EP2516854A2 - Centrale héliothermique et procédé pour faire fonctionner une centrale héliothermique - Google Patents

Centrale héliothermique et procédé pour faire fonctionner une centrale héliothermique

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Publication number
EP2516854A2
EP2516854A2 EP10787397A EP10787397A EP2516854A2 EP 2516854 A2 EP2516854 A2 EP 2516854A2 EP 10787397 A EP10787397 A EP 10787397A EP 10787397 A EP10787397 A EP 10787397A EP 2516854 A2 EP2516854 A2 EP 2516854A2
Authority
EP
European Patent Office
Prior art keywords
steam
temperature
solar
power plant
thermal power
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Withdrawn
Application number
EP10787397A
Other languages
German (de)
English (en)
Inventor
Jürgen Birnbaum
Peter Gottfried
Zsuzsa Preitl
Frank Thomas
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
Original Assignee
Siemens AG
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 filed Critical Siemens AG
Publication of EP2516854A2 publication Critical patent/EP2516854A2/fr
Withdrawn legal-status Critical Current

Links

Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F03—MACHINES OR ENGINES FOR LIQUIDS; WIND, SPRING, OR WEIGHT MOTORS; PRODUCING MECHANICAL POWER OR A REACTIVE PROPULSIVE THRUST, NOT OTHERWISE PROVIDED FOR
    • F03G—SPRING, WEIGHT, INERTIA OR LIKE MOTORS; MECHANICAL-POWER PRODUCING DEVICES OR MECHANISMS, NOT OTHERWISE PROVIDED FOR OR USING ENERGY SOURCES NOT OTHERWISE PROVIDED FOR
    • F03G6/00—Devices for producing mechanical power from solar energy
    • F03G6/06—Devices for producing mechanical power from solar energy with solar energy concentrating means
    • F03G6/065—Devices for producing mechanical power from solar energy with solar energy concentrating means having a Rankine cycle
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E10/00—Energy generation through renewable energy sources
    • Y02E10/40—Solar thermal energy, e.g. solar towers
    • Y02E10/46—Conversion of thermal power into mechanical power, e.g. Rankine, Stirling or solar thermal engines

Definitions

  • the invention relates to a solar thermal power plant with ei ⁇ ner solar panel steam generator unit for generating steam, with a solar panel steam generator unit downstream solar collector steam superheater unit for superheating the steam and a steam line via a system connected to an output of the solar panel steam superheater unit steam turbine, which is fed during operation with the superheated steam. Moreover, the invention relates to a method for operating such a solar thermal power plant.
  • Solar thermal power plants represent an alternative to conventional power generation ⁇ forth.
  • solar-thermal power plants with parabolic trough collectors with an indirect evaporative means of an additional oil circuit are ⁇ leads.
  • Solar thermal power plants with direct evaporation are being developed for the future.
  • a solar thermal power ⁇ factory with direct evaporation for example, from one or more solar panels nenkollektoren each with several parabolic trough and / or Fresnel collectors consist in which the in-pumped feed water is first preheated and vaporized and then the steam is superheated. The superheated steam is directed to a conventional power plant section, where the thermal energy of the water vapor is converted into electrical energy.
  • first preheating and evaporation of the water in first solar fields with multiple parallel strands of parabolic trough collectors and / or Fresnel collectors takes place (hereinafter also "evaporator solar fields” called.)
  • the generated steam or water produced - vapor mixture is then fed into a first of Dampfabschei- to deposit the remaining, not yet evaporated What ⁇ ser the steam is then further into the.
  • Solar panel steam superheater units piped.
  • the solar collector steam superheater units can be individual solar collectors, a plurality of parallel solar collector strands or solar fields that in turn consist of a plurality of solar collector strands.
  • the power plant part of coming from the solar collector steam superheater units superheated steam turbine is supplied ⁇ leads, which drives a generator.
  • the steam Upon subsequent cooling in a condenser, the steam reverts to water, which is collected in a feedwater tank and fed to the solar panels via the feed water pump.
  • the power plant part can not only have a turbine, but several with respect to the steam transport direction in series turbines, such as a high-pressure turbine, in the first steam is passed, and a medium-pressure and / or low-pressure turbine, in which of the high-pressure turbine coming steam is used again.
  • a typical temperature range is between 390 and 500 ° C, whereby the vapor pressure between 41 and 140 bar can lie.
  • these parameters may vary from plant to plant depending on the design of the components. Nevertheless, the problem always remains that the temperature of the delivered to the turbine
  • a steam temperature control can be controlled with steam cooling devices z. B. in the area of the solar collector steam superheater units that cool the initially over the actual desired temperature superheated steam to the required temperature.
  • this injection coolers are used, which inject precisely defined amounts of water into the steam and cool it.
  • Other steam cooling systems mix colder steam. Depending on the heat input or load case, the amount ofdemedi ⁇ ums be reduced or increased to maintain the desired Tem ⁇ temperature.
  • a solar thermal power plant has thereto according to the invention to an intermediate memory which th at at least one steam superheating unit and the steam turbine is arranged between the solar panel ers high-temperature storage connection point is connected to the Dampflei ⁇ processing system, is superheated in a memory operation mode steam from the Remove steam line system.
  • This buffer comprises a heat accumulator in which thermal energy is extracted and stored in the steam introduced in the storage operating mode. In a Entddlingbe ⁇ operation mode the stored thermal energy is released back into the steam which is supplied from the buffer memory to the steam circuit.
  • ⁇ tion according to a capacitor and / or a relaxation device of the solar thermal power plant connected.
  • connections to the high-temperature storage connection point and the low-temperature storage connection point can usefully take place via a storage connection valve device with one or more valves.
  • a part of the superheated steam in the insectspei- is accordingly rather directed to the heat accumulator in a SpeI ⁇ cher Seasmodus at a high-temperature storage ⁇ connection point.
  • this steam is extracted from the thermal energy and stored.
  • the cooled steam or water formed thereby / steam mixture is fed to a capacitor and / or an expansion device.
  • the latch at one is low-temperature storage connection ⁇ point of water and / or steam supplied and the stored thermal energy is released into the water or the steam and the superheated steam thus generated is supplied directly or indirectly to the steam turbine.
  • the buffer is therefore connected to a low-temperature storage connection point (preferably directly but possibly also indirectly, ie via further components) to a condenser and / or a relaxation device of the solar thermal power plant.
  • the expansion device may be, for example, a flash tank or the like, in which the pressurized steam or the water / steam mixture z. B. is relaxed atmospherically.
  • a feed water tank with a suitable design as a relaxation device for the derivative serve the medium at the low temperature end of the cache.
  • an expansion tank it is also possible for an expansion tank to be connected in series between the low-temperature-side outlet of the intermediate store and the condenser. This is particularly useful if it is specified by the herstel ⁇ ler of the condenser system is that only liquid medium should enter the condenser from such a bypass.
  • the supply line in a condenser or to a relaxation device has the advantage that regardless of the temperature and pressure conditions and the state of matter of the medium (water and / or steam) at the output of the buffer the medium carried away and the water / steam cycle of solar thermal Power plant can be fed again.
  • This allows a very high thermal charge of the heat accumulator.
  • the buffer can be brought to a higher temperature level in total, as in a construction in which, for example, only a storage operation is possible, as long as the capacity of the heat accumulator is sufficient to completely convert the steam into the liquid phase and supply the condensate to the feed water.
  • feed water can in particular be extracted from the Lucaswas ⁇ water pipe, which is then first vaporized in a thermally highly charged heat storage by releasing the stored thermal energy and then overheated, so that the superheated steam can be fed back at a high-temperature storage connection point the Dampf effetssys- tem can.
  • the buffer may be preferably connected via a valve at a low-temperature storage connection point with the feedwater line. At a common pressure difference between the feedwater line and the main steam line, the water flows in the removal mode automatically in the buffer and then steam in the main steam line.
  • the storage operation mode is usefully set when the solar thermal power plant is in a
  • the removal ⁇ operating mode is set when the solar-thermal power plant ⁇ is in a lower power mode, ie when the solar collector field less steam power supplies than is actually needed. It is clear that in such a system, the capacity of the solar field, ie the Son ⁇ nenkollektor-steam generator unit (s) and the solar collector ⁇ gate steam superheater unit (s), must be sized larger than it is needed in normal average operation, as sufficient to provide capacity to fill the insectspei ⁇ chers during the memory operation mode. In addition to the short-term increase in capacity or to support the live steam temperature, the buffer can be used even in sunny periods, especially in the evening and at night, to continue to produce steam and produce electricity with the solar thermal power plant even in these times.
  • the cooled and possibly even partially or completely condensed steam can at least temporarily be returned to the water / steam cycle of the solar thermal power at other suitable locations. plants are supplied.
  • the buffer is preferably connected to other low-temperature Speicheran gleichstel ⁇ len with different lines or other components in the line system of the solar thermal power plant.
  • the buffer may also be connected to various low-temperature storage connection points-via controllable valves-with different steam lines, in which steam is conducted at different temperatures or pressures during operation.
  • the connection to the various steam lines at the various low-temperature storage connection points is advantageously carried out via suitable valves, which are individually controllable.
  • the connection of the buffer with different low-temperature storage connection points on a condenser or a relaxation device and / or on different steam lines is particularly useful for those cases in which the heat accumulator due to design or because he is already so heavily charged, the steam not enough energy can escape, so that the steam condenses completely.
  • the valve can always be opened to the steam line, in which steam is guided with the suitable steam temperature range and in the appropriate pressure range.
  • the steam or the water / steam mixture can then be used without energy losses at the appropriate places in the circuit. It is preferably arranged to ⁇ least a part of the low-temperature storage connection points in output steam lines of a steam turbine and / or at least a part of the low-memory connection points connected to heat exchangers.
  • the medium coming from the intermediate storage can still be used for regenerative feedwater pre-heating. If the pressure and / or temperature conditions at the low-temperature end of the accumulator are not suitable for any of the connected steam pipes or other components, then the steam or the water / steam mixture according to the invention is supplied to the flash tank or the condenser.
  • the accumulator at the low-temperature accumulator connection point is preferably also connected to a feed water line via which the accumulator is connected in the buffer memory resulting water is fed as feed water to the solar collector steam generator unit.
  • the buffer is connected to the low-temperature storage connection point via a pump with the feedwater ⁇ line.
  • the connection preferably takes place via controllable valves.
  • the pump is controlled by a control device suitable for the valves.
  • a steam cooling device (hereinafter also referred to as “end steam cooling device”) is arranged in the steam line system between the abovementioned high-temperature storage connection point at which the steam is conducted into the intermediate store and the steam turbine.
  • the solar thermal power plant a control ⁇ device on which is formed so as to drove the be ⁇
  • the temperature of the superheated steam controlled to a Turbi ⁇ NEN-steam temperature by the steam first in the solar collector steam superheating unit to above the Superheater final temperature is superheated and is then cooled by means of the final steam cooling device to the turbine steam temperature in a corresponding preferred operating method so the temperature of the superheated steam beispielswe ise under measurement of a current actual temperature to a given turbine live steam temperature (as target temperature) regulated by the steam is first superheated to a lying above the Tur ⁇ binen fresh steam temperature steam superheater end temperature and then cooled only in a arranged behind the solar collector steam superheater steam cooling device controlled to the turbine live steam temperature.
  • the live steam temperature can thus be kept constant within certain limits even when the end steam cooling device is completely deactivated, even if the steam supplied by the solar collector steam superheater unit is below the live steam temperature lies. This means that even with a partial performance of the solar collector steam generator unit and / or the solar collector steam superheater unit, the fresh steam temperature for the door ⁇ bine easier in predetermined limits can be maintained. This increases the availability and operational flexibility of the entire solar thermal power plant.
  • this arrangement takes place while the Supplying the steam from the intermediate storage in the steam line system during the removal operating mode preferably at the first high-temperature storage connection point itself, ie at the same connection point at which the steam is also supplied to the memory in the storage mode of operation.
  • This can be used in any case within the steam line system angeord ⁇ designated end steam cooling device to cool and the next from the buffer superheated steam during the removal operation mode temperature to the appropriate Frischdampftempe-.
  • Another advantage of the arrangement is that when a short-term requirement of power reserves (so-called “seconds reserve”) stored in the long-term storage thermal see energy can be used to additional steam production, even if no temperature drop of coming from the solar panel steam superheater steam before ⁇ is, but merely to increase power, the amount of steam to be increased.
  • the vapor additionally produced can then be mixed into the steam circuit before the final steam cooling means the Hauptdampfström and be brought into the cooling device to the main steam temperature. Due to the advantageous coupling of the latch to the Steam line system before the final steam cooling device can thus be ensured in a simple manner, a constant live steam ⁇ temperature during the provision of seconds reserve.
  • the live steam temperature can also be maintained longer in an operating mode by the steam cooling device, in which, in times of low sunshine, e.g. As in the evening, continues to produce steam and electricity is produced.
  • a lowering of the temperature of the live steam via the steam cooling device and accepted by the turbine would also be possible with this arrangement, for B. if the cache is to be emptied in night mode.
  • the superheated steam is the steam circuit from the buffer at a second high-temperature storage junction leads conces- which is disposed in the steam circuit between the "end steam cooling means" and the turbine.
  • the yes should have a temperature above the steam temperature at the main steam temperature, a steam cooling device. It is true that with such further Supply line to the second high-temperature storage connection point and a second steam cooling device additional
  • the opening of the valve in response to a pre give ⁇ NEN mass flow setpoint in the steam circuit before the steam turbine is regulated.
  • the opening of the valve is regulated to a constant pressure upstream of the steam turbine.
  • the buffer is also connected by opening a valve with the steam line between the solar collector steam superheater unit and the steam turbine, but preferably here the opening of the valve is controlled to a constant temperature in the steam ⁇ line system at the high-temperature storage connection point. If the supply of steam from the Intermediate storage at the first high-temperature storage connection point, ie before the end steam cooling device, at which the steam is also led from the steam line system into the memory, it can be ensured in this way ⁇ the that before the last steam cooling device, the temperature already on a kept as constant as possible, so that in the context of temperature control using the final steam cooling device no large control fluctuations occur.
  • the heat accumulator can be constructed in different ways.
  • PCM phase change material
  • the heat-storing medium of a PCM memory can, for. B. from salts or already molten salts.
  • a phase change of the salts between a solid and a liquid state or the molten salts between a liquid and a gaseous state is used here to store thermi ⁇ specific energy.
  • Conversely is released during a phase ⁇ transition from gaseous to liquid or liquid to solid thermal energy.
  • the heat transfer between the steam and the storage medium for example, within a heat exchanger, preferably in a tube register, take place.
  • the buffer may also include at least one heat storage in which the thermal energy is stored or released again from a storage medium without phase transition.
  • a heat storage medium for example, high-temperature concrete can be used as the storage medium here.
  • the heat transfer in a heat exchanger preferably within a tube register, are performed.
  • the buffer memory comprises a plurality of storage stages for receiving and emitting thermal energy.
  • particular ⁇ DERS preferably composed of at least two of the memory stages functionally different. Ie.
  • one memory level is constructed as PCM memory and another is
  • the steam is stored in one of the storage stages
  • the storage stages are preferably constructed functionally parallel to the solar collector-steam generator unit with the downstream solar panel steam superheater unit. That is, for example, the buffer is parallel to the So ⁇ larfeldern in a kind of by-pass between the feed water supply line and the steam line system upstream of the turbine located and is graded in a manner similar to a ⁇ individual steps in the solar fields.
  • a storage stage is arranged parallel to the solar collector-steam generator units, in which steam condenses in the storage operating mode and water is evaporated in boss istsmodus and paral ⁇ lel to the solar collector steam superheater units then the storage stages are arranged, which cool the superheated steam in Speicher Stahlsmo ⁇ ; In recovery mode, overheat the steam again. It is clear that the condensation of steam in the low-temperature side last memory stage is only possible if the light coming from the pre-turn ⁇ th memory stage steam is sufficient till ⁇ cools and the last memory level is still able, extract enough energy from the steam. Because of he ⁇ inventive coupling of the latch on the low temperature side to a capacitor or an expansion device, and optionally other connection points but the water can, as explained above, regardless of the temperature and pressure conditions and the physical state
  • the single figure shows a schematic block diagram of a solar thermal power plant according to a preferred embodiment of the invention.
  • the figure shows a simplified solar thermal power plant with direct evaporation.
  • This has a solar collector steam generator unit 2 formed from a plurality of solar collector strands for the evaporation of feed water, which is supplied via a feedwater line.
  • the solar collector-boiler unit 2 is followed by a likewise formed of sev- eral solar panel solar collector strands steam superheating unit 4 to superheat the generated from the Son ⁇ nenkollektor steam generator steam unit 2 to about ⁇ .
  • a steam separator 3 in which residual water still present in the steam is separated off and fed back to the feedwater line 10 via a return line 11 with a pump 9.
  • the steam coming from the solar panel steam superheater unit 4 is supplied to a high pressure turbine 40 via a steam line system 13.
  • a check valve or turbine control valve 18 is located over an output shaft in front of the turbine inlet 41, the turbine 45 is connected to a 40 Ge ⁇ gear 46, which in turn is connected to a generator 62 connected to convert the kinetic energy of the drive shaft into electrical energy.
  • the steam used in the high-pressure turbine 40 is then routed in stages at different outputs of the high-pressure turbine 40 in output steam lines 42, 43, 44, which lead to heat exchangers 47, with which the feed water for the solar collector-steam generator unit 2 preheated can be.
  • a part of the steam from the steam output line 44 is fed to 50 to use the steam further to Encrypt ⁇ lung in electric power a turbine input 56 of a low pressure turbine.
  • An output shaft 53 of this low-pressure turbine 50 is also connected to the generator 62 for this purpose.
  • a separator 52 to separate condensed water, and a heat exchanger 51, in which the steam is heated again (reheated) before it is the low-pressure turbine 50 is fed.
  • a valve 54 in front of the turbine inlet 56 the pressure at the inlet of the low-pressure turbine 50 can be regulated. 50 supplying the steam for the low-pressure turbine in the heat exchanger 51 more thermal energy, this is traversed by steam, which is branched off via a diverter valve 48 in a branch ⁇ line 49 seen from the upstream se for the high-pressure turbine 40 superheated steam becomes.
  • the steam coming from the branch line 49 condenses in the furnishedtau ⁇ shear 51 and is fed via a line 55 via the heat exchanger 47 a feedwater tank 63.
  • the low-pressure turbine 50 also has at several turbine stages a plurality of outputs which are connected to output steam lines 57, 58, 59, 60, 61.
  • An output steam line 57 leads into the feedwater tank 63.
  • Another output steam line 61 which is located at the very end of the low pressure turbine 50, ie the line with the lowest vapor pressure, leads to a condenser 65, which via another heat exchanger 67 with a Cooling tower 68 is connected.
  • the residual steam condenses to water, which is supplied via a pump 69 to the feedwater tank 63.
  • several heat exchangers 70 can pass, which are supplied with residual steam via the outlet steam lines 58, 59, 60 from the low-pressure turbine 50.
  • the residual steam also condenses to water, which is mixed at the mixing point 66 with the condensed water in the condenser 65 and this is supplied via the pump 69 in turn through the heat exchanger 70 to the feedwater tank 63. This effectively condenses the water and keeps it at a high temperature (below the steam temperature) without giving away the thermal energy in the residual steam.
  • the feed water tank 63 is also supplied with the condensed in the other heat exchangers 51, 47 water.
  • the feed water is then fed back to the solar panel steam generator unit 2 via a feedwater line 10 by means of a feed water pump 64, so as to close the circuit.
  • the solar collector-steam generator unit 2 consists here, as already mentioned, of several strands of individual solar panels 5. This may be, for. For example, parabolic trough collectors or Fresnel collectors. Shown here are only four strands, each with three collectors 5. In reality, such a solar thermal power plant will have a variety of other solar collector strands with a significantly higher number of solar panels. Possibly. There are also several collector strands grouped into spatially separated solar fields and the steam generated therein is mixed behind the solar fields before entering the solar collector steam superheater units. In this case, the individual solar fields for generating steam each own solar panels are assigned to overheat the steam. Ie.
  • the solar collector steam superheater unit 4 consists of several solar collector strands, each with a plurality of solar panels 6V, 6E.
  • pre-superheater solar panels 6V
  • final superheater the solar panels 6E to end superheater solar panels 6E
  • injection coolers which are shown schematically here by an injection point 7.
  • injection point 7 water is injected for cooling, so as to regulate the output ⁇ temperature TD at the end of the final superheater 6E, ie the steam superheater end temperature TD to a predetermined value.
  • a control device 19 which inter alia receives the measured at a temperature measuring point 34 behind the final superheater 6E steam superheater end temperature TD as the current actual temperature and regulated to a predetermined target temperature by an intermediate injection control signal ZKS to a control valve outputs, which regulates the water to ⁇ drove to the injection coolers at the injection point.
  • the control can in principle be carried out separately for each collector strand, if the injection cooler of the collector strands are each supplied via separately controllable valves.
  • the cooling water can be removed, for example via adewas ⁇ sertechnisch 12 behind the pump 9 for returning the condensed water from the water separator 3.
  • the control device 19 may for this purpose one or more control devices (not shown) which entwe ⁇ the discrete electronic components in the form of individual or integrated into a computer in the form of software can be implemented.
  • This control device 19 may obtain another measurement data from the entire pipe system, such as the current pressure in the solar collector steam generator unit, in the solar collector steam superheater unit or Dampflei ⁇ processing system upstream of the turbine 40.
  • the desired temperature to which the steam superheater final temperature TD should always be higher than the required fresh steam temperature for the steam turbine 40.
  • a further actual temperature in this case, the actual live steam temperature TE, is measured at a temperature measuring point 35 behind the end injector 15 and measured with a setpoint temperature value, i. here with the setpoint value of the required for the turbine 40 live steam temperature, which the control device 19 is given for example by the block control of the turbine gets compared. Accordingly, the Endinspritzer 15 is then driven.
  • a high-temperature Storage connection HAI to which a buffer 20 is connected via a controllable valve 25.
  • This buffer 20 consists of several storage stages Sl, S2, S3 with different heat accumulators 22, 23, 24, which are connected in a chain in series.
  • the individual heat storage 22, 23, 24 may be constructed differently and also work differently. In the present case it is for all heat accumulators 22, 23, 24 to such a memory, the escape the guided medium by thermal energy for storage or thermal energy again consider ⁇ ben to the conducted medium, if necessary.
  • This may for example, be heat storage, which operate without a phase change of energiespei ⁇ chernden medium, eg. As solid state memory such as high-temperature concrete storage, or to PCM memory with storage media that perform a phase change in the energy storage.
  • solid state memory such as high-temperature concrete storage, or to PCM memory with storage media that perform a phase change in the energy storage.
  • An example of this is a storage facility with molten salt as storage medium, which undergoes a phase change to a gaseous state for energy storage.
  • the heat storage 22, 23 of the first two storage stages Sl, S2 are constructed as non-phase-change memory and the heat storage 24 in the storage stage S3 as a PCM memory.
  • other arrangements are mög ⁇ Lich.
  • the latch 20 is connected to two low-temperature connection points NAl, NA2 with the feedwater line 10.
  • the connection to the first low-temperature storage connection point NAl via a first valve 31, a pump 26 and a second valve 27.
  • a parallel connection to a second low-temperature storage connection NA2 takes place only via a third valve 28, ie without an intermediate ⁇ circuit of a pump.
  • the buffer 20 on the low-temperature side is connected at a branch point 30 via a fourth valve 32 to a line 80 which leads to a low-pressure storage connection NA3 on the capacitor 65 of the power plant.
  • a flash tank 81 is connected here, in which the medium coming from the line 80 from the buffer is atmospherically expanded.
  • the medium is supplied to the capacitor 65, can also be dispensed with this expansion tank 81.
  • the line 80 can be shut off to the expansion tank 81 or to the condenser 65.
  • the line 80 is connected via separate controllable ⁇ valves 82, 83, 84, 85, 86, 87 to different steam lines within the power plant block. As an example, it is shown here that part of the
  • All valves 27, 28, 31, 32, 82, 83, 84, 85, 86, 87, 88 of the low-temperature side of the buffer 20 are controlled as well as the valve 25 on the high-temperature side of the intermediate ⁇ memory 20 by a memory controller 21.
  • This also receives as a further input signal, a temperature SNT of the steam, which is measured at a temperature measuring point 36 on the low temperature side of the intermediate storage ⁇ chers 20.
  • This memory control device 21 in turn is in contact with the control device 19 via a communication connection 17, so that these two control signals Facilities 19, 21 work in a coordinated manner.
  • the memory controller 21 may also be formed as a subcomponent of the control device 19.
  • the first valve 27 is opened at the low-temperature storage connection point NA1 and the pump 26 is put into operation.
  • the valve is opened regulated at the high-temperature storage junction HAI 25, wherein a re ⁇ gelung the open position of the valve 25 is preferably carried out mass senstromgeregelt.
  • a required mass flow measuring device is provided accordingly (not shown in the figure).
  • a pressure-controlled ⁇ tes opening of the valve 25 is conceivable, so that the pressure within the steam line system 13 remains as constant as possible.
  • the pressure p is measured at a pressure measuring point 33 and supplied to the storage control device 21, so that the valve 25 can be regulated accordingly.
  • this is coordinated with an already effective Druckre ⁇ gelung on the steam turbine valve.
  • the buffer 20 is already significantly charged with thermal energy and the low temperature side last storage stage S3 is no longer able to remove so much heat from the supplied steam that it completely condenses. It is then a water / steam mixture.
  • this state can be detected by the Spei ⁇ cher control device 21.
  • the valves 27, 31 to the first low-temperature storage junction ⁇ NA1 are then closed and the pump is stopped 26 and instead be the valve 32 to the line 80 and open the valve 88 before the flash tank 81st
  • the water / steam mixture is thermally expanded and forwarded to the condenser 65 at the third low-temperature storage connection point NA3.
  • the expansion tank 81 in front of the condenser 65 is optional and that the water / steam mixture can also be fed directly to the condenser 65 if the condenser 65 is designed accordingly.
  • an additional pressure measurement (not shown) may be checked by the memory controller 21 determines whether the temperature and pressure of the steam at the low temperature side of the buffer 20 corresponds approximately to the temperature and the pressure in one of the steam lines 42, 43, 44, 58, 59, 60 of the further low-temperature connection points NA4, NA5, NA6, NA7, NA8, NA9. If so, the valve 88 in front of the flash tank 81 and the condenser 65 is closed again and the corresponding valve 82, 83, 84, 85, 86, 87 opened on the low temperature side. If the pressure and / or temperature conditions are not suitable for any of the lines 42, 43, 44, 58, 59, 60, the valve 88 in front of the expansion vessel 81 or the condenser 65 simply remains open or is opened when it was previously closed ,
  • the latch 20 can be brought to a higher temperature level in total than in a construction in which only a storage operation is possible, as long as the absorption capacity of the last storage stage S3 is sufficient to convert the steam completely in the liquid phase ⁇ .
  • the storage mode of operation can be carried out until the heat accumulator 20 is fully charged, ie can no longer absorb heat energy.
  • the storage operating mode can then be temporarily switched on again in phases for a short time.
  • a maximum steam temperature is defined, with which the temperature SNT at the low-temperature end of the buffer 20 is compared.
  • Such a removal operation mode is the pitch switched at ⁇ when the solar panels with the sun collector steam generator units 2 and solar panel steam superheating unit 4 are not able to achieve a vapor ⁇ superheater finish temperature TD, which is above the required steam temperature to the turbine 40 ,
  • the second valve 28 is opened at the second low-temperature storage connection point NA2 and again the valve 25 is opened controlled at the high-temperature storage connection HAI, but now this is not pressure-controlled, but temperature-controlled in the way that the Temperature is kept at the high-temperature Speicheran- closing point HAI to a constant value above the ei ⁇ cently required live steam temperature.
  • the exact setting of the live steam temperature then takes place as usual on the final injection 15. In this removal operating mode so water from the
  • Feedwater line 10 removed. Given a customary pressure difference between the feedwater line 10 (eg 50-145 bar) and the steam line system 13 (for example 41-110 bar), no pump is expected to be required for water to flow into the buffer memory 20 in the extraction mode of operation
  • the workflow of the intermediate memory 20 thus takes place functionally ⁇ in the same order as in the parallel switched solar collector-steam generator unit 2 with the downstream solar panel steam superheater unit 4, as can be seen easily from Figure 1.
  • the entire solar thermal power plant 1 not only in addition to the illustrated solar collector strands or solar fields have more solar fields, which are connected in parallel and superheated steam supply the Dampflei ⁇ processing system 13 in front of the turbine 40, but also several parallel memory 20, which also separately depending According to Be ⁇ may be operated in the various operating modes.
  • an optional bypass 14 from the high-temperature side end of the buffer 20 to a high-temperature connection point HA2 behind the Endin ⁇ splitter 15 is located.
  • This bypass 14 is opened over a se ⁇ parates valve 29th Behind this valve 29 is a separate bypass injection cooler 16 for reducing the temperature of the coming out of the buffer 20 steam.
  • the additional bypass injection cooler 16 is also controlled by the control device 19 and the valve 21 by the memory controller 29
  • the bypass 14 can be used in the extraction operation mode the overheated over ⁇ vapor not before the Endeinspritzung 15 via the valve 25 into the Admit steam line system 13, but instead via the valve 29 and the additional bypass injection cooler 16 already set exactly to the desired Frisch ⁇ steam temperature adjusted steam to the turbine 40.
  • any other direct or indirect processing ⁇ tends solar panels used.
  • use in connection with the newer solar tower technology with direct evaporation is possible.
  • the above-mentioned temperature and pressure ranges are merely exemplary and not restrictive. It is critically dependent on the available types and materials of storage, up to which temperatures and pressures the invention can be used.

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  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Development (AREA)
  • Sustainable Energy (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 une centrale héliothermique (1) comprenant une unité de génération de vapeur à capteurs solaires (2) destinée à générer de la vapeur, une unité de surchauffe de vapeur à capteurs solaires (4) montée en aval de l'unité de génération de vapeur à capteurs solaires (2) et destinée à surchauffer la vapeur, ainsi qu'une turbine à vapeur (40) reliée à une sortie de l'unité de surchauffe de vapeur à capteurs solaires (4) par un système de conduite de vapeur (13), cette turbine à vapeur (40) étant alimentée en vapeur surchauffée pendant le fonctionnement. La centrale héliothermique (1) présente un accumulateur intermédiaire (20) qui est relié au système de conduite de vapeur (13) au moins en un premier point de raccordement à l'accumulateur haute température (HA1) disposé entre l'unité de surchauffe de vapeur à capteurs solaires (4) et la turbine à vapeur (40) pour soutirer de la vapeur surchauffée du système de conduite de vapeur (13) dans un mode de fonctionnement d'accumulation. L'accumulateur intermédiaire (20) comprend un accumulateur thermique (22, 23, 24) dans lequel de l'énergie thermique est extraite de la vapeur introduite dans le mode de fonctionnement d'accumulation, et accumulée, et dans lequel l'énergie thermique accumulée est à nouveau fournie à la vapeur dans un mode de fonctionnement de soutirage, cette vapeur étant acheminée de l'accumulateur intermédiaire (20) au système de conduite de vapeur (13). L'accumulateur intermédiaire (20) est par ailleurs relié à un condensateur (65) et/ou à un dispositif de détente (89) de la centrale héliothermique (1) en un point de raccordement à l'accumulateur basse température (NA3). L'invention concerne en outre un procédé pour faire fonctionner une centrale héliothermique (1) de ce type.
EP10787397A 2009-12-22 2010-12-01 Centrale héliothermique et procédé pour faire fonctionner une centrale héliothermique Withdrawn EP2516854A2 (fr)

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DE102009060091 2009-12-22
PCT/EP2010/068618 WO2011080021A2 (fr) 2009-12-22 2010-12-01 Centrale héliothermique et procédé pour faire fonctionner une centrale héliothermique

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US (1) US20120255300A1 (fr)
EP (1) EP2516854A2 (fr)
CN (1) CN102762858A (fr)
AU (1) AU2010338478A1 (fr)
CL (1) CL2012001726A1 (fr)
WO (1) WO2011080021A2 (fr)

Families Citing this family (23)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20110203575A1 (en) * 2009-08-24 2011-08-25 Robert Emery Thermodynamic/Solar Steam Generator
US20130307273A1 (en) * 2011-02-08 2013-11-21 Brightsource Industries (Israel) Ltd. Solar energy storage system including three or more reservoirs
DE102011000946A1 (de) * 2011-02-25 2012-08-30 Hitachi Power Europe Gmbh Solarthermische Energieerzeugungsanlage und Verfahren zur Energiegewinnung mittels einer solarthermischen Ernergieerzeugungsanlage
EP2525051A1 (fr) * 2011-05-20 2012-11-21 Alstom Technology Ltd Centrale solaire thermique
US20130111902A1 (en) * 2011-11-03 2013-05-09 Mansour Maleki-Ardebili Solar power system and method of operating a solar power system
EP2647841B1 (fr) 2012-04-02 2020-09-23 General Electric Technology GmbH Système d'énergie solaire
DE102012209139A1 (de) * 2012-05-31 2013-12-05 Man Diesel & Turbo Se Verfahren zum Betreiben einer Solaranlage
AU2013291157B2 (en) * 2012-07-17 2016-08-18 Mitsubishi Power, Ltd. Solar power system
IL222613B (en) * 2012-10-22 2019-03-31 Newco 2Fuels Ltd Solar-gas combined cycle system for generating electrical power
DE102012111775B4 (de) * 2012-12-04 2016-08-04 Deutsches Zentrum für Luft- und Raumfahrt e.V. Solarthermische Dampferzeugungsstufe, solarthermisches Kraftwerk und Verfahren zum Betreiben einer solarthermischen Dampferzeugungsstufe
DE102012023898A1 (de) * 2012-12-07 2014-06-12 Man Diesel & Turbo Se Verfahren zum Betreiben einer Anlage zur Erzeugung mechanischer und/oder elektrischer Energie
CN103115445B (zh) * 2013-02-05 2014-09-24 中盈长江国际新能源投资有限公司 太阳能自动均热聚热管、槽式组件、热发电系统和工艺
CN104279537B (zh) * 2013-07-11 2017-08-25 上海工电能源科技有限公司 一种再热太阳能热利用系统及其运行方式
US10030636B2 (en) * 2013-05-27 2018-07-24 Stamicarbon B.V. Acting Under The Name Of Mt Innovation Center Solar thermal energy storage system
US20150089945A1 (en) * 2013-10-01 2015-04-02 Chevron U.S.A., Inc. Hybrid solar and fuel-fired steam generation system and method
PT2910781T (pt) * 2014-02-24 2021-07-07 General Electric Technology Gmbh Sistema de energia solar térmica
DE102014205629B4 (de) * 2014-03-26 2023-08-03 Siemens Energy Global GmbH & Co. KG Mehrgrößenzustandsregelung für einen Dampferzeuger eines Dampfkraftwerks
ES2565690B1 (es) * 2014-09-05 2017-01-20 Abengoa Solar New Technologies,S.A. Método y sistema de almacenamiento térmico para planta solar de generación de vapor y planta solar de generación de vapor
CN104456528A (zh) * 2014-11-05 2015-03-25 江苏太阳宝新能源有限公司 综合利用储能和智能电网的方法及其系统
EP3093488A1 (fr) * 2015-05-13 2016-11-16 Areva Solar, Inc Centrale d'énergie solaire thermique avec un appareil à accumulation de chaleur et procédé associé
JP2017014971A (ja) * 2015-06-30 2017-01-19 三菱日立パワーシステムズ株式会社 太陽熱発電システム及び太陽熱発電方法
US10987609B1 (en) * 2018-02-11 2021-04-27 John D. Walker Polar-linear-fresnel-concentrating solar-thermal power and desalination plant
US20230294014A1 (en) * 2019-02-11 2023-09-21 John D. Walker Enhanced power and desalination performance in medx plant design utilizing brine-waste and single-temperature- thermal energy storage coupled to thermal vapor expander

Family Cites Families (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4192144A (en) * 1977-01-21 1980-03-11 Westinghouse Electric Corp. Direct contact heat exchanger with phase change of working fluid
BE895148A (fr) * 1982-11-26 1983-03-16 Belgonucleaire Sa Cycle thermodynamique a vapeur pour la refrigeration des centrales solaires a recepteur central
JPH10318122A (ja) * 1997-05-22 1998-12-02 Takashi Uesugi 太陽光を利用した発電装置及び照明装置
SE0004930D0 (sv) * 2000-12-29 2000-12-29 Addpower Ab Soldriven turbinloop
US20070157614A1 (en) * 2003-01-21 2007-07-12 Goldman Arnold J Hybrid Generation with Alternative Fuel Sources
DE10329623B3 (de) * 2003-06-25 2005-01-13 Deutsches Zentrum für Luft- und Raumfahrt e.V. Verfahren zur solarthermischen Gewinnung elektrischer Energie und solarthermisches Kraftwerk
JP4659818B2 (ja) * 2004-03-15 2011-03-30 オルハン ウストゥーン 電気エネルギーへの変換のための熱エネルギー蓄積装置
US20070221208A1 (en) * 2006-03-07 2007-09-27 Goldman Arnold J High-temperature pipeline
US20080092551A1 (en) * 2006-10-18 2008-04-24 Mark Joseph Skowronski Method and system integrating combustion turbine with a regenerative solar rankine power plant
WO2008114248A1 (fr) * 2007-03-16 2008-09-25 T.O.U Millennium Electric Ltd. Génération d'énergie thermique solaire combinée et station énergétique prévue à cet effet
US8001960B2 (en) * 2007-11-12 2011-08-23 Brightsource Industries (Israel) Ltd. Method and control system for operating a solar power tower system
CN101307751A (zh) * 2008-07-03 2008-11-19 昆明理工大学 混合工质分散式低温太阳能热力发电系统及发电工艺
CN201318255Y (zh) * 2008-10-30 2009-09-30 常州宣纳尔新能源科技有限公司 太阳能综合利用系统

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See references of WO2011080021A2 *

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CN102762858A (zh) 2012-10-31
US20120255300A1 (en) 2012-10-11
WO2011080021A2 (fr) 2011-07-07
AU2010338478A1 (en) 2012-08-09
WO2011080021A3 (fr) 2012-03-08

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