cannot be maintained.

【0016】更に、蓄熱槽出口の冷媒過冷却度を保持で
きなくなると、蓄熱槽STRの放熱用熱交換器13b管
内側の冷媒は完全な2相状態となるために、蓄熱槽ST
Rにおける圧力損失が増大し、蓄熱槽STRの放熱用熱
交換器13bを流れる冷媒循環量が減少してしまう。
Further, when the refrigerant supercooling degree at the outlet of the heat storage tank cannot be maintained, the refrigerant inside the heat-radiating heat exchanger 13b of the heat storage tank STR becomes a complete two-phase state.
The pressure loss in R increases, and the refrigerant circulation amount flowing through the heat radiation heat exchanger 13b of the heat storage tank STR decreases.

【0017】その結果、蓄熱槽STR内の蓄熱量を有効
に取り出せなくなり、冷房能力の不足を生じるという欠
点を有していた。
As a result, the heat storage amount in the heat storage tank STR cannot be effectively taken out, and the cooling capacity is insufficient.

【0018】また、室内負荷が比較的大きく、熱源側
(1次側)冷凍サイクルを運転し、利用側(2次側)冷
凍サイクルの蓄熱槽STRの放熱用熱交換器13b、及
び第2補助熱交換器14bの両方を作用させる場合も同
様に、蓄熱槽STR内の蓄熱量の減少に伴って水温が上
昇すると蓄熱槽出口の冷媒過冷却度を保持できなくな
り、蓄熱槽STRの放熱用熱交換器13bを流れる冷媒
循環量が減少してしまう。
Further, the indoor load is relatively large, the heat source side (primary side) refrigerating cycle is operated, and the heat radiating heat exchanger 13b of the heat storage tank STR of the user side (secondary side) refrigerating cycle and the second auxiliary. Similarly, when both heat exchangers 14b are operated, when the water temperature rises as the amount of heat stored in the heat storage tank STR decreases, the degree of refrigerant supercooling at the outlet of the heat storage tank cannot be maintained, and the heat for radiating heat from the heat storage tank STR cannot be maintained. The circulation amount of the refrigerant flowing through the exchanger 13b is reduced.

【0019】その結果、蓄熱槽STR内の蓄熱量を有効
に取り出せなくなり、冷房能力の不足を生じるという欠
点を有していた。
As a result, there is a drawback that the amount of heat stored in the heat storage tank STR cannot be effectively taken out and the cooling capacity becomes insufficient.

【0020】そこで本発明は、利用側(2次側)冷凍サ
イクルの各運転モード時において、夜間に蓄えた蓄熱槽
STR内の蓄熱量を有効に取り出すことにより、室内負
荷に対する冷房能力の不足を防止し得る蓄熱式空気調和
機を提供することを目的とするものである。
Therefore, according to the present invention, in each operation mode of the use side (secondary side) refrigeration cycle, by effectively taking out the amount of heat stored in the heat storage tank STR stored at night, the cooling capacity against the indoor load is insufficient. It is an object of the present invention to provide a heat storage type air conditioner that can be prevented.

【0021】[0021]

【課題を解決するための手段】この目的を達成するため
本発明の蓄熱式空気調和機は、圧縮機と、第1四方弁
と、室外側熱交換器とを直列に接続し、かつ第1膨張弁
と冷媒対冷媒熱交換器の1次側熱交換部を、第2膨張弁
と蓄熱槽の1次側熱交換部に対して並列に接続した1次
側冷凍サイクルと、冷媒搬送ポンプと第2四方弁と冷媒
タンクとからなるポンプユニットと、室内側熱交換器と
室内流量弁とからなる室内ユニットとを接続し、かつ第
1流量弁と冷媒対冷媒熱交換器の2次側熱交換部を、第
2流量弁と蓄熱槽の2次側熱交換部に対して並列に接続
した2次側冷凍サイクルとからなり前記蓄熱槽に水温検
出装置と水位検出装置を設置して、蓄熱槽の水温と水位
とから蓄熱槽の蓄熱量を算出する蓄熱量検出装置を備
え、冷房運転時の2次側冷凍サイクルにおいて、冷媒対
冷媒熱交換器の2次側熱交換部を冷媒が流れる冷媒対冷
媒熱交換器運転モードと、蓄熱槽の2次側熱交換部を冷
媒が流れる蓄熱槽運転モードと、冷媒対冷媒熱交換器の
2次側熱交換部と蓄熱槽の2次側熱交換部の両方を冷媒
が流れる同時運転モードの各運転モードを切替えるモー
ド制御装置を備え更に冷房運転時の冷媒対冷媒熱交換器
の2次側熱交換部出口、及び蓄熱槽の2次側熱交換部出
口の冷媒過冷却度を検出する過冷却度検出装置を備え、
蓄熱槽運転モードの場合で、かつ蓄熱槽の蓄熱量が所定
値以下となった場合に第2流量弁を全開として、蓄熱槽
水温が所定値以上となるまで蓄熱槽運転モードでの運転
を行う第1制御装置を備えたものである。
In order to achieve this object, a heat storage type air conditioner of the present invention has a compressor, a first four-way valve, and an outdoor heat exchanger connected in series, and a first heat exchanger. A primary-side refrigeration cycle in which the expansion valve and the primary-side heat exchange section of the refrigerant-refrigerant heat exchanger are connected in parallel to the second expansion valve and the primary-side heat exchange section of the heat storage tank; A pump unit including a second four-way valve and a refrigerant tank is connected to an indoor unit including an indoor heat exchanger and an indoor flow valve, and the first flow valve and the secondary heat of the refrigerant-refrigerant heat exchanger are connected to each other. The heat exchange unit comprises a second flow valve and a secondary side refrigeration cycle connected in parallel to the secondary side heat exchange unit of the heat storage tank. A water temperature detection device and a water level detection device are installed in the heat storage tank to store heat. It is equipped with a heat storage amount detector that calculates the heat storage amount of the heat storage tank from the water temperature and water level of the tank In the refrigeration cycle, a refrigerant-to-refrigerant heat exchanger operation mode in which the refrigerant flows through the secondary side heat exchange section of the refrigerant-to-refrigerant heat exchanger, and a heat storage tank operation mode in which the refrigerant flows through the secondary side heat exchange section of the heat storage tank, Refrigerant-to-refrigerant Refrigerant pair at the time of cooling operation is provided with a mode controller that switches each operation mode of simultaneous operation modes in which the refrigerant flows through both the secondary-side heat exchange section and the secondary-side heat exchange section of the heat storage tank The secondary heat exchange section outlet of the refrigerant heat exchanger and the subcooling degree detection device for detecting the refrigerant supercooling degree of the secondary heat exchange section outlet of the heat storage tank are provided.
In the case of the heat storage tank operation mode, and when the heat storage amount of the heat storage tank is less than or equal to a predetermined value, the second flow valve is fully opened, and operation in the heat storage tank operation mode is performed until the water temperature of the heat storage tank reaches or exceeds the predetermined value. It is provided with a first control device.

【0022】また、同時運転モードの場合で、かつ蓄熱
槽の蓄熱量が所定値以下となった場合に第2流量弁を全
開とし、更にその後の運転において蓄熱槽の2次側熱交
換部出口の冷媒過冷却度を保持できなくなった場合に、
第1流量弁を所定開度以下として、蓄熱槽水温が所定値
以上となるまで同時運転モードでの運転を行う第2制御
装置を備えたものである。
In the simultaneous operation mode and when the amount of heat stored in the heat storage tank falls below a predetermined value, the second flow valve is fully opened, and in the subsequent operation, the outlet of the secondary side heat exchange section of the heat storage tank. When it becomes impossible to maintain the degree of refrigerant subcooling of
A second control device is provided, in which the first flow valve is set to a predetermined opening degree or less and the operation in the simultaneous operation mode is performed until the heat storage tank water temperature becomes a predetermined value or more.

【0023】[0023]

【作用】上記のような構成による本発明の蓄熱式空気調
和機の作用を以下に示す。
The operation of the heat storage type air conditioner of the present invention having the above construction will be described below.

【0024】ここで夜間蓄熱運転(製氷運転)について
は従来と同様の作用であるので説明を割愛し、昼間冷房
運転について以下説明していく。
The nighttime heat storage operation (ice making operation) has the same operation as the conventional one, and therefore its explanation is omitted, and the daytime cooling operation will be described below.

【0025】まず、昼間冷房運転において室内負荷が比
較的小さい場合には、モード制御装置により蓄熱槽運転
モードでの運転を行う。
First, in the daytime cooling operation, when the indoor load is relatively small, the mode control device operates in the heat storage tank operation mode.

【0026】この時、1次側冷凍サイクルは圧縮機を運
転しないために作用しない。また、2次側冷凍サイクル
において、冷媒は蓄熱槽の2次側熱交換部を介して蓄熱
槽内の蓄熱材と熱交換し、自身は冷却されて液冷媒とな
った後に冷媒搬送ポンプにより室内ユニットに送られて
室内を冷房する。
At this time, the primary side refrigeration cycle does not operate because the compressor is not operated. Also, in the secondary side refrigeration cycle, the refrigerant exchanges heat with the heat storage material in the heat storage tank via the secondary heat exchange section of the heat storage tank, and after cooling itself to become a liquid refrigerant, the refrigerant is transferred to the room by the refrigerant transfer pump. It is sent to the unit to cool the room.

【0027】そして、室内負荷が更に増大した場合に
は、モード制御装置により同時運転モードでの運転を行
う。
When the indoor load further increases, the mode control device operates in the simultaneous operation mode.

【0028】この時、1次側冷凍サイクルの圧縮機を運
転することにより、冷媒対冷媒熱交換器の1次側熱交換
部を介して2次側冷凍サイクルの冷媒を冷却する。
At this time, by operating the compressor of the primary side refrigeration cycle, the refrigerant of the secondary side refrigeration cycle is cooled via the primary side heat exchange section of the refrigerant-refrigerant heat exchanger.

【0029】また、2次側冷凍サイクルにおいて、冷媒
は蓄熱槽の2次側熱交換部、及び冷媒対冷媒熱交換器の
2次側熱交換部を介して冷却され、自身は液冷媒となっ
た後に冷媒搬送ポンプにより室内ユニットに送られて室
内を冷房する。
Further, in the secondary side refrigeration cycle, the refrigerant is cooled through the secondary side heat exchange section of the heat storage tank and the secondary side heat exchange section of the refrigerant-refrigerant heat exchanger, and becomes itself a liquid refrigerant. After that, it is sent to the indoor unit by the refrigerant transfer pump to cool the room.

【0030】尚、この時の2次側冷凍サイクルにおける
冷媒対冷媒熱交換器の2次側熱交換部、及び蓄熱槽の2
次側熱交換部への冷媒循環量は、第1流量弁、及び第2
流量弁によりそれぞれ所定の冷媒過冷却度となるように
制御されている。
At this time, in the secondary side refrigeration cycle, the secondary side heat exchange section of the refrigerant-refrigerant heat exchanger and the heat storage tank 2 are provided.
The amount of refrigerant circulated to the secondary heat exchange unit is the first flow valve and the second flow valve.
The flow rate valves are controlled so that the refrigerant has a predetermined degree of supercooling.

【0031】このように運転することにより、夜間の蓄
熱を利用し、かつ室内負荷に対応した冷房運転が可能と
なる。
By operating in this manner, it becomes possible to utilize the heat storage at night and perform the cooling operation corresponding to the indoor load.

【0032】更に、室内負荷が比較的小さい蓄熱槽運転
モードの場合には、第1制御装置により、蓄熱槽の蓄熱
量が所定値以下となった場合に第2流量弁を全開とし
て、蓄熱槽水温が所定値以上となるまで蓄熱槽運転モー
ドでの運転を行う。
Further, in the heat storage tank operation mode in which the indoor load is relatively small, the second flow valve is fully opened by the first control device when the heat storage amount of the heat storage tank becomes equal to or less than the predetermined value, and the heat storage tank is opened. The operation in the heat storage tank operation mode is performed until the water temperature reaches or exceeds the predetermined value.

【0033】このことにより蓄熱槽の2次側熱交換部の
冷媒循環量が増大し、それに伴って蓄熱槽の2次側熱交
換部管内側の熱伝達率が向上するために、蓄熱槽の2次
側熱交換部における管内側冷媒と、蓄熱材である水との
熱交換量を増大させることができる。
As a result, the amount of refrigerant circulating in the secondary side heat exchange section of the heat storage tank increases, and the heat transfer coefficient inside the secondary side heat exchange section tube of the heat storage tank improves accordingly. It is possible to increase the amount of heat exchange between the refrigerant inside the tube and the water as the heat storage material in the secondary side heat exchange section.

【0034】よって、室内負荷に対する冷房能力の不足
を防止することができる。また、室内負荷が比較的大き
い同時運転モードの場合には、第2制御装置により、蓄
熱槽の蓄熱量が所定値以下となった場合に第2流量弁を
全開とし、更にその後の運転において蓄熱槽の2次側熱
交換部出口の冷媒過冷却度を保持できなくなった場合
に、第1流量弁を所定開度以下として蓄熱槽に強制的に
冷媒を循環させ、蓄熱槽水温が所定値以上となるまで同
時運転モードでの運転を行う。
Therefore, it is possible to prevent a shortage of the cooling capacity with respect to the indoor load. Further, in the simultaneous operation mode in which the indoor load is relatively large, the second control device causes the second flow valve to be fully opened when the heat storage amount in the heat storage tank becomes equal to or less than a predetermined value, and the heat storage is performed in the subsequent operation. When the refrigerant supercooling degree at the outlet of the secondary side heat exchange section of the tank cannot be maintained, the first flow valve is set to a predetermined opening or less to forcibly circulate the refrigerant in the heat storage tank so that the water temperature of the heat storage tank is a predetermined value or more. The operation is performed in the simultaneous operation mode until it becomes.

【0035】このことにより、蓄熱槽内の蓄熱量が減少
した場合においても、それを有効に取り出すことがで
き、室内負荷に対する冷房能力の不足を防止することが
できる。
As a result, even when the amount of heat stored in the heat storage tank is reduced, it can be effectively taken out, and it is possible to prevent insufficient cooling capacity with respect to the indoor load.

【0036】以上のように、昼間冷房時の室内負荷が比
較的小さい蓄熱槽運転モードにおいて、蓄熱量が減少し
て蓄熱槽での熱交換量が低下した場合には、第1制御装
置により蓄熱槽運転モードにて蓄熱槽内の蓄熱量を有効
に取り出すと共に、室内負荷が比較的大きい同時運転モ
ードにおいて、蓄熱量が減少して蓄熱槽での熱交換量が
低下した場合には、第2制御装置により同時運転モード
にて蓄熱槽内の蓄熱量を有効に取り出すことにより、室
内負荷に対する冷房能力の不足を防止し得る蓄熱式空気
調和機を提供することができる。
As described above, in the heat storage tank operation mode in which the indoor load during daytime cooling is relatively small, when the heat storage amount decreases and the heat exchange amount in the heat storage tank decreases, the first control device stores the heat. In the tank operation mode, the heat storage amount in the heat storage tank is effectively taken out, and in the simultaneous operation mode in which the indoor load is relatively large, when the heat storage amount decreases and the heat exchange amount in the heat storage tank decreases, By effectively extracting the amount of heat stored in the heat storage tank by the control device in the simultaneous operation mode, it is possible to provide a heat storage type air conditioner capable of preventing insufficient cooling capacity with respect to the indoor load.

【0037】[0037]

【実施例】以下、本発明による蓄熱式空気調和機の第1
の実施例について、図面を参照しながら説明する。な
お、従来と同一構成については、同一符号を付して詳細
な説明を省略する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS First embodiment of a heat storage type air conditioner according to the present invention
Embodiments will be described with reference to the drawings. It should be noted that the same configurations as those of the conventional one are denoted by the same reference numerals and detailed description thereof will be omitted.

【0038】図1は本発明の第1の実施例の蓄熱式空気
調和機の冷凍サイクル図である。図1において、本発明
による第1の実施例の蓄熱式空気調和機は、室外ユニッ
ト1と、蓄熱槽STRと、室内ユニット12と、ポンプ
ユニットPUとからなる。
FIG. 1 is a refrigeration cycle diagram of the heat storage type air conditioner of the first embodiment of the present invention. In FIG. 1, the heat storage type air conditioner of the first embodiment according to the present invention comprises an outdoor unit 1, a heat storage tank STR, an indoor unit 12, and a pump unit PU.

【0039】室外ユニット1は、圧縮機2、第1四方弁
3a、室外側熱交換器4、第1膨張弁EXP1、第2膨
張弁EXP2、1次側熱交換部14aと2次側熱交換部
14bとからなる冷媒対冷媒熱交換器HEX、第1流量
弁RV1、第2流量弁RV2とから構成されている。
The outdoor unit 1 includes a compressor 2, a first four-way valve 3a, an outdoor heat exchanger 4, a first expansion valve EXP1, a second expansion valve EXP2, a primary side heat exchange section 14a and a secondary side heat exchange. The refrigerant-to-refrigerant heat exchanger HEX including the portion 14b, the first flow valve RV1, and the second flow valve RV2.

【0040】蓄熱槽STRは、蓄熱材である水16、蓄
熱槽の1次側熱交換部13a、蓄熱槽の2次側熱交換部
13b、水温検出装置18、水位検出装置19、蓄熱量
検出装置CALとから構成されている。
The heat storage tank STR includes water 16 as a heat storage material, a primary side heat exchange section 13a of the heat storage tank, a secondary side heat exchange section 13b of the heat storage tank, a water temperature detection device 18, a water level detection device 19, and a heat storage amount detection. And the device CAL.

【0041】また、複数の室内ユニット12a,12b
は、室内流量弁RVa,RVb、及び室内側熱交換器1
5a,15bとから構成されており、ポンプユニットP
Uは、冷媒タンク10、冷媒搬送ポンプPM、第2四方
弁3bとから構成されている。
Also, a plurality of indoor units 12a, 12b
Is the indoor flow valves RVa and RVb, and the indoor heat exchanger 1
5a, 15b, and a pump unit P
U is composed of a refrigerant tank 10, a refrigerant transfer pump PM, and a second four-way valve 3b.

【0042】室外ユニット1において、圧縮機2と、第
1四方弁3aと、室外側熱交換器4と、第1膨張弁EX
P1と、冷媒対冷媒熱交換器の1次側熱交換部14aと
を直列に接続し、さらに第2膨張弁EXP2と蓄熱槽の
1次側熱交換部13aを、第1膨張弁EXP1と冷媒対
冷媒熱交換器の1次側熱交換部14aに対して並列に接
続して1次側冷凍サイクルを形成している。
In the outdoor unit 1, the compressor 2, the first four-way valve 3a, the outdoor heat exchanger 4, and the first expansion valve EX.
P1 and the primary-side heat exchange section 14a of the refrigerant-refrigerant heat exchanger are connected in series, and the second expansion valve EXP2 and the primary-side heat exchange section 13a of the heat storage tank are connected to the first expansion valve EXP1 and the refrigerant. A primary side refrigeration cycle is formed by connecting in parallel to the primary side heat exchange section 14a of the heat exchanger for refrigerant.

【0043】また、ポンプユニットPUと、各室内ユニ
ット12a,12bと、冷媒対冷媒熱交換器の2次側熱
交換部14bと第1流量弁RV1とを直列に接続し、さ
らに蓄熱槽の2次側熱交換部13bと第2流量弁RV2
を、冷媒対冷媒熱交換器の2次側熱交換部14bと第1
流量弁RV1に対して並列に接続して2次側冷凍サイク
ルを形成している。
Further, the pump unit PU, the indoor units 12a and 12b, the secondary side heat exchange section 14b of the refrigerant-refrigerant heat exchanger and the first flow valve RV1 are connected in series, and further the heat storage tank 2 is connected. Secondary heat exchange section 13b and second flow valve RV2
To the secondary side heat exchange section 14b of the refrigerant-to-refrigerant heat exchanger and the first
The flow rate valve RV1 is connected in parallel to form a secondary side refrigeration cycle.

【0044】尚、第1四方弁3aのモ−ドについては、
圧縮機2吐出側と室外側熱交換器4とを、かつ圧縮機2
吸入側と蓄熱槽STRとを連通する場合を冷房モ−ド、
圧縮機2吐出側と蓄熱槽STRとを、かつ圧縮機2吸入
側と室外側熱交換器4とを連通する場合を暖房モ−ドと
定義する。
Regarding the mode of the first four-way valve 3a,
The discharge side of the compressor 2 and the outdoor heat exchanger 4, and the compressor 2
When connecting the suction side and the heat storage tank STR, the cooling mode is
A case where the discharge side of the compressor 2 and the heat storage tank STR and the suction side of the compressor 2 and the outdoor heat exchanger 4 are connected to each other are defined as a heating mode.

【0045】また、第2四方弁3bのモ−ドについて
は、冷媒搬送ポンプPM吐出側と室内ユニット12a,
12bとを、かつ冷媒搬送ポンプPM吸入側と室外ユニ
ット1、及び蓄熱槽STRとを連通する場合を冷房モ−
ド、冷媒搬送ポンプPM吐出側と室外ユニット1、及び
蓄熱槽STRとを、かつ冷媒搬送ポンプPM吸入側と室
内ユニット12a,12bとを連通する場合を暖房モ−
ドと定義する。
Regarding the mode of the second four-way valve 3b, the refrigerant transfer pump PM discharge side and the indoor unit 12a,
12b and the refrigerant transfer pump PM suction side communicates with the outdoor unit 1 and the heat storage tank STR.
In the case where the refrigerant transfer pump PM discharge side is connected to the outdoor unit 1 and the heat storage tank STR, and the refrigerant transfer pump PM suction side is connected to the indoor units 12a and 12b, the heating mode is set.
Defined as

【0046】また、第1膨張弁EXP1、及び第2膨張
弁EXP2については、第1膨張弁EXP1を全閉とし
て第2膨張弁EXP2を所定の開度とする場合を夜間モ
ード、第2膨張弁EXP2を全閉として第1膨張弁EX
P1を所定の開度とする場合を昼間モードと定義する。
Regarding the first expansion valve EXP1 and the second expansion valve EXP2, the night mode is used when the first expansion valve EXP1 is fully closed and the second expansion valve EXP2 is set to a predetermined opening, and the second expansion valve EXP2 is opened. First expansion valve EX with EXP2 fully closed
The case where P1 is set to a predetermined opening is defined as the daytime mode.

【0047】更に、昼間冷房運転時の2次側冷凍サイク
ルの運転モードについては、冷媒対冷媒熱交換器の2次
側熱交換部14bを冷媒が流れるモードを冷媒対冷媒熱
交換器運転モード、蓄熱槽の2次側熱交換部13bを冷
媒が流れるモードを蓄熱槽運転モード、冷媒対冷媒熱交
換器の2次側熱交換部14bと蓄熱槽の2次側熱交換部
13bの両方を冷媒が流れるモードを同時運転モードと
定義する。
Further, regarding the operation mode of the secondary side refrigeration cycle during the daytime cooling operation, the mode in which the refrigerant flows through the secondary side heat exchange section 14b of the refrigerant to refrigerant heat exchanger is the refrigerant to refrigerant heat exchanger operation mode, The mode in which the refrigerant flows through the secondary side heat exchange section 13b of the heat storage tank is the heat storage tank operation mode, and both the secondary side heat exchange section 14b of the refrigerant-refrigerant heat exchanger and the secondary side heat exchange section 13b of the heat storage tank are the refrigerant. The mode in which the current flows is defined as the simultaneous operation mode.

【0048】前記2次側冷凍サイクルの各運転モード
は、モード制御装置MODEにより切替えられる。
Each operation mode of the secondary side refrigeration cycle is switched by the mode controller MODE.

【0049】ここで、SUBは冷房モード時の冷媒対冷
媒熱交換器の2次側熱交換部14b出口の冷媒過冷却度
SC1、及び蓄熱槽の2次側熱交換部13b出口の冷媒
過冷却度SC2を検知する過冷却度検出装置である。
Here, SUB is the degree of refrigerant supercooling SC1 at the outlet of the secondary side heat exchange section 14b of the refrigerant-refrigerant heat exchanger in the cooling mode, and the refrigerant supercooling at the outlet of the secondary side heat exchange section 13b of the heat storage tank. This is a supercooling degree detection device that detects the degree SC2.

【0050】図2は本発明の第1の実施例の蓄熱式空気
調和機の動作を示すフローチャートである。
FIG. 2 is a flow chart showing the operation of the heat storage type air conditioner of the first embodiment of the present invention.

【0051】以上のように構成された蓄熱式空気調和機
について、以下その動作を図1、図2に基づいて説明す
る。
The operation of the heat storage type air conditioner configured as described above will be described below with reference to FIGS. 1 and 2.

【0052】但し、本発明は昼間の冷房運転に関するも
のであるため、夜間蓄熱運転(製氷運転)、及び暖房運
転についての説明は省略する。
However, since the present invention relates to the cooling operation in the daytime, the description of the night heat storage operation (ice making operation) and the heating operation will be omitted.

【0053】また、本発明は昼間の冷房運転における蓄
熱槽運転モード、及び同時運転モードに関するものであ
るため、他の運転モード(冷媒対冷媒熱交換器運転モー
ド)についての説明は省略する。
Since the present invention relates to the heat storage tank operation mode and the simultaneous operation mode in the daytime cooling operation, the description of the other operation modes (refrigerant-refrigerant heat exchanger operation mode) will be omitted.

【0054】昼間冷房運転(蓄熱槽運転モード);室内
負荷が比較的小さい場合には、STEP1、及びSTE
P2においてモード制御装置MODEにより蓄熱槽運転
モードに切替えられる。
Daytime cooling operation (heat storage tank operation mode); if the indoor load is relatively small, STEP 1 and STE
In P2, the mode controller MODE switches to the heat storage tank operation mode.

【0055】STEP3にて冷媒搬送ポンプPMが運転
を開始すると共に、STEP4にて蓄熱槽の2次側熱交
換部13b出口の冷媒過冷却度SC2の制御目標範囲B
(下限値Bmin、上限値Bmax)を設定し、STEP5に
移行する。
In STEP3, the refrigerant transfer pump PM starts to operate, and in STEP4, the control target range B of the refrigerant supercooling degree SC2 at the outlet of the secondary side heat exchange section 13b of the heat storage tank.
(Lower limit value Bmin, upper limit value Bmax) is set, and the process proceeds to STEP5.

【0056】STEP5において蓄熱槽の2次側熱交換
部13b出口の冷媒過冷却度SC2が制御目標範囲Bの
下限値Bminよりも小さい場合には、蓄熱槽STRの冷
媒循環量を減少させて蓄熱槽の2次側熱交換部13b出
口の冷媒過冷却度SC2を増大させるべく、STEP6
に移行して第2流量弁RV2を所定開度だけ閉じる。
In STEP 5, when the refrigerant supercooling degree SC2 at the outlet of the secondary side heat exchange section 13b of the heat storage tank is smaller than the lower limit value Bmin of the control target range B, the refrigerant circulation amount in the heat storage tank STR is reduced. In order to increase the degree of refrigerant supercooling SC2 at the outlet of the secondary side heat exchange section 13b of the tank, STEP6
And the second flow valve RV2 is closed by a predetermined opening degree.

【0057】逆に、蓄熱槽の2次側熱交換部13b出口
の冷媒過冷却度SC2が制御目標範囲Bの下限値Bmin
以上の場合にはSTEP7に進み、更に蓄熱槽の2次側
熱交換部13b出口の冷媒過冷却度SC2が制御目標範
囲Bの上限値Bmaxよりも大きい場合には、蓄熱槽ST
Rの冷媒循環量を増大させて蓄熱槽の2次側熱交換部1
3b出口の冷媒過冷却度SC2を減少させるべく、ST
EP8に移行して第2流量弁RV2を所定開度だけ開
く。
On the contrary, the refrigerant supercooling degree SC2 at the outlet of the secondary heat exchange section 13b of the heat storage tank is the lower limit value Bmin of the control target range B.
In the above case, the process proceeds to STEP 7, and when the refrigerant supercooling degree SC2 at the outlet of the secondary side heat exchange section 13b of the heat storage tank is larger than the upper limit value Bmax of the control target range B, the heat storage tank ST
The secondary side heat exchange section 1 of the heat storage tank is increased by increasing the refrigerant circulation amount of R.
In order to reduce the refrigerant supercooling degree SC2 at the 3b outlet, ST
The process moves to EP8, and the second flow valve RV2 is opened by a predetermined opening degree.

【0058】尚、蓄熱槽の2次側熱交換部13b出口の
冷媒過冷却度SC2が制御目標範囲Bに収まっている場
合には、第2流量弁RV2は動作しない。
When the refrigerant supercooling degree SC2 at the outlet of the secondary side heat exchange section 13b of the heat storage tank is within the control target range B, the second flow valve RV2 does not operate.

【0059】しかし、このように運転を続け、蓄熱槽S
TR内の蓄熱量の減少に伴って水温が上昇すると、蓄熱
槽の2次側熱交換部13bの管内側冷媒と管外側の水と
の温度差が小さくなって蓄熱槽STRにおける熱交換量
が低下し、蓄熱槽の2次側熱交換部13b出口の冷媒過
冷却度を保持できなくなってしまう。
However, the operation is continued in this way, and the heat storage tank S
When the water temperature rises as the amount of heat stored in TR decreases, the temperature difference between the refrigerant inside the pipe and the water outside the pipe of the secondary side heat exchange section 13b of the heat storage tank decreases, and the amount of heat exchange in the heat storage tank STR As a result, the refrigerant supercooling degree at the outlet of the secondary side heat exchange portion 13b of the heat storage tank cannot be maintained.

【0060】更に、蓄熱槽の2次側熱交換部13b出口
の冷媒過冷却度を保持できなくなると、蓄熱槽の2次側
熱交換部13b管内側の冷媒は完全な2相状態となるた
めに蓄熱槽STRにおける圧力損失が増大し、蓄熱槽の
2次側熱交換部13bを流れる冷媒循環量が減少してし
まう。
Further, if the degree of refrigerant supercooling at the outlet of the secondary side heat exchange section 13b of the heat storage tank cannot be maintained, the refrigerant inside the tube of the secondary side heat exchange section 13b of the heat storage tank becomes a complete two-phase state. In addition, the pressure loss in the heat storage tank STR increases, and the amount of refrigerant circulation flowing through the secondary heat exchange section 13b of the heat storage tank decreases.

【0061】その結果、蓄熱槽STR内の蓄熱量を有効
に取り出せなくなり、冷房能力の不足を生じてしまう。
As a result, the amount of heat stored in the heat storage tank STR cannot be effectively taken out, resulting in insufficient cooling capacity.

【0062】そこでSTEP9において、蓄熱量検出装
置CALにより蓄熱槽STR内の蓄熱量が所定値以下と
なったことを検知した場合にSTEP10に移行し、蓄
熱槽STR内の蓄熱量を使いきるべく第2流量弁RV2
の開度を全開として運転を行う。
Therefore, in STEP 9, when it is detected by the heat storage amount detecting device CAL that the heat storage amount in the heat storage tank STR is equal to or less than the predetermined value, the process proceeds to STEP 10 and the heat storage amount in the heat storage tank STR should be used up. 2 flow valve RV2
The operation is performed with the opening degree of fully opened.

【0063】このことにより蓄熱槽の2次側熱交換部1
3bの冷媒循環量が増大し、それに伴って蓄熱槽の2次
側熱交換部13b管内側の熱伝達率が向上するために、
蓄熱槽の2次側熱交換部13bにおける管内側冷媒と、
蓄熱材である水16との熱交換量を増大させることがで
きる。
As a result, the secondary side heat exchange section 1 of the heat storage tank 1
Since the refrigerant circulation amount of 3b increases and the heat transfer coefficient inside the secondary side heat exchange section 13b of the heat storage tank increases accordingly,
A pipe inside refrigerant in the secondary side heat exchange section 13b of the heat storage tank;
The amount of heat exchange with the water 16, which is the heat storage material, can be increased.

【0064】そして、STEP11において、蓄熱槽S
TR内の水温が所定値以上となるまで蓄熱槽運転モード
での運転を行う。
Then, in STEP 11, the heat storage tank S
The operation in the heat storage tank operation mode is performed until the water temperature in TR becomes equal to or higher than a predetermined value.

【0065】よって、蓄熱槽STR内の蓄熱量が減少し
た場合においても、それをを有効に取り出すことがで
き、室内負荷に対する冷房能力の不足を防止することが
できる。
Therefore, even when the amount of heat stored in the heat storage tank STR is reduced, it can be effectively taken out, and a shortage of the cooling capacity against the indoor load can be prevented.

【0066】次に、本発明による蓄熱式空気調和機の第
2の実施例について、図面を参照しながら説明する。
Next, a second embodiment of the heat storage type air conditioner according to the present invention will be described with reference to the drawings.

【0067】図3は本発明の第2の実施例の蓄熱式空気
調和機の冷凍サイクル図、図4は同実施例の蓄熱式空気
調和機の動作を示すフローチャートである。
FIG. 3 is a refrigeration cycle diagram of the heat storage type air conditioner of the second embodiment of the present invention, and FIG. 4 is a flow chart showing the operation of the heat storage type air conditioner of the same embodiment.

【0068】昼間冷房運転(同時運転モード);室内負
荷が比較的大きい場合には、STEP1、及びSTEP
2においてモード制御装置MODEにより同時運転モー
ドに切替えられる。
Daytime cooling operation (simultaneous operation mode); if the indoor load is relatively large, STEP1 and STEP
In 2, the mode controller MODE switches to the simultaneous operation mode.

【0069】STEP3にて冷媒搬送ポンプPM、及び
圧縮機2が運転を開始すると共に、STEP4にて冷媒
対冷媒熱交換器の2次側熱交換部14b出口の冷媒過冷
却度SC1の制御目標範囲A(下限値Amin、上限値Am
ax)、及び蓄熱槽の2次側熱交換部13b出口の冷媒過
冷却度SC2の制御目標範囲B(下限値Bmin、上限値
Bmax)を設定し、STEP5に移行する。
In STEP3, the refrigerant transport pump PM and the compressor 2 start operating, and in STEP4, the control target range of the refrigerant supercooling degree SC1 at the outlet of the secondary side heat exchange section 14b of the refrigerant-refrigerant heat exchanger. A (lower limit value Amin, upper limit value Am
ax) and the control target range B (lower limit value Bmin, upper limit value Bmax) of the refrigerant supercooling degree SC2 at the outlet of the secondary side heat exchange section 13b of the heat storage tank, and the process proceeds to STEP5.

【0070】STEP5において蓄熱槽の2次側熱交換
部13b出口の冷媒過冷却度SC2が制御目標範囲Bの
下限値Bmaxよりも小さい場合には、蓄熱槽STRの冷
媒循環量を減少させて蓄熱槽の2次側熱交換部13b出
口の冷媒過冷却度SC2を増大させるべく、STEP6
に移行して第2流量弁RV2を所定開度だけ閉じる。
In STEP 5, when the degree of refrigerant supercooling SC2 at the outlet of the secondary side heat exchange section 13b of the heat storage tank is smaller than the lower limit value Bmax of the control target range B, the refrigerant circulation amount in the heat storage tank STR is reduced to store heat. In order to increase the degree of refrigerant supercooling SC2 at the outlet of the secondary side heat exchange section 13b of the tank, STEP6
And the second flow valve RV2 is closed by a predetermined opening degree.

【0071】逆に、蓄熱槽の2次側熱交換部13b出口
の冷媒過冷却度SC2が制御目標範囲Bの下限値Bmin
以上の場合にはSTEP7に進み、更に蓄熱槽の2次側
熱交換部13b出口の冷媒過冷却度SC2が制御目標範
囲Bの上限値Bmaxよりも大きい場合には、蓄熱槽ST
Rの冷媒循環量を増大させて蓄熱槽の2次側熱交換部1
3b出口の冷媒過冷却度SC2を減少させるべく、ST
EP8に移行して第2流量弁RV2を所定開度だけ開
く。
On the contrary, the refrigerant supercooling degree SC2 at the outlet of the secondary side heat exchange section 13b of the heat storage tank is the lower limit value Bmin of the control target range B.
In the above case, the process proceeds to STEP 7, and when the refrigerant supercooling degree SC2 at the outlet of the secondary side heat exchange section 13b of the heat storage tank is larger than the upper limit value Bmax of the control target range B, the heat storage tank ST
The secondary side heat exchange section 1 of the heat storage tank is increased by increasing the refrigerant circulation amount of R.
In order to reduce the refrigerant supercooling degree SC2 at the 3b outlet, ST
The process moves to EP8, and the second flow valve RV2 is opened by a predetermined opening degree.

【0072】尚、蓄熱槽の2次側熱交換部13b出口の
冷媒過冷却度SC2が制御目標範囲Bに収まっている場
合には、第2流量弁RV2は動作しない。
When the refrigerant supercooling degree SC2 at the outlet of the secondary heat exchange section 13b of the heat storage tank is within the control target range B, the second flow valve RV2 does not operate.

【0073】その後STEP9において、冷媒対冷媒熱
交換器の2次側熱交換部14b出口の冷媒過冷却度SC
1が制御目標範囲Aの下限値Aminよりも小さい場合に
は、冷媒対冷媒熱交換器HEXの冷媒循環量を減少させ
て冷媒対冷媒熱交換器の2次側熱交換部14b出口の冷
媒過冷却度SC1を増大させるべく、STEP10に移
行して第1流量弁RV1を所定開度だけ閉じる。
Then, in STEP 9, the degree of refrigerant supercooling SC at the outlet of the secondary side heat exchange section 14b of the refrigerant-refrigerant heat exchanger.
When 1 is smaller than the lower limit value Amin of the control target range A, the refrigerant circulation amount of the refrigerant-refrigerant heat exchanger HEX is reduced to reduce the refrigerant excess at the outlet of the secondary side heat exchange section 14b of the refrigerant-refrigerant heat exchanger. In order to increase the cooling degree SC1, the process proceeds to STEP10 and the first flow valve RV1 is closed by a predetermined opening degree.

【0074】逆に、冷媒対冷媒熱交換器の2次側熱交換
部14b出口の冷媒過冷却度SC1が制御目標範囲Aの
下限値Amin以上の場合にはSTEP11に進み、更に
冷媒対冷媒熱交換器の2次側熱交換部14b出口の冷媒
過冷却度SC1が制御目標範囲Aの上限値Amaxよりも
大きい場合には、冷媒対冷媒熱交換器HEXの冷媒循環
量を増大させて冷媒対冷媒熱交換器の2次側熱交換部1
4b出口の冷媒過冷却度SC1を減少させるべく、ST
EP12に移行して第1流量弁RV1を所定開度だけ開
く。
On the contrary, when the refrigerant supercooling degree SC1 at the outlet of the secondary side heat exchange section 14b of the refrigerant-refrigerant heat exchanger is equal to or higher than the lower limit value Amin of the control target range A, the process proceeds to STEP11, and the refrigerant-refrigerant heat is further transferred. When the degree of refrigerant supercooling SC1 at the outlet of the secondary side heat exchange section 14b of the exchanger is larger than the upper limit value Amax of the control target range A, the refrigerant circulation amount of the refrigerant / refrigerant heat exchanger HEX is increased to increase the refrigerant pair. Secondary side heat exchange section 1 of refrigerant heat exchanger
In order to reduce the refrigerant supercooling degree SC1 at the 4b outlet, ST
The process moves to EP12, and the first flow valve RV1 is opened by a predetermined opening degree.

【0075】尚、冷媒対冷媒熱交換器の2次側熱交換部
14b出口の冷媒過冷却度SC1が制御目標範囲Aに収
まっている場合には、第1流量弁RV1は動作しない。
When the refrigerant supercooling degree SC1 at the outlet of the secondary side heat exchange section 14b of the refrigerant-refrigerant heat exchanger is within the control target range A, the first flow valve RV1 does not operate.

【0076】しかし、このように運転を続け、蓄熱槽S
TR内の蓄熱量の減少に伴って水温が上昇すると、蓄熱
槽の2次側熱交換部13bの管内側冷媒と管外側の水と
の温度差が小さくなって蓄熱槽STRにおける熱交換量
が低下し、蓄熱槽の2次側熱交換部13b出口の冷媒過
冷却度を保持できなくなってしまう。
However, the operation is continued in this way, and the heat storage tank S
When the water temperature rises as the amount of heat stored in TR decreases, the temperature difference between the refrigerant inside the pipe and the water outside the pipe of the secondary side heat exchange section 13b of the heat storage tank decreases, and the amount of heat exchange in the heat storage tank STR As a result, the refrigerant supercooling degree at the outlet of the secondary side heat exchange portion 13b of the heat storage tank cannot be maintained.

【0077】更に、蓄熱槽の2次側熱交換部13b出口
の冷媒過冷却度を保持できなくなると、蓄熱槽の2次側
熱交換部13b管内側の冷媒は完全な2相状態となるた
めに蓄熱槽STRにおける圧力損失が増大し、蓄熱槽の
2次側熱交換部13bを流れる冷媒循環量が減少してし
まう。
Further, if the degree of refrigerant supercooling at the outlet of the secondary side heat exchange section 13b of the heat storage tank cannot be maintained, the refrigerant inside the tube of the secondary side heat exchange section 13b of the heat storage tank becomes a complete two-phase state. In addition, the pressure loss in the heat storage tank STR increases, and the amount of refrigerant circulation flowing through the secondary heat exchange section 13b of the heat storage tank decreases.

【0078】その結果、蓄熱槽STR内の蓄熱量を有効
に取り出せなくなり、冷房能力の不足を生じてしまう。
As a result, the amount of heat stored in the heat storage tank STR cannot be effectively taken out, resulting in insufficient cooling capacity.

【0079】そこでSTEP13において、蓄熱量検出
装置CALにより蓄熱槽STR内の蓄熱量が所定値以下
となったことを検知した場合にはSTEP14に移行
し、蓄熱槽STR内の蓄熱量を使いきるべく第2流量弁
RV2の開度を全開として運転を行う。
Therefore, in STEP 13, when it is detected by the heat storage amount detecting device CAL that the heat storage amount in the heat storage tank STR is less than or equal to a predetermined value, the process proceeds to STEP 14 to use up the heat storage amount in the heat storage tank STR. The operation is performed by fully opening the second flow valve RV2.

【0080】そして、STEP15において、蓄熱槽の
2次側熱交換部13b出口の冷媒過冷却度SC2を保持
できなくなった時点でSTEP16に移行し、第1流量
弁RV1の開度を所定開度以下として蓄熱槽STRに強
制的に冷媒を循環させ、蓄熱槽STR内の水温が所定値
以上となるまで同時運転モードでの運転を行う。
Then, in STEP 15, when the refrigerant supercooling degree SC2 at the outlet of the secondary side heat exchange section 13b of the heat storage tank cannot be maintained, the process proceeds to STEP 16, and the opening degree of the first flow valve RV1 is set to a predetermined opening degree or less. As a result, the refrigerant is forcibly circulated in the heat storage tank STR, and the operation in the simultaneous operation mode is performed until the water temperature in the heat storage tank STR reaches or exceeds a predetermined value.

【0081】このことにより、蓄熱槽STR内の蓄熱量
が減少した場合においても蓄熱槽STR内の蓄熱量を有
効に取り出すと共に、冷媒対冷媒熱交換器HEXにおい
ても熱交換を行うため、室内負荷が大きい場合にも冷房
能力の不足を防止することができる。
As a result, even when the heat storage amount in the heat storage tank STR is reduced, the heat storage amount in the heat storage tank STR is effectively taken out, and heat is also exchanged in the refrigerant-refrigerant heat exchanger HEX. It is possible to prevent a shortage of the cooling capacity even when the value is large.

【0082】以上のように、昼間冷房運転時において、
室内負荷が比較的小さい蓄熱槽運転モードでかつ蓄熱槽
STRでの熱交換量が低下した場合に、第1制御装置C
NT1により蓄熱槽運転モードにて蓄熱槽STR内の蓄
熱量を有効に取り出すと共に、室内負荷が比較的大きい
同時運転モードでかつ蓄熱槽STRでの熱交換量が低下
した場合に、第2制御装置CNT2により同時運転モー
ドにて蓄熱槽STR内の蓄熱量を有効に取り出すことに
より、室内負荷に対する冷房能力の不足を防止し得る蓄
熱式空気調和機を提供することができる。
As described above, during the daytime cooling operation,
In the heat storage tank operation mode in which the indoor load is relatively small, and when the heat exchange amount in the heat storage tank STR decreases, the first control device C
When the amount of heat stored in the heat storage tank STR is effectively taken out by the NT1 in the heat storage tank operation mode, and the amount of heat exchange in the heat storage tank STR decreases in the simultaneous operation mode in which the indoor load is relatively large, the second control device By effectively extracting the amount of heat stored in the heat storage tank STR by the CNT 2 in the simultaneous operation mode, it is possible to provide the heat storage type air conditioner capable of preventing the insufficient cooling capacity with respect to the indoor load.

【0083】[0083]

【発明の効果】以上説明したように本発明は、冷媒対冷
媒熱交換器と蓄熱槽を介した1次側冷凍サイクルと2次
側冷凍サイクルとからなり、昼間冷房運転時において蓄
熱量が減少して蓄熱槽での熱交換量が低下した場合、室
内負荷が比較的小さい蓄熱槽運転モード時には第1制御
装置により蓄熱槽内の蓄熱量を有効に取り出すと共に、
室内負荷が比較的大きい同時運転モード時には第2制御
装置により蓄熱槽内の蓄熱量を有効に取り出すことによ
り、室内負荷に対する冷房能力の不足を防止し得る蓄熱
式空気調和機を提供することができる。
As described above, the present invention comprises the primary side refrigeration cycle and the secondary side refrigeration cycle through the refrigerant-refrigerant heat exchanger and the heat storage tank, and the heat storage amount decreases during the daytime cooling operation. Then, when the heat exchange amount in the heat storage tank decreases, the heat storage amount in the heat storage tank is effectively taken out by the first control device in the heat storage tank operation mode in which the indoor load is relatively small,
By effectively extracting the amount of heat stored in the heat storage tank by the second control device in the simultaneous operation mode in which the indoor load is relatively large, it is possible to provide a heat storage type air conditioner capable of preventing insufficient cooling capacity with respect to the indoor load. .

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

【図1】本発明の第1の実施例による蓄熱式空気調和機
の冷凍サイクル図
FIG. 1 is a refrigeration cycle diagram of a heat storage type air conditioner according to a first embodiment of the present invention.

【図2】同実施例の蓄熱式空気調和機の動作を示すフロ
ーチャート
FIG. 2 is a flowchart showing the operation of the heat storage type air conditioner of the same embodiment.

【図3】本発明の第2の実施例による蓄熱式空気調和機
の冷凍サイクル図
FIG. 3 is a refrigeration cycle diagram of a heat storage type air conditioner according to a second embodiment of the present invention.

【図4】同実施例の蓄熱式空気調和機の動作を示すフロ
ーチャート
FIG. 4 is a flowchart showing the operation of the heat storage type air conditioner of the same embodiment.

【図5】従来例を示す蓄熱式空気調和機の冷凍サイクル
FIG. 5 is a refrigeration cycle diagram of a heat storage type air conditioner showing a conventional example.

【符号の説明】[Explanation of symbols]

2 圧縮機 3a 第1四方弁 3b 第2四方弁 4 室外側熱交換器 12a,12b 室内ユニット 13a 蓄熱槽の1次側熱交換部 13b 蓄熱槽の2次側熱交換部 14a 冷媒対冷媒熱交換器の1次側熱交換部 14b 冷媒対冷媒熱交換器の2次側熱交換部 15a,15b 室内側熱交換器 RVa,RVb 室内流量弁 18 水温検出装置 19 水位検出装置 CAL 蓄熱量検出装置 STR 蓄熱槽 HEX 冷媒対冷媒熱交換器 PM 冷媒搬送ポンプ EXP1 第1膨張弁 EXP2 第2膨張弁 RV1 第1流量弁 RV2 第2流量弁 MODE モード制御装置 SUB 過冷却度検出装置 CNT1 第1制御装置 CNT2 第2制御装置 2 Compressor 3a First four-way valve 3b Second four-way valve 4 Outdoor heat exchanger 12a, 12b Indoor unit 13a Primary heat exchange part of heat storage tank 13b Secondary heat exchange part of heat storage tank 14a Refrigerant-to-refrigerant heat exchange Primary side heat exchange part 14b Refrigerant-to-refrigerant heat exchanger secondary side heat exchange part 15a, 15b Indoor side heat exchanger RVa, RVb Indoor flow valve 18 Water temperature detection device 19 Water level detection device CAL Heat storage amount detection device STR Heat storage tank HEX Refrigerant-refrigerant heat exchanger PM Refrigerant transfer pump EXP1 First expansion valve EXP2 Second expansion valve RV1 First flow valve RV2 Second flow valve MODE mode control device SUB Supercooling degree detection device CNT1 First control device CNT2 No. 2 control device

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 圧縮機と、第1四方弁と、室外側熱交換
器とを直列に接続し、かつ第1膨張弁と冷媒対冷媒熱交
換器の1次側熱交換部を、第2膨張弁と蓄熱槽の1次側
熱交換部に対して並列に接続した1次側冷凍サイクル
と、 冷媒搬送ポンプと第2四方弁と冷媒タンクとからなるポ
ンプユニットと、室内側熱交換器と室内流量弁とからな
る室内ユニットとを接続し、かつ第1流量弁と冷媒対冷
媒熱交換器の2次側熱交換部を、第2流量弁と蓄熱槽の
2次側熱交換部に対して並列に接続した2次側冷凍サイ
クルとからなり、 前記蓄熱槽に水温検出装置と水位検出装置を設置して、
蓄熱槽の水温と水位とから蓄熱槽の蓄熱量を算出する蓄
熱量検出装置を備え、 冷房運転時の2次側冷凍サイクルにおいて、冷媒対冷媒
熱交換器の2次側熱交換部を冷媒が流れる冷媒対冷媒熱
交換器運転モードと、蓄熱槽の2次側熱交換部を冷媒が
流れる蓄熱槽運転モードと、冷媒対冷媒熱交換器の2次
側熱交換部と蓄熱槽の2次側熱交換部の両方を冷媒が流
れる同時運転モードの各運転モードを切替えるモード制
御装置を備え、 更に冷房運転時の冷媒対冷媒熱交換器の2次側熱交換部
出口、及び蓄熱槽の2次側熱交換部出口の冷媒過冷却度
を検出する過冷却度検出装置を備え、 蓄熱槽運転モードの場合で、かつ蓄熱槽の蓄熱量が所定
値以下となった場合に第2流量弁を全開として、蓄熱槽
水温が所定値以上となるまで蓄熱槽運転モードでの運転
を行う第1制御装置を備えた蓄熱式空気調和機。
1. A compressor, a first four-way valve, and an outdoor heat exchanger are connected in series, and a first expansion valve and a primary-side heat exchange section of a refrigerant-refrigerant heat exchanger are connected to a second heat exchanger. A primary side refrigeration cycle connected in parallel to the expansion valve and the primary side heat exchange section of the heat storage tank, a pump unit consisting of a refrigerant transfer pump, a second four-way valve and a refrigerant tank, and an indoor side heat exchanger. An indoor unit including an indoor flow valve is connected, and the first flow valve and the secondary heat exchange part of the refrigerant-refrigerant heat exchanger are connected to the second flow valve and the secondary heat exchange part of the heat storage tank. And a secondary side refrigeration cycle connected in parallel, and a water temperature detecting device and a water level detecting device are installed in the heat storage tank,
A heat storage amount detection device that calculates the heat storage amount of the heat storage tank from the water temperature and the water level of the heat storage tank is provided, and in the secondary side refrigeration cycle during cooling operation, the refrigerant is used as the refrigerant for the secondary side heat exchange section of the refrigerant-refrigerant heat exchanger. Refrigerant-to-refrigerant heat exchanger operation mode, heat storage tank operation mode in which refrigerant flows through the secondary side heat exchange section of the heat storage tank, secondary side heat exchange section of refrigerant-to-refrigerant heat exchanger and secondary side of the heat storage tank A mode control device is provided for switching each operation mode of simultaneous operation modes in which the refrigerant flows through both the heat exchange parts, and further, the outlet of the secondary side heat exchange part of the refrigerant-refrigerant heat exchanger during the cooling operation, and the secondary of the heat storage tank. Equipped with a supercooling degree detection device that detects the degree of refrigerant supercooling at the outlet of the side heat exchange unit, and fully opens the second flow valve when in the heat storage tank operation mode and when the heat storage amount in the heat storage tank is below a predetermined value. As a result, in the heat storage tank operation mode until the water temperature of the heat storage tank exceeds a predetermined value Thermal storage type air conditioner having a first controller for rolling.
【請求項2】 同時運転モードの場合で、かつ蓄熱槽の
蓄熱量が所定値以下となった場合に第2流量弁を全開と
し、更にその後の運転において蓄熱槽の2次側熱交換部
出口の冷媒過冷却度を保持できなくなった場合に、第1
流量弁を所定開度以下として、蓄熱槽水温が所定値以上
となるまで同時運転モードでの運転を行う第2制御装置
を備えた請求項1記載の蓄熱式空気調和機。
2. In the simultaneous operation mode, when the amount of heat stored in the heat storage tank is below a predetermined value, the second flow valve is fully opened, and in the subsequent operation, the outlet of the secondary side heat exchange section of the heat storage tank. If the refrigerant supercooling degree of
The heat storage type air conditioner according to claim 1, further comprising a second control device that operates in the simultaneous operation mode until the heat storage tank water temperature becomes equal to or higher than a predetermined value with the flow valve set to a predetermined opening or less.
JP18228094A 1994-08-03 1994-08-03 Regenerative air-conditioner Pending JPH0849937A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18228094A JPH0849937A (en) 1994-08-03 1994-08-03 Regenerative air-conditioner

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18228094A JPH0849937A (en) 1994-08-03 1994-08-03 Regenerative air-conditioner

Publications (1)

Publication Number Publication Date
JPH0849937A true JPH0849937A (en) 1996-02-20

Family

ID=16115517

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18228094A Pending JPH0849937A (en) 1994-08-03 1994-08-03 Regenerative air-conditioner

Country Status (1)

Country Link
JP (1) JPH0849937A (en)

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