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JPH0784964B2 - Operation control device for heat storage type air conditioner - Google Patents
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JPH0784964B2 - Operation control device for heat storage type air conditioner - Google Patents

Operation control device for heat storage type air conditioner

Info

Publication number
JPH0784964B2
JPH0784964B2 JP1323593A JP32359389A JPH0784964B2 JP H0784964 B2 JPH0784964 B2 JP H0784964B2 JP 1323593 A JP1323593 A JP 1323593A JP 32359389 A JP32359389 A JP 32359389A JP H0784964 B2 JPH0784964 B2 JP H0784964B2
Authority
JP
Japan
Prior art keywords
heat
heat storage
capacity
saturation temperature
heat exchanger
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 - Fee Related
Application number
JP1323593A
Other languages
Japanese (ja)
Other versions
JPH03186160A (en
Inventor
伸廣 楠本
信英 吉田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
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 JP1323593A priority Critical patent/JPH0784964B2/en
Publication of JPH03186160A publication Critical patent/JPH03186160A/en
Publication of JPH0784964B2 publication Critical patent/JPH0784964B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Compression-Type Refrigeration Machines With Reversible Cycles (AREA)
  • Air Conditioning Control Device (AREA)

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は蓄熱式空気調和装置の運転制御装置に係り、特
に冷房及び蓄冷熱同時運転時における蓄冷熱能力の確保
及び運転効率の向上対策に関する。
Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an operation control device for a heat storage type air conditioner, and more particularly to a measure for ensuring a cold storage heat capacity and improving operating efficiency during simultaneous cooling and cold storage heat operation. .

(従来の技術) 従来より、例えば特開昭59−208364号公報に開示される
如く、圧縮機、熱源側熱交換器、減圧弁及び利用側熱交
換器を接続してなる冷媒回路と、蓄冷熱可能な蓄熱媒体
を有する蓄熱槽と、冷媒回路の冷媒との熱交換により蓄
熱槽に冷熱を付与する蓄熱熱交換器とを備えた蓄熱式空
気調和装置において、利用側熱交換器における蒸発作用
と蓄熱熱交換器における蓄冷熱作用とを同時に行う冷房
及び蓄冷熱同時運転を可能とすることにより、室内で冷
房運転を行いながら、その冷房負荷が小さいときには蓄
熱熱交換器側で蓄冷熱をして、全体としての運転効率の
向上を図ろうとするものは公知の技術である。
(Prior Art) Conventionally, as disclosed in, for example, Japanese Patent Application Laid-Open No. 59-208364, a refrigerant circuit formed by connecting a compressor, a heat source side heat exchanger, a pressure reducing valve and a use side heat exchanger, and a cold storage In a heat storage type air conditioner equipped with a heat storage tank having a heat storage medium capable of heating and a heat storage heat exchanger for applying cold heat to the heat storage tank by heat exchange with the refrigerant of the refrigerant circuit, an evaporating action in the use side heat exchanger By enabling simultaneous cooling and cold storage heat operation that simultaneously performs the cold storage heat operation in the heat storage heat exchanger, while performing the indoor cooling operation, the heat storage heat exchanger side stores the cold heat when the cooling load is small. It is a well-known technique to improve the operation efficiency as a whole.

(発明が解決しようとする課題) ところで、通常、蓄熱槽に冷熱を蓄える蓄冷熱運転は電
力料金の安価な夜間に行われるが、夜間でも、業務の継
続により室内側で冷房要求がある場合がある。そのよう
な場合、上述従来のもののを利用することにより、明日
のための冷熱を蓄えながら、現在の冷房要求に答えるこ
とができることになる。
(Problems to be solved by the invention) By the way, normally, the cold storage heat operation of storing cold heat in the heat storage tank is performed at night when the electricity rate is low, but even at night, there is a case where there is a demand for cooling indoors due to continuation of work. is there. In such a case, by using the above-mentioned conventional one, it is possible to meet the present cooling demand while storing the cold heat for tomorrow.

しかしながら、上記従来のものでは、利用側熱交換器の
能力と蓄熱熱交換器の能力の比を調節する手段が講じら
れていない。そのために、能力がいずれかの熱交換器に
片寄り、特に、通常利用側熱交換器の要求に応じること
が多いので、その夜間に予定している蓄冷熱量が確保さ
れない虞れが生じる。
However, the above-mentioned conventional device does not take any means for adjusting the ratio of the capacity of the heat exchanger on the utilization side to the capacity of the heat storage heat exchanger. Therefore, the capacity tends to be biased toward one of the heat exchangers, and in particular, it often meets the demand of the normal use side heat exchanger, so that there is a possibility that the planned amount of cold storage heat cannot be secured at night.

また、逆に能力的に余力があるにもかかわらず高能力運
転を行うと、いわゆる成績係数が悪化する虞れもある。
On the contrary, when high-performance driving is performed even though there is a surplus of capacity, the so-called coefficient of performance may be deteriorated.

本発明は斯かる点に鑑みてなされたものであり、その目
的は、蓄熱熱交換器の必要な能力を基準として利用側交
換器側と蓄熱熱交換器側とに能力を分配する手段を講ず
ることにより、蓄冷熱量の確保と運転効率の向上とを図
ることにある。
The present invention has been made in view of such a point, and an object thereof is to provide a means for distributing the capacity to the use side exchanger side and the heat storage heat exchanger side with reference to the necessary capacity of the heat storage heat exchanger. By doing so, it is intended to secure the amount of cold storage heat and improve the operation efficiency.

(課題を解決するための手段) 上記目的を達成するため本発明の解決手段は、吸入飽和
温度を目標値に収束させるよう圧縮機の容量を制御しな
がら、同時に蓄熱槽の現在蓄冷熱量から必要な蓄冷熱能
力を割り出し、その必要蓄冷熱能力を確保するのに必要
な吸入圧力相当飽和温度の目標値を演算するとともに、
その吸入圧力相当飽和温度を満足させるよう利用側熱交
換器の減圧弁開度を制限することにある。
(Means for Solving the Problem) In order to achieve the above-mentioned object, the solution means of the present invention is required from the current amount of cold storage heat of the heat storage tank while controlling the capacity of the compressor so that the suction saturation temperature converges to a target value. And calculate the target value of the saturation temperature equivalent to the suction pressure necessary to secure the required cold storage heat capacity,
The opening degree of the pressure reducing valve of the heat exchanger on the utilization side is limited so as to satisfy the saturation temperature equivalent to the suction pressure.

具体的には、第1の解決手段は、第1図に示すように
(破線部分を含まず)、容量可変形圧縮機(1)、熱源
側熱交換器(3)、利用側電動膨張弁(6)及び利用側
熱交換器(7)を順次接続してなる冷媒回路(10)と、
冷熱の蓄熱可能な蓄熱媒体(W)を有する蓄熱槽(11)
と、上記冷媒回路(10)の冷媒との熱交換により上記蓄
熱槽(11)に冷熱を付与する蓄熱熱交換器(12)とを備
えた蓄熱式空気調和装置の前提とする。
Specifically, the first solving means is, as shown in FIG. 1 (not including the broken line portion), the variable capacity compressor (1), the heat source side heat exchanger (3), the use side electric expansion valve. A refrigerant circuit (10) in which (6) and a heat exchanger (7) on the use side are sequentially connected,
Heat storage tank (11) having heat storage medium (W) capable of storing cold heat
And a heat storage heat exchanger (12) for applying cold heat to the heat storage tank (11) by heat exchange with the refrigerant in the refrigerant circuit (10).

そして、蓄熱式空気調和装置の運転制御装置として、冷
媒の吸入圧力相当飽和温度を検出する飽和温度検出手段
(SP)と、所定時間毎に、該飽和温度検出手段(SP)で
検出される吸入圧力相当飽和温度がその目標値に収束す
るよう上記圧縮機(1)の運転容量を設定制御する容量
制御手段(51)を設けるものとする。
Then, as an operation control device of the heat storage type air conditioner, a saturation temperature detecting means (SP) for detecting a saturation temperature equivalent to the suction pressure of the refrigerant, and an intake air detected by the saturation temperature detecting means (SP) at predetermined intervals. A capacity control means (51) for setting and controlling the operating capacity of the compressor (1) is provided so that the saturation temperature equivalent to the pressure converges to its target value.

さらに、利用側熱交換器(7)側による蒸発作用と蓄熱
熱交換器(12)による蓄冷熱作用とを同時に行う冷房及
び蓄冷熱同時運転時、上記蓄熱槽(11)内の蓄熱媒体
(W)の現在蓄冷熱量を検出する蓄冷量検出手段(Cl)
と、該蓄冷量検出手段(Cl)の出力を受け、上記容量制
御手段(51)で制御される圧縮機(1)の前回サンプリ
ング時における運転容量に基づき、蓄熱熱交換器(12)
における蓄冷熱能力が上記蓄熱槽(11)の目標蓄冷熱量
と現在蓄冷熱量との差から求まる必要蓄冷熱能力になる
よう吸入圧力相当飽和温度の目標値を演算する目標値演
算手段(52)と、上記吸入圧力相当飽和温度が該目標値
演算手段(52)で算出される目標値に収束するよう上記
利用側電動膨張弁(6)の開度を制限する開度制限手段
(53)とを設ける構成としたものである。
Furthermore, at the time of simultaneous cooling and cold storage heat operation in which the evaporation action by the use side heat exchanger (7) side and the cold storage heat action by the heat storage heat exchanger (12) are performed simultaneously, the heat storage medium (W in the heat storage tank (11) ) Cold storage amount detection means (Cl) for detecting the current cold storage amount
And a heat storage heat exchanger (12) based on the operating capacity of the compressor (1) controlled by the capacity control means (51) at the time of the previous sampling, which receives the output of the cold storage amount detection means (Cl).
And a target value calculation means (52) for calculating a target value of the saturation temperature equivalent to the suction pressure so that the cold storage heat capacity at the required cold storage heat capacity obtained from the difference between the target cold storage heat quantity of the heat storage tank (11) and the current cold storage heat capacity. And an opening degree limiting means (53) for limiting the opening degree of the use side electric expansion valve (6) so that the suction pressure equivalent saturation temperature converges to the target value calculated by the target value calculating means (52). It is configured to be provided.

第2の解決手段は、上記第1の解決手段における開度制
限手段(53)を、圧縮器(1)の現在の運転容量が最大
で、かつ吸入圧力相当飽和温度の現在値と目標値との差
が所定値以上のときには、利用側電動膨張弁(6)の最
大開度値を低減するものとしたものである。
A second solving means is the opening limiting means (53) in the first solving means, in which the present operating capacity of the compressor (1) is the maximum and the present value and the target value of the intake pressure equivalent saturation temperature are set. When the difference is greater than or equal to a predetermined value, the maximum opening value of the use side electric expansion valve (6) is reduced.

第3の解決手段は、第1図に示すように(破線部分を含
む)、上記第1又は第2の解決手段に加えて、圧縮機
(1)の運転容量が一定値以下のときに、利用側電動膨
張弁(6)の最大開度値を増大させるように変更する最
大開度増大手段(54)を設けたものである。
As shown in FIG. 1 (including the broken line portion), the third solving means is, in addition to the above first or second solving means, when the operating capacity of the compressor (1) is below a certain value, A maximum opening increasing means (54) for changing the maximum opening value of the use side electric expansion valve (6) is provided.

(作用) 以上の構成により、請求項(1)の発明では、所定の設
定時間毎に、容量制御手段(51)により、飽和温度検出
手段(SP)で検出される吸入圧力相当飽和温度がその目
標値に収束するよう圧縮機(1)の運転容量が調節さ
れ、目標値演算手段(52)により、蓄熱熱交換器(12)
における蓄冷熱能力が必要蓄冷熱能力になるよう吸入圧
力相当飽和温度の目標値が演算される。そして、開度制
御手段(53)により、吸入圧力相当飽和温度がその目標
値に収束するように利用側電動膨張弁(6)の最大開度
が制限される。
(Operation) With the above configuration, in the invention of claim (1), the suction pressure equivalent saturation temperature detected by the saturation temperature detecting means (SP) by the capacity control means (51) is set at predetermined time intervals. The operating capacity of the compressor (1) is adjusted so that it converges to the target value, and the target value calculation means (52) causes the heat storage heat exchanger (12).
The target value of the saturation temperature equivalent to the suction pressure is calculated so that the cold storage heat capacity at becomes the required cold storage heat capacity. Then, the opening degree control means (53) limits the maximum opening degree of the use side electric expansion valve (6) so that the suction pressure equivalent saturation temperature converges to the target value.

すなわち、吸入圧力相当飽和温度の値が必要な蓄冷熱能
力を維持しうる値から外れないように制御されるので、
夜間等に蓄冷熱運転を行っているとき、冷房要求がなさ
れても、予定の蓄冷熱を確実に確保しながら、冷房要求
に応じる冷房運転が行われることになる。しかも、その
間、吸入圧力相当飽和温度が目標値に収束するよう圧縮
機(1)の運転容量が調節されるので、必要な能力以上
の運転は回避される。したがって、予定の蓄冷熱量が確
保されるとともに、全体としての運転効率が向上するこ
とになる。
That is, since the value of the saturation temperature equivalent to the suction pressure is controlled so as not to deviate from the value capable of maintaining the required cold storage heat capacity,
Even if a cooling request is made during the cold storage operation at night or the like, the cooling operation is performed in accordance with the cooling request while surely ensuring the scheduled cool storage heat. In addition, during that time, the operating capacity of the compressor (1) is adjusted so that the saturation temperature equivalent to the suction pressure converges to the target value, so that operation exceeding the required capacity is avoided. Therefore, the planned amount of cold storage heat is secured and the operation efficiency as a whole is improved.

請求項(2)の判明では、上記請求項(1)の発明にお
いて、開度制限手段(53)により、圧縮機(1)の運転
容量が最大で、かつ吸入圧力相当飽和温度とその目標値
との差が所定値以上になると、利用側電動膨張弁(6)
の開度が低減するよう制限されるので、能力に余裕がな
いために吸入圧力相当飽和温度が目標値から外れようと
する場合には、利用側熱交換器(6)への能力の分配が
減少し、その結果、蓄熱熱交換器(12)側の蓄冷熱能力
の低下が抑制されることになる。よって、請求項(1)
の発明の実効を図ることができるのである。
According to claim (2), in the invention according to claim (1), the operating capacity of the compressor (1) is maximized and the suction pressure equivalent saturation temperature and its target value are set by the opening degree restricting means (53). When the difference between and exceeds a predetermined value, the user-side electric expansion valve (6)
Is limited so that the intake pressure equivalent saturation temperature is about to deviate from the target value because there is not enough capacity, the capacity distribution to the use side heat exchanger (6) As a result, the reduction of the cold storage heat capacity on the heat storage heat exchanger (12) side is suppressed. Therefore, claim (1)
The invention of can be effectively implemented.

請求項(3)の発明では、上記請求項(1)又は(2)
の発明に加えて、最大開度増大手段(54)により、圧縮
器(1)の運転容量が一定値以下のときには、利用側電
動膨張弁(6)の最大開度が増大するよう変更されるの
で、能力に余裕がある場合、室内側への能力の分配制限
が緩和され、所定の冷房要求に応えることができる。し
たがって、上記請求項(1)又は(2)の発明に加え
て、冷房能力が確保されることになる。
In the invention of claim (3), the above claim (1) or (2)
In addition to the invention described above, the maximum opening degree increasing means (54) changes the maximum opening degree of the use-side electric expansion valve (6) to increase when the operating capacity of the compressor (1) is below a certain value. Therefore, when the capacity is sufficient, the restriction on the distribution of the capacity to the indoor side is relaxed, and a predetermined cooling request can be met. Therefore, in addition to the invention of claim (1) or (2), the cooling capacity is secured.

(実施例) 以下、本発明の実施例について、第2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2図は本発明の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),…が接続されたいわゆるマルチ形
空気調和装置である。
FIG. 2 shows an overall configuration of an air conditioner according to an embodiment of the present invention, in which a plurality of indoor units (A), (B), ... Are connected to an outdoor unit (X), a so-called multi-type air. It is a harmony device.

上記室外ユニット(X)において、(1)はインバータ
(41)により運転周波数を可変に調節される容量可変形
の圧縮機、(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たる室外
熱交換器、(4)は冷房運転時には冷房流量を調節し、
暖房運転時には冷媒の減圧弁として機能する室外電動膨
張弁、(5)は冷媒量を調節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 variable capacity compressor in which the operating frequency is variably adjusted by the inverter (41), and (2) is switched as shown by the solid line in the figure during the cooling operation, and during the heating operation. A four-way switching valve that switches as shown by the broken line in the figure, (3) is an outdoor heat exchanger that is a heat source side heat exchanger that functions as a condenser during cooling operation, and as an evaporator during heating operation, and (4) is cooling during cooling operation. Adjust the flow rate,
An outdoor electric expansion valve that functions as a refrigerant pressure reducing valve during heating operation, (5) a receiver for adjusting the amount of refrigerant,
(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弁として機能し、暖
房運転時には冷媒流量を調節する利用側電動膨張弁たる
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
器たる室内熱交換器である。
On the other hand, each of the indoor units (A), (B), ... Has the same configuration, and (6) functions as a pressure reducing valve during the cooling operation and is an indoor electric motor that is a use-side electric expansion valve that adjusts the refrigerant flow rate during the heating operation. The expansion valve (7) is an indoor heat exchanger that is a utilization side heat exchanger that functions as an evaporator during cooling operation and 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とヒートポ
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 by a refrigerant pipe (9) so that the refrigerant can flow therethrough, and have a heat pump action when the heat obtained by heat exchange with the outdoor air is released 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、蓄暖熱をし、或いはその蓄冷
熱、蓄断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、それぞれ冷媒の流通可能
に接続されている。そして、上記第1バイパス路(13
a)には、水(W)に冷熱を蓄える蓄冷熱時に冷媒を減
圧する蓄熱電動膨張弁(14)が介設され、上記第2バイ
パス路(13b)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 storing cold heat or warm heat by exchanging heat with the refrigerant flowing through the main refrigerant circuit (10) or for utilizing the cold heat or heat storage is arranged. Has been done. 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),
A heat storage heat exchanger for exchanging heat between water (W) and a refrigerant, the heat storage heat exchanger (12) and the outdoor electric expansion valve (4) of the main refrigerant circuit (10) -indoor electric expansion The first bypass passage (13a) and the second bypass passage (13b) are connected to the liquid line (9a) between the valves (6) so that the refrigerant can flow therethrough. Then, the first bypass path (13
A heat storage electric expansion valve (14) for decompressing the refrigerant when cold heat is stored in water (W) is provided in a), and the second bypass path (13b) is provided with a second bypass path (13b). A first on-off valve (15) for opening and closing is installed.

また、第2バイパス路(13a)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 (13a)
− 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.

すなわち、蓄冷熱運転時、液冷媒を主冷媒回路(10)か
ら上記第1バイパス路(13a)にバイパスさせて蓄熱電
動膨張弁(14)で減圧し、蓄熱熱交換器(12)で蒸発さ
せることにより、水(W)に冷熱を付与して製氷するよ
うになされている。
That is, during the cold heat storage operation, the liquid refrigerant is bypassed from the main refrigerant circuit (10) to the first bypass passage (13a), decompressed by the heat storage electric expansion valve (14), and evaporated by the heat storage heat exchanger (12). As a result, cold heat is applied to the water (W) to make ice.

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)が介設されていて、以上の各弁(2),(4),
(6)(14),(15),(16),(17)の開閉もしくは
開度の調節により、各運転モードに応じて冷媒の循環経
路の切換えを行うようにしている。
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, and the above valves (2), (4),
(6) By switching the opening / closing of (14), (15), (16), (17) or adjusting the opening, the circulation path of the refrigerant is switched according to each operation mode.

また、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
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側圧力、冷房サイクル
時には吸入圧力相当飽和温度Teを検出する飽和温度検出
手段としての圧力センサ、(Cl)は蓄熱槽(11)の水面
付近に配置され、水位を検出することにより現在の蓄冷
熱量Qnを検出する蓄冷量検出手段としての水位センサで
ある。
Further, sensors are arranged in the device, (Thw) is arranged in the water of the heat storage tank (11), a water temperature sensor for detecting the water temperature Tw, and (Tha) is air of the outdoor heat exchanger (3). An outside air temperature sensor, which is arranged at the suction port and detects the outside air temperature Ta,
(Thi) is a cooling inlet sensor arranged on the upstream side of the junction of the liquid line (9a) with the second bypass passage (13b) during cooling operation, and (Tho) is the first bypass passage of the liquid line (9a). A cooling outlet sensor arranged on the downstream side of the joint portion with (13a) during cooling operation, (Ths) is a suction pipe sensor for detecting a suction pipe temperature, and (SP) is arranged in a gas line (9b). , A pressure sensor as a saturation temperature detecting means for detecting a high pressure side pressure during a heating cycle and a suction temperature equivalent saturation temperature Te during a cooling cycle, (Cl) is arranged near the water surface of the heat storage tank (11) to detect the water level Is a water level sensor as a cool storage amount detecting means for detecting the current cool storage heat amount Qn.

また、上記蓄熱槽(11)には、第3図に示すように、蓄
熱槽(11)内の水(W)の交換時等に蓄熱槽(11)内の
給水制御を行うための給水装置が設けられていて、(3
1)は、蓄熱槽(11)の上方に開口する給水口(31a)を
有し、該給水口(31a)から蓄熱槽(11)に水(W)を
供給する給水管、(32)は通常開けられた状態にある該
給水管(31)の手動開閉弁、(33)は蓄熱槽(11)から
水(W)を排出する排水管、(34)は通常閉じられ、蓄
熱槽(11)内の水(W)の交換時のみ開かれる排水弁、
(35)は蓄熱槽(11)のオーバーフロー管、(36)はそ
のドレンピット、(37)は上記給水管(31)からの水
(W)の供給を制御するための給水弁であって、該給水
弁(37)は、上記給水管(31)から蓄熱槽(11)に水
(W)を供給するときに、蓄熱槽(11)内の水位が所定
の基準水位になるまで開かれ、基準水位に達すると閉じ
られるものである。また、上記給水時、水位が過上昇し
たときはオーバーフロー管(35)から過剰な水(W)を
排出するようになされている。
Further, as shown in FIG. 3, the heat storage tank (11) has a water supply device for controlling water supply in the heat storage tank (11) when the water (W) in the heat storage tank (11) is replaced. Is provided, and (3
1) has a water supply port (31a) opened above the heat storage tank (11), and a water supply pipe (32) for supplying water (W) from the water supply port (31a) to the heat storage tank (11), A manual opening / closing valve of the water supply pipe (31) which is normally opened, (33) a drain pipe for discharging water (W) from the heat storage tank (11), and (34) normally closed and the heat storage tank (11). Drainage valve that is opened only when the water (W) in
(35) is an overflow pipe of the heat storage tank (11), (36) is its drain pit, (37) is a water supply valve for controlling the supply of water (W) from the water supply pipe (31), When supplying water (W) from the water supply pipe (31) to the heat storage tank (11), the water supply valve (37) is opened until the water level in the heat storage tank (11) reaches a predetermined reference water level, It is closed when the standard water level is reached. Further, when the water level rises excessively during the water supply, excess water (W) is discharged from the overflow pipe (35).

そして、上記排水弁(34)及び給水弁(37)は、装置の
運転を制御するコントローラ(40)の信号線で接続され
ていて、蓄熱槽(11)の蓄冷熱を利用する回数が一定値
に達すると、自動的に排水弁(34)を開き、蓄熱槽(1
1)内の水(W)を排出する一方、その排水開始から一
定時間が経過すると排水が完了したと判断して、上述の
ような給水弁(37)の開閉制御により蓄熱槽(11)に給
水を行い、蓄熱槽(11)内の水(W)を交換することに
より、水(W)の汚れ等による蓄冷熱機能の悪化を防止
するようになされている。つまり、自動的にメインテナ
ンスを行うことにより、使用中における水(W)の交換
忘れの防止と、水交換のための手間の省略とを図るよう
にしている。
The drain valve (34) and the water supply valve (37) are connected by a signal line of a controller (40) that controls the operation of the device, and the number of times the cold storage heat of the heat storage tank (11) is used is a constant value. When it reaches, the drain valve (34) is automatically opened and the heat storage tank (1
While discharging the water (W) in 1), it is judged that the drainage is completed after a certain time has passed from the start of drainage, and the open / close control of the water supply valve (37) controls the heat storage tank (11). By supplying water and replacing the water (W) in the heat storage tank (11), deterioration of the cold heat storage function due to contamination of the water (W) or the like is prevented. In other words, by automatically performing maintenance, it is possible to prevent forgetting to replace the water (W) during use and to save labor for water replacement.

ここで、各運転モードにおける冷媒の循環経路について
説明する。上記空気調和装置において、氷熱利用冷房運
転時には、第2図中実線矢印に示すように、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),
…、第1開閉弁(15)及び蓄熱電動膨張弁(14)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)で凝縮された冷媒が第1,第2バイパス
路(13a),(13b)に流れて蓄熱熱交換器(12)4で冷
却された後、主冷媒回路(10)に戻って各室内電動膨張
弁(6),…で減圧され、各室内熱交換器(7),…で
蒸発して圧縮機(1)に戻るように循環する。
Here, the circulation path of the refrigerant in each operation mode will be described. In the above air conditioner, during the cooling operation using ice heat, the four-way switching valve (2) is switched as shown by the solid line in the figure, as shown by the solid line arrow in FIG. 2, the outdoor electric expansion valve (4), the flow rate. Control valve (17), indoor electric expansion valve (6),
..., the first on-off valve (15) and the heat storage electric expansion valve (14) are opened, the second on-off valve (16) is closed, the operation is performed, and the refrigerant condensed in the outdoor heat exchanger (3) is discharged. After flowing through the first and second bypass passages (13a) and (13b) and being cooled by the heat storage heat exchanger (12) 4, the indoor electric expansion valve (6) returns to the main refrigerant circuit (10). It is decompressed by and is circulated so as to be evaporated in each indoor heat exchanger (7), ... And returned to the compressor (1).

一方、蓄熱槽(11)内の水(W)を製氷して冷熱を蓄え
る製氷運転時には、図中破線矢印に示すように、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(14)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、冷熱を蓄えるようになされている。
On the other hand, during the ice making operation in which water (W) in the heat storage tank (11) is ice-stored to store cold heat, as shown by the broken line arrow in the figure, the outdoor electric expansion valve (4), the flow control valve (17), the heat storage electric The outdoor heat exchanger (3) is operated with the expansion valve (14) and the second opening / closing valve (16) opened, and the indoor electric expansion valves (6), ... And the first opening / closing valve (15) closed. The liquid refrigerant condensed in 1. flows by bypassing the first bypass passage (13a), is decompressed by the heat storage electric expansion valve (14), evaporates in the heat storage heat exchanger (12) and returns to the compressor (1). To circulate. At that time, the heat storage heat exchanger (12) exchanges heat with the refrigerant to make water (W), which is a heat storage medium, into ice to store cold heat.

そして、室内熱交換器(7)による蒸発作用と蓄熱熱交
換器(12)による蓄冷熱作用とを同時に行う冷房及び蓄
冷熱同時運転時には、第1開閉弁(15)のみ閉じた状態
で、運転が行われ、室外熱交換器(3)で凝縮された液
冷媒がレシーバ(5)を通過後主冷媒回路(10)側と第
1バイパス路(13a)側とに分岐し、各熱交換器
(7),…及び(12)でそれぞれ蒸発した後、合流して
圧縮機(1)に戻るよう循環する。
Then, during the simultaneous cooling and cold storage heat operation in which the evaporation action by the indoor heat exchanger (7) and the cold storage heat action by the heat storage heat exchanger (12) are simultaneously performed, the operation is performed with only the first opening / closing valve (15) closed. The liquid refrigerant condensed in the outdoor heat exchanger (3) passes through the receiver (5) and then branches into the main refrigerant circuit (10) side and the first bypass path (13a) side, and each heat exchanger After being evaporated at (7), ... And (12) respectively, they are merged and circulated so as to return to the compressor (1).

ここで、本発明の特徴として、上記冷房及び蓄冷熱同時
運転時におけるコントローラ(40)の制御内容につい
て、第4図のフローチャートに基づき説明するに、ステ
ップS1で所定の第1設定時間TM1が経過するのを待っ
て、ステップS2で、吸入圧力相当飽和温度Teを前回のサ
ンプリングで求めた吸入圧力相当飽和温度Teの目標値
(以下、目標蒸発温度とする)Tesに収束させるべく、
圧縮機(1)の運転容量の制御量ΔFkを下記のように演
算する。
Here, as a feature of the present invention, the control of the controller (40) during the cooling and cold storage heat simultaneous operation, will be described with reference to the flow chart of FIG. 4, the predetermined first set time in step S 1 TM 1 There waiting for the elapse, in step S 2, the target value of the intake pressure corresponding saturation temperature Te of obtaining the suction pressure equivalent saturation temperature Te at the previous sampling (hereinafter, the target evaporation temperature) in order to converge to Tes,
The control amount ΔFk of the operating capacity of the compressor (1) is calculated as follows.

すなわち、e(t)=Te−Tes、Δtcをサンプリングタ
イム、Kcをゲイン、Tiを積分時間として、下記式 ΔFk=Kc[{e(t)−e(t−Δtc} +(Δtc/2Ti){e(t)+e(t−Δtc)}] により算出する。ただし、上記積分時間Tiは、下記のよ
うに設定されている。
That is, e (t) = Te−Tes, Δtc is a sampling time, Kc is a gain, and Ti is an integration time, and the following equation ΔFk = Kc [{e (t) −e (t−Δtc} + (Δtc / 2Ti) {E (t) + e (t-Δtc)}], where the integration time Ti is set as follows.

(i) |e(t)|<e1のとき Ti=∞ ただし、e1=−0.005Ft+1.65 (ii) |e(t)|>10degのとき Ti=5sec (iii) e1≦|e(t)|≦10degのとき Ti=60−(22/3)(|e(t)|−2.5) ただし、Fkの下限値Fkmin=50Hz 次に、ステップS3で、下記式のように、圧縮機(1)の
新容量Fkを、前回サンプリング時における圧縮機(1)
の運転容量Fk(t−Δtc)と上記圧縮機(1)の容量変
更量ΔFkとの和として設定制御する。
(I) | e (t) | <e 1 Ti = ∞ However, when e 1 = −0.005Ft + 1.65 (ii) | e (t) |> 10deg Ti = 5sec (iii) e 1 ≤ | When e (t) | ≦ 10deg Ti = 60− (22/3) (| e (t) | −2.5) However, the lower limit value of Fk Fkmin = 50Hz Next, in step S 3 , , The new capacity Fk of the compressor (1), the compressor (1) at the time of the previous sampling
The setting control is performed as the sum of the operating capacity Fk (t-Δtc) of the above and the capacity change amount ΔFk of the compressor (1).

Fk(t)=Fk(t−Δtc)+ΔFk 次に、上記制御を行った後、ステップS4で、上記第1設
定時間TM1よりも長い所定の第2設定時間TM2が経過する
のを待って、ステップS5で、下記手順により吸入圧力相
当飽和温度Teの目標値Tesを演算する。
Fk (t) = Fk (t−Δtc) + ΔFk Next, after performing the above control, in step S 4 , a predetermined second set time TM 2 longer than the first set time TM 1 is passed. After waiting, in step S 5 , the target value Tes of the saturation pressure equivalent saturation temperature Te is calculated by the following procedure.

すなわち、上記水位センサ(Cl)で検出される蓄冷熱量
をQn、目標蓄冷熱量をQs、残された蓄冷熱運転時間をTM
cとすると、単位時間当たりの必要蓄冷熱能力Qrは、下
記式 Qr=(Qs−Qn)/TMc (1) で表される。
That is, Qn is the amount of cold storage heat detected by the water level sensor (Cl), Qs is the target amount of cold storage heat, and TM is the remaining cold storage heat operation time.
If it is c, the required cold storage heat capacity Qr per unit time is expressed by the following equation Qr = (Qs-Qn) / TMc (1).

一方、水温をTw、蓄熱熱交換器(12)における蒸発圧力
相当飽和温度をTewとすると、蓄熱熱交換器(12)の蓄
冷熱能力Qは、下記式 Q=C1・(Tw−Tew) (2) で表される(ただし、C1所定の定数で温度を能力のディ
メンジョンに変換するものである)。
On the other hand, when the water temperature is Tw and the saturation temperature equivalent to the evaporation pressure in the heat storage heat exchanger (12) is Tew, the cold storage heat capacity Q of the heat storage heat exchanger (12) is expressed by the following formula Q = C 1 · (Tw−Tew) It is represented by (2) (however, the temperature is converted into the dimension of capacity with a constant of C 1 ).

また、吸入圧力相当飽和温度Teが目標蒸発温度値Tesに
制御されたものとした場合、Tesと蓄熱熱交換器(12)
における蒸発圧力相当飽和温度Tewとの間には、途中の
配管の圧力損失を考慮すると、下記式 Tes=Tew−C2・Ft (3) の関係が成立する。
When the suction pressure equivalent saturation temperature Te is controlled to the target evaporation temperature value Tes, Tes and the heat storage heat exchanger (12)
In consideration of the pressure loss of the pipe in the middle, the following equation Tes = Tew−C 2 · Ft (3) is established between the vaporization pressure equivalent saturation temperature Tew in Eq.

したがって、上記(1)〜(3)式から Tes={Tw−(Qs−Qn)/TMc}/C1−C2・Ft (4) となり、水温Tw、現在蓄冷熱量Q、圧縮機(1)の運転
容量Ftから、目標蒸発温度値Tesが演算される。
Therefore, from the above equations (1) to (3), Tes = {Tw− (Qs−Qn) / TMc} / C 1 −C 2 · Ft (4), and the water temperature Tw, the current cold storage heat quantity Q, the compressor (1 ), The target evaporation temperature value Tes is calculated from the operating capacity Ft.

そして、上記ステップS5の制御により目標蒸発温度値Te
sを演算すると、ステップS6で、上記第2設定時間TM2
りも長い所定の第3設定時間TM3が経過するのを待っ
て、ステッフS7に進み、ステップS7で、吸入圧力相当飽
和温度Teが上記目標蒸発温度Tesに収束するよう室内電
動膨張弁(6)の開度を制御する。
Then, the target evaporation temperature value Te under the control of the step S 5
When calculating the s, in step S 6, waits for the second set third set time TM 3 longer predetermined than the time TM 2 has elapsed, the process proceeds to stiff S 7, at step S 7, the suction pressure equivalent The opening degree of the indoor electric expansion valve (6) is controlled so that the saturation temperature Te converges on the target evaporation temperature Tes.

すなわち、Te−Tes≧C3(C3は定数)のときには、室内
電動膨張弁(6)の最大開度値Amaxを1ステップ(例え
ば50パルス程度の値)下げ、室内電動膨張弁(6)の開
度を制限する。一方、圧縮機(1)の運転容量Fkに対
し、Ft≦C4(C4は例えば110Hz程度の定数)のときに
は、室内電動膨張弁(6)の最大開度値Amaxを1ステッ
プ上げるよう設定して、開度の制限を緩和する。なお、
上記制御は、所定のサンプリングタイム(例えば2分間
程度の時間)毎に行うようになされている。
That is, when Te−Tes ≧ C 3 (C 3 is a constant), the maximum opening value Amax of the indoor electric expansion valve (6) is lowered by one step (for example, a value of about 50 pulses) to increase the indoor electric expansion valve (6). Limit the opening. On the other hand, when the operating capacity Fk of the compressor (1) is Ft ≤ C 4 (C 4 is a constant of, for example, about 110 Hz), the maximum opening value Amax of the indoor electric expansion valve (6) is set to be increased by one step. Then, the restriction on the opening is relaxed. In addition,
The above control is performed at every predetermined sampling time (for example, about 2 minutes).

上記フローにおいて、ステップS2及びS3により、吸入圧
力相当飽和温度Teが目標値Tesに収束するよう上記圧縮
機(1)の運転容量を設定制御する容量制御手段(51)
が構成され、ステップS5より、圧縮機(1)の前回サン
プリング時における運転容量に基づき、蓄熱熱交換器
(12)における蓄冷熱能力が上記蓄熱槽(11)の目標蓄
冷熱量Qsと現在蓄冷熱量Qnとの差から求まる必要蓄冷熱
能力Qrになるよう吸入圧力相当飽和温度Teの目標値Tes
を演算する目標値演算手段(52)が構成され、ステップ
S7により、上記吸入圧力相当飽和温度Teが上記目標値演
算手段(52)で算出される目標値Tesに収束するよう上
記利用側電動膨張弁(6)の開度を制限する開度制限手
段(53)が構成されている。
In the above flow, the capacity control means (51) for setting and controlling the operating capacity of the compressor (1) by steps S 2 and S 3 so that the suction pressure equivalent saturation temperature Te converges to the target value Tes.
From step S 5 , based on the operating capacity of the compressor (1) at the time of the previous sampling, the cold storage heat capacity of the heat storage heat exchanger (12) is the target cold storage heat quantity Qs of the heat storage tank (11) and the current cold storage capacity. Target value Tes of saturation temperature Te equivalent to suction pressure Te so that the required cold heat storage capacity Qr can be obtained from the difference with the heat quantity Qn
Target value calculation means (52) for calculating
An opening degree limiting means for limiting the opening degree of the use side electric expansion valve (6) so that the suction pressure equivalent saturation temperature Te converges to the target value Tes calculated by the target value calculating means (52) by S 7. (53) is configured.

また、請求項(2)の発明において、上記ステップS7
制御により、圧縮機(1)の現在の運転容量が増大で、
かつ吸入圧力相当飽和温度Teの現在値と目標値Tesとの
差が所定値以上のときには、利用側電動膨張弁(6)の
最大開度値Amaxを1ステップ低減する開度制限手段(5
3)の機能が構成されている。
Further, in the invention of claim (2), under the control of the step S 7, the current operating capacity of the compressor (1) is increased,
Further, when the difference between the current value of the saturation temperature Te corresponding to the suction pressure Te and the target value Tes is equal to or more than a predetermined value, the opening degree limiting means (5 that reduces the maximum opening value Amax of the use side electric expansion valve (6) by one step.
The function of 3) is configured.

さらに、請求項(3)の発明において、ステップS7の制
御により、圧縮機(1)の運転容量Fkが一定値以下のと
きには利用側電動膨張弁(6)の最大開度値Amaxを1ス
テップ増大させる最大開度増大手段(54)が構成されて
いる。
Further, in the invention of claim (3), the control of step S 7, 1 step a maximum opening value Amax of the usage-side motor-operated expansion valve (6) when the operating capacity Fk is equal to or less than a predetermined value of the compressor (1) The maximum opening increasing means (54) for increasing the opening degree is configured.

したがって、請求項(1)の発明では、所定の設定時間
(サンプリングタイム)毎に、容量制御手段(51)によ
り、圧力センサ(飽和温度検出手段)(SP)で検出され
る吸入圧力相当飽和温度Teが目標蒸発温度値Tesに収束
するよう圧縮機(1)の運転容量が調節され、目標値演
算手段(52)により、蓄熱熱交換器(12)における蓄冷
熱能力Qが必要蓄冷熱能力Qrになるよう目標蒸発温度Te
sが演算される。そして、開度制限手段(53)により、
吸入圧力相当飽和温度Teが目標蒸発温度Tesに収束する
よう室内電動膨張弁(6)の開度が制限される。
Therefore, in the invention of claim (1), the suction pressure equivalent saturation temperature detected by the pressure sensor (saturation temperature detection means) (SP) by the capacity control means (51) at every predetermined set time (sampling time). The operating capacity of the compressor (1) is adjusted so that Te converges to the target evaporation temperature value Tes, and the target value calculation means (52) requires the cold storage heat capacity Q in the heat storage heat exchanger (12). Target evaporation temperature Te
s is calculated. Then, by the opening degree limiting means (53),
The opening degree of the indoor electric expansion valve (6) is limited so that the suction pressure equivalent saturation temperature Te converges to the target evaporation temperature Tes.

すなわち、吸入圧力相当飽和温度Teの値が必要な蓄冷熱
能力Qrを維持しうる値から外れないように制御されるの
で、夜間等に蓄冷熱運転を行っているとき、冷房要求が
なされても、予定の蓄冷熱を確実に確保しながら、冷房
要求に応じた冷房運転を行うこともできる。しかも、そ
の間、吸入圧力相当飽和温度Teが目標値Tesに収束する
よう圧縮器(1)の運転容量が制御されるので、必要な
能力以上の運転を回避することができ、いわゆるCOP
(成績係数)の向上を得ることができる。よって、蓄冷
熱量の確保と全体としての運転効率の向上とを図ること
ができるのである。
That is, since the value of the saturation pressure Te equivalent saturation temperature Te is controlled so as not to deviate from the value capable of maintaining the required cold storage heat capacity Qr, even if a cooling request is made during cold storage operation at night or the like. It is also possible to perform the cooling operation in accordance with the cooling request while surely ensuring the scheduled cold storage heat. Moreover, during that time, since the operating capacity of the compressor (1) is controlled so that the suction pressure-equivalent saturation temperature Te converges to the target value Tes, it is possible to avoid an operation exceeding the required capacity.
(Coefficient of performance) can be improved. Therefore, it is possible to secure the amount of cold storage heat and improve the operation efficiency as a whole.

請求項(2)の発明では、上記請求項(1)の発明にお
いて、開度制限手段(53)により、圧縮機(1)の運転
容量が最大で、かつ吸入圧力相当飽和温度Teと目標蒸発
温度Tesの差(Te−Tes)が所定値以上になると、室内電
動膨張弁(6)の開度を1ステップ低減するよう制御さ
れるので、能力に余裕がないために吸入圧力相当飽和温
度Teが目標蒸発温度Tesから外れるようとする場合に
は、室内熱交換器(6)への能力の分配が減少し、その
結果、蓄熱熱交換器(12)の蓄冷熱能力の必要能力以下
への低下が抑制さえることになる。よって、請求項
(1)の発明の実効を図ることができるのである。
According to the invention of claim (2), in the invention of claim (1), the operating capacity of the compressor (1) is maximized by the opening degree restricting means (53), and the suction pressure equivalent saturation temperature Te and the target evaporation are increased. When the difference (Te-Tes) between the temperatures Tes exceeds a predetermined value, the opening degree of the indoor electric expansion valve (6) is controlled to be reduced by one step. If the temperature is to deviate from the target evaporating temperature Tes, the distribution of the capacity to the indoor heat exchanger (6) decreases, and as a result, the cool storage heat capacity of the heat storage heat exchanger (12) falls below the required capacity. The decline will be suppressed. Therefore, the invention of claim (1) can be realized.

請求項(3)の発明では、上記請求項(1)又は(2)
の発明に加えて、最大開度増大手段(54)により、圧縮
機(1)の運転容量が一定値以下のときには、室内電動
膨張弁(6)の最大開度値Amaxが増大するよう変更され
るので、能力に余裕がある場合、室内側への能力の分配
制限が緩和され、所定の冷房要求に応えることができ
る。したがって、上記請求項(1)又は(2)の発明に
加えて、冷房能力を確保できる効果がある。
In the invention of claim (3), the above claim (1) or (2)
In addition to the invention described above, the maximum opening degree increasing means (54) changes the maximum opening degree value Amax of the indoor electric expansion valve (6) to increase when the operating capacity of the compressor (1) is below a certain value. Therefore, when the capacity is sufficient, the restriction on the distribution of the capacity to the indoor side is relaxed, and a predetermined cooling request can be met. Therefore, in addition to the invention of claim (1) or (2), there is an effect that the cooling capacity can be secured.

なお、上記実施例では、室内熱交換器(7),…が複数
台配置されたいわゆるマルチ形空気調和装置について説
明したが、本発明は一台の室内熱交換器のみ備えたペア
タイプのものについても適用しうる。ただし、特にマル
チ形空気調和装置で夜間の蓄例熱中に、少数の室内ユニ
ット(A),…で冷房要求があるような場合に著効を得
ることができる。
In the above embodiment, a so-called multi-type air conditioner in which a plurality of indoor heat exchangers (7), ... Are arranged has been described, but the present invention is of a pair type having only one indoor heat exchanger. Can also be applied. However, particularly in a multi-type air conditioner, a remarkable effect can be obtained when there is a demand for cooling in a small number of indoor units (A), ...

(発明の効果) 以上説明したように、請求項(1)の発明によれば、蓄
熱槽を配置した蓄熱式空気調和装置の運転制御装置とし
て、冷房及び蓄冷熱同時運転時、吸入圧力相当飽和温度
がその目標値に収束するよう圧縮機の運転容量を制御す
る一方、現在の蓄冷熱量から必要な蓄冷熱量を演算し
て、その蓄冷熱量を確保するのに必要な蓄熱熱交換器の
能力から吸入圧力相当飽和温度の目標値を演算するとと
もに、吸入圧力相当飽和温度がその目標値に収束するよ
う利用側電動膨張弁の開度を制限するようにしたので、
必要な蓄冷熱を確保しながら、冷房要求に応えることが
でき、よって、蓄冷熱量の確保と全体としての運転効率
の向上とを図ることができる。
(Effect of the invention) As described above, according to the invention of claim (1), as the operation control device of the heat storage type air conditioner in which the heat storage tank is arranged, the suction pressure equivalent saturation is achieved during the simultaneous operation of cooling and cold storage heat. While controlling the operating capacity of the compressor so that the temperature converges to its target value, the required amount of cold storage heat is calculated from the current amount of cold storage heat, and the capacity of the heat storage heat exchanger necessary to secure that amount of cold storage heat is used. Since the target value of the saturation pressure equivalent saturation temperature is calculated, the opening of the use-side electric expansion valve is limited so that the intake pressure equivalent saturation temperature converges to the target value.
It is possible to meet the cooling demand while securing the required cold storage heat, and thus it is possible to secure the amount of cold storage heat and improve the operation efficiency as a whole.

請求項(2)の発明によれば、上記請求項(1)の発明
において、圧縮機の運転容量が最大で、かつ吸入圧力相
当飽和温度とその目標値との差が所定値以上のときには
利用側電動膨張弁の最大開度値を低減するようにしたの
で、全体としての能力に余裕がない場合、利用側熱交換
器側の能力を制限することで蓄熱熱交換器の能力を確保
することができ、よって、請求項(1)の発明の実効を
図ることができる。
According to the invention of claim (2), in the invention of claim (1), when the operating capacity of the compressor is maximum and the difference between the suction pressure equivalent saturation temperature and its target value is equal to or more than a predetermined value, it is used. Since the maximum opening value of the side electric expansion valve has been reduced, if the overall capacity is insufficient, the capacity of the heat storage heat exchanger should be secured by limiting the capacity of the heat exchanger on the use side. Therefore, the invention of claim (1) can be achieved.

請求項(3)の発明によれば、上記請求項(1)又は
(2)の発明に加えて、圧縮機の運転容量が一定値以下
のときには利用側電動膨張弁の最大開度値を増大するよ
うにしたので、能力に余裕がある場合、利用側熱交換器
の能力制限を緩和することができ、よって、上記請求項
(1)又は(2)の発明の効果に加えて、冷房能力を有
効に確保できる利点がある。
According to the invention of claim (3), in addition to the invention of claim (1) or (2), the maximum opening value of the use side electric expansion valve is increased when the operating capacity of the compressor is equal to or less than a certain value. Therefore, when there is a margin in the capacity, the capacity limitation of the heat exchanger on the utilization side can be relaxed. Therefore, in addition to the effect of the invention of claim (1) or (2), the cooling capacity can be increased. There is an advantage that can be effectively secured.

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

第1図は発明の構成を示すブロック図である。第2図以
下は本発明の実施例を示し、第2図は蓄熱式空気調和装
置の構成を示す冷媒配管系統図、第3図は蓄熱槽の構造
及び給排水配管構成を示す縦断面図、第4図はコントロ
ーラの制御内容を示すフローチャート図である。 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(利用側電動膨張弁) 7……室内熱交換器(利用側熱交換器) 10……主冷媒回路 11……蓄熱槽 12……蓄熱熱交換器 51……容量制御手段 52……目標値演算手段 53……開度制限手段 54……最大開度増大手段 Cl……水位センサ(蓄冷量検出手段) SP……圧力センサ(飽和温度検出手段)
FIG. 1 is a block diagram showing the configuration of the invention. 2 and the following show an embodiment of the present invention, FIG. 2 is a refrigerant piping system diagram showing a configuration of a heat storage type air conditioner, FIG. 3 is a longitudinal sectional view showing a structure of a heat storage tank and a water supply / drainage pipe configuration, FIG. 4 is a flow chart showing the control contents of the controller. 1 …… Compressor 3 …… Outdoor heat exchanger (heat source side heat exchanger) 6 …… Indoor electric expansion valve (use side electric expansion valve) 7 …… Indoor heat exchanger (use side heat exchanger) 10 …… Main refrigerant circuit 11 …… Heat storage tank 12 …… Heat storage heat exchanger 51 …… Capacity control means 52 …… Target value calculation means 53 …… Opening restriction means 54 …… Maximum opening increase means Cl …… Water level sensor (cold storage Quantity detection means) SP ... Pressure sensor (saturation temperature detection means)

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】容量可変形圧縮機(1)、熱源側熱交換器
(3)、利用側電動膨張弁(6)及び利用側熱交換器
(7)を順次接続してなる冷媒回路(10)と、冷熱の蓄
熱可能な蓄熱媒体(W)を有する蓄熱槽(11)と、上記
冷媒回路(10)の冷媒との熱交換により上記蓄熱槽(1
1)に冷熱を付与する蓄熱熱交換器(12)とを備えた蓄
熱式空気調和装置において、 冷媒の吸入圧力相当飽和温度を検出する飽和温度検出手
段(SP)と、所定時間毎に、該飽和温度検出手段(SP)
で検出される吸入圧力相当飽和温度がその目標値に収束
するよう上記圧縮機(1)の運転容量を設定制御する容
量制御手段(51)を備えるとともに、 利用側熱交換器(7)側による蒸発作用と蓄熱熱交換器
(12)による蓄冷熱作用とを同時に行う冷房及び蓄冷熱
同時運転時、上記蓄熱槽(11)内の蓄熱媒体(W)の現
在蓄冷熱量を検出する蓄冷量検出手段(Cl)と、該蓄冷
量検出手段(Cl)の出力を受け、上記容量制御手段(5
1)で制御される圧縮機(1)の前回サンプリング時に
おける運転容量に基づき、蓄熱熱交換器(12)における
蓄冷熱能力が上記蓄熱槽(11)の目標蓄冷熱量と現在蓄
冷熱量との差から求まる必要蓄冷熱能力になるよう吸入
圧力相当飽和温度の目標値を演算する目標値演算手段
(52)と、上記吸入圧力相当飽和温度が該目標値演算手
段(52)で算出される目標値に収束するよう上記利用側
電動膨張弁(6)の開度を制限する開度制限手段(53)
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 refrigerant circuit (10) comprising a variable capacity compressor (1), a heat source side heat exchanger (3), a use side electric expansion valve (6) and a use side heat exchanger (7), which are sequentially connected. ), A heat storage tank (11) having a heat storage medium (W) capable of storing cold heat, and heat exchange between the refrigerant in the refrigerant circuit (10) and the heat storage tank (1).
In a heat storage type air conditioner equipped with a heat storage heat exchanger (12) for applying cold heat to 1), a saturation temperature detecting means (SP) for detecting a saturation temperature equivalent to a suction pressure of a refrigerant, and a predetermined temperature Saturation temperature detection means (SP)
The intake pressure-equivalent saturation temperature detected by the above is provided with a capacity control means (51) for setting and controlling the operating capacity of the compressor (1) so as to converge to its target value, and by the use side heat exchanger (7) side. A cool storage amount detecting means for detecting the current cool storage heat amount of the heat storage medium (W) in the heat storage tank (11) during the simultaneous cooling and heat storage operation for simultaneously performing the evaporation operation and the cold storage heat operation by the heat storage heat exchanger (12). (Cl) and the output of the cold storage amount detecting means (Cl), the capacity control means (5
Based on the operating capacity of the compressor (1) controlled in 1) at the previous sampling, the cold storage heat capacity of the heat storage heat exchanger (12) is the difference between the target cold storage heat amount of the heat storage tank (11) and the current cold storage heat amount. Target value calculating means (52) for calculating a target value of the saturation pressure equivalent saturation temperature so as to obtain the required cold storage heat capacity obtained from the above, and a target value for calculating the suction pressure equivalent saturation temperature by the target value calculating means (52). Opening limit means (53) for limiting the opening of the use-side electric expansion valve (6) so as to converge to
An operation control device for a heat storage type air conditioner, comprising:
【請求項2】開度制限手段(53)は、圧縮器(1)の現
在の運転容量が最大で、かつ吸入圧力相当飽和温度の現
在値と目標値との差が所定値以上のときには、利用側電
動膨張弁(6)の最大開度値を低減するものであること
を特徴とする請求項(1)記載の蓄熱式空気調和装置の
運転制御装置。
2. The opening degree limiting means (53), when the current operating capacity of the compressor (1) is maximum and the difference between the current value of the saturation temperature equivalent to the suction pressure and the target value is a predetermined value or more, The operation control device for a heat storage type air conditioner according to claim 1, wherein the maximum opening value of the use side electric expansion valve (6) is reduced.
【請求項3】圧縮機(1)の運転容量が一定値以下のと
きに、利用側電動膨張弁(6)の最大開度値を増大させ
るよう変更する最大開度増大手段(54)を備えたことを
特徴とする請求項(1)又は(2)記載の蓄熱式空気調
和装置の運転制御装置。
3. A maximum opening increasing means (54) for changing the maximum opening value of the use side electric expansion valve (6) when the operating capacity of the compressor (1) is below a certain value. The operation control device for the heat storage type air conditioner according to claim 1 or 2.
JP1323593A 1989-12-13 1989-12-13 Operation control device for heat storage type air conditioner Expired - Fee Related JPH0784964B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1323593A JPH0784964B2 (en) 1989-12-13 1989-12-13 Operation control device for heat storage type air conditioner

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1323593A JPH0784964B2 (en) 1989-12-13 1989-12-13 Operation control device for heat storage type air conditioner

Publications (2)

Publication Number Publication Date
JPH03186160A JPH03186160A (en) 1991-08-14
JPH0784964B2 true JPH0784964B2 (en) 1995-09-13

Family

ID=18156439

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1323593A Expired - Fee Related JPH0784964B2 (en) 1989-12-13 1989-12-13 Operation control device for heat storage type air conditioner

Country Status (1)

Country Link
JP (1) JPH0784964B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPWO2019176099A1 (en) * 2018-03-16 2021-01-07 三菱電機株式会社 Air conditioner

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003028520A (en) * 2001-07-19 2003-01-29 Hitachi Ltd Thermal storage refrigeration system
JP5464947B2 (en) * 2009-09-02 2014-04-09 三菱電機株式会社 Thermal storage control method for ice thermal storage unit
JP2024173281A (en) * 2023-06-02 2024-12-12 三菱重工業株式会社 Cooling system, cooling method, and program

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPWO2019176099A1 (en) * 2018-03-16 2021-01-07 三菱電機株式会社 Air conditioner

Also Published As

Publication number Publication date
JPH03186160A (en) 1991-08-14

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