EP1368555A1 - Procede d'utilisation d'un groupe vapeur et groupe vapeur correspondant - Google Patents

Procede d'utilisation d'un groupe vapeur et groupe vapeur correspondant

Info

Publication number
EP1368555A1
EP1368555A1 EP02719925A EP02719925A EP1368555A1 EP 1368555 A1 EP1368555 A1 EP 1368555A1 EP 02719925 A EP02719925 A EP 02719925A EP 02719925 A EP02719925 A EP 02719925A EP 1368555 A1 EP1368555 A1 EP 1368555A1
Authority
EP
European Patent Office
Prior art keywords
condensate
steam
preheating
partial
turbine
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.)
Granted
Application number
EP02719925A
Other languages
German (de)
English (en)
Other versions
EP1368555B1 (fr
Inventor
Tilman Abel
Dieter Blanck
Georg Haberberger
Imke Riebeck
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
Priority to EP02719925A priority Critical patent/EP1368555B1/fr
Publication of EP1368555A1 publication Critical patent/EP1368555A1/fr
Application granted granted Critical
Publication of EP1368555B1 publication Critical patent/EP1368555B1/fr
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

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
    • F01K7/00—Steam engine plants characterised by the use of specific types of engine; Plants or engines characterised by their use of special steam systems, cycles or processes; Control means specially adapted for such systems, cycles or processes; Use of withdrawn or exhaust steam for feed-water heating
    • F01K7/34—Steam engine plants characterised by the use of specific types of engine; Plants or engines characterised by their use of special steam systems, cycles or processes; Control means specially adapted for such systems, cycles or processes; Use of withdrawn or exhaust steam for feed-water heating the engines being of extraction or non-condensing type; Use of steam for feed-water heating
    • F01K7/40—Use of two or more feed-water heaters in series

Definitions

  • the invention relates to a method for operating a steam power plant, wherein steam generated in a boiler is deposited in a condenser after flowing through at least one turbine, the condensate obtained is preheated and fed back to the boiler as feed water.
  • the invention further relates to a steam power plant for performing the method.
  • a steam power plant is usually used to generate electrical energy or to drive a work machine.
  • a working medium usually a water / water / steam mixture, which is carried in an evaporator circuit of the steam power plant is evaporated in an evaporator or steam generator (boiler). The steam generated thereby relaxes in a steam turbine, and is then fed to a condenser. The working medium condensed in the condenser is then fed again to the boiler for steam generation via a pump.
  • partial steam mass flows from the turbine steam quantity are used to gradually preheat the condensate used as feed water to near the boiling temperature, as a result of which the thermodynamic efficiency of the entire process increases. Due to the steam extraction from the turbine steam quantity, the subsequent steam turbine stages can, however, draw less power from the steam fluid.
  • EP-A2-1 055 801 a method for operating a steam power plant is known in which the partial steam mass flows from the turbine steam quantity preheat the condensate used as feed water to near the boiling point becomes.
  • the waste heat from fuel cells is used to preheat the condensate.
  • preheating which is relatively complex in terms of design and cost is achieved by the external supply of heat via the fuel cells.
  • the object of the invention is to provide a method of the type mentioned at the outset, in which preheating of the boiler feed water to be fed to the boiler while at the same time increasing the power of the turbine can be achieved.
  • Another object of the invention is to provide a steam power plant with which such an operating method can be carried out.
  • the invention is based on the consideration that to increase the output of a turbine connected to a steam power plant, the steam mass flow through the turbine on the one hand and on the other hand the preheating temperature of the boiler feed water supplied to the boiler must be taken into account. Both process sizes are linked to each other by the tapping of the turbine, which is usually carried out in steam power plants, whereby a partial steam mass flow for preheating the condensate obtained is taken from the steam turbine process. This steam extraction is at the expense of the performance of the turbine, in particular the overall efficiency of the steam power plant.
  • the condensate obtained in the condenser is completely preheated in the known systems by means of bleed steam, and preheated to a temperature as high as possible close to the boiling temperature before it is fed to the boiler as boiler feed water. This rigid coupling of the preheating of the condensate with the steam extraction determines the performance of the turbine at constant fresh steam pressure.
  • the invention now shows a completely different way of increasing the output of the turbine of a steam power plant, if required, by flexibly adjusting the preheating temperature as required by mixing partial flows of condensate.
  • the condensate flow is divided into a first partial flow and a second partial flow, only the first partial flow being preheated and the second partial flow being admixed again with the preheated first partial flow.
  • partial flow is to be understood here as a real partial flow of the condensate deposited in the condenser.
  • a preheating of the entire condensate can be achieved with a mixing temperature that is lower than the temperature of the preheated first sub-stream of condensate before mixing with the second sub-stream.
  • the mixing temperature can advantageously be flexibly adjusted by setting the partial flows.
  • Process heat in the form of a higher steam mass flow through the turbine is thus available to increase the performance of the turbine Available.
  • the method for the first time there is the possibility of increasing the output of the turbine up to the boiler reserve (not the seconds reserve) of a steam power plant as required, if necessary, by partially and selectively bypassing the second partial flow of condensate from the preheating without having to raise the live steam pressure above the design value.
  • the first partial flow and the second partial flow can advantageously be flexibly adjusted during the division, as a result of which more or less process steam is available in the turbine for performing work.
  • a further advantage is the fact that the solution presented makes it possible for the first time to achieve an increase in output by partially flowing through the preheating section without restricting the service life of the components, in particular the preheating devices of the steam turbine system.
  • this results in a significantly more efficient heat consumption than with a total bypass of the preheating section, in which, at least temporarily, no condensate is preheated, i.e. the first partial flow is 0. This is important, for example, for high-pressure preheaters or the like.
  • the first partial flow is preheated with bleed steam from the turbine. Preheating only the first partial stream with bleed steam from the turbine ensures that only a smaller amount of bleed steam is required for preheating than conventional bleed. This means that more process steam is immediately available in the steam turbine to increase the power of the turbine.
  • the condensate mass flow of the first partial flow advantageously correlates directly with the bleed steam mass flow, so that the larger the first partial flow, the greater the amount of Tapping steam required to preheat the first substream to a desired temperature.
  • the first partial flow is preheated in at least two stages.
  • a desired temperature of the first partial flow after the preheating can be set exactly.
  • all preheating stages or only a part of the preheating stages can be provided for preheating the first partial stream.
  • the precise setting of a desired temperature of the first partial flow after preheating and before mixing with the second partial flow also enables the mixing temperature to be set precisely when the partial flows are mixed, so that the preheating temperature of the boiler feed water can be set accordingly.
  • the preheating of the first partial strand is also possible in only one stage, in particular in exactly one stage.
  • a preheating temperature of the boiler feed water of 210 ° C. to 250 ° C., in particular from 220 ° C. to 240 ° C., is preferably set.
  • the pressure of the boiler feed water is typically around 300 bar.
  • the preheating temperature of the boiler feed water is reduced by approximately 30 ° C. to 70 ° C. by mixing with the second, non-preheated partial flow.
  • the first partial stream and the second partial stream are divided in a ratio of 0.4 to 0.8, in particular in a ratio of 0.6 to 0.7.
  • the condensate obtained in the condenser is divided such that the first partial flow of condensate is approximately 60% and the second partial flow of condensate is approximately 40%.
  • the first partial stream is preheated from a temperature of approximately 200 ° C. to a temperature of approximately 280 ° C., while the second partial stream is not preheated and therefore remains at a temperature of 200 ° C. until it is mixed with the first partial stream.
  • the pressure of the condensate flows remains largely unchanged at around 300 bar.
  • the preheating temperature of the feed water to be fed to the boiler can be adjusted as required by metering the second substream around the preheating section and mixing the two substreams after preheating the first substream.
  • the division of the partial flows is preferably carried out in a controlled or regulated manner.
  • the mixture is fed as boiler feed water to a fossil-fired steam generator.
  • the method of the invention is particularly intended for use in steam power plants which have a boiler which is fired with a fossil fuel, for example coal or oil.
  • a steam power plant for carrying out the method described above, comprising a boiler for generating steam, at least one turbine, a condenser connected downstream of the turbine on the exhaust side, a condensate line for returning the condensate to the boiler and one in the Condensate line switched preheater device for preheating condensate, a bypass line bypassing the preheating device being provided, so that the preheating device can only be acted upon with a first partial flow of the condensate.
  • bypass line which bypasses the preheating device ensures that the preheating device is only acted upon by the first partial flow of condensate, while a second partial flow flows through the bypass line without preheating.
  • Bypass line is understood here to mean that it is routed parallel to the preheating device, the bypass line branching upstream from the preheating device from the condensate line and reconnected downstream of the preheating device to the condensate line.
  • a branch point is provided upstream of the preheating device, while a mixing point is arranged downstream of the preheating device.
  • the condensate from the condenser can be divided at the branch into the first partial flow and a second partial flow that is complementary to the total condensate flow.
  • the first condensate flow is conducted in relation to the direction of flow of the condensate after the branch in the condensate line, into which the preheating device for preheating the first condensate flow is connected.
  • the second condensate stream and the preheated first condensate stream are at the mixing point, i.e. at the downstream connection point of the bypass line to the condensate line, miscible, a mixing temperature depending on the mass flow of the first and the second partial flow of condensate and depending on the heat absorption of the first condensate flow in the preheating device.
  • the preheating device is connected to the turbine via a bleed line.
  • a bleed line This enables a direct coupling of bleed steam as a preheating medium in the heat exchange with the first partial flow of condensate in the preheating device of the steam power plant. enough.
  • the thermal energy required for preheating can be set directly via the bleed steam mass flow, the bleed steam mass flow depending on the size of the mass flow of the first partial flow. The larger the first partial flow, the greater the heat requirement in the preheating device and thus also the amount of bleed steam which is withdrawn from the turbine.
  • the bypass line preferably has a control valve for controlling a second partial flow of the condensate bypassing the preheating device.
  • the control valve serves to regulate or also to preset the second partial flow, which does not flow through the preheating device and therefore does not lead to the extraction of bleed steam.
  • the second partial flow can be precisely adjusted via the control valve in the bypass line and therefore also the amount of heat required for preheating the second partial flow complementary to the first partial flow in the preheating device.
  • the mixing temperature which is established when the partial streams are mixed at the mixing point in the condensate line is advantageously controllable with the control valve. As a result, depending on the need by which the power of the steam turbine is to be increased, the amount of the second partial flow bypassing the preheating device in the bypass line can be adjusted, in particular regulated in a corresponding control loop.
  • the bypass line preferably opens into the condensate line downstream of the preheating device.
  • the confluence is at the same time the mixing point at which the first partial flow is mixed with the second partial flow, a desired preheating temperature of the boiler feed water to be supplied to the boiler being set automatically after the mixing.
  • the preheating device preferably has at least one heat exchanger, in particular a high-pressure preheater.
  • a plurality of heat exchangers can also be connected in series, thereby heating the first part in several stages. Allow flow of condensate.
  • the heat exchanger is designed as a high-pressure preheater of a steam power plant
  • the preheater is pressurized with condensate at a pressure of approximately 300 bar and assigned to a high-pressure stage of the turbine.
  • the turbine can also have a high-pressure sub-turbine and / or a medium-pressure sub-turbine and / or a low-pressure sub-turbine.
  • the system concept of the invention can therefore be applied very flexibly to different steam power plants, which comprise a combination of different turbine types (high-pressure, medium-pressure, low-pressure turbines) with corresponding preheating devices.
  • a bypass line which can be activated via a quick-action fitting is preferably connected in parallel with the preheating device.
  • This bypass line is provided for a complete bypassing of the preheating device with condensate in the event of a quick-close event, for example in an emergency situation when the preheating device is in danger of flooding or overheating.
  • the bypass line can be activated, ie enabled, via the quick-closing fitting, at the same time interrupting the flow of condensate in the condensate line to the preheating device.
  • the quick-action fitting is designed, for example, as a three-way fitting which leads at least the first partial flow of condensate after activation via the bypass line, so that condensate is no longer preheated in the preheating device.
  • the bypass line is not activated, so that the first partial flow is delivered to the preheating device via the condensate line.
  • the bypass line which can be activated via the quick-action fitting provides increased operational reliability of the steam power plant, in particular in combination with the bypass line according to the invention. Further advantages of the steam power plant result in an analogous manner to the advantages of the operating method of the steam power plant described above.
  • Steam turbine 5 and a boiler 3 for generating steam D The turbine 5 is followed by a condenser 7 on the exhaust side via an exhaust line 51.
  • the steam power plant 1 has a condensate line 13 which is connected to the condenser 7 on the output side.
  • a first pump 41, a feed water tank 45 and a second pump 43 are connected in succession in the condensate line 13 in the flow direction of the condensate.
  • a preheating device 15 for preheating condensate K is connected in the condensate line 13.
  • the preheating device 15 is arranged upstream of the boiler 3 in the flow direction of the condensate K.
  • the preheating device comprises a first preheating stage 9A and a second preheating stage 9B following the first preheating stage.
  • the preheating stages 9A, 9B are designed as respective heat exchangers 23A, 23B.
  • the boiler 3 has a fossil-fired steam generator 11, which comprises a fuel supply 53 for supplying a fossil fuel 29, for example coal or oil.
  • a bleed line 19A leads from a stage of the steam turbine 5 to the heat exchanger 23B.
  • a bleed line 19B leads from a further stage of the turbine 5 to the heat exchanger 23A.
  • a respective amount of bleed steam Ai, A 2 can be fed to the preheating device 15 or the heat exchangers 23A, 23B for preheating condensate K via the bleed lines 19A, 19B.
  • a bypass line 17 bypasses the preheating device 15, the bypass line branching off from the condensate line 13 at a separation point 47, bypassing the preheating device 15 and re-opening into the condensate line 13 at a mixing point 48 downstream of the preheating device 15.
  • a control valve 21 for regulating a umstructureden the preheater 15 substream K 2, hereinafter referred to as a second partial flow K 2, are provided.
  • the control valve 21 has a servomotor 33, via which the desired valve position of the control valve 21 and thus the first partial flow Ki can be set.
  • the condensate K conveyed from the feed water tank 45 via the second pump 43 can thereby be divided into a first partial flow Ki and a second partial flow K 2 , the first partial flow Ki being fed via the condensate line 13 to the preheating device 15 and the second partial flow K 2 bypasses the preheating device 15 via the bypass line 17, so that the preheating device 15 is only supplied with the first partial flow Ki of the condensate K.
  • a sliding valve 37 which is adjustable via a servomotor 33, is connected after the separation point 47 in the condensate line 13 and is open in the normal operating state.
  • a branch line 55 which is connected from the bypass line 17 to the condensate line 13 and has a low-load control valve 35 with an actuating element 35A, is connected in parallel to the slide valve 37. The control valve 35 is closed in normal operation, so that no condensate K passes through the branch line 55.
  • the low-load control valve 35 is provided only for the low-load case, in which case the slide valve 37 is closed and a small amount of condensate K, via the branch line 55, reaches the preheating device 15 via the actuating element 35A of the control valve 35. Furthermore, the preheating device 15 is connected in parallel with a bypass line 27 which can be activated via a quick-action fitting 25. A respective quick-action fitting 25 is connected to the condensate line 13 upstream and downstream of the preheating device 15. The quick-closing fitting 25 can be switched between two settings in a short time via an actuator 31.
  • the fitting 25 is designed as a three-way fitting, the bypass line 27 being closed, ie not activated, in the normal operating state.
  • Condensate K flows in a first partial flow Ki through the preheating device 15 and in a second partial flow K 2 via the bypass line 17.
  • the quick-closing fitting 25 is activated via the actuator 31, the bypass line 27 being released and the condensate flow via the Condensate line 13 is interrupted by the preheating device 15.
  • the preheating device 15 is therefore totally bypassed, ie no condensate K is delivered to the preheating device 15 and thus preheated.
  • the activatable bypass line 27 is used to bypass and thus protect the preheating device 15, in particular the heating surfaces of the heat exchangers 23A, 23B.
  • useful steam D generated in the boiler 3 is fed to the turbine 5 via the steam line 49, where it relaxes while performing work.
  • the turbine 5 is shown here in simplified form, but can consist of a plurality of sub-turbines, not shown, for example a high-pressure sub-turbine, a medium-pressure sub-turbine and a low-pressure sub-turbine.
  • the steam D expanded to low pressure is fed to the condenser 7 via the exhaust steam line 51 and condenses there to condensate K.
  • the condensate K is conveyed via the condensate line 13 by means of the first pump 41 into the feed water tank 45 and collected there.
  • the boiler 3 is preheated condensate K as the boiler feed water S by means of the second pump 43 via the preheating device 15. guided, so that a closed water-steam cycle is created.
  • the useful work obtained in the turbine 5 is transmitted via the rotating shaft 57 to a generator 39 coupled to the shaft 57 and converted into electrical energy.
  • the condensate K is divided into a first partial flow Ki and a second partial flow K 2 for preheating the condensate, only the first partial flow K ⁇ being preheated and the second partial flow K 2 being admixed with the preheated first partial flow Ki.
  • the division of the condensate K into the first partial flow Ki and the second partial flow K 2 takes place at the separation point 47, the second partial flow K 2 bypassing the preheating device 15 via the bypass line 17.
  • the first partial flow Ki is preheated from the turbine 5 by means of bleed steam Ai, A 2 .
  • the first partial flow Ki is preheated in two stages 9A, 9B, the first partial flow Ki being preheated to a temperature of approximately 280 ° C. at a pressure of 300 bar.
  • the first partial flow Ki is mixed with the second partial flow K 2 , a mixing temperature of 210 ° C. to 250 ° C., in particular of 220 ° C. to 240 ° C. being established.
  • the sub-streams K lr K 2 are divided, for example, in such a way that the first sub-stream Ki makes up about 40% of the total condensate stream and the second sub-stream K 2 correspondingly about 60% of the total condensate stream upstream of the separation point 47.
  • the division of the partial flows Ki, K 2 takes place in a controlled or regulated manner via the regulating or metering valve 21, which can be precisely adjusted in the valve position by means of the servomotor 33.
  • the preheating device 15 is bypassed in a metered manner via the bypass line 17, with a correspondingly lower requirement for bleed steam Ai, A 2 for preheating the first partial flow Ki in the preheating device 15. Due to the lower removal of bleed steam Ai, A 2 compared to conventional system concepts, through the targeted and metered bypassing of the preheating device 15, a corresponding chend larger mass flow of steam D to the working line in the turbine 5 available.
  • the temperature T s of the boiler feed water S fed to the boiler 3 can be precisely adjusted and, if necessary, varied by mixing the first partial flow Ki and the second partial flow K 2 at the mixing point 48, for example a boiler feed water temperature T s of 210 ° C to 250 ° C at a pressure of 300 bar if necessary.
  • the extraction of bleed steam Ai, A 2 from the turbine 5 is advantageously self-regulating, by coupling the first partial flow Ki with the bleed steam Ai, A 2 via the heat exchangers 23A, 23B.
  • the temperature of the first partial flow Ki after passing through the heat exchangers 23A, 23B is approximately the same as the temperature of the bleed steam Ai, A 2 , that is to say, for example, approximately 280 ° C. at a pressure of 300 bar.
  • the mixing temperature is set automatically in accordance with the division ratios of the partial flows Ki, K 2 and the temperature levels.
  • This mixing temperature is at the same time the preheating temperature T s of the boiler feed water S.
  • the preheating temperature T s is correspondingly reduced compared to conventional steam power plants, although an increase in the power of the turbine 5 is achieved due to the lower heat consumption for preheating the condensate K. This results in a significantly more efficient heat consumption than in the case of a total bypassing of the preheating device 15 which is usually carried out to increase the output. It is now possible to increase the output of the turbine by partially flowing through the preheating device 15 without restricting the life of the components of the preheating device 15, for example the heating surfaces of the heat exchangers 23A, 23B.

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

Abstract

L'invention concerne un procédé d'utilisation d'un groupe vapeur (1) consistant à faire précipiter dans un condenseur (7) de la vapeur (D) produite dans une chaudière (3) après passage dans au moins une turbine (5), à préchauffer le condensat (K) ainsi obtenu, et à réalimenter le condensat dans la chaudière (3) en tant qu'eau d'alimentation de chaudière (S). Le condensat (K) est séparé en un premier courant partiel (K1) et un deuxième courant partiel (K2) pour le préchauffage du condensat. Seul le premier courant partiel (K1) est préchauffé, et le deuxième courant partiel (K2) est mélangé au premier courant partiel préchauffé (K1). Ainsi, il est possible d'augmenter la puissance de la turbine (5) en fonction des besoins, jusqu'à la réserve de la chaudière du groupe vapeur (1).
EP02719925A 2001-03-15 2002-02-25 Procede d'utilisation d'un groupe vapeur et groupe vapeur correspondant Expired - Lifetime EP1368555B1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
EP02719925A EP1368555B1 (fr) 2001-03-15 2002-02-25 Procede d'utilisation d'un groupe vapeur et groupe vapeur correspondant

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
EP01106600 2001-03-15
EP01106600A EP1241323A1 (fr) 2001-03-15 2001-03-15 Procédé de fonctionnement d'une centrale d'énergie à vapeur et centrale d'énergie à vapeur
EP02719925A EP1368555B1 (fr) 2001-03-15 2002-02-25 Procede d'utilisation d'un groupe vapeur et groupe vapeur correspondant
PCT/EP2002/002023 WO2002075119A1 (fr) 2001-03-15 2002-02-25 Procede d'utilisation d'un groupe vapeur et groupe vapeur correspondant

Publications (2)

Publication Number Publication Date
EP1368555A1 true EP1368555A1 (fr) 2003-12-10
EP1368555B1 EP1368555B1 (fr) 2007-02-14

Family

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Family Applications (2)

Application Number Title Priority Date Filing Date
EP01106600A Withdrawn EP1241323A1 (fr) 2001-03-15 2001-03-15 Procédé de fonctionnement d'une centrale d'énergie à vapeur et centrale d'énergie à vapeur
EP02719925A Expired - Lifetime EP1368555B1 (fr) 2001-03-15 2002-02-25 Procede d'utilisation d'un groupe vapeur et groupe vapeur correspondant

Family Applications Before (1)

Application Number Title Priority Date Filing Date
EP01106600A Withdrawn EP1241323A1 (fr) 2001-03-15 2001-03-15 Procédé de fonctionnement d'une centrale d'énergie à vapeur et centrale d'énergie à vapeur

Country Status (9)

Country Link
US (1) US6964167B2 (fr)
EP (2) EP1241323A1 (fr)
AR (1) AR032996A1 (fr)
AT (1) ATE354016T1 (fr)
DE (1) DE50209484D1 (fr)
DK (1) DK1368555T3 (fr)
ES (1) ES2280526T3 (fr)
TW (1) TW538193B (fr)
WO (1) WO2002075119A1 (fr)

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EP2351914A1 (fr) 2010-01-11 2011-08-03 Alstom Technology Ltd Centrale électrique et son procédé de fonctionnement
WO2013005071A1 (fr) 2011-07-07 2013-01-10 Alstom Technology Ltd Centrale et procédé d'exploitation de celle-ci
EP3244030A1 (fr) 2016-05-09 2017-11-15 General Electric Technology GmbH Centrale thermique à vapeur avec amplification de puissance grâce à l'utilisation d'un réchauffage de drain de chauffage supérieur

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ES2605253T3 (es) 2009-11-13 2017-03-13 Siemens Aktiengesellschaft Central térmica de vapor y procedimiento para operar una central térmica de vapor
US9091182B2 (en) * 2010-12-20 2015-07-28 Invensys Systems, Inc. Feedwater heater control system for improved rankine cycle power plant efficiency
US9316122B2 (en) 2010-12-20 2016-04-19 Invensys Systems, Inc. Feedwater heater control system for improved Rankine cycle power plant efficiency
US8867689B2 (en) * 2011-02-15 2014-10-21 Nuscale Power, Llc Heat removal system and method for use with a nuclear reactor
EP2546476A1 (fr) * 2011-07-14 2013-01-16 Siemens Aktiengesellschaft Installation de turbines à vapeur et procédé pour opérer l'installation de turbines à vapeur
EP2589760B1 (fr) * 2011-11-03 2020-07-29 General Electric Technology GmbH Centrale thermique à vapeur avec réservoir de chaleur haute température
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Publication number Priority date Publication date Assignee Title
EP2351914A1 (fr) 2010-01-11 2011-08-03 Alstom Technology Ltd Centrale électrique et son procédé de fonctionnement
WO2013005071A1 (fr) 2011-07-07 2013-01-10 Alstom Technology Ltd Centrale et procédé d'exploitation de celle-ci
EP3244030A1 (fr) 2016-05-09 2017-11-15 General Electric Technology GmbH Centrale thermique à vapeur avec amplification de puissance grâce à l'utilisation d'un réchauffage de drain de chauffage supérieur

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ES2280526T3 (es) 2007-09-16
EP1241323A1 (fr) 2002-09-18
EP1368555B1 (fr) 2007-02-14
DE50209484D1 (de) 2007-03-29
DK1368555T3 (da) 2007-06-11
TW538193B (en) 2003-06-21
US6964167B2 (en) 2005-11-15
ATE354016T1 (de) 2007-03-15
US20040105518A1 (en) 2004-06-03
AR032996A1 (es) 2003-12-03
WO2002075119A1 (fr) 2002-09-26

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