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WO2016156177A1 - Système et procédé de stockage d'énergie - Google Patents

Système et procédé de stockage d'énergie Download PDF

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Publication number
WO2016156177A1
WO2016156177A1 PCT/EP2016/056483 EP2016056483W WO2016156177A1 WO 2016156177 A1 WO2016156177 A1 WO 2016156177A1 EP 2016056483 W EP2016056483 W EP 2016056483W WO 2016156177 A1 WO2016156177 A1 WO 2016156177A1
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WO
WIPO (PCT)
Prior art keywords
fluid
thermal storage
steam generator
energy
thermal
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.)
Ceased
Application number
PCT/EP2016/056483
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English (en)
Inventor
Volker Seidel
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.)
Siemens AG
Siemens Corp
Original Assignee
Siemens AG
Siemens Corp
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 Siemens AG, Siemens Corp filed Critical Siemens AG
Publication of WO2016156177A1 publication Critical patent/WO2016156177A1/fr
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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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
    • F01K3/12—Plants characterised by the use of steam or heat accumulators, or intermediate steam heaters, therein having two or more accumulators

Definitions

  • the present invention relates to the field of energy storage, in particular to a system for storing energy and a method of storing energy using thermal storage.
  • thermal energy at high temperature enters the system and leaves the sys ⁇ tem at low temperature (in the condensing and exhaust sys ⁇ tem) .
  • the efficiency of the thermal power plant is limited by the Carnot efficiency which is defined by the work divided by the heat added to the system or a relation between the abso ⁇ lute temperature of the cold and hot reservoir. This is a theoretical process and its efficiency cannot be surpassed physically.
  • additional mechanical e.g. flow irreversibility in the turbine, pump irreversibil- ity
  • thermal, electrical and exergy losses lead to a reduced efficiency.
  • thermal energy storage plant could be configured with a thermal storage, in which thermal energy is stored, and a HRSG with a water-steam cycle for re-electrification.
  • thermal energy is extracted from the thermal storage
  • air is guided through the thermal storage arrangement and leaves the storage as heated air.
  • This heated air is then used to generate steam in the HRSG.
  • the hot air cannot be cooled down to ambient temperature in the HRSG, so that unused heat leaves the system and reduces the efficiency of the system.
  • the problem may be partially solved by building more effi- cient and more expensive HRSGs with multiple steam pressure levels such as three pressure levels. This way the tempera ⁇ ture of the air that leaves the HRSG is further reduced, e.g. to around 90°C in state of the art high efficiency combined cycle power plants (CCPPs) .
  • the thermodynamic efficiency of the internal steam cycles with medium and low pressure is ra ⁇ ther low in comparison to the high pressure cycle.
  • the total efficiency adds up to a higher value when compared with a single pressure HRSG since the low tempera ⁇ ture heat losses are reduced due to the reduction of the HRSG outlet temperature. Further reduction of this temperature is economically not feasible due to the immense amount of re ⁇ quired heat exchanger surface in the HRSG.
  • thermal storage systems are among the sys ⁇ tems considered for temporarily storing extra power during periods of high production (e.g. strong wind, sunny days) in order to compensate for subsequent periods of low production (e.g. weak wind, cloudy days) .
  • high production e.g. strong wind, sunny days
  • low production e.g. weak wind, cloudy days
  • a system for storing energy comprising (a) a first thermal storage for storing thermal energy, (b) a steam generator comprising a fluid input in fluid communication with the first thermal storage to receive a working fluid, wherein the steam generator is adapted to heat a steam tur- bine fluid using the working fluid, the steam generator further comprising a fluid output for outputting the working fluid, and (c) a second thermal storage in fluid communica ⁇ tion with the fluid output of the steam generator and adapted to store thermal energy remaining in the working fluid.
  • thermal storage may in particular denote a device, arrangement or structure that is capable of storing received thermal energy and of releasing (outputting) stored thermal energy.
  • the (first and/or second) thermal storage may be a sensible thermal storage or a latent thermal stor ⁇ age.
  • the thermal storage may be filled with a thermal storage material.
  • the thermal storage material may be a solid or bulk material, such as stones, bricks, ceramics or other solid material which has the ability to be heated up, keep its temperature and thus store thermal energy over a predetermined period of time. However, it should be under ⁇ stood that also water may be used as the thermal storage ma ⁇ terial. The thermal storage material may be heated up
  • An exemplary thermal storage may comprise a first opening and a second opening.
  • a fluid such as the working fluid, may be flowed through the thermal storage from the first opening to the second opening or from the second opening to the first opening.
  • the fluid may be in direct physical contact with the thermal storage material when the fluid flows through the thermal storage.
  • the thermal storage material may be provided as stones and the fluid may be air.
  • the air and the stones may come in direct physical contact with each other when the air flows through the thermal storage.
  • the fluid may be in indi ⁇ rect contact with the thermal storage material when the fluid flows through the thermal storage.
  • the first opening may be an opening in the thermal storage through which fluid may be exchanged with one or more exter- nal devices, e.g. a thermal energy source, such as a heating device, and the steam generator.
  • a thermal energy source such as a heating device
  • the first opening and the device (s) may be connected by a pipe or a duct.
  • the second opening may be a further opening in the thermal storage through which the thermal storage is able to exchange fluid with some further external device (s), such as the steam generator, the heating device, or a pump.
  • the second opening and the further device (s) may be connected by a pipe or a duct.
  • the first opening and the second opening may respectively be denoted the hot opening (or hot end) and the cold opening (or cold end) of the thermal storage, and vice versa.
  • the first opening and the second opening are similarly or identically formed. It should however be un ⁇ derstood that the first opening and the second opening may also be formed to have different shapes.
  • the first opening and the second opening may be formed in the same side surface of the thermal stor- age. This configuration may be advantageous when geometric restraints of the overall configuration of the system do not permit another geometrical set-up.
  • the first opening and the second opening may be formed in differ ⁇ ent side surfaces, in particular in opposing side surfaces, of the thermal storage.
  • the working fluid may be a medium, such as for example a gas or a liquid, which flows through the system, in particular from the first thermal storage to the second thermal storage via the steam generator. Thereby, a part of the thermal en ⁇ ergy transported away from the thermal storage by the working fluid can be used by the steam generator while remaining thermal energy is stored in the second thermal storage.
  • the medium may be a mixture consisting of a main component, such as water, with added supplements for influencing physical characteristics of the mixture, such as for example the evaporation point or the condensation point.
  • the steam generator device may be a heat exchanger. In particular, the steam generator is adapted to heat the steam turbine fluid for driving a steam turbine system.
  • the steam generator may comprise a boiler or an evaporator.
  • Heat exchangers are devices for transferring thermal energy from one medium to another in the direction of a temperature gradient. Heat exchangers are built for changing a temperature of a medium, for example by cooling or heating.
  • the steam generator device may comprise an indirect heat ex ⁇ changer. In indirect heat exchangers, the heat is transferred from one medium to another medium over solid walls separating the two media from each other.
  • the steam generation device may also comprise a
  • Boilers are closed devices in which a medium is heated up and boiled, respectively.
  • the heated or vaporized medium leaves the boiler and may be used in the steam turbine system.
  • Evaporators are devices which are used to turn a medium from its liquid form into its gaseous form. The evaporated medium may as well be used in the steam turbine system.
  • the steam turbine fluid is a fluid that may be used to drive a steam turbine system.
  • the steam turbine fluid may be steam, water vapour or vapour with a high mass fraction of water in it, respectively.
  • water vapour may be saturated but also unsaturated.
  • the working fluid may further be an organic liquid which may be used in an Organic Rankine Cycle (ORC) .
  • ORC Organic Rankine Cycle
  • the steam turbine system may generally be a system which comprises a steam turbine and further devices for transforming thermal energy into mechanical energy and electricity, re- spectively.
  • the steam turbine system may com ⁇ prise a steam turbine, a condenser, a generator, a first pump and optionally a second pump.
  • the steam turbine may be a multi stage steam turbine or a single stage turbine. In the multi stage turbine the steam turbine fluid may be reheated between the different stages or a part of the steam turbine fluid may be extracted from the steam turbine, e.g. due to too excessive cooling of the steam turbine fluid. Fluid may also be extracted to preheat the feed water, district heat ⁇ ing, process steam for use in the chemical industry, or brew- eries.
  • the steam turbine comprises blades connected to a shaft.
  • the energy of the steam turbine fluid flowing through the steam turbine is transmitted by the blades of the steam turbine to the shaft.
  • the generator is connected to the shaft of the steam turbine and converts the rotational energy of the shaft of the steam turbine into electrical energy.
  • the generated electrical energy may then be transferred to a power supply network or any other end-user.
  • the steam turbine fluid flows through the condenser in which the steam turbine fluid is condensed into its liquid state.
  • the first pump and the sec ⁇ ond pump drive the steam turbine fluid through the different components of the steam turbine system and through the steam generation device.
  • the second pump may be of importance in order to reach the design pressure of the steam in the water steam cycle.
  • the system fur- ther comprises a heating device in fluid communication with the first thermal storage, wherein the heating device is adapted to heat a charging fluid during a charging phase.
  • the heating device heats a charging fluid which is then supplied to the first thermal storage.
  • the charging fluid may be similar or identi ⁇ cal to the working fluid discussed above.
  • the charging fluid is air.
  • the heat ⁇ ing device is adapted to transform electric or magnetic ener ⁇ gy into heat.
  • the heating may comprise a resistance heater, an electrical heater or an inductive heater.
  • the system may be used to store energy received in the form of electric or magnetic energy as thermal energy in the first thermal storage.
  • the received energy may e.g. be excess en- ergy produced by a power plant utilizing a renewable energy source, such as wind power or solar power.
  • the system further comprises a first pumping device for transporting heated charging fluid from the heating device to the first thermal storage.
  • the first pumping device may be a blower arranged to
  • the heat ⁇ ing device is in fluid communication with the second thermal storage, the system further comprising a second pumping device for transporting charging fluid from the second thermal device to the heating device.
  • the fluid communication between the second thermal storage and the heating device may be constituted by a pipe or a duct.
  • the second pumping device may e.g. be a blower arranged to transport air from the second thermal storage to the heat ⁇ ing device.
  • the second pumping device may replace the first pumping device in the sense that the second pumping device also performs the function of the first pumping de ⁇ vice, such that it is capable of transporting the charging fluid from the second thermal storage to the first thermal storage via the heating device.
  • the first pumping device may also undertake the function of the second pumping device, such that also in these embodiments only a single pumping device is needed in order to perform the functions of both the first pumping device and the second pumping device.
  • the first and second pumping devices may be implemented as two physi ⁇ cally separate pumping devices, e.g. one (the first pumping device) between the heating device and the first thermal storage and another one (the second pumping device) between the second thermal storage and the heating device.
  • the second pump ⁇ ing device serves to extract thermal energy from the second thermal storage in order to provide a pre-heated charging fluid to the heating device. Accordingly, the heating device will need less energy to heat the charging fluid to the de ⁇ sired temperature for storing in the first thermal storage. Thereby, the remaining thermal energy of the working fluid that has been stored in the second thermal storage is re ⁇ introduced into the first thermal storage, such that the losses within the system are minimized independently of the efficiency of the steam generator.
  • the system further comprises a third pumping device for transporting the working fluid from the first thermal storage through the steam generator and on to the second thermal storage during a discharging phase.
  • the third pumping device serves to transport the working fluid from the first thermal storage to the second thermal storage via the steam generator.
  • the working fluid leaves the first thermal storage with a relatively high content of thermal energy and is transported through the steam generator where a certain amount of the thermal energy is used to heat the steam turbine fluid.
  • the working fluid then leaves the steam generator with a lower content of thermal energy. This remaining thermal energy is, except for unavoidable losses, stored in the second thermal storage for later use.
  • the third pumping device comprises a single pumping unit arranged either between the first thermal storage and the steam generator or between the steam generator and the second thermal storage. In other embodiments, the third pumping device comprises two or more pumping units, of which at least one is arranged between the first thermal storage and the steam generator while another one is arranged between the steam generator and the second thermal storage.
  • the working fluid and/or the charging fluid is air.
  • the steam generator is a heat recovery steam generator (HRSG) .
  • HRSG may be an energy recovery heat exchanger which recovers energy from a fluid stream.
  • the HRSG may e.g. comprise the following four principal components: an economizer, an evaporator, a super-heater and a re-heater. The four
  • the HRSG may be a vertical type HRSG, a horizontal type HRSG, a single pressure HRSG or a multi pressure HRSG.
  • the steam generator is adapted to receive the working fluid at the flu ⁇ id input at a temperature between 550°C and 1000°C, such as around 600 °C, and to output the working fluid through the fluid output at a temperature between 100°C and 400°C, in particular between 150°C and 350°C, in particular between 200°C and 300°C, in particular around 250°C.
  • Highly advanced - and thus expensive - steam generators are capable of providing a working fluid output having a tempera ⁇ ture of 90°C.
  • the present invention can provide a highly efficient system for storing thermal energy, even if the steam generator as such is not particularly effective. Thereby, significant savings can be obtained by using simple and/or existing (old) steam generators.
  • the steam generator has a pinch point of at least 10K, in particular at least 20K.
  • a power plant comprising (a) a power generator for producing electrical energy based on a renewable energy source, and (b) a system according to the first aspect or any of the above embodiments thereof, wherein the system is adapted to store excess energy from the power generator during overproduction by charging the first thermal storage, and wherein the system is adapted to release stored energy during insuf ⁇ ficient production by discharging the first thermal storage.
  • This second aspect of the invention is based on essentially the same idea as the first aspect described above. More spe ⁇ cifically, the second aspect uses a system according to the first aspect as part of a power plant that relies upon a re ⁇ newable energy source, such as wind power or solar power, which by nature is prone to fluctuations.
  • the power plant according to the second aspect is capable of providing a more stable level of output by buffering excess energy during overproduction for later use to compensate for insufficient production.
  • a method of storing energy comprising (a) feeding a heated charging fluid to a first thermal storage to store thermal energy in the first thermal storage during a charging phase, (b) feeding a working fluid from the first thermal storage to a fluid input of a steam generator during a discharging phase, wherein the steam generator is adapted to heat a steam turbine fluid using the working fluid, and (c) conducting the working fluid from a fluid output of the steam generator to a second thermal storage to store thermal energy remaining in the working fluid.
  • This third aspect of the invention is based on essentially the same idea as the first and second aspects described above. More specifically, the third aspect relates to a meth ⁇ od of using or operating the system according to the first aspect or a power plant according to the second aspect. That is, thermal energy is stored in a first thermal storage dur ⁇ ing a charging phase and then, during a discharging phase, the thermal energy is extracted from the first thermal stor ⁇ age by a working fluid and used to heat a steam turbine flu- id. Remaining thermal energy in the working fluid output by the steam generator is stored in a second thermal storage.
  • Figure 2 shows a schematic diagram of a system according to a further embodiment of the present invention.
  • Figure 3 shows a plot of heat transfer in a steam generator in accordance with embodiments of the present invention.
  • Figure 1 shows a schematic diagram of a system 100 according to an embodiment of the present invention. More specifically, the system 100 comprises a first thermal storage 110, a steam generator 120, a second thermal storage and a pump 140.
  • the first thermal storage 110 is schematically illustrated as having a first opening 112 and a second opening 114 that allow a fluid, such as a gaseous or liquid working fluid or charging fluid, to enter and exit the thermal storage 110, whereby the fluid gets into direct or indirect contact with a thermal storage material disposed within the first thermal storage 110.
  • the thermal storage material may e.g. comprise stone, bricks, ceramics or another solid material which is capable of storing thermal energy over a predetermined period of time, such as 12 hours or more.
  • the second thermal stor ⁇ age 130 is schematically illustrated as having a first open ⁇ ing 132 and a second opening 134 that allow a fluid, such as a gaseous or liquid working fluid output by the steam genera- tor 120, to enter and exit the thermal storage 130, whereby the fluid gets into direct or indirect contact with a thermal storage material disposed within the second thermal storage 130.
  • the thermal storage material may e.g. comprise stone, bricks, ceramics or another solid material which is capable of storing thermal energy over a predetermined period of time, such as 12 hours or more.
  • the steam generator 120 comprises a fluid input 122 in fluid communication with the second opening 114 of the first ther- mal storage 110 via fluid connection 116.
  • the steam generator 120 further comprises a fluid output 124 in fluid connection with the first opening 132 of the second thermal storage 130 via fluid connection 136.
  • the steam generator 120 receives water via water supply 126 and outputs generated steam via steam output 128.
  • the steam output 128 may be connected to a steam turbine (not shown) for producing electricity.
  • the pump 140 may preferably be a blower arranged to blow a working fluid into the first thermal storage 110 through the first opening 112 in order to extract or discharge thermal energy stored in the first thermal storage 110.
  • the thus heated working fluid is transported through fluid connection 116 to the fluid input 122 of steam generator 120.
  • figure 1 only relates to the discharging of the system 100. Charging of the system 100 will be described in more detail in conjunction with the embodiment shown in figure 2.
  • the steam generator 120 uses a hot working fluid received from the first thermal storage 110 at the fluid input 122 to heat water received via water supply 126 and thereby generate steam.
  • the hot working fluid preferably has a temperature around 600 °C.
  • the working fluid loses thermal energy and thus leaves the steam generator through fluid output 124 at a lower temperature, such as between 100°C and 400°C, preferably around 200°C, depending on the efficiency of the steam generator 120.
  • the output working fluid is transported to the first opening 132 of the second thermal storage 130 via fluid con ⁇ nection 136. Thereby, the remaining thermal energy of the working fluid is stored in the second thermal storage such that it can be used for other purposes when needed.
  • the thermal energy stored in the second thermal storage 130 may be used for a number of purposes. For example, it may be used to generate electric or mechanical energy that may be needed at a power plant relying on renewable energy during periods of low energy availability, e.g. little or no wind or sunlight. As will be discussed in more detail with regard to the embodiment shown in figure 2, the stored thermal energy may also advantageously be used when charging the first ther- mal storage 110.
  • FIG. 2 shows a schematic diagram of a system 200 according to a further embodiment of the present invention. More spe ⁇ cifically, the system 200 comprises a first thermal storage 210, a steam generator 220, such as an HRSG, and a second thermal storage 230. These elements correspond to and are in- terconnected in the same way as the first thermal storage
  • a pump 244 such as a blower, is shown in the fluid connection 236 in order to transport the output working fluid from the HRSG 220 to the first open ⁇ ing 232 of the second thermal storage 230.
  • the system 200 further comprises a heating element 250 and a pump 242, such as a blower, arranged in a fluid path between the first opening 232 of the second thermal storage 230 and the second opening 214 of the first thermal storage 210.
  • the fluid path comprises a fluid connection 218 ar- ranged between the first thermal storage 210 and the heating device 250, and a fluid connection 238 between the second thermal storage 230 and the blower 242.
  • Discharging or recovery of energy stored in system 200 i.e. thermal energy stored in the first thermal storage 210 is done in a similar way as described above in conjunction with the embodiment shown in figure 1. Therefore, the correspond ⁇ ing description is not repeated here.
  • Charging the system 200 with energy is done by guiding a preheated charging fluid (e.g. having a temperature around
  • the heating device 250 adds thermal energy to the charging fluid and the fully heat- ed charging fluid (e.g. having a temperature of around 600°C) is injected into the first thermal storage 210 to store the corresponding thermal energy therein.
  • the fully heat- ed charging fluid e.g. having a temperature of around 600°C
  • Figure 3 shows a plot 301 of heat transfer in a steam genera ⁇ tor in accordance with embodiments of the present invention. More specifically, the plot 301 shows heat transfer in an HRSG system with an inlet temperature of 600°C and a pressure of 120 bar.
  • the solid curves 360 and 362 shows the characteristic curves of a state of the art CCPP system. That is, the solid curve 360 shows water temperature and the solid curve 362 shows the temperature of the working fluid (e.g. hot air) in the sys ⁇ tem.
  • the exit temperature 364 of the working fluid i.e. the output fluid temperature
  • the dashed curves 370 and 372 shows the characteristic curves of a HRSG system suitable for use with embodiments of the present invention.
  • the dashed curve 370 shows water temperature and the dashed curve 372 shows the temperature of the working fluid (e.g. hot air) in the system.
  • the exit tem- perature 374 of the working fluid i.e.
  • the output fluid tem ⁇ perature is around 250°C, i.e. significantly higher than in the conventional CCPP system characterized by the solid curves 360, 362.
  • the pinch point is the minimum temperature difference in the steam generator between gas and water flow. In HRSGs the pinch point is the difference between the gas temperature leaving the evaporator and the saturation temperature.
  • the pinch point for the conventional CCPP system is indicated by arrows 366 in figure 3.
  • the pinch point of the HRSG can fur ⁇ thermore be larger compared to conventional CCPPs with only minor effect on the cycle efficiency. This is due to the fact that in CCPP thermal energy remaining in the flue gas is dis- charged to the environment. Hence the pinch point is chosen as small as techno-economically feasible.
  • the heat exchanger surface area in the HRSG strongly increases when reducing the pinch point.
  • the energy in the air downstream of the HRSG is recovered (in the second thermal storage 130, 230) and reduces the tempera ⁇ ture difference between the air upstream and downstream of the charging equipment.
  • the thermal energy that is not trans ⁇ ferred to the steam in the HRSG remains in the system and is not lost. Therefore the HRSG can be designed with a larger pinch point and with significant less heat exchanger surface and consequently costs compared to a conventional CCPP.
  • the HRSG exit temperature increases which is not desired in CCPPs because the thermal losses then increase.
  • the systems according to the present invention can achieve higher steam cycle efficiency because the steam pres ⁇ sure and the HRSG exit temperature can be increased due to the recovery of the thermal energy in the storage system.
  • the steam pressure can be increased regardless of the HRSG outlet tem ⁇ perature.
  • the steam pressure in one pressure HRSGs is usually relatively low (compared to fired steam gen ⁇ erators) to reduce the saturation temperature of the water and consequently the HRSG exit temperature, cf. figure 3.
  • the continuous lines 360, 362 illustrate the wa ⁇ ter/steam and air temperature in a HRSG of a conventional system and the dashed line the temperatures of thermal stor ⁇ age systems according to the present invention.
  • the steam generator layout is especially designed for thermal storages. This allows for higher steam pressure and higher outlet tem ⁇ perature at the HRSG 120, 220 than in conventional CCPPs and hence these systems achieve higher steam cycle efficiency.
  • the recovery of the thermal energy in the steam generator 120, 220 outlet air reduces the required charge power for the storage and improves the total system efficiency.
  • the thermal energy remaining in the exhaust gas is not discharged in the environment but stored in the system.
  • the pinch point can be designed larger with minor effects on the cycle efficiency and the costs of the steam generator reduce significantly compared to conventional CCPPs.
  • the exhaust sys ⁇ tem of the HRSG is obsolete because the thermal energy in the exhaust air of the HRSG is stored in a thermal storage. The environmental impact of the low temperature thermal energy in the waste heat is avoided.

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Engine Equipment That Uses Special Cycles (AREA)

Abstract

L'invention concerne un système pour stocker de l'énergie, lequel système comprend (a) un premier stockage thermique (110, 210) pour stocker de l'énergie thermique, (b) un générateur de vapeur (120, 220) comprenant une entrée de fluide (222) en communication vis-à-vis des fluides avec le premier stockage thermique (110, 210) pour recevoir un fluide de travail, le générateur de vapeur (120, 220) étant apte à chauffer un fluide de turbine à vapeur à l'aide du fluide de travail, le générateur de vapeur (120, 220) comprenant en outre une sortie de fluide (124, 224) pour délivrer en sortie le fluide de travail, et (c) un second stockage thermique (130, 230) en communication vis-à-vis des fluides avec la sortie de fluide (124, 224) du générateur de vapeur (120, 220) et apte à stocker de l'énergie thermique restant dans le fluide de travail. L'invention concerne également une centrale électrique et un procédé de stockage d'énergie.
PCT/EP2016/056483 2015-03-31 2016-03-24 Système et procédé de stockage d'énergie Ceased WO2016156177A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
EP15161946.7 2015-03-31
EP15161946.7A EP3075969A1 (fr) 2015-03-31 2015-03-31 Système et procédé de stockage d'énergie

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WO2016156177A1 true WO2016156177A1 (fr) 2016-10-06

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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2013033200A2 (fr) * 2011-08-30 2013-03-07 Abengoa Solar Inc. Champ solaire hybride
EP2574784A2 (fr) * 2011-09-29 2013-04-03 Pratt & Whitney Rocketdyne Inc. Système d'énergie solaire et procédé associé
WO2013065492A1 (fr) * 2011-10-31 2013-05-10 三菱重工業株式会社 Dispositif générateur d'électricité à turbine à chaleur solaire et procédé de commande pour ce dispositif
WO2013174901A1 (fr) * 2012-05-25 2013-11-28 Cockerill Maintenance & Ingenierie S.A. Couplage de turbopompe pour sels fondus
WO2014052927A1 (fr) * 2012-09-27 2014-04-03 Gigawatt Day Storage Systems, Inc. Systèmes et procédés de récupération et de stockage d'énergie

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102013016077A1 (de) * 2013-09-27 2015-04-16 Rolf Schumacher Elektrische Energiespeicherung mittels thermischer Hochtemperaturspeicher

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2013033200A2 (fr) * 2011-08-30 2013-03-07 Abengoa Solar Inc. Champ solaire hybride
EP2574784A2 (fr) * 2011-09-29 2013-04-03 Pratt & Whitney Rocketdyne Inc. Système d'énergie solaire et procédé associé
WO2013065492A1 (fr) * 2011-10-31 2013-05-10 三菱重工業株式会社 Dispositif générateur d'électricité à turbine à chaleur solaire et procédé de commande pour ce dispositif
WO2013174901A1 (fr) * 2012-05-25 2013-11-28 Cockerill Maintenance & Ingenierie S.A. Couplage de turbopompe pour sels fondus
WO2014052927A1 (fr) * 2012-09-27 2014-04-03 Gigawatt Day Storage Systems, Inc. Systèmes et procédés de récupération et de stockage d'énergie

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