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JP5524571B2 - Heat pump equipment - Google Patents

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JP5524571B2
JP5524571B2 JP2009247477A JP2009247477A JP5524571B2 JP 5524571 B2 JP5524571 B2 JP 5524571B2 JP 2009247477 A JP2009247477 A JP 2009247477A JP 2009247477 A JP2009247477 A JP 2009247477A JP 5524571 B2 JP5524571 B2 JP 5524571B2
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heat
temperature
refrigerant
heat source
load
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JP2011094840A (en
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真典 上田
菅  崇
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Corona Corp
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/70Efficient control or regulation technologies, e.g. for control of refrigerant flow, motor or heating

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Description

この発明は、ヒートポンプ回路の蒸発側の冷媒温度を安定させて、効率の良い暖房等の負荷運転を行わせるヒートポンプ装置に関するものである。   The present invention relates to a heat pump device that stabilizes the refrigerant temperature on the evaporation side of a heat pump circuit and performs load operation such as efficient heating.

従来この種のヒートポンプ装置においては、図8に示すように、空気調和機等のヒートポンプユニット101と、熱媒循環式の熱源部102と、負荷熱交換部103とを備え、ヒートポンプユニット101は、圧縮機104と、圧縮機104から吐出された高圧冷媒を流通させ負荷側の熱媒と熱交換する凝縮器としての負荷側熱交換器105と、減圧手段としての膨張弁106と、膨張弁106からの低圧冷媒を流通させ外部の熱媒と熱交換する蒸発器としての熱源側熱交換器107とを備え、また、熱源部102は、熱源側熱交換器107の冷媒を加熱する熱源108と、熱源側熱交換器107と熱源108との間を熱媒配管で環状に接続する熱源側循環回路109と、熱源側循環回路109に熱媒である水や不凍液を循環させる回転数可変の熱源側循環ポンプ110と、熱源側熱交換器107から流出する地中熱循環回路109の熱媒の温度を検出する熱源側往き温度センサ111とを備え、また、負荷熱交換部103は、床暖房パネル等の負荷端末112と、負荷側熱交換器105と負荷端末112を循環可能に接続する負荷側循環回路113と、負荷側循環回路113に熱媒を循環させる負荷側循環ポンプ114と、負荷側熱交換器105から流出する負荷側循環回路113の熱媒の温度を検出する負荷側往き温度センサ115を備え、さらに、各センサの信号を受けて、各アクチュエータの駆動を制御するマイコンを有する制御手段116を備えたものであった。   Conventionally, in this type of heat pump apparatus, as shown in FIG. 8, the heat pump unit 101 such as an air conditioner, a heat medium circulation type heat source unit 102, and a load heat exchange unit 103 are provided. A compressor 104, a load-side heat exchanger 105 as a condenser for circulating the high-pressure refrigerant discharged from the compressor 104 and exchanging heat with a load-side heat medium, an expansion valve 106 as a decompression means, and an expansion valve 106 A heat source side heat exchanger 107 as an evaporator that circulates the low-pressure refrigerant from the heat source and exchanges heat with an external heat medium, and the heat source unit 102 includes a heat source 108 that heats the refrigerant of the heat source side heat exchanger 107, and , A heat source side circulation circuit 109 that connects the heat source side heat exchanger 107 and the heat source 108 in a ring shape with a heat medium pipe, and a heat source side circulation circuit 109 that can circulate water or antifreeze as a heat medium. The heat source side circulation pump 110 and the heat source side forward temperature sensor 111 for detecting the temperature of the heat medium in the underground heat circulation circuit 109 flowing out from the heat source side heat exchanger 107 are also provided. A load terminal 112 such as a floor heating panel, a load-side circulation circuit 113 that connects the load-side heat exchanger 105 and the load terminal 112 in a circulatory manner, and a load-side circulation pump 114 that circulates a heat medium in the load-side circulation circuit 113 , A load-side forward temperature sensor 115 for detecting the temperature of the heat medium in the load-side circulation circuit 113 flowing out from the load-side heat exchanger 105, and a microcomputer for controlling the driving of each actuator in response to a signal from each sensor The control means 116 having

このようなヒートポンプ装置において、圧縮機104、熱源側循環ポンプ110、負荷側循環ポンプ114を駆動させて、熱源側熱交換器107にて、熱源部102側の熱を冷媒側に採熱すると共に、その熱を利用して、負荷側熱交換器105にて負荷側の熱媒を加熱する負荷運転としての暖房運転を行う場合、この暖房運転時に、制御手段116は熱源側往き温度センサ111で検出する熱媒の温度が所定の目標温度になるように、熱源側循環ポンプ110の回転数を制御し熱媒の流量を調整するものであった。(例えば、特許文献1参照。)   In such a heat pump device, the compressor 104, the heat source side circulation pump 110, and the load side circulation pump 114 are driven, and the heat on the heat source unit 102 side is collected to the refrigerant side by the heat source side heat exchanger 107. When the heating operation is performed as a load operation in which the load-side heat exchanger 105 heats the load-side heat medium using the heat, the control means 116 uses the heat-source-side forward temperature sensor 111 during the heating operation. The rotational speed of the heat source side circulation pump 110 is controlled to adjust the flow rate of the heat medium so that the temperature of the heat medium to be detected becomes a predetermined target temperature. (For example, refer to Patent Document 1.)

特公平8−14437号公報Japanese Patent Publication No.8-14437

この従来のヒートポンプ装置は、前記暖房運転時に、熱源側往き温度センサ111で検出する熱媒の温度(熱源往き温度)が所定の目標温度になるように、熱源側循環ポンプ110の回転数を制御するもので、図9は前記暖房運転時のタイムチャートを示したものであり、ここでは、前記所定の目標温度を8℃に設定し、負荷側往き温度センサ115で検出する熱媒の温度(暖房往き温度)が、例えば45℃になるように圧縮機104が制御されるものである。また、時間t0は、前記暖房運転が安定した後の任意の時間とする。なお、図9中の蒸発側冷媒温度は、膨張弁106から吐出され圧縮機104に吸入されるまでの熱源側熱交換器107側の冷媒の温度とする。   This conventional heat pump device controls the rotation speed of the heat source side circulation pump 110 so that the temperature of the heat medium (heat source going temperature) detected by the heat source side going temperature sensor 111 becomes a predetermined target temperature during the heating operation. FIG. 9 shows a time chart during the heating operation. Here, the predetermined target temperature is set to 8 ° C., and the temperature of the heating medium (detected by the load side temperature sensor 115 ( The compressor 104 is controlled so that the heating temperature) is 45 ° C., for example. The time t0 is an arbitrary time after the heating operation is stabilized. 9 is the temperature of the refrigerant on the heat source side heat exchanger 107 side until it is discharged from the expansion valve 106 and sucked into the compressor 104.

ここで、図9に示す前記暖房運転時のタイムチャートについて説明する。まず、時間t1〜t2にかけて暖房往き温度が低下すると、負荷端末112での暖房出力(負荷出力)が足りないとして、制御手段116は圧縮機104の回転数を増加させ始める(時間t2)。また、それと連動して蒸発側冷媒温度が低下し始める(時間t2)。   Here, the time chart during the heating operation shown in FIG. 9 will be described. First, when the heating temperature decreases from time t1 to t2, the control means 116 starts increasing the rotation speed of the compressor 104 (time t2) because the heating output (load output) at the load terminal 112 is insufficient. In conjunction with this, the evaporation side refrigerant temperature starts to decrease (time t2).

そして、蒸発側冷媒温度が低下していき、蒸発側冷媒温度の低下を受けて遅延して熱源往き温度が低下し始める(時間t3)。そうすると、制御手段116は熱源往き温度が前記所定の目標温度を下回ったことを検知して、熱源側循環ポンプ110の回転数を増加させ始める(時間t4)。   Then, the evaporation side refrigerant temperature decreases, and the heat source going temperature begins to decrease with a delay in response to the decrease in the evaporation side refrigerant temperature (time t3). Then, the control means 116 detects that the heat source going temperature has fallen below the predetermined target temperature, and starts to increase the rotational speed of the heat source side circulation pump 110 (time t4).

時間t4において、熱源側循環ポンプ110の回転数を増加させ始めると、熱源側熱交換器107で熱源部102側から汲み上げる採熱出力も増加していき、また、蒸発側冷媒温度が上昇していく。その後、蒸発側冷媒温度の上昇を受けて遅延して熱源往き温度が上昇し始める(時間t5)。   When the rotation speed of the heat source side circulation pump 110 is started to increase at time t4, the heat collection output pumped up from the heat source unit 102 side by the heat source side heat exchanger 107 also increases, and the evaporation side refrigerant temperature rises. Go. Thereafter, in response to the increase in the evaporation side refrigerant temperature, the heat source going temperature begins to rise with a delay (time t5).

そして、時間t7において、暖房往き温度が45℃となり、暖房出力を満足すると共に、熱源往き温度が前記所定の目標温度である8℃に達したので、熱源側循環ポンプ110の回転数をその時の回転数に維持して、その後、安定した暖房運転を継続するものである。   At time t7, the heating going temperature reaches 45 ° C., the heating output is satisfied, and the heat source going temperature reaches 8 ° C., which is the predetermined target temperature. The rotation speed is maintained, and then stable heating operation is continued.

ところで、このような従来のヒートポンプ装置は、前記暖房運転時に、熱源側往き温度センサ111で検出する熱媒の温度(熱源往き温度)が所定の目標温度になるように、熱源側循環ポンプ110の回転数を制御すると、図9に示されるように、暖房出力の変動、ここでは暖房出力の増加が熱源往き温度に反映されるまでに時間差があり、所望の暖房出力を出すことができるまでに時間がかかってしまうと共に、その間、ヒートポンプ装置のシステムCOP(=「暖房出力÷(圧縮機104消費電力+熱源側循環ポンプ110消費電力)」とする)も悪くなってしまっていた。なお、ここでは、暖房出力が増加した場合について説明したが、暖房出力が減少した場合についても同様の課題を有するものであった。   By the way, in such a conventional heat pump device, the temperature of the heat medium detected by the heat source side going temperature sensor 111 (heat source going temperature) is adjusted to a predetermined target temperature during the heating operation. When the number of revolutions is controlled, as shown in FIG. 9, there is a time difference until the heating output fluctuation, here, the increase in heating output is reflected in the temperature going to the heat source, and the desired heating output can be output. In the meantime, the heat pump system COP (= “heating output ÷ (power consumption of the compressor 104 + consumption power of the heat source side circulation pump 110)”) has also deteriorated. In addition, although the case where heating output increased here was demonstrated, it had the same subject also when heating output decreased.

この発明は上記課題を解決するために、特に請求項ではその構成を、圧縮機、負荷側熱交換器、減圧手段、熱源側熱交換器を冷媒配管で環状に接続したヒートポンプ回路と、前記熱源側熱交換器の冷媒を加熱する熱媒循環式の熱源部と、該熱源部の熱源と前記熱源側熱交換器との間を熱媒配管で環状に接続した熱源側循環回路と、該熱源側循環回路に熱媒を循環させる熱源側循環ポンプと、熱源側熱交換器側の冷媒の温度を検出する冷媒温度検出手段と、これらの作動を制御する制御手段とを備え、前記熱源側熱交換器を蒸発器として機能させると同時に、前記負荷側熱交換器を凝縮器として機能させて負荷側を加熱する負荷運転を行うヒートポンプ装置であって、前記制御手段は、前記負荷運転中に、前記冷媒温度検出手段の検出する温度が所定の目標温度になるように前記熱源側循環ポンプの回転数を制御するもので、前記冷媒温度検出手段の目標温度は、前記熱源側熱交換器に流入する熱媒の温度を検出する熱源側戻り温度検出手段が、検出する戻り温度が高い程、高い温度に変更するようにしたものである。 In order to solve the above-described problems, the present invention particularly includes the configuration of a heat pump circuit in which a compressor, a load-side heat exchanger, a decompression unit, and a heat-source-side heat exchanger are annularly connected by refrigerant piping, and the heat source. A heat source circulation type heat source section for heating the refrigerant of the side heat exchanger, a heat source side circulation circuit in which the heat source of the heat source section and the heat source side heat exchanger are annularly connected by a heat medium pipe, and the heat source A heat source side circulation pump for circulating the heat medium in the side circulation circuit, a refrigerant temperature detection means for detecting the temperature of the refrigerant on the heat source side heat exchanger side, and a control means for controlling the operation of the heat source side heat. A heat pump device that performs a load operation of heating the load side by causing the load side heat exchanger to function as a condenser at the same time that the exchanger functions as an evaporator, and the control means is configured to perform the load operation, Temperature detected by the refrigerant temperature detecting means And controls the rotational speed of the heat source-side circulation pump to a predetermined target temperature, the target temperature of the refrigerant temperature detecting means, the heat source side for detecting the temperature of the heating medium flowing into the heat source side heat exchanger The return temperature detection means changes to a higher temperature as the return temperature detected is higher .

この発明によれば、冷媒温度検出手段で検出する温度の変動により負荷出力の変動を素早く把握して、冷媒温度検出手段の検出する温度が、システムCOPを高く維持できる予め設定された目標温度になるように、熱源側循環ポンプの回転数を制御し熱源側循環回路を循環する熱媒の流量を調整することで、最適な採熱を行わせて所望の負荷出力を出力するまでの時間を短縮することができると共に、ヒートポンプ装置のシステムCOPを高く維持したまま負荷運転を行うことができるものである。
更に負荷運転中に、熱源側戻り温度検出手段の検出する温度が高い程、所定の目標温度を高い温度に設定するようにしたことで、圧縮機の消費電力を小さくすることができ、ヒートポンプ装置のCOP向上、ひいてはヒートポンプ装置のシステムCOPを向上させることができるものである。
According to this inventions, to quickly grasp the variation of the load output due to variations in temperature detected by the refrigerant temperature detecting means, temperature detected by the refrigerant temperature detecting means, preset target temperature can maintain a high system COP By adjusting the flow rate of the heat medium that circulates through the heat source side circulation circuit by controlling the rotation speed of the heat source side circulation pump, the time required to perform optimum heat collection and output the desired load output The load operation can be performed while maintaining the system COP of the heat pump device high.
Further, during the load operation, the higher the temperature detected by the heat source side return temperature detection means, the higher the predetermined target temperature is set, so that the power consumption of the compressor can be reduced, and the heat pump device It is possible to improve the COP of the heat pump device, and consequently the system COP of the heat pump device.

この発明の一実施形態のヒートポンプ装置の概略構成図。BRIEF DESCRIPTION OF THE DRAWINGS The schematic block diagram of the heat pump apparatus of one Embodiment of this invention. 同一実施形態の負荷運転時の作動を示すフローチャート。The flowchart which shows the action | operation at the time of the load driving | operation of the same embodiment. 同一実施形態の負荷運転時の作動を示すタイムチャート。The time chart which shows the action | operation at the time of the load driving | operation of the same embodiment. 同一実施形態の負荷運転時の作動を示すタイムチャート。The time chart which shows the action | operation at the time of the load driving | operation of the same embodiment. 同一実施形態の負荷運転時の別の作動を示すフローチャート。The flowchart which shows another action | operation at the time of load driving | running of the same embodiment. 同一実施形態の負荷運転を給湯等に使用する湯水を加熱沸き上げする沸き上げ運転とした場合の概略図。Schematic when the load operation of the same embodiment is a boiling operation for heating and boiling hot water used for hot water supply or the like. 同一実施形態の負荷運転を空調用の室内機で被空調空間を暖める暖房運転とした場合の概略図。Schematic when the load operation of the same embodiment is a heating operation in which an air-conditioned space is warmed by an indoor unit for air conditioning. 従来のヒートポンプ装置の概略構成図。The schematic block diagram of the conventional heat pump apparatus. 従来のヒートポンプ装置の暖房運転時の作動を示すタイムチャート。The time chart which shows the action | operation at the time of the heating operation of the conventional heat pump apparatus.

次に、この発明の一実施形態のヒートポンプ装置を図1に基づき説明する。
図示のように、本実施形態のヒートポンプ装置は、大きく分けてヒートポンプユニット1と、熱源部として熱媒循環式の地中熱交換部2と、負荷熱交換部3とから構成されるものである。
Next, a heat pump device according to an embodiment of the present invention will be described with reference to FIG.
As shown in the figure, the heat pump device of the present embodiment is roughly composed of a heat pump unit 1, a heat medium circulation type underground heat exchange unit 2 as a heat source unit, and a load heat exchange unit 3. .

前記ヒートポンプユニット1は、冷媒を圧縮する回転数可変の圧縮機4と、圧縮機4から吐出された高圧冷媒を流通させこの高圧冷媒と負荷熱交換部3の負荷側の熱媒との熱交換を行う凝縮器としての負荷側熱交換器5と、負荷側熱交換器5から流出する冷媒を減圧する減圧手段としての膨張弁6と、膨張弁6からの低圧冷媒を流通させこの低圧冷媒と地中熱交換部2の熱源側の熱媒との熱交換を行う蒸発器としての熱源側熱交換器7とを備え、これらを冷媒配管で環状に接続しヒートポンプ回路8を形成しているものである。なお、ヒートポンプユニット1の冷媒としては、二酸化炭素冷媒やHFC冷媒等の任意の冷媒を用いることができるものである。また、9は冷媒の温度を検出する冷媒温度検出手段としての冷媒温度センサであり、膨張弁6から吐出され圧縮機4に吸入されるまでの熱源側熱交換器7側の冷媒配管に設けられているものである。   The heat pump unit 1 circulates a variable-speed compressor 4 that compresses the refrigerant and a high-pressure refrigerant discharged from the compressor 4, and exchanges heat between the high-pressure refrigerant and the load-side heat medium of the load heat exchange unit 3. A load side heat exchanger 5 as a condenser for performing the above, an expansion valve 6 as a pressure reducing means for reducing the pressure of the refrigerant flowing out from the load side heat exchanger 5, and a low pressure refrigerant from the expansion valve 6 by circulating the low pressure refrigerant. A heat source side heat exchanger 7 as an evaporator that performs heat exchange with the heat medium on the heat source side of the underground heat exchanging unit 2, and these are connected in an annular shape with a refrigerant pipe to form a heat pump circuit 8 It is. In addition, as a refrigerant | coolant of the heat pump unit 1, arbitrary refrigerant | coolants, such as a carbon dioxide refrigerant | coolant and a HFC refrigerant | coolant, can be used. Reference numeral 9 denotes a refrigerant temperature sensor as refrigerant temperature detection means for detecting the temperature of the refrigerant, which is provided in the refrigerant pipe on the heat source side heat exchanger 7 side until it is discharged from the expansion valve 6 and sucked into the compressor 4. It is what.

前記地中熱交換部2は、熱源側熱交換器7と、熱源側熱交換器7の冷媒を加熱する熱源として地盤G中に埋設され互いに並列に接続された複数の地中熱交換器10と、熱源側熱交換器7と地中熱交換器10との間を熱媒配管で環状に接続する熱源側循環回路としての地中熱循環回路11と、地中熱循環回路11に熱媒である水や不凍液を循環させる回転数可変の熱源側循環ポンプとしての地中熱循環ポンプ12と、地中熱循環回路11に設けられ地中熱交換器10から流出し熱源側熱交換器7に流入する熱媒の温度を検出する熱源側戻り温度検出手段としての地中戻り温度センサ13とを備えているものである。   The underground heat exchange unit 2 includes a heat source side heat exchanger 7 and a plurality of underground heat exchangers 10 embedded in the ground G as heat sources for heating the refrigerant of the heat source side heat exchanger 7 and connected in parallel to each other. And a ground heat circulation circuit 11 as a heat source side circulation circuit that connects the heat source side heat exchanger 7 and the ground heat exchanger 10 in a ring shape with a heat medium pipe, and a heat medium to the ground heat circulation circuit 11. A ground heat circulation pump 12 serving as a heat source side circulation pump having a variable number of revolutions for circulating water and antifreeze, and a heat source side heat exchanger 7 which is provided in the ground heat circulation circuit 11 and flows out of the ground heat exchanger 10. And an underground return temperature sensor 13 as a heat source side return temperature detection means for detecting the temperature of the heat medium flowing into the heat medium.

ここで、前記地中熱交換部2では、後述する負荷運転を行う際に、前記地中熱交換器10によって地盤G中から地中熱を採熱し、その熱を帯びた熱媒が地中熱循環ポンプ12により熱源側熱交換器7に供給される。そして、熱源側熱交換器7にて冷媒と熱媒とが対向して流れて熱交換が行われ、地中熱交換器10にて採熱された地中熱がヒートポンプユニット1の冷媒側に汲み上げられ、熱源側熱交換器7は蒸発器として機能するものとなる。   Here, in the underground heat exchanging section 2, when performing a load operation described later, the underground heat exchanger 10 collects underground heat from the ground G, and the heat transfer medium with the heat is underground. The heat circulation pump 12 supplies the heat source side heat exchanger 7. Then, the heat and the heat medium are opposed to each other in the heat source side heat exchanger 7 to exchange heat, and the underground heat collected in the underground heat exchanger 10 is transferred to the refrigerant side of the heat pump unit 1. The heat source side heat exchanger 7 is pumped up and functions as an evaporator.

前記負荷熱交換部3は、負荷側に熱を与える前記負荷側熱交換器5と、被空調空間を加熱する床暖房パネル等の負荷端末14と、負荷側熱交換器5と負荷端末14を循環可能に環状に接続する負荷側循環回路15と、負荷側循環回路15に加熱用循環液を循環させる負荷側循環ポンプ16と、負荷端末14毎に分岐した負荷側循環回路15に各々設けられその開閉により負荷端末14への加熱用循環液の供給を制御する熱動弁17(17a、17b)とを備えているものである。なお、18は負荷側循環回路15に設けられ負荷側熱交換器5から負荷端末14に流入する加熱用循環液の温度を検出する負荷側往き温度センサである。   The load heat exchanging unit 3 includes the load side heat exchanger 5 that applies heat to the load side, a load terminal 14 such as a floor heating panel that heats the air-conditioned space, the load side heat exchanger 5 and the load terminal 14. The load side circulation circuit 15 is connected to the load side circulation circuit 15 so as to circulate, the load side circulation pump 16 circulates the circulating fluid for heating in the load side circulation circuit 15, and the load side circulation circuit 15 branched for each load terminal 14. A thermal valve 17 (17a, 17b) that controls the supply of the circulating fluid for heating to the load terminal 14 by opening and closing thereof is provided. Reference numeral 18 denotes a load-side forward temperature sensor that is provided in the load-side circulation circuit 15 and detects the temperature of the circulating fluid for heating flowing into the load terminal 14 from the load-side heat exchanger 5.

前記負荷端末14によって加熱される被空調空間には、リモコン(図示せず)が各々設置されており、このリモコンにより被空調空間の加熱の指示がなされると、圧縮機4及び及び地中熱循環ポンプ12及び負荷側循環ポンプ16の駆動が開始され、熱源側熱交換器7を蒸発器として機能させると共に、負荷側熱交換器5を凝縮器として機能させて負荷側を加熱する負荷運転としての暖房運転が行われる。この暖房運転の際、前記負荷側熱交換器5では、冷媒と加熱用循環液とが対向して流れて熱交換が行われ、負荷側熱交換器5にて加熱された加熱用循環液は、熱動弁17を介して負荷端末14に送られ、リモコンにより指示を受けた被空調空間を加熱するものである。   A remote control (not shown) is installed in each air-conditioned space heated by the load terminal 14. When the remote controller instructs to heat the air-conditioned space, the compressor 4 and the underground heat are provided. The driving of the circulation pump 12 and the load-side circulation pump 16 is started, and the load-side heat exchanger 7 functions as an evaporator and the load-side heat exchanger 5 functions as a condenser to heat the load side. The heating operation is performed. During the heating operation, in the load-side heat exchanger 5, the refrigerant and the heating circulating fluid flow oppositely to perform heat exchange, and the heating circulating fluid heated in the load-side heat exchanger 5 is The air-conditioned space that is sent to the load terminal 14 via the thermal valve 17 and received an instruction from the remote controller is heated.

19は冷媒温度センサ9、地中戻り温度センサ13、暖房往き温度センサ18の入力や前記リモコンからの信号を受けて、圧縮機4、膨張弁6、地中熱循環ポンプ12、負荷側循環ポンプ16の各アクチュエータの駆動を制御するマイコンを有する制御手段であり、制御手段19は前記暖房運転の際に、冷媒温度センサ9の検出する温度が所定の目標温度になるように地中熱循環ポンプ12の回転数を制御し地中熱循環回路11を循環する熱媒の流量を調整するものであり、また、負荷側往き温度センサ18の検出する温度が所定温度になるように圧縮機4を制御するものである。   Reference numeral 19 denotes an input of the refrigerant temperature sensor 9, the underground return temperature sensor 13, the heating temperature sensor 18, and a signal from the remote controller, and the compressor 4, the expansion valve 6, the underground heat circulation pump 12, and the load side circulation pump. The control means 19 includes a microcomputer for controlling the driving of each of the 16 actuators, and the control means 19 is a geothermal circulation pump so that the temperature detected by the refrigerant temperature sensor 9 becomes a predetermined target temperature during the heating operation. 12 to adjust the flow rate of the heat medium circulating in the underground heat circulation circuit 11 by controlling the rotational speed of the compressor 12, and the compressor 4 is set so that the temperature detected by the load side temperature sensor 18 becomes a predetermined temperature. It is something to control.

次に、図1に示す一実施形態の暖房運転時の作動について図2に示すフローチャートに基づき説明する。
前記リモコンにより負荷端末14による被空調空間の暖房の指示がなされると、前記制御手段19は圧縮機4、地中熱循環ポンプ12、負荷側循環ポンプ16の駆動を開始させ、前記暖房運転が開始される。ここで、暖房運転開始時において、地中熱循環ポンプ12は予め設定された一定回転数で駆動を開始させるものである。暖房運転が開始されると、前記負荷側熱交換器5では負荷側循環ポンプ16により循環される加熱用循環液と圧縮機4から吐出された高温高圧の冷媒とが熱交換され、加熱された加熱用循環液が負荷端末14に供給され被空調空間を加熱すると共に、熱源側熱交換器7では、地中熱循環ポンプ12により循環され地中熱交換器10を介して地中熱を採熱した熱媒と膨張弁6から吐出された低温低圧の冷媒とが熱交換され、地中熱により冷媒を加熱し蒸発させるものである。
Next, the action | operation at the time of the heating operation of one Embodiment shown in FIG. 1 is demonstrated based on the flowchart shown in FIG.
When the load terminal 14 instructs the heating of the air-conditioned space by the remote controller, the control means 19 starts driving the compressor 4, the geothermal circulation pump 12, and the load-side circulation pump 16, and the heating operation is performed. Be started. Here, at the start of the heating operation, the underground heat circulation pump 12 starts to be driven at a preset constant rotation speed. When the heating operation is started, in the load-side heat exchanger 5, the heating circulating liquid circulated by the load-side circulation pump 16 and the high-temperature and high-pressure refrigerant discharged from the compressor 4 are heat-exchanged and heated. The circulating fluid for heating is supplied to the load terminal 14 to heat the air-conditioned space, and in the heat source side heat exchanger 7, the ground heat is circulated by the ground heat circulation pump 12 and the ground heat is taken through the ground heat exchanger 10. Heat exchange between the heated heat medium and the low-temperature and low-pressure refrigerant discharged from the expansion valve 6 heats and evaporates the refrigerant by underground heat.

前記暖房運転中は、冷媒温度センサ9で熱源側熱交換器7側の冷媒の温度を検出し(ステップS1)、検出した冷媒の温度と前記所定の目標温度との比較を行うものである(ステップS2)。ここで、前記所定の目標温度は、ヒートポンプ装置を用いて予め行った試験によりシステムCOP(=「暖房出力÷(圧縮機4消費電力+地中熱循環ポンプ12消費電力)」とする)が良い値を示している時の熱源側熱交換器7側の冷媒の温度であり、その温度を所定の目標温度として設定し制御手段19に記憶しておくものである。なお、所定の目標温度は制御する上で±A℃のヒステリシスを有していてもよく、Aは0以上の任意の値を使用するものとする。   During the heating operation, the refrigerant temperature sensor 9 detects the temperature of the refrigerant on the heat source side heat exchanger 7 side (step S1), and compares the detected refrigerant temperature with the predetermined target temperature ( Step S2). Here, the predetermined target temperature may be a system COP (= “heating output ÷ (power consumption of the compressor 4 + power consumption of the underground heat circulation pump 12)”) by a test performed in advance using a heat pump device. This is the temperature of the refrigerant on the heat source side heat exchanger 7 side when the value is shown, and the temperature is set as a predetermined target temperature and stored in the control means 19. It should be noted that the predetermined target temperature may have a hysteresis of ± A ° C. for control, and A uses an arbitrary value of 0 or more.

前記ステップS2で、制御手段19は、冷媒温度センサ9で検出した冷媒の温度が所定の目標温度、ここでは5℃であるか否かを判断し、検出した冷媒の温度が所定の目標温度であると判断したら、それまでの地中熱循環ポンプ12の回転数を維持するように制御し地中熱循環回路11の熱媒の循環流量を一定に保つようにし(ステップS3)、前記ステップS1の処理に戻るものである。   In step S2, the control means 19 determines whether or not the refrigerant temperature detected by the refrigerant temperature sensor 9 is a predetermined target temperature, in this case, 5 ° C., and the detected refrigerant temperature is the predetermined target temperature. If it is determined that there is, the control is performed so as to maintain the rotation speed of the underground heat circulation pump 12 so far, and the circulation flow rate of the heat medium in the underground heat circulation circuit 11 is kept constant (step S3), and the step S1 is performed. It returns to the process of.

また、前記ステップS2にて、制御手段19は、検出した冷媒の温度が所定の目標温度でないと判断したら、検出した冷媒の温度が所定の目標温度より低いか否か判断し(ステップS4)、検出した冷媒の温度が所定の目標温度より低いと判断したら、地中熱循環ポンプ12の回転数を所定回転数増加させ、地中熱循環回路11の熱媒の循環流量を増加させ(ステップS5)、前記ステップS1の処理に戻るものである。一方、前記ステップS4にて、検出した冷媒の温度が所定の目標温度より高いと判断したら、地中熱循環ポンプ12の回転数を所定回転数減少させ、地中熱循環回路11の熱媒の循環流量を減少させ(ステップS6)、前記ステップS1の処理に戻るものである。   In step S2, if the control unit 19 determines that the detected refrigerant temperature is not the predetermined target temperature, the control unit 19 determines whether the detected refrigerant temperature is lower than the predetermined target temperature (step S4). If it is determined that the detected refrigerant temperature is lower than the predetermined target temperature, the rotation speed of the geothermal circulation pump 12 is increased by a predetermined rotation speed, and the circulation flow rate of the heat medium in the geothermal circulation circuit 11 is increased (step S5). ), The process returns to step S1. On the other hand, if it is determined in step S4 that the detected refrigerant temperature is higher than the predetermined target temperature, the rotation speed of the underground heat circulation pump 12 is decreased by a predetermined rotation speed, and the heat medium of the underground heat circulation circuit 11 is reduced. The circulating flow rate is decreased (step S6), and the process returns to step S1.

次に、図2のフローチャートで示した暖房運転の作動を、図3、図4のタイムチャートを用いて説明する。ここで、初期条件として前記所定の目標温度を5℃とし、負荷端末14の暖房運転において、制御手段19は負荷側往き温度センサ18で検出する熱媒の温度(暖房往き温度)が、例えば45℃になるように圧縮機4を制御するものとする。また、時間t0は、前記暖房運転が安定した後の任意の時間とする。なお、図3、図4中の蒸発側冷媒温度は、膨張弁6から吐出され圧縮機4に吸入されるまでの熱源側熱交換器7側の冷媒の温度とし、地中往き温度は、熱源側熱交換器7から流出する地中熱循環回路11の熱媒の温度であり、図9に示したタイムチャートの熱源往き温度に相当する温度である。   Next, the operation of the heating operation shown in the flowchart of FIG. 2 will be described using the time charts of FIGS. Here, the predetermined target temperature is set to 5 ° C. as an initial condition, and in the heating operation of the load terminal 14, the temperature of the heating medium (heating heating temperature) detected by the control means 19 with the load side going temperature sensor 18 is 45, for example. It is assumed that the compressor 4 is controlled so as to be at ° C. The time t0 is an arbitrary time after the heating operation is stabilized. 3 and 4 is the temperature of the refrigerant on the heat source side heat exchanger 7 side until it is discharged from the expansion valve 6 and sucked into the compressor 4, and the underground temperature is the heat source It is the temperature of the heat medium of the underground heat circulation circuit 11 flowing out from the side heat exchanger 7, and is a temperature corresponding to the heat source going temperature in the time chart shown in FIG.

まず、図3のタイムチャートから説明すると、時間t1において、冷媒温度センサ9で熱源側熱交換器7側の冷媒の温度を検出し(前記ステップS1)、制御手段19は、冷媒温度センサ9で検出した冷媒の温度が5℃であるか否かを判断し(前記ステップS2)、検出した冷媒の温度が5℃であるので、それまでの地中熱循環ポンプ12の回転数を維持する(前記ステップS3)。   First, the time chart of FIG. 3 will be described. At time t1, the refrigerant temperature sensor 9 detects the temperature of the refrigerant on the heat source side heat exchanger 7 side (step S1). It is determined whether or not the detected temperature of the refrigerant is 5 ° C. (step S2), and since the detected temperature of the refrigerant is 5 ° C., the rotation speed of the underground heat circulation pump 12 is maintained ( Step S3).

続いて、時間t1から時間t2にかけて暖房往き温度が低下していき、制御手段19は、時間t2において負荷側往き温度センサ18の検出する暖房往き温度が低下したことを検知すると、負荷端末14での暖房出力(負荷出力)が足りないとして、圧縮機4の回転数を増加させ始める。また、圧縮機4の回転数増加と連動して蒸発側冷媒温度が低下し始める。なお、時間t2においては、時間t1と同様に、前記ステップS1、前記ステップS2、前記ステップS3の順に処理を行うものである。   Subsequently, the heating going temperature decreases from time t1 to time t2, and when the control means 19 detects that the heating going temperature detected by the load side going temperature sensor 18 has dropped at time t2, the load terminal 14 As the heating output (load output) is insufficient, the rotation speed of the compressor 4 is increased. Further, the evaporation side refrigerant temperature starts to decrease in conjunction with the increase in the rotational speed of the compressor 4. At time t2, as in time t1, processing is performed in the order of step S1, step S2, and step S3.

そして、時間t2から時間t3にかけて蒸発側冷媒温度が低下していき、時間t3において、冷媒温度センサ9で熱源側熱交換器7側の冷媒の温度を検出し(前記ステップS1)、制御手段19は、冷媒温度センサ9で検出した冷媒の温度が5℃であるか否かを判断し(前記ステップS2)、検出した冷媒の温度が5℃ではないので、前記ステップS4の処理に進み、前記ステップS4で、検出した冷媒の温度が5℃より低いと判断し、地中熱循環ポンプ12の回転数をそれまでの回転数より所定回転数増加させる(前記ステップS5)。   Then, the evaporation side refrigerant temperature decreases from time t2 to time t3. At time t3, the refrigerant temperature sensor 9 detects the temperature of the refrigerant on the heat source side heat exchanger 7 side (step S1), and the control means 19 Determines whether or not the temperature of the refrigerant detected by the refrigerant temperature sensor 9 is 5 ° C. (step S2). Since the detected temperature of the refrigerant is not 5 ° C., the process proceeds to step S4. In step S4, it is determined that the detected temperature of the refrigerant is lower than 5 ° C., and the rotational speed of the underground heat circulation pump 12 is increased by a predetermined rotational speed from the previous rotational speed (step S5).

そうすると、時間t3から時間t4にかけて蒸発側冷媒温度が上昇していき、熱源側熱交換器7で地中熱交換部2側から汲み上げる採熱出力も増加していき、時間t4においては、時間t3と同様に、前記ステップS1、前記ステップS2、前記ステップS4、前記ステップS5の順に処理を行い、時間t4から時間t5にかけて蒸発側冷媒温度が上昇していき、熱源側熱交換器7で地中熱交換部2側から汲み上げる採熱出力も増加していく。   Then, the evaporation side refrigerant temperature rises from time t3 to time t4, and the heat collection output pumped from the underground heat exchanging unit 2 side by the heat source side heat exchanger 7 also increases. At time t4, time t3 In the same manner as in step S1, step S2, step S4, and step S5, the evaporation side refrigerant temperature rises from time t4 to time t5, and the heat source side heat exchanger 7 The heat collection output pumped from the heat exchange part 2 side also increases.

そして、時間t5において、冷媒温度センサ9で熱源側熱交換器7側の冷媒の温度を検出し(前記ステップS1)、制御手段19は、冷媒温度センサ9で検出した冷媒の温度が5℃であるか否かを判断し(前記ステップS2)、検出した冷媒の温度が5℃であるので、それまでの地中熱循環ポンプ12の回転数を維持する(前記ステップS3)と共に、暖房往き温度が45℃で所望の暖房出力となり、時間t5以降は安定した暖房運転を継続するものである。   At time t5, the refrigerant temperature sensor 9 detects the temperature of the refrigerant on the heat source side heat exchanger 7 side (step S1), and the control means 19 detects that the refrigerant temperature detected by the refrigerant temperature sensor 9 is 5 ° C. It is determined whether or not there is (step S2), and since the detected refrigerant temperature is 5 ° C., the rotation speed of the geothermal circulation pump 12 up to that point is maintained (step S3) and the heating temperature Becomes a desired heating output at 45 ° C., and after time t5, stable heating operation is continued.

次に、図4のタイムチャートを説明すると、時間t1において、冷媒温度センサ9で熱源側熱交換器7側の冷媒の温度を検出し(前記ステップS1)、制御手段19は、冷媒温度センサ9で検出した冷媒の温度が5℃であるか否かを判断し(前記ステップS2)、検出した冷媒の温度が5℃であるので、それまでの地中熱循環ポンプ12の回転数を維持する(前記ステップS3)。   Next, the time chart of FIG. 4 will be described. At time t1, the refrigerant temperature sensor 9 detects the temperature of the refrigerant on the heat source side heat exchanger 7 side (step S1). It is determined whether or not the temperature of the refrigerant detected in step 5 is 5 ° C. (step S2). Since the detected temperature of the refrigerant is 5 ° C., the rotation speed of the underground heat circulation pump 12 is maintained. (Step S3).

続いて、時間t1から時間t2にかけて暖房往き温度が上昇していき、制御手段19は、時間t2において負荷側往き温度センサ18の検出する暖房往き温度が上昇したことを検知すると、負荷端末14での暖房出力が過剰だとして、圧縮機4の回転数を減少させ始める。また、圧縮機4の回転数減少と連動して蒸発側冷媒温度が上昇し始める。なお、時間t2においては、時間t1と同様に、前記ステップS1、前記ステップS2、前記ステップS3の順に処理を行うものである。   Subsequently, the heating going temperature rises from time t1 to time t2, and when the control means 19 detects that the heating going temperature detected by the load side going temperature sensor 18 has risen at time t2, the load terminal 14 The heating speed of the compressor 4 is excessive, and the rotation speed of the compressor 4 is started to decrease. Further, the evaporation side refrigerant temperature starts to rise in conjunction with a decrease in the rotational speed of the compressor 4. At time t2, as in time t1, processing is performed in the order of step S1, step S2, and step S3.

そして、時間t2から時間t3にかけて蒸発側冷媒温度が上昇していき、時間t3において、冷媒温度センサ9で熱源側熱交換器7側の冷媒の温度を検出し(前記ステップS1)、制御手段19は、冷媒温度センサ9で検出した冷媒の温度が5℃であるか否かを判断し(前記ステップS2)、検出した冷媒の温度が5℃ではないので、前記ステップS4の処理に進み、前記ステップS4で、検出した冷媒の温度が5℃より高いと判断し、地中熱循環ポンプ12の回転数をそれまでの回転数より所定回転数減少させる(前記ステップS6)。   Then, the evaporation side refrigerant temperature rises from time t2 to time t3. At time t3, the refrigerant temperature sensor 9 detects the temperature of the refrigerant on the heat source side heat exchanger 7 side (step S1), and the control means 19 Determines whether or not the temperature of the refrigerant detected by the refrigerant temperature sensor 9 is 5 ° C. (step S2). Since the detected temperature of the refrigerant is not 5 ° C., the process proceeds to step S4. In step S4, it is determined that the detected temperature of the refrigerant is higher than 5 ° C., and the rotational speed of the underground heat circulation pump 12 is decreased by a predetermined rotational speed from the rotational speed up to that point (step S6).

そうすると、時間t3から時間t4にかけて蒸発側冷媒温度が減少していき、熱源側熱交換器7で地中熱交換部2側から汲み上げる採熱出力も減少していき、時間t4においては、時間t3と同様に、前記ステップS1、前記ステップS2、前記ステップS4、前記ステップS6の順に処理を行い、時間t4から時間t5にかけて蒸発側冷媒温度が減少していき、熱源側熱交換器7で地中熱交換部2側から汲み上げる採熱出力も減少していく。   Then, the evaporation side refrigerant temperature decreases from the time t3 to the time t4, and the heat collection output pumped from the underground heat exchanging unit 2 side by the heat source side heat exchanger 7 also decreases. At the time t4, the time t3 In the same manner as above, the processing is performed in the order of Step S1, Step S2, Step S4, and Step S6. The evaporation side refrigerant temperature decreases from time t4 to time t5, and the heat source side heat exchanger 7 The heat collection output pumped from the heat exchange part 2 side also decreases.

そして、時間t5において、冷媒温度センサ9で熱源側熱交換器7側の冷媒の温度を検出し(前記ステップS1)、制御手段19は、冷媒温度センサ9で検出した冷媒の温度が5℃であるか否かを判断し(前記ステップS2)、検出した冷媒の温度が5℃であるので、それまでの地中熱循環ポンプ12の回転数を維持する(前記ステップS3)と共に、暖房往き温度が45℃で所望の暖房出力となり、時間t5以降は安定した暖房運転を継続するものである。   At time t5, the refrigerant temperature sensor 9 detects the temperature of the refrigerant on the heat source side heat exchanger 7 side (step S1), and the control means 19 detects that the refrigerant temperature detected by the refrigerant temperature sensor 9 is 5 ° C. It is determined whether or not there is (step S2), and since the detected refrigerant temperature is 5 ° C., the rotation speed of the geothermal circulation pump 12 up to that point is maintained (step S3) and the heating temperature Becomes a desired heating output at 45 ° C., and after time t5, stable heating operation is continued.

なお、上述の暖房運転において、制御手段19は、冷媒温度センサ9の検出する冷媒温度を監視することで、暖房出力(負荷出力)の変動を素早く把握することができたが、例えば暖房出力に変動がなく一定の状態で推移している時に、地盤G中の熱を連続して採熱したために地盤G中の温度が低下してきた場合においても、冷媒温度センサ9の検出する冷媒温度は低下するので、制御手段19は、冷媒温度センサ9の検出する冷媒温度を監視することで、地盤G中の温度の変動、すなわち採熱出力の変動も素早く把握することができ、その場合も制御手段19は、冷媒温度センサ9の検出する冷媒温度が所定の目標温度になるように地中熱循環ポンプ12の回転数を制御するものである。   In the heating operation described above, the control unit 19 can quickly grasp the fluctuation of the heating output (load output) by monitoring the refrigerant temperature detected by the refrigerant temperature sensor 9. The refrigerant temperature detected by the refrigerant temperature sensor 9 is lowered even when the temperature in the ground G is lowered because the heat in the ground G is continuously collected when there is no fluctuation and the temperature is constant. Therefore, the control means 19 can quickly grasp the temperature fluctuation in the ground G, that is, the fluctuation of the heat collection output by monitoring the refrigerant temperature detected by the refrigerant temperature sensor 9, and also in this case, the control means 19 controls the rotational speed of the underground heat circulation pump 12 so that the refrigerant temperature detected by the refrigerant temperature sensor 9 becomes a predetermined target temperature.

以上説明した暖房運転において、制御手段19は、冷媒温度センサ9で熱源側熱交換器7側の冷媒の温度を検出し(前記ステップS1)、検出した冷媒の温度と所定の目標温度との比較を行い(前記ステップS2)、冷媒温度センサ9の検出する温度が所定の目標温度になるように地中熱循環ポンプ12の回転数を制御し(前記ステップS3、S5、S6)、地中熱循環回路11を循環する熱媒の流量を調整することで、最適な採熱を行わせて所望の暖房出力を出力するまでの時間を短縮することができると共に、ヒートポンプ装置のシステムCOPを高く維持したまま暖房運転を行うことができるものである。   In the heating operation described above, the control means 19 detects the temperature of the refrigerant on the heat source side heat exchanger 7 side with the refrigerant temperature sensor 9 (step S1), and compares the detected refrigerant temperature with a predetermined target temperature. (Step S2), and the number of revolutions of the geothermal circulation pump 12 is controlled so that the temperature detected by the refrigerant temperature sensor 9 becomes a predetermined target temperature (steps S3, S5, S6). By adjusting the flow rate of the heat medium that circulates in the circulation circuit 11, it is possible to shorten the time required to perform optimum heat collection and output the desired heating output, and to maintain the system COP of the heat pump device high. Heating operation can be carried out with this.

また、前記所定の目標温度は、前記暖房運転時の作動を表す図5のフローチャートに示すように、地中戻り温度センサ13の検出する熱媒の温度に応じて設定するようにしてもよい。詳細に説明すると、暖房運転中において、制御手段19は、地中戻り温度センサ13の検出する熱媒の温度を検出し(ステップS7)、検出した熱媒の温度が予め設定した所定温度、例えば10℃より低いか否か判断し(ステップS8)、検出した熱媒の温度が予め設定した所定温度より低いと判断したら、所定の目標温度をα℃、例えば5℃に設定し(ステップS9)、一方、前記ステップS8で、検出した熱媒の温度が予め設定した所定温度以上と判断したら、所定の目標温度をβ(β>αとする)℃、例えば7℃に設定し(ステップS10)、前記ステップS9または前記ステップS10の処理が行われた後は、図2のフローチャートで示した前記ステップS1〜前記ステップS6の処理と同じ処理をステップS11〜ステップS16にて行い、前記ステップS7の処理に戻るものである。   The predetermined target temperature may be set according to the temperature of the heat medium detected by the underground return temperature sensor 13 as shown in the flowchart of FIG. 5 representing the operation during the heating operation. More specifically, during the heating operation, the control means 19 detects the temperature of the heat medium detected by the underground return temperature sensor 13 (step S7), and the detected temperature of the heat medium is set to a predetermined temperature, for example, It is determined whether or not the temperature is lower than 10 ° C. (step S8). If it is determined that the detected temperature of the heat medium is lower than a predetermined temperature set in advance, the predetermined target temperature is set to α ° C., for example, 5 ° C. (step S9). On the other hand, if it is determined in step S8 that the detected temperature of the heat medium is equal to or higher than a predetermined temperature, a predetermined target temperature is set to β (β> α) ° C., for example, 7 ° C. (step S10). After the process of step S9 or step S10 is performed, the same process as the process of step S1 to step S6 shown in the flowchart of FIG. 2 is performed in step S11 to step S16. Performed, in which the process returns to the step S7.

このように、制御手段19は、暖房運転中に、地中戻り温度センサ13の検出する熱媒の温度が高い程、つまり熱源側が保有する熱量に余裕がある程、所定の目標温度を高い温度に設定するようにすると、所定の目標温度を高くした分、圧縮機4へ吸入される冷媒温度が高くなり、そうすると、圧縮機4から吐出される冷媒温度、例えば70℃を得ようとした場合、圧縮機4への吸入冷媒温度が低い場合に比べて圧縮機4への吸入冷媒温度が高い方が圧縮機4の回転数が小さくて済む、すなわち圧縮機4の消費電力が小さくて済むのである。よって、暖房運転中に、地中戻り温度センサ13の検出する熱媒の温度が高い程、所定の目標温度を高い温度に設定することで、ヒートポンプ装置のCOP(=「暖房出力÷圧縮機104消費電力」とする)向上、ひいてはシステムCOPを向上させることができるものである。   Thus, during the heating operation, the control means 19 increases the predetermined target temperature as the temperature of the heat medium detected by the underground return temperature sensor 13 increases, that is, as the amount of heat held on the heat source side has a margin. When the predetermined target temperature is increased, the refrigerant temperature sucked into the compressor 4 is increased, so that the refrigerant temperature discharged from the compressor 4, for example, 70 ° C. is obtained. As compared with the case where the intake refrigerant temperature to the compressor 4 is low, the higher the intake refrigerant temperature to the compressor 4, the smaller the rotation speed of the compressor 4, that is, the lower the power consumption of the compressor 4. is there. Therefore, during heating operation, the higher the temperature of the heat medium detected by the underground return temperature sensor 13 is, the higher the predetermined target temperature is set, so that the COP (= “heating output ÷ compressor 104” of the heat pump device is set. It is possible to improve the "power consumption" and thus the system COP.

なお、制御手段19は、前記ステップS8で、地中戻り温度センサ13で検出した熱媒の温度が予め設定した所定温度より低いか否か判断し、前記ステップS9または前記ステップS10で、所定の目標温度をα℃またはβ℃にするようにしたが、地中戻り温度センサ13の検出する熱媒の温度が高い程、所定の目標温度を高い温度に設定してあればよく、例えば、予め行った試験により、地中戻り温度センサ13で検出する温度毎に所定の目標温度を対応させたデータテーブルを制御手段19に記憶させておいてもよいものである。   The control means 19 determines whether or not the temperature of the heat medium detected by the underground return temperature sensor 13 is lower than a predetermined temperature set in advance in step S8, and in step S9 or step S10, the predetermined temperature is determined. Although the target temperature is set to α ° C. or β ° C., the higher the temperature of the heat medium detected by the underground return temperature sensor 13, the higher the predetermined target temperature may be set. A data table in which a predetermined target temperature is associated with each temperature detected by the underground return temperature sensor 13 may be stored in the control means 19 based on the test performed.

また、本発明は上記の一実施形態に限定されるものではなく、本実施形態では、床暖房パネル等の負荷端末14により被空調空間である室内を加熱する暖房運転時に本発明の制御を適用したが、図6に示すように、負荷端末14が給湯等に使用する湯水を貯湯する貯湯タンク20であり、負荷運転として貯湯タンク20内の湯水を沸き上げる沸き上げ運転に本発明の制御を適用してもよいものであり、また、図7に示すように、負荷運転として空調用の室内機21による暖房運転に本発明の制御を適用してもよいものであり、本発明の要旨を変更しない範囲で様々な変形が可能であり、これを妨げるものではない。   Further, the present invention is not limited to the above-described embodiment. In the present embodiment, the control of the present invention is applied during a heating operation in which a room that is an air-conditioned space is heated by a load terminal 14 such as a floor heating panel. However, as shown in FIG. 6, the load terminal 14 is a hot water storage tank 20 for storing hot water used for hot water supply or the like, and the control of the present invention is applied to a boiling operation for boiling hot water in the hot water storage tank 20 as a load operation. Further, as shown in FIG. 7, the control of the present invention may be applied to the heating operation by the indoor unit 21 for air conditioning as the load operation. Various modifications are possible within the range not changed, and this is not disturbed.

また、本実施形態では、地盤G中に埋設された複数の地中熱交換器10は互いに並列に接続されているが、複数の地中熱交換器10を互いに直列に接続してもよく、さらに、地中熱交換器10を複数埋設せず、地盤G中から所望の採熱ができるのであれば、地中熱交換器10を1本だけ埋設したものであってもよい。   In the present embodiment, the plurality of underground heat exchangers 10 embedded in the ground G are connected in parallel to each other, but the plurality of underground heat exchangers 10 may be connected in series to each other, Furthermore, as long as desired heat collection can be performed from the ground G without embedding a plurality of underground heat exchangers 10, only one underground heat exchanger 10 may be embedded.

また、本実施形態では、熱媒循環式の熱源部として、地盤G中の地中熱を地中熱交換器10で採熱する地中熱交換部2を採用したが、熱源部としては、川・湖・海の水を循環させて熱源側熱交換器7の冷媒を加熱するような熱媒循環式のものでもよく、さらに、貯湯タンクに貯湯された湯水を直接的または間接的に利用して熱源側熱交換器7の冷媒を加熱するような熱媒循環式のものでもよく、本発明の要旨を変更しない範囲で様々な変形が可能であり、これを妨げるものではない。   Moreover, in this embodiment, although the underground heat exchange part 2 which collects the underground heat in the ground G with the underground heat exchanger 10 was employ | adopted as a heat-medium circulation type heat source part, It may be a heat medium circulation type that circulates water in the river, lake, or sea to heat the refrigerant in the heat source side heat exchanger 7, and directly or indirectly uses hot water stored in a hot water storage tank. Then, a heat medium circulation type that heats the refrigerant of the heat source side heat exchanger 7 may be used, and various modifications are possible without departing from the scope of the present invention, and this is not disturbed.

2 地中熱交換部
4 圧縮機
5 負荷側熱交換器
6 膨張弁
7 熱源側熱交換器
8 ヒートポンプ回路
9 冷媒温度センサ
10 地中熱交換器
11 地中熱循環回路
12 地中熱循環ポンプ
13 地中戻り温度センサ
19 制御手段
DESCRIPTION OF SYMBOLS 2 Ground heat exchange part 4 Compressor 5 Load side heat exchanger 6 Expansion valve 7 Heat source side heat exchanger 8 Heat pump circuit 9 Refrigerant temperature sensor 10 Ground heat exchanger 11 Ground heat circulation circuit 12 Ground heat circulation pump 13 Underground return temperature sensor 19 Control means

Claims (1)

圧縮機、負荷側熱交換器、減圧手段、熱源側熱交換器を冷媒配管で環状に接続したヒートポンプ回路と、前記熱源側熱交換器の冷媒を加熱する熱媒循環式の熱源部と、該熱源部の熱源と前記熱源側熱交換器との間を熱媒配管で環状に接続した熱源側循環回路と、該熱源側循環回路に熱媒を循環させる熱源側循環ポンプと、熱源側熱交換器側の冷媒の温度を検出する冷媒温度検出手段と、これらの作動を制御する制御手段とを備え、前記熱源側熱交換器を蒸発器として機能させると同時に、前記負荷側熱交換器を凝縮器として機能させて負荷側を加熱する負荷運転を行うヒートポンプ装置であって、前記制御手段は、前記負荷運転中に、前記冷媒温度検出手段の検出する温度が所定の目標温度になるように前記熱源側循環ポンプの回転数を制御するもので、前記冷媒温度検出手段の目標温度は、前記熱源側熱交換器に流入する熱媒の温度を検出する熱源側戻り温度検出手段が、検出する戻り温度が高い程、高い温度に変更するようにしたことを特徴とするヒートポンプ装置。 A heat pump circuit in which a compressor, a load-side heat exchanger, a decompression unit, a heat source-side heat exchanger are connected in a ring shape with a refrigerant pipe, a heat medium circulation type heat source for heating the refrigerant of the heat source-side heat exchanger, A heat source side circulation circuit in which the heat source of the heat source unit and the heat source side heat exchanger are annularly connected by a heat medium pipe, a heat source side circulation pump that circulates the heat medium in the heat source side circulation circuit, and heat source side heat exchange A refrigerant temperature detecting means for detecting the temperature of the refrigerant on the heater side, and a control means for controlling the operation of the refrigerant. The heat source side heat exchanger functions as an evaporator and at the same time the load side heat exchanger is condensed. A heat pump device that performs a load operation for heating the load side by functioning as a vessel, wherein the control means is configured so that the temperature detected by the refrigerant temperature detection means becomes a predetermined target temperature during the load operation. Controls the rotation speed of the heat source side circulation pump But that, a target temperature of the refrigerant temperature detecting means, the heat source-side return temperature detecting means for detecting the temperature of the heating medium flowing into the heat source side heat exchanger, as the return temperature detected is high, changes to a higher temperature A heat pump device characterized by that.
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