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JP6134856B2 - Heat source equipment - Google Patents
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JP6134856B2 - Heat source equipment - Google Patents

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JP6134856B2
JP6134856B2 JP2016504158A JP2016504158A JP6134856B2 JP 6134856 B2 JP6134856 B2 JP 6134856B2 JP 2016504158 A JP2016504158 A JP 2016504158A JP 2016504158 A JP2016504158 A JP 2016504158A JP 6134856 B2 JP6134856 B2 JP 6134856B2
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flow rate
heat source
heat
heat medium
water
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JPWO2015125863A1 (en
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勇司 松本
勇司 松本
誠二 築山
誠二 築山
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Carrier Japan Corp
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Toshiba Carrier Corp
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B13/00Compression machines, plants or systems, with reversible cycle
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F11/00Control or safety arrangements
    • F24F11/70Control systems characterised by their outputs; Constructional details thereof
    • F24F11/80Control systems characterised by their outputs; Constructional details thereof for controlling the temperature of the supplied air
    • F24F11/83Control systems characterised by their outputs; Constructional details thereof for controlling the temperature of the supplied air by controlling the supply of heat-exchange fluids to heat-exchangers
    • F24F11/85Control systems characterised by their outputs; Constructional details thereof for controlling the temperature of the supplied air by controlling the supply of heat-exchange fluids to heat-exchangers using variable-flow pumps
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F11/00Control or safety arrangements
    • F24F11/70Control systems characterised by their outputs; Constructional details thereof
    • F24F11/80Control systems characterised by their outputs; Constructional details thereof for controlling the temperature of the supplied air
    • F24F11/83Control systems characterised by their outputs; Constructional details thereof for controlling the temperature of the supplied air by controlling the supply of heat-exchange fluids to heat-exchangers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F11/00Control or safety arrangements
    • F24F11/70Control systems characterised by their outputs; Constructional details thereof
    • F24F11/80Control systems characterised by their outputs; Constructional details thereof for controlling the temperature of the supplied air
    • F24F11/83Control systems characterised by their outputs; Constructional details thereof for controlling the temperature of the supplied air by controlling the supply of heat-exchange fluids to heat-exchangers
    • F24F11/84Control systems characterised by their outputs; Constructional details thereof for controlling the temperature of the supplied air by controlling the supply of heat-exchange fluids to heat-exchangers using valves
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B41/00Fluid-circulation arrangements
    • F25B41/20Disposition of valves, e.g. of on-off valves or flow control valves
    • F25B41/26Disposition of valves, e.g. of on-off valves or flow control valves of fluid flow reversing valves
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B5/00Compression machines, plants or systems, with several evaporator circuits, e.g. for varying refrigerating capacity
    • F25B5/02Compression machines, plants or systems, with several evaporator circuits, e.g. for varying refrigerating capacity arranged in parallel
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2313/00Compression machines, plants or systems with reversible cycle not otherwise provided for
    • F25B2313/003Indoor unit with water as a heat sink or heat source
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2313/00Compression machines, plants or systems with reversible cycle not otherwise provided for
    • F25B2313/025Compression machines, plants or systems with reversible cycle not otherwise provided for using multiple outdoor units
    • F25B2313/0253Compression machines, plants or systems with reversible cycle not otherwise provided for using multiple outdoor units in parallel arrangements
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2400/00Component parts or details not otherwise provided for in this subclass
    • F25B2400/06Several compression cycles arranged in parallel

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Fluid Mechanics (AREA)
  • Air Conditioning Control Device (AREA)
  • Other Air-Conditioning Systems (AREA)

Description

本発明は、複数の熱源機を備えた熱源装置に関する。   The present invention relates to a heat source device including a plurality of heat source machines.

複数の熱源機を備え、これら熱源機の運転により得られる温熱または冷熱を負荷側(利用側)に供給する熱源装置が知られている。   2. Description of the Related Art A heat source device that includes a plurality of heat source devices and supplies hot or cold energy obtained by operating these heat source devices to a load side (use side) is known.

熱源機は、ポンプの運転により熱媒体(水やブライン等)を取込み、取込んだ熱媒体をヒートポンプ式冷凍サイクルの運転により加熱または冷却する。   The heat source machine takes in a heat medium (water, brine, etc.) by operating the pump, and heats or cools the captured heat medium by operating the heat pump refrigeration cycle.

各熱源機は熱媒体配管を介して互いに並列接続され、これら熱源機の運転台数が負荷に応じて制御される。   The heat source devices are connected in parallel to each other through a heat medium pipe, and the number of operating heat source devices is controlled according to the load.

特開2008−224182号公報JP 2008-224182 A

複数の熱源機を運転する場合、その各熱源機のポンプの能力が負荷側の要求能力に応じて制御される。   When operating a plurality of heat source machines, the capacity of the pump of each heat source machine is controlled according to the required capacity on the load side.

ただし、運転する複数の熱源機の配管抵抗が互いに異なる場合、各熱源機に流れる熱媒体の流量に差異が生じ、流量が少ない側の熱源機のポンプが失速して異常停止する可能性がある。   However, when the piping resistance of the plurality of heat source units to be operated is different from each other, there is a possibility that the flow rate of the heat medium flowing to each heat source unit will be different, and the pump of the heat source unit on the side with the lower flow rate may stall and stop abnormally .

本実施形態の目的は、熱源機におけるポンプの異常停止を生じることなく、適正な量の温熱または冷熱を負荷側に供給できる信頼性にすぐれた熱源装置を提供することである。   An object of the present embodiment is to provide a heat source device with excellent reliability capable of supplying an appropriate amount of hot or cold to the load side without causing an abnormal stop of the pump in the heat source machine.

請求項1の熱源装置は、熱媒体が流れる熱媒体熱交換器、この熱媒体熱交換器内の前記熱媒体を加熱または冷却するヒートポンプ式冷凍サイクル、負荷側を経た熱媒体を吸込み前記熱媒体熱交換器に通して前記負荷側へ送出するポンプを含み、互いに並列に配管接続された複数の熱源機と、前記負荷側に流れる前記熱媒体の量を調整する第1流量調整弁と、前記負荷側に流れる前記熱媒体の量を検知する流量検知部と、前記負荷側へと流れる前記熱媒体をバイパスするバイパス配管と、前記バイパス配管に流れる前記熱媒体の量を調整する第2流量調整弁と、前記バイパス配管の両端間における前記熱媒体の圧力差Pを検知する第1差圧検知部と、前記各熱媒体熱交換器の両端間における前記熱媒体の圧力差Pwを検知する第2差圧検知部と、コントローラとを備える。コントローラは、前記負荷側に流れる前記熱媒体の量Qと前記バイパス配管の両端間における前記熱媒体の圧力差Pとの関係を表わす負荷側配管抵抗特性を検出する第1検出部と;前記負荷側の要求能力に応じて前記各熱源機の運転台数および前記第1流量調整弁の開度を制御する第1制御部と;運転中の前記各熱源機の個々に流れる前記熱媒体の量Wを、前記第2圧力差検知部の検知圧力差Pwに基づき検出する第2検出部と;前記流量検知部の検知流量Qtおよび前記第1検出部で検出した負荷側配管抵抗特性に応じて、前記第2流量調整弁の開度を制御する第2制御部と;前記流量検知部の検知流量Qtを運転中の前記各熱源機に配分してそれぞれ必要流量Wtとして割当て、これら必要流量Wtに前記第2検出部の各検出流量Wが一致するように、運転中の前記各熱源機における前記ポンプの能力を制御する第3制御部と;を含む。 The heat source device according to claim 1 is a heat medium heat exchanger through which a heat medium flows, a heat pump refrigeration cycle that heats or cools the heat medium in the heat medium heat exchanger, and a heat medium that sucks in a heat medium that has passed through a load side. A plurality of heat source devices including a pump that passes through a heat exchanger to the load side and is connected in parallel to each other; a first flow rate adjustment valve that adjusts the amount of the heat medium flowing to the load side; A flow rate detection unit that detects the amount of the heat medium that flows to the load side, a bypass pipe that bypasses the heat medium that flows to the load side, and a second flow rate adjustment that adjusts the amount of the heat medium that flows to the bypass pipe A first differential pressure detection unit that detects a pressure difference P of the heat medium between both ends of the valve, the bypass pipe, and a first differential pressure detection unit that detects the pressure difference Pw of the heat medium between both ends of each heat medium heat exchanger. 2 differential pressure detector and And a controller. A controller for detecting a load-side pipe resistance characteristic representing a relationship between an amount Q of the heat medium flowing to the load side and a pressure difference P of the heat medium between both ends of the bypass pipe; A first control unit that controls the number of operating heat source units and the opening of the first flow rate adjusting valve according to the required capacity on the side; the amount W of the heat medium that flows individually in each operating heat source unit In accordance with the detected flow difference Pw of the second pressure difference detection unit, the detected flow rate Qt of the flow rate detection unit and the load side pipe resistance characteristic detected by the first detection unit, A second control unit that controls the opening of the second flow rate adjustment valve; and the detected flow rate Qt of the flow rate detection unit is allocated to each of the heat source units that are in operation and assigned as the required flow rate Wt. Each detection flow rate W of the second detection unit is one. As to a third control unit for controlling the capacity of the pump in each of the heat source machines in operation; including.

一実施形態の全体的な構成を示す図。The figure which shows the whole structure of one Embodiment. 一実施形態における各熱源機の冷凍サイクルの構成を示す図。The figure which shows the structure of the refrigerating cycle of each heat-source equipment in one Embodiment. 一実施形態におけるコントローラの制御を示すフローチャート。The flowchart which shows control of the controller in one Embodiment. 一実施形態における負荷側配管抵抗特性を示す図。The figure which shows the load side piping resistance characteristic in one Embodiment. 一実施形態の各熱源機における水の流量とポンプ能力との関係を示す図。The figure which shows the relationship between the flow volume of the water in each heat source machine of one Embodiment, and pump capability.

以下、本発明の熱源装置の一実施形態について図面を参照して説明する。
図1に示すように、複数の熱源機1a,1b,…1nに、熱媒体配管(以下、水配管という)2aおよび熱媒体配管(以下、水配管という)2bを介して、負荷側の機器である例えば複数の空気熱交換器3a,3b,…3nが接続される。熱源機1a,1b,…1nは、水配管2a,2bを介して互いに並列接続された状態にある。空気熱交換器3a,3b,…3nも、水配管2a,2bを介して互いに並列接続された状態にある。
Hereinafter, an embodiment of a heat source device of the present invention will be described with reference to the drawings.
As shown in FIG. 1, load-side equipment is connected to a plurality of heat source units 1a, 1b,... 1n via a heat medium pipe (hereinafter referred to as water pipe) 2a and a heat medium pipe (hereinafter referred to as water pipe) 2b. For example, a plurality of air heat exchangers 3a, 3b,... 3n are connected. The heat source machines 1a, 1b,... 1n are connected in parallel to each other through the water pipes 2a, 2b. The air heat exchangers 3a, 3b,... 3n are also connected in parallel to each other through the water pipes 2a, 2b.

水配管2aは、空気熱交換器3a,3b,…3nの水流入口につながる複数の枝管2aa,2ab,…2anを含む。水配管2bは、空気熱交換器3a,3b,…3nの水流出口につながる複数の枝管2ba,2bb,…2bnを含む。   The water pipe 2a includes a plurality of branch pipes 2aa, 2ab, ... 2an connected to the water inlets of the air heat exchangers 3a, 3b, ... 3n. The water pipe 2b includes a plurality of branch pipes 2ba, 2bb, ... 2bn connected to the water outlets of the air heat exchangers 3a, 3b, ... 3n.

熱源機1a,1b,…1nは、熱媒体熱交換器(後述の水熱交換器60,30)、ヒートポンプ式冷凍サイクル、およびポンプ(後述のポンプ80)を備え、負荷側を経た水配管2b内の水(熱媒体)を上記ポンプの吸入圧により熱媒体熱交換器に導入し、その熱媒体熱交換器内の水を上記ヒートポンプ式冷凍サイクルの運転により加熱または冷却し、その加熱または冷却した水を上記ポンプの吐出圧により水配管2aに供給する。   The heat source devices 1a, 1b,... 1n include a heat medium heat exchanger (water heat exchangers 60 and 30 described later), a heat pump refrigeration cycle, and a pump (a pump 80 described later), and a water pipe 2b passing through the load side. Water (heat medium) is introduced into the heat medium heat exchanger by the suction pressure of the pump, and the water in the heat medium heat exchanger is heated or cooled by the operation of the heat pump refrigeration cycle. The supplied water is supplied to the water pipe 2a by the discharge pressure of the pump.

空気熱交換器3a,3b,…3nは、水配管2aから流入する水の熱と室内ファンから送られる室内空気の熱とを交換し、この熱交換後の水を水配管2bへ流出する。   The air heat exchangers 3a, 3b,... 3n exchange the heat of the water flowing in from the water pipe 2a and the heat of the indoor air sent from the indoor fan, and flow out the water after the heat exchange to the water pipe 2b.

水配管2bの枝管2ba,2bb,…2bnに、開度可変の流量調整弁(第1流量調整弁)4a,4b,…4nがそれぞれ配設される。流量調整弁4a,4b,…4nは、空気熱交換器3a,3b,…3nの個々に流れる水の量を開度変化により調整する。   .. 2bn are provided with variable flow rate adjusting valves (first flow rate adjusting valves) 4a, 4b,... 4n on the branch pipes 2ba, 2bb,. The flow rate adjusting valves 4a, 4b,... 4n adjust the amount of water flowing individually in the air heat exchangers 3a, 3b,.

水配管2bにおいて、枝管2ba,2bb,…2bnより下流側の位置に、流量センサ(流量検知部)5が配置される。流量センサ5は、空気熱交換器3a,3b,…3nから流出する水の量(総量)を、空気熱交換器3a,3b,…3nに流れる水の量(総量)Qtとして、検知する。   In the water pipe 2b, a flow rate sensor (flow rate detector) 5 is arranged at a position downstream of the branch pipes 2ba, 2bb,... 2bn. The flow sensor 5 detects the amount (total amount) of water flowing out from the air heat exchangers 3a, 3b,... 3n as the amount (total amount) of water flowing into the air heat exchangers 3a, 3b,.

水配管2aにおける熱源機1a,1b,…1nの接続位置と、空気熱交換器3a,3b,…3nの接続位置との間に、バイパス配管6の一端が接続される。バイパス配管6の他端は、水配管2bにおける流量センサ5より下流側の位置に接続される。バイパス配管6は、熱源機1a,1b,…1nから空気熱交換器3a,3b,…3nへと向かって流れる水をバイパスして熱源機1a,1b,…1n側に戻す。このバイパス配管6の中途部に、開度可変の流量調整弁(第2流量調整弁)7が配設される。流量調整弁7は、バイパス弁とも称し、バイパス配管6に流れる水の量を開度変化により調整する。   One end of the bypass pipe 6 is connected between the connection position of the heat source devices 1a, 1b,... 1n in the water pipe 2a and the connection position of the air heat exchangers 3a, 3b,. The other end of the bypass pipe 6 is connected to a position downstream of the flow rate sensor 5 in the water pipe 2b. The bypass pipe 6 bypasses the water flowing toward the air heat exchangers 3a, 3b, ... 3n from the heat source machines 1a, 1b, ... 1n and returns them to the heat source machines 1a, 1b, ... 1n side. A flow rate adjustment valve (second flow rate adjustment valve) 7 having a variable opening is disposed in the middle of the bypass pipe 6. The flow rate adjusting valve 7 is also referred to as a bypass valve, and adjusts the amount of water flowing through the bypass pipe 6 by changing the opening.

流量調整弁7が全閉した場合、配管2a内の水はバイパス配管6に流入することなく負荷側へ流れる。流量調整弁7が開いた場合、配管2a内の水のうち、流量調整弁7の開度に比例する量の水が、バイパス配管6を通って配管2bに流れる。配管2a内の水のうち、バイパス配管6に流入しなかった水が、負荷側へ流れる。   When the flow rate adjustment valve 7 is fully closed, the water in the pipe 2 a flows to the load side without flowing into the bypass pipe 6. When the flow regulating valve 7 is opened, an amount of water in proportion to the opening of the flow regulating valve 7 out of the water in the pipe 2 a flows into the pipe 2 b through the bypass pipe 6. Of the water in the pipe 2a, the water that did not flow into the bypass pipe 6 flows to the load side.

バイパス配管6の両端間に、第1差圧検知部である差圧センサ8が接続される。差圧センサ8は、バイパス配管6の一端側の水の圧力と他端側の水の圧力との差(バイパス配管6の両端間の水の圧力差)Pを検知する。   A differential pressure sensor 8 that is a first differential pressure detector is connected between both ends of the bypass pipe 6. The differential pressure sensor 8 detects a difference (pressure difference of water between both ends of the bypass pipe 6) P between the water pressure on one end side of the bypass pipe 6 and the water pressure on the other end side.

熱源機1a,1b,…1nは、上記したように、熱媒体熱交換器(後述の水熱交換器60,30)、およびその熱媒体熱交換器と負荷側との間で水を循環させるポンプ(後述のポンプ80)を備え、熱媒体熱交換器を通る水をヒートポンプ式冷凍サイクルの運転により加熱または冷却する。   As described above, the heat source units 1a, 1b,... 1n circulate water between the heat medium heat exchanger (water heat exchangers 60 and 30 described later) and the heat medium heat exchanger and the load side. A pump (a pump 80 described later) is provided, and water passing through the heat medium heat exchanger is heated or cooled by operation of a heat pump refrigeration cycle.

熱源機1aに搭載されているヒートポンプ式冷凍サイクルの構成を図2に示す。なお、熱源機1b,…1nに搭載されている各ヒートポンプ式冷凍サイクルも同様の構成である。   FIG. 2 shows the configuration of the heat pump refrigeration cycle mounted on the heat source unit 1a. Each heat pump refrigeration cycle mounted on the heat source devices 1b,.

圧縮機21の吐出冷媒が四方弁22を介して空気熱交換器23a,23bに流れ、その空気熱交換器23a,23bを経た冷媒が電子膨張弁24a,24bを介して水熱交換器(熱媒体熱交換器)30の第1冷媒流路30aに流れる。この第1冷媒流路30aを経た冷媒は、四方弁22およびアキュームレータ25を通って圧縮機21に吸込まれる。この冷媒流れ方向は冷却運転(冷水生成運転)時のもので、空気熱交換器23a,23bが凝縮器、水熱交換器30の第1冷媒流路30aが蒸発器として機能する。加熱運転(温水生成運転)時は、四方弁22の流路が切替わって冷媒の流れ方向が逆となり、水熱交換器30の第1冷媒流路30aが凝縮器、空気熱交換器23a,23bが蒸発器として機能する。   The refrigerant discharged from the compressor 21 flows to the air heat exchangers 23a and 23b via the four-way valve 22, and the refrigerant passing through the air heat exchangers 23a and 23b passes through the electronic expansion valves 24a and 24b to the water heat exchanger (heat It flows to the first refrigerant flow path 30a of the medium heat exchanger 30). The refrigerant that has passed through the first refrigerant flow path 30 a is sucked into the compressor 21 through the four-way valve 22 and the accumulator 25. This refrigerant flow direction is at the time of cooling operation (cold water generation operation), and the air heat exchangers 23a and 23b function as condensers, and the first refrigerant flow path 30a of the water heat exchanger 30 functions as an evaporator. At the time of heating operation (warm water generation operation), the flow path of the four-way valve 22 is switched to reverse the flow direction of the refrigerant, and the first refrigerant flow path 30a of the water heat exchanger 30 is the condenser, the air heat exchanger 23a, 23b functions as an evaporator.

これら圧縮機21、四方弁22、空気熱交換器23a,23b、電子膨張弁24a,24b、水熱交換器30の第1冷媒流路30a、およびアキュームレータ25により、第1ヒートポンプ式冷凍サイクルが構成される。   The compressor 21, the four-way valve 22, the air heat exchangers 23a and 23b, the electronic expansion valves 24a and 24b, the first refrigerant flow path 30a of the water heat exchanger 30, and the accumulator 25 constitute a first heat pump refrigeration cycle. Is done.

圧縮機41の吐出冷媒が四方弁42を介して空気熱交換器43a,43bに流れ、その空気熱交換器43a,43bを経た冷媒が電子膨張弁44a,44bを介して上記水熱交換器30の第2冷媒流路30bに流れる。この第2冷媒流路30bを経た冷媒は、四方弁42およびアキュームレータ45を通って圧縮機41に吸込まれる。この冷媒流れ方向は冷却運転(冷水生成運転)時のもので、空気熱交換器43a,43bが凝縮器、水熱交換器30の第2冷媒流路30bが蒸発器として機能する。加熱運転(温水生成運転)時は、四方弁42の流路が切替わって冷媒の流れ方向が逆となり、水熱交換器30の第2冷媒流路30bが凝縮器、空気熱交換器43a,43bが蒸発器として機能する。   The refrigerant discharged from the compressor 41 flows to the air heat exchangers 43a and 43b via the four-way valve 42, and the refrigerant passing through the air heat exchangers 43a and 43b passes through the electronic expansion valves 44a and 44b. To the second refrigerant flow path 30b. The refrigerant that has passed through the second refrigerant flow path 30 b is sucked into the compressor 41 through the four-way valve 42 and the accumulator 45. This refrigerant flow direction is at the time of cooling operation (cold water generating operation), and the air heat exchangers 43a and 43b function as condensers, and the second refrigerant flow path 30b of the water heat exchanger 30 functions as an evaporator. At the time of heating operation (warm water generation operation), the flow path of the four-way valve 42 is switched to reverse the flow direction of the refrigerant, and the second refrigerant flow path 30b of the water heat exchanger 30 is the condenser, the air heat exchanger 43a, 43b functions as an evaporator.

これら圧縮機41、四方弁42、空気熱交換器43a,43b、電子膨張弁44a,44b、水熱交換器30の第2冷媒流路30b、およびアキュームレータ45により、第2ヒートポンプ式冷凍サイクルが構成される。   The compressor 41, the four-way valve 42, the air heat exchangers 43a and 43b, the electronic expansion valves 44a and 44b, the second refrigerant flow path 30b of the water heat exchanger 30, and the accumulator 45 constitute a second heat pump refrigeration cycle. Is done.

圧縮機51の吐出冷媒が四方弁52を介して空気熱交換器53a,53bに流れ、その空気熱交換器53a,53bを経た冷媒が電子膨張弁54a,54bを介して水熱交換器(熱媒体熱交換器)60の第1冷媒流路60aに流れる。この第1冷媒流路60aを経た冷媒は、四方弁52およびアキュームレータ55を通って圧縮機51に吸込まれる。この冷媒流れ方向は冷却運転(冷水生成運転)時のもので、空気熱交換器53a,53bが凝縮器、水熱交換器60の第1冷媒流路60aが蒸発器として機能する。加熱運転(温水生成運転)時は、四方弁52の流路が切替わって冷媒の流れ方向が逆となり、水熱交換器60の第1冷媒流路60aが凝縮器、空気熱交換器53a,53bが蒸発器として機能する。   The refrigerant discharged from the compressor 51 flows to the air heat exchangers 53a and 53b via the four-way valve 52, and the refrigerant passing through the air heat exchangers 53a and 53b passes through the electronic expansion valves 54a and 54b to the water heat exchanger (heat It flows to the first refrigerant flow path 60a of the medium heat exchanger 60). The refrigerant that has passed through the first refrigerant flow path 60 a is sucked into the compressor 51 through the four-way valve 52 and the accumulator 55. This refrigerant flow direction is at the time of cooling operation (cold water generation operation), the air heat exchangers 53a and 53b function as condensers, and the first refrigerant flow path 60a of the water heat exchanger 60 functions as an evaporator. During the heating operation (warm water generating operation), the flow path of the four-way valve 52 is switched to reverse the flow direction of the refrigerant, and the first refrigerant flow path 60a of the water heat exchanger 60 is the condenser, the air heat exchanger 53a, 53b functions as an evaporator.

これら圧縮機51、四方弁52、空気熱交換器53a,53b、電子膨張弁54a,54b、水熱交換器60の第1冷媒流路60a、およびアキュームレータ55により、第3ヒートポンプ式冷凍サイクルが構成される。   The compressor 51, the four-way valve 52, the air heat exchangers 53a and 53b, the electronic expansion valves 54a and 54b, the first refrigerant flow path 60a of the water heat exchanger 60, and the accumulator 55 constitute a third heat pump refrigeration cycle. Is done.

圧縮機71の吐出冷媒が四方弁72を介して空気熱交換器73a,73bに流れ、その空気熱交換器73a,73bを経た冷媒が電子膨張弁74a,74bを介して上記水熱交換器60の第2冷媒流路60bに流れる。この第2冷媒流路60bを経た冷媒は、四方弁72およびアキュームレータ75を通って圧縮機71に吸込まれる。この冷媒流れ方向は冷却運転(冷水生成運転)時のもので、空気熱交換器73a,73bが凝縮器、水熱交換器60の第2冷媒流路60bが蒸発器として機能する。加熱運転(温水生成運転)時は、四方弁72の流路が切替わって冷媒の流れ方向が逆となり、水熱交換器60の第2冷媒流路60bが凝縮器、空気熱交換器73a,73bが蒸発器として機能する。   The refrigerant discharged from the compressor 71 flows into the air heat exchangers 73a and 73b via the four-way valve 72, and the refrigerant passing through the air heat exchangers 73a and 73b passes through the electronic expansion valves 74a and 74b. To the second refrigerant flow path 60b. The refrigerant that has passed through the second refrigerant flow path 60 b is sucked into the compressor 71 through the four-way valve 72 and the accumulator 75. This refrigerant flow direction is at the time of cooling operation (cold water generating operation), and the air heat exchangers 73a and 73b function as condensers, and the second refrigerant flow path 60b of the water heat exchanger 60 functions as an evaporator. At the time of heating operation (warm water generating operation), the flow path of the four-way valve 72 is switched to reverse the flow direction of the refrigerant, and the second refrigerant flow path 60b of the water heat exchanger 60 is the condenser, the air heat exchanger 73a, 73b functions as an evaporator.

これら圧縮機71、四方弁72、空気熱交換器73a,73b、電子膨張弁74a,74b、水熱交換器60の第2冷媒流路60b、およびアキュームレータ75により、第4ヒートポンプ式冷凍サイクルが構成される。   The compressor 71, the four-way valve 72, the air heat exchangers 73a and 73b, the electronic expansion valves 74a and 74b, the second refrigerant flow path 60b of the water heat exchanger 60, and the accumulator 75 constitute a fourth heat pump refrigeration cycle. Is done.

水配管2bの水は、水配管101を通って水熱交換器60の水流路60cに流れる。水流路60cから流出する水は、水配管102を通って水熱交換器30の水流路30cに流れる。水流路30cから流出する水は、水配管2aに流れる。水熱交換器60の水流路60cおよび水熱交換器30の水流路30cは、水配管102を介して直列接続された状態にある。   The water in the water pipe 2b flows through the water pipe 101 to the water flow path 60c of the water heat exchanger 60. The water flowing out from the water channel 60 c flows through the water pipe 102 to the water channel 30 c of the water heat exchanger 30. The water flowing out from the water channel 30c flows into the water pipe 2a. The water flow path 60 c of the water heat exchanger 60 and the water flow path 30 c of the water heat exchanger 30 are in a state of being connected in series via the water pipe 102.

水配管101に、ポンプ80が配設される。ポンプ80は、水配管2b内の水を水配管101に吸込み、吸込んだ水を水熱交換器60、水配管102、水熱交換器30、水配管103に通して水配管2bに送出する。ポンプ80は、インバータ81から供給される交流電圧により動作するモータを有し、そのモータの回転数に応じて能力(揚程)が変化する。インバータ81は、商用交流電源82の電圧を整流し、整流後の直流電圧をスイッチングにより所定周波数の交流電圧に変換し、変換した交流電圧をポンプ80のモータに対する駆動電力として供給する。このインバータ81の出力電圧の周波数(出力周波数)Fを変化させることにより、ポンプ80のモータの回転数が変化する。   A pump 80 is disposed in the water pipe 101. The pump 80 sucks the water in the water pipe 2b into the water pipe 101, passes the sucked water through the water heat exchanger 60, the water pipe 102, the water heat exchanger 30, and the water pipe 103 and sends it out to the water pipe 2b. The pump 80 has a motor that is operated by the AC voltage supplied from the inverter 81, and the capacity (lift) changes according to the rotation speed of the motor. The inverter 81 rectifies the voltage of the commercial AC power supply 82, converts the rectified DC voltage into an AC voltage having a predetermined frequency by switching, and supplies the converted AC voltage as drive power to the motor of the pump 80. By changing the frequency (output frequency) F of the output voltage of the inverter 81, the rotational speed of the motor of the pump 80 changes.

水配管101と水配管103との相互間(水熱交換器60,30の両端間)に、第2差圧検知部である差圧センサ90が接続される。差圧センサ90は、水熱交換器60に流入する水の圧力と水熱交換器30から流出する水の圧力との差Pwを検知する。この差圧センサ90の検知圧力差Pwに基づき、水熱交換器60,30に流れる水の量つまり熱源機1aに流れる水の量Waを検出することができる。   A differential pressure sensor 90 that is a second differential pressure detector is connected between the water pipe 101 and the water pipe 103 (between both ends of the water heat exchangers 60 and 30). The differential pressure sensor 90 detects a difference Pw between the pressure of water flowing into the water heat exchanger 60 and the pressure of water flowing out of the water heat exchanger 30. Based on the detected pressure difference Pw of the differential pressure sensor 90, the amount of water flowing to the water heat exchangers 60 and 30, that is, the amount Wa of water flowing to the heat source unit 1a can be detected.

一方、熱源機1a,1b,…1n、流量調整弁4a,4b,…4n、流量センサ5、流量調整弁7、および差圧センサ8に、コントローラ10が接続される。これら熱源機1a,1b,…1n、水配管2a,2b、流量調整弁4a,4b,…4n、流量センサ5、バイパス配管6、流量調整弁7、差圧センサ8、コントローラ10により、熱源装置が構成される。   On the other hand, the controller 10 is connected to the heat source devices 1a, 1b,... 1n, the flow rate adjustment valves 4a, 4b,... 4n, the flow rate sensor 5, the flow rate adjustment valve 7, and the differential pressure sensor 8. These heat source units 1a, 1b,... 1n, water pipes 2a, 2b, flow rate adjusting valves 4a, 4b,... 4n, flow rate sensor 5, bypass pipe 6, flow rate adjusting valve 7, differential pressure sensor 8, and controller 10 Is configured.

コントローラ10は、熱源機1a,1b,…1nの運転、流量調整弁4a,4b,…4nの開度、および流量調整弁7の開度を制御するもので、主要な機能として第1検出部11、第2検出部12、第1制御部13、第2制御部14、第3制御部15、メモリ16を含む。   The controller 10 controls the operation of the heat source devices 1a, 1b,... 1n, the opening degree of the flow rate adjusting valves 4a, 4b,... 4n, and the opening degree of the flow rate adjusting valve 7. 11, a second detector 12, a first controller 13, a second controller 14, a third controller 15, and a memory 16.

第1検出部11は、当該熱源装置が設置された後(据付け後)の試運転時、熱源機1a,1b,…1nの各ポンプ80をそれぞれ定格能力(所定の運転周波数F)で運転しながら、負荷側に流れる水の量Qとバイパス配管6の両端間における水の圧力差Pとの関係を表わす負荷側配管抵抗特性(2次側配管抵抗特性ともいう)を検出する。   The first detection unit 11 operates the pumps 80 of the heat source devices 1a, 1b,..., 1n at their rated capacities (predetermined operating frequency F) during a trial operation after the heat source device is installed (after installation). Then, a load side pipe resistance characteristic (also referred to as a secondary side pipe resistance characteristic) representing the relationship between the amount Q of water flowing on the load side and the pressure difference P of water between both ends of the bypass pipe 6 is detected.

第2検出部12は、熱源機1a,1b,…1nにおける各差圧センサ90の検知圧力差Pwと熱源機1a,1b,…1nの個々における熱交換器抵抗特性とに基づく演算により、運転中の各熱源機の個々に流れる水の量Wを検出する。熱交換器抵抗特性は、水熱交換器60,30に固有のもので、予め実測されてコントローラ10のメモリ16に記憶されている。   The second detector 12 is operated by calculation based on the detected pressure difference Pw of each differential pressure sensor 90 in the heat source devices 1a, 1b,... 1n and the heat exchanger resistance characteristics in each of the heat source devices 1a, 1b,. The amount W of water flowing individually in each heat source machine is detected. The heat exchanger resistance characteristic is unique to the water heat exchangers 60 and 30, is actually measured in advance, and is stored in the memory 16 of the controller 10.

第1制御部13は、負荷側の空気熱交換器3a,3b,…3nの要求能力(室内空気温度Taと設定温度Tsとの差)の総和に応じて、熱源機1a,1b,…1nの運転台数および流量調整弁4a,4b,…4nの開度を制御する。   The 1st control part 13 is heat source machine 1a, 1b, ... 1n according to the sum total of the required capacity | capacitance (difference between indoor air temperature Ta and set temperature Ts) of the air heat exchangers 3a, 3b, ... 3n of load side. , And the opening degree of the flow rate adjusting valves 4a, 4b,.

第2制御部14は、空気熱交換器3a,3b,…3nの要求能力の総和に見合う最適な量の水が空気熱交換器3a,3b,…3nに流れるよう、流量センサ5の検知流量Qtおよび第1検出部11で検出した負荷側配管抵抗特性に応じて、流量調整弁(バイパス弁)7の開度を制御する。   The second control unit 14 detects the flow rate of the flow sensor 5 so that an optimal amount of water that matches the total required capacity of the air heat exchangers 3a, 3b,... 3n flows to the air heat exchangers 3a, 3b,. The opening degree of the flow rate adjusting valve (bypass valve) 7 is controlled in accordance with Qt and the load side pipe resistance characteristic detected by the first detection unit 11.

第3制御部15は、流量センサ5の検知流量Qtを熱源機1a,1b,…1nのうち運転中の各熱源機に配分(例えば均等分)してそれぞれ必要流量Wtとして割当て、これら割当て流量Wtに第2検出部12の各検出流量Wが一致するように、運転中の各熱源機におけるポンプ80の能力(熱媒体の供給能力)を制御する。   The third control unit 15 allocates the detected flow rate Qt of the flow rate sensor 5 to each operating heat source unit among the heat source units 1a, 1b,. The capacity of the pump 80 (heat medium supply capacity) in each operating heat source apparatus is controlled so that the detected flow rates W of the second detection unit 12 coincide with Wt.

つぎに、コントローラ10が実行する制御を図3のフローチャートを参照しながら説明する。
当該熱源装置が設置された後の試運転時(ステップS1のYES)、コントローラ10は、次の処理により負荷側配管抵抗特性を検出する(ステップS2)。
Next, the control executed by the controller 10 will be described with reference to the flowchart of FIG.
During the trial operation after the heat source device is installed (YES in step S1), the controller 10 detects the load-side pipe resistance characteristic by the following process (step S2).

まず、コントローラ10は、バイパス配管6の流量調整弁7を全閉し、かつ流量調整弁4a,4b,…4nのうち配管抵抗が最も大きい空気熱交換器に対応する流量調整弁のみ全開して残りの流量調整弁を全閉する。この状態で、コントローラ10は、熱源機1a,1b,…1nの各ポンプ80をそれぞれ定格能力(所定の運転周波数F)で運転し、このときの流量センサ5の検知流量Qtの値(最小流量)Qnと差圧センサ8の検知圧力差Pの値Pnとの対応点(交点)を図4に示す第1特性点Snとしてメモリ16に保持する。この場合、流量調整弁7が全閉しているので、熱源機1a,1b,…1nから流出する水の総てがバイパスされることなく負荷側に流れる。   First, the controller 10 fully closes the flow rate adjustment valve 7 of the bypass pipe 6 and fully opens only the flow rate adjustment valve corresponding to the air heat exchanger having the largest pipe resistance among the flow rate adjustment valves 4a, 4b,. Fully close the remaining flow control valves. In this state, the controller 10 operates the pumps 80 of the heat source devices 1a, 1b,... 1n at their rated capacities (predetermined operating frequency F). ) A corresponding point (intersection) between Qn and the value Pn of the detected pressure difference P of the differential pressure sensor 8 is held in the memory 16 as the first characteristic point Sn shown in FIG. In this case, since the flow rate adjusting valve 7 is fully closed, all the water flowing out from the heat source units 1a, 1b,... 1n flows to the load side without being bypassed.

配管抵抗が最も大きい空気熱交換器として、熱源機1a,1b,…1nからの配管長が最も長い末端位置に存する例えば空気熱交換器3nが、予め選定される。あるいは、末端位置の空気熱交換器3nよりも熱源機1a,1b,…1nに近い側の例えば空気熱交換器3bが、水配管2a,2bにつながる枝管2ab,2bbが他の空気熱交換器側の枝管より細いこと等の要因により、配管抵抗が最も大きい空気熱交換器として予め選定されることもある。配管抵抗が最も大きい空気熱交換器の選定は、当該熱源装置の設置に際しての作業員の経験則や実測に基づいて行われる。この選定結果がコントローラ10のメモリ16に記憶される。   As the air heat exchanger having the largest pipe resistance, for example, the air heat exchanger 3n existing at the end position where the pipe length from the heat source units 1a, 1b,. Alternatively, for example, the air heat exchanger 3b on the side closer to the heat source devices 1a, 1b,... 1n than the air heat exchanger 3n at the end position, the branch pipes 2ab, 2bb connected to the water pipes 2a, 2b are exchanged with other air. Depending on factors such as being thinner than the branch pipe on the vessel side, the air heat exchanger having the largest piping resistance may be selected in advance. The air heat exchanger having the largest piping resistance is selected based on the empirical rules and actual measurements of the workers when installing the heat source device. This selection result is stored in the memory 16 of the controller 10.

続いて、コントローラ10は、バイパス配管6の流量調整弁7を全閉したまま、流量調整弁4a,4b,…4nのすべてを全開する。この状態で、コントローラ10は、熱源機1a,1b,…1nの各ポンプ80をそれぞれ定格能力で運転し、このときの流量センサ5の検知流量Qtの値(最大流量)Qmと差圧センサ8の検知圧力差Pの値Pmとの対応点(交点)を図4に示す第2特性点Smとしてメモリ16に保持する。   Subsequently, the controller 10 fully opens all of the flow rate adjusting valves 4a, 4b,... 4n while the flow rate adjusting valve 7 of the bypass pipe 6 is fully closed. In this state, the controller 10 operates the pumps 80 of the heat source devices 1a, 1b,... 1n with their rated capacities, and the value (maximum flow rate) Qm of the detected flow rate Qt of the flow rate sensor 5 and the differential pressure sensor 8 at this time. The corresponding point (intersection) with the detected pressure difference P of Pm is held in the memory 16 as the second characteristic point Sm shown in FIG.

そして、コントローラ10は、保持した第1特性点Snと第2特性点Smとを結んで“負荷側に流れる水の量Q”と“バイパス配管6の両端間の水の圧力差P”との関係を近似的に表わす2次近似曲線を、負荷側配管抵抗特性として検出する。コントローラ10は、検出した負荷側配管抵抗特性としてメモリ16に記憶する。   Then, the controller 10 connects the held first characteristic point Sn and the second characteristic point Sm to “the amount Q of water flowing to the load side” and “the water pressure difference P between both ends of the bypass pipe 6”. A quadratic approximate curve that approximately represents the relationship is detected as a load-side piping resistance characteristic. The controller 10 stores the detected load side pipe resistance characteristic in the memory 16.

一方、試運転が終了した後の通常運転時(ステップS1のNO)、コントローラ10は、負荷側の空気熱交換器3a,3b,…3nの要求能力(室内空気温度Taと設定温度Tsとの差)の総和に応じて、熱源機1a,1b,…1nの運転台数および流量調整弁4a,4b,…4nの開度を制御する(ステップS3)。   On the other hand, during the normal operation after the trial operation is completed (NO in step S1), the controller 10 determines the required capacity of the load-side air heat exchangers 3a, 3b,... 3n (the difference between the indoor air temperature Ta and the set temperature Ts). ) And the opening degree of the flow rate adjusting valves 4a, 4b,... 4n are controlled (step S3).

すなわち、コントローラ10は、空気熱交換器3a,3b,…3nの要求能力の総和が大きいほど熱源機1a,1b,…1nの運転台数を増やし、空気熱交換器3a,3b,…3nの要求能力の総和が小さくなるのに伴い熱源機1a,1b,…1nの運転台数を減らしていく。さらに、コントローラ10は、空気熱交換器3aの要求能力が大きいほど流量調整弁4aの開度を増大(流量増加)し、空気熱交換器3aの要求能力が小さくなるのに伴い流量調整弁4aの開度を縮小(流量減少)していく。空気熱交換器3b,…3nに対応する流量調整弁4b,…4nの開度についても、同様に制御する。   That is, the controller 10 increases the number of operating heat source units 1a, 1b,... 1n as the sum of the required capacities of the air heat exchangers 3a, 3b,... 3n increases, and requests the air heat exchangers 3a, 3b,. As the total capacity decreases, the number of operating heat source devices 1a, 1b,. Furthermore, the controller 10 increases the opening degree of the flow rate adjustment valve 4a (increases the flow rate) as the required capacity of the air heat exchanger 3a increases, and the flow rate adjustment valve 4a increases as the required capacity of the air heat exchanger 3a decreases. The opening degree of the is reduced (flow reduction). The opening degree of the flow rate adjusting valves 4b,... 4n corresponding to the air heat exchangers 3b,.

この運転台数制御および開度制御の実行に伴い、空気熱交換器3a,3b,…3nに実際に流れる水の量(総量)Qtが流量センサ5により検知される。   Along with the execution number control and opening degree control, the flow rate sensor 5 detects the amount (total amount) Qt of water actually flowing to the air heat exchangers 3a, 3b,.

コントローラ10は、流量センサ5の検知流量Qtに対応する“バイパス配管6の両端間の水の目標圧力差Pt”を、試運転時に検出して記憶した図4の負荷側配管抵抗特性から求める(ステップS4)。そして、コントローラ10は、差圧センサ8の検知圧力差(バイパス配管6の両端間の水の圧力差)Pが上記求めた目標圧力差Ptとなるように、流量調整弁7の開度(水のバイパス量)を制御する(ステップS5)。   The controller 10 obtains the “target pressure difference Pt of water between both ends of the bypass pipe 6” corresponding to the detected flow rate Qt of the flow sensor 5 from the load-side pipe resistance characteristics of FIG. S4). The controller 10 then opens the flow rate adjustment valve 7 so that the detected pressure difference of the differential pressure sensor 8 (pressure difference of water between both ends of the bypass pipe 6) P becomes the above-obtained target pressure difference Pt. Is controlled) (step S5).

差圧センサ8の検知圧力差Pを目標圧力差Ptに設定することにより、空気熱交換器3a,3b,…3nの要求能力の総和に見合う最適な量の水が空気熱交換器3a,3b,…3nに流れる。空気熱交換器3a,3b,…3nにとって余分となる水は、バイパス配管6を通って運転中の1台または複数台の熱源機に戻る。   By setting the detected pressure difference P of the differential pressure sensor 8 to the target pressure difference Pt, an optimal amount of water corresponding to the total required capacity of the air heat exchangers 3a, 3b,. , ... flows to 3n. The excess water for the air heat exchangers 3a, 3b,..., 3n returns to one or more heat source units in operation through the bypass pipe 6.

コントローラ10は、流量センサ5の検知流量Qtを運転中の1台または複数台の熱源機に均等分してそれぞれ必要流量Wtとして割当てる(ステップS6)。例えば、流量センサ5の検知流量Qtが1000リットル/hで、熱源機1a,1b,…1nの運転台数が5台の場合、200(=1000/5)リットル/hを熱源機1台当りの必要流量Wtとして割当てる。流量センサ5の検知流量Qtが1200リットル/hで、熱源機1a,1b,…1nの運転台数が4台の場合は、300(=1200/4)リットル/hを熱源機1台当りの必要流量Wtとして割当てる。   The controller 10 equally divides the detected flow rate Qt of the flow rate sensor 5 into one or a plurality of operating heat source units and assigns them as necessary flow rates Wt (step S6). For example, if the detected flow rate Qt of the flow sensor 5 is 1000 liters / h and the number of operating heat source devices 1a, 1b,... 1n is 5, 200 (= 1000/5) liters / h per heat source device Assigned as the required flow rate Wt. When the detected flow rate Qt of the flow sensor 5 is 1200 liters / h and the number of operating heat source devices 1a, 1b,... 1n is four, 300 (= 1200/4) liters / h is required per heat source device. Assigned as the flow rate Wt.

コントローラ10は、運転中の1台または複数台の熱源機における差圧センサ90の検知圧力差Pwと、運転中の1台または複数台の熱源機における水熱交換器(水熱交換器60,30)の熱交換器抵抗特性と、に基づく演算により、運転中の1台または複数台の熱源機の個々に流れる水の量Wを検出する(ステップS7)。   The controller 10 detects the pressure difference Pw detected by the differential pressure sensor 90 in one or more heat source units in operation, and the water heat exchanger (the water heat exchanger 60, The amount W of water flowing individually in one or a plurality of heat source units in operation is detected by calculation based on the heat exchanger resistance characteristics of 30) (step S7).

例えば2台の熱源機1a,1bが運転中である場合、コントローラ10は、熱源機1aにおける差圧センサ90の検知圧力差Pwaおよび熱源機1bにおける差圧センサ90の検知圧力差Pwbを読込むとともに、熱源機1aにおける熱交換器抵抗特性および熱源機1bにおける熱交換器抵抗特性をメモリ16から読出し、これら検知圧力差Pwa,Pwbおよび各熱交換器抵抗特性に基づく演算により、熱源機1aに流れる水の量Waおよび熱源機1bに流れる水の量Wbを検出する。   For example, when two heat source units 1a and 1b are in operation, the controller 10 reads the detected pressure difference Pwa of the differential pressure sensor 90 in the heat source unit 1a and the detected pressure difference Pwb of the differential pressure sensor 90 in the heat source unit 1b. The heat exchanger resistance characteristics in the heat source machine 1a and the heat exchanger resistance characteristics in the heat source machine 1b are read from the memory 16 and flow to the heat source machine 1a by calculation based on these detected pressure differences Pwa, Pwb and each heat exchanger resistance characteristic. The amount of water Wa and the amount of water Wb flowing to the heat source unit 1b are detected.

コントローラ10は、各検出流量Wa,Wbが熱源機1a,1bに割当てた各必要流量Wtにそれぞれ一致するように、熱源機1a,1bにおける各インバータ81の出力周波数Fを制御する(ステップS8)。   The controller 10 controls the output frequency F of each inverter 81 in the heat source devices 1a and 1b so that the detected flow rates Wa and Wb respectively match the required flow rates Wt assigned to the heat source devices 1a and 1b (step S8). .

具体的には、コントローラ10は、検出流量Waが、熱源機1aに割当てた必要流量Wtより少ない場合、熱源機1aにおけるインバータ81の出力周波数Fを上げる。これにより、熱源機1aにおけるポンプ80の能力が増えて、熱源機1aに流れる水の量Waが増加方向に変化する。コントローラ10は、検出流量Waが、熱源機1aに割当てた必要流量Wtより多い場合、熱源機1aにおけるインバータ81の出力周波数Fを下げる。これにより、熱源機1aにおけるポンプ80の能力が減って、熱源機1aに流れる水の流量Waが減少方向に変化する。コントローラ10は、検出流量Waが、熱源機1aに割当てた必要流量Wtに一致したとき、そのときの熱源機1aにおけるインバータ81の出力周波数Fを保持する。   Specifically, the controller 10 increases the output frequency F of the inverter 81 in the heat source unit 1a when the detected flow rate Wa is smaller than the necessary flow rate Wt allocated to the heat source unit 1a. Thereby, the capacity | capacitance of the pump 80 in the heat-source equipment 1a increases, and the quantity Wa of the water which flows into the heat-source equipment 1a changes to an increase direction. When the detected flow rate Wa is higher than the necessary flow rate Wt assigned to the heat source device 1a, the controller 10 decreases the output frequency F of the inverter 81 in the heat source device 1a. Thereby, the capacity | capacitance of the pump 80 in the heat-source equipment 1a reduces, and the flow volume Wa of the water which flows into the heat-source equipment 1a changes in the decreasing direction. When the detected flow rate Wa coincides with the required flow rate Wt assigned to the heat source unit 1a, the controller 10 holds the output frequency F of the inverter 81 in the heat source unit 1a at that time.

同様に、コントローラ10は、検出流量Wbが、熱源機1bに割当てた必要流量Wtより少ない場合、熱源機1bにおけるインバータ81の出力周波数Fを上げる。コントローラ10は、検出流量Wbが、熱源機1bに割当てた必要流量Wtより多い場合、熱源機1bにおけるインバータ81の出力周波数Fを下げる。コントローラ10は、検出流量Wbが、熱源機1bに割当てた必要流量Wtに一致したとき、そのときの熱源機1bにおけるインバータ81の出力周波数Fを保持する。   Similarly, the controller 10 increases the output frequency F of the inverter 81 in the heat source unit 1b when the detected flow rate Wb is less than the required flow rate Wt allocated to the heat source unit 1b. When the detected flow rate Wb is larger than the necessary flow rate Wt assigned to the heat source device 1b, the controller 10 decreases the output frequency F of the inverter 81 in the heat source device 1b. When the detected flow rate Wb matches the required flow rate Wt assigned to the heat source device 1b, the controller 10 holds the output frequency F of the inverter 81 in the heat source device 1b at that time.

なお、熱源機1a,1b,…1nに流れる水の量Wa,Wb,…Wnは、熱源機1a,1b,…1nと負荷側との間の配管抵抗によって異なる。すなわち、負荷側から最も遠い末端位置に存する熱源機1nの配管抵抗は大きく、よって熱源機1nに流れる水の量Wnは少なめとなる。負荷側に近い側の熱源機1aの配管抵抗は小さく、よって熱源機1aに流れる水の量Waは多めとなる。   The amount of water Wa, Wb,... Wn flowing through the heat source devices 1a, 1b,... 1n varies depending on the pipe resistance between the heat source devices 1a, 1b,. That is, the pipe resistance of the heat source device 1n existing at the end position farthest from the load side is large, and therefore the amount of water Wn flowing to the heat source device 1n is small. The pipe resistance of the heat source unit 1a on the side close to the load side is small, and therefore the amount of water Wa flowing to the heat source unit 1a is large.

例えば2台の熱源機1a,1nが運転している場合に、熱源機1a,1nに流れる水の量Wa,Wnとその熱源機1a,1nにおける各ポンプ80の能力(ポンプ能力)との関係を、その熱源機1a,1nにおける熱交換器抵抗Ra,Rnをパラメータとして示したのが図5である。熱源機1aに流れる水の量Waをその熱源機1aに割当てた必要流量Wtに一致させるためには、熱源機1aにおけるポンプ80の運転周波数Fを所定値Faに設定すればよい。末端位置の熱源機1nに流れる水の量Wnをその熱源機1nに割当てた必要流量Wtに一致させるためには、熱源機1nにおけるポンプ80の運転周波数Fを所定値Fn(>Fa)に設定すればよい。   For example, when two heat source machines 1a and 1n are operating, the relationship between the amount of water Wa and Wn flowing through the heat source machines 1a and 1n and the capacity (pump capacity) of each pump 80 in the heat source machines 1a and 1n. FIG. 5 shows the heat exchanger resistances Ra and Rn in the heat source devices 1a and 1n as parameters. In order to make the amount Wa of the water flowing to the heat source unit 1a coincide with the required flow rate Wt assigned to the heat source unit 1a, the operating frequency F of the pump 80 in the heat source unit 1a may be set to a predetermined value Fa. In order to make the amount of water Wn flowing to the heat source device 1n at the end position coincide with the required flow rate Wt assigned to the heat source device 1n, the operating frequency F of the pump 80 in the heat source device 1n is set to a predetermined value Fn (> Fa). do it.

したがって、上記のように、負荷側の空気熱交換器3a,3b,…3nに流れる水の量(総量)Qtを検知し、その検知流量Qtを運転中の例えば熱源機1a,1nに配分してそれぞれ必要流量Wtとして割当て、これら必要流量Wtに熱源機1a,1nに流れる水の量Wa,Wnが一致するように、熱源機1a,1nにおける各ポンプ80の運転周波数Fを制御することにより、熱源機1aの配管抵抗と熱源機1nの配管抵抗とが互いに異なる場合でも、熱源機1a,1nに流れる水の量Wa,Wnを均一にすることができる。   Therefore, as described above, the amount (total amount) Qt of water flowing through the load-side air heat exchangers 3a, 3b,... 3n is detected, and the detected flow rate Qt is distributed to the operating heat source devices 1a, 1n, for example. By assigning the necessary flow rates Wt, and controlling the operating frequency F of each pump 80 in the heat source units 1a and 1n so that the water amounts Wa and Wn flowing through the heat source units 1a and 1n coincide with these necessary flow rates Wt. Even when the pipe resistance of the heat source unit 1a and the pipe resistance of the heat source unit 1n are different from each other, the amounts of water Wa and Wn flowing through the heat source units 1a and 1n can be made uniform.

運転中の熱源機1a,1nに流れる水の量Wa,Wnが均一となるので、熱源機1a,1nにおける各ポンプ80の失速および異常停止を防ぐことができる。これにより、空気熱交換器3a,3b,…3nの要求能力の総和に見合う常に適正な量の温水または冷水を空気熱交換器3a,3b,…3nに供給できる。   Since the amounts of water Wa and Wn flowing to the heat source devices 1a and 1n during operation become uniform, it is possible to prevent stalling and abnormal stop of each pump 80 in the heat source devices 1a and 1n. This makes it possible to always supply an appropriate amount of hot water or cold water to the air heat exchangers 3a, 3b,... 3n corresponding to the sum of the required capacities of the air heat exchangers 3a, 3b,.

必要流量Wtが得られるように各ポンプ80の運転周波数Fを増減するだけなので、いわゆる熱源機側配管抵抗特性(1次側配管抵抗特性)や各ポンプ80の特性を予め検出しておく必要がない。熱源機1a,1b,…1nが複雑に配置される据付け環境であっても、配管抵抗をそろえるためのヘッダー施工や、リバースターン配管など、対処療法的な処置が不要となる。   Since only the operating frequency F of each pump 80 is increased or decreased so as to obtain the required flow rate Wt, it is necessary to detect in advance the so-called heat source side pipe resistance characteristics (primary side pipe resistance characteristics) and the characteristics of each pump 80. Absent. Even in an installation environment where the heat source devices 1a, 1b,..., 1n are arranged in a complicated manner, it is not necessary to deal with countermeasures such as header construction for adjusting piping resistance and reverse turn piping.

[変形例]
上記実施形態では、4つのヒートポンプ式冷凍サイクルおよび2つの水熱交換器30,60を備える熱源機1a,1b,…1nを例に説明したが、各熱源機におけるヒートポンプ式冷凍サイクルの個数および水熱交換器の個数については適宜に選定可能である。
[Modification]
In the embodiment described above, the heat source devices 1a, 1b,. The number of heat exchangers can be selected as appropriate.

上記実施形態では、負荷側の機器が空気熱交換器である場合を例に説明したが、負荷側の機器が例えば貯湯タンクである場合も同様に実施できる。   In the above-described embodiment, the case where the load-side device is an air heat exchanger has been described as an example, but the same can be applied to the case where the load-side device is, for example, a hot water storage tank.

上記実施形態では、負荷側に流れる水の量を検知し、その検知流量を運転中の各熱源機に均等分して割当てるようにしたが、均等分でなくても、各ポンプ80が失速なく動作を続け得る配分であればよい。   In the above-described embodiment, the amount of water flowing to the load side is detected, and the detected flow rate is equally divided and allocated to each operating heat source unit. However, even if it is not equal, each pump 80 is not stalled. Any distribution that can continue operation is acceptable.

上記実施形態では、負荷側配管抵抗特性を当該熱源装置の設置後の試運転によって検出したが、それに限らず、負荷側の空気熱交換器の増設や減設の後の試運転時に負荷側配管抵抗特性を検出してもよい。   In the above embodiment, the load-side pipe resistance characteristic is detected by a trial operation after the installation of the heat source device. May be detected.

その他、上記実施形態および変形例は、例として提示したものであり、発明の範囲を限定することは意図していない。この新規な実施形態および変形例は、その他の様々な形態で実施されることが可能であり、発明の要旨を逸脱しない範囲で、種々の省略、書き換え、変更を行うことができる。これら実施形態や変形は、発明の範囲は要旨に含まれるとともに、特許請求の範囲に記載された発明とその均等の範囲に含まれる。   In addition, the said embodiment and modification are shown as an example and are not intending limiting the range of invention. The novel embodiments and modifications can be implemented in various other forms, and various omissions, rewrites, and changes can be made without departing from the spirit of the invention. In these embodiments and modifications, the scope of the invention is included in the gist, and is included in the invention described in the claims and the equivalents thereof.

本発明の熱源装置は、空気調和機や給湯機等への利用が可能である。   The heat source device of the present invention can be used for an air conditioner, a water heater, and the like.

1a,1b,…1n……熱源機、2a,2b…水配管(熱媒体配管)、3a,3b,…3n……空気熱交換器(負荷側の機器)、4a,4b,…4n……流量調整弁(第1流量調整弁)、5…流量センサ(流量検知部)、6…バイパス配管、7…流量調整弁(第2流量調整弁)、8…差圧センサ(第1差圧検知部)、10…コントローラ、11…第1検出部、12…第2検出部、13…第1制御部、14…第2制御部、15…第3制御部、21,41,51,71…圧縮機、30,60…水熱交換器(熱媒体熱交換器)、80…ポンプ、81…インバータ、82…商用交流電源、90…差圧センサ(第2差圧検知部)   1a, 1b, ... 1n ... heat source machine, 2a, 2b ... water pipe (heat medium pipe), 3a, 3b, ... 3n ... air heat exchanger (load side equipment), 4a, 4b, ... 4n ... Flow adjusting valve (first flow adjusting valve), 5 ... Flow sensor (flow detecting unit), 6 ... Bypass piping, 7 ... Flow adjusting valve (second flow adjusting valve), 8 ... Differential pressure sensor (first differential pressure detecting) Part), 10 ... controller, 11 ... first detection part, 12 ... second detection part, 13 ... first control part, 14 ... second control part, 15 ... third control part, 21, 41, 51, 71 ... Compressor, 30, 60 ... water heat exchanger (heat medium heat exchanger), 80 ... pump, 81 ... inverter, 82 ... commercial AC power supply, 90 ... differential pressure sensor (second differential pressure detector)

Claims (6)

熱媒体が流れる熱媒体熱交換器、この熱媒体熱交換器内の前記熱媒体を加熱または冷却するヒートポンプ式冷凍サイクル、負荷側を経た熱媒体を吸込み前記熱媒体熱交換器に通して前記負荷側へ送出するポンプを含み、互いに並列に配管接続された複数の熱源機と、
前記負荷側に流れる前記熱媒体の量を調整する第1流量調整弁と、
前記負荷側に流れる前記熱媒体の量を検知する流量検知部と、
前記負荷側へと流れる前記熱媒体をバイパスするバイパス配管と、
前記バイパス配管に流れる前記熱媒体の量を調整する第2流量調整弁と、
前記バイパス配管の両端間における前記熱媒体の圧力差Pを検知する第1差圧検知部と、
前記各熱媒体熱交換器の両端間における前記熱媒体の圧力差Pwを検知する第2差圧検知部と、
コントローラと、
を備え
前記コントローラは、
前記負荷側に流れる前記熱媒体の量Qと前記バイパス配管の両端間における前記熱媒体の圧力差Pとの関係を表わす負荷側配管抵抗特性を検出する第1検出部と、
前記負荷側の要求能力に応じて前記各熱源機の運転台数および前記第1流量調整弁の開度を制御する第1制御部と、
運転中の前記各熱源機の個々に流れる前記熱媒体の量Wを、前記第2圧力差検知部の検知圧力差Pwに基づき検出する第2検出部と、
前記流量検知部の検知流量Qtおよび前記第1検出部で検出した負荷側配管抵抗特性に応じて、前記第2流量調整弁の開度を制御する第2制御部と、
前記流量検知部の検知流量Qtを運転中の前記各熱源機に配分してそれぞれ必要流量Wtとして割当て、これら必要流量Wtに前記第2検出部の各検出流量Wが一致するように、運転中の前記各熱源機における前記ポンプの能力を制御する第3制御部と、
を含む、
ことを特徴とする熱源装置。
A heat medium heat exchanger through which a heat medium flows, a heat pump refrigeration cycle for heating or cooling the heat medium in the heat medium heat exchanger, a heat medium that has passed through a load side is sucked through the heat medium heat exchanger, and the load A plurality of heat source devices including a pump for sending to the side and connected in parallel to each other ;
A first flow rate adjustment valve that adjusts the amount of the heat medium flowing to the load side;
A flow rate detector for detecting the amount of the heat medium flowing to the load side;
Bypass piping for bypassing the heat medium flowing to the load side;
A second flow rate adjustment valve that adjusts the amount of the heat medium flowing through the bypass pipe;
A first differential pressure detector that detects a pressure difference P of the heat medium between both ends of the bypass pipe;
A second differential pressure detector that detects a pressure difference Pw of the heat medium between both ends of each heat medium heat exchanger;
A controller,
Equipped with a,
The controller is
A first detector for detecting a load side pipe resistance characteristic representing a relationship between the amount Q of the heat medium flowing to the load side and the pressure difference P of the heat medium between both ends of the bypass pipe;
A first control unit for controlling the number of operating heat source units and the opening of the first flow rate adjustment valve according to the required capacity on the load side;
A second detection unit that detects the amount W of the heat medium individually flowing in each heat source unit during operation based on the detected pressure difference Pw of the second pressure difference detection unit;
A second control unit that controls the opening of the second flow rate adjustment valve according to the detected flow rate Qt of the flow rate detection unit and the load-side piping resistance characteristic detected by the first detection unit;
The detected flow rate Qt of the flow rate detection unit is allocated to each of the heat source devices in operation and assigned as the required flow rate Wt, and the detected flow rate W of the second detection unit matches the required flow rate Wt. A third control unit for controlling the capacity of the pump in each of the heat source units;
including,
A heat source device characterized by that.
前記第1流量調整弁は、前記負荷側に流れる前記熱媒体の量を開度変化により調整する、
前記バイパス配管は、前記各熱源機から前記負荷側に向かって流れる前記熱媒体をバイパスして前記各熱源機側に戻す、
前記第2流量調整弁は、前記バイパス配管に流れる前記熱媒体の量を開度変化により調整する、
ことを特徴とする請求項1記載の熱源装置。
The first flow rate adjusting valve adjusts the amount of the heat medium flowing to the load side by changing the opening;
The bypass pipe bypasses the heat medium flowing from the heat source devices toward the load side and returns to the heat source device side.
The second flow rate adjustment valve adjusts the amount of the heat medium flowing through the bypass pipe by changing the opening;
The heat source device according to claim 1 .
前記第1検出部は、前記負荷側配管抵抗特性を試運転時に検出する
ことを特徴とする請求項1記載の熱源装置。
The heat source device according to claim 1, wherein the first detection unit detects the load-side pipe resistance characteristic during a trial operation.
前記第2検出部は、運転中の前記各熱源機の個々に流れる前記熱媒体の量Wを、前記第2差圧検知部の検知圧力差Pwと前記各熱源機における熱交換器抵抗特性とに基づき、検出する
ことを特徴とする請求項1記載の熱源装置。
The second detection unit is configured to determine the amount W of the heat medium flowing individually in each heat source unit in operation, the detected pressure difference Pw of the second differential pressure detection unit, and the heat exchanger resistance characteristic in each heat source unit. The heat source device according to claim 1 , wherein the detection is based on the following.
前記流量検知部は、前記負荷側において互いに並列に配管接続された複数の機器に流れる前記熱媒体の総量を検知する、
前記第1流量調整弁は、複数の第1流量調整弁であって、前記各機器の個々に流れる前記熱媒体の量を開度変化により調整する
ことを特徴とする請求項1記載の熱源装置。
The flow rate detection unit detects the total amount of the heat medium flowing through a plurality of devices connected in parallel to each other on the load side;
2. The heat source device according to claim 1, wherein the first flow rate adjustment valve is a plurality of first flow rate adjustment valves, and adjusts the amount of the heat medium that flows individually in each of the devices by a change in opening degree. .
前記第1検出部は、
前記熱源装置の試運転時、前記第2流量調整弁を全閉し、かつ前記各機器のうち配管抵抗が最も大きい機器に対応する1つの前記第1流量調整弁のみ全開して残りの1つまたは複数の前記第1流量調整弁を全閉し、この状態で前記各熱源機における前記各ポンプを定格能力で運転し、このときの前記流量検知部の検知流量Qtの値Qnと前記第1差圧検知部の検知圧力差Pの値Pnとの対応点を第1特性点Snとして保持し、
続いて、前記第2流量調整弁を全閉したまま、前記各第1流量調整弁のすべてを全開し、この状態で前記各熱源機における前記各ポンプを定格能力で運転し、このときの前記流量検知部の検知流量Qtの値Qmと前記第1差圧検知部の検知圧力差Pの値Pmとの対応点を第2特性点Smとして保持し、
前記保持した第1特性点Snと第2特性点Smとを結んで“負荷側に流れる水の量Q”と“バイパス配管6の両端間の水の圧力差P”との関係を近似的に表わす2次近似曲線を、前記負荷側配管抵抗特性として検出する、
ことを特徴とする請求項5記載の熱源装置。
The first detection unit includes:
During the trial operation of the heat source device, the second flow rate adjustment valve is fully closed and only one of the first flow rate adjustment valves corresponding to the device having the largest piping resistance among the devices is fully opened and the remaining one or A plurality of the first flow rate adjusting valves are fully closed, and in this state, the pumps in the heat source devices are operated with a rated capacity. The corresponding point with the value Pn of the detected pressure difference P of the pressure detector is held as the first characteristic point Sn,
Subsequently, with the second flow rate adjustment valve fully closed, all the first flow rate adjustment valves are fully opened, and in this state, the pumps in the heat source units are operated with rated capacity, A corresponding point between the value Qm of the detected flow rate Qt of the flow rate detector and the value Pm of the detected pressure difference P of the first differential pressure detector is held as a second characteristic point Sm,
Connecting the held first characteristic point Sn and the second characteristic point Sm, approximately the relationship between “the amount Q of water flowing to the load side” and “the water pressure difference P between both ends of the bypass pipe 6”. A quadratic approximate curve is detected as the load side pipe resistance characteristic,
The heat source device according to claim 5 .
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