EP1710498A1 - Dampferzeuger - Google Patents

Dampferzeuger Download PDF

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Publication number
EP1710498A1
EP1710498A1 EP05007413A EP05007413A EP1710498A1 EP 1710498 A1 EP1710498 A1 EP 1710498A1 EP 05007413 A EP05007413 A EP 05007413A EP 05007413 A EP05007413 A EP 05007413A EP 1710498 A1 EP1710498 A1 EP 1710498A1
Authority
EP
European Patent Office
Prior art keywords
steam generator
water
tubes
superheater
evaporator
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Withdrawn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
EP05007413A
Other languages
German (de)
English (en)
French (fr)
Inventor
Joachim Dr. Franke
Rudolf Kral
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 EP05007413A priority Critical patent/EP1710498A1/de
Priority to PCT/EP2006/061225 priority patent/WO2006106079A2/de
Priority to BRPI0609735-9A priority patent/BRPI0609735A2/pt
Priority to CA2603934A priority patent/CA2603934C/en
Priority to JP2008504750A priority patent/JP4833278B2/ja
Priority to RU2007140865/06A priority patent/RU2397405C2/ru
Priority to CN2006800155792A priority patent/CN101384854B/zh
Priority to US11/887,859 priority patent/US8297236B2/en
Priority to EP06743231A priority patent/EP1926934A2/de
Priority to UAA200710991A priority patent/UA89523C2/uk
Priority to AU2006232687A priority patent/AU2006232687B2/en
Priority to TW095111862A priority patent/TWI356891B/zh
Priority to MYPI20061547A priority patent/MY146130A/en
Priority to ARP060101341A priority patent/AR053572A1/es
Publication of EP1710498A1 publication Critical patent/EP1710498A1/de
Priority to ZA200708412A priority patent/ZA200708412B/xx
Withdrawn legal-status Critical Current

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Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22—STEAM GENERATION
    • F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B1/00—Methods of steam generation characterised by form of heating method
    • F22B1/02—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers
    • F22B1/18—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being a hot gas, e.g. waste gas such as exhaust gas of internal-combustion engines
    • F22B1/1807—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being a hot gas, e.g. waste gas such as exhaust gas of internal-combustion engines using the exhaust gases of combustion engines
    • F22B1/1815—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being a hot gas, e.g. waste gas such as exhaust gas of internal-combustion engines using the exhaust gases of combustion engines using the exhaust gases of gas-turbines
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22—STEAM GENERATION
    • F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B29/00—Steam boilers of forced-flow type
    • F22B29/06—Steam boilers of forced-flow type of once-through type, i.e. built-up from tubes receiving water at one end and delivering superheated steam at the other end of the tubes

Definitions

  • the invention relates to a steam generator in which in a Walkergaskanal formed from a number of evaporator tubes evaporator fürlaufterrorism behavior and one of a number of the evaporator tubes flow medium side downstream superheater tubes formed Matterhitzerterrorism phenomenon are arranged.
  • a continuous steam generator In a continuous steam generator, the heating of a number of evaporator tubes leads to a complete evaporation of the flow medium in the evaporator tubes in one pass.
  • the flow medium - usually water - is supplied to the evaporator tubes downstream superheater tubes after its evaporation and overheated there.
  • the position of the evaporation end point, ie the boundary region between unvaporized and vaporized flow medium, is variable and mode-dependent.
  • the evaporation end point is, for example, in an end region of the evaporator tubes, so that the overheating of the evaporated flow medium already begins in the evaporator tubes.
  • a continuous steam generator is not subject to any pressure limitation, so that it is possible for live steam pressures far above the critical pressure of water (P Kri ⁇ 221 bar) - where no differentiation of the phases water and steam and thus no phase separation is possible. can be designed.
  • the hot exhaust gas from the gas turbine is usually first passed to the uncooled tubes of the superheater section of the continuous steam generator, which usually must be made of high-quality temperature-resistant materials for this reason.
  • the feeding of the evaporator section may be provided with a minimum flow of flow medium to ensure safe cooling of the steam generator tubes.
  • Just at low loads of, for example, less than 40% of the design load of the corresponding steam power flow pass through the steam generator tubes usually no longer sufficient for their cooling, so that this passage of flow medium through the evaporator, an additional flow rate of fluid is superimposed. In this case, usually a separation of water from the flow medium is necessary before it enters the superheater section of the continuous steam generator.
  • the continuous heating surface can be formed in its entirety by a arranged in a Schugaskanal, formed from a number of evaporator tubes evaporator für Aviation Mixing Technology (Gaussian), and by a flow medium side downstream, formed from a number of superheater tubes Kochhitzerterrorism simulation, wherein the flow medium side between the evaporator fürlaufterrorism configuration and Kochhitzerterrorism simulation a Wasserabscheidesystem is connected.
  • the evaporator tubes forming the evaporator section typically open into one or more outlet collectors, from which the flow medium is guided into a downstream water-steam separator. There, a separation of the flow medium in water and in steam, wherein the steam is transferred into a superheater tubes upstream distribution system, where a division of the steam mass flow is carried out on the individual, on the flow medium side parallel superheater tubes.
  • the vaporization end point of the continuous steam generator is determined by the interposition of the Wasserabscheidesystems in start-up and low load operation and not - as in full load operation - variable.
  • the operational flexibility is significantly limited in such a construction of the continuous steam generator in low load operation.
  • the separation systems must generally be designed, in particular with regard to the choice of material, for the steam in the separator to be clearly overheated in the pure continuous operation. The required material selection also leads to a significant restriction of operational flexibility.
  • the said construction also requires that the water discharge occurring during the startup of the continuous steam generator in the first start-up phase must be completely absorbed in the separation system and be able to be discharged via the downstream separation tank and the discharge valves into the expander.
  • the resulting comparatively large dimensioning of separating bottle and drain valves leads to a considerable manufacturing and assembly costs.
  • the invention is therefore based on the object to provide a steam generator of the type mentioned above, which is kept at comparatively low manufacturing and assembly costs also has a particularly high operational flexibility when starting and in low load operation.
  • This object is achieved according to the invention by integrating in each case one water separation element into a number of one or more evaporator tubes, each with one or more superheater tubes connecting the flow medium side.
  • the invention is based on the consideration that the continuous steam generator should be designed to ensure a particularly high operational flexibility even in start-up or low-load operation for a variable evaporation endpoint.
  • the usual construction-related fixation of the evaporation end point in the water separation system should be avoided.
  • this fixation is essentially due to the collection of the flowing out of the evaporator tubes flow medium
  • the subsequent separation of water in a central Wasserabscheide responded and the subsequent distribution of the steam on the superheater tubes
  • a decentralization of Wasserabscheidefunktion should be made.
  • the water separation should in particular be designed such that after the water separation no too complex distribution of the flow medium is provided, since this is not practical for a water-steam mixture. This can be achieved by deviating from the conventionally provided central water-steam separation, the water separation system is designed decentralized, the separation function is integrated into the flow medium-side connection of the evaporator tubes with the downstream superheater tubes anyway necessary pieces of pipe.
  • the continuous steam generator can be designed in so-called upright construction or in so-called horizontal construction.
  • a particularly simple construction of the Wasserabscheideetic with high reliability of the water separation can be achieved by the respective Wasserabscheideelement is advantageously designed for a Trägheitsseparation of water from the steam in the flow medium.
  • the knowledge is preferably used that the water content of the flow medium preferably continues to flow straight ahead in its flow direction due to its higher inertia compared to the vapor component, while the vapor component is comparatively better able to follow an imposed deflection.
  • this is embodied in a particularly advantageous embodiment in the manner of a T-piece.
  • the respective Wasserabscheideelement preferably comprises a connected to the upstream evaporator tube Einströmrohr laminate, seen in its longitudinal direction merges into a Wasserableitrohr sensible, wherein in the transition region branches off a number of each connected to a downstream superheater tube Abströmrohr structurien.
  • the water content of the flow medium flowing into the inflow pipe section is transported further at the branching point substantially without deflection in the longitudinal direction and thus passes into the water drainage pipe section.
  • a deflection is easier for the vapor content due to its relatively lower inertia, so that the vapor content in the branching or the AbströmrohrFigs.
  • the Einströmrohr choir is designed to be substantially rectilinear, wherein it may be arranged with its longitudinal direction substantially horizontally or in a predetermined tilt or tilt angle.
  • an inclination in the flow direction downwards is preferably provided.
  • an inflow of the inflow pipe piece may be provided via a pipe bend coming from above, so that in this case the flow medium is pressed towards the outside of the curvature due to the centrifugal force.
  • the water component of the flow medium preferably flows along the outer region of the bend.
  • preferably provided for the discharge of the vapor portion outflow pipe piece is aligned to the inside of the curvature.
  • the Wasserableitrohr choir is preferably designed in its inlet region as downwardly curved pipe bend. This is facilitated in a particularly simple and low-loss way, a deflection of the separated water for demand-feeding into subsequent systems.
  • the Wasserabscheide comprise water outlet side so in particular with their Wasserableitrohr choiren, groups connected to a number of common outlet collectors.
  • the respective water-separating element is now connected upstream of the outlet collector.
  • the outlet headers are advantageously followed by a number of water collection containers.
  • the water collection container (s) may in turn be connected on the output side with suitable systems such as, for example, an atmospheric expander or via a circulating pump with the circulation of the continuous steam generator.
  • the mass flow flowing out of the water collecting container can be adjusted in the operating mode of the bypassed separating system by targeted activation of the valve connected in the outflow line of the water collecting container.
  • the mass flow is adjustable, which passes from the Wasserabscheideijnn in the collection system.
  • that partial flow is adjustable, which is passed together with the steam in the superheater tubes, so that a predetermined enthalpy can be maintained via an appropriate setting of this partial flow, for example, at the end of the superheater section of naturallaufterrorism phenomenon.
  • the water partial flow passed on together with the steam to the superheater pipes can also be influenced by a corresponding control of the superimposed circulation circuit.
  • the water separation system associated with the control device associated with the evaporator tubes circulating pump can be controlled.
  • the steam generator is used as a heat recovery steam generator of a gas and steam turbine plant.
  • the Wasserabscheideieri can be designed in particular as T-pieces based on the already existing bore of the continuous steam generator. These tees can be made comparatively thin-walled, with diameter and wall thickness can be kept approximately comparable to those of the wall tubes.
  • the start-up times of the boiler as a whole or the load change speeds are not further limited by the thin-walled design of Wasserabscheideetic, so that even in systems for high steam conditions comparatively short reaction times can be achieved under load changes.
  • such tees are particularly inexpensive to produce.
  • an intermediate over-feeding of the separation elements during start-up or during low-load operation is permissible, so that part of the evaporator water to be ejected can be collected in the superheater tubes connected downstream of the evaporator tubes.
  • the design of the water collection systems such as the separation bottles or drain valves for correspondingly lower flow rates and thus cost-effective.
  • the displacement of the evaporation end point into the superheater tubes makes it possible to limit a possibly required water injection and the associated losses.
  • the steam generator 1 according to FIG. 1 is designed as a continuous steam generator and is connected downstream of the exhaust gas as part of a gas and steam turbine plant in the manner of a heat recovery steam generator of a gas turbine (not shown).
  • the steam generator 1 has a Um Publishedswand 2, which forms a Schugaskanal 4 for the exhaust gas from the gas turbine.
  • an evaporator pass-through heating surface 8 formed from a number of evaporator tubes 6 and a superheater heating surface 12 arranged downstream of the latter for the passage of a flow medium W, D are arranged, formed from a number of superheater tubes 10.
  • the superheater heating surface 12 of the evaporator throughflow heating surface 8 is arranged upstream, so that the exhaust gas from the gas turbine initially acts on the superheater heating surface 12.
  • the steam generator 1 is designed in a vertical construction, wherein the heating gas channel 4 is flowed through from the exhaust gas of the gas turbine in the area of the evaporator fürlaufsammlung phenomenon 8 and the Kochhitzersammlung constitutional 12 in a substantially vertical direction from bottom to top and at its upper end in a chimney 14th ends.
  • the evaporator tubes 6 and the superheater tubes 10 are laid in the manner of pipe coils alternately oriented horizontally in the heating gas channel 4.
  • the steam generator 1 could also be designed in a horizontal construction for a substantially horizontally guided flue gas flow in the heating gas channel 4, preferably with alternately vertically oriented coils.
  • the evaporator tubes 6 of the evaporator continuous heating surface 8 are connected with their inlet ends to an inlet header 16.
  • the superheater tubes 10, however, are connected on the outlet side to an outlet header 18.
  • each evaporator tube 6 is connected to one superheater tube 10 via a respective overflow tube piece 20.
  • the continuous steam generator 1 is designed so that even in start-up or low-load operation in which the evaporator tubes 6 in addition to the vaporizable mass flow of flow medium W for reasons of operational safety yet another Ummélzmassenstrom is superimposed on flow medium W, the position of the evaporation end point for a particularly high operational flexibility can be kept variable.
  • the evaporation end point in start-up and low-load operation in the interpretation of the flow medium at the end of the evaporator tubes 6 is not completely evaporated, are moved into the superheater tubes 10.
  • the overflow pipe pieces 20 are provided with an integrated water separation function.
  • a water separation element 30 is integrated into each overflow pipe piece 20. This is in particular also achieved that after the water-vapor deposition, a complex distribution of water-vapor mixture W, D is not required on the superheater tubes 10.
  • This ensures that in connection with the water-vapor separation neither a collection of effluent from the evaporator tubes 6 flow medium nor a distribution of the continuing flow medium to the subsequent superheater tubes 10 is required.
  • the displacement of the evaporation end point in the superheater tubes 10 is made possible in a particularly simple manner.
  • a sufficiently uniform or evenly distributed transfer of water-vapor mixture to the superheater tubes 10 is also possible if a distribution to not more than about ten superheater tubes 10 takes place.
  • the respective Wasserabscheideelement 30 comprises a connected to the upstream evaporator tube 6 Einströmrohr Kab 32, seen in its longitudinal direction merges into a Wasserableitrohr Kab 34, wherein in the transition region 36 branches off a connected to the downstream superheater tube 10 Abströmrohr collage 38.
  • the Wasserabscheideelement 30 is designed for inertial separation of the flowing from the upstream evaporator tube 6 in the Einströmrohr.99 32 water-steam mixture. Because of its comparatively higher inertia, the proportion of water flowing through the inflow pipe 32 flows at the transition point 36 preferably in the axial extension of the Einströmrohr matterss 32 straight ahead and thus passes into the Wasserableitrohr collage 34. By contrast, the vapor fraction of the water-steam mixture flowing in the inflow pipe section 32 can better follow an imposed deflection due to its comparatively lower inertia and thus flows via the outflow pipe section 38 and the overflow pipe section 20 to the downstream superheater pipe 10.
  • Water outlet side, so on the Wasserableitrohr publishede 34, the Wasserabscheideieri 30 are connected in groups with a respective common outlet header 40, wherein a plurality of outlet headers 40 may be provided in groups.
  • the outlet headers 40 are in turn connected on the output side to a common water collecting container 42, in particular a separating bottle.
  • the designed as a T-piece of water Wasserabscheidemaschine 30 can be designed optimized in terms of their separation efficiency. Exemplary embodiments of this can be taken from FIGS. 3A to 3D.
  • the Einströmrohr consensus 32 may be carried out in a substantially rectilinear with its subsequent Wasserableitrohr yoga 34 and inclined with its longitudinal direction relative to the horizontal.
  • the bent pipe section 50 is additionally preceded by a bent pipe section 50 which due to its bending and its spatial arrangement causes the water flowing into the inflow pipe section 32 to flow preferentially to the inner wall side of the inflow pipe section 32 opposite the outflow pipe section 38 due to the centrifugal force and Wasserableitrohr collage 34 is pressed.
  • the further transport of the water content in the Wasserableitrohr Anlagen 34 is favored into, so that the Abscheide Angel increases overall.
  • the water collection tank 42 is connected on the output side via a connected drain line 52 with a sewer system, not shown.
  • the drainage line 52 may be connected directly or via an economizer heating surface, not shown, to the inlet header 12 upstream of the evaporator tubes 6, so that a closed circulating circuit is created, via which the flow medium flowing into the evaporator tubes 6 during start-up or low-load operation has an additional circulation can be superimposed to increase the operational safety.
  • the separation system 31 can be operated in such a manner that almost all of the water still entrained at the exit of the evaporator tubes 6 is separated from the flow medium and substantially only evaporated flow medium is passed on to the superheater tubes 10.
  • the Wasserabscheidesystem 31 but also be operated in the so-called over-feed mode in which not all water is separated from the flow medium, but together with the steam D a partial flow of entrained water is passed on to the superheater tubes 10.
  • the evaporation end point shifts into the superheater tubes 10.
  • first of all the water collecting container 42 and the upstream outlet collector 40 fill completely with water, so that a backflow forms up to the transition region 36 of the respective water separation elements 30, at which the outlet pipe piece 38 branches off. Due to this backwater also experiences the water content of the Wasserabscheidemaschinen 30 incoming flow medium at least partially a deflection and thus passes together with the steam in the Abströmrohr consensus 38.
  • the height of the partial flow, which is supplied to the superheater tubes 10 together with the steam results here on the one hand from the total of the respective Wasserabscheideelement 30 supplied water mass flow and on the other hand from the discharged via the Wasserableitrohr Cluster 34 partial mass flow.
  • mass flow of water passed into the superheater tubes 10 mass flow of non-evaporated flow medium can be adjusted. This makes it possible, by controlling one or both of the mentioned variables, to adjust the proportion of unvaporized flow medium passed on to the superheater tubes 10 in such a way that, for example, a predetermined enthalpy is established at the end of the superheater heating surface 12.
  • the water separation system 31 is associated with a control device 60 which is connected on the input side to a measuring sensor 62 designed to determine a characteristic value characteristic of the enthalpy at the flue gas end of the superheater heating surface 12.
  • the control device 60 acts on the one hand on a switched into the drain line 52 of the water collection container 42 control valve 64 a. This can be achieved by targeted activation of the Control valve 64, the water flow can be specified, which is taken from the separation system 31. This mass flow can in turn be withdrawn from the flow medium in the water separation elements 30 and forwarded to the subsequent collection systems.
  • control valve 64 influencing the Wasserabscheideelement 30 respectively branched off water flow and thus influencing the after the deposition still passed in the flow medium to the superheater 10, water content possible.
  • control device 60 can still act on a circulating pump, so that the inflow rate of the medium into the water separation system 31 can be adjusted accordingly.

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Sustainable Development (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Energy (AREA)
  • Control Of Steam Boilers And Waste-Gas Boilers (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
  • Engine Equipment That Uses Special Cycles (AREA)
  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)
EP05007413A 2005-04-05 2005-04-05 Dampferzeuger Withdrawn EP1710498A1 (de)

Priority Applications (15)

Application Number Priority Date Filing Date Title
EP05007413A EP1710498A1 (de) 2005-04-05 2005-04-05 Dampferzeuger
US11/887,859 US8297236B2 (en) 2005-04-05 2006-03-31 Steam generator
EP06743231A EP1926934A2 (de) 2005-04-05 2006-03-31 Dampferzeuger
CA2603934A CA2603934C (en) 2005-04-05 2006-03-31 Steam generator
JP2008504750A JP4833278B2 (ja) 2005-04-05 2006-03-31 ボイラ
RU2007140865/06A RU2397405C2 (ru) 2005-04-05 2006-03-31 Парогенератор
CN2006800155792A CN101384854B (zh) 2005-04-05 2006-03-31 锅炉
PCT/EP2006/061225 WO2006106079A2 (de) 2005-04-05 2006-03-31 Dampferzeuger
BRPI0609735-9A BRPI0609735A2 (pt) 2005-04-05 2006-03-31 gerador de vapor
UAA200710991A UA89523C2 (en) 2005-04-05 2006-03-31 Steam generator
AU2006232687A AU2006232687B2 (en) 2005-04-05 2006-03-31 Steam generator
TW095111862A TWI356891B (en) 2005-04-05 2006-04-04 Steam generator
MYPI20061547A MY146130A (en) 2005-04-05 2006-04-05 Steam generator
ARP060101341A AR053572A1 (es) 2005-04-05 2006-04-05 Generador de vapor
ZA200708412A ZA200708412B (en) 2005-04-05 2007-10-02 Steam generator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP05007413A EP1710498A1 (de) 2005-04-05 2005-04-05 Dampferzeuger

Publications (1)

Publication Number Publication Date
EP1710498A1 true EP1710498A1 (de) 2006-10-11

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ID=34980384

Family Applications (2)

Application Number Title Priority Date Filing Date
EP05007413A Withdrawn EP1710498A1 (de) 2005-04-05 2005-04-05 Dampferzeuger
EP06743231A Withdrawn EP1926934A2 (de) 2005-04-05 2006-03-31 Dampferzeuger

Family Applications After (1)

Application Number Title Priority Date Filing Date
EP06743231A Withdrawn EP1926934A2 (de) 2005-04-05 2006-03-31 Dampferzeuger

Country Status (14)

Country Link
US (1) US8297236B2 (ja)
EP (2) EP1710498A1 (ja)
JP (1) JP4833278B2 (ja)
CN (1) CN101384854B (ja)
AR (1) AR053572A1 (ja)
AU (1) AU2006232687B2 (ja)
BR (1) BRPI0609735A2 (ja)
CA (1) CA2603934C (ja)
MY (1) MY146130A (ja)
RU (1) RU2397405C2 (ja)
TW (1) TWI356891B (ja)
UA (1) UA89523C2 (ja)
WO (1) WO2006106079A2 (ja)
ZA (1) ZA200708412B (ja)

Cited By (3)

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Publication number Priority date Publication date Assignee Title
WO2010029100A2 (de) * 2008-09-09 2010-03-18 Siemens Aktiengesellschaft Durchlaufdampferzeuger
WO2010029022A2 (de) * 2008-09-09 2010-03-18 Siemens Aktiengesellschaft Durchlaufdampferzeuger
WO2010029033A3 (de) * 2008-09-09 2010-06-10 Siemens Aktiengesellschaft Abhitzedampferzeuger

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EP2065641A3 (de) * 2007-11-28 2010-06-09 Siemens Aktiengesellschaft Verfahren zum Betrieben eines Durchlaufdampferzeugers sowie Zwangdurchlaufdampferzeuger
EP2119880A1 (de) * 2008-02-15 2009-11-18 Siemens Aktiengesellschaft Verfahren zum Anfahren eines Durchdampferzeugers
EP2180251A1 (de) * 2008-09-09 2010-04-28 Siemens Aktiengesellschaft Durchlaufdampferzeuger
DE102011006390A1 (de) * 2011-03-30 2012-10-04 Siemens Aktiengesellschaft Verfahren zum Betreiben eines Durchlaufdampferzeugers und zur Durchführung des Verfahrens ausgelegter Dampferzeuger
JP5187707B2 (ja) 2011-08-12 2013-04-24 株式会社ビクター特販 熱回収装置及び熱回収システム
CN103748414B (zh) 2012-01-17 2016-06-29 阿尔斯通技术有限公司 单程水平蒸发器中的管布置
CN103732989B (zh) 2012-01-17 2016-08-10 阿尔斯通技术有限公司 单程水平蒸发器中的管和挡板布置
US20140041359A1 (en) * 2012-08-13 2014-02-13 Babcock & Wilcox Power Generation Group, Inc. Rapid startup heat recovery steam generator
RU2515877C2 (ru) * 2012-09-10 2014-05-20 Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Самарский государственный технический университет" Промышленный прямоточный парогенератор
US20140123914A1 (en) * 2012-11-08 2014-05-08 Vogt Power International Inc. Once-through steam generator
EP2770171A1 (en) 2013-02-22 2014-08-27 Alstom Technology Ltd Method for providing a frequency response for a combined cycle power plant
EP3048366A1 (de) * 2015-01-23 2016-07-27 Siemens Aktiengesellschaft Abhitzedampferzeuger
EP3835653A1 (en) * 2019-12-11 2021-06-16 Siemens Aktiengesellschaft Hot evaporator refilling

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WO2010029022A2 (de) * 2008-09-09 2010-03-18 Siemens Aktiengesellschaft Durchlaufdampferzeuger
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EP2182278A1 (de) * 2008-09-09 2010-05-05 Siemens Aktiengesellschaft Durchlaufdampferzeuger
WO2010029100A3 (de) * 2008-09-09 2010-05-14 Siemens Aktiengesellschaft Durchlaufdampferzeuger
WO2010029022A3 (de) * 2008-09-09 2010-05-27 Siemens Aktiengesellschaft Durchlaufdampferzeuger
WO2010029033A3 (de) * 2008-09-09 2010-06-10 Siemens Aktiengesellschaft Abhitzedampferzeuger
EP2204611A1 (de) * 2008-09-09 2010-07-07 Siemens Aktiengesellschaft Abhitzedampferzeuger
CN102171513A (zh) * 2008-09-09 2011-08-31 西门子公司 废热蒸汽发生器
CN102089583B (zh) * 2008-09-09 2013-04-10 西门子公司 连续蒸汽发生器
CN102171513B (zh) * 2008-09-09 2013-11-20 西门子公司 废热蒸汽发生器
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US8701602B2 (en) 2008-09-09 2014-04-22 Siemens Aktiengesellschaft Waste heat steam generator
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JP4833278B2 (ja) 2011-12-07
CA2603934A1 (en) 2006-10-12
TW200702598A (en) 2007-01-16
BRPI0609735A2 (pt) 2010-04-27
AU2006232687A1 (en) 2006-10-12
RU2007140865A (ru) 2009-05-20
EP1926934A2 (de) 2008-06-04
AU2006232687B2 (en) 2011-06-16
CN101384854A (zh) 2009-03-11
RU2397405C2 (ru) 2010-08-20
UA89523C2 (en) 2010-02-10
WO2006106079A2 (de) 2006-10-12
US20090071419A1 (en) 2009-03-19
WO2006106079A3 (de) 2008-04-10
AR053572A1 (es) 2007-05-09
US8297236B2 (en) 2012-10-30
MY146130A (en) 2012-06-29
CN101384854B (zh) 2010-12-08
ZA200708412B (en) 2009-10-28
JP2008534909A (ja) 2008-08-28
TWI356891B (en) 2012-01-21

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