EP4146916A1 - Thermal energy storage system - Google Patents
Thermal energy storage systemInfo
- Publication number
- EP4146916A1 EP4146916A1 EP21739574.8A EP21739574A EP4146916A1 EP 4146916 A1 EP4146916 A1 EP 4146916A1 EP 21739574 A EP21739574 A EP 21739574A EP 4146916 A1 EP4146916 A1 EP 4146916A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- energy storage
- heat
- thermal energy
- transfer medium
- heat transfer
- 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.)
- Withdrawn
Links
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- 238000003860 storage Methods 0.000 claims description 38
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- 238000005338 heat storage Methods 0.000 claims description 29
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Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
- F01K3/00—Plants characterised by the use of steam or heat accumulators, or intermediate steam heaters, therein
- F01K3/18—Plants characterised by the use of steam or heat accumulators, or intermediate steam heaters, therein having heaters
Definitions
- the present invention relates to a thermal energy storage system and a method for operating such a thermal energy storage system.
- Thermal energy storage systems with an energy storage device are well known in the prior art. These systems are used for storing thermal energy in an energy storage device (charging mode) by transferring thermal energy from a heat source to the energy storage device with a heat transfer medium. During discharging, these systems transfer thermal energy stored in the energy storage device to a heat consumer by means of a heat transfer medium.
- Common energy storage devices used in these thermal energy storage systems include a first and a second port coupled to a storage chamber and a heat storage material. Possible energy storage devices for the thermal energy storage systems are for example described in detail in the document EP 3102 796 A1.
- thermal energy storage system is limited because the energy storage device within the energy storage system can only be operated efficiently at high temperatures, for example between 700 and 900° C. Consequently, the heat transfer medium flowing through the energy storage device is also heated up to such a high temperature.
- the heat transfer medium at such high temperature is then used for specific applications, for example for generating high temperature and high pressure steam (e.g. 565°C at 180 bar) for a steam turbine which is used to reconvert the stored thermal energy to electrical energy.
- high temperature and high pressure steam e.g. 565°C at 180 bar
- the document US 4,094,148 A is related to the generation of electrical power using coal as source of energy, wherein heat released by exhaust gases is stored and is utilized at peak demand periods to generate increased electrical power.
- a thermal energy storage system comprises an energy storage device configured to store thermal energy and a charging flow path configured to provide thermal energy from a heat source to the energy storage device via a heat transfer medium.
- the thermal energy storage system is operable in a charging mode in which the heat transfer medium is transported along the charging flow path.
- the thermal energy storage system further includes a discharging flow path configured to provide thermal energy from the energy storage device to a first heat consumer via the heat transfer medium, and configured to return the heat transfer medium at least partially to the energy storage device.
- the thermal energy storage system is operable in a discharging mode in which the heat transfer medium is transported along the discharging flow path.
- the charging and discharging flow paths are configured such that the heat transfer medium is at least partly transported along same passage through the energy storage device.
- the thermal energy storage system further includes a second heat consumer arranged in the charging flow path and in the discharging flow path such that the heat transfer medium passes through the second heat consumer both during operation in the charging mode and during operation in the discharging mode.
- the discharging flow path is configured to, at least partially, bypass the heat source.
- the thermal energy storage system As the heat transfer medium that is flowing through the second heat consumer has either passed the energy storage device (charging mode) or the first heat consumer (discharging mode), considerable amounts of thermal energy have already been withdrawn from the heat transfer medium, so that the temperature of the medium is significantly lower compared to medium directly leaving the heater or from the storage device. Furthermore, heat transfer medium that still includes a considerable amount of residual thermal energy flows through the second heat consumer both in the charging mode and the discharging mode. The second heat consumer thus continuously receives a substantial amount of thermal energy. With the thermal energy storage system, it therefore becomes possible to supply a plurality of different applications with heat that require only lower temperatures and/or that require a constant heat supply. Examples are district heating, feedwater heaters for steam turbines and the like. The versatility of the system is thus significantly improved.
- the temperature of the heat transfer medium received by the second heat consumer does also not fall below a threshold temperature (e.g. 150°C or 200° C) during charging as well as during discharging mode, so that sufficient heat can continuously be provided to the second heat consumer.
- a threshold temperature e.g. 150°C or 200° C
- the location of the second heat consumer in the discharging flow path has also the advantage that the temperature of the heat transfer medium entering the energy storage device during the discharging mode is further reduced by the heat transfer in the second heat consumer. This leads to a higher temperature difference between the heat transfer medium entering the energy storage device during discharging and the temperature of the heat storage material. Thus, a 'deeper' discharge is possible and thus more thermal energy can be extracted from the energy storage device. A higher amount of extractable energy may thus be stored, or the energy storage device can be built smaller for storing the same amount of extractable energy.
- the charging flow path is preferably configured to at least partially return the heat transfer medium to the heat source.
- the discharging flow path is configured to, at least partially, bypass the heat source.
- the discharging flow path is configured to bypass the heat source. In case of the latter configuration, the heat source is completely bypassed.
- 'energy storage device' means a system that is configured to store thermal energy. Thereby, the energy storage device is not restricted to a single energy storage chamber.
- the energy storage device may comprise 1, 2, 3 or more energy storage chambers which are connected parallel or in series.
- the charging flow path and the discharging flow path may be provided by any kind of e. g. pipes or conduits, in particular thermally insulated pipes, which are used in the thermal energy storage system for routing the heat transfer medium through the charging and discharging flow paths.
- the 'charging mode' corresponds to a mode in which the heat transfer medium passes along the charging flow path and the 'discharging mode' corresponds to a mode in which the heat transfer medium passes along the discharging flow path.
- the first heat consumer may be a steam generator (in particular a heat recovery steam generator, HRSG) that generates steam during the discharging mode, in particular steam that is suitable for powering a steam turbine configured to convert stored thermal energy into electrical energy.
- HRSG heat recovery steam generator
- the steam generator may also be termed main steam generator and may be configured to generate steam having a temperature of higher than 400°C at a pressure of more than 100 bar.
- the first heat consumer may only be operable during the discharging mode.
- the heat transfer medium is a gaseous medium, in particular air or nitrogen.
- Air is cost efficient and readily available, and the medium may thus be replenished from the environment. Also, sealing of the storage device and of the flow paths is not a major concern when using air.
- the charging flow path may implement a closed cycle that is configured to return the heat transfer medium leaving the energy storage device, via the second heat consumer, back to the heat source in order to increase the amount of thermal energy stored in the heat transfer medium.
- the heat transfer medium is cycled in the charging flow path through the heat source and the energy storage device for continuously transferring thermal energy to the energy storage device.
- Such closed cycle is more energy efficient.
- the discharging flow path may implement a closed cycle that is configured to return the heat transfer medium that has provided thermal energy to the first and second heat consumer back to the energy storage device to take up thermal energy stored in the energy storage device.
- the heat transfer medium is cycled in the discharging flow path through the energy storage device, the first and the second heat consumer.
- the thermal energy storage system comprises a conduit that provides a flow coupling between the energy storage device and the second heat consumer.
- the thermal energy storage system is configured such that in the charging mode, heat transfer medium leaving the energy storage device is passed by the conduit to the second heat consumer and in the discharging mode, heat transfer medium leaving the second heat consumer is passed by the conduit to the energy storage device.
- the conduit may be any kind of pipe or conduit, in particular an insulated pipe, for routing the heat transfer medium in the charging and discharging mode.
- the second heat consumer may thus be connected at a position in the system at which it receives the heat transfer medium directly from the energy storage device in the charging mode, and at which the flow through the second heat consumer corresponds to the flow through the energy storage device. Such position may be favorable with respect to the temperature of the medium flowing through the second heat consumer in both modes.
- the flow coupling is preferably a flow connection, in particular a direct flow connection.
- a port of the second heat consumer through which the heat transfer medium leaves the second heat consumer is fluidically coupled to a port of the storage device through which the medium enters the storage device.
- the coupling may be a direct or indirect connection, a blower may for example be arranged as an intervening element in the coupling.
- the coupling may in particular bypass the heat source.
- the thermal energy storage system may be configured to supply in the discharging mode the heat transfer medium at a temperature between 500 and 1000°C to the first heat consumer.
- the heat transfer medium may have a temperature between 500 and 1000°C or 600 and 900°C, preferably between 600 and 800°C when leaving the energy storage device.
- the thermal energy storage system supplies in the discharging mode the heat transfer medium at a temperature of 500°C to 900°C (e.g. 700°C to 800°C) to the first heat consumer.
- the thermal energy storage system may be configured to supply in the charging mode and in the discharging mode the heat transfer medium at a temperature between 100 and 400°C to the second heat consumer.
- the heat transfer medium at the second heat consumer may have the same or substantially the same temperature in the charging and discharging mode.
- the heat transfer medium supplied to the second heat consumer may in particular have a temperature between 150 and 350°C, or 200 and 350°C.
- the second heat consumer is a steam generator configured to transfer the thermal energy of the heat transfer medium to a working medium of a steam cycle (water/steam).
- the second heat consumer may be configured to generate steam for the steam cycle.
- the second consumer may be a heat exchanger or steam boiler.
- the second heat consumer may be a heat exchanger configured to transfer thermal energy of the heat transfer medium to water of a water cycle, in particular to generate hot (heated) water in the water cycle, or to a thermal oil of a thermal oil cycle.
- the first heat consumer powers a first steam cycle (or first water cycle) and the second heat consumer powers a second steam cycle (or second water cycle) which is separate from the first steam cycle (or the first water cycle, if the medium is water).
- first steam cycle or first water cycle
- second steam cycle or second water cycle
- a nominal pressure level of the first steam cycle may be different to a nominal pressure level of the second steam cycle (or second water cycle) at the respective heat consumer.
- a pressure level of the first steam cycle may be higher or equal to a pressure level of the second steam cycle (or second water cycle) at the respective heat consumer.
- the first heat consumer and the second heat consumer may not part of the same consumer.
- the first heat consumer and the second heat consumer may be positioned upstream of the blower.
- the second heat consumer may thus generate steam/hot water having a 'lower quality' than steam generated by the first heat consumer.
- the generated steam or hot water may have a (low) temperature between 120°C and 190°C and a (low) pressure between 5 and 20 bar, e.g. about 10 bar.
- the thermal energy storage system is configured to provide a continuous heat supply to the second heat consumer via the heat transfer medium when operating the thermal energy storage system alternatingly in the charging mode and the discharging mode.
- the continuous heat supply leads to greater application possibilities because there are some heat consumers, e.g. district heating that require a permanent heat supply.
- the thermal energy storage system may further comprise at least one blower configured to convey (i.e. to transport) the heat transfer medium along the charging flow path in the charging mode and to convey the heat transfer medium along the discharging flow path in the discharging mode.
- at least one blower configured to convey (i.e. to transport) the heat transfer medium along the charging flow path in the charging mode and to convey the heat transfer medium along the discharging flow path in the discharging mode.
- the heat transfer medium is, in particular, circulated from the blower through the heat source, the energy storage device, the second heat consumer and back to the blower.
- the heat transfer medium provides thermal energy to the energy storage device and to the second heat consumer.
- the heat transfer medium is circulated from the blower through the second heat consumer, the energy storage device, the first heat consumer and back to the blower.
- thermal energy is transferred from the energy storage device to the heat transfer medium and the heat transfer medium may provide heat to the first and second heat consumers.
- the output of the at least one blower may have the same flow direction in the charging and discharging mode.
- At least one control valve may be provided downstream of the at least one blower to separate the flow paths into the charging and the discharging flow paths. Further control valves, e. g. three way valves or on/off valves, may be provided upstream of the at least one blower.
- the thermal energy storage system may include a control unit configured to control the control valves such that in charging mode, the heat transfer medium flows along the charging flow path and in discharging mode, the heat transfer medium flows along the discharging flow path.
- At least one blower may be used for the charging flow path and at least one blower for the discharging flow path.
- Further blowers may be provided, e.g. for redundancy, for boosting or if the pressure drop is too large along the charging/discharging flow path.
- the at least one blower is arranged in the charging flow path downstream of the second heat consumer and upstream of the heat source with regard to the flow direction in the charging flow path, and is arranged in the discharging flow path downstream of the first heat consumer and upstream of the second heat consumer with regard to the flow direction in the discharging flow path.
- the same blower may be used for transporting the medium in the charging and discharging flow paths. This is efficient and reduces costs for further blowers.
- the charging flow path is configured to guide the heat transfer medium through the energy storage de vice in a first flow direction to increase the amount of thermal energy stored in the energy storage device and the discharging flow path is configured to guide the heat trans fer medium through the energy storage device in a second flow direction that is opposite to the first flow direction.
- the second heat consumer is arranged in the charging flow path downstream of the energy storage device and upstream of the heat source with regard to the first flow direction and is arranged in the discharging flow path downstream of the first heat consumer and upstream of the energy storage device with regard to the second flow direction.
- 'Downstream' means 'in flow direction behind'.
- 'downstream' of the energy storage device means that the heat transfer medium first passes the energy storage device and then the second heat consumer and 'upstream' of the heat source means that the heat transfer medium passes the second heat consumer prior to being returned to the heat source.
- 'downstream' of the first heat consumer means that the heat transfer medium first passes the first heat consumer and then the second heat consumer and 'upstream' of the energy storage device means that the heat transfer medium passes the second heat consumer prior to being returned to the energy storage device.
- the energy storage device comprises a stor age chamber.
- the storage chamber may comprise at least one first port operated as an inlet for the heat transfer medium in the charging mode and as an outlet for the heat transfer medium in the discharging mode and at least one second port operated as an outlet for the heat transfer medium in the charging mode and as an inlet for the heat transfer medium in the discharging mode.
- the energy storage device may further comprise a heat storage material disposed in the storage chamber.
- the heat storage material may have open pores and/or may provide flow channels through which the heat transfer me dium may flow and exchange thermal energy with the heat stor age material.
- the thermal energy storage system may be configured to store thermal energy in the energy storage device at a temperature between 300 °C and 1000 °C, preferably between 500 °C and 1000 °C, more preferably between 600°C and 900°C when the thermal energy storage device is in a charged state.
- the temperature in the charged energy storage device may be kept between 650 and 800°C.
- Flow channels can be built into the heat storage material, or such channels may form due to the structure of the material, e.g. by interspaces or gaps in the heat storage material, e.g. between rocks/stones.
- the heat storage material comprises a mesh of heat ex change channels through which the heat transfer medium pass es, both along the charging and the discharging flow path.
- the heat storage material may comprise or con sist of rocks, bricks, stone, lava stone, granite, basalt and/or ceramics provided as bulk material (which may be con figured as pebble bed).
- the heat storage material comprises or consists of sand and/or stones, in particular gravel, rubble and/or grit.
- the stones can be natural stones or artificial stones (e.g. containers filled with material, such as clinkers or ceramics). The heat storage device can thus be provided cost efficiently while being capable of storing large amounts of thermal energy.
- the energy storage device may be a horizontal storage device wherein a main flow direction of the heat transfer medium through the storage device is in horizontal direction (i.e. substantially parallel to the earth's surface).
- a horizontally oriented direction of the heat exchange flow may be achieved by providing the first and second ports laterally, e.g. in side walls/boundaries of the storage chamber.
- the energy storage device may be a vertical storage device wherein a main flow direction of the heat transfer medium through the storage device is in vertical direction (i.e. substantially perpendicular to the earth's surface).
- the inlet/outlet ports may then be provided in upper/lower walls/boundaries of the storage chamber, or one port may be provided in an upper part and the other in a lower part of side walls/boundaries of the storage chamber.
- the energy storage device may com prise a diffuser section for evenly distributing the heat transfer medium into the storage and for reducing the flow speed of the medium.
- the diffuser may be provided at either port of the energy storage device.
- the diffuser may comprise a convection reducing structure, for example by providing a vertical layer of convection reducing elements within the diffuser of the respective port.
- the storage chamber may be a space, a cavity, an excavation or a housing in which the heat storage material is located.
- the energy storage device may further comprise a nozzle sec tion provided between the storage chamber and the respective port.
- the nozzle section may for example include a tapered portion leading from the storage chamber to the respective port. Flow speed and pressure of the heat transfer medium en tering/leaving the energy storage device through the respec tive port may be adjusted by providing such nozzle section.
- the thermal energy storage system is con figured to alternatingly operate in the charging mode and the discharging mode. Accordingly, the system may cause alternat ing flows in opposite direction or in the same direction through the energy storage device to charge/discharge the en ergy storage device.
- the charging mode heat transfer medium that has been heated by the heat source passing through the energy storage device and thereby heats the heat storage material, a cooler medium being exhausted from the energy storage device.
- the storage device may be left in a standstill period of hours or even days until the stored thermal energy is needed.
- the flow direction may be the same as in the charging mode or may be reversed, so that colder heat transfer medium (e.g.
- the energy storage device may include a plurality of hot ports and/or a plurality of cold ports.
- the heat storage material may be separated into a layered thermal energy storage structure by dividing elements, such as steel plates or metal sheets.
- the sheets or plates may comprise any suitable heat resistant material, such as metal, synthetic fabric or the like, that are substantially imperme able for the working fluid.
- the dividing elements may prevent a change in the temperature distribution within the thermal energy storage structure due to natural convection during the standstill period, i.e. prevent that hot fluid surrounding heat storage material in the lower part of the chamber flows to the upper part of the chamber.
- the energy storage device may include several storage chambers placed in series and/or parallel with valves and piping in between, including bypass-lines. This may allow an adaptation of the size of the active stor age chamber to the present needs. For example, during charg ing, the flow of the heat transfer medium and thus the heat- ing may be stopped for one chamber if the specific chamber has been fully charged. This allows the maintaining of a de sired temperature gradient within each of the storage cham bers.
- the thermal energy storage system may be con figured such that during the charging cycle of a storage chamber, a temperature front travels through the heat storage material from the hot end to the cold end of the chamber.
- the temperature front is a zone of strong temperature gradient in the heat storage material, which separates the hot and the cold zones in the chamber.
- the charging of the respective storage chamber will preferably be stopped when the tempera ture at the cold end begins to rise above a predetermined temperature threshold.
- the heat source is configured to receive energy from a renewable energy source, in particular from a wind and/or solar and/or water energy source.
- a renewable energy source in particular from a wind and/or solar and/or water energy source.
- the use of renewable energy sources is environmentally friendly.
- the heat source may also be provided with energy from nonrenewable energy sources like coal, oil, nuclear and/or natural gas.
- the heat source may for example comprise a heater, in particular an electrical heater that converts electrical energy into thermal energy. It may additionally or alternatively comprise a heat exchanger that for example provides heat exchange between a working fluid (e.g. of a solar plant, of an industrial process, or the like, such as an exhaust gas or waste heat) and the heat transfer medium.
- the heat source may additionally or alternatively comprise a heat pump.
- the second heat consumer may implement at least one of a feedwater heater configured to heat feedwater of a steam turbine, a district heating system heater configured to heat a medium of a district heating system, or a steam turbine standby heater configured to supply steam to a steam turbine to maintain the steam turbine or components of the steam turbine at a predetermined temperature.
- a feedwater heater configured to heat feedwater of a steam turbine
- a district heating system heater configured to heat a medium of a district heating system
- a steam turbine standby heater configured to supply steam to a steam turbine to maintain the steam turbine or components of the steam turbine at a predetermined temperature.
- the second heat consumer is implemented as a feedwater heater of a steam turbine, it is not necessary to extract steam from an intermediate stage of the steam turbine of the steam cycle for feedwater heating. Therefore, the steam that is conventionally extracted from the steam turbine to be used in the feedwater heater can be transformed to work by expansion in the steam turbine and thus, the efficiency of the system is increased.
- the second heat consumer may also be implemented as one, two or more heat exchangers, which may for example directly heat feedwater, e.g. it may be implemented as an LP feedwater heater and an HP feedwater heater providing respective LP/HP feedwater heating.
- the steam or hot water generated in the district heating system heater may be distributed through a system of insulated pipes and may be provided for residential and commercial heating requirements, such as space heating or water heating.
- the second heat consumer as a steam turbine standby heater
- components of the main steam cycle can be maintained at a predetermined temperature, which reduces the ramp-up time of the main steam cycle.
- the efficiency of the steam turbine can be increased.
- the thermal energy storage system may comprise a respective steam turbine, and the steam turbine may be provided with steam for operation from the first heat consumer.
- the steam turbine may further be configured to drive an electrical generator to convert stored thermal energy into electrical energy.
- a further embodiment of the invention provides a method of operating a thermal energy storage system.
- the method comprises operating the thermal energy storage system in a charging mode in which a heat transfer medium is transported along a charging flow path from a heat source to an energy storage device to thereby provide thermal energy from the heat source to the energy storage device; and operating the thermal energy storage system in a discharging mode in which the heat transfer medium is transported along a discharging flow path from the energy storage device to a first heat consumer to thereby provide thermal energy from the energy storage device to the first heat consumer.
- the heat transfer medium is at least partly transported along same passage through the energy storage device.
- the method further comprises providing thermal energy from the heat transfer medium to a second heat consumer that is arranged in the charging flow path and in the discharging flow path such that the heat transfer medium passes through the second heat consumer both during operation in the charging mode and during operation in the discharging mode.
- Fig. 1 is a schematic drawing showing a thermal energy storage system according to an embodiment of the invention.
- Fig. 2 is a schematic drawing showing a thermal energy storage system according to an embodiment of the invention.
- Fig. 3 is a schematic drawing showing a steam turbine in cluding a feedwater heater supplied with thermal energy by the second heat consumer of a thermal energy storage system according to an embodiment of the invention.
- Fig. 4 is a schematic drawing showing an energy storage device according to an embodiment of the invention.
- Fig. 1 is a schematic drawing showing a thermal energy stor age system according to an embodiment of the invention.
- the thermal energy storage system 2 includes an energy storage device 4, a heat source 6, a blower 8, a first and second heat consumer 12, 10 and a heat transfer medium flowing and transferring thermal energy within the thermal energy storage system.
- the heat transfer medium may be a gaseous medium, e. g. air.
- an outlet of the blower 8b is con nected to the inlet of the heat source 6a by conduit 18d.
- the heat transfer medium exiting the heat source 6 through an outlet of the heat source 6b is transported to junction 20a by conduit 18a.
- conduit 18b is connected to an inlet 12a of the first heat consumer 12.
- the thermal energy storage system 2 includes a conduit 18e from the junction 20a to a first port 4a of the energy storage de vice 4.
- the heat transfer medium exits the energy storage de vice 4 through a second port 4b and is guided to a first port 10a of the second heat consumer 10.
- the heat transfer medium exits the second heat consumer 10 through a second port 10b and flows through a conduit 18h which is connected to conduit 18k at junction 20b.
- Another conduit 18g is provided in the thermal energy storage system 2 which connects junction 20c of conduit 18d and junction 20d of conduit 18h.
- the junctions 20a-d may include a component configured to control through which of the conduits connected to the junction the heat transfer medium flows. Such control may occur in dependence on the operating mode of the thermal energy storage system 2. Some of the junctions 20a-d may be controlled by at least one control valve, such as one or a combination of a three way valve, an on/off valve, a directional valves and the like.
- control valves can be controlled such that the heat transfer medium flows along a discharging and a charging flow path, which do not form separate circuits and therefore share the same heat transfer medium.
- the thermal energy storage system 2 can be operated in two operation modes, a charging and a discharging mode:
- the heat transfer medium is transported in a first flow direction A along a charging flow path 16 that includes the blower 8, the heat source 6, the energy storage device 4, and the second heat consumer 10.
- the heat source 6 may be, e. g., an electrical heater which converts electrical en ergy to thermal energy by heating an electrical resistor, or it may be a heat exchanger that is supplied with heat from a different source via a working fluid, such as a working fluid of a solar power plant or an exhaust gas from an industrial process, in particular waste heat.
- the heat source 6 may be any other kind of heat source which supplies thermal energy and can be used for heating the heat transfer medium.
- the thermal energy of the heat source 6 is transferred to the heat transfer medium while the heat transfer medium is pass ing the heat source 6.
- the heat transfer medium may be heated up to a temperature between 600 and 1000° C at the heat source 6.
- the 'heated' heat transfer medium is further trans- ported to the energy storage device 4 through conduits 18a and 18e.
- the flow connection at junction 20a between conduit 18a and conduit 18e may by established by controlling a respective control valve.
- the thermal energy of the heat transfer medium is transferred to the energy storage device, in particular to a heat storage material 24 (see Fig. 4) disposed in the energy storage de vice 4.
- the heat transfer medium exits the energy storage device 4 at lower temperature (compared to the temperature at which it exits the heat source 6), flows through conduit 18f in the first flow direction A and enters the second heat consumer 10.
- the heat trans fer medium may have a temperature between 100°C and 500°C, preferably 180°C and 350°C.
- the second heat consumer 10 may be a heat exchanger or a steam generator for generating steam or hot water with relatively low temperatures, e. g. about 100-350°C.
- the heat transfer medium exiting the energy storage device 4 may be used for operating the second heat consumer 10, in particular for transferring heat to a second medium of the second heat consumer 10 and generating e. g. steam or hot water.
- the heat transfer medium exiting the sec ond heat consumer 10 is guided back to the blower 8 through conduits 18h and 18k, which are in flow communication at junction 20b.
- the charging cycle is completed.
- the system 2 may be oper ated in the charging mode (i.e. cycle the heat transfer medi um along the charging flow path) until the energy storage is fully charged.
- the heat transfer medium is trans ported in a second flow direction B along a discharging flow path 14 that includes the blower 8, the second heat consumer 10, the energy storage device 4, and the first heat consumer 12.
- the heat transfer medium is transported to the second heat consumer 10 through conduits 18d, 18g and 18h.
- the discharging flow path 14 branches off from the charging flow path 16, e.g. con trolled by a control valve, such a three way valve or two on/off valves.
- Conduit 18g is brought into flow communication with conduit 18h at junction 20d, by e.g.
- the heat transfer medium is flowing in conduit 18h in the second flow direction B towards the second heat con sumer 10, flow direction B being opposite to the first flow direction A in conduit 18h.
- the heat transfer medium is guided by conduit 18f to the energy storage device 4 in which thermal energy is transferred from the heat storage material 24 (see Fig. 3) to the heat transfer medium while passing the energy storage de vice 4.
- the heat transfer medium may be heated up to a tem perature between 600 and 1000° C in the energy storage device 4.
- the 'heated' heat transfer medium (compared to the heat transfer medium enter ing the energy storage device 4) flows, via conduits 18e and 18b and junction 20a into the first heat consumer 12.
- the second flow direction B of the heat transfer medium in the discharging mode through the second heat consumer 10 and the energy storage device 4 is opposite to the first flow direc tion A through these components in the charging mode.
- the heat transfer medium transfers the thermal energy to a second medium.
- the first heat consumer may be a steam generator that generates steam from the second medium with high temperature and pressure (e.g. 565° C at 180 bar).
- the heat transfer medium exiting the first heat consumer 12 and being guided back to the blow er 8 through conduits 18c and 18k has a temperature of, e.g., between 150 and 450°C.
- the discharging cycle is completed.
- the system 2 may operate in the discharging mode in which the heat transfer medium is cycled along the discharging flow path un- til the energy storage device is fully discharged or no fur ther heat demand is present.
- the thermal en ergy storage system may be operated in the charging mode again until the energy storage device is re-charged.
- the heat transfer medium in discharging mode may still have a temperature in the range of e. g. 150 and 350 °C when enter ing the second heat consumer 10, which is sufficient to oper ate said heat consumer 10 in the same way as in the charging mode.
- the second heat consumer 10 may be operated in the charging mode as well as in the discharging mode at a temperature of the heat transfer medium in the range of, e.g., 150 to 450° C.
- the output of the blower 8 has the same flow direction in the charging and discharging mode.
- At least one control valve may be provided downstream of the blower 8 to separate the flow paths into the charging and the discharging flow paths 14,
- the thermal energy storage system 2 may include a control unit configured to control the control valves such that in charging mode, the heat transfer medium flows along the charging flow path 16 (dashed arrows) and in discharging mode, the heat transfer medium flows along the discharging flow path 14 (dotted arrows). It should be clear that there may be arranged more than one blower 8 in the thermal energy storage system 2. Further blowers could be used e.g. for boosting the pressure of the heat transfer medium or for the purpose of redundancy.
- a respective control unit configured to control such control valves may include a microprocessor and memory, which stores control instructions which are executed by the processor and which alternatingly operate the system 2 in the charging mode and the discharging mode and possibly in an idle mode.
- Such processor may for example be a digital signal processor, an application specific integrated circuit (ASIC), a microprocessor or the like.
- the memory may include flash- memory, a hard disk drive, RAM, ROM, and other types of volatile and non-volatile memory.
- Such control unit may furthermore include input and output interfaces for controlling the control valves and for receiving sensor signals.
- the temperature in the energy storage device 4 may be monitored to determine when operation in the charging mode is necessary or when the maximum amount of energy is stored. Likewise, it may determine the heat demand of heat consumer 12 and operate the system 2 accordingly in the discharging mode to supply the respective thermal energy.
- Fig. 2 is a schematic drawing showing a thermal energy stor age system according to an embodiment of the invention.
- the thermal energy storage system 2a includes the same components as the thermal energy storage system 2 shown in Fig. 1.
- the structure of the two systems is substantially the same, therefore only the differences of system 2a compared to sys tem 2 of Fig. 1 are described in the following.
- the explana tions given above with respect to system 2 of Fig. 1 are therefore also valid for the thermal energy storage system 2a of Fig. 2.
- the main difference of system 2a is the position of the sec ond heat consumer 10.
- the second heat consumer 10 is arranged downstream of the energy storage device 4 and upstream of the blower 8 with regard to the charging mode and the first flow direction. With regard to the discharging mode and the second flow direction, the second heat consumer 10 is arranged down stream of the first heat consumer 12 and upstream of the blower 8. The second heat consumer 10 is arranged in the charging mode as well as in the discharging mode upstream of the blower 8. As shown in Fig. 2, the second heat consumer 10 is arranged between junction 20b and blower 8.
- Conduit 18c which is connected at the one end to the outlet of the first heat consumer 12b is connected at the other end to junction 20b which is connected to the inlet of the second heat con sumer 10a through conduit 18j.
- the outlet of the second heat consumer 10b is connected to the inlet of the blower 8a through conduit 18i.
- conduit 18h is connected at the one end to the second port of the energy storage device 4b and at the other end to conduit 18c at junction 20b. Due to the position of the second heat consumer 10 and in con trast to the thermal energy storage system 2 of Fig. 1, the flow direction through the second heat consumer 10 of the thermal energy storage system 2a of Fig. 2 is the same in the charging mode and the discharging mode.
- the port 4b of the energy storage device 4 is connected to a conduit (18f in figure 1 and the conduit between 4b and 20d in figure 2) that provides a flow coupling to the second heat consumer 10, which is a direct connection in figure 1 and an indirect con nection (e.g. via blower 8) in figure 2.
- the second heat consumer 10 is connected at a posi tion in the system at which it receives in the charging mode the heat transfer medium directly from the energy storage de vice 4 via the conduit, and blower 8 is configured to convey the heat transfer medium along the charging flow path.
- the energy storage device 4 receives the heat transfer medium from the second heat consumer 10 direct ly (figure 1) or indirectly (figure 2, intervening blower 8) via the conduit.
- the conduit can in clude one or more pipes through which the heat transfer medi um flows both in the charging mode and the discharging mode (e.g. in reverse direction), or may include separate pipes for the charging mode and the discharging mode.
- Fig. 3 is a schematic drawing showing a steam turbine includ ing feedwater heaters of a steam power plant according to an embodiment of the invention.
- the function of the steam power plant 45 and its components is first briefly described and then reference is made to the specific application of the thermal energy storage system 2, 2a of Figs. 1 and 2 in the steam power plant 45.
- a boiler 56 is heated up by e.g. burning fuel and air which is supplied into the boiler through an inlet 42.
- the boiler 56 may also be heated up by the output of a heat storage or a heater which is supplied into the boiler through the inlet 42.
- gas is discharged from the boiler 56 via the outlet 44.
- the boiler 56 further includes an economizer 46, a re heater 48, a drum 50, and a superheater 52 through which a working medium of the steam cycle flows. The working medium exiting the superheater 52 and thus the boiler 56 as super heated steam is fed to a high-pressure (HP) turbine 34.
- HP high-pressure
- the HP turbine 34 is coupled to a low-pressure (LP) turbine 32 and both turbines are further coupled to a generator 30 for generating electrical energy.
- the HP turbine 34 is driven by expanding the superheated steam.
- the steam exiting the HP turbine 34 is reheated in a reheater 48 in the boiler 56 and then transported to the LP turbine 32 in which the reheated steam is expanded and the LP turbine 32 is driven.
- Both tur bines 34, 32 drive the generator 30, which generates elec tricity.
- the steam exiting the turbine 32 is fed to a conden ser 36 in which the steam is condensed to water.
- the water is further fed to a LP feedwater heater 38.
- a feedwater heater in general is used in a steam power plant to pre-heat water (feedwater) that is transported to the boiler 56 by transferring heat from steam to the feedwater flowing through the feedwater heater.
- feedwater feedwater
- the feedwater of LP feedwater heater 38 is heated by the energy derived from steam extracted between the stages of the LP turbine 32.
- the steam is then returned into the cycle via condenser 36.
- the heated feedwater exiting the LP feedwater heater 38 is pressurized by a pump 54 and fed to a HP feedwa ter heater 40. Part of the steam exiting the HP turbine 34 may be used for heating the feedwater flowing through the HP feedwater heater 40.
- the feedwater flowing through the HP feedwater heater 40 is heated by transferring heat from the steam of the HP turbine 34 to the feedwater, and it is thereafter fed to the econo mizer 46.
- the economizer 46 is used for heating the water up to but not normally beyond the boiling point of the water.
- the heated feedwater is further fed to the steam drum 50.
- the saturated steam is drawn off the top of the drum and is further guided through the superheater in which the superheated steam is generated by transferring heat resulting from the combustion process of e.g. fluid and air.
- the steam cycle repeats as described above.
- Su perheated steam is a dry gas which is used to drive turbines, since water droplets can severely damage the turbines.
- the second heat consumer 10 of the ther mal energy storage systems 2, 2a is supplied with heat trans fer medium at a temperature between 100 and 500° C in the charging mode and in the discharging mode.
- the feed water heaters 38, 40 may be operated with the steam provided by the second heat consumer 10 for heating the feedwater that is circulated in the steam power plant.
- the second heat consum er 10 may implement one or both of the feedwater heaters 38, 40, i.e. may directly heat the feedwater.
- the feedwater heaters 38, 40 do no longer need to be supplied with steam extracted from an intermediate stage of the steam turbines 32, 34 of the steam power plant. This is an ad vantage since the steam that was previously extracted from the steam turbines 32, 34 to be used in the feedwater heaters can now be transformed to work by expanding the steam in the turbine. Thus, the efficiency of the steam power plant is in creased.
- the second heat consumer 10 of the thermal energy storage system 2, 2a may be used for any kind of steam power plant which may have a different structure than the steam power plant 45 of Fig. 4 including at least one feedwater heater for heating the feedwater flowing through the feedwater heater.
- the steam turbine may form part of the thermal energy storage system, it may for example be employed to convert stored thermal energy back into electri cal energy.
- the boiler may then not operate with combustible fuel, but may be provided with thermal energy by the first heat consumer 12.
- Fig. 4 is a schematic drawing showing an energy storage de vice 4 according to an embodiment of the invention.
- the ener gy storage device 4 includes at least one first and at least one second port 4a, 4b which provide a flow connection into a storage chamber 22.
- the at least one first port 4a is oper ated as an inlet and the at least one second port 4b as an outlet for the heat transfer medium while the heat transfer medium flows in a first flow direction A.
- the at least one first port 4a is operated as an outlet and the at least one second port 4b as an inlet for the heat transfer medium while the heat transfer medium flows in a second flow direction B which is opposite to the first flow direction A of the charging mode.
- the energy storage device 4 further includes a heat storage material 24 that is disposed in the storage chamber 22.
- the heat storage material may have open pores and/or provides flow channels through which the heat transfer medium can flow and exchange thermal energy with the heat storage material 24.
- the heat storage material 24 may be e.g. sand or rocks/gravel.
- the energy storage device 4 may have any of the above-described configurations.
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Supply And Distribution Of Alternating Current (AREA)
- Engine Equipment That Uses Special Cycles (AREA)
- Heat-Pump Type And Storage Water Heaters (AREA)
Abstract
Description
Claims
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP20183435.5A EP3933175A1 (en) | 2020-07-01 | 2020-07-01 | Thermal energy storage system |
| PCT/EP2021/066932 WO2022002683A1 (en) | 2020-07-01 | 2021-06-22 | Thermal energy storage system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| EP4146916A1 true EP4146916A1 (en) | 2023-03-15 |
Family
ID=71451980
Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP20183435.5A Withdrawn EP3933175A1 (en) | 2020-07-01 | 2020-07-01 | Thermal energy storage system |
| EP21739574.8A Withdrawn EP4146916A1 (en) | 2020-07-01 | 2021-06-22 | Thermal energy storage system |
Family Applications Before (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP20183435.5A Withdrawn EP3933175A1 (en) | 2020-07-01 | 2020-07-01 | Thermal energy storage system |
Country Status (2)
| Country | Link |
|---|---|
| EP (2) | EP3933175A1 (en) |
| WO (1) | WO2022002683A1 (en) |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4094148A (en) * | 1977-03-14 | 1978-06-13 | Stone & Webster Engineering Corporation | Thermal storage with molten salt for peaking power |
| EP2220343B8 (en) * | 2007-10-03 | 2013-07-24 | Isentropic Limited | Energy storage apparatus and method for storing energy |
| WO2012120556A1 (en) * | 2011-03-07 | 2012-09-13 | 株式会社 日立製作所 | Solar heat steam cycle system |
| EP3102796B1 (en) | 2014-09-30 | 2018-01-31 | Siemens Aktiengesellschaft | High temperature thermal energy exchange system and method for exchanging thermal energy by using the high temperature thermal energy exchange system |
| GB2537126A (en) * | 2015-04-07 | 2016-10-12 | Isentropic Ltd | Hybrid energy storage system |
-
2020
- 2020-07-01 EP EP20183435.5A patent/EP3933175A1/en not_active Withdrawn
-
2021
- 2021-06-22 EP EP21739574.8A patent/EP4146916A1/en not_active Withdrawn
- 2021-06-22 WO PCT/EP2021/066932 patent/WO2022002683A1/en not_active Ceased
Also Published As
| Publication number | Publication date |
|---|---|
| WO2022002683A1 (en) | 2022-01-06 |
| EP3933175A1 (en) | 2022-01-05 |
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