Patent Application
20200166291
The invention relates to a latent heat storage system having a latent heat storage device and to a method for operating a latent heat storage system.
From EP 2614330 A1, an ice storage system is known, in which an extraction heat exchanger extracts heat from an ice storage device during the heating period, until the ice storage device is thermally unloaded. The heat carrier medium of the extraction heat exchanger reaches the feed line of a heat pump which generates a higher temperature level at its output from the supplied low-calorie heat. During the thermal unloading of the ice storage device, a predetermined volume has completely solidified into ice around the extraction heat exchanger.
The heat transfer between the heat carrier medium in the extraction heat exchanger and the storage medium is limited. The ice around the extraction heat exchanger can be strongly supercooled when the ice storage device has a high icing degree. The consequence is that the heat pump switches off in such operating states. As a result, the efficiency of the system drops.
The aim of the invention is to create a latent heat storage system which has an increased efficiency.
Another aim of the invention is to create an advantageous method for operating such a latent heat storage system.
The invention starts, according to an aspect thereof, from a latent heat storage system comprising at least one latent heat storage device which contains a storage medium with latent heat, at least one heat pump coupled to the latent heat storage device, and at least one extraction circuit which has a first heat carrier medium and with which, during normal operation, in accordance with the intended purpose, heat can be extracted from the storage medium and supplied to the heat pump on the input side, and an extraction heat exchanger in contact with the storage medium, which is connected to the extraction circuit.
It is proposed that, between the extraction heat exchanger and the heat pump, a coupling device is arranged in a connection line, which at least temporarily supplies a second heat carrier medium, which can be heated by at least one heat source, into a section of the connection line to the heat pump.
Preferably, the latent heat storage system can be operated by means of a method as explained below according to an additional aspect of the invention. In the proposed method for operating the latent heat storage system, the latent heat storage system comprises at least one latent heat storage device which contains a storage medium with latent heat, at least one heat pump coupled to the latent heat storage device, and at least one extraction circuit which has a first heat carrier medium and with which, during normal operation, in accordance with the intended purpose, heat can be extracted from the storage medium and supplied to the heat pump on the input side. The at least one latent heat storage device comprises at least one extraction heat exchanger in contact with the storage medium, which is connected to the extraction circuit. At least temporarily, a second heat carrier medium, which is heated by at least one heat source, is supplied into a section of the supply line.
The invention works advantageously in operating states in which the latent heat storage device is strongly or completely thermally unloaded, i.e., the storage medium is largely or in a predetermined region completely solidified, and in which the second heat carrier medium of the at least one heat source is at a higher temperature than the first heat carrier medium of the extraction heat exchanger.
Then, the feed line of the heat pump can be supplied with a heat exchange medium which is at a temperature which is higher than the temperature of the first heat carrier medium at the output of the extraction heat exchanger in the direction of the heat pump. The first heat carrier medium can be mixed with the hotter second heat carrier medium of the at least one heat source and heated in this manner. The feed temperature of the heat pump can thereby at least temporarily be maintained above a critical temperature for the feed line of the heat pump, at which the heat pump otherwise has to be switched off.
Thereby, in spite of a thermally unloaded latent heat storage device, the heat pump can be in operation for a longer time period and supply a consumer with heat.
The latent heat storage device can be, for example, an ice storage device with water as storage medium. In the thermally unloaded, i.e., frozen state, the ice is at a temperature of at most 0° C., or even as low as −10° C. The temperature of the first heat carrier medium is correspondingly low. If the temperature of the first heat carrier medium undershoots a critical temperature for the feed line of the heat pump, for example, 0° C., said heat pump has to be switched off. If the second heat carrier medium is hotter, the feed temperature can be raised by admixing the heat carrier medium or heat transfer of the second heat carrier medium to the first heat carrier medium.
“Heat which can be extracted from the storage medium in accordance with the intended purpose” should be understood to mean that, during normal operation, the extraction heat exchanger extracts heat from the storage medium and cools said storage medium in the process. Preferably, heat can be extracted until the thermal unloading of a region around the extraction heat exchanger. This is the case during normal operation, for example, in winter. From the beginning of the cold season to the end of the cold season, the volume around the extraction heat exchanger solidifies gradually. In the case in which water is used as storage medium, a monolithic ice block forms, preferably in a controlled manner, into which the extraction heat exchanger is embedded. The heat transfer from the storage medium into the heat carrier medium in the extraction heat exchanger occurs via the monolithic ice block. In the extraction circuit, the extraction heat exchanger is preferably connected to the heat pump, which raises the extracted heat to a higher temperature level which can be used by a consumer. A typical heat carrier medium in the extraction circuit can be, for example, a sol or a glycol-water mixture.
According to an advantageous embodiment, the section of the connection line to the heat pump into which the second heat carrier medium is admixed can be arranged between coupling device and heat pump. This enables a targeted metered addition of a volume flow of the second heat carrier medium. In particular, the addition can occur with variable volume flow, in particular with a closed-loop or open-loop controlled volume flow.
According to an advantageous embodiment, at least one regeneration circuit is provided with the second heat carrier medium, with which, during normal operation, in accordance with the intended purpose, heat can be supplied from at least one heat source into the storage medium, wherein the at least one latent heat storage device comprises a regeneration arrangement within the storage medium, wherein the regeneration arrangement is connected to the regeneration circuit. Advantageously, the heat source can be an air-source collector which collects heat from the environmental air, an exhaust air installation, in which heat is absorbed from exhaust air, or another heat source. Optionally, a combination of two or more heat sources can be provided. Advantageously, the second heat carrier medium of the regeneration circuit can be the same as the first heat carrier medium. Thereby, a simple mixing of the heat transfer media via the coupling device is possible.
“Heat which can be supplied into the storage medium in accordance with the intended purpose” should be understood to mean that, during normal operation, the regeneration arrangement releases heat into the storage medium and heats said storage medium in the process. As a result of the heat supply, the thermally unloaded latent heat storage device can be loaded. Preferably, the solidified region around the extraction heat exchanger can be thawed again in the process. This is the case during normal operation, for example, for example, in summer. Preferably, from the beginning of the warm season to the end of the warm season, the solidified volume of the storage medium around the extraction heat exchanger liquefies gradually, preferably in a controlled manner, wherein the extraction heat exchanger embedded therein is gradually exposed again. In the case of water as storage medium, the monolithic ice block is thawed in a controlled manner. The heat transfer from the heated storage medium into the heat carrier medium in the extraction heat exchanger occurs via the melting monolithic ice block. If said ice block is melted and heat continues to be supplied via the regeneration arrangement, the temperature of the storage medium rises correspondingly.
In the extraction circuit, the regeneration arrangement is advantageously connected to one or more heat sources. Preferably, a heat source is an air-source collector which absorbs heat from the environmental air. Optionally, heat sources such as exhaust heat from refrigeration machines, exhaust air from refrigerators and the like can be connected alternatively or additionally at least temporarily. A typical heat carrier medium in the regeneration circuit can be, for example, a sol or a glycol-water mixture. This is preferably the case when the regeneration arrangement is a heat exchanger which is arranged in the storage medium. Alternatively, an “open” regeneration arrangement can be provided, in which the storage medium itself is used as heat carrier medium of the regeneration arrangement and at least partially in the regeneration circuit. The regeneration arrangement then comprises one or more outlets for the heat carrier medium into the storage medium, and one or more inlets for the storage medium into the regeneration circuit. In the regeneration circuit, advantageously, a heat exchanger can be arranged so that, in a region of the regeneration circuit which is connected to the heat source(s), another heat carrier medium, for example, a sol or a glycol-water mixture, can circulate.
As long as solidified storage medium is present in the latent heat storage device, or as long as the storage medium is still cold enough, it is possible to cool via the regeneration circuit. For example, in summer, a residence can be cooled. The cold heat carrier medium in the regeneration circuit can cool, for example, a residential area via a heat exchanger.
The at least one extraction heat exchanger and the at least one regeneration arrangement are preferably adjusted to one another so that a seasonal thawing and solidification of the storage medium can occur in a manageable manner. The extraction circuit and the regeneration circuit are here necessarily hydraulically separated during normal operation.
According to an advantageous embodiment, the coupling device can fluidically connect the regeneration circuit to the heat pump, so that the regeneration arrangement can be bypassed at least partially. Advantageously, a variable setting of the volume flow of the second heat carrier medium, which otherwise flows in the regeneration circuit, can occur in the section of the feed line-side connection line to the heat pump. The volume flow can be set as needed depending on the desired temperature in the feed line of the heat pump and/or the available heat in the heat carrier medium.
According to an advantageous embodiment, the extraction circuit and the regeneration circuit can be temporarily in fluidic contact via connection lines, wherein a first connection line can connect a section of the extraction circuit downstream of a conveyance means to a connection line between regeneration arrangement and heat source of the regeneration circuit, and a second connection line can connect the coupling device to a section of the regeneration circuit upstream of a conveyance means in the regeneration circuit.
Alternatively, a first connection line can connect a section of the extraction circuit upstream of a conveyance means to a connection line between regeneration arrangement and heat source of the regeneration circuit, and a second connection line can connect the coupling device to a section of the regeneration circuit downstream of a conveyance means in the regeneration circuit.
Therefore, at least one of the conveyance means can be arranged in the mixed circuit formed by the sections.
According to an advantageous embodiment, the coupling device can comprise a mixing element that can be closed-loop and/or open-loop controlled. This enables a precise setting and variation of the volume flow of second heat carrier medium, which raises the temperature of the first heat carrier medium of the extraction beat exchanger.
According to an advantageous embodiment, in the latent heat storage system, a closed-loop and/or open-loop control device can be provided, which can actuate the coupling device depending on at least one operating parameter of the latent heat storage device and/or of the latent heat storage system. A precise setting of the mixing temperature in the section of the connection line to the heat pump of the second heat carrier medium depending on one or more operating parameters of the latent beat storage system and/or of the heat pump is possible.
According to an advantageous embodiment, the at least one regeneration circuit can comprise an air-source collector as heat source. Herewith, advantageous benefits can be drawn from elevated environmental temperatures.
According to an advantageous embodiment, the regeneration arrangement can comprise a heat exchanger arranged in the storage medium. Advantageously, as heat carrier medium, in the extraction heat exchanger and in the heat exchanger of the regeneration arrangement, the same medium can be used as heat carrier medium which is easy to mix via the coupling device.
According to an advantageous embodiment, the regeneration arrangement can comprise one or more inflows or outflows in the latent heat storage device, and the storage medium circulates at least in a part of the regeneration circuit. The second heat carrier medium can be coupled indirectly via a heat exchanger to the first heat carrier medium. In this case, the regeneration arrangement is designed as an “open” system and comprises inflows and outflows in the latent heat storage device. For example, the inflows and outflows can be formed by annular lines which comprise, along their circumference, openings for the passage of the storage medium. Through the heat exchanger in the regeneration circuit, in the region of the regeneration circuit connected to the heat source(s), another heat carrier medium, for example, a sol or a glycol-water mixture, can circulate.
According to an additional aspect of the invention, a method for operating a latent heat storage system according to the invention is proposed, wherein the latent heat storage system comprises at least one latent heat storage device which contains a storage medium with latent heat, at least one heat pump coupled to the latent heat storage device, and at least one extraction circuit with a first heat carrier medium, with which, during normal operation, in accordance with the intended purpose, heat is extracted from the storage medium and supplied to the heat pump on the input side, wherein the at least one latent heat storage device comprises at least one extraction heat exchanger in contact with the storage medium, which is connected to the extraction circuit. At least temporarily, a second heat exchange medium, which is heated by at least one heat source, is supplied into a section of the supply line.
The invention works advantageously in operating states in which the latent heat storage device is strongly or completely thermally unloaded, i.e., the storage medium is largely or in a predetermined region completely solidified, and in which the second heat carrier medium of the at least one heat source is at a higher temperature than the first heat carrier medium of the extraction heat exchanger.
Then, the feed line of the heat pump can be supplied with a heat carrier medium at a temperature which is higher than the temperature of the first heat carrier medium at the output of the extraction heat exchanger in the direction of the heat pump. The first heat carrier medium can be mixed with hotter second heat carrier medium of the at least one heat source and heated accordingly. The feed temperature of the heat pump can thereby be maintained at least temporarily above a critical temperature for the feed line of the heat pump, at which the heat pump otherwise has to be switched off. Thereby, in spite of a thermally unloaded latent heat storage device, the heat pump can be in operation for a longer time period and supply a consumer with heat.
According to an advantageous embodiment, via a regeneration circuit with the second heat carrier medium, during normal operation, in accordance with the intended purpose, heat from at least one heat source can be supplied into the storage medium, wherein the at least one latent heat storage device comprises a regeneration arrangement within the storage medium, which is connected to the regeneration circuit. Advantageously, the heat source can be an air-source collector, an exhaust air installation or another heat source. Optionally, a combination of two or more heat sources can be provided. Advantageously, the heat carrier medium of the regeneration circuit can be the same as the first heat carrier medium. Thereby, a simple mixing of the heat carrier media via the coupling device is possible.
According to an advantageous embodiment, the heat carrier medium can be supplied with a variable volume flow; in particular, the volume flow of the second heat carrier medium can be set depending on a feed temperature of the heat pump. In the case of a thermally unloaded or nearly unloaded latent heat storage device, the feed temperature of the heat pump can thus also be varied over wide ranges, in particular raised. On warm winter days, a benefit can be drawn from elevated air temperatures, and the heat pump can be continued to be operated, in spite of the fact that, for example, the temperature of the first heat carrier medium in the extraction heat exchanger would be too low for the heat pump and said heat pump would have to be switched off. The latent heat storage system can therefore be operated in an energetically advantageous manner for a longer time period in the cold season.
According to an advantageous embodiment, the second heat carrier medium can be supplied when a predetermined icing degree of the latent heat storage device with respect to a volume capable of freezing in accordance with the intended purpose is reached, preferably starting from an icing degree of at least 90% with respect to a volume of the latent heat storage device, capable of freezing in accordance with the intended purpose.
The term “volume capable of freezing” should be understood to mean that it is the volume in which solidified storage medium is present, which can be water ice. However, in principle, another storage medium with latent heat can also be provided.
Advantageously, it is provided that the maximum volume capable of freezing is smaller than the holding capacity of the latent heat storage device. Preferably, the volume capable of freezing is also surrounded at maximum icing degree by liquid storage medium. The size of the maximum volume capable of freezing can be predetermined primarily by the design of the extraction heat exchanger. The latent heat storage device can be designed so that, under normal conditions, the maximum volume capable of freezing can always be surrounded by liquid storage medium.
According to an advantageous embodiment, the second heat carrier medium can be supplied when a temperature of the first heat carrier medium of the extraction circuit is less than or equal to 1° C., preferably less than or equal to 0° C., and the second heat carrier medium of the at least one heat source is hotter than the first heat carrier medium in the extraction heat exchanger. Thereby, an advantageous feed temperature of the heat pump can be set and said heat pump can also be operated for a longer time period with thermally unloaded latent heat storage device.
Additional advantages result from the following description of the drawing. In the drawings, embodiment examples of the invention are represented. The drawings, the description and the claims contain numerous features in combination. Advantageously, the person skilled in the art will also consider the features individually and combine them into appropriate additional combinations.
In the drawings, in an exemplary manner:
In the figures, identical or equivalent components are numbered with identical reference numerals. The figures merely show examples and are understood to be non-limiting.
Direction terminology used below with terms such as “left,” “right,” “top,” “bottom,” “in front of,” “behind,” “after,” and the like are only used to improve the understanding of the figures and are never intended to represent a limitation of the generality. The represented components and elements as well as their design and use can vary depending on the considerations of a person skilled in the an and can be adapted to the respective applications.
During normal operation, no fluid connection between extraction circuit 30 and regeneration circuit 40 is provided.
The latent heat storage device 10 comprises an extraction heat exchanger 32 in contact with the storage medium 20, in particular immersed therein, which is arranged in the extraction circuit 30, and a regeneration arrangement 42 within the storage medium 20, which is arranged in the regeneration circuit 40. The latent heat storage device 10 comprises a surrounding wall 12, for example, a housing, which is preferably provided or arranged in the ground and which is filled with the storage medium 20. Optionally, the storage medium 20 can also be provided directly in the ground, for example, as a pond installation or cavern. A region 14 of the ground which acts thermally on the latent heat storage device 10 by heat supply or heat absorption is indicated with a double dashed line. The latent heat storage device 10 itself can here act as a geothermal probe.
In the extraction circuit 30, the extraction heat exchanger 32 is connected via lines 112, 114 to a heat pump 104. The heat pump 104 raises the temperature level of the heat carrier medium 34 and supplies a consumer 130 with heat at a correspondingly higher level.
The heat carrier medium 34 is circulated in the extraction circuit 30 with a feed pump 106. By means of a circuit not designated in further detail, the heat pump 104 supplies the consumer 130, for example, a building, a residence or the like, with heat and conveys a corresponding heat carrier medium with a conveyance means 110, for example, a feed pump.
In the regeneration circuit 40, the regeneration arrangement 42 is connected via lines 116, 118 to a heat source 102. For example, the regeneration arrangement 42 is provided in the form of a regeneration heat exchanger 46 which is connected, for example, to an air-source collector as heat source 102, which absorbs heat of the environmental air. The heat carrier medium 44 in the regeneration circuit 40 is circulated with a feed pump 108. Alternatively or additionally, other heat sources can also be provided, for example, exhaust air devices and the like.
In the regeneration arrangement 42 with the regeneration heat exchanger 46, the heat carrier medium 44 circulates, which preferably corresponds to the heat carrier medium 34 from the extraction circuit 30, for example, a sol or a water-glycol mixture.
During normal operation, the extraction heat exchanger 32 extracts heat from the storage medium 20 and cools said storage medium in the process. Preferably, heat can be extracted until the thermal unloading of a predetermined region 36 around the extraction heat exchanger 32. This is the case during normal operation, for example, during the winter. From the beginning of the cold season to the end of the cold season, the volume 36 here solidifies gradually around heat exchange pipes of the extraction heat exchanger 32. When water is used as storage medium 20, a monolithic ice block forms in a controlled manner, which, in the completely unloaded state of the storage medium 20, maximally assumes the volume 36 in which the extraction heat exchanger 32 is embedded. The maximum volume 36 results substantially from the design of the extraction heat exchanger 32.
The heat transfer from the storage medium 20 into the heat carrier medium 34 in the extraction heat exchanger 32 occurs via the monolithic ice block. In the extraction circuit 20, the extraction heat exchanger 32 is connected to the heat pump 104, which raises the extracted heat to a higher temperature level which can be used by the consumer 130. A typical heat carrier medium 20 in the extraction circuit 30 can be, for example, a sol or a glycol-water mixture.
During normal operation, the regeneration arrangement 42 releases heat into the storage medium 20 and in the process it heats said storage medium. Due to the heat supply, the thermally unloaded latent heat storage device 10 can be thermally loaded and/or the unloading of the latent heat storage device 10 can be delayed. Preferably, during the thermal loading of the latent heat storage device 10, storage medium 20 which has solidified around the extraction heat exchanger 32 is thawed again. This is the case during normal operation, for example, during the summer. Preferably, from the beginning of the warm season to the end of the warm season, the solidified storage medium 20 on the extraction heat exchanger 32 gradually in a controlled manner liquefies again due to the heat supply, wherein the extraction heat exchanger 32 embedded therein is exposed again. In the case in which water is used as storage medium 20, the monolithic ice block is thawed in a controlled manner. The heat contribution of the heated storage medium 20 into the heat carrier medium 34 in the extraction heat exchanger 32 occurs via the melting monolithic ice block. If, after completed melting of the ice block, additional heat is supplied via the regeneration arrangement 42 into the latent heat storage device 10, the temperature of the storage medium 20 rises correspondingly.
Extraction circuit 30 and regeneration circuit 40 are strictly separated hydraulically during normal operation due to their different functions.
Due to the limited heat transfer between the heat exchanger pipes of the extraction heat exchanger 32, in the case of strongly frozen storage medium 20, the heat carrier medium 34 in the extraction heat exchanger 32 is rapidly supercooled and then supplies an insufficient feed temperature on the heat pump 104. According to the invention, a coupling device 50 is arranged in the connection line 112 from the extraction heat exchanger 32 to the heat pump 104, which at least temporarily supplies heat carrier medium 44 of the regeneration circuit 40, which can be heated by at least one heat source 102, into a section 113 of the connection line 112, which is provided downstream of the coupling device 50.
The coupling device 50 establishes a fluid connection between the regeneration circuit 40 and the heat pump 104, so that the regeneration arrangement 42 is at least partially bypassed.
Extraction circuit 30 and regeneration circuit 40 are in fluidic connection via two connection lines 66, 68. The first connection line 66 connects a section 115 of the extraction circuit 30 downstream of the feed pump 106 to a section 117 of the connection line 116 between regeneration arrangement 42 and heat source 102 of the regeneration circuit 40. The second connection line 68 connects the coupling device 50 to a section 119 of the connection line 118 of the regeneration circuit 40 upstream of the feed pump 108 in the regeneration circuit 40.
Thereby, a circuit 48 is formed, in which the heat carrier medium circulates in sections 113, 115 of the connection lines 112, 114 of the extraction circuit 30, in the connection lines 66, 68 and sections 117, 119 of the lines 116, 118 of the regeneration circuit 40, in the heat pump 104 and in the heat source 102. Advantageously, the feed pump 108 in the regeneration circuit 40 can be stopped when the coupling device 50 admixes a volume flow of the second heat carrier medium 44 into the first heat carrier medium 34.
The coupling device 50 is preferably designed as a mixing element 52 that can be closed-loop or open-loop controlled, so that the second heat carrier medium 44 from the regeneration circuit 40 can be admixed with variable volume flow.
A closed-loop and/or open-loop control device 60 is provided, which actuates the coupling device 50 depending on at least one operating parameter of the latent heat storage device 10 and/or of the latent heat storage system 100. In particular, the at least one operating parameter can be an icing degree of the latent heat storage device and/or a temperature of the first heat carrier medium.
The closed-loop and/or open-loop control device 60 can advantageously be in connection with various additional components and sensors of the latent heat storage system 100, for example, with the conveyance means 106, 108, temperature sensors which are not represented, which are associated with the heat pump 104 and the heat source 102, and the like, which is indicated with dashed double arrows in the closed-loop and/or open-loop control device 60.
In the embodiment example in the figure, the regeneration arrangement 42 of the regeneration circuit 40 is designed as an “open” system and, instead of a heat exchanger 46 (
The regeneration circuit 40 comprises two sections 43, 45, a section 43 close to the heat source and a section 45 close to the latent heat storage device, which are separated by a heat exchanger 82. In the section 45, a conveyance means 120, for example, a pump, conveys the heat carrier medium 20 which, in this region forms the heat carrier medium of the regeneration circuit 40; in section 43, the conveyance means 108 conveys the second heat carrier medium 44 of the regeneration circuit 40. In the section 45, the storage medium 20 circulates as second heat carrier medium 44; in the section 43, preferably the same medium as in the extraction circuit 30 circulates as second heat carrier medium 44.
For example, the inflows 47 and outflows 49 can be formed by annular lines in the non-icing region of the latent heat storage device 10, which comprise, along their circumference, openings for the passage of the storage medium 20 which represents the heat carrier medium 44 of the section 45.
The heat exchanger 82 also represents a separation of the circuits into the section 45 of the open regeneration arrangement 42 and the circuit 48 with lines 113, 115, 106, 66, 117, 119, 66.
If the beat exchange medium 44 from the section 43 of the regeneration circuit 40 is admixed via the coupling device 50 into the feed line to the heat pump 104, the conveyance means 120 can be shut down in the section 45 of the regeneration circuit 40 close to the latent heat storage device.
The method for operating the latent heat storage system 100 provides that a second heat carrier medium 44 which is heated by at least one heat source 102 is supplied at least temporarily into a section 113, arranged downstream of a coupling device 50, of a connection line 112 to a heat pump 108 in the extraction circuit 30 with a first heat carrier medium 32, and in particular is admixed with the first heat carrier medium 32. This can advantageously occur with variable volume flow of the second heat carrier medium 44, in particular, the volume flow of the second heat carrier medium 44 can be set independently of a feed temperature of the heat pump 104.
The second heat carrier medium 44 is preferably supplied when a predetermined icing degree of the latent heat storage device 10 with respect to a volume 36 capable of freezing in accordance with the intended purpose has been reached, preferably starting from an icing degree of at least 90% with respect to a volume 36 of the latent heat storage device 10, capable of freezing in accordance with the intended purpose.
In particular, the second heat carrier medium 44 can be supplied when a temperature of the first heat carrier medium 34 of the extraction circuit 30 is less than or equal to 1° C., preferably less than or equal to 0° C., and the second heat carrier medium 44 of the at least one heat source 102 is hotter than the first heat carrier medium 32.
In S100, on the open-loop and/or closed-loop control unit 60 of the latent heat storage system 100, a demand for heating a consumer 130 is present. The latent heat storage device 10 is almost unloaded, and the temperature of the heat carrier medium 34 in the extraction circuit 30 is low, for example, close to 0° C. In S102, ACTUAL values are compared between the heat source 102 and the latent heat storage device 10. The heat source 102 can be a roof collector. Additionally or alternatively, other heat sources can optionally be coupled to the regeneration circuit 40.
In S104, the heat pump 104 is supplied with the heat carrier medium 32, 44 of the hotter of the two energy sources, latent heat storage device 10 and heat source 102. If, during operation, the temperature of the heat carrier medium 34 or 44 in question remains higher than the temperature of the other heat carrier medium 44 or 34, in S106, the heating process with this source is continued as long as this temperature is higher than the other temperature. The heat pump 104 thus receives the highest possible feed temperature of the latent heat storage system 100.
However, if the temperature of the heat carrier medium 34 or 44 in question drops below the temperature of the other so far colder heat carrier medium 44 or 34, in S108, the volume flows from heat source 102 and extraction heat exchanger 32 are mixed by means of the coupling device 50, until, in the latent heat storage system 100, the highest possible temperature of the mixture of the heat transfer media 34, 44 is reached. The system can also switch from S106 into this path when the temperature of the hotter heat carrier medium 34 or 44 drops too much.
| Number | Date | Country | Kind |
|---|---|---|---|
| 102017112407.1 | Jun 2017 | DE | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/EP2018/064693 | 6/5/2018 | WO | 00 |
