EP2923149A2 - Entwässerung einer kraftwerksanlage - Google Patents
Entwässerung einer kraftwerksanlageInfo
- Publication number
- EP2923149A2 EP2923149A2 EP13799059.4A EP13799059A EP2923149A2 EP 2923149 A2 EP2923149 A2 EP 2923149A2 EP 13799059 A EP13799059 A EP 13799059A EP 2923149 A2 EP2923149 A2 EP 2923149A2
- Authority
- EP
- European Patent Office
- Prior art keywords
- steam
- water
- power plant
- atmospheric pressure
- container
- 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
Links
- 238000011144 upstream manufacturing Methods 0.000 claims abstract description 15
- 238000000034 method Methods 0.000 claims abstract description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 53
- 239000003990 capacitor Substances 0.000 claims description 8
- 239000012530 fluid Substances 0.000 claims description 7
- 239000012535 impurity Substances 0.000 claims description 7
- 238000001816 cooling Methods 0.000 claims description 6
- 238000012545 processing Methods 0.000 claims description 6
- 239000008400 supply water Substances 0.000 claims description 2
- 208000005156 Dehydration Diseases 0.000 description 13
- 230000018044 dehydration Effects 0.000 description 13
- 238000006297 dehydration reaction Methods 0.000 description 13
- 238000005516 engineering process Methods 0.000 description 8
- 238000009833 condensation Methods 0.000 description 7
- 230000005494 condensation Effects 0.000 description 7
- 239000007788 liquid Substances 0.000 description 6
- 239000002351 wastewater Substances 0.000 description 6
- 238000004140 cleaning Methods 0.000 description 4
- 238000010248 power generation Methods 0.000 description 4
- 238000007639 printing Methods 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000012808 vapor phase Substances 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000001143 conditioned effect Effects 0.000 description 1
- 230000003750 conditioning effect Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 239000008367 deionised water Substances 0.000 description 1
- 229910021641 deionized water Inorganic materials 0.000 description 1
- 238000010612 desalination reaction Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000000977 initiatory effect Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B37/00—Component parts or details of steam boilers
- F22B37/02—Component parts or details of steam boilers applicable to more than one kind or type of steam boiler
- F22B37/48—Devices for removing water, salt, or sludge from boilers; Arrangements of cleaning apparatus in boilers; Combinations thereof with boilers
- F22B37/486—Devices for removing water, salt, or sludge from boilers
-
- 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
- F01K23/00—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids
- F01K23/02—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled
- F01K23/06—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled combustion heat from one cycle heating the fluid in another cycle
- F01K23/10—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled combustion heat from one cycle heating the fluid in another cycle with exhaust fluid of one cycle heating the fluid in another cycle
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B37/00—Component parts or details of steam boilers
- F22B37/02—Component parts or details of steam boilers applicable to more than one kind or type of steam boiler
- F22B37/48—Devices for removing water, salt, or sludge from boilers; Arrangements of cleaning apparatus in boilers; Combinations thereof with boilers
- F22B37/50—Devices for removing water, salt, or sludge from boilers; Arrangements of cleaning apparatus in boilers; Combinations thereof with boilers for draining or expelling water
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28G—CLEANING OF INTERNAL OR EXTERNAL SURFACES OF HEAT-EXCHANGE OR HEAT-TRANSFER CONDUITS, e.g. WATER TUBES OR BOILERS
- F28G9/00—Cleaning by flushing or washing, e.g. with chemical solvents
Definitions
- the present invention relates to a power plant, in particular a coupled gas and steam power plant, which has a number of drainage pipes for dewatering a water-steam cycle, and a method for operating such a power plant.
- Steam-powered power plants in particular coupled gas and steam power plants, have a water-steam cycle, which can sometimes be designed as one or more circulating steam generator with steam drums and the associated heating surfaces.
- Such circulating steam generators are usually subdivided into a high-pressure stage, a medium-pressure stage and a low-pressure stage, depending on their working pressure regime.
- steam hereinafter referred to simply as steam
- the steam generator can also be designed as a forced-circulation steam generator (Benson boiler, Sulzer boiler, etc.).
- Circulation also condensation water, which precludes an efficient use of the water-steam cycle.
- condensation water forms, in particular, due to time-varying operating conditions in the water-steam cycle. Condensation falls so, for example, when you shut down the power plants in the water-steam cycle, since at decreasing operating temperatures, the vapor contained in the water-steam cycle condenses increasingly condensed and the resulting condensed water also accumulates in parts of the system, for a longer Contact with liquid water are not provided.
- it is necessary to remove more water from the water-steam circuit in order to avoid unwanted condensation of water in unscheduled plant parts.
- less water is refilled in the water-steam circuit when driving down to keep at the end of the Abfahrreaes relevant plant components largely free of condensed water. In order to remove such condensation water from the water-steam
- the drained from the water-steam circuit drainages must be prepared in an energetically complex process, in particular to separate the slurries of reusable as deionized water. It is particularly unfavorable in terms of the balance of resources if the treated water is no longer returned to the water-steam cycle but is discarded, for example, into the environment.
- the technical solution to be proposed is intended to enable an energetically advantageous use of the energy extracted by the discharge of dehydrations from the water-steam cycle. In other words, it should be made with respect to the overall energy balance of the power plant operation improved drainage. Moreover, it is desirable to make available again the energy dissipated from the water-steam cycle and the drainages for the power plant and in particular for the water-steam cycle.
- a power plant in particular a coupled gas and steam power plant, comprising a number of first drainage pipes, which
- upstream with a pressure stages having water-steam circuit are fluidly connected, and which are fluidly connected at the downstream side with an overpressure container, further at least one steam supply line leading to the fluid pressure tank is fluid technically connected via which steam the water vapor - Circuit can be supplied again, wherein the at least one steam leading supply line can supply the water-steam cycle in the region of a low-pressure stage, in particular in the region of the steam drum of the low pressure stage steam.
- a method for operating a power plant as described above and below comprising the following steps: Dewatering water and / or steam from a water-steam cycle by supplying to a pressure vessel;
- the idea of the invention teaches the dehydration of the water-steam cycle by means of a number of first drainage pipes, which are fluidly connected upstream with the water-steam cycle.
- first drainage pipes which are fluidly connected upstream with the water-steam cycle.
- Pressure level can be adjusted in comparison to the pressure level of the water-steam cycle.
- the pressure vessel further has a pressure level which is above the ambient pressure level.
- the steam in the overpressure container which furthermore has usable thermal energy, is again supplied to the water-steam cycle for further use via the supply line which is fluidly connected to the overpressure container.
- the at least one steam leading supply line the water-steam cycle in the region of a low-pressure stage, in particular in the field the steam drum of the low pressure stage can supply steam.
- the term "in the field” is to be understood in the sense of "in the local area”, as will be explained below.
- the connection is made, in particular, with the low-pressure stage, in particular the steam drum of the low-pressure stage. Due to the prevailing in the low pressure stage relatively lower pressure levels, a transfer of steam from the pressure vessel in the water-steam cycle is energetically particularly favorable.
- the pressure level of the vapor in the pressure vessel is not substantially below the pressure level of the low pressure stage or even at the same pressure level or above.
- the low-pressure stage is suitable for printing, and thus energy technology for returning the discharged from the pressure vessel vapor particularly.
- the term of steam in the sense of vaporous water should be understood, as it occurs, for example, in the water-steam cycle.
- the quality of the water for example, due to an alternating content of various impurities, should have no influence on the conceptual meaning.
- the term of the water should include wastewater as well as in the water-steam cycle remaining useful water or condensation water.
- the steam discharged from the water-steam cycle as well as to the useful steam remaining in the water-steam cycle.
- the concept of water or steam can also be equated with the concept of drainage.
- the power plant comprises only one drainage pipe
- the number of first drainage lines upstream with the water-steam cycle in the region of a high-pressure and / or medium-pressure stage in particular in the region of a steam drum of high-pressure
- a fluid-technical interconnection "in the area” means in local proximity, wherein a fluid-technical interaction is brought about.
- the interconnection can also take place with a forced-circulation steam generator of the high-pressure and / or a forced-circulation steam generator of the medium-pressure stage.
- the number of first drainage lines upstream can also be connected to the water-steam cycle in the region of the low-pressure stage, in particular in the region of the steam drum of the low-pressure stage.
- the interconnection can also with a
- Pressure levels of the derived from the high-pressure and / or medium pressure stage steam is in particular in the pressure vessel before a relatively higher pressure level, which favors the return to the water-steam cycle energetically.
- the power plant also has an atmospheric pressure vessel, which enables a Dampfentspan- voltage to substantially atmospheric pressure, and which is line technology connected to the pressure vessel so that steam from the pressure vessel are passed into the atmospheric pressure vessel can.
- the atmospheric pressure vessel and the pressure vessel are thus to Collection of drainages ready.
- the drains are passed in vapor phase from the pressure vessel into the atmospheric pressure vessel, wherein the pressure vessel can be converted to a correspondingly lower pressure level.
- the atmospheric pressure vessel serves on the one hand to accumulate dehydration and at the same time also to regulate the pressure of the pressure in the pressure vessel.
- the atmospheric pressure container allows a suitable drainage of the drainage systems without the pressure vessel having to be subjected to changes in terms of printing technology, for example during operation.
- relaxation to substantially atmospheric pressure level should include a pressure level corresponding to the atmospheric pressure level with a pressure tolerance of up to 20%.
- Power plant are included, which are adapted to set the amount of steam, which can be passed from the pressure vessel into the atmospheric pressure vessel.
- the adjusting means between the pressure vessel and atmospheric pressure vessel is connected by line technology.
- the actuating means can interrupt the fluid connection between the overpressure container and the drainage container, so that removal from the atmospheric pressure container can be carried out without further influence with respect to the change of the pressure level in the overpressure container.
- a number of second drainage lines is connected, which are connected upstream with the water-steam cycle, and which downstream side are connected to the atmospheric pressure vessel, and via which water and steam from the water-steam cycle can be fed to the atmospheric pressure vessel.
- water and steam from the water-steam cycle which is in particular at a relatively low pressure level, can thus be transferred into the atmospheric pressure tank. It may also prove advantageous, according to the embodiment, to transfer dehydrations from the water-steam circuit into the atmospheric pressure vessel if the dewatering collected therein is to be subjected to a different treatment form than the dehydration collected in the overpressure vessel.
- the number of second drainage conduits prefferably be "one", i.e. according to the invention the power plant comprises only a second drainage conduit.
- the number of second drainage lines is connected upstream to the water-steam cycle in the region of the low-pressure stage.
- the term "in the range" in a local area means that, in particular, the connection is made with the low-pressure stage
- the pressure level in the low-pressure stage is sometimes sufficiently low to transfer steam into the atmospheric pressure vessel, which is not energy-efficient
- the liquid drains discharged from the low-pressure stage preferably provide for a rejection into the environment Vapor drains discharged from the low-pressure stage can preferably likewise be supplied to the overpressure container, as already explained above.
- the atmospheric pressure container is connected to a recirculation line, which makes it possible to supply water from the atmospheric pressure container to a first cooling source, and to recycle the thus thermally treated water back into the atmospheric pressure container.
- the recirculation of water from the atmospheric pressure vessel allows the prevention of steam formation in the atmospheric pressure vessel.
- the overpressure container and / or the atmospheric pressure container is line-connected with a second cold source, which makes it possible to thermally treat water discharged from the overpressure container and / or the atmospheric pressure container.
- the drains discharged from the pressure vessel or the atmospheric pressure vessel can be cooled before further processing or separation and cleaning. This cooling is known to most of the prior art
- This cooling can in turn be done by means of water from the main capacitor of the power plant or water from an intermediate cooling to provide the second source of cold.
- the water thus treated can, according to the embodiment, again be provided for recycling into the water-steam cycle as a deionate.
- the overpressure container and / or the atmospheric pressure container is line-connected to a collecting container, in which water located in the overpressure container and / or in the atmospheric pressure container can be transferred for storage.
- the collecting container is capable in particular of the collection of condensed drainages and allows the merging of these before, for example, a further cleaning and treatment of these drains can take place.
- the merger presents be as process technology as well as energetically particularly useful and advantageous.
- the collecting container to be connected to a processing unit in terms of line technology, wherein the processing unit can at least partially clean the water of impurities. After cleaning the water present as drainage by means of the treatment unit, the recycled water can be added to the water-steam
- the collecting container and / or the treatment unit is connected in terms of line technology with the main capacitor of the power plant such that water from this the
- Main capacitor can be supplied.
- the main capacitor corresponds to the capacitor in which the steam is condensed, which is fed to the steam turbine or steam turbines for power generation.
- Figure 1 is a schematic representation of an embodiment of the power plant according to the invention
- FIG. 2 shows a flow chart representation of an embodiment of the method according to the invention for operating a power plant installation
- FIG. 1 shows a possible embodiment of the present power plant 1 according to the invention, which has a water-steam circuit 2.
- the water-steam circuit 2 is comprised by the steam part of a gas and steam power plant 1.
- the water-steam cycle 2 a total of three different pressure levels 3, 5, 7, the
- the steam processed in these pressure stages 3, 5, 7 is supplied to a steam turbine 90 (or a plurality of steam turbines 90) for power generation, which is connected in a fluidic manner to a main capacitor 100 as a cold source.
- a steam turbine 90 or a plurality of steam turbines 90
- main condenser 100 it is possible for the steam prepared in the pressure stages 3, 5, 7 to be led to the main condenser 100 via condensation diverter stations not provided with reference numerals.
- first drainage lines 11 are fluidically connected upstream with corresponding line sections of the respective pressure stage 3, 5, 7.
- first drainage pipes 11 are fluidically connected upstream with corresponding line sections of the respective pressure stage 3, 5, 7.
- a feed line 12 is fluidically connected to the overpressure container 20, which is connected downstream of the steam drum 8 of the low-pressure stage 7. This makes it possible, located in the pressure vessel 20 steam, compared to the high pressure stage 3 and medium pressure stage 5 at a lower
- Supplied pressure level operated low-pressure stage 7 wherein the thus returned steam for electric power generation by means of the turbine 90 (steam turbine) may be available again.
- the turbine 90 can likewise be designed as a number of individual turbines which are suitably connected to the respective pressure stages 3, 5, 7.
- the power plant 1 comprises an atmospheric pressure tank 30, which is also fluidly connected to the pressure tank 20.
- an adjusting means 25 is also provided, which allows to interrupt the fluid connection or the Adjust fluid flow suitable.
- the pressure level in the pressure vessel 20 can be suitably adjusted, and on the other hand, the costs incurred in the atmospheric pressure vessel 30 drainages can be suitably dissipated without having to change the pressure level in the pressure vessel 20 at the same time.
- a discharge line 35 is provided, via which, in particular, vaporous water can be supplied from the atmospheric pressure container 30 to the environment U.
- a first cold source 50 as well as a second cold source 60 are provided.
- Recirculation line 40 which drainages can be seen from the atmospheric pressure tank 30 to supply the first source of cold 50. Thereafter, the so thermally conditioned dehydrations are completely or partially recycled to the atmospheric pressure vessel 30, but at a lower temperature level. This temperature treatment allows the reduction of an undesirable
- FIG. 2 shows a flow chart representation of an embodiment of the method according to the invention for operating a power plant.
- Steps includes:
Abstract
Description
Claims
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP12198121.1A EP2746656A1 (de) | 2012-12-19 | 2012-12-19 | Entwässerung einer Kraftwerksanlage |
PCT/EP2013/075334 WO2014095337A2 (de) | 2012-12-19 | 2013-12-03 | Entwässerung einer kraftwerksanlage |
Publications (2)
Publication Number | Publication Date |
---|---|
EP2923149A2 true EP2923149A2 (de) | 2015-09-30 |
EP2923149B1 EP2923149B1 (de) | 2020-02-05 |
Family
ID=47563062
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP12198121.1A Withdrawn EP2746656A1 (de) | 2012-12-19 | 2012-12-19 | Entwässerung einer Kraftwerksanlage |
EP13799059.4A Active EP2923149B1 (de) | 2012-12-19 | 2013-12-03 | Entwässerung einer kraftwerksanlage |
Family Applications Before (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP12198121.1A Withdrawn EP2746656A1 (de) | 2012-12-19 | 2012-12-19 | Entwässerung einer Kraftwerksanlage |
Country Status (4)
Country | Link |
---|---|
US (1) | US9719676B2 (de) |
EP (2) | EP2746656A1 (de) |
ES (1) | ES2781836T3 (de) |
WO (1) | WO2014095337A2 (de) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CA2941547A1 (en) | 2014-03-05 | 2015-09-11 | Siemens Aktiengesellschaft | Flash tank design |
DE102015206484A1 (de) * | 2015-04-10 | 2016-10-13 | Siemens Aktiengesellschaft | Verfahren zum Aufbereiten eines flüssigen Mediums und Aufbereitungsanlage |
DE102016214447B4 (de) * | 2016-08-04 | 2020-12-24 | Siemens Aktiengesellschaft | Kraftwerk mit Phasenwechselmaterial-Wärmespeicher und Verfahren zum Betreiben eines Kraftwerks mit Phasenwechselmaterial-Wärmespeicher |
CN110374700B (zh) * | 2019-07-18 | 2024-05-03 | 中国电力工程顾问集团西南电力设计院有限公司 | 一种燃气-蒸汽联合循环机组疏水回收系统 |
Family Cites Families (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3008295A (en) * | 1958-04-21 | 1961-11-14 | Sulzer Ag | Steam power plant |
DE3166099D1 (en) * | 1980-12-23 | 1984-10-25 | Sulzer Ag | Forced-circulation steam boiler |
WO1997007323A1 (de) * | 1995-08-18 | 1997-02-27 | Siemens Aktiengesellschaft | Gas- und dampfturbinenanlage und verfahren zum betreiben einer derartigen anlage sowie abhitzedampferzeuger für eine gas- und dampfturbinenanlage |
JP3690972B2 (ja) * | 2000-08-08 | 2005-08-31 | 三菱重工業株式会社 | 蒸気冷却ガスタービン |
WO2005068905A1 (de) * | 2004-01-20 | 2005-07-28 | Siemens Aktiengesellschaft | Verfahren und vorrichtung zur entwässerung bei einer dampfkraftanlage |
EP1662096A1 (de) | 2004-11-30 | 2006-05-31 | Siemens Aktiengesellschaft | Verfahren zum Betrieb einer Dampfkraftanlage, insbesondere einer Dampfkraftanlage eines Kraftwerks zur Erzeugung von zumindest elektrischer Energie, und entsprechende Dampfkraftanlage |
ITMI20102121A1 (it) * | 2010-11-16 | 2012-05-17 | Ansaldo Energia Spa | Impianto a ciclo combinato per la produzione di energia e metodo per operare tale impianto |
EP2503112A1 (de) * | 2011-03-24 | 2012-09-26 | Siemens Aktiengesellschaft | Verfahren zum schnellen Zuschalten eines Dampferzeugers |
JP2014008501A (ja) * | 2012-07-03 | 2014-01-20 | Mitsubishi Heavy Ind Ltd | 排水処理システム及び複合発電設備 |
-
2012
- 2012-12-19 EP EP12198121.1A patent/EP2746656A1/de not_active Withdrawn
-
2013
- 2013-12-03 EP EP13799059.4A patent/EP2923149B1/de active Active
- 2013-12-03 ES ES13799059T patent/ES2781836T3/es active Active
- 2013-12-03 WO PCT/EP2013/075334 patent/WO2014095337A2/de active Application Filing
- 2013-12-03 US US14/652,194 patent/US9719676B2/en active Active
Non-Patent Citations (1)
Title |
---|
See references of WO2014095337A3 * |
Also Published As
Publication number | Publication date |
---|---|
US9719676B2 (en) | 2017-08-01 |
ES2781836T3 (es) | 2020-09-08 |
EP2923149B1 (de) | 2020-02-05 |
WO2014095337A3 (de) | 2014-11-20 |
EP2746656A1 (de) | 2014-06-25 |
WO2014095337A2 (de) | 2014-06-26 |
US20150323176A1 (en) | 2015-11-12 |
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