WO2018163345A1 - Dispositif d'alimentation en eau chaude d'une pompe à chaleur - Google Patents

Dispositif d'alimentation en eau chaude d'une pompe à chaleur Download PDF

Info

Publication number
WO2018163345A1
WO2018163345A1 PCT/JP2017/009418 JP2017009418W WO2018163345A1 WO 2018163345 A1 WO2018163345 A1 WO 2018163345A1 JP 2017009418 W JP2017009418 W JP 2017009418W WO 2018163345 A1 WO2018163345 A1 WO 2018163345A1
Authority
WO
WIPO (PCT)
Prior art keywords
refrigerant
temperature
hot water
inlet
condenser
Prior art date
Application number
PCT/JP2017/009418
Other languages
English (en)
Japanese (ja)
Inventor
徹 小出
Original Assignee
三菱電機株式会社
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 三菱電機株式会社 filed Critical 三菱電機株式会社
Priority to PCT/JP2017/009418 priority Critical patent/WO2018163345A1/fr
Priority to JP2019504216A priority patent/JP6704505B2/ja
Priority to EP17899425.7A priority patent/EP3594587B1/fr
Publication of WO2018163345A1 publication Critical patent/WO2018163345A1/fr

Links

Images

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24HFLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
    • F24H4/00Fluid heaters characterised by the use of heat pumps
    • F24H4/02Water heaters
    • F24H4/04Storage heaters
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24DDOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
    • F24D17/00Domestic hot-water supply systems
    • F24D17/02Domestic hot-water supply systems using heat pumps
    • 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
    • F25B30/00Heat pumps
    • F25B30/02Heat pumps of the compression type
    • 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
    • F25B40/00Subcoolers, desuperheaters or superheaters
    • 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
    • F25B2339/00Details of evaporators; Details of condensers
    • F25B2339/04Details of condensers
    • F25B2339/047Water-cooled condensers
    • 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
    • F25B2500/00Problems to be solved
    • F25B2500/12Sound
    • 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
    • F25B2600/00Control issues
    • F25B2600/25Control of valves
    • F25B2600/2513Expansion 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
    • F25B2700/00Sensing or detecting of parameters; Sensors therefor
    • F25B2700/21Temperatures
    • F25B2700/2116Temperatures of a condenser
    • F25B2700/21161Temperatures of a condenser of the fluid heated by the condenser
    • 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
    • F25B2700/00Sensing or detecting of parameters; Sensors therefor
    • F25B2700/21Temperatures
    • F25B2700/2116Temperatures of a condenser
    • F25B2700/21162Temperatures of a condenser of the refrigerant at the inlet of the condenser

Definitions

  • This invention relates to a heat pump water heater equipped with a refrigerant amount regulator.
  • the refrigerant from the condenser outlet to the expansion valve inlet is cooled, thereby increasing the refrigerant density on the high-pressure side and suppressing an abnormal increase in the high-pressure side pressure.
  • the refrigerant from the condenser outlet to the expansion valve inlet is cooled by the refrigerant from the evaporator outlet to the compressor.
  • Patent Document 1 the efficiency is improved by adjusting the refrigerant amount and pressure on the high-pressure side using a refrigerant quantity regulator.
  • a refrigerant volume regulator having a large volume is necessary, and there is a problem that the equipment becomes large and the cost increases.
  • Patent Document 2 since the refrigerant quantity regulator is not used, an increase in the size of the apparatus can be avoided, but an internal heat exchanger is used in place of the refrigerant quantity regulator as means for suppressing an increase in the high-pressure side pressure during high-temperature water entry. . In this case, there are the following problems.
  • the refrigerant flows into the evaporator having a small heat capacity and accumulates as a liquid refrigerant. After a certain period of time, liquid refrigerant accumulates in the compressor having a large heat capacity.However, when the apparatus is restarted immediately after the liquid refrigerant is accumulated in the evaporator, there is no refrigerant amount regulator, so the refrigerant is liquid in the compressor. There is a risk of backing. If the compressor liquid-compresses the liquid-backed refrigerant, it may lead to failure.
  • This invention has been made to solve the above-mentioned problems, and while suppressing the increase in size and cost of the equipment, it reduces the high pressure at the time of high-temperature incoming water and avoids liquid compression due to liquid back during transition. It aims at providing the heat pump hot-water supply apparatus which can ensure the reliability of an apparatus.
  • a heat pump hot water supply apparatus includes a refrigerant circuit formed by annularly connecting a compressor, a condenser, an expansion valve, an evaporator, and a refrigerant amount regulator, and a hot water tank for storing hot water heated by the condenser
  • a hot water circulation pump that circulates hot water between the condenser and the hot water tank, an inlet refrigerant temperature detector that detects an inlet refrigerant temperature of the condenser, and an inlet that detects an inlet water temperature of the condenser
  • the valve opening of the expansion valve is set so that the difference between the temperature of the hot water supplied from the water temperature detector and the tank controller provided in the hot water tank and the inlet refrigerant temperature is a preset temperature difference.
  • a heat source device control unit that adjusts, and the heat source device control unit adjusts the valve opening of the expansion valve in the opening direction by changing the temperature difference when the inlet water temperature becomes equal to or higher than a threshold value. It is characterized by that
  • the heat pump hot water supply apparatus adjusts the opening degree of the expansion valve in the opening direction when the fluid sent from the hot water tank to the condenser by the hot water circulation pump is at a high temperature (that is, at high temperature water entry),
  • the refrigerant density on the high-pressure side is reduced to suppress the high pressure so as not to exceed a certain pressure.
  • the liquid is stored in the refrigerant quantity regulator as an excess liquid refrigerant. Even when the apparatus is restarted immediately after the liquid refrigerant is stored in the evaporator, the refrigerant backed from the evaporator can be stored as the liquid refrigerant in the refrigerant amount regulator.
  • the heat pump hot water supply apparatus includes a hot water instruction temperature from a tank control unit provided in a hot water tank and a temperature detected by an inlet refrigerant detection unit of the condenser (hereinafter referred to as an inlet refrigerant temperature).
  • the valve opening degree of the expansion valve is controlled so that the difference becomes a preset temperature difference (hereinafter referred to as a set temperature difference).
  • the temperature difference is set in advance so that the inlet refrigerant temperature ⁇ the temperature of the hot water instruction> 0, and the opening of the expansion valve is adjusted so as to be the temperature difference.
  • the water can be boiled reliably.
  • FIG. 6 is a pressure-enthalpy diagram showing the effect of improving the coefficient of performance (Coefficent of Performance; hereinafter referred to as COP).
  • Embodiment 1 FIG.
  • an outdoor unit 100 of an air conditioner according to Embodiment 1 of the present invention will be described with reference to the drawings.
  • FIG. 1 is a circuit diagram of a heat pump water heater 100 according to an embodiment of the present invention.
  • the heat pump hot water supply apparatus 100 includes a heat source unit 200 and a tank unit 300.
  • the heat source unit 200 includes a compressor 1 that compresses and discharges a refrigerant, a condenser 2 that exchanges heat between the refrigerant and water, an electronically controlled expansion valve 3 that depressurizes a high-pressure refrigerant to a low pressure with variable opening, and air And an evaporator 4 for exchanging heat between the refrigerant and the refrigerant, and a refrigerant circuit formed by annularly connecting a refrigerant amount regulator 6 capable of temporarily storing liquid refrigerant by a refrigerant pipe 19.
  • the heat source unit 200 includes an inlet water temperature detection unit 9 that detects the inlet water temperature of the condenser 2, an outlet water temperature detection unit 10 that detects the outlet water temperature of the condenser 2, and the outside air that detects the outside air temperature.
  • a temperature detector 16, an inlet refrigerant temperature detector 17 that detects the inlet refrigerant temperature of the condenser 2, and an outlet refrigerant temperature detector 18 that detects the outlet refrigerant temperature of the evaporator 4 are provided.
  • Each of these detection units can be constituted by a temperature sensor.
  • a fan 8 is installed near the evaporator 4 for promoting heat exchange between the refrigerant in the evaporator 4 and air.
  • the fan 8 is rotated by driving the fan motor 7, and an air flow passing through the evaporator 4 is generated by the rotation.
  • Carbon dioxide (CO 2 ) can be used as the refrigerant.
  • the operation of the heat source unit 200 is controlled by the heat source unit control unit 13.
  • the tank unit 300 includes a hot water tank 14 that stores hot water heated by the condenser 2, and a hot water circulation pump 11 that is disposed between the condenser 2 and the hot water tank 14 and circulates the hot water therebetween. .
  • the condenser 2 and the hot water tank 14 are connected to each other by a hot water circulation pipe 15.
  • the operation of the tank unit 300 is controlled by the tank control unit 12.
  • the tank control unit 12 can transmit a tapping instruction temperature to the heat source unit control unit of the heat source unit 200.
  • FIG. 2 is a block diagram of the heat source machine control unit 13.
  • the heat source machine control unit 13 sets the rotation speed of the compressor rotation speed control section 21 that controls the rotation speed of the compressor 1, the fan rotation speed control section 22 that controls the rotation speed of the fan motor 7, and the rotation speed of the hot water circulation pump 11.
  • a pump speed controller 23 for controlling, a detection temperature receiver 24 for receiving a detected temperature such as an inlet refrigerant temperature of the condenser 2, an expansion valve opening adjusting unit 25 for adjusting the opening of the expansion valve 3, and a tank
  • a hot water command temperature receiving unit 26 that receives the hot water command temperature emitted from the control unit 12.
  • the expansion valve opening degree adjusting unit 25 adjusts the valve opening degree of the expansion valve 3 so that the difference between the tapping instruction temperature and the inlet refrigerant temperature becomes a set temperature difference.
  • the expansion valve opening degree adjusting unit 25 changes the set temperature difference and adjusts the valve opening degree of the expansion valve 3 in the opening direction when the inlet water temperature becomes equal to or higher than a predetermined threshold value.
  • the set temperature difference is stored in advance in the storage unit 30 in the heat source unit 200.
  • the heat source machine control unit 13 is configured by, for example, a microchip.
  • the storage unit 30 is configured by a semiconductor memory, for example.
  • FIG. 3 is a cross-sectional view of the compressor 1 and the refrigerant amount regulator 6.
  • the refrigerant in the gas-liquid two-phase state flows from the evaporator 4 into the refrigerant amount adjuster 6 through the suction pipe 31, the gas refrigerant flows into the compressor 1 through the relay pipe 32, and the liquid refrigerant is surplus.
  • the refrigerant is stored in the liquid refrigerant storage section 33 of the refrigerant amount regulator 6.
  • the compressor 1 compresses the gaseous refrigerant, discharges it from the discharge pipe 34, and sends it to the condenser 2.
  • the liquid refrigerant reservoir 33 is an internal space provided at the bottom of the cylindrical refrigerant quantity regulator 6.
  • a so-called suction muffler that provides a silencing effect can be used as the refrigerant amount adjuster 6.
  • the suction muffler serves as both a muffler and a surplus refrigerant reservoir.
  • Refrigerating machine oil flows into the refrigerant amount adjuster 6 from the suction pipe 31 together with the refrigerant.
  • the relay pipe 32 is provided with an oil return hole 35 for returning the refrigeration oil accumulated at the bottom of the liquid refrigerant reservoir 33 to the compressor 1.
  • the refrigerant and the refrigerating machine oil may be mixed or separated and temporarily stored.
  • FIG. 4 is a flowchart of the boiling operation control by the heat source machine control unit 13.
  • the boiling operation control of the heat pump water heater 100 will be described with reference to FIG.
  • the heat source device control unit 13 provided in the heat source device unit 200 starts the boiling operation when receiving a boiling operation instruction from the tank control unit 12 provided in the tank unit 300 (step S11).
  • the heat source machine control unit 13 receives the hot water instruction temperature together with the boiling operation instruction.
  • the heat source device control unit 13 receives the inlet water temperature of the condenser 2 (step S12).
  • the heat source machine control unit 13 ends the operation control without performing the boiling operation (step S13).
  • the heat source machine controller 13 controls the rotation frequency of the compressor 1 based on the inlet water temperature detected by the outside air temperature detector 16 and the inlet water temperature detector 9 ( Step S14).
  • the heat source machine control unit 13 determines whether or not the inlet water temperature detected by the inlet water temperature detection unit 9 of the condenser 2 is equal to or higher than a predetermined threshold (step S15). When the inlet water temperature is less than the predetermined threshold, the heat source machine control unit 13 reads the first temperature difference stored in the storage unit 30 and sets this as the set temperature difference (step S16). When the inlet water temperature is equal to or higher than the predetermined threshold, the heat source machine control unit 13 reads the second temperature difference stored in the storage unit 30 and sets this as the set temperature difference (step S17). The second temperature difference is smaller than the first temperature difference.
  • the heat source machine control unit 13 performs the following processing after setting the temperature difference.
  • the heat source device controller 13 receives the inlet refrigerant temperature detected by the inlet refrigerant detector 17 of the condenser 2 (step S18).
  • the heat source machine control unit 13 calculates the difference between the tapping temperature and the inlet refrigerant temperature (step S19).
  • the difference is referred to as a calculated temperature difference.
  • the heat source machine control unit 13 adjusts the opening degree of the expansion valve 3 so that the calculated temperature difference becomes the set temperature difference (step S20).
  • the valve opening is adjusted in the opening direction as a result of adjusting the valve opening in accordance with a second temperature difference smaller than the first temperature difference.
  • the first temperature difference should be set to be the optimum COP under environmental conditions, for example, certain outside air temperature conditions, incoming water temperature conditions (winter standard heating conditions, intermediate standard heating conditions, etc. defined by JIS). Can do.
  • the second temperature difference is set to a value smaller than the first temperature difference so that the high-pressure side pressure at the time of high-temperature water entry does not exceed the designed upper limit value.
  • These temperature differences are constant values under certain conditions such as the outside air temperature and the incoming water temperature, and can be constant values within a range of 15 to 30 ° C., for example.
  • the opening degree of the expansion valve 3 is the target value of the outside air temperature, the inlet water temperature detected by the inlet water temperature detector 9 of the condenser 2, and the inlet refrigerant temperature detected by the inlet refrigerant detector 17 of the condenser 2. And it is controllable only with the hot water instruction temperature from the tank controller 12. However, depending on the environmental conditions, there is a relationship of the hot water instruction temperature> the target value of the inlet refrigerant temperature, and the hot water may not boil.
  • the relationship between the hot water instruction temperature> the target value of the inlet refrigerant temperature Can be.
  • a temperature difference that satisfies the inlet refrigerant temperature ⁇ the hot water instruction temperature> 0 is stored in advance in the storage unit 30 as the first and second temperature differences.
  • the first temperature difference is set as the set temperature difference
  • the second temperature difference smaller than the first temperature difference is set as the set temperature difference. Then, the opening degree of the expansion valve 3 is adjusted so that the calculated temperature difference becomes the set temperature difference.
  • FIG. 5 is a schematic diagram showing the temperature transition of hot water in the hot water tank 14.
  • the temperature of water supplied to the heat source unit 200 is low (for example, 5 ° C.) from the start of boiling to the time of boiling operation, the inlet water temperature of the condenser 2 increases (for example, 5 to 5) before the completion of boiling. 60 ° C.).
  • the temperature of the water in the hot water tank 14 before the boiling operation is about 5 ° C.
  • the temperature of the hot water in the hot water tank 14 during the boiling operation is The upper side is 90 ° C and the lower side is 5 ° C.
  • the temperature of the hot water in the hot water tank 14 before completion of boiling is 90 ° C. on the upper side and medium temperature water, for example, 60 ° C. on the lower side.
  • the inlet water temperature rises When the inlet water temperature rises, the density of the refrigerant present in the condenser 2 decreases. At this time, the pressure rises abnormally with the first temperature difference set in advance so that the optimum COP is obtained under certain environmental conditions. Therefore, the environmental conditions where the pressure on the high pressure side may exceed the design pressure (for example, under the low outside air conditions, the maximum boiling temperature and the maximum heating capacity are required, the high inlet refrigerant temperature of the condenser 2 and the compressor Under the condition of reaching a maximum rotational speed of 1, a second temperature difference smaller than the first temperature difference is set as a set temperature difference. Since the second temperature difference is smaller than the first temperature difference, the set temperature difference becomes small when the inlet water temperature becomes equal to or higher than the predetermined temperature.
  • the design pressure for example, under the low outside air conditions, the maximum boiling temperature and the maximum heating capacity are required, the high inlet refrigerant temperature of the condenser 2 and the compressor
  • the opening degree of the expansion valve 3 is adjusted so that the difference between the tapping temperature from the tank controller 12 and the detected temperature obtained by the inlet refrigerant detector 17 of the condenser 2 becomes the set temperature difference after the change. adjust.
  • the refrigerant density on the high pressure side can be reduced, and the high pressure can be suppressed so that the pressure on the high pressure side does not exceed the design pressure.
  • FIG. 6 shows an inlet water temperature 41 of the condenser 2, an inlet refrigerant temperature 42 of the condenser 2, a tapping instruction temperature 43 of the tank controller 12, a stored refrigerant quantity 44 of the refrigerant quantity regulator 6, and a valve opening of the expansion valve. It is a time chart which shows.
  • the liquid refrigerant is not stored in the refrigerant quantity regulator 6.
  • the inlet refrigerant temperature 42 and the tapping hot water instruction temperature 43 are also constant.
  • the excess liquid refrigerant is stored in the refrigerant amount regulator 6 in order to operate at a design pressure or lower. And suppress high pressure. That is, the valve opening adjustment in steps S17 to S20 is started from time T1 when the inlet water temperature exceeds the predetermined threshold value 41.
  • the valve opening degree 45 is adjusted so that the difference between the inlet refrigerant temperature 42 and the hot water instruction temperature 43 is the same as a certain set temperature difference (second temperature difference).
  • the valve opening 45 increases from time T1. This reduces the actual temperature difference. For example, the temperature difference between the inlet refrigerant temperature 42 and the tapping temperature 43 until the time point T1 when the inlet water temperature 41 reaches the predetermined threshold value 41a is 30 ° C., and after the time point T1 when the inlet water temperature 41 reaches the predetermined threshold value 41a. The temperature difference is 25 ° C.
  • the boiling operation is terminated at time T2 when the inlet water temperature 41 reaches the predetermined temperature 41b (step S13).
  • the refrigerant filling amount of the entire refrigeration circuit can be about 1000 g, for example.
  • the target value 44a of the liquid refrigerant storage amount 44 in the refrigerant amount adjuster 6 can be set to about 30 g, for example.
  • the heat source machine control unit 13 may start the boiling operation soon after the boiling operation is stopped. After the operation is stopped, the expansion valve 3 is fully opened, and the pressures on the high pressure side and the low pressure side are balanced. At this time, the refrigerant is drawn to the outside air temperature, flows into the evaporator 4 having a small heat capacity (easy to radiate heat), and is stored as a liquid refrigerant. After a certain period of time, the liquid refrigerant is stored in the compressor 1 having a large heat capacity. However, when restarted immediately after the liquid refrigerant has been stored in the evaporator 4, the liquid refrigerant stored in the evaporator 4 flows into the compressor 1 at once. .
  • the liquid refrigerant when there is no refrigerant amount adjuster 6, the liquid refrigerant may be liquid-backed to the compressor 1 and the compressor 1 may be liquid-compressed.
  • the liquid refrigerant from the evaporator 4 at the time of starting the apparatus is temporarily stored in the refrigerant amount regulator 6, so that the refrigerant liquid by the compressor 1 is stored. Compression can be prevented and the reliability of the compressor 1 can be ensured.
  • the expansion valve 3 when the fluid sent from the bottom of the hot water tank 14 to the condenser 2 by the hot water circulation pump 11 is high temperature (that is, at high temperature water entry), the expansion valve 3.
  • the refrigerant density on the high pressure side is decreased by adjusting the valve opening degree of the valve in the opening direction, and the high pressure is suppressed so as not to exceed a certain pressure.
  • the refrigerant density on the low pressure side increases, the excess liquid refrigerant is stored in the refrigerant amount regulator 6.
  • the refrigerant amount regulator 6 Since the surplus liquid refrigerant is stored in the refrigerant amount regulator 6, it is not necessary to provide an internal heat exchanger for exchanging heat between the high-pressure side refrigerant and the low-pressure side refrigerant, and the cost can be reduced.
  • the refrigerant flows into the evaporator 4 having a small heat capacity and is stored as a liquid refrigerant. Thereafter, when a certain time has elapsed, the liquid refrigerant is stored in the compressor 1 having a large heat capacity.
  • the apparatus is restarted immediately after the liquid refrigerant is stored in the evaporator 4, the compression is performed when the refrigerant amount regulator 6 is not provided. There is a risk of liquid back into the machine 1 and liquid compression.
  • the heat pump hot water supply apparatus 100 of the present embodiment is provided with the refrigerant amount adjuster 6, and by storing the liquid refrigerant in this, the liquid compression of the compressor 1 can be avoided and the reliability of the compressor 1 can be ensured. It becomes possible.
  • a suction muffler can be used as the refrigerant amount regulator 6. By combining the suction muffler with the silencer and the refrigerant amount adjuster 6, it is not necessary to provide another refrigerant amount adjuster, and the effects of cost reduction and volume increase suppression of the outdoor unit are obtained.
  • Embodiment 2 FIG.
  • an outdoor unit 100 for an air conditioner according to Embodiment 2 of the present invention will be described with reference to the drawings.
  • FIG. 7 is a circuit diagram of the heat pump hot water supply apparatus 100 including the internal heat exchanger 5.
  • the refrigerant quantity regulator 6 having a certain size or more may not be installed due to structural restrictions.
  • the refrigerant from the outlet of the condenser 2 to the inlet of the expansion valve 3 and the outlet of the evaporator 4 to the compressor 1 It is possible to provide an internal heat exchanger 5 that exchanges heat with the refrigerant up to the inlet.
  • the expansion valve 3 is provided on the refrigerant flow path between the evaporator 4 and the internal heat exchanger 5.
  • FIG. 8 is a pressure-enthalpy diagram showing the effect of suppressing high pressure.
  • FIG. 9 is a pressure-enthalpy diagram showing the effect when COP is improved.
  • the internal heat exchanger 5 has two roles. One role is to increase the refrigerant density of the evaporator 4 when the inlet water temperature of the condenser 2 rises due to heat exchange by the internal heat exchanger 5, as shown in FIG. Accumulate. Accordingly, the refrigerant density on the high pressure side can be reduced to suppress high pressure.
  • Reference numerals 51 and 52 indicate enthalpy ranges on the low-pressure side and the high-pressure side that vary due to heat exchange by the internal heat exchanger 5. Another role is to apply superheat at the outlet of the evaporator 4 as shown in FIG.
  • Reference numeral 54 in FIG. 9 indicates an enthalpy range that increases when superheat is applied to the outlet of the evaporator 4 by the internal heat exchanger 5.
  • Reference numeral 55 is a refrigerant state transition when the internal heat exchanger 5 is present, and reference numeral 56 is a refrigerant state transition when the internal heat exchanger 5 is not present.
  • the internal heat exchanger 5 and the refrigerant amount regulator 6 are used in combination as in the present embodiment, the above-described effects of high pressure suppression and COP improvement are obtained. If the amount of liquid stored in the refrigerant amount controller 6 can be increased to an extent that does not overflow, the internal heat exchanger 5 can be made compact, leading to cost reduction. Moreover, if it controls so that only the refrigerant

Abstract

La présente invention garantit la fiabilité d'un compresseur en réduisant la pression maximale au moyen d'un stockage de fluide frigorigène dans un régulateur de quantité de fluide frigorigène servant de suppresseur de haute pression lorsque de l'eau à haute température est injectée, et en évitant la compression de liquide au moyen d'un stockage de reflux de liquide pendant le trop-plein dans le régulateur de quantité de fluide frigorigène. Le degré selon lequel une soupape d'expansion est ouverte est ajusté de sorte que la différence entre la température de décharge d'eau chaude indiquée et la température de fluide frigorigène d'entrée pendant l'ébullition soit un différentiel de température prédéfini et, lorsqu'un fluide envoyé depuis le réservoir d'eau chaude vers un condenseur est à une température élevée, la pression élevée est supprimée par la réduction de la densité de fluide frigorigène côté haute pression au moyen de la modification du différentiel de température et l'ajustement, dans la direction d'ouverture, du degré selon lequel la soupape d'expansion est ouverte. Parallèlement, étant donné que la densité de fluide frigorigène côté basse pression augmente, le fluide frigorigène liquide en excès est stocké dans le régulateur de quantité de fluide frigorigène. De plus, après que le fonctionnement est arrêté et redémarré immédiatement après que le fluide frigorigène liquide est stocké dans l'évaporateur, il y a un risque qu'une compression de liquide se produise par le retour de liquide dans le compresseur s'il n'y a pas de régulateur de quantité de fluide frigorigène. Ainsi, une compression de liquide est évitée en stockant un fluide frigorigène dans le régulateur de quantité de fluide frigorigène et la fiabilité du compresseur est assurée.
PCT/JP2017/009418 2017-03-09 2017-03-09 Dispositif d'alimentation en eau chaude d'une pompe à chaleur WO2018163345A1 (fr)

Priority Applications (3)

Application Number Priority Date Filing Date Title
PCT/JP2017/009418 WO2018163345A1 (fr) 2017-03-09 2017-03-09 Dispositif d'alimentation en eau chaude d'une pompe à chaleur
JP2019504216A JP6704505B2 (ja) 2017-03-09 2017-03-09 ヒートポンプ給湯装置
EP17899425.7A EP3594587B1 (fr) 2017-03-09 2017-03-09 Dispositif d'alimentation en eau chaude d'une pompe à chaleur

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/JP2017/009418 WO2018163345A1 (fr) 2017-03-09 2017-03-09 Dispositif d'alimentation en eau chaude d'une pompe à chaleur

Publications (1)

Publication Number Publication Date
WO2018163345A1 true WO2018163345A1 (fr) 2018-09-13

Family

ID=63448305

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/JP2017/009418 WO2018163345A1 (fr) 2017-03-09 2017-03-09 Dispositif d'alimentation en eau chaude d'une pompe à chaleur

Country Status (3)

Country Link
EP (1) EP3594587B1 (fr)
JP (1) JP6704505B2 (fr)
WO (1) WO2018163345A1 (fr)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115095986A (zh) * 2022-06-30 2022-09-23 九阳股份有限公司 一种即热出水机的控制方法

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0718602A (ja) 1993-06-29 1995-01-20 Sekisui Chem Co Ltd 埋込栓
JPH0718602B2 (ja) * 1989-01-09 1995-03-06 シンヴェント・アクシェセルスカープ 超臨界蒸気圧縮サイクルの運転方法およびその装置
JP2005164103A (ja) 2003-12-01 2005-06-23 Matsushita Electric Ind Co Ltd 冷凍サイクル装置およびその制御方法
JP2007212103A (ja) * 2006-02-13 2007-08-23 Matsushita Electric Ind Co Ltd ヒートポンプ式給湯機
JP2012013267A (ja) * 2010-06-30 2012-01-19 Corona Corp ヒートポンプ式給湯装置
JP2012233626A (ja) * 2011-04-28 2012-11-29 Noritz Corp ヒートポンプ給湯機
JP2014016041A (ja) * 2012-07-05 2014-01-30 Denso Corp 給湯装置

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3659197B2 (ja) * 2000-06-21 2005-06-15 松下電器産業株式会社 ヒートポンプ給湯機
JP4948374B2 (ja) * 2007-11-30 2012-06-06 三菱電機株式会社 冷凍サイクル装置
JP5173469B2 (ja) * 2008-02-15 2013-04-03 三菱電機株式会社 ヒートポンプ給湯装置

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0718602B2 (ja) * 1989-01-09 1995-03-06 シンヴェント・アクシェセルスカープ 超臨界蒸気圧縮サイクルの運転方法およびその装置
JPH0718602A (ja) 1993-06-29 1995-01-20 Sekisui Chem Co Ltd 埋込栓
JP2005164103A (ja) 2003-12-01 2005-06-23 Matsushita Electric Ind Co Ltd 冷凍サイクル装置およびその制御方法
JP2007212103A (ja) * 2006-02-13 2007-08-23 Matsushita Electric Ind Co Ltd ヒートポンプ式給湯機
JP2012013267A (ja) * 2010-06-30 2012-01-19 Corona Corp ヒートポンプ式給湯装置
JP2012233626A (ja) * 2011-04-28 2012-11-29 Noritz Corp ヒートポンプ給湯機
JP2014016041A (ja) * 2012-07-05 2014-01-30 Denso Corp 給湯装置

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115095986A (zh) * 2022-06-30 2022-09-23 九阳股份有限公司 一种即热出水机的控制方法
CN115095986B (zh) * 2022-06-30 2023-03-14 九阳股份有限公司 一种即热出水机的控制方法

Also Published As

Publication number Publication date
JP6704505B2 (ja) 2020-06-03
EP3594587B1 (fr) 2021-04-21
JPWO2018163345A1 (ja) 2019-07-18
EP3594587A4 (fr) 2020-02-26
EP3594587A1 (fr) 2020-01-15

Similar Documents

Publication Publication Date Title
JP4337880B2 (ja) ヒートポンプ式給湯器
JP5042058B2 (ja) ヒートポンプ式給湯用室外機及びヒートポンプ式給湯装置
EP2631562B1 (fr) Dispositif de chauffage de l'air du type pompe à chaleur
JP4931848B2 (ja) ヒートポンプ式給湯用室外機
EP3301380B1 (fr) Dispositif à cycle de réfrigération et procédé de commande de dispositif à cycle de réfrigération
JP3783711B2 (ja) ヒートポンプ給湯装置
WO2018185841A1 (fr) Dispositif à cycle frigorifique
EP2752628A1 (fr) Cycle supercritique et installation de distribution d'eau chaude à pompe à chaleur mettant en uvre ledit cycle
JP3915770B2 (ja) ヒートポンプ給湯機
WO2014010531A1 (fr) Dispositif chauffant de type pompe à chaleur
EP3267130B1 (fr) Dispositif à cycle frigorifique
CN112739966A (zh) 热泵装置
JP3919736B2 (ja) ヒートポンプ給湯装置の起動制御装置および起動制御方法
EP2594867A2 (fr) Appareil de cycle de réfrigération et appareil de production d'eau chaude
JP2009264715A (ja) ヒートポンプ温水システム
WO2018163345A1 (fr) Dispositif d'alimentation en eau chaude d'une pompe à chaleur
JP2009264718A (ja) ヒートポンプ温水システム
JP2008008499A (ja) 冷凍サイクル装置及びヒートポンプ式給湯機
JP6076583B2 (ja) ヒートポンプ
JP2016048126A (ja) 給水加温システム
KR102460317B1 (ko) 냉동 사이클 장치 및 그 제어 방법
JP2012026637A (ja) ヒートポンプ給湯装置
JP3516519B2 (ja) エンジンヒートポンプの室外機
JP5753977B2 (ja) 冷凍サイクル装置
JP2016133238A (ja) ヒートポンプサイクル装置

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 17899425

Country of ref document: EP

Kind code of ref document: A1

ENP Entry into the national phase

Ref document number: 2019504216

Country of ref document: JP

Kind code of ref document: A

NENP Non-entry into the national phase

Ref country code: DE

ENP Entry into the national phase

Ref document number: 2017899425

Country of ref document: EP

Effective date: 20191009