EP4249812A1 - System and method for providing domestic hot water and/or space heating within a building - Google Patents

System and method for providing domestic hot water and/or space heating within a building Download PDF

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Publication number
EP4249812A1
EP4249812A1 EP22164465.1A EP22164465A EP4249812A1 EP 4249812 A1 EP4249812 A1 EP 4249812A1 EP 22164465 A EP22164465 A EP 22164465A EP 4249812 A1 EP4249812 A1 EP 4249812A1
Authority
EP
European Patent Office
Prior art keywords
heat exchanger
storage device
phase change
compressor
change material
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
EP22164465.1A
Other languages
German (de)
French (fr)
Inventor
James Freeman
Christopher OLKIS
Georgeanna KAWALEY
Duan WU
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Electric Corp
Mitsubishi Electric R&D Centre Europe BV Netherlands
Original Assignee
Mitsubishi Electric Corp
Mitsubishi Electric R&D Centre Europe BV Netherlands
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 Mitsubishi Electric Corp, Mitsubishi Electric R&D Centre Europe BV Netherlands filed Critical Mitsubishi Electric Corp
Priority to EP22164465.1A priority Critical patent/EP4249812A1/en
Priority to JP2023043041A priority patent/JP2023143814A/en
Priority to CN202310261381.8A priority patent/CN116804466A/en
Publication of EP4249812A1 publication Critical patent/EP4249812A1/en
Pending legal-status Critical Current

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Classifications

    • 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
    • F24D3/00Hot-water central heating systems
    • F24D3/18Hot-water central heating systems using heat pumps
    • 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
    • F24D19/00Details
    • F24D19/10Arrangement or mounting of control or safety devices
    • F24D19/1006Arrangement or mounting of control or safety devices for water heating systems
    • F24D19/1066Arrangement or mounting of control or safety devices for water heating systems for the combination of central heating and domestic hot water
    • 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
    • F24H15/00Control of fluid heaters
    • F24H15/30Control of fluid heaters characterised by control outputs; characterised by the components to be controlled
    • F24H15/375Control of heat pumps
    • F24H15/385Control of expansion valves of heat pumps
    • 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
    • F24H15/00Control of fluid heaters
    • F24H15/30Control of fluid heaters characterised by control outputs; characterised by the components to be controlled
    • F24H15/375Control of heat pumps
    • F24H15/39Control of valves for distributing refrigerant to different evaporators or condensers in 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
    • F25B13/00Compression machines, plants or systems, with reversible cycle
    • 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
    • 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
    • F25B41/30Expansion means; Dispositions thereof
    • 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
    • F25B41/40Fluid line arrangements
    • F25B41/42Arrangements for diverging or converging flows, e.g. branch lines or junctions
    • 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
    • F25B47/00Arrangements for preventing or removing deposits or corrosion, not provided for in another subclass
    • F25B47/02Defrosting cycles
    • F25B47/022Defrosting cycles hot gas defrosting
    • 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
    • F25B49/00Arrangement or mounting of control or safety devices
    • F25B49/02Arrangement or mounting of control or safety devices for compression type machines, plants or systems
    • 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
    • F24D2220/00Components of central heating installations excluding heat sources
    • F24D2220/10Heat storage materials, e.g. phase change materials or static water enclosed in a space
    • 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
    • F25B2313/027Compression machines, plants or systems with reversible cycle not otherwise provided for characterised by the reversing means
    • F25B2313/02732Compression machines, plants or systems with reversible cycle not otherwise provided for characterised by the reversing means using two three-way 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
    • F25B2313/00Compression machines, plants or systems with reversible cycle not otherwise provided for
    • F25B2313/027Compression machines, plants or systems with reversible cycle not otherwise provided for characterised by the reversing means
    • F25B2313/02741Compression machines, plants or systems with reversible cycle not otherwise provided for characterised by the reversing means using one four-way valve
    • 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
    • F25B2313/029Control issues
    • F25B2313/0292Control issues related to 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
    • F25B2400/00General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
    • F25B2400/16Receivers
    • 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
    • F25B2400/00General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
    • F25B2400/24Storage receiver heat
    • 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
    • F25B2600/2507Flow-diverting 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
    • F25B2600/00Control issues
    • F25B2600/25Control of valves
    • F25B2600/2513Expansion valves

Definitions

  • a system and for providing domestic hot water and/or space heating within a building is provided.
  • the system which can be used in the method, is characterized in that it comprises a first storage device containing a first phase change material, a first detector for determining the state of charge of the first storage device and a first phase change material heat exchanger suitable for exchanging heat between a refrigerant from a refrigeration circuit and the first phase change material.
  • the system further comprises a second storage device containing a second phase change material, a second detector for determining the state of charge of the second storage device and a second phase change material heat exchanger suitable for exchanging heat between the second phase change material and water of a heat medium circuit.
  • a controller is configured to control an operation of the system based on at least a state of charge of the first storage device and a state of charge of the second storage device.
  • a major limitation for heat pump heating products for single-dwelling homes is a low heat delivery rate (typically 5-15 kW) compared small combination boilers (typically 20-30 kW). This means that heat pumps usually must be installed with a storage cylinder for domestic hot water which can be charged over a longer period of time when convenient.
  • a typical shower uses around 7 litres per minute of water at supply temperatures around 42 °C: assuming mains water at 10 °C this leads to heat load of ⁇ 16 kW.
  • a single shower uses around 50 Litres of water, and 6.5 MJ (1.8 kWh) of heat.
  • Phase change materials have been proposed as a more compact alternative to conventional water-based thermal storage for use in domestic heating applications, namely space heating and domestic hot water heating. These two applications have different temperature requirements.
  • point-of-use temperature tends to be in the range 40-55 °C
  • space heating the temperature range can be higher or lower depending on the type of heating system and the basis for sizing that heating system.
  • Older central heating systems designed with fossil-fuel boilers and conventional panel radiators may use water flow temperatures in the range 60-80 °C, while modern heating systems designed for electric heat pumps use large heat emitter areas for water flow temperatures in the range 35-45 °C.
  • heat pumps are designed to operate all year round, under a range of outdoor conditions.
  • a typical mode for heat pump control in space heating operation is to use a weather compensation curve, for which water flow temperature is increased as outdoor ambient temperature decreases.
  • air-source heat pumps are required to operate over a wide range of "temperature lift” conditions; where the "temperature lift” is the difference between the source temperature and output temperature of a heat pump in heating mode.
  • air source heat pumps are subject to part-load inefficiencies when designed for higher peak-load conditions in winter, when heat source temperature (outdoor air temperature) is very low and the required heat delivery temperature (water flow temperature) is very high. In other words, the coefficient of performance (COP) of such heat pump systems is low.
  • One proposed configuration for improving heat pump efficiency and the COP is to separate the heat pumping process into two stages, each with a smaller temperature lift, and to use the ground as a thermal store to store the thermal energy pumped from the air (e.g. at ⁇ 0 °C) at an intermediate temperature (e.g. at 10 °C) until it is required, at which point it can be pumped across the second stage to its required delivery temperature (e.g. 40 C for space heating).
  • a problem with this approach is that the cost and inconvenience of installing shallow-coil or deep borehole type ground heat exchangers tends to be high, which makes said methods and systems very expensive.
  • thermal storage that can be used for both DHW and space heating.
  • thermal stores that can be used to off-set the time of heat pump operation from the time of space heating demand.
  • a problem with this approach is that the space requirement inside the building for both a DHW storage tank and thermal store for space heating (which is usually a water storage cylinder) can be excessively large for many single-family dwellings.
  • JP 2008 180473 A discloses a system and method in which, when a heat source is insufficient or not matched to consumer-side needs, a backup of heat supply is provided by operating a heat pump by midnight power with the atmosphere as a heat source.
  • JP 2012 007796 A discloses a system and method in which a heat storage system includes heat storage tanks that individually store a latent heat accumulating material, a circulating passage that passes through the heat storage tanks in ascending order of the melting point of the latent heat accumulating material in the heat storage tanks, a supply path that supplies a heating medium to an end of the circulating passage and a distribution passage that takes out the heating medium from the other end of the circulating passage.
  • the systems and methods of the prior art suffer at least the following disadvantages. Firstly, if a single-stage heat pump system is used, it must operate across a large temperature difference between an outdoor air heat source and a required delivery temperature for domestic hot water, which does not allow an efficient operation, i.e. does not allow an operation at a high coefficient of performance (COP). Secondly, if two-stage heat pump systems or two compressors are used, the complexity of said systems and thus the costs for providing said systems is high. Thirdly, if a thermal storage device like a water storage cylinder is used, a large space is occupied by said thermal storage device leaving less space for other purposes in a room, which is particularly relevant in an indoor room.
  • COP coefficient of performance
  • a system for providing domestic hot water and/or space heating within a building comprising
  • the system has the advantage that it can provide domestic hot water and space heating in a building in a more efficient manner.
  • the higher efficiency and coefficient of performance (COP) is achieved by having the first storage device and second storage device in the described arrangement, wherein both the first storage device and the second storage device contain a phase change material.
  • the two storage devices allow to separate the heat pumping process into two stages with an intermediate storage temperature condition, i.e. allows a first heat-pumping stage between a low temperature and an intermediate temperature and allows a second heat-pumping stage between an intermediate temperature and a high temperature.
  • a higher efficiency and coefficient of performance is also achieved by the control of the system based on at least a state of charge of the first storage device and a state of charge of the second storage device, because the system can reliable select a proper operation mode based on the respective state of charge. For example, if the state of charge of the first storage device is high (e.g. at or above a set lower limit), the controller can select an operation mode in which heat for heating a space or for charging the second storage device is provided directly by the first storage device instead of being provided directly by outside air (which can be inefficient especially at low outside air temperatures). Furthermore, if the state of charge of the second storage device is low (e.g. below a set lower limit), the controller can select an operation mode in which heat is conveyed only to the second storage device to charge the second storage device and to render it capable to efficiently provide large volumes of domestic hot water.
  • the system also has the advantage that it can provide domestic hot water and space heating in a building with a minimum of space needed by the system. Since the system uses two storage devices containing a phase change material and phase change materials have a relatively high heat storage capability, the overall volume of the two storage devices can be smaller than if e.g. a water storage tank without a phase change material (e.g. a typical domestic hot water storage cylinder) for storing heat energy is employed in the system. It is preferred that the system does not comprise a water storage tank lacking a phase change material.
  • the state of charge of a storage device is the amount of heat energy stored in the storage device.
  • the state of charge of a storage device represent the amount of heat energy that can be provided by the storage device.
  • the state of charge of a storage device also indicates the amount of heat energy that is required to charge the storage device.
  • the detector for determining the state of charge (i.e. the first and second detector for determining the state of charge, respectively) of the storage device can comprise at least one temperature sensor (optionally more than one temperature sensor) suitable for detecting a temperature inside the storage device.
  • Said at least one temperature sensor (optionally all temperature sensors) can be suitable to detect a temperature of an outer surface of the storage device (e.g. by being placed on or at an outer surface of the storage device).
  • the at least one temperature sensor (optionally all temperature sensors), or at least one further temperature sensor in addition to the at least one temperature sensor can be suitable to detect a temperature of a content inside the storage device (e.g.
  • the state of charge of the storage device can e.g. be determined as described in EP patent application EP21213459.7 .
  • the detector for determining the state of charge comprises at least one temperature sensor and at least one electrical resistance sensor (e.g. as separate sensors or as a combined temperature-and-electrical-resistance sensor), wherein at least the electrical resistance sensor is suitable to detect an electrical resistance of a content (specifically: a fluid comprising or consisting of a PCM) inside the storage device (e.g. by being placed in an inner volume of the storage device and by contacting the inner content).
  • the state of charge of the storage device can e.g. be determined as described in the EP patent application EP21166193.9 .
  • the conveying means for circulating water through the heat medium heat exchanger can be a pump.
  • the system according to the invention does not comprise a two stage-compressor and/or does not comprise a further (i.e. at least a second) compressor.
  • a further compressor i.e. at least a second compressor.
  • the first storage device is located outdoors, preferably within a heat pump outdoor unit comprising the compressor, the first expansion valve, the second expansion valve, the first three-way valve, the second three-way valve, the four-way switching valve, the outdoor heat exchanger and the heat medium heat exchanger.
  • a heat pump outdoor unit comprising the compressor, the first expansion valve, the second expansion valve, the first three-way valve, the second three-way valve, the four-way switching valve, the outdoor heat exchanger and the heat medium heat exchanger.
  • the second storage device (containing the phase change material with the higher phase change temperature) is preferably located indoors (i.e. inside a building). Since a significant fraction of the total required heat storage can be provided by the low-temperature phase change material in the first storage device, the size of the second storage device can be smaller than the size of the first storage device, which provides more free space in a room in which the second storage device is located. This is especially relevant if the room is inside of a building.
  • the first phase change material can have a phase transition temperature which is half way between an outdoor ambient air temperature in winter in a location where the system is located, and the phase change temperature of the second phase change material.
  • the first phase change material can have a phase transition temperature in the range of 10 °C to 35 °C, preferably 20 °C to 30 °C.
  • the second phase change material can have a phase transition temperature in the range of 35 °C to 60 °C, preferably 40 °C to 50 °C.
  • the controller can be configured to control an operation of the system which is further based on a requirement of a defrosting operation (of the outdoor heat exchanger).
  • the outdoor heat exchanger can comprise a temperature sensor which is suitable to communicate with the controller or the system can comprise a temperature sensor for detecting a refrigerant temperature which is suitable to communicate with the controller.
  • the outdoor heat exchanger can comprise an outdoor heat exchanger temperature sensor and the controller can be configured to select a defrosting operation mode based on a temperature information communicated by said temperature sensor.
  • This configuration has the advantage that in a case in which a defrosting operation is needed, the controller can switch to a defrosting operation mode. In said defrosting operation mode, the outdoor heat exchanger can be defrosted which allows a more efficient operation of the outdoor heat exchanger after the defrosting operation.
  • the controller can be configured to control an operation of the system which is further based on a demand for space heating within a building.
  • the system can comprise an indoor air temperature sensor in an indoor space to be heated and the controller can be configured to select a space heating operation mode based on a temperature information communicated by said temperature sensor.
  • This configuration of the controller has the advantage that, if there is a demand of space heating, the system can switch to a space heating only operation mode. For example, in said heating mode, no heating energy is used for charging the first storage device and/or for charging the second storage device (with heat energy) and/or for providing domestic hot water. This is beneficial because heating a space to be heated becomes more efficient.
  • the system can switch to operation modes in which no heat is used to provide space heating. For example, in said operation modes, heat is used for charging the first storage device and/or second storage device (with heat energy) and/or for providing domestic hot water. This is beneficial because heating domestic hot water and/or charging the first and/or second storage device becomes more efficient.
  • the controller can be configured to control an operation of the system which is further based on an outdoor ambient air temperature.
  • the system can comprise an outdoor air temperature sensor in an outdoor space and the controller can be configured to select an operation mode of the system based on a temperature information communicated by said temperature sensor.
  • This configuration of the controller has the advantage that an outdoor ambient air temperature can be used to decide whether the second storage device is charged with heat from outdoor air (if outdoor ambient air temperature is at or above a set lower limit) or charged with heat from the first storage device (if outdoor ambient air temperature is below a set lower limit). This allows a more efficient charging of the second storage device because heat is pumped over a shallower temperature gradient into the second storage device.
  • an outdoor air temperature can be used to decide whether space heating is performed with heat from outdoor air (if outdoor ambient air temperature is at or above a set lower limit) or performed with heat from the first storage device (if outdoor ambient air temperature is below a set lower limit). This allows a more efficient space heating because heat is pumped over a shallower temperature gradient to the space to be heated.
  • the first three-way valve is preferably located in a fluid line connecting the compressor with the first phase change material heat exchanger and the heat medium heat exchanger.
  • the second three-way valve is preferably located in a fluid line connecting the compressor with the first phase change material heat exchanger and the outdoor heat exchanger.
  • the refrigeration circuit of the system can comprise a receiver (accumulator).
  • the receiver can be located in a fluid line between the first expansion valve and the second expansion valve in the refrigeration circuit.
  • the first expansion valve of the refrigeration circuit of the system can be located in a fluid line between the outdoor heat exchanger and a receiver of the refrigerant circuit.
  • the second expansion valve of the refrigeration circuit can be located in a fluid line between a receiver of the refrigerant circuit and a fluid line branching to the first phase change material heat exchanger and to the heat medium heat exchanger.
  • the controller of the system can be configured to
  • This configuration of the controller has the advantage that heat stored in the second storage device can be used to defrost the outdoor heat exchanger in cold-ambient conditions, without compromising comfort conditions in the internal living space or supply temperature of the domestic hot water output.
  • the controller of the system can be configured to,
  • This configuration of the controller has the advantage that the second storage device can be charged with heat energy from outside air.
  • the controller can be configured to
  • This configuration of the controller has the advantage that the second storage device can be charged with heat energy from the first storage device.
  • the controller can be configured to,
  • This configuration of the controller has the advantage that heat energy from outside air can be (directly) transported to at least one space in a building. Hence, heat can be directly pumped from the outdoor air to a heat emitter circuit of a building.
  • the controller can be configured to,
  • This configuration of the controller has the advantage that heat energy from the first storage device can be (directly) transported to at least one space in a building. Hence, heat can be directly pumped from the first storage device (containing phase change material at lower temperature) to a heat emitter circuit of a building.
  • the controller can be configured to,
  • This configuration of the controller has the advantage that the first storage device can be charged with heat energy from outside air.
  • the heat medium circuit of the system can comprise a further heat exchanger suitable for exchanging heat between water (flowing in the heat medium circuit) and mains water (flowing in domestic hot water circuit).
  • the further heat exchanger has the advantage that heat can be provided to mains water beside the second phase change material heat exchanger of the second storage device.
  • the further heat exchanger can be located upstream of the second phase change material heat exchanger of the second storage device. This location allows the further heat exchanger to preheat mains water before it enters into the second phase change material heat exchanger of the second storage device.
  • the further heat exchanger may be located downstream of the second phase change material heat exchanger of the second storage device.
  • the heat medium circuit preferably comprises a further three-way valve which is suitable to switch a flow of water to the second phase change material heat exchanger of the second storage device via the further heat exchanger or directly to the second phase change material heat exchanger of the second storage device by bypassing the further heat exchanger.
  • the first storage device of the system can comprise a renewable energy heat exchanger suitable for exchanging heat between the first phase change material and a fluid which receives heat energy from a renewable energy source.
  • the renewable energy source can be a solar thermal array.
  • water can flow through the solar thermal array, absorb heat energy from the sun and transfer the absorbed heat energy to the first storage device by the renewable energy heat exchanger.
  • the renewable energy source is a solar photovoltaic-thermal array.
  • water can flow through the solar photovoltaic thermal array, absorb heat energy from the sun and transfer the absorbed heat energy to the first storage device by the renewable energy heat exchanger and additionally, electric energy generated by the solar photovoltaic thermal array can be used to provide electricity to the system, i.e. can be used to operate the complete system or at least parts thereof (e.g. parts relating to the heat pump).
  • the system can further comprise an inverter to convert a DC voltage to an AC voltage.
  • a method for providing domestic hot water (DHW) and/or space heating (SH) within a building comprising
  • the method has at least the advantages that it can provide domestic hot water and space heating in a building in a more efficient manner and with a minimum of space needed.
  • the first storage device of the system used in the method can be placed outdoors, preferably within a heat pump outdoor unit comprising the compressor, the first expansion valve, the second expansion valve, the first three-way valve, the second three-way valve, the four-way switching valve, the outdoor heat exchanger and the heat medium heat exchanger.
  • the advantage is that carrying out the method requires less indoor space and results in a more efficient operation.
  • the method can be characterized in that, if a defrosting of the outdoor heat exchanger is required, heat from the first phase change material heat exchanger is allowed to be conveyed to the outdoor heat exchanger, wherein preferably
  • This method has the advantage that heat stored in the second storage device can be used to defrost the outdoor heat exchanger in cold-ambient conditions, without compromising comfort conditions in the internal living space or supply temperature of the domestic hot water output.
  • the method can be characterized in that,
  • This method has the advantage that the second storage device can be charged with heat energy from outside air.
  • the method can be characterized in that,
  • This method has the advantage that heat energy from outside air can be (directly) transported to at least one space in a building. Hence, heat can be directly pumped from the outdoor air to a heat emitter circuit of a building.
  • the method can be characterized in that,
  • This method has the advantage that heat energy from the first storage device can be (directly) transported to at least one space in a building. Hence, heat can be directly pumped from the first storage device (containing phase change material at lower temperature) to a heat emitter circuit of a building.
  • This method has the advantage that the first storage device can be charged with heat energy from outside air.
  • a system according to the invention can be provided and used, i.e. the method can be conducted with a system according to the invention.
  • the controller of the system can be configured to control steps of the method, e.g. control the settings of parts of the system.
  • Figure 1 illustrates a system according to the invention.
  • the system comprises a first storage device 5 which contains a first phase change material (not shown) and comprises a first phase change material heat exchanger 6 and a first detector (not shown) for determining the state of charge of the first storage device.
  • the system also comprises a second storage device 7 which contains a second phase change material having a higher phase change temperature than the first phase change material (not shown) and comprises a second phase change material heat exchanger 8.
  • the heat medium circuit 22 comprises a three-way valve to switch a direction of water flow to the second phase change material heat exchanger 8 or to the heat emitter(s) 18.
  • the heat medium circuit 22 further comprises a pump 10 for conveying water through the heat medium circuit 22.
  • the system also comprises a heat medium heat exchanger 11 which is comprised by both the refrigeration circuit and the heat medium circuit 11 and which is suitable for transferring heat between the refrigerant and water of the heat medium circuit 22.
  • Figure 2 illustrates schematically components of a system according to the invention which relate to the refrigeration circuit 30.
  • the refrigeration circuit 30 comprises a compressor 1, a first expansion valve 2, a second expansion valve 2', a four-way switching valve 3, an outdoor heat exchanger 4 and a first storage device 5 containing a first phase change material (not shown) and comprising a first phase change material heat exchanger 6 and a first detector (not shown) for determining the state of charge of the first storage device.
  • the refrigeration circuit further comprises a first three-way valve 13, a second three-way valve 14 and a receiver located between the first expansion valve 2 and the second expansion valve 2'.
  • system comprises a heat medium heat exchanger 11 which is comprised by both the refrigeration circuit 30 and the heat medium circuit and which is suitable for transferring heat between the refrigerant of the refrigeration circuit 30 and water of the heat medium circuit, i.e. a cold water flow 28 from the heat medium circuit can be heated in the heat medium heat exchanger 11 and exit the heat medium heat exchanger 11 as a hot water flow 29 to the heat medium circuit.
  • a heat medium heat exchanger 11 which is comprised by both the refrigeration circuit 30 and the heat medium circuit and which is suitable for transferring heat between the refrigerant of the refrigeration circuit 30 and water of the heat medium circuit, i.e. a cold water flow 28 from the heat medium circuit can be heated in the heat medium heat exchanger 11 and exit the heat medium heat exchanger 11 as a hot water flow 29 to the heat medium circuit.
  • FIG 3 illustrates the components shown in Figure 2 and indicates a flow direction of refrigerant in a first operation mode (HP mode 1).
  • HP mode 1 outside air 16 is used as a heat source. Heat is transferred to the first storage device 5 (to allow efficient charging of the first storage device 5).
  • FIG 4 illustrates the components shown in Figure 2 and indicates a flow direction of refrigerant in a second operation mode (HP mode 2) and in a fifth operation mode (HP mode 5).
  • HP mode 2 the first storage device 5 is used as a heat source.
  • HP mode 2 heat is transferred to the second storage device 7 to charge the second storage device (to allow an efficient provision of domestic hot water) whereas in HP mode 5, heat is transferred to one or more heat emitter(s) 18 in a building (to allow an efficient provision of heat in a one or more room(s) in a building).
  • Switching between HP mode 2 and 5 can be performed by switching three-way valve 9 of the heat medium circuit.
  • FIG 5 illustrates the components shown in Figure 2 and indicates a flow direction of refrigerant in a third operation mode (HP mode 3) and in a fourth operation mode (HP mode 4).
  • HP mode 3 heat is transferred to the second storage device 7 to charge the second storage device (to allow an efficient provision of domestic hot water) whereas in HP mode 4, heat is transferred to one or more heat emitter(s) 18 in a building (to allow an efficient provision of heat in one or more room(s) in a building).
  • Switching between HP mode 3 and 4 can be performed by switching three-way valve 9 of the heat medium circuit.
  • Figure 6 illustrates the components shown in Figure 2 and indicates a flow direction of refrigerant in a sixth heating operation mode (HP mode 6).
  • HP mode 6 the first storage device 5 is used as a heat source. Heat is transferred to the outdoor heat exchanger 4 (to allow an efficient defrosting of the outdoor heat exchanger).
  • Figure 7 illustrates schematically a decision tree for performing the method according to the invention and which can be implemented in the controller of the system according to the invention
  • FIG 8 illustrates a further system according to the invention having the features shown in Figure 1 , wherein the heat medium circuit 22 of the system further comprises a heat exchanger 23 (preheating heat exchanger) which is suitable for directly exchanging heat between water in the heat medium circuit 22 and a water flow of mains water 19.
  • the heat exchanger 23 is suitable to preheat mains water before it enters the second storage device 7, where the preheated mains water is further heated by the second phase change material heat exchanger 8 and exits the second storage device as a water flow of domestic hot water 20.
  • the second storage device 7 contains two heat exchanger coils in contact with the phase change material (PCM).
  • PCM phase change material
  • One heat exchanger coil is for transferring heat from the heat medium circuit to the PCM and one heat exchanger coil is for transferring stored heat from the PCM to the domestic hot water fluid stream.
  • the heat medium circuit 22 can comprise a further three-way valve 24 which is suitable to switch a flow of water of the heat medium circuit 22 either to the second phase change material heat exchanger 8 or to the heat exchanger 23, which allows a selection whether a preheating of mains water shall be performed or not.
  • FIG 9 illustrates a further system according to the invention having the features shown in Figure 1 , wherein the system further comprises a solar photovoltaic-thermal array 26 (PVT array).
  • the PVT array 26 can provide heat energy to the first storage container 5 via a renewable energy heat exchanger 25 located in the first storage container 5 and can provide electrical energy to parts of the system relating to the heat pump 17.
  • the system can comprise an inverter 27 which is suitable for converting DC voltage to AC voltage.
  • Example 1 Outdoor air as heat source for charging the first storage container ( Figure 3)
  • HP mode 1 Charging the first storage device from air source
  • the heat pump is used to pump heat from the outdoor air 16 to the first storage device 5 via the first phase change material heat exchanger 6 embedded in the first storage device 5.
  • the refrigerant circuit flow configuration is set according to Fig 3 .
  • the four-way switching valve 3 is set to its normal "heating" position.
  • the three-way valve 13 is set to direct superheated refrigerant vapour from the compressor 1 discharge to the first storage device store heat exchanger 6, where it condenses, releasing heat to melt the first phase change material.
  • the three-way valve 14 is set to direct 2-phase refrigerant leaving the linear expansion valve 2 to the outdoor heat exchanger 4, where it evaporates, absorbing heat from the air stream.
  • the orifice of the first linear expansion valve 2 is adjusted to control the superheat temperature at the evaporator outlet, while the second linear expansion valve 2' is set fully open.
  • Example 2 First storage device as heat source for providing domestic hot water and/or space heating within a building ( Figure 4)
  • the heat pump is used to pump heat from the first storage device 5 to the second storage device 7, which allows an efficient provision of domestic hot water by the second storage device.
  • This mode is used when outdoor air temperature is sufficiently low that using the heat stored in the first storage device 5 as the heat source offers a significant improvement to the COP of the heat pump compared to using outdoor air 16.
  • the refrigerant circuit flow configuration is set according to Fig 4 .
  • the four-way switching valve 3 is set to its normal "heating" position.
  • the three-way valve 13 is set to direct superheated refrigerant vapour from the compressor 1 discharge to the heat medium heat exchanger 11, where it condenses, releasing heat to primary circulating fluid.
  • the three-way valve 14 is set to direct 2-phase refrigerant leaving linear expansion valve 2 to the first storage device 5, where it evaporates, absorbing heat from the first phase change material which changes phase from liquid to solid.
  • the orifice of the first linear expansion valve 2 is adjusted to control the superheat temperature at the evaporator outlet, while the second linear expansion valve 2' is set fully open.
  • the three-way valve 9 (shown in Fig. 1 ) is set to direct water of the heat medium circuit 22 to the second storage device 7 and not to the heat emitter(s) 18.
  • the heat pump is used to pump heat from the first storage device 5 to at least one heat emitter 18, which allows an efficient heating of at least one inside room in which the heat emitter is located.
  • This mode is used when outdoor air temperature is sufficiently low and heat demand is sufficiently high that using the heat stored in the first storage device 5 as the heat source offers a significant improvement to the heat pump COP compared to using outdoor air 16.
  • the refrigerant circuit flow configuration is set according to Fig 4 .
  • the four-way switching valve 3 is set to its normal "heating" position.
  • the three-way valve 13 is set to direct superheated refrigerant vapour from the compressor 1 discharge to the heat medium heat exchanger 11, where it condenses, releasing heat to primary circulating fluid.
  • the three-way valve 14 is set to direct 2-phase refrigerant leaving linear expansion valve 2 to the first storage device 5, where it evaporates, absorbing heat from the first phase change material which changes phase from liquid to solid.
  • the orifice of the first linear expansion valve 2 is adjusted to control the superheat temperature at the evaporator outlet, while the second linear expansion valve 2' is set fully open.
  • the three-way valve 9 (shown in Fig. 1 ) is set to direct water of the heat medium circuit 22 to the heat emitter(s) 18 and not to the second storage device 7.
  • Example 3 Outdoor air as heat source for providing domestic hot water and/or space heating within a building ( Figure 5)
  • HP mode 3 charging second storage device from outdoor air source
  • the heat pump is used to pump heat from the outdoor air 16 to the second storage device 7.
  • This mode is used when there is an immediate demand for domestic hot water (DHW), but there is not sufficient thermal energy stored in the first storage device 5, or when outdoor air 16 temperature is sufficiently high that using the heat stored in the first storage device 5 as the heat source offers no significant improvement to the heat pump COP compared to using the outdoor air 16.
  • the refrigerant circuit flow configuration is set according to Fig 5 .
  • the four-way switching valve 3 is set to its normal "heating" position.
  • the three-way valve 13 is set to direct superheated refrigerant vapour from the compressor 1 discharge to the heat medium heat exchanger 11, where it condenses, releasing heat to primary circulating fluid.
  • the three-way valve 14 is set to direct 2-phase refrigerant leaving linear expansion valve 2 to the outdoor heat exchanger 4, where it evaporates, absorbing heat from the air stream.
  • the orifice of the first linear expansion valve 2 is adjusted to control the superheat temperature at the evaporator outlet, while the second linear expansion valve 2' is set fully open.
  • the three-way valve 9 (shown in Fig. 1 ) is set to direct water of the heat medium circuit 22 to the second storage device 7 and not to the heat emitter(s) 18.
  • the heat pump is used to pump heat from the outdoor air 16 to the heat emitter(s) 18.
  • This mode is used when outdoor air 16 temperature is sufficiently high and heat demand is sufficiently low that using the heat stored in the first storage device 5 as heat source offers no significant improvement to the heat pump COP compared to using the outdoor air 16.
  • the refrigerant circuit flow configuration is set according to Fig 5 .
  • the four-way switching valve 3 is set to its normal "heating" position.
  • the three-way valve 13 is set to direct superheated refrigerant vapour from the compressor 1 discharge to the heat medium heat exchanger 11, where it condenses, releasing heat to primary circulating fluid.
  • the three-way valve 14 is set to direct 2-phase refrigerant leaving linear expansion valve 2 to the outdoor heat exchanger 4, where it evaporates, absorbing heat from the air stream.
  • the orifice of the first linear expansion valve 2 is adjusted to control the superheat temperature at the evaporator outlet, while the second linear expansion valve 2' is set fully open.
  • the three-way valve 9 (shown in Fig. 1 ) is set to direct water of the heat medium circuit to the heat emitter(s) 18 and not to the second storage device 7.
  • Example 4 First storage device as heat source for defrosting outdoor heat exchanger ( Figure 6)
  • HP mode 6 Defrost outdoor heat exchanger using stored heat from first storage device
  • the heat pump is used to pump heat from the first storage device 5 to (periodically) defrost the outdoor heat exchanger 4 during cold outdoor temperatures.
  • the refrigerant circuit flow configuration is set according to Figure 6 .
  • the four-way switching valve 3 is set to its reverse "defrost" position.
  • Low-pressure 2-phase refrigerant enters the first phase change material heat exchanger 6 where it is evaporated, absorbing latent heat released by the first phase change material.
  • the three-way valve 13 is set to direct the low-pressure vapour leaving the first phase change material heat exchanger 6 to the compressor 1 intake.
  • the three-way valve 14 directs the high pressure superheated vapour leaving the compressor 1 discharge to the outdoor heat exchanger 4 where it condenses, releasing heat to defrost the ice build-up on the external surface of outdoor heat exchanger 4.
  • the orifice of the second linear expansion valve 2' is adjusted to control the superheat temperature at the outlet of the first phase change material heat exchanger 6, while the first linear expansion valve 2 is set fully open.
  • Example 5 Further heat exchanger for preheating mains water ( Figure 8)
  • FIG 8 shows a possible implementation by which mains water can be preheated using the heat pump (either with air as heat source or the first storage device 5 as heat source) and a further heat exchanger (e.g. a plate type heat exchanger) and a further 3-way valve 24 in the heat medium circuit.
  • the heat pump either with air as heat source or the first storage device 5 as heat source
  • a further heat exchanger e.g. a plate type heat exchanger
  • a further 3-way valve 24 in the heat medium circuit e.g. a plate type heat exchanger
  • Such an arrangement is particularly beneficial during longer DHW draw-off events (e.g. bath or shower), allowing the fraction of the DHW heating load extracted from the second storage device 7 to be reduced by as much as 20-50% (depending on the nominal capacity of the heat pump).
  • a larger volume of DHW can be supplied before it is necessary to charge the second storage device 7 or, when the aim is to provide a comparable volume of DHW, the second storage device 7 can be sized smaller which allows for less indoor room to be occupied by the second storage device 7.
  • Example 6 Solar thermal array or a solar PVT array as heat source for charging the first storage device ( Figure 9)
  • a secondary renewable heat source such as a solar thermal collector array can be used to provide thermal input to the system.
  • a secondary renewable heat source such as a solar thermal collector array
  • the solar thermal collector array can achieve a higher-efficiency operation at the low melting temperature of the first storage device 5 compared to a conventional arrangement where solar thermal collectors are required to heat DHW to higher storage temperatures of approx. 60 °C.
  • lower-cost solar collector designs e.g. unglazed flat-plat collectors
  • a hybrid photovoltaic-thermal collector array in which a photovoltaic cell and solar-thermal collector are incorporated in the same module are used instead of the solar thermal array.
  • PVT-array a hybrid photovoltaic-thermal collector array
  • These are often designed for lower operating temperatures in order to maintain both a high PV electrical efficiency and a reasonable solar thermal efficiency.
  • a proposed arrangement of the system in combination with a PVT array is shown in Fig 9 .
  • the use of PVT collectors is highly advantageous because electricity generated by the PVT array can be used to run the whole system or at least components thereof (e.g. parts relating to the heat pump).
  • the system can be operated completely or at least partially from renewable energy (i.e. solar energy).

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Abstract

A system and for providing domestic hot water and/or space heating within a building is provided. The system, which can be used in the method, is characterized in that it comprises a first storage device containing a first phase change material, a first detector for determining the state of charge of the first storage device and a first phase change material heat exchanger suitable for exchanging heat between a refrigerant from a refrigeration circuit and the first phase change material. The system further comprises a second storage device containing a second phase change material, a second detector for determining the state of charge of the second storage device and a second phase change material heat exchanger suitable for exchanging heat between the second phase change material and water of a heat medium circuit. A controller is configured to control an operation of the system based on at least a state of charge of the first storage device and a state of charge of the second storage device.

Description

  • A system and for providing domestic hot water and/or space heating within a building is provided. The system, which can be used in the method, is characterized in that it comprises a first storage device containing a first phase change material, a first detector for determining the state of charge of the first storage device and a first phase change material heat exchanger suitable for exchanging heat between a refrigerant from a refrigeration circuit and the first phase change material. The system further comprises a second storage device containing a second phase change material, a second detector for determining the state of charge of the second storage device and a second phase change material heat exchanger suitable for exchanging heat between the second phase change material and water of a heat medium circuit. A controller is configured to control an operation of the system based on at least a state of charge of the first storage device and a state of charge of the second storage device.
  • A major limitation for heat pump heating products for single-dwelling homes is a low heat delivery rate (typically 5-15 kW) compared small combination boilers (typically 20-30 kW). This means that heat pumps usually must be installed with a storage cylinder for domestic hot water which can be charged over a longer period of time when convenient. A typical shower uses around 7 litres per minute of water at supply temperatures around 42 °C: assuming mains water at 10 °C this leads to heat load of ~16 kW. A single shower uses around 50 Litres of water, and 6.5 MJ (1.8 kWh) of heat.
  • Phase change materials have been proposed as a more compact alternative to conventional water-based thermal storage for use in domestic heating applications, namely space heating and domestic hot water heating. These two applications have different temperature requirements. For DHW, point-of-use temperature tends to be in the range 40-55 °C, while for space heating the temperature range can be higher or lower depending on the type of heating system and the basis for sizing that heating system. Older central heating systems designed with fossil-fuel boilers and conventional panel radiators may use water flow temperatures in the range 60-80 °C, while modern heating systems designed for electric heat pumps use large heat emitter areas for water flow temperatures in the range 35-45 °C.
  • Meanwhile, heat pumps are designed to operate all year round, under a range of outdoor conditions. A typical mode for heat pump control in space heating operation is to use a weather compensation curve, for which water flow temperature is increased as outdoor ambient temperature decreases. This means that air-source heat pumps are required to operate over a wide range of "temperature lift" conditions; where the "temperature lift" is the difference between the source temperature and output temperature of a heat pump in heating mode. Thus, air source heat pumps are subject to part-load inefficiencies when designed for higher peak-load conditions in winter, when heat source temperature (outdoor air temperature) is very low and the required heat delivery temperature (water flow temperature) is very high. In other words, the coefficient of performance (COP) of such heat pump systems is low.
  • One proposed configuration for improving heat pump efficiency and the COP is to separate the heat pumping process into two stages, each with a smaller temperature lift, and to use the ground as a thermal store to store the thermal energy pumped from the air (e.g. at < 0 °C) at an intermediate temperature (e.g. at 10 °C) until it is required, at which point it can be pumped across the second stage to its required delivery temperature (e.g. 40 C for space heating). A problem with this approach is that the cost and inconvenience of installing shallow-coil or deep borehole type ground heat exchangers tends to be high, which makes said methods and systems very expensive.
  • For demand-side flexibility services, attention has focused on increasing thermal storage that can be used for both DHW and space heating. To this extent, many heat pump systems are designed with thermal stores that can be used to off-set the time of heat pump operation from the time of space heating demand. A problem with this approach is that the space requirement inside the building for both a DHW storage tank and thermal store for space heating (which is usually a water storage cylinder) can be excessively large for many single-family dwellings.
  • JP 2008 180473 A discloses a system and method in which, when a heat source is insufficient or not matched to consumer-side needs, a backup of heat supply is provided by operating a heat pump by midnight power with the atmosphere as a heat source.
  • JP 2012 007796 A discloses a system and method in which a heat storage system includes heat storage tanks that individually store a latent heat accumulating material, a circulating passage that passes through the heat storage tanks in ascending order of the melting point of the latent heat accumulating material in the heat storage tanks, a supply path that supplies a heating medium to an end of the circulating passage and a distribution passage that takes out the heating medium from the other end of the circulating passage.
  • Taken together, the systems and methods of the prior art suffer at least the following disadvantages. Firstly, if a single-stage heat pump system is used, it must operate across a large temperature difference between an outdoor air heat source and a required delivery temperature for domestic hot water, which does not allow an efficient operation, i.e. does not allow an operation at a high coefficient of performance (COP). Secondly, if two-stage heat pump systems or two compressors are used, the complexity of said systems and thus the costs for providing said systems is high. Thirdly, if a thermal storage device like a water storage cylinder is used, a large space is occupied by said thermal storage device leaving less space for other purposes in a room, which is particularly relevant in an indoor room.
  • Starting therefrom, it was the object of the present application to provide a system and a method for providing domestic hot water and space heating in a building, which does not have the disadvantages of prior art systems and methods. Specifically, it should be possible with the system and method to provide domestic hot water and/or space heating in a building in a more efficient manner and at a minimum of space needed by the system and for implementing the method. Preferably, it should also be possible to provide the system method for providing domestic hot water and space heating in a building, and carry out the respective method, at low costs.
  • The object is solved by the device having the features of claim land the method having the features of claim 9. The dependent claims illustrate advantageous embodiments of the invention.
  • According to the invention, a system for providing domestic hot water and/or space heating within a building is presented, comprising
    1. a) a refrigeration circuit comprising
      • a refrigerant as heat medium,
      • a compressor,
      • a first expansion valve and a second expansion valve,
      • a first three-way valve and a second three-way valve,
      • a four-way switching valve, and
      • an outdoor heat exchanger suitable for exchanging heat between the refrigerant and air,
      • a first storage device containing a first phase change material, wherein the first storage device comprises a first detector for determining the state of charge of the first storage device and comprises a first phase change material heat exchanger suitable for exchanging heat between the refrigerant and the first phase change material;
    2. b) a heat medium circuit comprising
      • water as heat medium,
      • a second storage device being thermally connected to a domestic hot water circuit and containing a second phase change material, wherein the phase change temperature of the second phase change material is higher than the phase change temperature of the first phase change material, wherein the second storage device comprises a second detector for determining the state of charge of the second storage device and comprises a second phase change material heat exchanger suitable for exchanging heat between water of the heat medium circuit and the second phase change material;
      • a third three-way valve suitable for switching a flow of water to either at least one heat emitter for space heating within a building or to the second phase change material heat exchanger;
      • at least one conveying means for circulating water through the heat medium heat exchanger;
    3. c) a heat medium heat exchanger comprised by both the refrigeration circuit and the heat medium circuit, and being suitable for transferring heat between the refrigerant and water; and
    4. d) a controller configured to control an operation of the system based on at least a state of charge of the first storage device determined by information obtained from the first detector and a state of charge of the second storage device determined by information obtained from the second detector.
  • The system has the advantage that it can provide domestic hot water and space heating in a building in a more efficient manner. The higher efficiency and coefficient of performance (COP) is achieved by having the first storage device and second storage device in the described arrangement, wherein both the first storage device and the second storage device contain a phase change material. The two storage devices allow to separate the heat pumping process into two stages with an intermediate storage temperature condition, i.e. allows a first heat-pumping stage between a low temperature and an intermediate temperature and allows a second heat-pumping stage between an intermediate temperature and a high temperature. A higher efficiency and coefficient of performance is also achieved by the control of the system based on at least a state of charge of the first storage device and a state of charge of the second storage device, because the system can reliable select a proper operation mode based on the respective state of charge. For example, if the state of charge of the first storage device is high (e.g. at or above a set lower limit), the controller can select an operation mode in which heat for heating a space or for charging the second storage device is provided directly by the first storage device instead of being provided directly by outside air (which can be inefficient especially at low outside air temperatures). Furthermore, if the state of charge of the second storage device is low (e.g. below a set lower limit), the controller can select an operation mode in which heat is conveyed only to the second storage device to charge the second storage device and to render it capable to efficiently provide large volumes of domestic hot water.
  • The system also has the advantage that it can provide domestic hot water and space heating in a building with a minimum of space needed by the system. Since the system uses two storage devices containing a phase change material and phase change materials have a relatively high heat storage capability, the overall volume of the two storage devices can be smaller than if e.g. a water storage tank without a phase change material (e.g. a typical domestic hot water storage cylinder) for storing heat energy is employed in the system. It is preferred that the system does not comprise a water storage tank lacking a phase change material.
  • According to the invention, the state of charge of a storage device (i.e. of the first and second storage device, respectively) is the amount of heat energy stored in the storage device. In other words, the state of charge of a storage device represent the amount of heat energy that can be provided by the storage device. The state of charge of a storage device also indicates the amount of heat energy that is required to charge the storage device.
  • The detector for determining the state of charge (i.e. the first and second detector for determining the state of charge, respectively) of the storage device (i.e. of the first and second storage device, respectively) can comprise at least one temperature sensor (optionally more than one temperature sensor) suitable for detecting a temperature inside the storage device. Said at least one temperature sensor (optionally all temperature sensors) can be suitable to detect a temperature of an outer surface of the storage device (e.g. by being placed on or at an outer surface of the storage device). The at least one temperature sensor (optionally all temperature sensors), or at least one further temperature sensor in addition to the at least one temperature sensor, can be suitable to detect a temperature of a content inside the storage device (e.g. by being placed in an inner volume of the storage device, like an interior of the storage device or an interior of a phase change material heat exchanger within the storage device). In this regard, the state of charge of the storage device can e.g. be determined as described in EP patent application EP21213459.7 . It is also possible that the detector for determining the state of charge comprises at least one temperature sensor and at least one electrical resistance sensor (e.g. as separate sensors or as a combined temperature-and-electrical-resistance sensor), wherein at least the electrical resistance sensor is suitable to detect an electrical resistance of a content (specifically: a fluid comprising or consisting of a PCM) inside the storage device (e.g. by being placed in an inner volume of the storage device and by contacting the inner content). In this regard, the state of charge of the storage device can e.g. be determined as described in the EP patent application EP21166193.9 .
  • The conveying means for circulating water through the heat medium heat exchanger can be a pump.
  • In a preferred embodiment, the system according to the invention does not comprise a two stage-compressor and/or does not comprise a further (i.e. at least a second) compressor. By using only one single compressor to pump heat across the first stage and the second stage, a smaller degree of complexity is achieved and the system can be provided at lower costs. Furthermore, since heat can be pumped across smaller temperature differences in two stages by the same single compressor, a smaller temperature lift across the heat pump and a higher COP is achieved.
  • In a further preferred embodiment, the first storage device is located outdoors, preferably within a heat pump outdoor unit comprising the compressor, the first expansion valve, the second expansion valve, the first three-way valve, the second three-way valve, the four-way switching valve, the outdoor heat exchanger and the heat medium heat exchanger. The advantage of this embodiment is that the system only needs a minimum of space in a room inside of a building and that the system can perform a more efficient operation. Furthermore, locating the first storage device outdoors is not connected to high thermal losses because the first storage device contains a phase change material with a lower phase change temperature than the second storage device. Hence, the temperature inside the first storage device can be kept lower so that a temperature gradient to an outdoor environment can be lower than if the second storage device was located outdoors.
  • Hence, in a further preferred embodiment, the second storage device (containing the phase change material with the higher phase change temperature) is preferably located indoors (i.e. inside a building). Since a significant fraction of the total required heat storage can be provided by the low-temperature phase change material in the first storage device, the size of the second storage device can be smaller than the size of the first storage device, which provides more free space in a room in which the second storage device is located. This is especially relevant if the room is inside of a building.
  • The first phase change material can have a phase transition temperature which is half way between an outdoor ambient air temperature in winter in a location where the system is located, and the phase change temperature of the second phase change material. For example, the first phase change material can have a phase transition temperature in the range of 10 °C to 35 °C, preferably 20 °C to 30 °C.
  • The second phase change material can have a phase transition temperature in the range of 35 °C to 60 °C, preferably 40 °C to 50 °C.
  • The controller can be configured to control an operation of the system which is further based on a requirement of a defrosting operation (of the outdoor heat exchanger). To this end, the outdoor heat exchanger can comprise a temperature sensor which is suitable to communicate with the controller or the system can comprise a temperature sensor for detecting a refrigerant temperature which is suitable to communicate with the controller. In this embodiment, the outdoor heat exchanger can comprise an outdoor heat exchanger temperature sensor and the controller can be configured to select a defrosting operation mode based on a temperature information communicated by said temperature sensor. This configuration has the advantage that in a case in which a defrosting operation is needed, the controller can switch to a defrosting operation mode. In said defrosting operation mode, the outdoor heat exchanger can be defrosted which allows a more efficient operation of the outdoor heat exchanger after the defrosting operation.
  • The controller can be configured to control an operation of the system which is further based on a demand for space heating within a building. In this embodiment, the system can comprise an indoor air temperature sensor in an indoor space to be heated and the controller can be configured to select a space heating operation mode based on a temperature information communicated by said temperature sensor. This configuration of the controller has the advantage that, if there is a demand of space heating, the system can switch to a space heating only operation mode. For example, in said heating mode, no heating energy is used for charging the first storage device and/or for charging the second storage device (with heat energy) and/or for providing domestic hot water. This is beneficial because heating a space to be heated becomes more efficient. If there is no demand for space heating, the system can switch to operation modes in which no heat is used to provide space heating. For example, in said operation modes, heat is used for charging the first storage device and/or second storage device (with heat energy) and/or for providing domestic hot water. This is beneficial because heating domestic hot water and/or charging the first and/or second storage device becomes more efficient.
  • The controller can be configured to control an operation of the system which is further based on an outdoor ambient air temperature. In this embodiment, the system can comprise an outdoor air temperature sensor in an outdoor space and the controller can be configured to select an operation mode of the system based on a temperature information communicated by said temperature sensor. This configuration of the controller has the advantage that an outdoor ambient air temperature can be used to decide whether the second storage device is charged with heat from outdoor air (if outdoor ambient air temperature is at or above a set lower limit) or charged with heat from the first storage device (if outdoor ambient air temperature is below a set lower limit). This allows a more efficient charging of the second storage device because heat is pumped over a shallower temperature gradient into the second storage device. Furthermore, an outdoor air temperature can be used to decide whether space heating is performed with heat from outdoor air (if outdoor ambient air temperature is at or above a set lower limit) or performed with heat from the first storage device (if outdoor ambient air temperature is below a set lower limit). This allows a more efficient space heating because heat is pumped over a shallower temperature gradient to the space to be heated.
  • The first three-way valve is preferably located in a fluid line connecting the compressor with the first phase change material heat exchanger and the heat medium heat exchanger.
  • Moreover, the second three-way valve is preferably located in a fluid line connecting the compressor with the first phase change material heat exchanger and the outdoor heat exchanger.
  • The refrigeration circuit of the system can comprise a receiver (accumulator). The receiver can be located in a fluid line between the first expansion valve and the second expansion valve in the refrigeration circuit.
  • The first expansion valve of the refrigeration circuit of the system can be located in a fluid line between the outdoor heat exchanger and a receiver of the refrigerant circuit.
  • The second expansion valve of the refrigeration circuit can be located in a fluid line between a receiver of the refrigerant circuit and a fluid line branching to the first phase change material heat exchanger and to the heat medium heat exchanger.
  • The controller of the system can be configured to
    • if a defrosting of the outdoor heat exchanger is required,
    • allow heat from the first phase change material heat exchanger to be conveyed to the outdoor heat exchanger,
    • wherein the controller is preferably configured to
      1. i) set the four-way switching valve to a position which allows refrigerant to flow from the first phase change material heat exchanger via the compressor to the outdoor heat exchanger,
      2. ii) set the first three-way valve to direct refrigerant from the first phase change material heat exchanger to the compressor;
      3. iii) set the second three-way valve to direct refrigerant from the compressor to the outdoor heat exchanger;
      adjust an orifice of the first expansion valve and adjust an orifice of the second expansion valve in combination, to control an evaporator superheating and a compressor subcooling.
  • This configuration of the controller has the advantage that heat stored in the second storage device can be used to defrost the outdoor heat exchanger in cold-ambient conditions, without compromising comfort conditions in the internal living space or supply temperature of the domestic hot water output.
  • The controller of the system can be configured to,
    • if no defrosting of the outdoor heat exchanger is required,
    • if a determined state of charge of the second storage device is below a set lower limit and
    • if a determined state of charge of the first storage device is below a set lower limit, or if a determined outdoor air temperature is at or above a set lower limit for outdoor ambient air temperature,
    • allow heat from the outdoor heat exchanger to be conveyed to the heat medium heat exchanger, especially until a determined state of charge of the second storage device is at or above a set upper limit,
    • wherein the controller is preferably configured to, especially until a determined state of charge of the second storage device is at or above a set upper limit,
      1. i) set the four-way switching valve to a position which allows refrigerant to flow from the outdoor heat exchanger via the compressor to the heat medium heat exchanger,
      2. ii) set the first three-way valve to direct refrigerant from the compressor to the heat medium heat exchanger,
      3. iii) set the second three-way valve to direct refrigerant from the outdoor heat exchanger to the compressor;
      4. iv) adjust an orifice of the first expansion valve and adjust an orifice of the second expansion valve in combination, to control an evaporator superheating and a compressor subcooling; and
      5. v) set the third three-way valve to direct water to the second phase change material heat exchanger.
  • This configuration of the controller has the advantage that the second storage device can be charged with heat energy from outside air.
  • The controller can be configured to
    • if no defrosting of the outdoor heat exchanger is required,
    • if a determined state of charge of the second storage device is below a set lower limit and
    • if a determined state of charge of the first storage device is at or above a set lower limit and if a determined outdoor air temperature is below a set lower limit for outdoor ambient air temperature,
    • allow heat from the first phase change material heat exchanger to be conveyed to the to the heat medium heat exchanger, especially until a determined state of charge of the second storage device is at or above a set upper limit, wherein the controller is preferably configured to, especially until a determined state of charge of the second storage device is at or above a set upper limit,
      1. i) set the four-way switching valve to a position which allows refrigerant to flow from the first phase change material heat exchanger via the compressor to the heat medium heat exchanger,
      2. ii) set the first three-way valve to direct refrigerant from the compressor to the heat medium heat exchanger,
      3. iii) set the second three-way valve to direct refrigerant from the first phase change material heat exchanger to the compressor;
      4. iv) adjust an orifice of the first expansion valve and adjust an orifice of the second expansion valve in combination, to control an evaporator superheating and a compressor subcooling; and
      5. v) set the third three-way valve to direct water to the second phase change material heat exchanger.
  • This configuration of the controller has the advantage that the second storage device can be charged with heat energy from the first storage device.
  • The controller can be configured to,
    • if no defrosting of the outdoor heat exchanger is required,
    • if a determined state of charge of the second storage device is at or above a set lower limit,
    • if there is a demand for space heating within a building, and
    • if a determined state of charge of the first storage device is below a set lower limit, or if a determined outdoor air temperature is at or above a set lower limit for outdoor ambient air temperature,
    • allow heat from the outdoor heat exchanger to be conveyed to the heat medium heat exchanger,
    • wherein the controller is preferably configured to
      1. i) set the four-way switching valve to a position which allows refrigerant to flow from the outdoor heat exchanger via the compressor to the heat medium heat exchanger,
      2. ii) set the first three-way valve to direct refrigerant from the compressor to the heat medium heat exchanger,
      3. iii) set the second three-way valve to direct refrigerant from the outdoor heat exchanger to the compressor;
      4. iv) adjust an orifice of the first expansion valve and adjust an orifice of the second expansion valve in combination, to control an evaporator superheating and a compressor subcooling; and
      5. v) set the third three-way valve to direct water to at least one heat emitter for space heating within a building.
  • This configuration of the controller has the advantage that heat energy from outside air can be (directly) transported to at least one space in a building. Hence, heat can be directly pumped from the outdoor air to a heat emitter circuit of a building.
  • The controller can be configured to,
    • if no defrosting of the outdoor heat exchanger is required,
    • if a determined state of charge of the second storage device is at or above a set lower limit,
    • if there is a demand for space heating within a building, and
    • if a determined state of charge of the first storage device is at or above a set lower limit and if a determined outdoor air temperature is below a set lower limit for outdoor ambient air temperature,
    • allow heat from the first phase change material heat exchanger to be conveyed
    • to the to the heat medium heat exchanger, especially until a determined state of charge of the second storage device is at or above a set upper limit, wherein the controller is preferably configured to, especially until a determined state of charge of the second storage device is at or above a set upper limit,
      1. i) set the four-way switching valve to a position which allows refrigerant to flow from the first phase change material heat exchanger via the compressor to the heat medium heat exchanger,
      2. ii) set the first three-way valve to direct refrigerant from the compressor to the heat medium heat exchanger,
      3. iii) set the second three way valve to direct refrigerant from the first phase change material heat exchanger to the compressor;
      4. iv) adjust an orifice of the first expansion valve and adjust an orifice of the second expansion valve in combination, to control an evaporator superheating and a compressor subcooling; and
      5. v) set the third three-way valve to direct water to at least one heat emitter for space heating within a building.
  • This configuration of the controller has the advantage that heat energy from the first storage device can be (directly) transported to at least one space in a building. Hence, heat can be directly pumped from the first storage device (containing phase change material at lower temperature) to a heat emitter circuit of a building.
  • The controller can be configured to,
    • if no defrosting of the outdoor heat exchanger is required,
    • if a determined state of charge of the second storage device is at or above a set lower limit,
    • if there is no demand for space heating within a building, and if a determined state of charge of the first storage device is below a set lower limit,
    • allow heat from the outdoor heat exchanger to be conveyed to the to the first phase change material heat exchanger, especially until a determined state of charge of the second storage device is at or above a set upper limit,
    • wherein the controller is preferably configured to, especially until a determined state of charge of the second storage device is at or above a set upper limit,
      1. i) set the four-way switching valve to a position which allows refrigerant to flow from the outdoor heat exchanger via the compressor to the first phase change material heat exchanger,
      2. ii) set the first three-way valve to direct refrigerant from the compressor to the first phase change material heat exchanger,
      3. iii) set the second three way valve to direct refrigerant from the outdoor heat exchanger to the compressor;
      4. iv) adjust an orifice of the first expansion valve and adjust an orifice of the second expansion valve in combination, to control an evaporator superheating and a compressor subcooling.
  • This configuration of the controller has the advantage that the first storage device can be charged with heat energy from outside air.
  • The heat medium circuit of the system can comprise a further heat exchanger suitable for exchanging heat between water (flowing in the heat medium circuit) and mains water (flowing in domestic hot water circuit). The further heat exchanger has the advantage that heat can be provided to mains water beside the second phase change material heat exchanger of the second storage device. For example, the further heat exchanger can be located upstream of the second phase change material heat exchanger of the second storage device. This location allows the further heat exchanger to preheat mains water before it enters into the second phase change material heat exchanger of the second storage device. Alternatively, the further heat exchanger may be located downstream of the second phase change material heat exchanger of the second storage device. This location allows the further heat exchanger to postheat mains water exiting the second phase change material heat exchanger of the second storage device. In this embodiment, the heat medium circuit preferably comprises a further three-way valve which is suitable to switch a flow of water to the second phase change material heat exchanger of the second storage device via the further heat exchanger or directly to the second phase change material heat exchanger of the second storage device by bypassing the further heat exchanger.
  • The first storage device of the system can comprise a renewable energy heat exchanger suitable for exchanging heat between the first phase change material and a fluid which receives heat energy from a renewable energy source.
  • This embodiment has the advantage that heat energy from a renewable energy source can be transferred to the first storage device and stored by the first phase change material inside the first storage device. The renewable energy source can be a solar thermal array. In this case, water can flow through the solar thermal array, absorb heat energy from the sun and transfer the absorbed heat energy to the first storage device by the renewable energy heat exchanger. In a particularly preferred embodiment, the renewable energy source is a solar photovoltaic-thermal array. In this case, water can flow through the solar photovoltaic thermal array, absorb heat energy from the sun and transfer the absorbed heat energy to the first storage device by the renewable energy heat exchanger and additionally, electric energy generated by the solar photovoltaic thermal array can be used to provide electricity to the system, i.e. can be used to operate the complete system or at least parts thereof (e.g. parts relating to the heat pump). In this embodiment, the system can further comprise an inverter to convert a DC voltage to an AC voltage.
  • According to the invention, a method for providing domestic hot water (DHW) and/or space heating (SH) within a building is provided, comprising
    1. a) providing a system comprising
      • a refrigeration circuit comprising
        • a refrigerant as heat medium,
        • a compressor,
        • a first expansion valve and a second expansion valve,
        • a first three-way valve and a second three-way valve,
        • a four-way switching valve, and
        • an outdoor heat exchanger suitable for exchanging heat between the refrigerant and air,
        • a first storage device containing a first phase change material, wherein the first storage device comprises a first detector for determining the state of charge of the first storage device and comprises a first phase change material heat exchanger suitable for exchanging heat between the refrigerant and the first phase change material;
      • a heat medium circuit comprising
        • water as heat medium,
        • a second storage device being thermally connected to a domestic hot water circuit and containing a second phase change material, wherein the phase change temperature of the second phase change material is higher than the phase change temperature of the first phase change material, wherein the second storage device comprises a second detector for determining the state of charge of the second storage device and comprises a second phase change material heat exchanger suitable for exchanging heat between water of the heat medium circuit and the second phase change material;
        • a third three-way valve suitable for switching a flow of water to either at least one heat emitter for space heating within a building or to the second phase change material heat exchanger;
        • at least one conveying means or circulating water through the heat medium heat exchanger;
      • a heat medium heat exchanger comprised by both the refrigeration circuit and the heat medium circuit, and being suitable for transferring heat between the refrigerant and water; and
      • a controller;
    2. b) control an operation of the system based on at least a state of charge of the first storage device determined by information obtained from the first detector and a state of charge of the second storage device determined by information obtained from the second detector.
  • The method has at least the advantages that it can provide domestic hot water and space heating in a building in a more efficient manner and with a minimum of space needed.
  • The first storage device of the system used in the method can be placed outdoors, preferably within a heat pump outdoor unit comprising the compressor, the first expansion valve, the second expansion valve, the first three-way valve, the second three-way valve, the four-way switching valve, the outdoor heat exchanger and the heat medium heat exchanger. The advantage is that carrying out the method requires less indoor space and results in a more efficient operation.
  • The method can be characterized in that, if a defrosting of the outdoor heat exchanger is required,
    heat from the first phase change material heat exchanger is allowed to be conveyed to the outdoor heat exchanger,
    wherein preferably
    1. i) the four-way switching valve is set to a position which allows refrigerant to flow from the first phase change material heat exchanger via the compressor to the outdoor heat exchanger,
    2. ii) the first three-way valve is set to direct refrigerant from the first phase change material heat exchanger to the compressor;
    3. iii) the second three-way valve is set to direct refrigerant from the compressor to the outdoor heat exchanger;
    4. iv) an orifice of the first expansion valve and an orifice of the second expansion valve is adjusted in combination, to control an evaporator superheating and a compressor subcooling.
  • This method has the advantage that heat stored in the second storage device can be used to defrost the outdoor heat exchanger in cold-ambient conditions, without compromising comfort conditions in the internal living space or supply temperature of the domestic hot water output.
  • The method can be characterized in that,
    • if no defrosting of the outdoor heat exchanger is required,
    • if a determined state of charge of the second storage device is below a set lower limit and
    • if a determined state of charge of the first storage device is below a set lower limit, or if a determined outdoor air temperature is at or above a set lower limit for outdoor ambient air temperature,
    • heat from the outdoor heat exchanger is allowed to be conveyed to the heat medium heat exchanger, especially until a determined state of charge of the second storage device is at or above a set upper limit,
    • wherein preferably, especially until a determined state of charge of the second storage device is at or above a set upper limit,
      1. i) the four-way switching valve is set to a position which allows refrigerant to flow from the outdoor heat exchanger via the compressor to the heat medium heat exchanger,
      2. ii) the first three-way valve is set to direct refrigerant from the compressor to the heat medium heat exchanger,
      3. iii) the second-three way valve is set to direct refrigerant from the outdoor heat exchanger to the compressor;
      4. iv) an orifice of the first expansion valve and an orifice of the second expansion valve is adjusted in combination, to control an evaporator superheating and a compressor subcooling; and
      5. v) the third three-way valve is set to direct water to the second phase change material heat exchanger.
  • This method has the advantage that the second storage device can be charged with heat energy from outside air.
  • The method can be characterized in that
    • if no defrosting of the outdoor heat exchanger is required,
    • if a determined state of charge of the second storage device is below a set lower limit and
    • if a determined state of charge of the first storage device is at or above a set lower limit and if a determined outdoor air temperature is below a set lower limit for outdoor ambient air temperature,
    • heat from the first phase change material heat exchanger is allowed to be conveyed to the to the heat medium heat exchanger, especially until a determined state of charge of the second storage device is at or above a set upper limit, wherein preferably, especially until a determined state of charge of the second storage device is at or above a set upper limit,
      1. i) the four-way switching valve is set to a position which allows refrigerant to flow from the first phase change material heat exchanger via the compressor to the heat medium heat exchanger,
      2. ii) the first three-way valve is set to direct refrigerant from the compressor to the heat medium heat exchanger,
      3. iii) the second three way valve is set to direct refrigerant from the first phase change material heat exchanger to the compressor;
      4. iv) an orifice of the first expansion valve and an orifice of the second expansion valve is adjusted in combination, to control an evaporator superheating and a compressor subcooling; and
      5. v) the third three-way valve is set to direct water to the second phase change material heat exchanger.
  • This method has the advantage that the second storage device can be charged with heat energy from the first storage device
  • The method can be characterized in that,
    • if no defrosting of the outdoor heat exchanger is required,
    • if a determined state of charge of the second storage device is at or above a set lower limit,
    • if there is a demand for space heating within a building, and if a determined state of charge of the first storage device is below a set lower limit, or if a determined outdoor air temperature is at or above a set lower limit for outdoor ambient air temperature,
    • heat from the outdoor heat exchanger is allowed to be conveyed to the heat medium heat exchanger,
    • wherein preferably
      1. i) the four-way switching valve is set to a position which allows refrigerant to flow from the outdoor heat exchanger via the compressor to the heat medium heat exchanger,
      2. ii) the first three-way valve is set to direct refrigerant from the compressor to the heat medium heat exchanger,
      3. iii) the second three way valve is set to direct refrigerant from the outdoor heat exchanger to the compressor;
      4. iv) an orifice of the first expansion valve and an orifice of the second expansion valve is adjusted in combination, to control an evaporator superheating and a compressor subcooling; and
      5. v) the third three-way valve is set to direct water to at least one heat emitter for space heating within a building.
  • This method has the advantage that heat energy from outside air can be (directly) transported to at least one space in a building. Hence, heat can be directly pumped from the outdoor air to a heat emitter circuit of a building.
  • The method can be characterized in that,
    • if no defrosting of the outdoor heat exchanger is required,
    • if a determined state of charge of the second storage device is at or above a set lower limit,
    • if there is a demand for space heating within a building, and
    • if a determined state of charge of the first storage device is at or above a set lower limit and if a determined outdoor air temperature is below a set lower limit for outdoor ambient air temperature,
    • heat from the first phase change material heat exchanger is allowed to be conveyed to the to the heat medium heat exchanger, especially until a determined state of charge of the second storage device is at or above a set upper limit, wherein preferably, especially until a determined state of charge of the second storage device is at or above a set upper limit,
      1. i) the four-way switching valve is set to a position which allows refrigerant to flow from the first phase change material heat exchanger via the compressor to the heat medium heat exchanger,
      2. ii) the first three-way valve is set to direct refrigerant from the compressor to the heat medium heat exchanger,
      3. iii) the second three way valve is set to direct refrigerant from the first phase change material heat exchanger to the compressor;
      4. iv) an orifice of the first expansion valve and an orifice of the second expansion valve is adjusted in combination, to control an evaporator superheating and a compressor subcooling; and
      5. v) the third three-way valve is set to direct water to at least one heat emitter for space heating within a building.
  • This method has the advantage that heat energy from the first storage device can be (directly) transported to at least one space in a building. Hence, heat can be directly pumped from the first storage device (containing phase change material at lower temperature) to a heat emitter circuit of a building.
  • The method can be characterized in that
    • if no defrosting of the outdoor heat exchanger is required,
    • if a determined state of charge of the second storage device is at or above a set lower limit,
    • if there is no demand for space heating within a building, and if a determined state of charge of the first storage device is below a set lower limit,
    • heat from the outdoor heat exchanger is allowed to be conveyed to the to the first phase change material heat exchanger, especially until a determined state of charge of the second storage device is at or above a set upper limit,
    • wherein preferably, especially until a determined state of charge of the second storage device is at or above a set upper limit,
      1. i) the four-way switching valve is set to a position which allows refrigerant to flow from the outdoor heat exchanger via the compressor to the first phase change material heat exchanger,
      2. ii) the first three-way is set to direct refrigerant from the compressor to the first phase change material heat exchanger,
      3. iii) the second three way valve is set to direct refrigerant from the outdoor heat exchanger to the compressor;
      4. iv) an orifice of the first expansion valve and an orifice of the second expansion valve is adjusted in combination, to control an evaporator superheating and a compressor subcooling.
  • This method has the advantage that the first storage device can be charged with heat energy from outside air.
  • In the method, a system according to the invention can be provided and used, i.e. the method can be conducted with a system according to the invention. The controller of the system can be configured to control steps of the method, e.g. control the settings of parts of the system.
  • With reference to the following figures and examples, the subject according to the invention is intended to be explained in more detail without wishing to restrict said subject to the specific embodiments shown here.
  • Figure 1 illustrates a system according to the invention. As can be seen in said Figure, the system comprises a first storage device 5 which contains a first phase change material (not shown) and comprises a first phase change material heat exchanger 6 and a first detector (not shown) for determining the state of charge of the first storage device. The system also comprises a second storage device 7 which contains a second phase change material having a higher phase change temperature than the first phase change material (not shown) and comprises a second phase change material heat exchanger 8. The heat medium circuit 22 comprises a three-way valve to switch a direction of water flow to the second phase change material heat exchanger 8 or to the heat emitter(s) 18. The heat medium circuit 22 further comprises a pump 10 for conveying water through the heat medium circuit 22. The system also comprises a heat medium heat exchanger 11 which is comprised by both the refrigeration circuit and the heat medium circuit 11 and which is suitable for transferring heat between the refrigerant and water of the heat medium circuit 22.
  • Figure 2 illustrates schematically components of a system according to the invention which relate to the refrigeration circuit 30. As can be seen in said Figure, the refrigeration circuit 30 comprises a compressor 1, a first expansion valve 2, a second expansion valve 2', a four-way switching valve 3, an outdoor heat exchanger 4 and a first storage device 5 containing a first phase change material (not shown) and comprising a first phase change material heat exchanger 6 and a first detector (not shown) for determining the state of charge of the first storage device. The refrigeration circuit further comprises a first three-way valve 13, a second three-way valve 14 and a receiver located between the first expansion valve 2 and the second expansion valve 2'. Furthermore, system comprises a heat medium heat exchanger 11 which is comprised by both the refrigeration circuit 30 and the heat medium circuit and which is suitable for transferring heat between the refrigerant of the refrigeration circuit 30 and water of the heat medium circuit, i.e. a cold water flow 28 from the heat medium circuit can be heated in the heat medium heat exchanger 11 and exit the heat medium heat exchanger 11 as a hot water flow 29 to the heat medium circuit.
  • Figure 3 illustrates the components shown in Figure 2 and indicates a flow direction of refrigerant in a first operation mode (HP mode 1). In HP mode 1, outside air 16 is used as a heat source. Heat is transferred to the first storage device 5 (to allow efficient charging of the first storage device 5).
  • Figure 4 illustrates the components shown in Figure 2 and indicates a flow direction of refrigerant in a second operation mode (HP mode 2) and in a fifth operation mode (HP mode 5). In both HP mode 2 and HP mode 5, the first storage device 5 is used as a heat source. In HP mode 2, heat is transferred to the second storage device 7 to charge the second storage device (to allow an efficient provision of domestic hot water) whereas in HP mode 5, heat is transferred to one or more heat emitter(s) 18 in a building (to allow an efficient provision of heat in a one or more room(s) in a building). Switching between HP mode 2 and 5 can be performed by switching three-way valve 9 of the heat medium circuit.
  • Figure 5 illustrates the components shown in Figure 2 and indicates a flow direction of refrigerant in a third operation mode (HP mode 3) and in a fourth operation mode (HP mode 4). In both HP mode 3 and HP mode 4, outside air 16 is used as a heat source. In HP mode 3, heat is transferred to the second storage device 7 to charge the second storage device (to allow an efficient provision of domestic hot water) whereas in HP mode 4, heat is transferred to one or more heat emitter(s) 18 in a building (to allow an efficient provision of heat in one or more room(s) in a building). Switching between HP mode 3 and 4 can be performed by switching three-way valve 9 of the heat medium circuit.
  • Figure 6 illustrates the components shown in Figure 2 and indicates a flow direction of refrigerant in a sixth heating operation mode (HP mode 6). In HP mode 6, the first storage device 5 is used as a heat source. Heat is transferred to the outdoor heat exchanger 4 (to allow an efficient defrosting of the outdoor heat exchanger).
  • Figure 7 illustrates schematically a decision tree for performing the method according to the invention and which can be implemented in the controller of the system according to the invention
  • Figure 8 illustrates a further system according to the invention having the features shown in Figure 1, wherein the heat medium circuit 22 of the system further comprises a heat exchanger 23 (preheating heat exchanger) which is suitable for directly exchanging heat between water in the heat medium circuit 22 and a water flow of mains water 19. The heat exchanger 23 is suitable to preheat mains water before it enters the second storage device 7, where the preheated mains water is further heated by the second phase change material heat exchanger 8 and exits the second storage device as a water flow of domestic hot water 20. Specifically, the second storage device 7 contains two heat exchanger coils in contact with the phase change material (PCM). One heat exchanger coil is for transferring heat from the heat medium circuit to the PCM and one heat exchanger coil is for transferring stored heat from the PCM to the domestic hot water fluid stream. The heat medium circuit 22 can comprise a further three-way valve 24 which is suitable to switch a flow of water of the heat medium circuit 22 either to the second phase change material heat exchanger 8 or to the heat exchanger 23, which allows a selection whether a preheating of mains water shall be performed or not.
  • Figure 9 illustrates a further system according to the invention having the features shown in Figure 1, wherein the system further comprises a solar photovoltaic-thermal array 26 (PVT array). As illustrated, the PVT array 26 can provide heat energy to the first storage container 5 via a renewable energy heat exchanger 25 located in the first storage container 5 and can provide electrical energy to parts of the system relating to the heat pump 17. To this end, the system can comprise an inverter 27 which is suitable for converting DC voltage to AC voltage.
  • Example 1 - Outdoor air as heat source for charging the first storage container (Figure 3) HP mode 1 - Charging the first storage device from air source
  • In this operating mode, the heat pump is used to pump heat from the outdoor air 16 to the first storage device 5 via the first phase change material heat exchanger 6 embedded in the first storage device 5. The refrigerant circuit flow configuration is set according to Fig 3.
  • The four-way switching valve 3 is set to its normal "heating" position. The three-way valve 13 is set to direct superheated refrigerant vapour from the compressor 1 discharge to the first storage device store heat exchanger 6, where it condenses, releasing heat to melt the first phase change material. The three-way valve 14 is set to direct 2-phase refrigerant leaving the linear expansion valve 2 to the outdoor heat exchanger 4, where it evaporates, absorbing heat from the air stream. The orifice of the first linear expansion valve 2 is adjusted to control the superheat temperature at the evaporator outlet, while the second linear expansion valve 2' is set fully open.
  • Example 2 - First storage device as heat source for providing domestic hot water and/or space heating within a building (Figure 4) HP mode 2 - Charging second storage device from first storage device source
  • In this operating mode, the heat pump is used to pump heat from the first storage device 5 to the second storage device 7, which allows an efficient provision of domestic hot water by the second storage device. This mode is used when outdoor air temperature is sufficiently low that using the heat stored in the first storage device 5 as the heat source offers a significant improvement to the COP of the heat pump compared to using outdoor air 16. The refrigerant circuit flow configuration is set according to Fig 4.
  • The four-way switching valve 3 is set to its normal "heating" position. The three-way valve 13 is set to direct superheated refrigerant vapour from the compressor 1 discharge to the heat medium heat exchanger 11, where it condenses, releasing heat to primary circulating fluid. The three-way valve 14 is set to direct 2-phase refrigerant leaving linear expansion valve 2 to the first storage device 5, where it evaporates, absorbing heat from the first phase change material which changes phase from liquid to solid. The orifice of the first linear expansion valve 2 is adjusted to control the superheat temperature at the evaporator outlet, while the second linear expansion valve 2' is set fully open.
  • The three-way valve 9 (shown in Fig. 1) is set to direct water of the heat medium circuit 22 to the second storage device 7 and not to the heat emitter(s) 18.
  • HP mode 5 - Space heating from first storage device source
  • In this operating mode, the heat pump is used to pump heat from the first storage device 5 to at least one heat emitter 18, which allows an efficient heating of at least one inside room in which the heat emitter is located. This mode is used when outdoor air temperature is sufficiently low and heat demand is sufficiently high that using the heat stored in the first storage device 5 as the heat source offers a significant improvement to the heat pump COP compared to using outdoor air 16. The refrigerant circuit flow configuration is set according to Fig 4.
  • The four-way switching valve 3 is set to its normal "heating" position. The three-way valve 13 is set to direct superheated refrigerant vapour from the compressor 1 discharge to the heat medium heat exchanger 11, where it condenses, releasing heat to primary circulating fluid. The three-way valve 14 is set to direct 2-phase refrigerant leaving linear expansion valve 2 to the first storage device 5, where it evaporates, absorbing heat from the first phase change material which changes phase from liquid to solid. The orifice of the first linear expansion valve 2 is adjusted to control the superheat temperature at the evaporator outlet, while the second linear expansion valve 2' is set fully open.
  • The three-way valve 9 (shown in Fig. 1) is set to direct water of the heat medium circuit 22 to the heat emitter(s) 18 and not to the second storage device 7.
  • Example 3 - Outdoor air as heat source for providing domestic hot water and/or space heating within a building (Figure 5) HP mode 3 - charging second storage device from outdoor air source
  • In this operating mode, the heat pump is used to pump heat from the outdoor air 16 to the second storage device 7. This mode is used when there is an immediate demand for domestic hot water (DHW), but there is not sufficient thermal energy stored in the first storage device 5, or when outdoor air 16 temperature is sufficiently high that using the heat stored in the first storage device 5 as the heat source offers no significant improvement to the heat pump COP compared to using the outdoor air 16. The refrigerant circuit flow configuration is set according to Fig 5.
  • The four-way switching valve 3 is set to its normal "heating" position. The three-way valve 13 is set to direct superheated refrigerant vapour from the compressor 1 discharge to the heat medium heat exchanger 11, where it condenses, releasing heat to primary circulating fluid. The three-way valve 14 is set to direct 2-phase refrigerant leaving linear expansion valve 2 to the outdoor heat exchanger 4, where it evaporates, absorbing heat from the air stream. The orifice of the first linear expansion valve 2 is adjusted to control the superheat temperature at the evaporator outlet, while the second linear expansion valve 2' is set fully open.
  • The three-way valve 9 (shown in Fig. 1) is set to direct water of the heat medium circuit 22 to the second storage device 7 and not to the heat emitter(s) 18.
  • HP mode 4 - space heating with outdoor air source
  • In this operating mode, the heat pump is used to pump heat from the outdoor air 16 to the heat emitter(s) 18. This mode is used when outdoor air 16 temperature is sufficiently high and heat demand is sufficiently low that using the heat stored in the first storage device 5 as heat source offers no significant improvement to the heat pump COP compared to using the outdoor air 16. The refrigerant circuit flow configuration is set according to Fig 5.
  • The four-way switching valve 3 is set to its normal "heating" position. The three-way valve 13 is set to direct superheated refrigerant vapour from the compressor 1 discharge to the heat medium heat exchanger 11, where it condenses, releasing heat to primary circulating fluid. The three-way valve 14 is set to direct 2-phase refrigerant leaving linear expansion valve 2 to the outdoor heat exchanger 4, where it evaporates, absorbing heat from the air stream. The orifice of the first linear expansion valve 2 is adjusted to control the superheat temperature at the evaporator outlet, while the second linear expansion valve 2' is set fully open.
  • The three-way valve 9 (shown in Fig. 1) is set to direct water of the heat medium circuit to the heat emitter(s) 18 and not to the second storage device 7.
  • Example 4 - First storage device as heat source for defrosting outdoor heat exchanger (Figure 6) HP mode 6 - Defrost outdoor heat exchanger using stored heat from first storage device
  • In this operating mode, the heat pump is used to pump heat from the first storage device 5 to (periodically) defrost the outdoor heat exchanger 4 during cold outdoor temperatures. The refrigerant circuit flow configuration is set according to Figure 6.
  • The four-way switching valve 3 is set to its reverse "defrost" position. Low-pressure 2-phase refrigerant enters the first phase change material heat exchanger 6 where it is evaporated, absorbing latent heat released by the first phase change material. The three-way valve 13 is set to direct the low-pressure vapour leaving the first phase change material heat exchanger 6 to the compressor 1 intake. The three-way valve 14 directs the high pressure superheated vapour leaving the compressor 1 discharge to the outdoor heat exchanger 4 where it condenses, releasing heat to defrost the ice build-up on the external surface of outdoor heat exchanger 4. The orifice of the second linear expansion valve 2' is adjusted to control the superheat temperature at the outlet of the first phase change material heat exchanger 6, while the first linear expansion valve 2 is set fully open.
  • Example 5 - Further heat exchanger for preheating mains water (Figure 8)
  • Figure 8 shows a possible implementation by which mains water can be preheated using the heat pump (either with air as heat source or the first storage device 5 as heat source) and a further heat exchanger (e.g. a plate type heat exchanger) and a further 3-way valve 24 in the heat medium circuit.
  • Such an arrangement is particularly beneficial during longer DHW draw-off events (e.g. bath or shower), allowing the fraction of the DHW heating load extracted from the second storage device 7 to be reduced by as much as 20-50% (depending on the nominal capacity of the heat pump). Thus a larger volume of DHW can be supplied before it is necessary to charge the second storage device 7 or, when the aim is to provide a comparable volume of DHW, the second storage device 7 can be sized smaller which allows for less indoor room to be occupied by the second storage device 7.
  • Example 6 - Solar thermal array or a solar PVT array as heat source for charging the first storage device (Figure 9)
  • By incorporating a dual heat exchanger design for the first storage device 5, a secondary renewable heat source, such as a solar thermal collector array can be used to provide thermal input to the system. This has a particular advantage in this arrangement because the solar thermal collector array can achieve a higher-efficiency operation at the low melting temperature of the first storage device 5 compared to a conventional arrangement where solar thermal collectors are required to heat DHW to higher storage temperatures of approx. 60 °C. This means that lower-cost solar collector designs (e.g. unglazed flat-plat collectors) could be used, for which there is usually a more pronounced reduction in efficiency at higher operating temperatures than for higher-cost designs (e.g. evacuated-tube collectors).
  • More preferably, a hybrid photovoltaic-thermal collector array (PVT-array) in which a photovoltaic cell and solar-thermal collector are incorporated in the same module are used instead of the solar thermal array. These are often designed for lower operating temperatures in order to maintain both a high PV electrical efficiency and a reasonable solar thermal efficiency. A proposed arrangement of the system in combination with a PVT array is shown in Fig 9. The use of PVT collectors is highly advantageous because electricity generated by the PVT array can be used to run the whole system or at least components thereof (e.g. parts relating to the heat pump). Thus, the system can be operated completely or at least partially from renewable energy (i.e. solar energy).
  • List of reference signs and abbreviations
  • 1:
    compressor;
    2:
    first expansion valve;
    2':
    second expansion valve;
    3:
    four-way switching valve;
    4:
    outdoor heat exchanger;
    5:
    first storage device containing a first phase change material
    6:
    first phase change material heat exchanger;
    7:
    second storage device containing a second phase change material;
    8:
    second phase change material heat exchanger;
    9:
    third three-way valve (three-way valve of heat medium circuit);
    10:
    conveying means (e.g. a pump) of heat medium circuit;
    11:
    a heat medium heat exchanger;
    12:
    controller;
    13:
    first three-way valve (1st three-way valve of refrigeration circuit);
    14:
    second three-way valve (2nd three way valve of refrigeration circuit);
    15:
    receiver of the refrigerant circuit;
    16:
    outdoor air;
    17:
    dual source/dual sink heat pump;
    18:
    heat emitter(s) for space heating;
    19:
    water flow of mains water;
    20:
    water flow of domestic hot water;
    21:
    integrated outdoor unit;
    22:
    heat medium circuit;
    23:
    preheating heat exchanger of heat medium circuit;
    24:
    further three-way valve of heat medium circuit;
    25:
    renewable energy heat exchanger;
    26:
    renewable energy source (PVT array);
    27:
    inverter;
    28:
    cold water flow from heat medium circuit;
    29:
    hot water flow to heat medium circuit;
    30:
    refrigeration circuit;
    SOC1:
    state of charge of first phase change material;
    SOC2:
    state of charge of second phase change material;
    LL1:
    set lower limit for SOC1;
    LL2:
    set lower limit for SOC2;
    UL1:
    set upper limit for SOC1;
    UL2:
    set upper limit for SOC2;
    TOA:
    outdoor ambient air temperature;
    LLTOA:
    set lower limit for outdoor ambient air temperature;
    DHW:
    Domestic hot water;
    SH:
    space heating (within a building);
    HP mode:
    heat pump mode.

Claims (16)

  1. System for providing domestic hot water (DHW) and/or space heating (SH) within a building, comprising
    a) a refrigeration circuit comprising
    a refrigerant as heat medium,
    a compressor (1),
    a first expansion valve (2) and a second expansion valve (2'),
    a first three-way valve (13) and a second three-way valve (14),
    a four-way switching valve (3), and
    an outdoor heat exchanger (4) suitable for exchanging heat between the refrigerant and air,
    a first storage device (5) containing a first phase change material, wherein the first storage device (5) comprises a first detector for determining the state of charge (SOC1) of the first storage device (5) and comprises a first phase change material heat exchanger (6) suitable for exchanging heat between the refrigerant and the first phase change material;
    b) a heat medium circuit comprising
    water as heat medium,
    a second storage device (7) being thermally connected to a domestic hot water circuit and containing a second phase change material, wherein the phase change temperature of the second phase change material is higher than the phase change temperature of the first phase change material, wherein the second storage device (7) comprises a second detector for determining the state of charge (SOC2) of the second storage device (7) and comprises a second phase change material heat exchanger (8) suitable for exchanging heat between water of the heat medium circuit and the second phase change material;
    a third three-way valve (9) suitable for switching a flow of water to either at least one heat emitter for space heating within a building or to the second phase change material heat exchanger (8);
    at least one conveying means (10) for circulating water through the heat medium heat exchanger;
    c) a heat medium heat exchanger (11) comprised by both the refrigeration circuit and the heat medium circuit, and being suitable for transferring heat between the refrigerant and water; and
    d) a controller (12) configured to control an operation of the system based on at least a state of charge (SOC1) of the first storage device (5) determined by information obtained from the first detector and a state of charge (SOC2) of the second storage device (7) determined by information obtained from the second detector.
  2. System according to the preceding claim, characterized in that the first storage device (5) is located outdoors, preferably within a heat pump outdoor unit comprising the compressor (1), the first expansion valve (2), the second expansion valve (2'), the first three-way valve (13), the second three-way valve (14), the four-way switching valve (3), the outdoor heat exchanger (4) and the heat medium heat exchanger (11).
  3. System according to one of the preceding claims, characterized in that the controller (12) is configured to,
    if a defrosting of the outdoor heat exchanger (4) is required,
    allow heat from the first phase change material heat exchanger (6) to be conveyed to the outdoor heat exchanger (4),
    wherein the controller (12) is preferably configured to
    i) set the four-way switching valve (3) to a position which allows refrigerant to flow from the first phase change material heat exchanger (6) via the compressor (1) to the outdoor heat exchanger (4),
    ii) set the first three-way valve (13) to direct refrigerant from the first phase change material heat exchanger (6) to the compressor (1);
    iii) set the second three-way valve (14) to direct refrigerant from the compressor (1) to the outdoor heat exchanger (4); and
    iv) adjust an orifice of the first expansion valve (2) and adjust an orifice of the second expansion valve (2') in combination, to control an evaporator superheating and a compressor subcooling.
  4. System according to one of the preceding claims, characterized in that the controller (12) is configured to,
    if no defrosting of the outdoor heat exchanger (4) is required,
    if a determined state of charge (SOC2) of the second storage device (7) is below a set lower limit (LL2) and
    if a determined state of charge (SOC1) of the first storage device (5) is below a set lower limit (LL1), or if a determined outdoor air temperature (TOA) is at or above a set lower limit for outdoor ambient air temperature (LLTOA),
    allow heat from the outdoor heat exchanger (4) to be conveyed to the heat medium heat exchanger (11), especially until a determined state of charge (SOC2) of the second storage device (7) is at or above a set upper limit (UL2),
    wherein the controller (12) is preferably configured to, especially until a determined state of charge (SOC2) of the second storage device is at or above a set upper limit (UL2),
    i) set the four-way switching valve (3) to a position which allows refrigerant to flow from the outdoor heat exchanger (4) via the compressor (1) to the heat medium heat exchanger (11),
    ii) set the first three-way valve (13) to direct refrigerant from the compressor (1) to the heat medium heat exchanger (11),
    iii) set the second-three way valve (14) to direct refrigerant from the outdoor heat exchanger (4) to the compressor (1);
    iv) adjust an orifice of the first expansion valve (2) and adjust an orifice of the second expansion valve (2') in combination, to control an evaporator superheating and a compressor subcooling; and
    v) set the third three-way valve (9) to direct water to the second phase change material heat exchanger (8).
  5. System according to one of the preceding claims, characterized in that the controller (12) is configured to,
    if no defrosting of the outdoor heat exchanger (4) is required,
    if a determined state of charge (SOC2) of the second storage device is below a set lower limit (LL2) and
    if a determined state of charge (SOC1) of the first storage device (5) is at or above a set lower limit (LL1) and if a determined outdoor air temperature (TOA) is below a set lower limit for outdoor ambient air temperature (LLTOA),
    allow heat from the first phase change material heat exchanger (6) to be conveyed to the to the heat medium heat exchanger (11), especially until a determined state of charge (SOC2) of the second storage device (7) is at or above a set upper limit (UL2),
    wherein the controller (12) is preferably configured to, especially until a determined state of charge (SOC2) of the second storage device (7) is at or above a set upper limit (UL2),
    i) set the four-way switching valve (3) to a position which allows refrigerant to flow from the first phase change material heat exchanger (6) via the compressor (1) to the heat medium heat exchanger (11),
    ii) set the first three-way valve (13) to direct refrigerant from the compressor (1) to the heat medium heat exchanger (11),
    iii) set the second three-way valve (14) to direct refrigerant from the first phase change material heat exchanger (6) to the compressor (1);
    iv) adjust an orifice of the first expansion valve (2) and adjust an orifice of the second expansion valve (2') in combination, to control an evaporator superheating and a compressor subcooling; and
    v) set the third three-way valve (9) to direct water to the second phase change material heat exchanger (8).
  6. System according to one of the preceding claims, characterized in that the controller (12) is configured to,
    if no defrosting of the outdoor heat exchanger (4) is required,
    if a determined state of charge (SOC2) of the second storage device (7) is at or above a set lower limit (LL2),
    if there is a demand for space heating (SH) within a building, and
    if a determined state of charge (SOC1) of the first storage device (5) is below a set lower limit (LL1), or if a determined outdoor air temperature (TOA) is at or above a set lower limit for outdoor ambient air temperature (LLTOA),
    allow heat from the outdoor heat exchanger (4) to be conveyed to the heat medium heat exchanger (11),
    wherein the controller (12) is preferably configured to
    i) set the four-way switching valve (3) to a position which allows refrigerant to flow from the outdoor heat exchanger (4) via the compressor (1) to the heat medium heat exchanger (11),
    ii) set the first three-way valve (13) to direct refrigerant from the compressor (1) to the heat medium heat exchanger (11),
    iii) set the second three-way valve (14) to direct refrigerant from the outdoor heat exchanger (4) to the compressor (1);
    iv) adjust an orifice of the first expansion valve (2) and adjust an orifice of the second expansion valve (2') in combination, to control an evaporator superheating and a compressor subcooling; and
    v) set the third three-way valve (9) to direct water to at least one heat emitter for space heating within a building.
  7. System according to one of the preceding claims, characterized in that the controller (12) is configured to,
    if no defrosting of the outdoor heat exchanger (4) is required,
    if a determined state of charge (SOC2) of the second storage device (7) is at or above a set lower limit (LL2),
    if there is a demand for space heating (SH) within a building, and
    if a determined state of charge (SOC1) of the first storage device (5) is at or above a set lower limit (LL1) and if a determined outdoor air temperature (TOA) is below a set lower limit for outdoor ambient air temperature (LLTOA),
    allow heat from the first phase change material heat exchanger (6) to be conveyed to the to the heat medium heat exchanger (11), especially until a determined state of charge (SOC2) of the second storage device (7) is at or above a set upper limit (UL2),
    wherein the controller (12) is preferably configured to, especially until a determined state of charge (SOC2) of the second storage device (7) is at or above a set upper limit (UL2),
    i) set the four-way switching valve (3) to a position which allows refrigerant to flow from the first phase change material heat exchanger (6) via the compressor (1) to the heat medium heat exchanger (11),
    ii) set the first three-way valve (13) to direct refrigerant from the compressor (1) to the heat medium heat exchanger (11),
    iii) set the second three-way valve (14) to direct refrigerant from the first phase change material heat exchanger (6) to the compressor (1);
    iv) adjust an orifice of the first expansion valve (2) and adjust an orifice of the second expansion valve (2') in combination, to control an evaporator superheating and a compressor subcooling; and
    v) set the third three-way valve (9) to direct water to at least one heat emitter for space heating within a building.
  8. System according to one of the preceding claims, characterized in that the controller (12) is configured to,
    if no defrosting of the outdoor heat exchanger (4) is required,
    if a determined state of charge (SOC2) of the second storage device (7) is at or above a set lower limit (LL2),
    if there is no demand for space heating (SH) within a building, and
    if a determined state of charge (SOC1) of the first storage device (5) is below a set lower limit (LL1),
    allow heat from the outdoor heat exchanger (4) to be conveyed to the to the first phase change material heat exchanger (6), especially until a determined state of charge (SOC2) of the second storage device (7) is at or above a set upper limit (UL2),
    wherein the controller (12) is preferably configured to, especially until a determined state of charge (SOC2) of the second storage device (7) is at or above a set upper limit (UL2),
    i) set the four-way switching valve (3) to a position which allows refrigerant to flow from the outdoor heat exchanger (4) via the compressor (1) to the first phase change material heat exchanger (6),
    ii) set the first three-way valve (13) to direct refrigerant from the compressor (1) to the first phase change material heat exchanger (6),
    iii) set the second three-way valve (14) to direct refrigerant from the outdoor heat exchanger (4) to the compressor (1);
    iv) adjust an orifice of the first expansion valve (2) and adjust an orifice of the second expansion valve (2') in combination, to control an evaporator superheating and a compressor subcooling.
  9. Method for providing domestic hot water (DHW) and/or space heating (SH) within a building, comprising
    a) providing a system comprising
    a refrigeration circuit comprising
    a refrigerant as heat medium,
    a compressor (1),
    a first expansion valve (2) and a second expansion valve (2'),
    a first three-way valve (13) and a second three-way valve (14),
    a four-way switching valve (3), and
    an outdoor heat exchanger (4) suitable for exchanging heat between the refrigerant and air,
    a first storage device (5) containing a first phase change material, wherein the first storage device (5) comprises a first detector for determining the state of charge (SOC1) of the first storage device (5) and comprises a first phase change material heat exchanger (6) suitable for exchanging heat between the refrigerant and the first phase change material;
    a heat medium circuit comprising
    water as heat medium,
    a second storage device (7) being thermally connected to a domestic hot water circuit and containing a second phase change material, wherein the phase change temperature of the second phase change material is higher than the phase change temperature of the first phase change material, wherein the second storage device (7) comprises a second detector for determining the state of charge (SOC2) of the second storage device (7) and comprises a second phase change material heat exchanger (8) suitable for exchanging heat between water of the heat medium circuit and the second phase change material;
    a third three-way valve (9) suitable for switching a flow of water to either at least one heat emitter for space heating within a building or to the second phase change material heat exchanger (8);
    at least one conveying means (10) for circulating water through the heat medium heat exchanger;
    a heat medium heat exchanger (11) comprised by both the refrigeration circuit and the heat medium circuit, and being suitable for transferring heat between the refrigerant and water; and
    a controller (12);
    b) control an operation of the system based on at least a state of charge (SOC1) of the first storage device (5) determined by information obtained from the first detector and a state of charge (SOC2) of the second storage device (7) determined by information obtained from the second detector.
  10. Method according to claim 9, characterized in that the first storage device (5) is placed outdoors, preferably within a heat pump outdoor unit comprising the compressor (1), the first expansion valve (2), the second expansion valve (2'), the first three-way valve (13), the second three-way valve (14), the four-way switching valve (3), the outdoor heat exchanger (4) and the heat medium heat exchanger (11).
  11. Method according to one of claims 9 or 10, characterized in that,
    if a defrosting of the outdoor heat exchanger (4) is required,
    heat from the first phase change material heat exchanger (6) is allowed to be conveyed to the outdoor heat exchanger (4),
    wherein preferably
    i) the four-way switching valve (3) is set to a position which allows refrigerant to flow from the first phase change material heat exchanger (6) via the compressor (1) to the outdoor heat exchanger (4),
    ii) the first three-way valve (13) is set to direct refrigerant from the first phase change material heat exchanger (6) to the compressor (1);
    iii) the second three-way valve (14) is set to direct refrigerant from the compressor (1) to the outdoor heat exchanger (4); and
    iv) an orifice of the first expansion valve (2) and an orifice of the second expansion valve (2') is adjusted in combination, to control an evaporator superheating and a compressor subcooling.
  12. Method according to one the claims 9 to 11, characterized in that,
    if no defrosting of the outdoor heat exchanger (4) is required,
    if a determined state of charge (SOC2) of the second storage device (7) is below a set lower limit (LL2) and
    if a determined state of charge (SOC1) of the first storage device (5) is below a set lower limit (LL1), or if a determined outdoor air temperature (TOA) is at or above a set lower limit for outdoor ambient air temperature (LLTOA),
    heat from the outdoor heat exchanger (4) is allowed to be conveyed to the heat medium heat exchanger (11), especially until a determined state of charge (SOC2) of the second storage device (7) is at or above a set upper limit (UL2),
    wherein preferably, especially until a determined state of charge (SOC2) of the second storage device (7) is at or above a set upper limit (UL2),
    i) the four-way switching valve (3) is set to a position which allows refrigerant to flow from the outdoor heat exchanger (4) via the compressor (1) to the heat medium heat exchanger (11),
    ii) the first three-way valve (13) is set to direct refrigerant from the compressor (1) to the heat medium heat exchanger (11),
    iii) the second-three way valve (14) is set to direct refrigerant from the outdoor heat exchanger (4) to the compressor (1);
    iv) an orifice of the first expansion valve (2) and an orifice of the second expansion valve (2') is adjusted in combination, to control an evaporator superheating and a compressor subcooling; and
    v) the third three-way valve (9) is set to direct water to the second phase change material heat exchanger (8).
  13. Method according to one of the claims 9 to 12, characterized in that,
    if no defrosting of the outdoor heat exchanger (4) is required,
    if a determined state of charge (SOC2) of the second storage device (7) is below a set lower limit (LL2) and
    if a determined state of charge (SOC1) of the first storage device (5) is at or above a set lower limit (LL1) and if a determined outdoor air temperature (TOA) is below a set lower limit for outdoor ambient air temperature (LLTOA),
    heat from the first phase change material heat exchanger (6) is allowed to be conveyed to the to the heat medium heat exchanger (11), especially until a determined state of charge (SOC2) of the second storage device (7) is at or above a set upper limit (UL2),
    wherein preferably, especially until a determined state of charge (SOC2) of the second storage device (7) is at or above a set upper limit (UL2),
    i) the four-way switching valve (3) is set to a position which allows refrigerant to flow from the first phase change material heat exchanger (6) via the compressor (1) to the heat medium heat exchanger (11),
    ii) the first three-way valve (13) is set to direct refrigerant from the compressor (1) to the heat medium heat exchanger (11),
    iii) the second three way valve (14) is set to direct refrigerant from the first phase change material heat exchanger (6) to the compressor (1);
    iv) an orifice of the first expansion valve (2) and an orifice of the second expansion valve (2') is adjusted in combination, to control an evaporator superheating and a compressor subcooling; and
    v) the third three-way valve (9) is set to direct water to the second phase change material heat exchanger (8).
  14. Method according to one of the claims 9 to 13, characterized in that,
    if no defrosting of the outdoor heat exchanger (4) is required,
    if a determined state of charge (SOC2) of the second storage device (7) is at or above a set lower limit (LL2),
    if there is a demand for space heating (SH) within a building, and
    if a determined state of charge (SOC1) of the first storage device (5) is below a set lower limit (LL1), or if a determined outdoor air temperature (TOA) is at or above a set lower limit for outdoor ambient air temperature (LLTOA),
    heat from the outdoor heat exchanger (4) is allowed to be conveyed to the heat medium heat exchanger (11),
    wherein preferably
    i) the four-way switching valve (3) is set to a position which allows refrigerant to flow from the outdoor heat exchanger (4) via the compressor (1) to the heat medium heat exchanger (11),
    ii) the first three-way valve (13) is set to direct refrigerant from the compressor (1) to the heat medium heat exchanger (11),
    iii) the second three-way valve (14) is set to direct refrigerant from the outdoor heat exchanger (4) to the compressor (1);
    iv) an orifice of the first expansion valve (2) and an orifice of the second expansion valve (2') is adjusted in combination, to control an evaporator superheating and a compressor subcooling; and
    v) the third three-way valve (9) is set to direct water to at least one heat emitter for space heating within a building.
  15. Method according to one of the claims 9 to 14, characterized in that,
    if no defrosting of the outdoor heat exchanger (4) is required,
    if a determined state of charge (SOC2) of the second storage device (7) is at or above a set lower limit (LL2),
    if there is a demand for space heating (SH) within a building, and
    if a determined state of charge (SOC1) of the first storage device (5) is at or above a set lower limit (LL1) and if a determined outdoor air temperature (TOA) is below a set lower limit for outdoor ambient air temperature (LLTOA),
    heat from the first phase change material heat exchanger (6)is allowed to be conveyed to the to the heat medium heat exchanger (11), especially until a determined state of charge (SOC2) of the second storage device (7) is at or above a set upper limit (UL2),
    wherein preferably, especially until a determined state of charge (SOC2) of the second storage device (7) is at or above a set upper limit (UL2),
    i) the four-way switching valve (3) is set to a position which allows refrigerant to flow from the first phase change material heat exchanger (6) via the compressor (1) to the heat medium heat exchanger (11),
    ii) the first three-way valve (13) is set to direct refrigerant from the compressor (1) to the heat medium heat exchanger (11),
    iii) the second three way valve (14) is set to direct refrigerant from the first phase change material heat exchanger (6) to the compressor (1);
    iv) an orifice of the first expansion valve (2) and an orifice of the second expansion valve (2') is adjusted in combination, to control an evaporator superheating and a compressor subcooling; and
    v) the third three-way valve (9) is set to direct water to at least one heat emitter for space heating within a building.
  16. Method according to one of the claims 9 to 15, characterized in that,
    if no defrosting of the outdoor heat exchanger (4) is required,
    if a determined state of charge (SOC2) of the second storage device (7) is at or above a set lower limit (LL2),
    if there is no demand for space heating (SH) within a building, and
    if a determined state of charge (SOC1) of the first storage device (5) is below a set lower limit (LL1),
    heat from the outdoor heat exchanger (4) is allowed to be conveyed to the to the first phase change material heat exchanger (6), especially until a determined state of charge (SOC2) of the second storage device (7) is at or above a set upper limit (UL2),
    wherein preferably, especially until a determined state of charge (SOC2) of the second storage device (7) is at or above a set upper limit (UL2),
    i) the four-way switching valve (3) is set to a position which allows refrigerant to flow from the outdoor heat exchanger (4) via the compressor (1) to the first phase change material heat exchanger (6),
    ii) the first three-way valve (13) is set to direct refrigerant from the compressor (1) to the first phase change material heat exchanger (6),
    iii) the second three way valve (14) is set to direct refrigerant from the outdoor heat exchanger (4) to the compressor (1);
    iv) an orifice of the first expansion valve (2) and an orifice of the second expansion valve (2') is adjusted in combination, to control an evaporator superheating and a compressor subcooling.
EP22164465.1A 2022-03-25 2022-03-25 System and method for providing domestic hot water and/or space heating within a building Pending EP4249812A1 (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
EP22164465.1A EP4249812A1 (en) 2022-03-25 2022-03-25 System and method for providing domestic hot water and/or space heating within a building
JP2023043041A JP2023143814A (en) 2022-03-25 2023-03-17 System and method for providing domestic hot water and/or space heating within building
CN202310261381.8A CN116804466A (en) 2022-03-25 2023-03-17 System and method for providing domestic hot water and/or space heating in a building

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP22164465.1A EP4249812A1 (en) 2022-03-25 2022-03-25 System and method for providing domestic hot water and/or space heating within a building

Publications (1)

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EP4249812A1 true EP4249812A1 (en) 2023-09-27

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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008180473A (en) 2007-01-26 2008-08-07 Kenji Umetsu Hybrid energy-using heat pump device
JP2012007796A (en) 2010-06-24 2012-01-12 Panasonic Corp Heat storage system
GB2488331A (en) * 2011-02-23 2012-08-29 Star Refrigeration Heat pump system with a thermal store comprising a phase change material
DE102012004094B3 (en) * 2012-02-29 2013-06-13 Glen Dimplex Deutschland Gmbh Heat pump apparatus of heating system installed in e.g. single or multi-family dwelling, has control unit for passing refrigerant heated in heat accumulator through evaporator and defrosting refrigerant, in defrost mode
WO2015133107A1 (en) * 2014-03-04 2015-09-11 パナソニックIpマネジメント株式会社 Heat-pump hot water generator

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008180473A (en) 2007-01-26 2008-08-07 Kenji Umetsu Hybrid energy-using heat pump device
JP2012007796A (en) 2010-06-24 2012-01-12 Panasonic Corp Heat storage system
GB2488331A (en) * 2011-02-23 2012-08-29 Star Refrigeration Heat pump system with a thermal store comprising a phase change material
DE102012004094B3 (en) * 2012-02-29 2013-06-13 Glen Dimplex Deutschland Gmbh Heat pump apparatus of heating system installed in e.g. single or multi-family dwelling, has control unit for passing refrigerant heated in heat accumulator through evaporator and defrosting refrigerant, in defrost mode
WO2015133107A1 (en) * 2014-03-04 2015-09-11 パナソニックIpマネジメント株式会社 Heat-pump hot water generator

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
EMHOFER JOHANN ET AL: "Experimental demonstration of an air-source heat pump application using an integrated phase change material storage as a desuperheater for domestic hot water generation", APPLIED ENERGY, ELSEVIER SCIENCE PUBLISHERS, GB, vol. 305, 25 September 2021 (2021-09-25), XP086855052, ISSN: 0306-2619, [retrieved on 20210925], DOI: 10.1016/J.APENERGY.2021.117890 *

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