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JPH0792289B2 - Operation control device and operation control method for heat storage type air conditioner - Google Patents
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JPH0792289B2 - Operation control device and operation control method for heat storage type air conditioner - Google Patents

Operation control device and operation control method for heat storage type air conditioner

Info

Publication number
JPH0792289B2
JPH0792289B2 JP16213789A JP16213789A JPH0792289B2 JP H0792289 B2 JPH0792289 B2 JP H0792289B2 JP 16213789 A JP16213789 A JP 16213789A JP 16213789 A JP16213789 A JP 16213789A JP H0792289 B2 JPH0792289 B2 JP H0792289B2
Authority
JP
Japan
Prior art keywords
heat
heat exchanger
compressor
cold
storage
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
JP16213789A
Other languages
Japanese (ja)
Other versions
JPH0328671A (en
Inventor
凡敏 増井
伸廣 楠本
伸二 松浦
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 Industries Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Daikin Industries Ltd filed Critical Daikin Industries Ltd
Priority to JP16213789A priority Critical patent/JPH0792289B2/en
Publication of JPH0328671A publication Critical patent/JPH0328671A/en
Publication of JPH0792289B2 publication Critical patent/JPH0792289B2/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】 (産業上の利用分野) 本発明は、蓄熱媒体を貯溜してなる蓄熱槽を備えた蓄熱
式空気調和装置の運転制御装置及び運転制御方法に係
り、特に、蓄冷熱運転時、通常冷房および蓄冷熱同時運
転時における運転制御対策に関する。
Description: TECHNICAL FIELD The present invention relates to an operation control device and an operation control method for a heat storage type air conditioner provided with a heat storage tank that stores a heat storage medium, and more particularly to a cold storage heat storage device. The present invention relates to operation control measures during operation, during normal cooling and simultaneous cold storage heat operation.

(従来の技術) 近年、開発の進んでいる蓄熱式空気調和装置の一般的な
構成としては、圧縮機、熱源側熱交換器、主減圧弁及び
利用側熱交換器が冷媒配管で順次接続されて主冷房回路
が構成される一方、蓄熱用の氷を貯溜する蓄熱槽を備
え、該蓄熱槽内に配置されると共に上記主冷媒回路に接
続されて冷媒と蓄熱媒体との熱交換を行う蓄熱熱交換器
と、該蓄熱熱交換器の冷媒上流側に配設された蓄冷熱用
減圧機構とを備えている。
(Prior Art) As a general configuration of a heat storage type air conditioner which has been developed in recent years, a compressor, a heat source side heat exchanger, a main pressure reducing valve and a use side heat exchanger are sequentially connected by a refrigerant pipe. A heat storage tank that is configured to form a main cooling circuit and that includes a heat storage tank that stores ice for heat storage, is arranged in the heat storage tank, and is connected to the main refrigerant circuit to perform heat exchange between the refrigerant and the heat storage medium. It comprises a heat exchanger and a cold storage heat decompression mechanism arranged on the refrigerant upstream side of the heat storage heat exchanger.

また、この蓄熱式空気調和装置で生成される蓄熱媒体と
しての氷の生成手段には、これまで様々なものが開発さ
れている。その一例として、特開昭61−289253号公報に
開示されるような蓄熱運転制御方法がある。この公報に
開示されている方法は、所定時刻に対し蓄熱量と目標蓄
熱量との差により、予め設定された補正係数へ加減算し
て蓄熱運転の開始時刻を補正することにより、最終的に
上記所定時刻に目標蓄熱量が得られるように製氷開始時
刻を定めるべく制御するものである。
In addition, various means have been developed so far as means for generating ice as a heat storage medium generated by this heat storage type air conditioner. As an example thereof, there is a heat storage operation control method as disclosed in JP-A-61-289253. The method disclosed in this publication corrects the start time of the heat storage operation by adding / subtracting to / from a preset correction coefficient depending on the difference between the heat storage amount and the target heat storage amount at a predetermined time, and finally The ice making start time is controlled so that the target heat storage amount can be obtained at a predetermined time.

一方、この主の蓄熱式空気調和装置において、通常冷房
運転や蓄冷熱運転を単独で行うだけでは余剰の運転性能
が生じ、運転効率が悪いという問題があり、夜間に通常
冷房運転と並行して蓄冷熱運転を行う、即ち、通常冷房
および蓄冷熱同時運転を可能にすることが望まれてい
る。
On the other hand, in this main heat storage type air conditioner, there is a problem that operating efficiency is poor due to excess operation performance caused only by performing the normal cooling operation and the cold storage operation alone, and in parallel with the normal cooling operation at night. It is desired to perform the cold storage heat operation, that is, to enable the normal cooling and the cold storage heat simultaneous operation.

(発明が解決しようとする課題) しかしながら、上記蓄熱式空気調和装置にあっては、各
運転時に以下に述べるような課題を有している。
(Problems to be Solved by the Invention) However, the heat storage type air conditioner has the following problems during each operation.

つまり、通常冷房及び蓄冷熱同時運転を行うようにする
と、 (I)冷房負荷が大きくなり、蒸発圧力相当飽和温度が
高くなると(例えば−5℃以上)、冷媒の温度と蓄熱媒
体としての水の凍結温度との温度差が十分に取れないた
めに製氷量が少なく、蓄冷熱が十分に行われないことに
なる。
That is, when the normal cooling and the cold storage heat simultaneous operation are performed, (I) When the cooling load increases and the evaporation pressure-equivalent saturation temperature rises (for example, −5 ° C. or higher), the temperature of the refrigerant and the water as the heat storage medium are increased. Since the temperature difference from the freezing temperature cannot be sufficiently obtained, the amount of ice making is small and the cold storage heat is not sufficiently performed.

(II)一方、逆に冷房負荷が小さくなり、蒸発圧力相当
飽和温度が低くなると(例えば−10℃以下)、上記冷媒
と水との温度差が十分に取れ、蓄冷熱量は十分に得られ
るが、室内側で空気温度が低下し過ぎてドラフトの原因
となったり、利用側(室内側)熱交換器が凍結してしま
い連続運転が不可能になる虞れがある。
(II) On the other hand, conversely, when the cooling load becomes small and the saturation pressure equivalent to the evaporation pressure becomes low (for example, -10 ° C or lower), the temperature difference between the refrigerant and water can be sufficiently obtained, and the amount of cold storage heat can be sufficiently obtained. However, there is a risk that the air temperature in the room will drop too much, causing drafts, or the user-side (indoor) heat exchanger will freeze, making continuous operation impossible.

また、蓄冷熱運転時においては、これまで上述した公報
に示されるように目標蓄熱量にするために蓄熱運転開始
時間を変化させる制御をしたものがあり、この場合、継
続運転時間は一定であり、圧縮機をその運転周波数が高
い領域で使用する場合が多く、圧縮機の成績係数の最良
の周波数領域での制御をしておらず、消費電力の増大に
繋っていた。
Further, during the cold heat storage operation, there is a control for changing the heat storage operation start time in order to achieve the target heat storage amount as shown in the above publications, and in this case, the continuous operation time is constant. In many cases, the compressor is used in a region where the operating frequency is high, and the compressor is not controlled in the best frequency region of the coefficient of performance, leading to an increase in power consumption.

そこで、本発明は、上述した様々な不具合を生じさせる
ことなく、運転効率の良い蓄冷熱運転および実用性の高
い通常冷房および蓄冷熱同時運転を行うことが可能な蓄
熱式空気調和装置の運転制御装置および運転制御方法を
得ることを目的とする。
Therefore, the present invention is an operation control of a heat storage type air conditioner capable of performing a cool storage heat operation with good operation efficiency and a highly practical normal cooling and cool storage heat simultaneous operation without causing the various problems described above. An object is to obtain an apparatus and an operation control method.

(課題を解決するための手段) 上記目的を達成するための本発明の解決手段を以下に述
べる。
(Means for Solving the Problem) The solving means of the present invention for achieving the above object will be described below.

先ず、請求項(1)記載の発明は、第1図に示すよう
に、容量の可変な圧縮機(1)、熱源側熱交換器
(3)、開度の可変自在な主減圧弁(6)及び利用側熱
交換器(7)を冷媒配管(9)で順次接続してなる主冷
媒回路(10)と、蓄冷熱用の氷を貯溜する蓄熱槽(11)
とを備える一方、上記蓄熱槽(11)内に配置されると共
に、上記主冷媒回路(10)に接続され、冷媒と蓄熱媒体
との熱交換を行うための蓄熱熱交換器(12)と、蓄冷熱
用減圧機構(14)とを備えている。そして、少なくとも
通常冷房運転時には、熱源側熱交換器(3)で凝縮され
た液冷媒が主冷媒回路(10)のみを流れて主減圧弁
(6)で減圧され、利用側熱交換器(7)で蒸発して圧
縮機(1)に戻るように循環し、蓄冷熱運転時には、熱
源側熱交換器(3)で凝縮された液冷媒が蓄冷熱用減圧
機構(14)で減圧され、蓄熱熱交換器(12)で蒸発した
のち圧縮機(1)に戻るように循環し、蓄冷熱回収運転
時には、熱源側熱交換器(3)で凝縮された液冷媒が主
冷媒回路(10)から蓄熱熱交換器(12)で過冷却された
後、主冷媒回路(10)の利用側熱交換器(7)で蒸発し
て圧縮機(1)に戻るように循環し、通常冷房及び蓄冷
熱同時運転時には、熱源側熱交換器(3)で凝縮された
液冷媒の一部が主冷媒回路(10)の利用側熱交換器
(7)で蒸発する一方、液冷媒の残部が蓄熱熱交換器
(12)で蒸発した後、それぞれ圧縮機(1)に戻るよう
に回路接続を切換える切換手段(51)を備えた蓄熱式空
気調和装置を対象としている。そして、通常冷房及び蓄
冷熱同時運転時に、主減圧弁(6)の最大開度を通常冷
房運転時に設定される第1最大開度より小さい所定の第
2最大開度に設定する最大開度設定手段(52)と、蒸発
圧力相当飽和温度を検出する蒸発温度検出手段(53)
と、圧縮機(1)の最大容量運転時を検出する容量検出
手段(54)と、該容量検出手段(54)が圧縮機(1)の
最大容量運転を検出し、且つ上記蒸発温度検出手段(5
3)が検出した蒸発圧力相当飽和温度が予め設定された
設定温度以上になると、主減圧弁(6)の最大開度を第
2最大開度より小さい所定の第3最大開度に設定する最
大開度規制手段(55)とを備えた構成としている。
First, according to the invention described in claim (1), as shown in FIG. 1, a compressor (1) with variable capacity, a heat source side heat exchanger (3), and a main pressure reducing valve (6) with variable opening degree are provided. ) And the heat exchanger (7) on the use side are sequentially connected by a refrigerant pipe (9), and a heat storage tank (11) for storing ice for cold storage heat.
And a heat storage heat exchanger (12) for performing heat exchange between the refrigerant and the heat storage medium, the heat storage tank being provided in the heat storage tank (11) and connected to the main refrigerant circuit (10). The cold storage heat reducing mechanism (14) is provided. Then, at least during normal cooling operation, the liquid refrigerant condensed in the heat source side heat exchanger (3) flows only through the main refrigerant circuit (10) and is decompressed by the main pressure reducing valve (6), and the use side heat exchanger (7). ) And circulates to return to the compressor (1), and during the cold heat storage operation, the liquid refrigerant condensed in the heat source side heat exchanger (3) is decompressed by the cold heat decompression mechanism (14), After being evaporated in the heat exchanger (12), it circulates back to the compressor (1), and during the cold heat recovery operation, the liquid refrigerant condensed in the heat source side heat exchanger (3) is discharged from the main refrigerant circuit (10). After being supercooled in the heat storage heat exchanger (12), it is circulated so as to evaporate in the utilization side heat exchanger (7) of the main refrigerant circuit (10) and return to the compressor (1) for normal cooling and cold storage heat. During the simultaneous operation, a part of the liquid refrigerant condensed in the heat source side heat exchanger (3) is vaporized in the use side heat exchanger (7) of the main refrigerant circuit (10). On the other hand, for the heat storage type air conditioner provided with the switching means (51) for switching the circuit connection so as to return to the compressor (1) after the rest of the liquid refrigerant is evaporated in the heat storage heat exchanger (12). There is. Then, during the simultaneous normal cooling and cold storage heat operation, the maximum opening setting for setting the maximum opening of the main pressure reducing valve (6) to a predetermined second maximum opening smaller than the first maximum opening set in the normal cooling operation. Means (52) and evaporation temperature detection means (53) for detecting a saturation temperature equivalent to the evaporation pressure
A capacity detecting means (54) for detecting the maximum capacity operation of the compressor (1), the capacity detecting means (54) detecting the maximum capacity operation of the compressor (1), and the evaporation temperature detecting means. (Five
When the vapor pressure equivalent saturation temperature detected by 3) becomes equal to or higher than the preset set temperature, the maximum opening of the main pressure reducing valve (6) is set to a predetermined third maximum opening smaller than the second maximum opening. The opening regulation means (55) is provided.

一方、請求項(2)記載の発明は、第2図に示すよう
に、容量の可変な圧縮機(1)、熱源側熱交換器
(3)、主減圧弁(6)及び利用側熱交換器(7)を冷
媒配管(9)で順次接続してなる主冷媒回路(10)と、
蓄冷熱用の氷を貯溜する蓄熱槽(11)とを備える一方、
上記蓄熱槽(11)内に配置されると共に、上記主冷媒回
路(10)に接続され、冷媒と蓄熱媒体との熱交換を行う
ための蓄熱熱交換器(12)と、蓄冷熱用減圧機構(14)
とを備えている。そして、少なくとも通常冷房運転時に
は、熱源側熱交換器(3)で凝縮された液冷媒が主冷媒
回路(10)のみを流れて主減圧弁(6)で減圧され、利
用側熱交換器(7)で蒸発して圧縮機(1)に戻るよう
に循環し、蓄冷熱運転時には、熱源側熱交換器(3)で
凝縮された液冷媒が蓄冷熱用減圧機構(14)で減圧さ
れ、蓄熱熱交換器(12)で蒸発したのち圧縮機(1)に
戻るように循環し、蓄冷熱回収運転時には、熱源側熱交
換器(3)で凝縮された液冷媒が主冷媒回路(10)から
蓄熱熱交換器(12)で過冷却された後、主冷媒回路(1
0)の利用側熱交換器(7)で蒸発して圧縮機(1)に
戻るように循環し、通常冷房及び蓄冷熱同時運転時に
は、熱源側熱交換器(3)で凝縮された液冷媒の一部が
主冷媒回路(10)の利用側熱交換器(7)で蒸発する一
方、液冷媒の残部が蓄熱熱交換器(12)で蒸発した後、
それぞれ圧縮機(1)に戻るように回路接続を切換える
切換手段(51)を備えた蓄熱式空気調和装置を対象とし
ている。そして、通常冷房及び蓄冷熱同時運転時に、蒸
発圧力相当飽和温度を検出する蒸発温度検出手段(53)
と、該蒸発温度検出手段(53)の出力信号を受けて蒸発
圧力相当飽和温度が予め設定された目標値になるように
圧縮機(1)の容量を制御する容量制御手段(56)とを
備えた構成としている。
On the other hand, the invention according to claim (2), as shown in FIG. 2, has a variable capacity compressor (1), a heat source side heat exchanger (3), a main pressure reducing valve (6), and a use side heat exchange. A main refrigerant circuit (10) formed by sequentially connecting a container (7) with a refrigerant pipe (9),
While having a heat storage tank (11) for storing ice for cold storage heat,
A heat storage heat exchanger (12) arranged in the heat storage tank (11) and connected to the main refrigerant circuit (10) for exchanging heat between the refrigerant and the heat storage medium, and a decompression mechanism for cold storage heat. (14)
It has and. Then, at least during normal cooling operation, the liquid refrigerant condensed in the heat source side heat exchanger (3) flows only through the main refrigerant circuit (10) and is decompressed by the main pressure reducing valve (6), and the use side heat exchanger (7). ) And circulates to return to the compressor (1), and during the cold heat storage operation, the liquid refrigerant condensed in the heat source side heat exchanger (3) is decompressed by the cold heat decompression mechanism (14), After being evaporated in the heat exchanger (12), it circulates back to the compressor (1), and during the cold heat recovery operation, the liquid refrigerant condensed in the heat source side heat exchanger (3) is discharged from the main refrigerant circuit (10). After being supercooled by the heat storage heat exchanger (12), the main refrigerant circuit (1
Liquid refrigerant that is circulated to return to the compressor (1) after being evaporated in the use side heat exchanger (7) of (0) and condensed in the heat source side heat exchanger (3) during normal cooling and cold storage simultaneous operation Part of the liquid refrigerant evaporates in the use side heat exchanger (7) of the main refrigerant circuit (10), while the rest of the liquid refrigerant evaporates in the heat storage heat exchanger (12),
The heat storage type air conditioner is provided with a switching means (51) for switching the circuit connection so as to return to the compressor (1). Then, the evaporation temperature detecting means (53) for detecting the saturation temperature corresponding to the evaporation pressure during the normal cooling and the cold storage heat simultaneous operation.
And a capacity control means (56) for receiving the output signal of the evaporation temperature detection means (53) and controlling the capacity of the compressor (1) so that the saturation temperature equivalent to the evaporation pressure becomes a preset target value. It has a configuration provided.

また、請求項(3)記載の発明は、上記請求項(1)記
載の蓄熱式空気調和装置の運転制御装置において、上記
請求項(2)に記載された容量制御手段(56)が設けら
れた構成となっている。
The invention according to claim (3) is the operation control device for a heat storage type air conditioner according to claim (1), wherein the capacity control means (56) according to claim (2) is provided. It has been configured.

そして、請求項(4)記載の発明は、第3図に示すよう
に、容量の可変な圧縮機(1)、熱源側熱交換器
(3)、主減圧弁(6)及び利用側熱交換器(7)を冷
媒配管(9)で順次接続してなる主冷媒回路(10)と、
蓄冷熱用の氷を貯溜する蓄熱槽(11)とを備える一方、
上記蓄熱槽(11)内に配置されると共に、上記主冷媒回
路(10)に接続され、冷媒と蓄熱媒体との熱交換を行う
ための蓄熱熱交換器(12)と、蓄冷熱用減圧機構(14)
とを備えている。そして、少なくとも通常冷房運転時に
は、熱源側熱交換器(3)で凝縮された液冷媒が主冷媒
回路(10)のみを流れて主減圧弁(6)で減圧され、利
用側熱交換器(7)で蒸発して圧縮機(1)に戻るよう
に循環し、蓄冷熱運転時には、熱源側熱交換器(3)で
凝縮された液冷媒が蓄冷熱用減圧機構(14)で減圧さ
れ、蓄熱熱交換器(12)で蒸発したのち圧縮機(1)に
戻るように循環し、蓄冷熱回収運転時には、熱源側熱交
換器(3)で凝縮された液冷媒が主冷媒回路(10)から
蓄熱熱交換器(12)で過冷却された後、主冷媒回路(1
0)の利用側熱交換器(7)で蒸発して圧縮機(1)に
戻るように循環し、通常冷房及び蓄冷熱同時運転時に
は、熱源側熱交換器(3)で凝縮された液冷媒の一部が
主冷媒回路(10)の利用側熱交換器(7)で蒸発する一
方、液冷媒の残部が蓄熱熱交換器(12)で蒸発した後、
それぞれ圧縮機(1)に戻るように回路接続を切換える
切換手段(51)を備えた蓄熱式空気調和装置を対象とし
ている。そして、蓄冷熱運転時に、蓄冷熱運転時間を設
定する蓄冷熱時間設定手段(61)と、蓄熱槽(11)内の
必要製氷量を検出する製氷量検出手段(62)と、上記蓄
冷熱時間設定手段(61)および製氷量検出手段(62)か
らの出力信号を受けて、該必要製氷量を設定時間で製氷
するのに要する圧縮機(1)の最低運転周波数を算出す
る演算手段(63)と、演算手段(63)からの出力信号を
受け、該演算手段(63)で算出された圧縮機運転周波数
に基づき圧縮機(1)の運転を制御する運転制御手段
(64)と備えた構成としている。
The invention according to claim (4) is, as shown in FIG. 3, a compressor (1) having a variable capacity, a heat source side heat exchanger (3), a main pressure reducing valve (6) and a use side heat exchange. A main refrigerant circuit (10) formed by sequentially connecting a container (7) with a refrigerant pipe (9),
While having a heat storage tank (11) for storing ice for cold storage heat,
A heat storage heat exchanger (12) arranged in the heat storage tank (11) and connected to the main refrigerant circuit (10) for exchanging heat between the refrigerant and the heat storage medium, and a decompression mechanism for cold storage heat. (14)
It has and. Then, at least during normal cooling operation, the liquid refrigerant condensed in the heat source side heat exchanger (3) flows only through the main refrigerant circuit (10) and is decompressed by the main pressure reducing valve (6), and the use side heat exchanger (7). ) And circulates to return to the compressor (1), and during the cold heat storage operation, the liquid refrigerant condensed in the heat source side heat exchanger (3) is decompressed by the cold heat decompression mechanism (14), After being evaporated in the heat exchanger (12), it circulates back to the compressor (1), and during the cold heat recovery operation, the liquid refrigerant condensed in the heat source side heat exchanger (3) is discharged from the main refrigerant circuit (10). After being supercooled by the heat storage heat exchanger (12), the main refrigerant circuit (1
Liquid refrigerant that is circulated to return to the compressor (1) after being evaporated in the use side heat exchanger (7) of (0) and condensed in the heat source side heat exchanger (3) during normal cooling and cold storage simultaneous operation Part of the liquid refrigerant evaporates in the use side heat exchanger (7) of the main refrigerant circuit (10), while the rest of the liquid refrigerant evaporates in the heat storage heat exchanger (12),
The heat storage type air conditioner is provided with a switching means (51) for switching the circuit connection so as to return to the compressor (1). Then, during the cold storage heat operation, the cold storage heat time setting means (61) for setting the cold storage heat operation time, the ice making amount detection means (62) for detecting the required ice making amount in the heat storage tank (11), and the cold storage heat time. An arithmetic means (63) for receiving output signals from the setting means (61) and the ice making quantity detecting means (62) and calculating a minimum operating frequency of the compressor (1) required to make the required ice making quantity in a set time. ) And an operation control means (64) for controlling the operation of the compressor (1) on the basis of the compressor operating frequency calculated by the operation means (63) by receiving the output signal from the operation means (63). It is configured.

更に、請求項(5)記載の発明は、上記請求項(1),
(2)または(3)記載の蓄熱式空気調和装置の運転制
御装置において、上記請求項(4)に記載の蓄冷熱時間
設定手段(61)、製氷量検出手段(62)、演算手段(6
3)および運転制御手段(64)が設けられた構成として
いる。
Further, the invention according to claim (5) is based on the above-mentioned claim (1),
In the operation control device of the heat storage type air conditioner according to (2) or (3), the cold storage heat time setting means (61), the ice making amount detection means (62), and the calculation means (6) according to claim (4).
3) and operation control means (64) are provided.

最後に、請求項(6)記載の発明は、容量の可変な圧縮
機(1)、熱源側熱交換器(3)、開度の可変自在な主
減圧弁(6)及び利用側熱交換器(7)を冷媒配管
(9)で順次接続してなる主冷媒回路(10)と、蓄冷熱
用の氷を貯溜する蓄熱槽(11)とを備える一方、上記蓄
熱槽(11)内に配置されると共に、上記主冷媒回路(1
0)に接続され、冷媒と蓄熱媒体との熱交換を行うため
の蓄熱熱交換器(12)と、蓄冷熱用減圧機構(14)とを
備えている。そして、少なくとも通常冷房運転時には、
熱源側熱交換器(3)で凝縮された液冷媒が主冷媒回路
(10)のみを流れて主減圧弁(6)で減圧され、利用側
熱交換器(7)で蒸発して圧縮機(1)に戻るように循
環し、蓄冷熱運転時には、熱源側熱交換器(3)で凝縮
された液冷媒が蓄冷熱用減圧機構(14)で減圧され、蓄
熱熱交換器(12)で蒸発したのち圧縮機(1)に戻るよ
うに循環し、蓄冷熱回収運転時には、熱源側熱交換器
(3)で凝縮された液冷媒が主冷媒回路(10)から蓄熱
熱交換器(12)で過冷却された後、主冷媒回路(10)の
利用側熱交換器(7)で蒸発して圧縮機(1)に戻るよ
うに循環し、通常冷房及び蓄冷熱同時運転時には、熱源
側熱交換器(3)で凝縮された液冷媒の一部が主冷媒回
路(10)の利用側熱交換器(7)で蒸発する一方、液冷
媒の残部が蓄熱熱交換器(12)で蒸発した後、それぞれ
圧縮機(1)に戻るように回路接続を切換える切換手段
(51)を備えた蓄熱式空気調和装置を対象とした運転制
御方法である。そして、蓄冷熱運転時には、蓄冷熱運転
時間を蓄冷熱時間設定手段(61)によって設定すると同
時に蓄熱槽(11)内の必要製氷量を製氷量検出手段(6
2)が検出した後、演算手段(63)が上記蓄冷熱運転時
間で必要製氷量を製氷するのに要する圧縮機(1)の最
低運転周波数を算出し、この算出された圧縮機運転周波
数に基づいて運転制御手段(64)が圧縮機(1)の運転
を制御する一方、通常冷房及び蓄冷熱同時運転時には、
最大開度設定手段(52)が主減圧弁(6)の最大開度を
通常冷房運転時に設定される第1最大開度より小さい所
定の第2最大開度に設定して、該主減圧弁(6)の開度
を過熱度制御すると共に、蒸発温度検出手段(53)が蒸
発圧力相当飽和温度を検出して容量制御手段(56)が圧
縮機(1)の容量を蒸発圧力相当飽和温度が所定の目標
値になるように制御し、その後、容量検出手段(54)が
圧縮機(1)の最大容量運転を検出し、且つ、蒸発圧力
相当飽和温度が所定温度以上になると、最大開度規制手
段(55)が主減圧弁(6)の最大開度を第2最大開度よ
り小さい第3最大開度に設定することを特徴とする (作用) 以上の構成により、請求項(1),(5)及び(6)の
発明では、切換手段(51)により回路接続が切換えられ
て、適宜、通常冷房運転,蓄冷熱運転,蓄冷熱回収運
転,通常冷房及び蓄冷熱同時運転が行われる。
Finally, the invention according to claim (6) is such that the compressor (1) with a variable capacity, the heat source side heat exchanger (3), the main pressure reducing valve (6) with a variable opening degree, and the use side heat exchanger. A main refrigerant circuit (10) in which (7) is sequentially connected by a refrigerant pipe (9), and a heat storage tank (11) for storing ice for cold storage heat are provided while being arranged in the heat storage tank (11). The main refrigerant circuit (1
A heat storage heat exchanger (12) connected to the heat storage medium (0) for exchanging heat between the refrigerant and the heat storage medium, and a cold storage heat decompression mechanism (14). And at least during normal cooling operation,
The liquid refrigerant condensed in the heat source side heat exchanger (3) flows only in the main refrigerant circuit (10), is decompressed by the main pressure reducing valve (6), and is evaporated in the use side heat exchanger (7) to generate a compressor ( During the cold storage heat operation, the liquid refrigerant condensed in the heat source side heat exchanger (3) is depressurized by the cold storage heat decompression mechanism (14) and evaporated in the heat storage heat exchanger (12). Then, it circulates back to the compressor (1), and during the cold storage heat recovery operation, the liquid refrigerant condensed in the heat source side heat exchanger (3) is transferred from the main refrigerant circuit (10) to the heat storage heat exchanger (12). After being supercooled, it circulates so as to evaporate in the use side heat exchanger (7) of the main refrigerant circuit (10) and return to the compressor (1), and heat exchange on the heat source side during normal cooling and cold storage heat simultaneous operation. A part of the liquid refrigerant condensed in the device (3) is evaporated in the utilization side heat exchanger (7) of the main refrigerant circuit (10), while the rest of the liquid refrigerant is the heat storage heat exchanger. After evaporation at 12), a operation control method of a thermal storage type air conditioner targeted with a switching means (51) for switching the circuit connection back to each compressor (1). During the cold storage heat operation, the cold storage heat operation time is set by the cold storage heat time setting means (61), and at the same time, the required ice making amount in the heat storage tank (11) is detected by the ice making amount detecting means (6).
After the detection by 2), the calculating means (63) calculates the minimum operating frequency of the compressor (1) required to make the required ice making amount in the above cold storage heat operation time, and the calculated operating frequency of the compressor is calculated. While the operation control means (64) controls the operation of the compressor (1) based on this,
The maximum opening setting means (52) sets the maximum opening of the main pressure reducing valve (6) to a predetermined second maximum opening smaller than the first maximum opening set during normal cooling operation, and the main pressure reducing valve is set. The degree of opening of (6) is controlled by the degree of superheat, the evaporation temperature detecting means (53) detects the saturation temperature equivalent to the evaporation pressure, and the capacity control means (56) changes the capacity of the compressor (1) to the saturation temperature equivalent to the evaporation pressure. Is controlled to reach a predetermined target value, and thereafter, when the capacity detection means (54) detects the maximum capacity operation of the compressor (1) and the saturation temperature corresponding to the evaporation pressure becomes equal to or higher than a predetermined temperature, the maximum opening is reached. The degree regulating means (55) sets the maximum opening degree of the main pressure reducing valve (6) to a third maximum opening degree that is smaller than the second maximum opening degree. In the inventions of (), (5) and (6), the circuit connection is switched by the switching means (51), and the Tufts operation, cold storage heat operation, cold storage heat recovery operation, normal cooling and cold storage heat simultaneous operation is performed.

そして、通常冷房及び蓄冷熱同時運転時には、最大開度
設定手段(52)の作動によって主減圧弁(6)の最大開
度を通常冷房運転時に設定される第1最大開度より小さ
い所定の第2最大開度に設定して、蒸発圧力相当飽和温
度の上昇を抑制し、蓄冷熱用減圧機構(14)内での冷媒
の温度と水の凍結温度との差が十分にとれるようにし、
製氷量の低下を防ぐ。また、上記容量検出手段(54)が
圧縮機(1)の最大容量運転を検出し、且つ上記蒸発温
度検出手段(53)が検出した蒸発圧力相当飽和温度が予
め設定された設定温度以上になると、最大開度規制手段
(55)の作動によって主減圧弁(6)の最大開度を第2
最大開度より小さい所定の第3最大開度に設定して、冷
房負荷の増大に伴う蒸発圧力相当飽和温度の上昇を抑制
し、十分な製氷量が得られるように制御する。このよう
に、主減圧弁(6)の開度調整によって冷房負荷を可変
とし、蒸発圧力相当飽和温度を常に最適な状態に制御
し、冷房負荷の大小に起因する不具合が解消される。
Then, during the normal cooling and cold storage heat simultaneous operation, the maximum opening degree setting means (52) operates to make the maximum opening degree of the main pressure reducing valve (6) smaller than the first maximum opening degree set during the normal cooling operation. 2 The maximum opening is set to suppress the increase in the saturation temperature equivalent to the evaporation pressure, so that the difference between the temperature of the refrigerant and the freezing temperature of water in the cold storage heat decompression mechanism (14) can be sufficiently taken.
Prevent a decrease in the amount of ice making. When the capacity detecting means (54) detects the maximum capacity operation of the compressor (1) and the evaporation pressure equivalent saturation temperature detected by the evaporation temperature detecting means (53) becomes equal to or higher than a preset temperature. The maximum opening degree of the main pressure reducing valve (6) is set to the second value by the operation of the maximum opening degree regulating means (55).
By setting a predetermined third maximum opening smaller than the maximum opening, an increase in the evaporation pressure equivalent saturation temperature due to an increase in cooling load is suppressed, and control is performed so that a sufficient amount of ice making is obtained. In this way, the cooling load is made variable by adjusting the opening degree of the main pressure reducing valve (6), the evaporative pressure equivalent saturation temperature is always controlled to the optimum state, and the problems caused by the magnitude of the cooling load are eliminated.

また、請求項(2),(3),(5)及び(6)の発明
では、通常冷房及び蓄冷熱同時運転時に、蒸発温度検出
手段(53)が蒸発圧力相当飽和温度を検出し、該蒸発温
度検出手段(53)の出力信号を受けて蒸発圧力相当飽和
温度が予め設定された目標値になるように容量制御手段
(56)が圧縮機(1)の容量を制御する。このことによ
り、蒸発圧力相当飽和温度の上下動を抑制し、該蒸発圧
力相当飽和温度の高低に起因する不具合が解消される。
Further, in the inventions of claims (2), (3), (5) and (6), the evaporation temperature detecting means (53) detects the saturation temperature equivalent to the evaporation pressure during the normal cooling and cold storage heat simultaneous operation, Upon receiving the output signal of the evaporation temperature detecting means (53), the capacity control means (56) controls the capacity of the compressor (1) so that the saturation temperature equivalent to the evaporation pressure becomes a preset target value. As a result, the vertical movement of the saturation temperature equivalent to the evaporation pressure is suppressed, and the problem caused by the elevation of the saturation temperature equivalent to the evaporation pressure is eliminated.

更に、請求項(4),(5)及び(6)の発明では、蓄
冷熱運転時に、蓄冷熱時間設定手段(61)が蓄冷熱運転
時間を設定し、製氷量検出手段(62)が蓄熱槽(11)内
での必要製氷量を検出し、上記蓄冷熱時間設定手段(6
1)および製氷量検出手段(62)からの出力信号が、演
算手段(63)に送られ、該演算手段(63)によって必要
製氷量を設定時間で製氷するのに要する圧縮機(1)の
最低運転周波数を算出した後、演算手段(63)からの出
力信号が運転制御手段(64)に送られ、該運転制御手段
(64)によって上記演算手段(63)で算出された圧縮機
運転周波数に基づき圧縮機(1)の運転を制御する。こ
れにより、蓄冷熱運転可能な時間を最大限に使うこと
で、運転周波数の低い、即ち、成績係数の高い領域で圧
縮機を駆動させることができ、消費電力の低減に伴ない
省エネ性が向上する。
Further, in the inventions of claims (4), (5) and (6), during the cold storage heat operation, the cold storage heat time setting means (61) sets the cold storage heat operation time, and the ice making amount detection means (62) stores the heat storage. The required amount of ice making in the tank (11) is detected, and the cool storage heat time setting means (6
1) and the output signals from the ice making amount detecting means (62) are sent to the calculating means (63), and the calculating means (63) causes the compressor (1) required to make the required ice making amount in a set time. After calculating the minimum operating frequency, the output signal from the calculating means (63) is sent to the operation controlling means (64), and the compressor operating frequency calculated by the calculating means (63) by the operating controlling means (64). The operation of the compressor (1) is controlled based on the above. This makes it possible to drive the compressor in a region where the operating frequency is low, that is, where the coefficient of performance is high, by maximizing the use of the cool storage heat operation time, which improves energy efficiency with a reduction in power consumption. To do.

(実施例) 以下、本発明の実施例について、第4図以下の図面に基
づき説明する。
(Embodiment) An embodiment of the present invention will be described below with reference to the drawings starting from FIG.

第4図は本実施例に係る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),(B),…が接続された所謂マルチ形空気調和
装置である。
FIG. 4 shows the overall configuration of the air conditioner according to the present embodiment, a so-called multi-type air conditioner in which a plurality of indoor units (A), (B), ... Are connected to the outdoor unit (X). Is.

上記室外ユニット(X)において、(1)は圧縮機、
(2)は冷房運転時には図中実線のごとく切換わり、暖
房運転時には図中破線のごとく切換わる四路切換弁、
(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熱交換器としての室外熱交
換器、(4)は冷房運転時には冷媒流量を調節し、暖房
運転時には冷媒を減圧する減圧機構として機能する室外
電動膨張弁、(5)は凝縮された液冷媒を貯溜するため
のレシーバ、(8)は吸入冷媒中の液成分を除去するた
めのアキュムレータである。
In the outdoor unit (X), (1) is a compressor,
(2) is a four-way switching valve that switches during cooling operation as shown by the solid line in the figure, and during heating operation as shown by the broken line in the figure,
(3) is an outdoor heat exchanger as a heat source side heat exchanger that functions as a condenser during cooling operation and as an evaporator during heating operation, and (4) adjusts the refrigerant flow rate during cooling operation and reduces the refrigerant during heating operation. An outdoor electric expansion valve functioning as a pressure reducing mechanism, (5) is a receiver for storing the condensed liquid refrigerant, and (8) is an accumulator for removing the liquid component in the suction refrigerant.

一方、各室内ユニット(A),(B),…は同一構成を
有し、(6)は冷房運転時には減圧機構として機能し、
暖房運転時には冷媒流量を調節する主減圧弁としての室
内電動膨張弁、(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, the indoor units (A), (B), ... Have the same configuration, and (6) functions as a pressure reducing mechanism during the cooling operation,
An indoor electric expansion valve as a main pressure reducing valve for adjusting the refrigerant flow rate during heating operation, and (7) as an evaporator during cooling operation,
It is an indoor heat exchanger as a utilization side heat exchanger that functions as a condenser during heating operation.

そして、上記各機器(1)〜(8)は冷媒配管(9)に
より冷媒の流通可能に順次接続されていて、室外空気と
の熱交換により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(10)が構成されている。
The above-mentioned devices (1) to (8) are sequentially connected to each other through a refrigerant pipe (9) so that the refrigerant can flow therethrough, and have a heat pump action of releasing the heat obtained by heat exchange with the outdoor air to the indoor air. A main refrigerant circuit (10) is configured.

また、装置には上記主冷媒回路(10)を流れる冷媒との
熱交換により蓄冷熱、蓄暖熱を、或いはその蓄冷熱、蓄
暖熱の利用をするための蓄熱ユニット(Y)が配置され
ている。該蓄熱ユニット(Y)において、(11)は冷熱
及び暖熱の蓄熱可能な蓄熱媒体たる水(W)を貯溜した
蓄熱槽、(12)は該蓄熱槽(11)内に配置され、水
(W)と冷媒との熱交換を行うための蓄熱熱交換器であ
って、該蓄熱熱交換器(12)と主冷媒回路(10)の上記
室外電動膨張弁(4)−室内電動膨張弁(6)間の液ラ
イン(9a)との間は、第1バイパス路(13a)及び第2
バイパス路(13b)により、室内電動膨張弁(6)側か
ら順に冷媒の流通可能に接続されている。そして、上記
第1バイパス路(13a)には、水(W)に冷熱を蓄える
ときに冷媒を減圧する蓄冷熱用減圧機構としての蓄熱電
動膨張弁(14)が介設され、上記第2バイパス路(13
b)には、第2バイパス路(13b)を開閉する第1開閉弁
(15)が介設されている。
Further, in the device, a heat storage unit (Y) for arranging cold heat storage, heat storage heat, or use of the cold heat storage, heat storage heat by heat exchange with the refrigerant flowing in the main refrigerant circuit (10) is arranged. ing. In the heat storage unit (Y), (11) is a heat storage tank that stores water (W), which is a heat storage medium capable of storing cold heat and warm heat, and (12) is arranged in the heat storage tank (11). W) is a heat storage heat exchanger for exchanging heat with the refrigerant, wherein the heat storage heat exchanger (12) and the outdoor electric expansion valve (4) of the main refrigerant circuit (10) -indoor electric expansion valve ( Between the liquid line (9a) between 6), the first bypass passage (13a) and the second bypass passage (13a)
The bypass passage (13b) is connected to the indoor electric expansion valve (6) so that the refrigerant can flow sequentially from the side. The first bypass path (13a) is provided with a heat storage electric expansion valve (14) as a cold storage heat reducing mechanism that reduces the pressure of the refrigerant when cold water is stored in the water (W). Road (13
In b), a first opening / closing valve (15) for opening / closing the second bypass passage (13b) is provided.

また、第2バイパス路(13b)の上記第1開閉弁(15)
−蓄熱熱交換器(12)間の途中配管と主冷媒回路(10)
のガスライン(9b)とは第3バイパス路(13c)によ
り、冷媒の流通可能に接続されていて、該第3バイパス
路(13c)には、バイパス路(13c)を開閉する第2開閉
弁(16)が介設されている。
Further, the first on-off valve (15) of the second bypass passage (13b)
− Intermediate piping between the heat storage heat exchanger (12) and the main refrigerant circuit (10)
Is connected to the gas line (9b) by a third bypass passage (13c) so that the refrigerant can flow therethrough, and the third bypass passage (13c) is provided with a second opening / closing valve for opening and closing the bypass passage (13c). (16) is installed.

一方、主冷媒回路(10)の液ライン(9a)の上記第1,第
2バイパス路(13a),(13b)との2つの接合部間に
は、冷媒の流量を可変に調節するための流量制御弁(1
7)が介設されている。即ち、各運転状態に応じて回路
接続を切換える切換手段(51)が上記第1開閉弁(1
5),第2開閉弁(16),流量制御弁(17)によって構
成されている。
On the other hand, between the two joints between the liquid line (9a) of the main refrigerant circuit (10) and the first and second bypass passages (13a) and (13b), the flow rate of the refrigerant is variably adjusted. Flow control valve (1
7) is installed. That is, the switching means (51) for switching the circuit connection according to each operating state is the first opening / closing valve (1).
5), the second on-off valve (16), and the flow control valve (17).

また、この蓄熱式空気調和装置にはセンサ類が配置され
ていて、(Thw)は上記蓄熱槽(11)の水中に配置さ
れ、水温Twを検出することで蓄熱槽(11)内の残氷の有
無を検知する水温センサ、(Tha)は室外熱交換器
(3)の空気吸込口に配置され、外気温度Taを検出する
外気温センサ、(Thi)は液ライン(9a)の第2バイパ
ス路(13b)との接合部の冷房運転時における上流側に
配置された冷却入口センサ、(Tho)は液ライン(9a)
の第1バイパス路(13a)との接合部の冷房運転時にお
ける下流側に配置された冷却出口センサ、(Ths)は吸
入ライン(9d)に配置され、吸入管温度を検出するため
の吸入管センサ、(Sp)はガスライン(9b)に配置さ
れ、暖房サイクル時には高圧Tc、冷房サイクル時には低
圧(吸入圧力)を検出する圧力センサ、(Cl)は蓄熱槽
(11)内の水位を検出することで、該蓄熱槽(11)内の
残氷量を検知する水位センサである。そして、これらセ
ンサで検出された信号は第1及び第2コントローラ
(C1),(C2)に送られる。
Further, sensors are arranged in this heat storage type air conditioner, (Thw) is arranged in the water of the heat storage tank (11), and residual ice in the heat storage tank (11) is detected by detecting the water temperature Tw. A water temperature sensor that detects the presence or absence of air, (Tha) is arranged at the air inlet of the outdoor heat exchanger (3), and an outside air temperature sensor that detects the outside air temperature Ta, and (Thi) is the second bypass of the liquid line (9a). The cooling inlet sensor (Tho) arranged on the upstream side during the cooling operation of the joint portion with the passage (13b) is the liquid line (9a).
The cooling outlet sensor (Ths) is arranged in the suction line (9d) on the downstream side during the cooling operation of the joint with the first bypass passage (13a) of the suction pipe for detecting the temperature of the suction pipe. A sensor, (Sp) is arranged in the gas line (9b), a pressure sensor that detects high pressure Tc during a heating cycle and a low pressure (suction pressure) during a cooling cycle, and (Cl) detects the water level in the heat storage tank (11). This is a water level sensor that detects the amount of residual ice in the heat storage tank (11). Then, the signals detected by these sensors are sent to the first and second controllers (C 1 ) and (C 2 ).

次に、この2つのコントローラ(C1),(C2)について
述べる。
Next, these two controllers (C 1 ) and (C 2 ) will be described.

第1コントローラ(C1)には、運転状態が通常冷房およ
び蓄冷熱同時運転を時に、室内電動膨張弁(6)最大開
度を小さく設定する最大開度設定手段(52)、圧力セン
サ(SP)の検知信号より蒸発圧力相当飽和温度Teを検出
する蒸発温度検出手段(53)、圧縮機(1)の最大容量
運転を検出する容量検出手段(54)、上記蒸発温度検出
手段(53)と容量検出手段(54)からの信号を受けて、
室内電動膨張弁(6)最大開度を設定する最大開度規制
手段(55)、蒸発温度検出手段(53)からの信号を受け
て圧縮機(1)の容量を制御する容量制御手段(56)と
を備えている。
The first controller (C 1 ) has a maximum opening setting means (52) for setting the maximum opening of the indoor electric expansion valve (6) to a small value, and a pressure sensor (SP) when the operating states are normal cooling and cold storage simultaneous operation. ), The evaporation temperature detecting means (53) for detecting the saturation temperature Te corresponding to the evaporation pressure, the capacity detecting means (54) for detecting the maximum capacity operation of the compressor (1), and the evaporation temperature detecting means (53). Upon receiving the signal from the capacitance detecting means (54),
Capacity control means (56) for controlling the capacity of the compressor (1) in response to signals from the maximum opening regulating means (55) for setting the maximum opening of the indoor electric expansion valve (6) and the evaporation temperature detecting means (53). ) And.

一方、第2コントローラ(C2)には、蓄冷熱運転時間を
設定する蓄冷熱時間設定手段(61)、水位センサ(Cl)
から検知信号が送られて、蓄熱槽(11)内での必要製氷
量を検出する製氷量検出手段(62)、上記蓄冷熱時間設
定手段(61)および製氷量検出手段(62)からの出力信
号を受けて、該必要製氷量を設定時間で製氷するのに要
する圧縮機(1)の最低運転周波数を算出する演算手段
(63)と、演算手段(63)からの出力信号を受け、該演
算手段(63)で算出された圧縮機運転周波数に基づき圧
縮機(1)の運転を制御する運転制御手段(64)と備え
ている。
On the other hand, the second controller (C 2 ) has a cold storage heat time setting means (61) for setting a cold storage heat operation time, and a water level sensor (Cl).
Output from the ice storage amount detection means (62) for detecting the required ice production amount in the heat storage tank (11), the cold storage heat time setting means (61) and the ice production amount detection means (62). Receiving a signal and receiving an output signal from a calculating means (63) for calculating a minimum operating frequency of the compressor (1) required to make the required ice making amount in a set time, and an output signal from the calculating means (63), The operation control means (64) controls the operation of the compressor (1) based on the compressor operation frequency calculated by the calculation means (63).

次に、この蓄熱式空気調和装置の各運転モードにおける
各弁の開閉(もしくは開度調節)と、冷媒の循環経路に
ついて、第5図〜第12図に基づき説明する。
Next, the opening / closing (or opening adjustment) of each valve and the circulation path of the refrigerant in each operation mode of this heat storage type air conditioner will be described based on FIGS. 5 to 12.

通常冷房運転時には、第5図矢印に示すように、四路切
換弁(2)が図中実線のように切換わり、室外電動膨張
弁(4)、流量制御弁(17)、室内電動膨張弁(6),
…が開き、他の弁はいずれも閉じた状態で運転が行わ
れ、室外熱交換器(3)で凝縮された冷媒が主冷媒回路
(10)のみを循環し、各室内電動膨張弁(6),…で減
圧され、各室内熱交換器(7),…で蒸発して圧縮機
(1)に戻る。
During normal cooling operation, as shown by the arrow in FIG. 5, the four-way switching valve (2) is switched as shown by the solid line in the figure, and the outdoor electric expansion valve (4), flow control valve (17), indoor electric expansion valve (6),
... is opened and all the other valves are operated in a closed state, the refrigerant condensed in the outdoor heat exchanger (3) circulates only in the main refrigerant circuit (10), and each indoor electric expansion valve (6 ), ... Decompresses, and each indoor heat exchanger (7) evaporates and returns to the compressor (1).

蓄冷熱運転には、第6図矢印に示すように、室外電動膨
張弁(4)、流量制御弁(17)、蓄熱電動膨張弁(14)
及び第2開閉弁(16)が開き、室内電動膨張弁(6),
…及び第1開閉弁(15)が閉じた状態で運転が行われ、
室外熱交換器(3)で凝縮された液冷媒が、第1バイパ
ス路(13a)にバイパスして流れ、蓄熱電動膨張弁(1
4)で減圧され、蓄熱熱交換器(12)で蒸発して圧縮機
(1)に戻るように循環する。そのとき、蓄熱熱交換器
(12)で冷媒との熱交換により、蓄熱媒体たる水(W)
を製氷し、冷熱を蓄える。
In the cold storage operation, as shown by the arrow in FIG. 6, the outdoor electric expansion valve (4), the flow control valve (17), the heat storage electric expansion valve (14).
And the second on-off valve (16) opens, and the indoor electric expansion valve (6),
... and operation is performed with the first on-off valve (15) closed,
The liquid refrigerant condensed in the outdoor heat exchanger (3) flows by bypassing the first bypass passage (13a), and the heat storage electric expansion valve (1
It is decompressed in 4), evaporated in the heat storage heat exchanger (12) and circulated back to the compressor (1). At that time, water (W) as a heat storage medium is generated by heat exchange with the refrigerant in the heat storage heat exchanger (12).
Make ice and store cold heat.

通常冷房及び蓄冷熱同時運転時には、第7図矢印に示す
ように、室外電動膨張弁(4)、流量制御弁(17)、室
内電動膨張弁(6),…、蓄熱電動膨張弁(14)及び第
2開閉弁(16)が開き、第1開閉弁(15)が閉じて、室
外熱交換器(3)で凝縮された液冷媒の一部が、主冷媒
回路(10)を流れ、室内電動膨張弁(6),…で減圧さ
れて室内熱交換器(7),…で蒸発する一方、液冷媒の
残部が第1バイパス路(13a)側に流れ、蓄熱電動膨張
弁(14)で減圧されて蓄熱熱交換器(12)で蒸発する。
そして、これらのガス状態となった冷媒がそれぞれガス
ライン(9b)で合流した圧縮機(1)に戻るように循環
する。
During the normal cooling and cold storage heat simultaneous operation, as shown by the arrow in FIG. 7, the outdoor electric expansion valve (4), the flow control valve (17), the indoor electric expansion valve (6), ..., The heat storage electric expansion valve (14) And the second opening / closing valve (16) is opened, the first opening / closing valve (15) is closed, and a part of the liquid refrigerant condensed in the outdoor heat exchanger (3) flows through the main refrigerant circuit (10), While being decompressed by the electric expansion valves (6), ..., Evaporated by the indoor heat exchangers (7), ..., the remaining part of the liquid refrigerant flows to the first bypass passage (13a) side, and the heat storage electric expansion valve (14) It is decompressed and evaporated in the heat storage heat exchanger (12).
Then, these refrigerants in the gas state are circulated so as to return to the compressor (1) which merges in the gas line (9b).

上記蓄冷熱運転で蓄えた冷熱を利用する蓄冷熱回収運転
時には、第8時矢印に示すように、室外電動膨張弁
(4)、流量制御弁(17)、室内電動膨張弁(6),
…、蓄熱電動膨張弁(14)及び第1開閉弁(15)が開
き、第2開閉弁(16)が閉じた状態で運転が行われ、室
外熱交換器(3)で凝縮された液冷媒の一部が主冷媒回
路(10)から第2バイパス路(13b)側にバイパスして
流れ、蓄熱熱交換器(12)で水(W)(又は氷)との熱
交換により過冷却されて第1バイパス路(13a)から主
冷媒回路(10)に戻る一方、液冷媒の残部は流量制御弁
(17)を経てそのまま主冷媒回路(10)の液ライン(9
a)を流れる。そして、合流後、各室内電動膨張弁
(6),…で減圧され、各室内熱交換器(7),…で蒸
発したのち圧縮機(1)に戻るように循環する。そのと
き、流量制御弁(17)と蓄熱電動膨張弁(14)の相対的
な開度調節により、冷媒の分流量が調節され、冷却入口
センサ(Thi),冷却出口センサ(Tho)で検出される液
冷媒温度Tl1,Tl2の差温ΔTlとしての冷媒の過冷却度が
適切に調節される。
During the cold storage heat recovery operation using the cold heat stored in the cold storage heat operation, as shown by the arrow at the 8th hour, the outdoor electric expansion valve (4), the flow control valve (17), the indoor electric expansion valve (6),
The liquid refrigerant condensed in the outdoor heat exchanger (3) is operated with the heat storage electric expansion valve (14) and the first opening / closing valve (15) open and the second opening / closing valve (16) closed. Part of the refrigerant flows from the main refrigerant circuit (10) to the second bypass passage (13b) side, and is supercooled by heat exchange with water (W) (or ice) in the heat storage heat exchanger (12). While returning from the first bypass path (13a) to the main refrigerant circuit (10), the rest of the liquid refrigerant passes through the flow rate control valve (17) and remains in the liquid line (9) of the main refrigerant circuit (10).
flow through a). Then, after merging, the pressure is reduced by the indoor electric expansion valves (6), ..., Evaporated by the indoor heat exchangers (7), and then circulated so as to return to the compressor (1). At that time, the partial flow rate of the refrigerant is adjusted by adjusting the relative opening of the flow control valve (17) and the heat storage electric expansion valve (14), and is detected by the cooling inlet sensor (Thi) and the cooling outlet sensor (Tho). The subcooling degree of the refrigerant as the temperature difference ΔTl between the liquid refrigerant temperatures Tl1 and Tl2 is appropriately adjusted.

次に、通常暖房運転においては、第9図矢印に示すよう
に、四路切換弁(2)が図中破線側に切換わり、各室内
電動膨張弁(6),…、流量制御弁(17)、室外電動膨
張弁(4)が開き、他の弁がいずれも閉じた状態で運転
が行われ、吐出ガスが各室内熱交換器(7),…で凝縮
され、室外電動膨張弁(4)で減圧されて室外熱交換器
(3)で蒸発したのち圧縮機(1)に戻るように循環す
る。
Next, in the normal heating operation, as shown by the arrow in FIG. 9, the four-way switching valve (2) is switched to the broken line side in the figure, and each indoor electric expansion valve (6), ..., Flow control valve (17). ), The outdoor electric expansion valve (4) is opened, and the operation is performed with all the other valves closed, and the discharge gas is condensed in the indoor heat exchangers (7), ... ), Is decompressed, evaporated in the outdoor heat exchanger (3), and then circulated so as to return to the compressor (1).

蓄暖熱運転時には、第10図矢印に示すように、第2開閉
弁(16)、蓄熱電動膨張弁(14)、流量制御弁(17)、
室外電動膨張弁(4)が開き、各室内電動膨張弁
(6),…、第1開閉弁(15)が閉じた状態で運転が行
われ、吐出ガスが主冷媒回路(10)から第3バイパス路
(13c)にバイパスして流れて、蓄熱熱交換器(12)で
凝縮された後、第1バイパス路(13a)から主冷媒回路
(10)に流れ、室外電動膨張弁(4)で減圧されて室外
熱交換器(3)で蒸発したのち圧縮機(1)に戻るよう
に循環する。そのとき、蓄熱熱交換器(12)で冷媒との
熱交換により、蓄熱槽(11)内の水(W)が暖められ、
暖熱が蓄えられる。
During the warm storage operation, as shown by the arrow in FIG. 10, the second opening / closing valve (16), the heat storage electric expansion valve (14), the flow control valve (17),
The outdoor electric expansion valve (4) is opened, the indoor electric expansion valves (6), ..., And the first opening / closing valve (15) are closed, and the operation is performed with the discharge gas from the main refrigerant circuit (10) to the third. After bypassing to the bypass passage (13c) and being condensed in the heat storage heat exchanger (12), it flows from the first bypass passage (13a) to the main refrigerant circuit (10) and then at the outdoor electric expansion valve (4). After being decompressed and evaporated in the outdoor heat exchanger (3), it is circulated so as to return to the compressor (1). At that time, the water (W) in the heat storage tank (11) is warmed by heat exchange with the refrigerant in the heat storage heat exchanger (12),
Warm heat is stored.

通常暖房及び蓄暖熱同時運転時には、第11図矢印に示す
ように、各室内電動膨張弁(6),…、第2開閉弁(1
6)、蓄熱電動膨張弁(14)、流量制御弁(17)、室外
電動膨張弁(4)が開き、第1開閉弁(15)が閉じた状
態で運転が行われ、吐出ガスの一部が主冷媒回路(10)
から第3バイパス路(13c)側にバイパスして流れ、蓄
熱熱交換器(12)で凝縮される一方、吐出ガスの残部が
主冷媒回路(10)側を流れて各室内熱交換器(7),…
で凝縮される。そして、両者が合流後、室外電動膨張弁
(4)で減圧され、室外熱交換器(3)で蒸発したのち
圧縮機(1)に戻るように循環する。
At the time of simultaneous normal heating and storage heat simultaneous operation, as shown by the arrow in FIG. 11, each indoor electric expansion valve (6), ..., The second opening / closing valve (1
6), the heat storage electric expansion valve (14), the flow control valve (17), the outdoor electric expansion valve (4) are opened and the first opening / closing valve (15) is closed, and the operation is performed, and a part of the discharged gas is discharged. Is the main refrigerant circuit (10)
To the third bypass passage (13c) side, and is condensed in the heat storage heat exchanger (12), while the rest of the discharge gas flows to the main refrigerant circuit (10) side to reach each indoor heat exchanger (7). ), ...
Is condensed in. Then, after both merge, they are decompressed by the outdoor electric expansion valve (4), evaporated in the outdoor heat exchanger (3), and then circulated so as to return to the compressor (1).

さらに、蓄暖熱回収デフロスト運転時には、第12図矢印
に示すように、四路切換弁(2)が図中実線側に切換わ
り、室外電動膨張弁(4)、流量制御弁(17)、各室内
電動膨張弁(6),…、蓄熱電動膨張弁(14)、第2開
閉弁(16)が開き、第1開閉弁(15)が閉じた状態で運
転が行われ、吐出ガスが室外熱交換器(3)で凝縮さ
れ、凝縮された液冷媒の一部が主冷媒回路(10)から第
1バイパス路(13a)側にバイパスして流れて、蓄熱電
動膨張弁(14)で減圧され、蓄熱熱交換器(12)で蒸発
する一方、液冷媒の残部が主冷媒回路(10)の各室内電
動膨張弁(6),…で減圧され、各室内熱交換器
(7),…で蒸発する。そして、それぞれガスライン
(9b)で合流して圧縮機(1)に戻るように循環する。
そのとき、吐出ガス(ホットガス)により、室外熱交換
器(3)の除霜を行うとともに、蓄熱槽(11)の蓄暖熱
を利用して室外熱交換器(3)における凝縮能力を増大
せしめ、デフロスト運転時間を短縮するようになされて
いる。
Further, during the storage heat recovery defrost operation, as shown by the arrow in FIG. 12, the four-way switching valve (2) is switched to the solid line side in the figure, and the outdoor electric expansion valve (4), the flow control valve (17), The indoor electric expansion valves (6), ..., The heat storage electric expansion valve (14), the second opening / closing valve (16) are opened, the operation is performed with the first opening / closing valve (15) closed, and the discharge gas is discharged outdoors. Part of the liquid refrigerant condensed in the heat exchanger (3) bypasses from the main refrigerant circuit (10) to the first bypass passage (13a) side, and is decompressed by the heat storage electric expansion valve (14). While being evaporated in the heat storage heat exchanger (12), the remaining portion of the liquid refrigerant is decompressed by the indoor electric expansion valves (6), ... Of the main refrigerant circuit (10), and the indoor heat exchangers (7) ,. Evaporates at. Then, they are circulated so as to join each other in the gas line (9b) and return to the compressor (1).
At that time, the discharge gas (hot gas) defrosts the outdoor heat exchanger (3) and increases the condensation capacity of the outdoor heat exchanger (3) by utilizing the stored heat of the heat storage tank (11). It is designed to shorten the defrost operation time.

そして、本発明が特徴とする所は、上述した蓄冷熱運転
時と、通常冷房及び蓄冷熱同時運転時とにおける運転制
御に係る。以下、この運転制御について各々フローチャ
ートに沿って説明する。尚、第13図は本装置の蓄冷熱運
転時(通常冷房との同時運転を含む)における制御内容
を示すフローチャート、第14図は蓄冷熱運転が単独で行
われている時の制御内容の詳細を示すフローチャートで
ある。
The feature of the present invention relates to the operation control during the cold storage heat operation described above and the normal cooling and cold storage heat simultaneous operation. The operation control will be described below with reference to each flowchart. Incidentally, FIG. 13 is a flowchart showing the control contents during the cold storage heat operation of this device (including simultaneous operation with normal cooling), and FIG. 14 is the details of the control contents when the cold storage heat operation is performed independently. It is a flowchart showing.

先ず、第13図のフローチャートに示すように、装置の運
転モードが蓄冷熱運転に切換えられると、スタートして
イニシャライズされた後、ステップS1で室内ユニットが
サーモオンしているか否かが判定される。即ち、室内ユ
ニットがサーモオフしていれば蓄冷熱運転が単独で行わ
れていることになり、サーモオンしておれば通常冷房及
び蓄冷熱同時運転が行われていることになる。そして、
このステップS1で室内ユニットがサーモオンしている
と、通常冷房及び蓄冷熱同時運転状態が開始され、ステ
ップS2以下の制御に移り、一方、室内ユニットがサーモ
オフしていると、蓄冷熱の単独運転状態が開始され、ス
テップS10以下の制御に移る。
First, as shown in the flow chart of FIG. 13, when the operation mode of the device is switched to the cold storage operation, after starting and initializing, it is determined in step S 1 whether or not the indoor unit is thermo-on. . That is, if the indoor unit is thermo-off, the cold heat storage operation is performed independently, and if the indoor unit is thermo-on, normal cooling and cold heat storage simultaneous operation are performed. And
If the indoor unit is thermo-ON in this step S 1 , the normal cooling and cold storage heat simultaneous operation state is started, and the control proceeds to step S 2 and subsequent steps, while if the indoor unit is thermo-OFF, the cold storage heat is independently operation state is started, the process proceeds to the control of step S 10 follows.

そこで、先ず、ステップS10以下の蓄冷熱運転時につい
て説明する。ステップS1で室内ユニットがサーモオンし
ていないことが検知された後、ステップS10で、第1タ
イマがセットされ、その後、ステップS11に移り、蓄冷
熱運転時における圧縮機の運転周波数Fk′が算出された
後、ステップS6に移り、室内ユニットのサーモオフ状態
が変更したか否かが判定される。そして、該室内ユニッ
トが継続してサーモオフしている場合にはステップS7
移り、室内ユニットがサーモオンか否かが判定され、サ
ーモオフしてる場合にはステップS9に移り、上記ステッ
プS10でセットした第1タイマがタイムアップしたか否
かが判定され、タイムアップするまでステップS6に戻
り、上述の動作が繰返される。その後、第1タイマがタ
イムアップすると、ステップS9よりステップS10に移
り、上述の動作が繰返される。つまり、室内ユニットが
サーモオフ状態の場合に蓄冷熱運転が行われると同時に
第1タイマのタイムアップ毎に圧縮機(1)の運転周波
数が演算される。そこで、上記蓄冷熱運転時における圧
縮機(1)の運転周波数の演算処理(ステップS11)に
ついて第14図に示すフローチャートに基づき説明する。
Therefore, first described during cold storage heat operation step S 10 follows. After the indoor unit in Step S 1 is that is not thermo sensed, in step S 10, the first timer is set, then the routine goes to Step S 11, the operating frequency Fk of the compressor during cold storage heat operation ' after There is calculated, the flow proceeds to step S 6, whether or not changes the thermo-off state of the indoor unit is determined. Then, the flow proceeds to step S 7 in the case where the indoor unit is thermo-off continues, the indoor unit is determined whether or not thermo-on, if you are thermo-off proceeds to step S 9, in step S 10 set the first timer is determined whether the time is up, the process returns to the step S 6 until the time is up, the above-described operation is repeated. After that, when the first timer times out, the process moves from step S 9 to step S 10 , and the above-described operation is repeated. That is, when the indoor unit is in the thermo-off state, the cold heat storage operation is performed, and at the same time, the operating frequency of the compressor (1) is calculated every time the first timer times up. Accordingly, it will be described with reference to the flowchart shown in FIG. 14 for processing (step S 11) of the operating frequency of the compressor (1) during the cold storage heat operation.

このフローチャートに示す如く、先ず、ステップS21
蓄冷熱運転終了時に得るべき蓄冷熱量、即ち目標蓄冷熱
量(IPFs)を設定する。ここで設定される目標蓄冷熱量
(IPFs)は、日中の外気温度等に応じて設定されると共
に、蓄熱槽(11)に氷が残留している場合には、その残
氷量をも含んでいるものであるため、実際に、蓄冷熱運
転時に生成される製氷量は、この残氷量を差引いた値に
なる。即ち、蓄熱槽(11)内に配設された水位センサ
(Cl)により残氷量を検出し、その検出信号が製氷量検
出手段(62)に送信されることで、上記目標蓄冷熱量
(IPFs)からこの残氷量を差引いて実際の製氷量を得る
ものである。尚、この目標蓄冷熱量(IPFs)は、蓄熱槽
(11)内における氷量の体積百分率で表される。
As shown in this flowchart, first, cold quantity to be obtained during cold storage heat operation ends in step S 21, that is, sets the target cold quantity (IPFS). The target amount of cold heat storage (IPFs) set here is set according to the outside air temperature during the day, and also includes the amount of remaining ice when ice remains in the heat storage tank (11). Therefore, the ice making amount actually generated during the cold storage heat operation is a value obtained by subtracting the remaining ice amount. That is, the water level sensor (Cl) arranged in the heat storage tank (11) detects the amount of remaining ice, and the detection signal is transmitted to the ice making amount detecting means (62), whereby the target amount of stored cold heat (IPFs) ) Is subtracted from the remaining ice amount to obtain the actual ice-making amount. The target amount of stored cold heat (IPFs) is represented by the volume percentage of the amount of ice in the heat storage tank (11).

次に、ステップS21で求められた目標蓄冷熱量(IPFs)
に基づきステップS22において圧縮機(1)の運転周波
数Fk′を決定する。ここでは、上記蓄冷熱時間設定手段
(61)によって、予め蓄冷熱運転時間を8hr等に設定し
ておいたり、若しくは蓄冷熱運転終了時間を設定してお
き、その時間までの時間数即ち、蓄冷熱運転残り時間を
算出するなどして求めておく。そして、上記蓄冷熱時間
設定手段(61)および製氷量検出手段(62)からの検出
信号が演算手段(63)に送信され、該演算手段(63)に
よって上記蓄冷熱時間設定手段(61)で設定された設定
時間で上記のステップS21で求められた目標蓄冷熱量(I
PFs)を得るのに要する圧縮機(1)の最低運転周波数F
k′が算出される。尚、この演算手段(63)での運転周
波数Fk′の算出には、以下の式により行われる。
Next, the target cold quantity obtained in step S 21 (IPFs)
Determining the operation frequency Fk 'of the compressor (1) in step S 22 based on. Here, the cool storage heat time setting means (61) has previously set the cool storage heat operation time to 8 hours or the like, or has set the cool storage heat operation end time, and the number of hours until that time, that is, the cool storage heat Calculate it by calculating the remaining time of thermal operation. Then, the detection signals from the cold storage heat time setting means (61) and the ice making amount detection means (62) are transmitted to the calculation means (63), and the calculation means (63) causes the cold storage heat time setting means (61) to set set time above the target cold quantity obtained in step S 21 (I
Minimum operating frequency F of compressor (1) required to obtain PFs)
k'is calculated. The operating frequency Fk 'is calculated by the calculating means (63) by the following equation.

Fk′=(c2/A)(IPFs−IPF)−c1 … c1:定数(=67) c2:定数(=18) IPFs:蓄冷熱運転終了時の蓄冷熱量 A=CTDF−C3 (CTDF:蓄冷熱運転残り時間(Hr)、 C3:定数(=0.5)) 但し、A≦0.2のときはA=0.2 また、ここで算出された運転周波数Fk′の制限として、
Fk′≦50(Hz)のときはFk′=50(Hz)として、圧縮機
(1)の固有振動数を回避する等、低周波数領域での不
具合を生ぜせしめないように設定し、一方、FK′≧117.
5(Hz)のときはFK′=135(Hz)として、製氷速度を速
める加速チャージ運転を行うように設定されている。以
上の如く演算手段(63)で算出された運転周波数Fk′に
基づき、演算手段(63)からの信号が運転制御手段(6
4)に送信され、該運転制御手段(64)の作動によって
圧縮機(1)の運転が制御され、蓄冷熱運転が開始され
る。
Fk ′ = (c 2 / A) (IPFs−IPF) −c 1 … c 1 : Constant (= 67) c 2 : Constant (= 18) IPFs: Cold storage heat quantity at the end of cold storage heat operation A = CTDF−C 3 (CTDF: cold storage heat operating time remaining (Hr), C 3: constant (= 0.5)) as a limit where, a = 0.2 also when a ≦ 0.2, where calculated the operating frequency Fk ',
When Fk '≤ 50 (Hz), set Fk' = 50 (Hz) so that the natural frequency of the compressor (1) is avoided and other problems are not caused in the low frequency range. FK ′ ≧ 117.
At 5 (Hz), FK 'is set to 135 (Hz), and it is set to perform the acceleration charge operation that accelerates the ice making speed. Based on the operating frequency Fk 'calculated by the calculating means (63) as described above, the signal from the calculating means (63) is changed to the operation control means (6).
4), the operation of the compressor (1) is controlled by the operation of the operation control means (64), and the cold storage operation is started.

次に、この運転周波数Fk′の補正手段としてのステップ
S23以下の制御について説明する。
Next, a step as a means for correcting this operating frequency Fk '
S 23 for the following control will be described.

ステップS23でタイマによって蓄冷熱運転残り時間が所
定時間間隔、つまりステップS10で設定される第1タイ
マの12分間隔でカウントされており、その所定時間を経
過すると、ステップS24で、そのカウント時間において
蓄熱槽(11)内に貯留されている蓄冷熱量がサンプリン
グされる。そして、再び上記式を用い、ステップS25
において、上記第1タイマで検出された時間により求め
られる蓄冷熱運転残り時間で上記のステップS21で求め
られた目標蓄冷熱量(IPFs)を得るべく残りの必要製氷
量を製氷するのに要する圧縮機(1)の最低運転周波数
Fk′が算出される。その後、ステップS26に移り、この
ステップS25で算出された運転周波数Fk′について、上
記ステップS22で設定された運転周波数Fk′と比較して
変更を要するか否かが判定され、変更を要する場合には
ステップS27に進んで圧縮機(1)の運転周波数Fk′を
変更制御し、その後、再びステップS23に戻されて上述
と同様の制御を行う。一方、ステップS26で前回算出し
た運転周波数Fk′の変更を要しない場合には、そのまま
の運転周波数Fk′でステップS23に戻る。つまり、上述
のようにステップS10で設定された第1タイマがタイム
アップする毎にステップS23〜S27の動作が行われ、12分
毎に上記の如く運転周波数の補正がなされることにな
り、最初にステップS21,S22で設定された圧縮機(1)
の初期運転周波数及びステップS25で設定された前回の
運転周波数は適宜、補正されて、蓄熱運転時に冷房運転
が行われたり、外気温度が変化した場合などの状況の変
化に追従して圧縮機(1)の運転周波数(ロード)を変
更する。従って、蓄冷熱運転終了時にはステップS21
設定された目標製氷量(IPFs)が確実に得られる。
Step S 23 the predetermined time interval is cold storage heat operating time remaining by timer, i.e. are counted in 12-minute intervals of the first timer is set in step S 10, after a lapse of the predetermined time, in step S 24, the The amount of cold storage heat stored in the heat storage tank (11) is sampled during the counting time. Then, using the above equation again, step S 25
In the compression required to ice and the remaining required ice quantity to obtain the first in cold storage heat operating time remaining to be determined by the detected time with the timer of step S 21 in the determined target cold quantity (IPFS) Minimum operating frequency of machine (1)
Fk 'is calculated. After that, the process proceeds to step S 26, 'for, set operation frequency Fk at step S 22' The step S 25 the operating frequency calculated in Fk whether requiring a change in comparison with is determined, the changes compressor proceeds to step S 27 a (1) operating frequency Fk 'of change control if necessary, then performs the same control as described above is returned to step S 23 again. On the other hand, 'if it does not require changes, as the operation frequency Fk' operating frequency Fk previously calculated in the step S 26 returns to step S 23 at. That is, the first timer operation in step S 23 to S 27 are performed for each time is up set at the step S 10 as described above, in the above as the correction of the operating frequency is made every 12 minutes Then, the compressor (1) first set in steps S 21 and S 22
The initial operating frequency and the previous operating frequency set in the step S 25 of appropriate, be corrected, or the cooling operation is performed during the thermal storage operation, the compressor following the change of situation, such as when the outside air temperature changes Change the operating frequency (load) in (1). Therefore, the target ice amount set in the step S 21 (IPFs) can be surely obtained at the time of cold storage heat operation end.

この各運転周波数Fk′における蓄冷熱所要時間と必要製
氷量の関係を第15図に示す。この図に基づいて、蓄冷熱
時間(縦軸)と残氷量(横軸)から求められた製氷量と
が決定すれば、圧縮機(1)の最低の運転周波数が定ま
るので、蓄冷熱運転時間の残り時間等より運転周波数を
算出する。
Fig. 15 shows the relationship between the required time for cold storage heat and the required ice-making amount at each operating frequency Fk '. If the cold storage heat time (vertical axis) and the ice making amount obtained from the remaining ice amount (horizontal axis) are determined based on this figure, the lowest operating frequency of the compressor (1) is determined, so the cold storage operation is performed. The operating frequency is calculated from the remaining time, etc.

このように、蓄冷熱の単独運転時の制御については、蓄
冷熱運転可能な時間を最大限に使って、できるだけ圧縮
機(1)の運転周波数が低い領域において運転を行い、
成績係数の高い運転状態を行い、消費電力の低下を図り
ながら製氷運転を行うものである。また、蓄冷熱運転時
の状況変化に対応し適宜、圧縮機(1)の運転周波数を
補正するために、正確な蓄冷熱量を得ることができる。
In this way, for the control of the cold storage heat in the independent operation, the operation is performed in the region where the operating frequency of the compressor (1) is as low as possible by using the maximum time during which the cold storage heat can be operated.
The ice-making operation is performed while operating with a high coefficient of performance and reducing the power consumption. Further, since the operating frequency of the compressor (1) is appropriately corrected according to the change in the situation during the cold storage heat operation, it is possible to obtain an accurate amount of cold storage heat.

次に、第13図におけるステップS1で室内ユニットがサー
モオンしていると判定された場合、即ち通常冷房及び蓄
冷熱同時運転の制御について述べる。
Next, when it is determined in step S 1 in FIG. 13 that the indoor unit is thermo-ON, that is, control of simultaneous normal cooling and cold storage heat operation will be described.

先ず、制御フローは示さないが、通常冷房及び蓄冷熱同
時運転が開始されると、その開始信号が最大開度設定手
段(52)に送信され、該最大開度設定手段(52)の作動
により、それまで通常冷房運転時には2000plsを最大開
度(第1最大開度)としていた室内電動膨張弁(6)の
最大開度(第2最大開度)を1250plsとするように設定
される。つまり、以下の条件が全て満たされると室内電
動膨張弁(6)の最大開度が第1最大開度の略半分の第
2最大開度に設定される。
First, although a control flow is not shown, when the normal cooling and cold storage heat simultaneous operation is started, the start signal is transmitted to the maximum opening setting means (52), and the maximum opening setting means (52) is operated. The maximum opening (second maximum opening) of the indoor electric expansion valve (6), which has been set to the maximum opening (first maximum opening) of 2000 pls during the normal cooling operation until then, is set to 1250 pls. That is, when all of the following conditions are satisfied, the maximum opening degree of the indoor electric expansion valve (6) is set to the second maximum opening degree that is approximately half the first maximum opening degree.

・通常冷房及び蓄冷熱同時運転モード ・蓄冷熱運転中 ・室内ユニットがサーモオン状態 これら上限をIN条件として室内電動膨張弁(6)の最大
開度が小さく設定され、冷媒の流量が抑制されること
で、蒸発圧力相当飽和温度Teが大幅に上昇することが抑
制され、蓄熱槽(11)内の水の凍結温度との温度差を十
分に取れるようにし、この蓄熱運転時に十分な蓄熱量が
得られるようにする。
・ Normal cooling and cold storage heat simultaneous operation mode ・ Cooling heat storage operation ・ Indoor unit is in thermo-ON state The maximum opening of the indoor electric expansion valve (6) is set small with these upper limits as IN conditions, and the flow rate of the refrigerant is suppressed. In this way, the saturation temperature Te equivalent to the evaporation pressure is prevented from rising significantly, and the temperature difference between the freezing temperature of the water in the heat storage tank (11) and the freezing temperature can be sufficiently secured to obtain a sufficient heat storage amount during this heat storage operation. To be able to

尚、以下の条件の何れかが成立すると室内電動膨張弁
(6)の最大開度は第1最大開度(2000plsの開度)に
戻される。
When any of the following conditions is satisfied, the maximum opening degree of the indoor electric expansion valve (6) is returned to the first maximum opening degree (2000 pls opening degree).

・蓄冷熱運転が解除 ・室内ユニットがサーモオフ状態 また、この通常冷房及び蓄冷熱同時運転においては、圧
縮機(1)の容量制御、つまり、運転周波数制御が行わ
れて蒸発圧力相当飽和温度Teの一定制御が行われる。以
下、この制御について説明する。
・ Cold heat storage operation is released ・ Indoor unit is in thermo-off state Also, in this normal cooling and cold heat storage simultaneous operation, the capacity control of the compressor (1), that is, the operating frequency control, is performed and the evaporating pressure equivalent saturation temperature Te Constant control is performed. Hereinafter, this control will be described.

先ず、第13図におけるステップS1で室内熱交換器(7)
がサーモオンされていると、ステップS2で、第2タイマ
がセットされ(例えば20sec)、その後、このセットさ
れた第2タイマがタイムアップするまでの所定時間中に
行われる通常冷房及び蓄冷熱同時の圧縮機運転制御とし
てのステップS3〜S5に移る。ステップS3において圧力セ
ンサ(SP)の検知信号が蒸発温度検出手段(53)に送ら
れると共に、この蒸発温度検出手段(53)によって、最
適な蒸発圧力相当飽和温度Tes(以下目標飽和温度とす
る)が次式に基づいて算出される。
First, in step S 1 in FIG. 13, the indoor heat exchanger (7)
If the thermostat is turned on, the second timer is set in step S 2 (for example, 20 seconds), and then the normal cooling and cold storage heat are performed simultaneously during the predetermined time until the set second timer expires. proceeds to step S 3 to S 5 as compressor operation control. In step S 3 with the detection signal of the pressure sensor (SP) is sent to the evaporation temperature detection means (53), by the evaporation temperature detection means (53), the optimum evaporation pressure corresponding saturation temperature Tes (hereinafter the target saturation temperature ) Is calculated based on the following equation.

Tes=−6−(FT−50)×0.025 … 次に、この目標飽和温度Tesを得るべく、ステップS4
おいて圧縮機の運転周波数の増減量ΔFkが算出される。
このステップS4における圧縮機の運転周波数の増減量Δ
Fkは次式によって算出される。
Tes = -6− (FT−50) × 0.025 ... Next, in order to obtain this target saturation temperature Tes, the increase / decrease amount ΔFk of the operating frequency of the compressor is calculated in step S 4 .
Increase / decrease in the operating frequency of the compressor in step S 4 Δ
Fk is calculated by the following equation.

ΔFk=Kc[{e(t)−e(t−Δtc)} +Δtc/2Ti{e(t)+e(t−tc)}] … e(t):Te(t)−Tes(t) Δtc:サンプリングタイム Kc:ゲイン Ti:積分時間 そして、ステップS5において圧縮機の運転周波数の増減
量が加減算されて圧縮機の運転周波数Fkが決定される。
ΔFk = Kc [{e (t) -e (t-Δtc)} + Δtc / 2Ti {e (t) + e (t-tc)}] ... e (t): Te (t) -Tes (t) Δtc: Sampling time Kc: Gain Ti: Integration time Then, in step S 5 , the increase / decrease amount of the operating frequency of the compressor is added / subtracted to determine the operating frequency Fk of the compressor.

Fk=Fk(t−ΔTc)+ΔFk … このようにして、決定された圧縮機(1)の運転周波数
Fkに基づいて圧縮機(1)の運転容量が制御され、蒸発
圧力相当飽和温度が最適な一定値に保持される。
Fk = Fk (t−ΔTc) + ΔFk ... The operating frequency of the compressor (1) thus determined
The operating capacity of the compressor (1) is controlled based on Fk, and the vapor pressure equivalent saturation temperature is maintained at an optimum constant value.

その後、ステップS5よりステップS6に移り、室内ユニッ
トのサーモオン状態が変更されたか否かが判定され、サ
ーモオン状態のままの場合、ステップS7に移り、再び室
内ユニットがサーモオンか否かが判定され、サーモオン
の場合ステップS8に移り、第2タイマがタイムアップし
たか否かが判定され、タイムアップするまでステップS6
に戻る一方、タイムアップするとステップS2に戻り、上
述の動作が繰返される。つまり、第2タイマの20秒毎
に、Teが目標値になるように圧縮機(1)の運転周波数
が算出されて、該周波数に圧縮機(1)が容量制御され
る。
Then, from step S 5 to step S 6 , it is determined whether the thermo-on state of the indoor unit has been changed.If the thermo-on state remains, the process proceeds to step S 7 and it is determined again whether or not the indoor unit is thermo-on. is, in the case of thermo proceeds to step S 8, the second timer is determined whether or not the time is up, step S 6 until the time is up
On the other hand, when the time is up, the process returns to step S 2 and the above-described operation is repeated. That is, every 20 seconds of the second timer, the operating frequency of the compressor (1) is calculated so that Te reaches the target value, and the capacity of the compressor (1) is controlled to the frequency.

更に、図示しないが、上述したような室内電動膨張弁
(6)の最大開度及び圧縮機(11)の運転周波数制御に
よって蒸発圧力相当飽和温度Teを最適な状態にした後、
冷房負荷が大きくなった場合、つまり、蒸発圧力相当飽
和温度Teが上昇した場合、該蒸発温度検出手段(53)に
よる検出温度が所定温度以上になり、容量検出手段(5
4)によって圧縮機の容量が最大になったことが検知さ
れた場合には、上記蒸発温度検出手段(53)および容量
検出手段(54)からの検知信号が最大開度規制手段(5
5)に送信されて、上述の如く、1250plsを最大開度(第
2最大開度)としていた室内電動膨張弁(6)の開度を
500plsの開度を最大(第3最大開度)とするように設定
される。つまり、以下の両条件が満たされることによっ
て室内電動膨張弁(6)の最大開度が第2最大開度より
更に小さい第3最大開度に設定し、蒸発圧力相当飽和温
度Teを低下させて十分な蓄冷熱量を得るようにする。
Further, although not shown, after the evaporation pressure equivalent saturation temperature Te is optimized by controlling the maximum opening of the indoor electric expansion valve (6) and the operating frequency of the compressor (11) as described above,
When the cooling load becomes large, that is, when the evaporation pressure equivalent saturation temperature Te rises, the temperature detected by the evaporation temperature detecting means (53) becomes equal to or higher than a predetermined temperature, and the capacity detecting means (5
When it is detected by 4) that the capacity of the compressor has become maximum, the detection signals from the evaporation temperature detecting means (53) and the capacity detecting means (54) are the maximum opening regulating means (5
5), and as described above, the opening degree of the indoor electric expansion valve (6) whose maximum opening degree (1250 pls) (second maximum opening degree) is changed.
The opening of 500 pls is set to the maximum (3rd maximum opening). That is, by satisfying the following two conditions, the maximum opening degree of the indoor electric expansion valve (6) is set to the third maximum opening degree which is smaller than the second maximum opening degree, and the evaporation pressure equivalent saturation temperature Te is lowered. Try to get a sufficient amount of cold storage heat.

・室内電動膨張弁の最大開度が第2最大開度に設定され
ている。
-The maximum opening of the indoor electric expansion valve is set to the second maximum opening.

・Te>−5℃で且つFk≧130Hz、若しくはFk>107.5Hzで
且つ加速蓄冷運転中となっている。
・ Te> -5 ° C and Fk ≥ 130Hz, or Fk> 107.5Hz and accelerated cold storage operation.

(尚、加速蓄冷運転のIN条件はFk′>117.5Hzとし、OUT
条件はFk′<95Hzとする) 一方、以下の条件のうち何れかが成立すると、それをOU
T条件として室内電動膨張弁(6)の第3最大開度制御
は解除される。
(The IN condition for accelerated cold storage operation is Fk '> 117.5Hz, and OUT
On the other hand, the condition is Fk '<95Hz).
As the T condition, the third maximum opening degree control of the indoor electric expansion valve (6) is released.

・第2最大開度の制御条件解除 ・Fk<85Hz且つ加速蓄冷運転解除 ・Fk<65Hz且つ加速蓄冷運転開始 そして、上述した制御が繰返されることになる。-Release of control conditions for the second maximum opening-Fk <85Hz and acceleration cold storage operation release-Fk <65Hz and acceleration cold storage operation start Then, the above-mentioned control is repeated.

上述してきたように、本例における蓄熱式空気調和装置
の運転制御装置及び運転制御方法では、蓄冷熱運転残り
時間と蓄冷熱量とを検知して、この残り時間を最大限に
使って、圧縮機(1)をできるだけ低周波数の運転を行
わせるようにしたことで圧縮機(1)は成績係数の高い
領域での運転状態が得られることになり、省エネ性が向
上されている。また、蒸発圧力相当飽和温度Teを一定と
するべく、室内電動膨張弁(6)及び圧縮機(1)の最
大運転周波数を設定することで従来のような蓄冷熱量の
不足やドラフトの発生、更には、室内熱交換機(7)の
凍結が防止されている。
As described above, in the operation control device and the operation control method of the heat storage type air conditioner in the present example, the cold storage heat operation remaining time and the cold storage heat amount are detected, and the remaining time is used to the maximum, the compressor By making the operation of (1) as low as possible, the compressor (1) can obtain an operating state in a region where the coefficient of performance is high, and energy saving is improved. In addition, by setting the maximum operating frequency of the indoor electric expansion valve (6) and the compressor (1) in order to keep the saturation temperature Te equivalent to the evaporation pressure constant, the shortage of cold storage heat and the generation of drafts as in the conventional case, Of the indoor heat exchanger (7) is prevented from freezing.

尚、室内電動膨張弁(6)の各最大開度のパルス信号の
値は適宜設定可能である。
The value of the pulse signal for each maximum opening of the indoor electric expansion valve (6) can be set as appropriate.

また、主冷媒回路も本実施例のものに限られるものでは
ない。
Also, the main refrigerant circuit is not limited to that of this embodiment.

(発明の効果) 以上説明したように、請求項(1)の発明では、通常冷
房及び蓄冷熱同時運転時に、最大開度設定手段の作動に
よって主減圧弁の最大開度を通常冷房運転時に設定され
る第1最大開度より小さい所定の第2最大開度に設定し
て、蒸発圧力相当飽和温度の上昇を抑制し、蓄熱用熱交
換器内での冷媒の温度と水の凍結温度との差が十分にと
れるようにし、製氷量の低下を防ぐ。また、容量検出手
段が圧縮機の最大容量運転を検出し、且つ上記蒸発温度
検出手段が検出した蒸発圧力相当飽和温度が予め設定さ
れた設定温度以上になると、最大開度規制手段の作動に
よって主減圧弁の最大開度を第2最大開度より更に小さ
い所定の第3最大開度に設定して、冷房負荷の増大に伴
う蒸発圧力相当飽和温度の上昇を抑制し、十分な製氷量
が得られるように制御する。このように、主減圧弁の開
度調整によって、蒸発圧力相当飽和温度を常に一定に制
御し、冷房負荷の大小に起因する不具合が解消され、十
分な蓄冷熱量が得られると同時に、利用側熱交換器のド
ラフトの発生や凍結が回避されて連続運転が可能とな
り、装置の信頼性が向上する。
(Effect of the Invention) As described above, in the invention of claim (1), the maximum opening degree of the main pressure reducing valve is set during the normal cooling operation by the operation of the maximum opening setting means during the normal cooling and cold heat simultaneous operation. Is set to a predetermined second maximum opening smaller than the first maximum opening to suppress the increase in the evaporation pressure-equivalent saturation temperature, and to prevent the temperature of the refrigerant and the freezing temperature of water in the heat exchanger for heat storage from increasing. Make sure that the difference is sufficient and prevent the amount of ice making from decreasing. Further, when the capacity detection means detects the maximum capacity operation of the compressor and the evaporation pressure equivalent saturation temperature detected by the evaporation temperature detection means becomes equal to or higher than a preset set temperature, the operation of the maximum opening control means causes The maximum opening of the pressure reducing valve is set to a predetermined third maximum opening, which is smaller than the second maximum opening, to suppress the rise of the evaporation temperature equivalent saturation temperature due to the increase of the cooling load, and obtain a sufficient amount of ice making. To be controlled. In this way, by adjusting the opening of the main pressure reducing valve, the saturation temperature equivalent to the evaporating pressure is always controlled to be constant, and the problems caused by the size of the cooling load are eliminated, and a sufficient amount of cold storage heat can be obtained, and at the same time, the heat on the use side Draft and freezing of the exchanger are avoided, and continuous operation is possible, improving the reliability of the device.

また、請求項(2)の発明では、通常冷房及び蓄冷熱同
時運転時に、蒸発温度検出手段の出力信号を受けて蒸発
圧力相当飽和温度が予め設定された目標値になるように
容量制御手段が圧縮機の容量を制御する。このことによ
り、蒸発圧力相当飽和温度の上下動を抑制し、正確な蓄
冷熱運転が行われると共に、利用側熱交換器の凍結等を
防止することができる。
Further, in the invention of claim (2), during the normal cooling and the cold storage heat simultaneous operation, the capacity control means receives the output signal of the evaporation temperature detection means so that the evaporation pressure equivalent saturation temperature becomes a preset target value. Controls compressor capacity. As a result, vertical movement of the saturation temperature equivalent to the evaporation pressure can be suppressed, accurate cold storage heat operation can be performed, and freezing of the use-side heat exchanger can be prevented.

そして、請求項(3)の発明では、上記請求項(1)お
よび(2)に記載された両作用によって、主減圧弁の開
度および圧縮機の容量制御によって確実な通常冷房およ
び蓄冷熱同時運転が行える。
Further, according to the invention of claim (3), both normal cooling and cold storage heat can be reliably performed by controlling the opening degree of the main pressure reducing valve and the capacity of the compressor by both actions described in claims (1) and (2). Can drive.

更に、請求項(4)の発明では、蓄冷熱運転時に、蓄冷
熱時間設定手段が蓄冷熱運転時間を設定し、製氷量検出
手段が蓄熱槽内での必要製氷量を検出し、上記蓄冷熱時
間設定手段および製氷量検出手段からの出力信号が、演
算手段に送られ、該演算手段によって必要製氷量を設定
時間で製氷するのに要する圧縮機の最低運転周波数を算
出した後、演算手段からの出力信号が運転制御手段に送
られ、該運転制御手段によって上記演算手段で算出され
た圧縮機運転周波数に基づき圧縮機の運転を制御する。
これにより、蓄冷熱運転可能な時間を最大限に使って圧
縮機を最低周波数で運転させることができるので、成績
係数の高い領域で圧縮機を駆動させることができ、消費
電力の低減に伴ない省エネ性が向上する。
Further, in the invention of claim (4), during the cold storage heat operation, the cold storage heat time setting means sets the cold storage heat operation time, and the ice making amount detection means detects the necessary ice making amount in the heat storage tank, and Output signals from the time setting means and the ice making amount detecting means are sent to the calculating means, and the calculating means calculates the minimum operating frequency of the compressor required to make the required ice making amount in the set time, and then from the calculating means. Is sent to the operation control means, and the operation control means controls the operation of the compressor based on the compressor operation frequency calculated by the operation means.
As a result, the compressor can be operated at the lowest frequency by making the maximum use of the cold storage heat operation time, so it is possible to drive the compressor in a region with a high coefficient of performance, which results in a reduction in power consumption. Energy efficiency is improved.

最後に、請求項(5)および(6)記載の発明では、通
常冷房及び蓄冷熱同時運転時には上記請求項(1)〜
(3)記載の作用により、また、蓄冷熱運転時には上記
請求項(4)記載の作用により主減圧弁の閉度および圧
縮機の運転周波数が制御され、最適な運転状態が得られ
る。
Finally, in the inventions described in claims (5) and (6), the above claims (1) to (1) to
By the action described in (3) and by the action described in claim (4) during the cold heat storage operation, the degree of closure of the main pressure reducing valve and the operating frequency of the compressor are controlled, and an optimum operating state is obtained.

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

第1図は請求項(1)に記載された発明の構成を示すブ
ロック図である。第2図は請求項(2)に記載された発
明の構成を示すブロック図である。第3図は請求項
(4)に記載された発明の構成を示すブロック図であ
る。 第4図〜第15図は本発明の一実施例を示し、第4図は装
置の全体構成を示す冷媒配管系統図、第5図〜第8図は
それぞれ冷房運転における各運転モードを示し、第5図
は通常冷房運転、第6図は蓄冷熱運転、第7図は通常冷
房及び蓄冷熱同時運転、第8図は蓄冷熱回収運転におけ
る冷媒の循環を示す説明図である。第9図〜第12図はそ
れぞれ暖房運転における各運転モードを示し、第9図は
通常暖房運転、第10図は蓄暖熱運転、第11図は通常暖房
及び蓄暖熱同時運転、第12図は蓄暖熱回収デフロスト運
転における冷媒の循環経路を示す説明図である。第13図
は本装置の制御内容を示すフローチャート図、第14図は
蓄冷熱運転時のコントローラの制御内容を示すフローチ
ャート図、第15図は蓄熱所要時間と残氷量との関係を示
した図である。 (1)……圧縮機 (3)……室外熱交換器(熱源側熱交換器) (6)……室内電動膨張弁(主減圧弁) (7)……室内熱交換器(利用側熱交換器) (9)……冷媒配管 (10)……主冷媒回路 (11)……蓄熱槽 (12)……蓄熱熱交換器 (14)……蓄熱電動膨張弁(蓄冷熱用減圧機構) (51)……切換手段 (52)……最大開度設定手段 (53)……蒸発温度検出手段 (54)……容量検出手段 (55)……最大開度規制手段 (56)……容量制御手段 (61)……蓄冷熱時間設定手段 (62)……製氷量検出手段 (63)……演算手段 (64)……運転制御手段
FIG. 1 is a block diagram showing the configuration of the invention described in claim (1). FIG. 2 is a block diagram showing the configuration of the invention described in claim (2). FIG. 3 is a block diagram showing the configuration of the invention described in claim (4). 4 to 15 show an embodiment of the present invention, FIG. 4 is a refrigerant piping system diagram showing the overall configuration of the apparatus, and FIGS. 5 to 8 show respective operation modes in the cooling operation, 5 is a normal cooling operation, FIG. 6 is a cold storage heat operation, FIG. 7 is an explanatory view showing refrigerant circulation in a normal cooling and cold storage heat simultaneous operation, and FIG. 8 is a cold storage heat recovery operation. 9 to 12 show each operation mode in the heating operation, FIG. 9 is a normal heating operation, FIG. 10 is a heat storage / heat storage operation, and FIG. 11 is a normal heating and heat storage / heat storage simultaneous operation, FIG. The figure is an explanatory view showing a circulation path of a refrigerant in the warm storage heat recovery defrost operation. FIG. 13 is a flow chart showing the control content of this device, FIG. 14 is a flow chart showing the control content of the controller during cold storage heat operation, and FIG. 15 is a diagram showing the relationship between the heat storage required time and the amount of residual ice. Is. (1) ...... Compressor (3) …… Outdoor heat exchanger (heat source side heat exchanger) (6) …… Indoor electric expansion valve (main pressure reducing valve) (7) …… Indoor heat exchanger (use side heat Exchanger) (9) …… Refrigerant piping (10) …… Main refrigerant circuit (11) …… Heat storage tank (12) …… Heat storage heat exchanger (14) …… Heat storage electric expansion valve (decompression mechanism for cold storage heat) (51) …… Switching means (52) …… Maximum opening setting means (53) …… Evaporation temperature detecting means (54) …… Capacity detecting means (55) …… Maximum opening regulating means (56) …… Capacity Control means (61) …… Cold storage heat time setting means (62) …… Ice making amount detection means (63) …… Calculation means (64) …… Operation control means

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 昭59−208366(JP,A) 特開 昭64−10067(JP,A) 特開 昭64−10068(JP,A) ─────────────────────────────────────────────────── ─── Continuation of the front page (56) References JP-A-59-208366 (JP, A) JP-A-64-10067 (JP, A) JP-A-64-10068 (JP, A)

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】容量の可変な圧縮機(1)、熱源側熱交換
器(3)、開度の可変自在な主減圧弁(6)及び利用側
熱交換器(7)を冷媒配管(9)で順次接続してなる主
冷媒回路(10)と、蓄冷熱用の氷を貯溜する蓄熱槽(1
1)とを備える一方、上記蓄熱槽(11)内に配置される
と共に、上記主冷媒回路(10)に接続され、冷媒と蓄熱
媒体との熱交換を行うための蓄熱熱交換器(12)と、蓄
冷熱用減圧機構(14)とを備えるとともに、 少なくとも通常冷房運転時には、熱源側熱交換器(3)
で凝縮された液冷媒が主冷媒回路(10)のみを流れて主
減圧弁(6)で減圧され、利用側熱交換器(7)で蒸発
して圧縮機(1)に戻るように循環し、蓄冷熱運転時に
は、熱源側熱交換器(3)で凝縮された液冷媒が蓄冷熱
用減圧機構(14)で減圧され、蓄熱熱交換器(12)で蒸
発したのち圧縮機(1)に戻るように循環し、蓄冷熱回
収運転時には、熱源側熱交換器(3)で凝縮された液冷
媒が主冷媒回路(10)から蓄熱熱交換器(12)で過冷却
された後、主冷媒回路(10)の利用側熱交換器(7)で
蒸発して圧縮機(1)に戻るように循環し、通常冷房及
び蓄冷熱同時運転時には、熱源側熱交換器(3)で凝縮
された液冷媒の一部が主冷媒回路(10)の利用側熱交換
器(7)で蒸発する一方、液冷媒の残部が蓄熱熱交換器
(12)で蒸発した後、それぞれ圧縮機(1)に戻るよう
に回路接続を切換える切換手段(51)を備えた蓄熱式空
気調和装置であって、 通常冷房及び蓄冷熱同時運転時に、主減圧弁(6)の最
大開度を通常冷房運転時に設定される第1最大開度より
小さい所定の第2最大開度に設定する最大開度設定手段
(52)と、蒸発圧力相当飽和温度を検出する蒸発温度検
出手段(53)と、圧縮機(1)の最大容量運転時を検出
する容量検出手段(54)と、該容量検出手段(54)が圧
縮機(1)の最大容量運転を検出し、且つ上記蒸発温度
検出手段(53)が検出した蒸発圧力相当飽和温度が予め
設定された設定温度以上になると、主減圧弁(6)の最
大開度を第2最大開度より小さい所定の第3最大開度に
設定する最大開度規制手段(55)とを備えたことを特徴
とする蓄熱式空気調和装置の運転制御装置。
1. A compressor (1) having a variable capacity, a heat source side heat exchanger (3), a main pressure reducing valve (6) having a variable opening degree, and a use side heat exchanger (7) are connected to a refrigerant pipe (9). ), A main refrigerant circuit (10) connected in sequence, and a heat storage tank (1) for storing ice for cold heat storage.
1) and a heat storage heat exchanger (12) arranged in the heat storage tank (11) and connected to the main refrigerant circuit (10) for exchanging heat between the refrigerant and the heat storage medium. And a decompression mechanism (14) for storing cold heat, and at least during normal cooling operation, the heat source side heat exchanger (3)
The liquid refrigerant condensed in circulates only in the main refrigerant circuit (10), is decompressed by the main pressure reducing valve (6), evaporates in the utilization side heat exchanger (7) and returns to the compressor (1). During the cold storage heat operation, the liquid refrigerant condensed in the heat source side heat exchanger (3) is decompressed by the cold storage heat decompression mechanism (14), evaporated in the heat storage heat exchanger (12), and then stored in the compressor (1). During the cold heat recovery operation, the liquid refrigerant condensed in the heat source side heat exchanger (3) is supercooled in the heat storage heat exchanger (12) from the main refrigerant circuit, and then circulates so as to return to the main refrigerant. It circulates so as to evaporate in the utilization side heat exchanger (7) of the circuit (10) and return to the compressor (1), and is condensed in the heat source side heat exchanger (3) during normal cooling and cold storage simultaneous operation. Part of the liquid refrigerant evaporates in the use side heat exchanger (7) of the main refrigerant circuit (10), while the rest of the liquid refrigerant evaporates in the heat storage heat exchanger (12). A heat storage type air conditioner equipped with a switching means (51) for switching the circuit connection so as to return to the compressor (1) respectively, which is the maximum of the main pressure reducing valve (6) during normal cooling and cold storage simultaneous operation. A maximum opening setting means (52) for setting the opening to a predetermined second maximum opening smaller than the first maximum opening set during normal cooling operation, and an evaporation temperature detecting means (52) for detecting the saturation temperature equivalent to the evaporation pressure ( 53), a capacity detecting means (54) for detecting the maximum capacity operation of the compressor (1), the capacity detecting means (54) detecting the maximum capacity operation of the compressor (1), and the evaporation temperature. When the vapor pressure equivalent saturation temperature detected by the detection means (53) becomes equal to or higher than a preset set temperature, the maximum opening of the main pressure reducing valve (6) is set to a predetermined third maximum opening smaller than the second maximum opening. A heat storage type air conditioner characterized by being provided with a maximum opening control means (55) to be set. The operation control device.
【請求項2】容量の可変な圧縮機(1)、熱源側熱交換
器(3)、主減圧弁(6)及び利用側熱交換器(7)を
冷媒配管(9)で順次接続してなる主冷媒回路(10)
と、蓄冷熱用の氷を貯溜する蓄熱槽(11)とを備える一
方、上記蓄熱槽(11)内に配置されると共に、上記主冷
媒回路(10)に接続され、冷媒と蓄熱媒体との熱交換を
行うための蓄熱熱交換器(12)と、蓄冷熱用減圧機構
(14)とを備えるとともに、 少なくとも通常冷房運転時には、熱源側熱交換器(3)
で凝縮された液冷媒が主冷媒回路(10)のみを流れて主
減圧弁(6)で減圧され、利用側熱交換器(7)で蒸発
して圧縮機(1)に戻るように循環し、蓄冷熱運転時に
は、熱源側熱交換器(3)で凝縮された液冷媒が蓄冷熱
用減圧機構(14)で減圧され、蓄熱熱交換器(12)で蒸
発したのち圧縮機(1)に戻るように循環し、蓄冷熱回
収運転時には、熱源側熱交換器(3)で凝縮された液冷
媒が主冷媒回路(10)から蓄熱熱交換器(12)で過冷却
された後、主冷媒回路(10)の利用側熱交換器(7)で
蒸発して圧縮機(1)に戻るように循環し、通常冷房及
び蓄冷熱同時運転時には、熱源側熱交換器(3)で凝縮
された液冷媒の一部が主冷媒回路(10)の利用側熱交換
器(7)で蒸発する一方、液冷媒の残部が蓄熱熱交換器
(12)で蒸発した後、それぞれ圧縮機(1)に戻るよう
に回路接続を切換える切換手段(51)を備えた蓄熱式空
気調和装置であって、 通常冷房及び蓄冷熱同時運転時に、蒸発圧力相当飽和温
度を検出する蒸発温度検出手段(53)と、該蒸発温度検
出手段(53)の出力信号を受けて蒸発圧力相当飽和温度
が予め設定された目標値になるように圧縮機(1)の容
量を制御する容量制御手段(56)とを備えたことを特徴
とする蓄熱式空気調和装置の運転制御装置。
2. A compressor (1) having a variable capacity, a heat source side heat exchanger (3), a main pressure reducing valve (6) and a use side heat exchanger (7) are sequentially connected by a refrigerant pipe (9). Become a main refrigerant circuit (10)
And a heat storage tank (11) for storing ice for cold storage, while being arranged in the heat storage tank (11) and connected to the main refrigerant circuit (10), the refrigerant and the heat storage medium are connected. A heat storage heat exchanger (12) for performing heat exchange and a cold storage heat decompression mechanism (14) are provided, and at least during normal cooling operation, the heat source side heat exchanger (3).
The liquid refrigerant condensed in circulates only in the main refrigerant circuit (10), is decompressed by the main pressure reducing valve (6), evaporates in the utilization side heat exchanger (7) and returns to the compressor (1). During the cold storage heat operation, the liquid refrigerant condensed in the heat source side heat exchanger (3) is decompressed by the cold storage heat decompression mechanism (14), evaporated in the heat storage heat exchanger (12), and then stored in the compressor (1). During the cold heat recovery operation, the liquid refrigerant condensed in the heat source side heat exchanger (3) is supercooled in the heat storage heat exchanger (12) from the main refrigerant circuit, and then circulates so as to return to the main refrigerant. It circulates so as to evaporate in the utilization side heat exchanger (7) of the circuit (10) and return to the compressor (1), and is condensed in the heat source side heat exchanger (3) during normal cooling and cold storage simultaneous operation. Part of the liquid refrigerant evaporates in the use side heat exchanger (7) of the main refrigerant circuit (10), while the rest of the liquid refrigerant evaporates in the heat storage heat exchanger (12). A heat storage type air conditioner equipped with a switching means (51) for switching the circuit connection so as to return to the compressor (1) respectively, and detects a saturation temperature equivalent to an evaporation pressure during normal cooling and cold storage simultaneous operation. Evaporation temperature detection means (53) and a capacity for receiving the output signal of the evaporation temperature detection means (53) and controlling the capacity of the compressor (1) so that the saturation temperature equivalent to the evaporation pressure becomes a preset target value. An operation control device for a heat storage type air conditioner, comprising: a control means (56).
【請求項3】上記請求項(1)記載の蓄熱式空気調和装
置の運転制御装置において、蒸発温度検出手段(53)の
出力信号を受けて蒸発圧力相当飽和温度が予め設定され
た目標値になるように圧縮機(1)の容量を制御する容
量制御手段(56)を備えたことを特徴とする蓄熱式空気
調和装置の運転制御装置。
3. An operation control device for a heat storage type air conditioner according to claim 1, wherein an evaporation pressure equivalent saturation temperature is set to a preset target value in response to an output signal of an evaporation temperature detecting means (53). An operation control device for a heat storage type air conditioner comprising a capacity control means (56) for controlling the capacity of the compressor (1).
【請求項4】容量の可変な圧縮機(1)、熱源側熱交換
器(3)、主減圧弁(6)及び利用側熱交換器(7)を
冷媒配管(9)で順次接続してなる主冷媒回路(10)
と、蓄冷熱用の氷を貯溜する蓄熱槽(11)とを備える一
方、上記蓄熱槽(11)内に配置されると共に、上記主冷
媒回路(10)に接続され、冷媒と蓄熱媒体との熱交換を
行うための蓄熱熱交換器(12)と、蓄冷熱用減圧機構
(14)とを備えるとともに、 少なくとも通常冷房運転時には、熱源側熱交換器(3)
で凝縮された液冷媒が主冷媒回路(10)のみを流れて主
減圧弁(6)で減圧され、利用側熱交換器(7)で蒸発
して圧縮機(1)に戻るように循環し、蓄冷熱運転時に
は、熱源側熱交換器(3)で凝縮された液冷媒が蓄冷熱
用減圧機構(14)で減圧され、蓄熱熱交換器(12)で蒸
発したのち圧縮機(1)に戻るように循環し、蓄冷熱回
収運転時には、熱源側熱交換器(3)で凝縮された液冷
媒が主冷媒回路(10)から蓄熱熱交換器(12)で過冷却
された後、主冷媒回路(10)の利用側熱交換器(7)で
蒸発して圧縮機(1)に戻るように循環し、通常冷房及
び蓄冷熱同時運転時には、熱源側熱交換器(3)で凝縮
された液冷媒の一部が主冷媒回路(10)の利用側熱交換
器(7)で蒸発する一方、液冷媒の残部が蓄熱熱交換器
(12)で蒸発した後、それぞれ圧縮機(1)に戻るよう
に回路接続を切換える切換手段(51)を備えた蓄熱式空
気調和装置であって、 蓄冷熱運転時に、蓄冷熱運転時間を設定する蓄冷熱時間
設定手段(61)と、蓄熱槽(11)内の必要製氷量を検出
する製氷量検出手段(62)と、上記蓄冷熱時間設定手段
(61)および製氷量検出手段(62)からの出力信号を受
けて、該必要製氷量を設定時間で製氷するのに要する圧
縮機(1)の最低運転周波数を算出する演算手段(63)
と、演算手段(63)からの出力信号を受け、該演算手段
(63)で算出された圧縮機運転周波数に基づき圧縮機
(1)の運転を制御する運転制御手段(64)と備えてい
ることを特徴とする蓄熱式空気調和装置の運転制御装
置。
4. A compressor (1) having a variable capacity, a heat source side heat exchanger (3), a main pressure reducing valve (6) and a use side heat exchanger (7) are sequentially connected by a refrigerant pipe (9). Become a main refrigerant circuit (10)
And a heat storage tank (11) for storing ice for cold storage, while being arranged in the heat storage tank (11) and connected to the main refrigerant circuit (10), the refrigerant and the heat storage medium are connected. A heat storage heat exchanger (12) for performing heat exchange and a cold storage heat decompression mechanism (14) are provided, and at least during normal cooling operation, the heat source side heat exchanger (3).
The liquid refrigerant condensed in circulates only in the main refrigerant circuit (10), is decompressed by the main pressure reducing valve (6), evaporates in the utilization side heat exchanger (7) and returns to the compressor (1). During the cold storage heat operation, the liquid refrigerant condensed in the heat source side heat exchanger (3) is decompressed by the cold storage heat decompression mechanism (14), evaporated in the heat storage heat exchanger (12), and then stored in the compressor (1). During the cold heat recovery operation, the liquid refrigerant condensed in the heat source side heat exchanger (3) is supercooled in the heat storage heat exchanger (12) from the main refrigerant circuit, and then circulates so as to return to the main refrigerant. It circulates so as to evaporate in the utilization side heat exchanger (7) of the circuit (10) and return to the compressor (1), and is condensed in the heat source side heat exchanger (3) during normal cooling and cold storage simultaneous operation. Part of the liquid refrigerant evaporates in the use side heat exchanger (7) of the main refrigerant circuit (10), while the rest of the liquid refrigerant evaporates in the heat storage heat exchanger (12). A heat storage type air conditioner equipped with a switching means (51) for switching the circuit connection so as to return to the compressor (1), respectively, wherein a cold storage heat time setting means for setting a cold storage heat operation time during cold storage heat operation. (61), an ice making amount detecting means (62) for detecting a necessary ice making amount in the heat storage tank (11), and output signals from the cold heat storage time setting means (61) and the ice making amount detecting means (62). Calculating means (63) for calculating the minimum operating frequency of the compressor (1) required to make the required ice making amount in a set time.
And an operation control means (64) for receiving the output signal from the arithmetic means (63) and controlling the operation of the compressor (1) based on the compressor operating frequency calculated by the arithmetic means (63). An operation control device of a heat storage type air conditioner characterized by the above.
【請求項5】上記請求項(1),(2)または(3)記
載の蓄熱式空気調和装置の運転制御装置において、蓄冷
熱運転時に、蓄冷熱運転時間を設定する蓄冷熱時間設定
手段(61)と、蓄熱槽(11)内の必要製氷量を検出する
製氷量検出手段(62)と、上記蓄冷熱時間設定手段(6
1)および製氷量検出手段(62)からの出力信号を受け
て、該必要製氷量を設定時間で製氷するのに要する圧縮
機(1)の最低運転周波数を算出する演算手段(63)
と、演算手段(63)からの出力信号を受け、該演算手段
(63)で算出された圧縮機運転周波数に基づき圧縮機
(1)の運転を制御する運転制御手段(64)とを備えて
いることを特徴とする蓄熱式空気調和装置の運転制御装
置。
5. An operation control device for a heat storage type air conditioner according to any one of claims (1), (2) and (3), wherein a cold storage heat time setting means for setting a cold storage heat operation time during cold storage heat operation ( 61), an ice making amount detecting means (62) for detecting a necessary ice making amount in the heat storage tank (11), and the cold storage heat time setting means (6).
1) and an arithmetic means (63) for receiving the output signals from the ice making amount detecting means (62) and calculating the minimum operating frequency of the compressor (1) required to make the required ice making amount in a set time.
And an operation control means (64) for receiving the output signal from the arithmetic means (63) and controlling the operation of the compressor (1) based on the compressor operating frequency calculated by the arithmetic means (63). An operation control device for a heat storage type air conditioner characterized by being provided.
【請求項6】容量の可変な圧縮機(1)、熱源側熱交換
器(3)、開度の可変自在な主減圧弁(6)及び利用側
熱交換器(7)を冷媒配管(9)で順次接続してなる主
冷媒回路(10)と、蓄冷熱用の氷を貯溜する蓄熱槽(1
1)とを備える一方、上記蓄熱槽(11)内に配置される
と共に、上記主冷媒回路(10)に接続され、冷媒と蓄熱
媒体との熱交換を行うための蓄熱熱交換器(12)と、蓄
冷熱用減圧機構(14)とを備えるとともに、 少なくとも通常冷房運転時には、熱源側熱交換器(3)
で凝縮された液冷媒が主冷媒回路(10)のみを流れて主
減圧弁(6)で減圧され、利用側熱交換器(7)で蒸発
して圧縮機(1)に戻るように循環し、蓄冷熱運転時に
は、熱源側熱交換器(3)で凝縮された液冷媒が蓄冷熱
用減圧機構(14)で減圧され、蓄熱熱交換器(12)で蒸
発したのち圧縮機(1)に戻るように循環し、蓄冷熱回
収運転時には、熱源側熱交換器(3)で凝縮された液冷
媒が主冷媒回路(10)から蓄熱熱交換器(12)で過冷却
された後、主冷媒回路(10)の利用側熱交換器(7)で
蒸発して圧縮機(1)に戻るように循環し、通常冷房及
び蓄冷熱同時運転時には、熱源側熱交換器(3)で凝縮
された液冷媒の一部が主冷媒回路(10)の利用側熱交換
器(7)で蒸発する一方、液冷媒の残部が蓄熱熱交換器
(12)で蒸発した後、それぞれ圧縮機(1)に戻るよう
に回路接続を切換える切換手段(51)を備えた蓄熱式空
気調和装置の運転制御方法であって、 蓄冷熱運転時には、蓄冷熱運転時間を蓄冷熱時間設定手
段(61)によって設定すると同時に蓄熱槽(11)内の必
要製氷量を製氷量検出手段(62)が検出した後、演算手
段(63)が上記蓄冷熱運転時間で必要製氷量を製氷する
のに要する圧縮機(1)の最低運転周波数を算出し、こ
の算出された圧縮機運転周波数に基づいて運転制御手段
(64)が圧縮機(1)の運転を制御する一方、 通常冷房及び蓄冷熱同時運転時には、最大開度設定手段
(52)が主減圧弁(6)の最大開度を通常冷房運転時に
設定される第1最大開度より小さい所定の第2最大開度
に設定して、該主減圧弁(6)の開度を過熱度制御する
と共に、蒸発温度検出手段(53)が蒸発圧力相当飽和温
度を検出して容量制御手段(56)が圧縮機(1)の容量
を蒸発圧力相当飽和温度が所定の目標値になるように制
御し、その後、容量検出手段(54)が圧縮機(1)の最
大容量運転を検出し、且つ、蒸発圧力相当飽和温度が所
定温度以上になると、最大開度規制手段(55)が主減圧
弁(6)の最大開度を第2最大開度より小さい第3最大
開度に設定することを特徴とする蓄熱式空気調和装置の
運転制御方法。
6. A compressor (1) having a variable capacity, a heat source side heat exchanger (3), a main pressure reducing valve (6) having a variable opening degree, and a use side heat exchanger (7) are connected to a refrigerant pipe (9). ), A main refrigerant circuit (10) connected in sequence, and a heat storage tank (1) for storing ice for cold heat storage.
1) and a heat storage heat exchanger (12) arranged in the heat storage tank (11) and connected to the main refrigerant circuit (10) for exchanging heat between the refrigerant and the heat storage medium. And a decompression mechanism (14) for storing cold heat, and at least during normal cooling operation, the heat source side heat exchanger (3)
The liquid refrigerant condensed in circulates only in the main refrigerant circuit (10), is decompressed by the main pressure reducing valve (6), evaporates in the utilization side heat exchanger (7) and returns to the compressor (1). During the cold storage heat operation, the liquid refrigerant condensed in the heat source side heat exchanger (3) is decompressed by the cold storage heat decompression mechanism (14), evaporated in the heat storage heat exchanger (12), and then stored in the compressor (1). During the cold heat recovery operation, the liquid refrigerant condensed in the heat source side heat exchanger (3) is supercooled in the heat storage heat exchanger (12) from the main refrigerant circuit, and then circulates so as to return to the main refrigerant. It circulates so as to evaporate in the utilization side heat exchanger (7) of the circuit (10) and return to the compressor (1), and is condensed in the heat source side heat exchanger (3) during normal cooling and cold storage simultaneous operation. Part of the liquid refrigerant evaporates in the use side heat exchanger (7) of the main refrigerant circuit (10), while the rest of the liquid refrigerant evaporates in the heat storage heat exchanger (12). A method for controlling the operation of a heat storage type air conditioner comprising switching means (51) for switching the circuit connection so as to return to the compressor (1), respectively. After setting by the setting means (61), the ice making quantity detecting means (62) detects the necessary ice making quantity in the heat storage tank (11), and then the calculating means (63) makes the necessary ice making quantity in the cold storage heat operation time. The minimum operating frequency of the compressor (1) required for the operation is calculated, and the operation control means (64) controls the operation of the compressor (1) based on the calculated operating frequency of the compressor, while normal cooling and cold storage During the simultaneous heat operation, the maximum opening setting means (52) sets the maximum opening of the main pressure reducing valve (6) to a predetermined second maximum opening smaller than the first maximum opening set during the normal cooling operation. , The degree of superheat control of the opening of the main pressure reducing valve (6), and the evaporation temperature The detection means (53) detects the saturation temperature corresponding to the evaporation pressure, and the capacity control means (56) controls the capacity of the compressor (1) so that the saturation temperature corresponding to the evaporation pressure reaches a predetermined target value. When the detecting means (54) detects the maximum capacity operation of the compressor (1) and the saturation temperature equivalent to the evaporation pressure becomes equal to or higher than a predetermined temperature, the maximum opening regulating means (55) causes the maximum pressure reducing valve (6) to reach the maximum. An operation control method for a heat storage type air conditioner, characterized in that the opening is set to a third maximum opening smaller than the second maximum opening.
JP16213789A 1989-06-23 1989-06-23 Operation control device and operation control method for heat storage type air conditioner Expired - Lifetime JPH0792289B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16213789A JPH0792289B2 (en) 1989-06-23 1989-06-23 Operation control device and operation control method for heat storage type air conditioner

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16213789A JPH0792289B2 (en) 1989-06-23 1989-06-23 Operation control device and operation control method for heat storage type air conditioner

Publications (2)

Publication Number Publication Date
JPH0328671A JPH0328671A (en) 1991-02-06
JPH0792289B2 true JPH0792289B2 (en) 1995-10-09

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ID=15748743

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Application Number Title Priority Date Filing Date
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Country Link
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* Cited by examiner, † Cited by third party
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