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JP2008286474A - Cooling storage and its operation method - Google Patents

Cooling storage and its operation method Download PDF

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JP2008286474A
JP2008286474A JP2007131877A JP2007131877A JP2008286474A JP 2008286474 A JP2008286474 A JP 2008286474A JP 2007131877 A JP2007131877 A JP 2007131877A JP 2007131877 A JP2007131877 A JP 2007131877A JP 2008286474 A JP2008286474 A JP 2008286474A
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refrigerant
target temperature
temperature
compressor
storage
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Naoshi Kondo
直志 近藤
Akihiko Hirano
明彦 平野
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Hoshizaki Electric Co Ltd
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Hoshizaki Electric Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a cooling storage and its operation method capable of performing the stable cooling operation even when set temperatures of storage compartments are close to each other in the cooling storage where the plurality of storage compartments are cooled by one compressor. <P>SOLUTION: This cooling storage comprises the compressor 20 driven by an invertor motor, a condenser 21, electric expansion valves 26A, 26B, evaporators 16A, 16B, a target temperature setting means 55 for setting target temperatures of the storage compartments, inside temperature sensors 51A, 51B detecting inside temperatures of the storage compartments, a compressor rotation control means 51 generating cooling capacity to keep the storage compartment at its target temperatures by controlling the rotational frequency of the compressor on the basis of the deviation between the target temperature set by the target temperature setting means and the inside temperature detected by the inside temperature sensor, and an electric expansion valve control means distributing the refrigerant from the condenser to each of the evaporators by controlling an opening of each of the plurality of electric expansion valves according to the deviation between the target temperature of each storage compartment and the inside temperature. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

本発明は、複数の蒸発器を備え、それらに1台の圧縮機から冷媒を供給する冷却貯蔵庫及びその運転方法に関する。   The present invention relates to a cooling storage that includes a plurality of evaporators and supplies refrigerant from a single compressor to the evaporator, and an operation method thereof.

この種の冷却貯蔵庫としては、断熱性の貯蔵庫本体に例えば冷凍室と冷蔵室とを断熱して区画形成すると共に各室に夫々蒸発器を配置し、これらの蒸発器に1台の圧縮機から冷媒を交互に供給して冷却作用を生じさせるようにしたものが知られており、例えば特許文献1が例示できる。   As this type of cooling storage, for example, a freezing compartment and a refrigeration compartment are insulated and formed in a heat-insulating storage body, and an evaporator is disposed in each chamber, and each evaporator is provided with a single compressor. One in which a coolant is alternately supplied to cause a cooling action is known. For example, Patent Document 1 can be exemplified.

このものは、冷媒を圧縮機によって圧縮すると共に凝縮器により液化し、これを三方弁の出口側にそれぞれキャピラリチューブを介して接続した冷凍室用蒸発器及び冷蔵室用蒸発器に交互に供給するようになっており、設定温度に近い温度域で通常の冷却運転を行っているいわゆるコントロール運転時には、いずれかの貯蔵室がオン温度に達したら圧縮機の運転を開始し、冷却している側の貯蔵室がオフ温度に達したら、三方弁を切り替えて他方側の貯蔵室の冷却モードに切替え、両室の検出温度が共にオフ温度以下になったら圧縮機を停止する。
実開昭60−188982号公報
In this system, the refrigerant is compressed by a compressor and liquefied by a condenser, and this is alternately supplied to a freezer evaporator and a refrigerator refrigerator connected to the outlet side of the three-way valve via a capillary tube, respectively. During the so-called control operation in which the normal cooling operation is performed in a temperature range close to the set temperature, the compressor starts operating when one of the storage chambers reaches the on temperature, and the cooling side When the storage chamber reaches the off temperature, the three-way valve is switched to switch to the cooling mode of the other storage chamber, and the compressor is stopped when the detected temperatures in both chambers are both below the off temperature.
Japanese Utility Model Publication No. 60-188982

しかしながら、上述のように二室の目標温度が、それぞれ冷凍温度域及び冷蔵温度域のように大きく相違する温度域に設定されている場合にはともかく、たとえば共に冷蔵温度域とするような温度設定では、安定的な運転を行い得ないという問題があった。例えば貯蔵室が二室ある場合に、一方の設定温度を5℃、他方の設定温度を3℃に設定したとする。一方の貯蔵室の庫内温度がオン温度を上回ったところで圧縮機が起動し、一方の貯蔵室がオフ温度(オフ温度とオン温度とは通常最低3Kの温度差が必要である)まで冷却されたところで三方弁が他方側の冷却モードに切り替わる。このとき、他方側の貯蔵室がオフ温度になっていれば、圧縮機は運転が継続されることになる。ところが、両貯蔵室の設定温度が近いと、両貯蔵室のコントロール温度が重なり合ってしまうため、細かな設定温度を区別してコントロールすることが困難になるのである。   However, regardless of whether the target temperatures of the two chambers are set to greatly different temperature ranges such as the refrigeration temperature range and the refrigeration temperature range as described above, for example, a temperature setting that sets both to the refrigeration temperature range, for example. Then, there was a problem that stable operation could not be performed. For example, when there are two storage rooms, it is assumed that one set temperature is set to 5 ° C. and the other set temperature is set to 3 ° C. The compressor starts when the internal temperature of one storage room exceeds the on-temperature, and one storage room is cooled to the off-temperature (the temperature difference between the off-temperature and the on-temperature usually requires a minimum of 3K). At this point, the three-way valve switches to the cooling mode on the other side. At this time, if the storage chamber on the other side is at an off temperature, the compressor is continuously operated. However, if the set temperatures of both storage chambers are close, the control temperatures of both storage chambers overlap, making it difficult to distinguish and control the fine set temperatures.

本発明は上記のような事情に基づいて完成されたものであって、一台の圧縮機で複数の貯蔵室を冷却するものでありながら、各貯蔵室の設定温度が近い場合でも、安定的な冷却運転を可能にできる冷却貯蔵庫及びその運転方法を提供することを目的とする。   The present invention has been completed based on the above circumstances, and is capable of stably cooling a plurality of storage rooms with a single compressor even when the set temperatures of the respective storage rooms are close. It is an object of the present invention to provide a cooling storage and a method of operating the same that can perform a cooling operation.

本発明の冷却貯蔵庫は、インバータモータにより駆動される圧縮機と、この圧縮機が圧縮した冷媒から放熱させる凝縮器と、この凝縮器からの冷媒をそれぞれ電動膨張弁を介して流す複数の冷媒供給路と、前記各冷媒供給路に設けた蒸発器と、前記各蒸発器で蒸発した冷媒を合流させて前記圧縮機の吸入側に戻す冷媒環流路と、前記各蒸発器によって生成された冷気によって冷却される複数の貯蔵室と、前記各貯蔵室内の目標温度を設定するための目標温度設定手段と、前記各貯蔵室の庫内温度を検出する庫内温度センサと、前記目標温度設定手段に設定された前記目標温度と前記庫内温度センサにより検出された庫内温度との偏差に基づいて前記圧縮機の回転数を制御することで前記各貯蔵室を前記目標温度に維持するための冷却能力を生じさせる圧縮機回転制御手段と、前記各貯蔵室の前記目標温度と前記庫内温度との各偏差に応じて複数の前記各電動膨張弁の開度を制御することで前記凝縮器からの冷媒を前記各蒸発器に配分する電動膨張弁制御手段とを備えるところに特徴を有する。   The cooling storage of the present invention includes a compressor driven by an inverter motor, a condenser that releases heat from the refrigerant compressed by the compressor, and a plurality of refrigerant supplies that respectively flow the refrigerant from the condenser through an electric expansion valve. Passages, evaporators provided in the respective refrigerant supply paths, refrigerant circulation passages for bringing the refrigerant evaporated in the respective evaporators together and returning them to the suction side of the compressor, and cold air generated by the respective evaporators A plurality of storage chambers to be cooled, target temperature setting means for setting a target temperature in each of the storage chambers, an internal temperature sensor for detecting the internal temperature of each of the storage chambers, and the target temperature setting means Cooling for maintaining each storage chamber at the target temperature by controlling the number of revolutions of the compressor based on the deviation between the set target temperature and the internal temperature detected by the internal temperature sensor Ability A compressor rotation control means for controlling the opening degree of each of the plurality of electric expansion valves according to each deviation between the target temperature of the storage chamber and the internal temperature, and the refrigerant from the condenser is An electric expansion valve control means for distributing to each of the evaporators is provided.

上記構成によれば、電動膨張弁を電動膨張弁制御手段が開度制御することによって冷媒が各貯蔵室の目標温度を維持するように配分制御され、かつ、それを実現するために圧縮機回転制御手段によって各貯蔵室を目標温度に維持するための冷却能力を生じさせるように圧縮機の回転数が制御される。このため、圧縮機のオンオフに依存せずに冷却能力を各貯蔵室向けに配分することができるから、各貯蔵室の設定温度が近くとも安定的な制御を行うことができる。   According to the above configuration, the electric expansion valve control means controls the opening degree of the electric expansion valve so that the refrigerant is distributed and controlled so as to maintain the target temperature of each storage chamber, and in order to realize this, the compressor rotates. The rotation speed of the compressor is controlled by the control means so as to generate a cooling capacity for maintaining each storage chamber at the target temperature. For this reason, since the cooling capacity can be distributed to each storage room without depending on on / off of the compressor, stable control can be performed even if the set temperature of each storage room is close.

上記の圧縮機回転制御手段は、所定時間毎に前記目標温度設定手段に設定された前記目標温度と前記温度センサにより検出された庫内温度との偏差を算出する偏差算出手段と、この偏差算出手段により算出された偏差の積算値を所定の基準値と比較して前記インバータモータの回転数を変化させる回転数制御手段とを備えることが好ましい。   The compressor rotation control means includes a deviation calculation means for calculating a deviation between the target temperature set in the target temperature setting means and the internal temperature detected by the temperature sensor every predetermined time, and the deviation calculation It is preferable that a rotation speed control means for changing the rotation speed of the inverter motor by comparing the integrated value of the deviation calculated by the means with a predetermined reference value.

また、上記の電動膨張弁制御手段は、所定時間毎に前記目標温度設定手段に設定された前記目標温度と前記温度センサにより検出された庫内温度との偏差を算出する偏差算出手段と、前記各貯蔵室毎に前記偏差算出手段により算出された偏差の積算値を所定の基準値と比較して前記積算値が所定の基準値よりも小さい場合に前記電動膨張弁を所定量閉じると共に前記積算値が所定の基準値よりも大きい場合に前記電動膨張弁を所定量開放する制御を行う電動膨張弁比較駆動手段とを備えることが好ましい。   The electric expansion valve control means includes a deviation calculating means for calculating a deviation between the target temperature set in the target temperature setting means and the internal temperature detected by the temperature sensor every predetermined time; The integrated value of the deviation calculated by the deviation calculating means for each storage chamber is compared with a predetermined reference value, and when the integrated value is smaller than the predetermined reference value, the electric expansion valve is closed by a predetermined amount and the integrated It is preferable to provide an electric expansion valve comparison drive means for performing control to open the electric expansion valve by a predetermined amount when the value is larger than a predetermined reference value.

また、圧縮機に吸入される冷媒の過熱度を検出する過熱度検出手段を設け、その過熱度が所定値以下に低下したときに圧縮機の運転を停止することがさらに好ましい。   It is further preferable to provide a superheat degree detecting means for detecting the superheat degree of the refrigerant sucked into the compressor and stop the operation of the compressor when the superheat degree falls below a predetermined value.

本発明の冷却貯蔵庫によれば、一台の圧縮機で複数の貯蔵室を冷却するものでありながら、各貯蔵室の設定温度が近い場合でも、安定的な冷却運転を可能にできる。   According to the cooling storage of the present invention, a plurality of storage chambers are cooled by a single compressor, and a stable cooling operation can be performed even when the set temperatures of the respective storage chambers are close.

<実施形態1>
本発明の実施形態1を図1ないし図6によって説明する。この実施形態1では業務用の横型(テーブル型)冷蔵庫に適用した場合を例示しており、まず図1により全体構造を説明する。符号10は貯蔵庫本体であって、前面に開口した横長の断熱箱体により構成され、底面の四隅に設けられた脚11によって支持されている。貯蔵庫本体10の内部は、後付けされる断熱性の仕切壁12によって内部が左右に仕切られ、左の相対的に狭い側が第1の貯蔵室13A、右の広い側が第2の貯蔵室13Bとなっている。なお、図示はしないが各貯蔵室13A,13Bの前面の開口には揺動式の断熱扉が開閉可能に装着されている。
<Embodiment 1>
A first embodiment of the present invention will be described with reference to FIGS. In this Embodiment 1, the case where it applies to the horizontal type | mold (table type) refrigerator for business is illustrated, First, FIG. 1 demonstrates the whole structure. Reference numeral 10 denotes a storage body, which is composed of a horizontally long heat insulating box that opens to the front surface, and is supported by legs 11 provided at the four corners of the bottom surface. The interior of the storage body 10 is divided into left and right by a heat-insulating partition wall 12 to be retrofitted, and the left relatively narrow side is the first storage chamber 13A, and the right wide side is the second storage chamber 13B. ing. Although not shown, a swinging heat insulating door is attached to the opening of the front surface of each of the storage chambers 13A and 13B so as to be openable and closable.

貯蔵庫本体10の正面から見た左側部には、機械室14が設けられている。機械室14内の上部の奥側には、第1の貯蔵室13Aとダクト15Aを介して連通した断熱性の蒸発器室15が張り出し形成され、ここに第1の蒸発器16Aと蒸発器ファン17Aとが設けられているとともに、機械室14の下方には、圧縮機ユニット18が出し入れ可能に収納されている。また、仕切壁12の第2の貯蔵室13B側の面には、ダクト19Aを張ることで蒸発器室19が形成され、ここに第2の蒸発器16Bと蒸発器ファン17Bとが設けられている。   A machine room 14 is provided on the left side as viewed from the front of the storage body 10. A heat-insulating evaporator chamber 15 communicating with the first storage chamber 13A via a duct 15A is formed on the back side of the upper portion in the machine chamber 14, and the first evaporator 16A and the evaporator fan are formed here. 17A and a compressor unit 18 is housed in the lower part of the machine room 14 so as to be able to be taken in and out. An evaporator chamber 19 is formed on the surface of the partition wall 12 on the second storage chamber 13B side by extending a duct 19A, and a second evaporator 16B and an evaporator fan 17B are provided there. Yes.

前記圧縮機ユニット18は、インバータ駆動モータによって駆動される能力可変型の圧縮機20と、その圧縮機20の冷媒吐出側に接続した凝縮器21とを基台40上に設置して機械室14内から出し入れ可能に構成したものであり、併せて凝縮器21を空冷するための凝縮器ファン22(図2にのみ図示)も搭載されている。   The compressor unit 18 includes a variable capacity compressor 20 driven by an inverter drive motor, and a condenser 21 connected to the refrigerant discharge side of the compressor 20 on a base 40, and is installed in a machine room 14. A condenser fan 22 (shown only in FIG. 2) for air-cooling the condenser 21 is also mounted.

図2は冷凍サイクルとその制御装置とを併せて示す。同図に示すように、凝縮器21の出口側はドライヤ23を通した後に複数、たとえば第1及び第2の各冷媒供給路24A,24Bの二つの流路に分岐する分岐部25が設けられている。   FIG. 2 shows the refrigeration cycle and its control device together. As shown in the figure, the outlet side of the condenser 21 is provided with a branching portion 25 that branches into a plurality of, for example, two flow paths of the first and second refrigerant supply paths 24A and 24B after passing through the dryer 23. ing.

第1の冷媒供給路24Aには、絞り装置としての第1の電動膨張弁26Aと、前記第1の蒸発器16Aとが直列に設けられている。また、第2の冷媒供給路24Bには、やはり絞り装置である第2の電動膨張弁26Bと、前記第2の蒸発器16Bとが直列に設けられている。両蒸発器16A,16Bの冷媒出口側には合流接続点28により共通接続し、アキュムレータ29を介して圧縮機20の吸入側に連なる冷媒環流路30が設けられている。   A first electric expansion valve 26A as a throttling device and the first evaporator 16A are provided in series in the first refrigerant supply path 24A. The second refrigerant supply path 24B is provided with a second electric expansion valve 26B, which is also a throttling device, and the second evaporator 16B in series. A refrigerant circulation passage 30 is provided on the refrigerant outlet side of both the evaporators 16A and 16B. The refrigerant circulation passage 30 is connected in common by a confluence connection point 28 and is connected to the suction side of the compressor 20 via an accumulator 29.

さて、上記圧縮機20並びに第1及び第2の各電動膨張弁26A,26Bは、冷凍サイクル制御回路50によって制御される。この冷凍サイクル制御回路50はCPUを内蔵したコントローラ51を備え、ここに第1の貯蔵室13A内の空気温度を検出する第1の温度センサ51A及び第2の貯蔵室13B内の空気温度を検出する第2の温度センサ51Bからの信号が与えられる。   The compressor 20 and the first and second electric expansion valves 26A, 26B are controlled by a refrigeration cycle control circuit 50. The refrigeration cycle control circuit 50 includes a controller 51 with a built-in CPU, which detects the air temperature in the first storage chamber 13A and the first temperature sensor 51A for detecting the air temperature in the first storage chamber 13A. A signal from the second temperature sensor 51B is provided.

また、各蒸発器27A,27Bには、それらに流入する冷媒の温度を検出する第1及び第2の蒸発器入口温度センサ52A,52Bが設けられ、さらに合流接続点28よりも下流側であってアキュムレータ29の流入側には、合流後の冷媒の温度を検出する吸入冷媒温度センサ53が設けられ、これらのセンサ52A,52B,53からの信号も前記冷凍サイクル制御回路50のコントローラ51に与えられる。   Each of the evaporators 27A and 27B is provided with first and second evaporator inlet temperature sensors 52A and 52B for detecting the temperature of the refrigerant flowing into the evaporators 27A and 27B, and further downstream of the junction connection point 28. An intake refrigerant temperature sensor 53 for detecting the temperature of the combined refrigerant is provided on the inflow side of the accumulator 29, and signals from these sensors 52A, 52B, 53 are also given to the controller 51 of the refrigeration cycle control circuit 50. It is done.

一方、冷凍サイクル制御回路50には目標温度設定器55が設けられている。この目標温度設定器55は、ユーザが各貯蔵室13A,13Bの貯蔵物の維持温度として設定した設定温度に応じて、時間の経過と共に変化する態様で目標温度を順次出力する構成である。すなわち、各貯蔵室13A,13Bの各目標温度は、庫内温度を設定温度に至らせる経時的な変化態様(すなわち時間tと共に目標温度を設定温度に向けて変化させる様子)として出力する。その目標温度の変化態様(目標温度変化カーブ)としては、プルダウン冷却運転時の変化態様と、コントロール運転時の変化態様との2種類がある。後者は、食品等の貯蔵物をユーザーにより設定された設定温度(例えば冷蔵室の温度域では+4℃程度で、冷凍室の温度域では−20℃程度)に維持するように冷却する運転を行う際の目標温度の変化態様である。後者は、例えば冷蔵庫を設置して始めて電源を投入したときのように、コントロール運転時の設定温度よりも相当に高い常温(例えば+15℃)からコントロール運転時の温度域まで冷却する際の目標温度の変化態様である。いずれの変化態様も、各貯蔵室13A,13B毎にかつ設定温度毎に圧縮機20の運転を開始してからの経過時間tを変数とした関数によって表し、その関数が例えばEPROM等により構成した記憶手段に記憶されている。プルダウン冷却運転時の目標温度の変化態様のうち、例えば冷凍室の温度域への変化態様を示す関数fF(t)と、冷蔵室の温度域に至る目標温度の変化態様を示す関数fR(t)としては、図3に示したグラフで表されるものを例示できる。   On the other hand, the refrigeration cycle control circuit 50 is provided with a target temperature setter 55. The target temperature setter 55 is configured to sequentially output the target temperature in a manner that changes with the passage of time according to the set temperature set by the user as the maintenance temperature of the stored items in the storage chambers 13A and 13B. That is, each target temperature of each of the storage chambers 13A and 13B is output as a temporal change mode that brings the internal temperature to the set temperature (that is, a state in which the target temperature is changed toward the set temperature with time t). There are two types of target temperature change modes (target temperature change curves): a change mode during pull-down cooling operation and a change mode during control operation. The latter performs an operation of cooling a stored product such as food so as to be maintained at a set temperature set by the user (for example, about + 4 ° C. in the temperature range of the refrigerator compartment and about −20 ° C. in the temperature range of the freezer compartment). It is a change mode of the target temperature at the time. The latter is a target temperature for cooling from room temperature (for example, + 15 ° C.), which is considerably higher than the set temperature during control operation, to a temperature range during control operation, such as when the power is turned on for the first time after installing a refrigerator. It is a change aspect of. Each change mode is expressed by a function with the elapsed time t from the start of the operation of the compressor 20 as a variable for each storage chamber 13A, 13B and for each set temperature, and the function is configured by, for example, EPROM or the like. It is stored in the storage means. Of the target temperature change modes during the pull-down cooling operation, for example, a function fF (t) indicating a change mode to the temperature range of the freezer compartment and a function fR (t) indicating a target temperature change mode reaching the temperature range of the refrigerator compartment. ) Can be exemplified by those represented by the graph shown in FIG.

さらに、冷凍サイクル制御回路50には、目標温度設定器55に設定された第1の貯蔵室13Aの目標温度TAaと、温度センサ51Aにより検出された第1の貯蔵室13Aの実際の庫内温度TA との差(TA −TAa)である第1温度偏差ΔTA を算出すると共に、目標温度設定器55に設定された第2の貯蔵室13Bの目標温度TBaと、温度センサ51Bにより検出された第2の貯蔵室13Bの実際の庫内温度TB との差(TB −TBa)である第2温度偏差ΔTB を算出する温度偏差算出手段が設けられている。上記の温度偏差算出手段及び電動膨張弁制御手段は、CPUによって実行されるソフトウエアにより構成されており、その具体的な制御態様は図4ないし図6のフローチャートに示す通りであって、それを本実施形態の作用と共に次に説明する。   Further, the refrigeration cycle control circuit 50 includes the target temperature TAa of the first storage chamber 13A set in the target temperature setter 55 and the actual internal temperature of the first storage chamber 13A detected by the temperature sensor 51A. A first temperature deviation ΔTA, which is a difference from TA (TA−TAa), is calculated, and the target temperature TBa of the second storage chamber 13B set in the target temperature setter 55 is detected by the temperature sensor 51B. There is provided temperature deviation calculating means for calculating a second temperature deviation ΔTB which is a difference (TB−TBa) from the actual internal temperature TB of the second storage chamber 13B. The temperature deviation calculating means and the electric expansion valve control means are configured by software executed by the CPU, and the specific control mode is as shown in the flowcharts of FIGS. Next, the operation of this embodiment will be described.

電源を投入して目標温度設定器55にて各目標温度TAa、TBaを設定すると、圧縮機20が起動され、図4ないし図6に示す各制御フローが同時的に実行される。   When the power is turned on and the target temperatures TAa and TBa are set by the target temperature setter 55, the compressor 20 is started and the control flows shown in FIGS. 4 to 6 are executed simultaneously.

<圧縮機回転制御ルーチン>
図4に示す圧縮機回転制御ルーチンでは、まず、積算値Cを初期化し(ステップS11)、次に第1の貯蔵室13Aの目標温度カーブを表す関数によって目標温度TAaを算出し(ステップS12)、さらに第2の貯蔵室13Bの目標温度カーブを表す関数によって目標温度TBaを算出する(ステップS13)。そして、その時点で第1の温度センサ51Aから与えられる第1の貯蔵室13Aの実際の庫内温度TA と目標温度TAaとの偏差(TA −TAa)、及び、第2の温度センサ51Bから与えられる第2の貯蔵室13Bの実際の庫内温度TB と目標温度TBaとの偏差(TB −TBa)を算出して両者を加算し、これを積算値Cに加える積算処理(ステップS14)を行う。
<Compressor rotation control routine>
In the compressor rotation control routine shown in FIG. 4, first, the integrated value C is initialized (step S11), and then the target temperature TAa is calculated by a function representing the target temperature curve of the first storage chamber 13A (step S12). Further, the target temperature TBa is calculated by a function representing the target temperature curve of the second storage chamber 13B (step S13). At that time, the deviation (TA−TAa) between the actual internal temperature TA and the target temperature TAa of the first storage chamber 13A given from the first temperature sensor 51A and the second temperature sensor 51B give An integration process (step S14) is performed in which a deviation (TB-TBa) between the actual internal temperature TB of the second storage chamber 13B and the target temperature TBa is calculated and added to the integrated value C. .

次に、ステップS14にて算出された積算値Cを、2つの上限基準値L_UP,下限基準値L_DOWNと比較し(ステップS15)、積算値Cが上限基準値L_UPよりも大きければ、圧縮機20の回転数を所定量増加させ(ステップS16)、積算値Cが下限基準値L_DOWNよりも小さければ、圧縮機20の回転数を所定量減少させ(ステップS17)、積算値Cを初期化(ステップS18)して、ステップS12に戻る。なお、積算値Cが上記の上限基準値L_UP及び下限基準値L_DOWNの間にある場合には、圧縮機20の回転数を変更することなく、ステップS12に戻る。   Next, the integrated value C calculated in step S14 is compared with two upper limit reference values L_UP and a lower limit reference value L_DOWN (step S15). If the integrated value C is larger than the upper limit reference value L_UP, the compressor 20 Is increased by a predetermined amount (step S16), and if the integrated value C is smaller than the lower limit reference value L_DOWN, the rotational speed of the compressor 20 is decreased by a predetermined amount (step S17) and the integrated value C is initialized (step S16). S18) and the process returns to step S12. When the integrated value C is between the upper limit reference value L_UP and the lower limit reference value L_DOWN, the process returns to step S12 without changing the rotational speed of the compressor 20.

このルーチンを繰り返すことにより、全体的な冷却能力が両貯蔵室13A,13Bを目標温度カーブに追従可能となるように維持される。
なお、熱負荷が小さく、圧縮機を所定の最低回転数で運転しても、冷却能力が過剰になる(圧縮機の回転数の低下処理(ステップS17)が繰り返される)場合には、圧縮機20を停止して庫内の過冷却を防止する(フローチャート省略)。ここで、圧縮機20の停止・再起動をできるだけ少なくして温度の変動を防ぐには、想定される熱負荷が最も小さな時でも圧縮機20を最低回転数で運転すれば能力過剰とならない圧縮機20の能力を選定することが好ましい。
By repeating this routine, the overall cooling capacity is maintained so that both storage chambers 13A and 13B can follow the target temperature curve.
In addition, when the heat load is small and the cooling capacity becomes excessive even when the compressor is operated at a predetermined minimum rotational speed (the process of reducing the rotational speed of the compressor (step S17) is repeated), the compressor 20 is stopped to prevent overcooling in the cabinet (the flowchart is omitted). Here, in order to prevent the fluctuation of the temperature by minimizing the stop / restart of the compressor 20, even if the assumed heat load is the smallest, the compressor 20 is operated so as not to have excessive capacity if it is operated at the minimum rotation speed. It is preferable to select the capacity of the machine 20.

<膨張弁開度制御ルーチン>
一方、以上のようにして全体的な冷却能力が確保されつつ、次に説明する膨張弁開度制御ルーチンによって第1及び第2の各貯蔵室13A,13Bのための冷却能力の配分が決定される。
図5には第1の貯蔵室13Aのための膨張弁開度制御ルーチンを示した。ここでは、まず、積算値Dを初期化し(ステップS21)、次に第1の貯蔵室13Aの目標温度カーブを表す関数によって目標温度TAaを算出し(ステップS22)、次にその時点で温度センサ51Aから与えられる第1の貯蔵室13Aの実際の庫内温度TA と上記の目標温度TAaとの偏差(TA −TAa)を算出し、これを積算値Dに加える積算処理(ステップS23)を行う。
<Expansion valve opening control routine>
On the other hand, while the overall cooling capacity is secured as described above, the distribution of the cooling capacity for the first and second storage chambers 13A and 13B is determined by the expansion valve opening degree control routine described below. The
FIG. 5 shows an expansion valve opening control routine for the first storage chamber 13A. Here, first, the integrated value D is initialized (step S21), then the target temperature TAa is calculated by a function representing the target temperature curve of the first storage chamber 13A (step S22), and then the temperature sensor at that point in time. A deviation (TA-TAa) between the actual internal temperature TA of the first storage chamber 13A given from 51A and the target temperature TAa is calculated, and this is added to the integrated value D (step S23). .

そして、ステップS23にて算出された積算値Dを、開弁閾値L_OPENと閉弁閾値L_CLOSEと比較する(ステップS24)。ここで、積算値Dが上記開弁閾値L_OPENよりも大きければ、第1の電動膨張弁26Aの開度を所定量大きくし(ステップS25)、第1の蒸発器27Aに流れる冷媒の流量を増加させて第1の貯蔵室13Aの冷却能力を増大させる。逆に、積算値Dが閉弁閾値L_CLOSEよりも小さければ、第1の電動膨張弁26Aの開度を所定量小さくし(ステップS26)、冷媒流量を減少させて第1の貯蔵室13Bの冷却能力を減少させる。上記のように第1の電動膨張弁26Aの開度を調節した場合には、積算値Dを初期化して(ステップS27)、ステップS22に戻る。積算値Dが上記の2つの閾値の間にある場合には、第1の電動膨張弁26Aの開度を変更することなく、ステップS22に戻る。   Then, the integrated value D calculated in step S23 is compared with the valve opening threshold L_OPEN and the valve closing threshold L_CLOSE (step S24). Here, if the integrated value D is larger than the valve opening threshold L_OPEN, the opening degree of the first electric expansion valve 26A is increased by a predetermined amount (step S25), and the flow rate of the refrigerant flowing through the first evaporator 27A is increased. Thus, the cooling capacity of the first storage chamber 13A is increased. Conversely, if the integrated value D is smaller than the valve closing threshold L_CLOSE, the opening degree of the first electric expansion valve 26A is decreased by a predetermined amount (step S26), and the refrigerant flow rate is decreased to cool the first storage chamber 13B. Decrease ability. When the opening degree of the first electric expansion valve 26A is adjusted as described above, the integrated value D is initialized (step S27), and the process returns to step S22. If the integrated value D is between the above two thresholds, the process returns to step S22 without changing the opening of the first electric expansion valve 26A.

このルーチンを繰り返すことにより、第1の蒸発器27Aに流れる冷媒流量を第1の貯蔵室13Aの温度が目標温度カーブに追従するように調整される。   By repeating this routine, the flow rate of the refrigerant flowing through the first evaporator 27A is adjusted so that the temperature of the first storage chamber 13A follows the target temperature curve.

また、第2の貯蔵室13Bについては、上述の第1の貯蔵室13Aの場合と同様である。すなわち、温度センサ51Bから与えられる第2の貯蔵室13Bの実際の庫内温度TB と上記の目標温度TBaとの偏差を積算し、その積算値がある値を超えると第2の電動膨張弁26Bの開度を広げ、ある値を下回ると開度を狭くして、第2の蒸発器27Bに流れる冷媒流量を第2の貯蔵室13Bの温度が目標温度カーブに追従するように調整するのである。   Further, the second storage chamber 13B is the same as the case of the first storage chamber 13A described above. That is, the deviation between the actual internal temperature TB of the second storage chamber 13B given from the temperature sensor 51B and the target temperature TBa is integrated, and if the integrated value exceeds a certain value, the second electric expansion valve 26B is added. The opening degree of the second storage chamber 13B is adjusted so that the temperature of the second storage chamber 13B follows the target temperature curve. .

上述の第1及び第2の各電動膨張弁26A,26Bの各開度調整の結果、凝縮器21からの液冷媒が各各貯蔵室13A,13Bの目標温度と庫内温度との各偏差に応じて各蒸発器16A,16Bに配分され、両貯蔵室13A,13Bの各庫内温度が各目標温度にそれぞれ維持される。   As a result of adjusting the opening degree of each of the first and second electric expansion valves 26A, 26B, the liquid refrigerant from the condenser 21 has a deviation between the target temperature of each storage chamber 13A, 13B and the internal temperature. Accordingly, the temperature is distributed to the evaporators 16A and 16B, and the internal temperatures of the storage chambers 13A and 13B are respectively maintained at the target temperatures.

<液バック防止制御ルーチン>
上記の制御を組み合わせただけでは、冷却負荷が非常に大きくなると、たとえばプルダウン冷却運転中に目標温度カーブに実際の貯蔵室温TA,TBが追従できないような場合、各電動膨張弁26A,26Bが所定量づつ開弁動作を行い続け、結局、全開状態となる可能性がある。すると、圧縮機20の流入側に液冷媒が戻り、圧縮機20が破損するおそれを生ずる。
<Liquid back prevention control routine>
If the cooling load becomes very large only by combining the above-described controls, for example, when the actual storage room temperature TA, TB cannot follow the target temperature curve during the pull-down cooling operation, the electric expansion valves 26A, 26B are provided. There is a possibility that the valve-opening operation will continue to be performed in a fixed amount and eventually become fully open. Then, the liquid refrigerant returns to the inflow side of the compressor 20 and the compressor 20 may be damaged.

そこで、本実施形態では、次の液バック防止制御ルーチンも同時的に実行するようにしている。すなわち、ステップS31で吸入冷媒温度センサ53の位置における冷媒の過熱度SH を算出する。ここでは、吸入冷媒温度センサ53によって測定されている温度TS から第1の蒸発器入口温度センサ52Aによって測定されている温度TEAを減算した値を過熱度SH とする。そして、その過熱度SH が所定の下限値L_DOWN(たとえば3K)以下となったときには(ステップS32)、第1及び第2の両電動膨張弁26A,26Bの開度を所定量小さくし(ステップS33,S34)、ステップS31に戻る。   Therefore, in this embodiment, the following liquid back prevention control routine is also executed simultaneously. That is, the superheat degree SH of the refrigerant at the position of the intake refrigerant temperature sensor 53 is calculated in step S31. Here, the superheat degree SH is a value obtained by subtracting the temperature TEA measured by the first evaporator inlet temperature sensor 52A from the temperature TS measured by the suction refrigerant temperature sensor 53. When the degree of superheat SH becomes equal to or less than a predetermined lower limit L_DOWN (for example, 3K) (step S32), the opening degrees of both the first and second electric expansion valves 26A, 26B are reduced by a predetermined amount (step S33). , S34), the process returns to step S31.

なお、前述した膨張弁開度制御ルーチンは上記液バック防止制御ルーチンと同時的に実行されているため、膨張弁開度制御ルーチンによって電動膨張弁26A又は26Bの開度を広げる指示が出され、液バック防止制御ルーチンではこれと競合して開度を狭める指示が出される可能性がある。この場合には、液バック防止制御ルーチンの指示結果が優先されて電動膨張弁26A、26Bの開度が狭められる(フローチャート省略)。   Since the expansion valve opening control routine described above is executed simultaneously with the liquid back prevention control routine, an instruction to increase the opening of the electric expansion valve 26A or 26B is issued by the expansion valve opening control routine. In the liquid back prevention control routine, there is a possibility that an instruction to narrow the opening degree is issued in competition with this. In this case, the instruction result of the liquid back prevention control routine is prioritized and the opening degree of the electric expansion valves 26A, 26B is narrowed (the flowchart is omitted).

このように本実施形態によれば、圧縮機回転制御ルーチンによって圧縮機20の回転数を第1及び第2の各貯蔵室13A,13Bの各目標温度カーブとの偏差を足し合わせた値の積算値によって上下に調整し、かつ、膨張弁開度制御ルーチンによって各電動膨張弁26A,26Bの開度を各目標温度カーブとの偏差を積算した値によって開度調節を行うことで各蒸発器27A,27Bに流れる冷媒流量のバランスを決定するようにしているから、各貯蔵室の設定温度が近い場合であっても、その設定温度に到達するように確実に冷却することができる。   As described above, according to the present embodiment, the compressor rotation control routine integrates values obtained by adding the deviations of the rotation speed of the compressor 20 from the target temperature curves of the first and second storage chambers 13A and 13B. Each evaporator 27A is adjusted up and down by the value, and the opening of each electric expansion valve 26A, 26B is adjusted by the value obtained by integrating the deviation from each target temperature curve by the expansion valve opening control routine. , 27B, the balance of the refrigerant flow rate is determined, so that even when the set temperatures of the respective storage chambers are close, it is possible to reliably cool so as to reach the set temperature.

しかも、そのような電動膨張弁の開度制御を行いながら、液バック防止制御ルーチンによって冷媒の過熱度を検出してそれが一定以下に低下しないようにしているから、液バックによる圧縮機20の破損も確実に防止できる。   In addition, while controlling the opening degree of such an electric expansion valve, the liquid back prevention control routine detects the degree of refrigerant superheat so that it does not drop below a certain level. Breakage can be reliably prevented.

<実施形態2>
図7及び図8は本発明の実施形態2を示したもので、やはり2つの貯蔵室を備えた横型冷蔵庫に本発明を適用した例を示す。この実施形態2で、冷凍サイクル40の構成は実施形態1と同様で図7に示した通りである。冷凍サイクル制御装置50の構成は次のように相違する。前記実施形態1では、圧縮機20に戻る冷媒の過熱度を検出するためにアキュムレータ29の流入側に吸入冷媒温度センサ53を設けたが、この実施形態2では、第1及び第2の各蒸発器27A,27Bの出口側にそれぞれ蒸発器出口温度センサ56A,56Bを設けている。
<Embodiment 2>
7 and 8 show Embodiment 2 of the present invention, and show an example in which the present invention is applied to a horizontal refrigerator that also has two storage rooms. In the second embodiment, the configuration of the refrigeration cycle 40 is the same as that of the first embodiment, as shown in FIG. The configuration of the refrigeration cycle control device 50 is different as follows. In the first embodiment, the suction refrigerant temperature sensor 53 is provided on the inflow side of the accumulator 29 in order to detect the degree of superheat of the refrigerant returning to the compressor 20, but in the second embodiment, the first and second evaporations are performed. Evaporator outlet temperature sensors 56A and 56B are provided on the outlet sides of the evaporators 27A and 27B, respectively.

圧縮機20及び2つの電動膨張弁26A,26Bの制御ルーチンは図4及び図5に示して説明した実施形態1のものと同様である。一方、液バック防止制御ルーチンは図8に示す通りとなる。ステップS41,S42で蒸発器出口温度センサ56A,56Bの位置における冷媒の過熱度SHA,SHBをそれぞれ算出する。各過熱度は、各蒸発器出口温度センサ56A,56Bの位置の検出温度から各蒸発器入口温度センサ52A,52Bの位置の検出温度を減算して求める。そして、それらの過熱度SHA,SHBが所定の下限値L_DOWN(たとえば3K)以下となったときには(ステップS43,S44)、第1及び第2の両電動膨張弁26A,26Bの開度を所定量小さくし(ステップS45,S46)、ステップS41に戻る。   The control routine of the compressor 20 and the two electric expansion valves 26A and 26B is the same as that of the first embodiment described with reference to FIGS. On the other hand, the liquid back prevention control routine is as shown in FIG. In steps S41 and S42, the superheat degrees SHA and SHB of the refrigerant at the positions of the evaporator outlet temperature sensors 56A and 56B are calculated. Each degree of superheat is obtained by subtracting the detected temperature at the position of each evaporator inlet temperature sensor 52A, 52B from the detected temperature at the position of each evaporator outlet temperature sensor 56A, 56B. When the degree of superheat SHA, SHB becomes a predetermined lower limit L_DOWN (for example, 3K) or less (steps S43, S44), the opening degree of both the first and second electric expansion valves 26A, 26B is set to a predetermined amount. Decrease the size (steps S45 and S46) and return to step S41.

なお、前述した膨張弁開度制御ルーチンは上記液バック防止制御ルーチンと同時的に実行されているため、膨張弁開度制御ルーチンによって電動膨張弁26A又は26Bの開度を広げる指示が出され、液バック防止制御ルーチンではこれと競合して開度を狭める指示が出される可能性がある。この場合には、液バック防止制御ルーチンの指示結果が優先されて電動膨張弁26A、26Bの開度が狭められる(フローチャート省略)。   Since the expansion valve opening control routine described above is executed simultaneously with the liquid back prevention control routine, an instruction to increase the opening of the electric expansion valve 26A or 26B is issued by the expansion valve opening control routine. In the liquid back prevention control routine, there is a possibility that an instruction to narrow the opening degree is issued in competition with this. In this case, the instruction result of the liquid back prevention control routine is prioritized and the opening degree of the electric expansion valves 26A, 26B is narrowed (the flowchart is omitted).

このように本実施形態によれば、圧縮機回転制御ルーチンによって圧縮機20の回転数を第1及び第2の各貯蔵室13A,13Bの各目標温度カーブとの偏差を足し合わせた値の積算値によって上下に調整し、かつ、膨張弁開度制御ルーチンによって各電動膨張弁26A,26Bの開度を各目標温度カーブとの偏差を積算した値によって開度調節を行うことで各蒸発器27A,27Bに流れる冷媒流量のバランスを決定するようにしているから、各貯蔵室の設定温度が近い場合であっても、その設定温度に到達するように確実に冷却することができる。   As described above, according to the present embodiment, the compressor rotation control routine integrates values obtained by adding the deviations of the rotation speed of the compressor 20 from the target temperature curves of the first and second storage chambers 13A and 13B. Each evaporator 27A is adjusted up and down by the value, and the opening of each electric expansion valve 26A, 26B is adjusted by the value obtained by integrating the deviation from each target temperature curve by the expansion valve opening control routine. , 27B, the balance of the refrigerant flow rate is determined, so that even when the set temperatures of the respective storage chambers are close, it is possible to reliably cool so as to reach the set temperature.

しかも、そのような電動膨張弁の開度制御を行いながら、液バック防止制御ルーチンによって冷媒の過熱度を検出してそれが一定以下に低下しないようにしているから、液バックによる圧縮機20の破損も確実に防止できる。   In addition, while controlling the opening degree of such an electric expansion valve, the liquid back prevention control routine detects the degree of refrigerant superheat so that it does not drop below a certain level. Breakage can be reliably prevented.

<他の実施形態>
本発明は上記記述及び図面によって説明した実施形態に限定されるものではなく、例えば次のような実施形態も本発明の技術的範囲に含まれる。
<Other embodiments>
The present invention is not limited to the embodiments described with reference to the above description and drawings. For example, the following embodiments are also included in the technical scope of the present invention.

(1)上記各実施形態では、目標温度と庫内温度との偏差を所定時間毎に算出して積算し、その積算値が所定の基準値を越えた場合に、直ちに圧縮機の回転数を高めるようにしたが、圧縮機の回転数を決定するに際してさらに他の条件を加味してもよい。   (1) In each of the above embodiments, the deviation between the target temperature and the internal temperature is calculated and integrated every predetermined time, and when the integrated value exceeds a predetermined reference value, the rotational speed of the compressor is immediately set. However, other conditions may be taken into account when determining the rotational speed of the compressor.

(2)上記各実施形態では、目標温度設定手段を目標温度の経時的変化態様を表した関数を記憶手段に記憶させ、その関数を読み出して時間の経過に合わせて目標温度を算出する構成としたが、これに限らず、例えば目標温度の経時的変化態様を温度と経過時間とを対照させた参照テーブルを予め作成しておき、この参照テーブルを記憶手段に記憶しておき、計時手段からの信号に応じて、テーブル読み出し手段によって時間の経過に合わせてその記憶手段における目標温度を読み出す構成としてもよい。   (2) In each of the above-described embodiments, the target temperature setting unit stores a function that represents a temporal change mode of the target temperature in the storage unit, reads the function, and calculates the target temperature as time elapses. However, the present invention is not limited to this. For example, a reference table in which the temporal change mode of the target temperature is compared with the temperature and the elapsed time is prepared in advance, and the reference table is stored in the storage unit. In response to this signal, the target temperature in the storage means may be read out by the table reading means as time passes.

(3)上記各実施形態では2つの貯蔵室を備えた冷蔵庫について説明したが、3つ以上の貯蔵室を備えた場合であっても同様に構成することができ、また各貯蔵室の温度域は夫々独立して自由に決定することができる。   (3) In each of the above embodiments, a refrigerator having two storage rooms has been described. However, even when three or more storage rooms are provided, the refrigerator can be similarly configured, and the temperature range of each storage room Can be determined independently and independently.

(4)上記各実施形態では、2つの貯蔵室13A,13Bが共に冷蔵温度域であるような同一の温度域を目標温度として設定される場合について説明したが、これに限らず、たとえば冷蔵温度域と冷凍温度域のように大きな温度差がある異なる温度域に目標温度が設定される場合であってもよい。   (4) In each of the above embodiments, the case where the same temperature range in which the two storage chambers 13A and 13B are both in the refrigeration temperature range is set as the target temperature has been described. The target temperature may be set in different temperature ranges where there is a large temperature difference, such as the temperature range and the freezing temperature range.

本発明の実施形態1を示す冷却貯蔵庫の断面図Sectional drawing of the cooling storehouse which shows Embodiment 1 of this invention 実施形態1の冷凍サイクル構成図Refrigeration cycle configuration diagram of Embodiment 1 実施形態1における目標温度の経時的変化態様の例を示すグラフThe graph which shows the example of the time-dependent change aspect of the target temperature in Embodiment 1. 実施形態1における圧縮機回転制御ルーチンの制御手順を示すフローチャートThe flowchart which shows the control procedure of the compressor rotation control routine in Embodiment 1. 実施形態1における膨張弁解度制御ルーチンの制御手順を示すフローチャートThe flowchart which shows the control procedure of the expansion valve solution degree control routine in Embodiment 1. 実施形態1における液バック防止制御ルーチンの制御手順を示すフローチャート6 is a flowchart showing a control procedure of a liquid back prevention control routine in the first embodiment. 実施形態2の冷凍サイクル構成図Refrigeration cycle configuration diagram of Embodiment 2 実施形態2における液バック防止制御ルーチンの制御手順を示すフローチャート7 is a flowchart showing a control procedure of a liquid back prevention control routine in the second embodiment.

符号の説明Explanation of symbols

10…断熱貯蔵庫 13A…第1の貯蔵室 13B…第2の貯蔵室 16A…第1の蒸発器 16B…第2の蒸発器 20…圧縮機 24A…第1の冷媒供給路 24B…第2の冷媒供給路 26A…第1の電動膨張弁 26B…第2の電動膨張弁 30…冷媒環流路 51A,51B…庫内温度センサ 52A、52B…蒸発器入口温度センサ 55…目標温度設定手段 50…冷凍サイクル制御回路(圧縮機回転制御手段、電動膨張弁制御手段、偏差算出手段、電動膨張弁比較駆動手段、過熱度検出手段、記憶手段)   DESCRIPTION OF SYMBOLS 10 ... Thermal insulation storage 13A ... 1st storage chamber 13B ... 2nd storage chamber 16A ... 1st evaporator 16B ... 2nd evaporator 20 ... Compressor 24A ... 1st refrigerant | coolant supply path 24B ... 2nd refrigerant | coolant Supply path 26A ... 1st electric expansion valve 26B ... 2nd electric expansion valve 30 ... Refrigerant ring flow path 51A, 51B ... Inside temperature sensor 52A, 52B ... Evaporator inlet temperature sensor 55 ... Target temperature setting means 50 ... Refrigeration cycle Control circuit (compressor rotation control means, electric expansion valve control means, deviation calculation means, electric expansion valve comparison drive means, superheat degree detection means, storage means)

Claims (10)

インバータモータにより駆動される圧縮機と、この圧縮機が圧縮した冷媒から放熱させる凝縮器と、この凝縮器からの冷媒をそれぞれ電動膨張弁を介して流す複数の冷媒供給路と、前記各冷媒供給路に設けた蒸発器と、前記各蒸発器で蒸発した冷媒を合流させて前記圧縮機の吸入側に戻す冷媒環流路と、前記各蒸発器によって生成された冷気によって冷却される複数の貯蔵室と、前記各貯蔵室内の目標温度を設定するための目標温度設定手段と、前記各貯蔵室の庫内温度を検出する庫内温度センサと、前記目標温度設定手段に設定された前記目標温度と前記庫内温度センサにより検出された庫内温度との偏差に基づいて前記圧縮機の回転数を制御することで前記各貯蔵室を前記目標温度に維持するための冷却能力を生じさせる圧縮機回転制御手段と、前記各貯蔵室の前記目標温度と前記庫内温度との各偏差に応じて複数の前記各電動膨張弁の開度を制御することで前記凝縮器からの冷媒を前記各蒸発器に配分する電動膨張弁制御手段とを備えた冷却貯蔵庫。 A compressor driven by an inverter motor; a condenser that dissipates heat from the refrigerant compressed by the compressor; a plurality of refrigerant supply passages through which the refrigerant from the condenser flows through an electric expansion valve; An evaporator provided in a passage, a refrigerant circulation passage for condensing refrigerant evaporated in each evaporator and returning the refrigerant to the suction side of the compressor, and a plurality of storage chambers cooled by cold air generated by each evaporator Target temperature setting means for setting a target temperature in each of the storage chambers, an internal temperature sensor for detecting the internal temperature of each of the storage chambers, and the target temperature set in the target temperature setting means Compressor rotation that produces cooling capacity for maintaining each storage chamber at the target temperature by controlling the rotation speed of the compressor based on the deviation from the internal temperature detected by the internal temperature sensor control The refrigerant from the condenser is supplied to each evaporator by controlling the opening of each of the plurality of electric expansion valves according to the stage and the deviation between the target temperature and the internal temperature of each storage chamber Cooling storage provided with electric expansion valve control means for distributing. 前記圧縮機回転制御手段は、所定時間毎に前記目標温度設定手段に設定された前記目標温度と前記温度センサにより検出された庫内温度との偏差を算出する偏差算出手段と、この偏差算出手段により算出された偏差の積算値を所定の基準値と比較して前記インバータモータの回転数を変化させる回転数制御手段とを備えてなる請求項1記載の冷却貯蔵庫。 The compressor rotation control means includes a deviation calculating means for calculating a deviation between the target temperature set in the target temperature setting means at every predetermined time and the internal temperature detected by the temperature sensor, and the deviation calculating means. The cooling storage according to claim 1, further comprising: a rotation speed control unit that changes the rotation speed of the inverter motor by comparing the integrated value of the deviation calculated by the above with a predetermined reference value. 前記電動膨張弁制御手段は、所定時間毎に前記目標温度設定手段に設定された前記目標温度と前記温度センサにより検出された庫内温度との偏差を算出する偏差算出手段と、前記各貯蔵室毎に前記偏差算出手段により算出された偏差の積算値を所定の基準値と比較して前記積算値が所定の基準値よりも小さい場合に前記電動膨張弁を所定量閉じると共に前記積算値が所定の基準値よりも大きい場合に前記電動膨張弁を所定量開放する制御を行う電動膨張弁比較駆動手段とを備える請求項1又は請求項2に記載の冷却貯蔵庫。 The electric expansion valve control means includes a deviation calculating means for calculating a deviation between the target temperature set in the target temperature setting means at every predetermined time and the internal temperature detected by the temperature sensor; Every time the integrated value calculated by the deviation calculating means is compared with a predetermined reference value and the integrated value is smaller than the predetermined reference value, the electric expansion valve is closed by a predetermined amount and the integrated value is predetermined. The cooling storage according to claim 1 or 2, further comprising: an electric expansion valve comparison / drive means for performing control to open the electric expansion valve by a predetermined amount when the electric expansion valve is larger than a reference value. 前記圧縮機に吸入される冷媒の過熱度を検出する過熱度検出手段を備え、その過熱度が所定値以下に低下したときに前記圧縮機の運転を停止する請求項1ないし請求項3のいずれか一項に記載の冷却貯蔵庫。 The superheat degree detection means for detecting the superheat degree of the refrigerant sucked into the compressor is provided, and the operation of the compressor is stopped when the superheat degree falls below a predetermined value. The cooling storage according to claim 1. 前記過熱度検出手段は、前記複数の蒸発器のうちのいずれか1つの蒸発器へ流入する冷媒の温度を検出する蒸発器入口温度センサと、前記冷媒環流路のうち冷媒の合流点よりも下流に設けた吸入冷媒温度センサとを備え、両温度センサにより検出される温度差に基づいて冷媒の過熱度を検出する構成とした請求項1ないし請求項4のいずれか一項に記載の冷却貯蔵庫。 The superheat degree detection means includes an evaporator inlet temperature sensor that detects a temperature of a refrigerant flowing into any one of the plurality of evaporators, and a downstream of a refrigerant confluence in the refrigerant circulation passage. The cooling storage according to any one of claims 1 to 4, wherein the refrigerant is provided with an intake refrigerant temperature sensor and detects a degree of superheat of the refrigerant based on a temperature difference detected by the two temperature sensors. . 前記過熱度検出手段は、前記複数の各蒸発器の冷媒入口側に設けた蒸発器入口温度センサと、各蒸発器の冷媒出口側に設けた蒸発器出口温度センサとを備え、複数の各蒸発器のうちのいずれか1つについて両温度センサにより検出される温度差が所定の基準値を越えたことに基づいて冷媒の過熱度を検出する構成とした請求項1ないし請求項4のいずれか一項に記載の冷却貯蔵庫。 The superheat degree detection means includes an evaporator inlet temperature sensor provided on the refrigerant inlet side of each of the plurality of evaporators, and an evaporator outlet temperature sensor provided on the refrigerant outlet side of each of the evaporators. 5. The refrigerant superheat degree is detected based on the fact that the temperature difference detected by the two temperature sensors exceeds a predetermined reference value for any one of the chambers. 6. The cooling storage according to one item. 前記目標温度設定手段は時間の経過と共に異なる目標温度を順次出力する構成であることを特徴とする請求項1ないし請求項6のいずれか一項に記載の冷却貯蔵庫。 The cooling storage according to any one of claims 1 to 6, wherein the target temperature setting means is configured to sequentially output different target temperatures as time passes. 前記目標温度設定手段は、目標温度の経時的変化態様を表した関数を記憶する記憶手段と、この記憶手段に記憶された関数を読み出して時間の経過に合わせて目標温度を算出する目標温度算出手段とを備える請求項7に記載の冷却貯蔵庫。 The target temperature setting means is a storage means for storing a function representing a temporal change mode of the target temperature, and a target temperature calculation for reading the function stored in the storage means and calculating the target temperature as time passes. The cooling storage according to claim 7, comprising means. 前記目標温度設定手段は、目標温度の経時的変化態様を温度と経過時間とを対照させた参照テーブルとして記憶する記憶手段と、時間の経過に合わせて前記記憶手段における目標温度を読み出すテーブル読み出し手段とを備える請求項7に記載の冷却貯蔵庫。 The target temperature setting means stores storage means as a reference table in which the temporal change mode of the target temperature is contrasted between temperature and elapsed time, and table reading means for reading out the target temperature in the storage means as time elapses The cooling storage of Claim 7 provided with these. 能力可変型の圧縮機によって冷媒を圧縮して凝縮器で放熱すると共に、それぞれ電動膨張弁を介した複数の冷媒供給路に分流させ、前記各冷媒供給路に設けた蒸発器によって冷却作用を生じさせた後に、冷媒を合流させて前記圧縮機の吸入側に戻すようにした冷凍サイクルを備えた冷却貯蔵庫において、前記各貯蔵室の目標温度が維持されるように前記各電動膨張弁の開度を調節すると共に、前記圧縮機は両貯蔵室の目標温度が維持されるに足る冷却能力を生じさせるように運転し、かつ、前記蒸発器から流出する液冷媒の過熱度が液バックを生じさせる程度に低下したときには前記圧縮機を停止することを特徴とする冷却貯蔵庫の運転方法。 The refrigerant is compressed by a variable capacity compressor and radiated by a condenser, and is divided into a plurality of refrigerant supply passages through electric expansion valves, respectively, and a cooling action is generated by an evaporator provided in each refrigerant supply passage. In the cooling storage having a refrigeration cycle in which the refrigerant is combined and returned to the suction side of the compressor, the opening degree of each electric expansion valve is maintained so that the target temperature of each storage chamber is maintained. The compressor is operated to generate a cooling capacity sufficient to maintain the target temperature of both storage chambers, and the superheat of the liquid refrigerant flowing out of the evaporator generates a liquid back. A cooling storage operation method, wherein the compressor is stopped when the pressure drops to a certain extent.
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