EP1701090A1 - Dampferzeuger in liegender Bauweise - Google Patents

Dampferzeuger in liegender Bauweise Download PDF

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Publication number
EP1701090A1
EP1701090A1 EP05003268A EP05003268A EP1701090A1 EP 1701090 A1 EP1701090 A1 EP 1701090A1 EP 05003268 A EP05003268 A EP 05003268A EP 05003268 A EP05003268 A EP 05003268A EP 1701090 A1 EP1701090 A1 EP 1701090A1
Authority
EP
European Patent Office
Prior art keywords
steam generator
water
flow
tubes
steam
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Withdrawn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
EP05003268A
Other languages
German (de)
English (en)
French (fr)
Inventor
Jan BRÜCKNER
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 EP05003268A priority Critical patent/EP1701090A1/de
Priority to ES06708193.5T priority patent/ES2609410T3/es
Priority to PCT/EP2006/050851 priority patent/WO2006087299A2/de
Priority to RU2007134409/06A priority patent/RU2382936C2/ru
Priority to US11/884,284 priority patent/US7628124B2/en
Priority to EP06708193.5A priority patent/EP1848925B1/de
Priority to BRPI0608082-0A priority patent/BRPI0608082A2/pt
Priority to AU2006215685A priority patent/AU2006215685B2/en
Priority to CA2597936A priority patent/CA2597936C/en
Priority to PL06708193T priority patent/PL1848925T3/pl
Priority to CNB2006800050837A priority patent/CN100572911C/zh
Priority to JP2007554565A priority patent/JP4781370B2/ja
Priority to TW095104819A priority patent/TWI357965B/zh
Priority to ARP060100530A priority patent/AR052290A1/es
Priority to MYPI20060678A priority patent/MY145953A/en
Publication of EP1701090A1 publication Critical patent/EP1701090A1/de
Priority to UAA200709315A priority patent/UA88350C2/ru
Priority to ZA200705853A priority patent/ZA200705853B/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Withdrawn legal-status Critical Current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
    • 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
    • F22B37/26—Steam-separating arrangements

Definitions

  • the invention relates to a steam generator, in which an evaporator fürlaufterrorism Design is arranged in a flow-through in an approximately horizontal Kleingasschschkanal an evaporator fürlaufterrorism phenomenon comprising a number of parallel to the flow of a flow medium steam generator tubes, with a number of each a few steam generator tubes flow medium side downstream outlet collectors.
  • the heat contained in the relaxed working fluid or heating gas from the gas turbine is used to generate steam for the steam turbine.
  • the heat transfer takes place in a gas turbine downstream heat recovery steam generator, in which usually a number of heating surfaces for water preheating, steam generation and steam superheating is arranged.
  • the heating surfaces are connected in the water-steam cycle of the steam turbine.
  • the water-steam cycle usually includes several, z. B. three, pressure levels, each pressure stage may have a Verdampferloom phenomenon.
  • a continuous steam generator In contrast to a natural or forced circulation steam generator, 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.
  • a high live steam pressure promotes a high thermal efficiency and thus low CO 2 emissions of a fossil-fired power plant.
  • a continuous steam generator in comparison to a circulating steam generator a simple construction and is thus produced with very little effort.
  • the use of a designed according to the flow principle steam generator as heat recovery steam generator of a gas and steam turbine plant is therefore particularly favorable to achieve a high overall efficiency of the gas and steam turbine plant with a simple design.
  • this continuous steam generator In order to ensure between homogenization and stabilization of the flow conditions seen in Schugasraum successively arranged evaporator tubes, this continuous steam generator, a number of the Evaporator fürlaufsammlung configuration downstream outlet collectors, which are aligned with their longitudinal direction substantially parallel to the direction of the heating gas and thus record the seen from in Walkergasraum successively arranged and thus differently heated evaporator tubes flowing out flow medium.
  • These outlet headers of the evaporator continuous heating surface also serve as inlet manifolds for the downstream superheater heating surface.
  • a continuous steam generator is operated in low-load operation or when starting with a minimum flow of flow medium in the evaporator tubes to ensure reliable cooling of the evaporator tubes and to avoid possible formation of steam in the evaporator fürlaufsammlung Structure flow medium side upstream economizer heating.
  • This minimum flow is not completely evaporated during startup or during low-load operation in the evaporator tubes, so that in such an operating mode at the end of the evaporator tubes still unvaporized flow medium is present. In other words, in this mode of operation, a water-steam mixture emerges from the evaporator tubes.
  • the invention is therefore an object of the invention to provide a continuous steam generator of the type mentioned above, which allows for low production costs even in start-up or low load operation, a particularly high operational flexibility and thus in particular also kept low start-up and load change times.
  • each outlet collector each comprises an integrated Wasserabscheiderelement via which the respective outlet collector flow medium side is connected to a number of downstream superheater tubes a Kochhitzerschreib phenomenon.
  • the invention is based on the consideration that in order to achieve a particularly high operational flexibility even in start-up or low-load operation, a particularly large proportion of the total available heating surfaces should be usable for evaporation purposes.
  • a superheater heating surface connected downstream of the evaporator throughflow heating surface should also be used for evaporation of the flow medium if necessary, that is to say just for start-up or light-load purposes.
  • the evaporation end point should be slidable into the superheater heating surface.
  • the transition area between the evaporator passage heating surface and the subsequent superheater heating surface should be designed such that a feed of water into the superheater heating surface is possible.
  • the water separation system connected between the evaporator flow heating surface and the superheater heating surface should be designed such that a complex distribution is not required.
  • the type of construction anyway associated with only a small number of evaporator tubes, provided with their longitudinal direction in Walkergasraum outlet collector are provided.
  • the outlet collectors are designed for a water-vapor separation according to the principle of inertial separation as required.
  • the knowledge is used that due to the considerable inertial differences between steam on the one hand and water on the other hand, the vapor content of a water-steam mixture at an existing flow comparatively much easier deflection can be subjected as the proportion of water.
  • the respective outlet header is designed substantially as a cylinder body which is connected at its not connected to the steam generator tubes end with a Wasserableitrohr consensus.
  • the discharge collector provided with an integrated water separation function is thus essentially in the manner of a T-piece formed, in which the cylinder body forms a substantially straight-through channel, in which due to its relatively higher inertia preferably the water content of the flow medium is performed. From this channel branches off the Abströmrohr congress, in which due to its relatively lower inertia preferably the vapor content of the flow medium is deflected into.
  • the outlet collector viewed from above - aligned with its longitudinal direction substantially parallel to the Schugasraum so that they take the view of Schugasraum successively arranged and thus differently heated evaporator tubes flowing flow medium.
  • the outlet header Viewed in the lateral direction, can also be aligned substantially parallel to the direction of the heating gas.
  • the outlet collector with integrated separation function is preferably designed so that on the one hand the water content of the flow medium is preferably guided on the inner wall of the cylinder body opposite the branching outflow pipe piece and on the other hand the discharge of the water is favored.
  • the cylinder body and / or the Wasserableitrohr choir are advantageously arranged with its longitudinal direction relative to the horizontal in the flow direction of the flow medium inclined downwards.
  • the inclination can also be relatively strong, so that the cylinder body is oriented substantially vertically.
  • said inertia separation is additionally favored by the gravitational effect on the water content of the flow medium flowing in the cylinder body.
  • a particularly simple design with regard to the flow guidance of the separated water can be achieved by advantageously some or all Wasserabscheideretti water outlet side groups each with a common Outlet collector are connected, in turn, in a further advantageous embodiment, a water collection tank is connected downstream.
  • downstream water components such as outlet header or water tank are completely filled with water, so that forms a backwater with further inflowing water in the corresponding line pieces.
  • this backwater has reached the Wasserabscheideremia, at least a partial flow of new inflowing water is passed along with the entrained in the flow medium steam to the subsequent superheater tubes.
  • this partial flow corresponds to the amount of water that can not be absorbed by the downstream components of the water separator elements.
  • control device is advantageously in a connected to the water collection drain pipe connected via an associated control device controllable control valve.
  • the control device is advantageously acted upon by an input value characteristic of the enthalpy of the flow medium on the steam-side outlet of the superheater heating surface arranged downstream of the water separation system.
  • 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. Since this is replaced by a corresponding mass flow of water from the Wasserabscheiderettin, thus, the mass flow is adjustable, which passes from the Wasserabscheiderimplantationn in the collection system. Thus, in turn, the remaining 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 downstream superheater.
  • 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.
  • the control device associated with the evaporator tubes circulating pump can be controlled.
  • the respective outlet collector provided with integrated water separation function is designed for the use of gravity to facilitate the removal of the separated water.
  • the or each outlet collector is advantageously arranged above the Schugaskanals.
  • a particularly high operational stability of the steam generator can be achieved by the evaporator fürlaufsammlung Design is designed for a self-stabilizing flow behavior with occurring heating differences between individual steam generator tubes of fürlaufsammlung description.
  • This can be achieved by the evaporator fürlaufsammlung construction is designed in a particularly advantageous embodiment such that a more heated compared to another steam generator tube fürlaufsammlung construction same steam generator tube has a higher compared to the other steam generator tube throughput of the flow medium.
  • the thus designed evaporator fürlauf carving phenomenon thus shows in the nature of the flow characteristics of a Bachumlaufverdampferloom configuration (natural circulation) with occurring different heating individual steam generator tubes a self-stabilizing behavior that leads to an adjustment of the exit temperatures even at differently heated, flow medium side parallel steam turbine tubes without the need for external influence ,
  • the steam generator is used as a heat recovery steam generator of a gas and steam turbine plant.
  • the steam generator is advantageously followed by a gas turbine on the hot gas side.
  • this circuit can expediently be arranged behind the gas turbine an additional firing to increase the temperature of the heating gas.
  • a decentralized Wasserabscheidesystem can be provided by the integration of Wasserabscheidefunktion in the outlet collector, in which due to the small number of each water separator downstream Uberhitzerrohre a complex distribution system can be omitted, so is also a feed-through of unevaporated flow medium through the water separator possible, so that the evaporation end point can be moved into the superheater tubes if necessary.
  • a particularly high operational flexibility can be achieved even under these load conditions.
  • the T-piece-like configuration of the outlet collector as a cylinder body with branching Abströmrohr published can also be achieved by simple means a reliable water separation according to the principle of inertial separation.
  • FIG. 1 shows in a simplified representation in longitudinal section the evaporator section of a steam generator in horizontal construction.
  • the steam generator 1 has a surrounding wall 2, which forms a in a nearly horizontal, indicated by the arrows 4
  • Bankgasraum x fuel gas channel 6 for the exhaust gas from the gas turbine.
  • a designed according to the flow principle evaporator fürlauf redesign 8 is arranged, which is followed by a superheater 10 for the flow of a flow medium W, D.
  • the evaporator fürlauf carving scene 8 is acted upon with unvaporized flow medium W, which evaporates in normal or full load operation with a single pass through the evaporator fürlaufsammlung construction 8 and after exiting the evaporator fürlaufsammlung construction 8 as steam D superheater 10 is supplied.
  • the evaporator through-flow heating surface 8 and the superheater 10 formed evaporator system is connected in the non-illustrated water-steam cycle of a steam turbine.
  • a number of other, not shown in FIG heating surfaces are connected in the water-steam cycle of the steam turbine, which, for example, in which can be superheater, medium pressure evaporator, low pressure evaporator and / or preheater.
  • the evaporator passage heating surface 8 is formed by a number of parallel to the flow of the flow medium W steam generator tubes 12.
  • the steam generator tubes 12 are aligned substantially vertically with their longitudinal axis and designed for a flow through the flow medium W from a lower inlet region to an upper outlet region, ie from bottom to top.
  • the evaporator fürlaufsammlung design 8 comprises in the manner of a tube bundle a number of seen in Bankgasraum x successively arranged pipe layers 14, each of which is formed from a number of viewed in Bankgasraum x juxtaposed steam generator tubes 12, and of which in FIG each only one Steam generator tube 12 is visible.
  • Each pipe layer 14 may comprise up to 200 steam generator tubes 12.
  • the steam generator tubes 12 of each tube layer 14 are each preceded by a common inlet collector 16 aligned with its longitudinal direction substantially perpendicular to the heating gas direction x and arranged below the heating gas channel 6.
  • a common inlet header 16 may also be assigned to a plurality of pipe layers 14.
  • the inlet header 16 are connected to a in FIG only schematically indicated water supply system 18, which may include a distribution system for needs-based distribution of the influx of flow medium W to the inlet header 16.
  • the superheater heating surface 10 is formed by a number of superheater tubes 22. These are designed in the exemplary embodiment for a flow of the flow medium in the downward direction, ie from top to bottom.
  • the superheater tubes 22 On the input side is the superheater tubes 22 upstream of a number of designed as a so-called T-distributor distributors 24.
  • the superheater tubes 22 open into a common live steam collector 26, from which the superheated live steam can be supplied in a manner not shown to an associated steam turbine.
  • the live steam collector 26 is arranged below the heating gas channel 6.
  • the Uberhitzersammlung the Uberhitzerterrorism
  • each superheater tube 22 each comprise a downcomer piece and this downstream riser piece, wherein the live steam collector 26 as well as the outlet header 20 is disposed above the Schugaskanals 6.
  • a drainage collector can be connected between downpipe pipe and riser pipe piece.
  • the evaporator pass-through heating surface 8 is designed such that it is suitable for feeding the steam generator tubes 12 with a comparatively low mass flow density, wherein the design flow conditions in the steam generator tubes 12 have a natural circulation characteristic. In this natural circulation characteristic, a more heated steam generator tube 12 compared to another steam generator tube 12 of the same evaporator pass-through heating surface 8 has a higher throughput of the flow medium W compared to the other steam generator tube 12.
  • the steam generator 1 is designed for a reliable, homogeneous flow guidance with a comparatively simple construction.
  • the designed according to the design of the evaporator fürlaufsammlung Design 8 natural circulation characteristic is consistently used for a simple held distribution system.
  • This natural circulation characteristic and the concomitantly designed, comparatively low mass flow density that is provided allow the merging of the partial flows from one another in heating gas direction x arranged and thus differently heated steam generator tubes in a common room.
  • With the saving of an autonomous complex distribution system it is thus possible to shift the mixing of the flow medium W flowing out of the evaporator through-flow heating surface 8 into the outlet collector or outlets 20.
  • the number of outlet headers 20 is adapted to the number of steam generator tubes 12 in each tube layer 14, so that in each case an outlet header 20 is assigned to each of the steam generator tubes 12 positioned one behind the other, forming a so-called evaporator disc.
  • the distributors 24 are each aligned with their longitudinal axis parallel to the heating gas direction x, so that in each case a respective distributor 24 is assigned to the respective superheater tubes 22 positioned in succession.
  • the steam generator 1 is designed so that, if necessary, in particular in start-up or low-load operation, the steam generator tubes 12 in addition to the vaporizable mass flow of flow medium for reasons of operational safety yet another Umicalzmassenstrom can be superimposed on the flow medium.
  • the steam generator tubes 12 in the Superheater tubes 22 can be moved into it.
  • each of the outlet headers 20 comprises an integrated water separator element 28, via which the respective outlet header 20 is connected via an overflow pipe 30 to one of the downstream distributors 24 on the flow medium side.
  • the discharge collectors 20 each provided with integrated separation function are designed for the concept of inertial separation of a water-steam mixture.
  • the knowledge is used that the water content of a water-steam mixture due to its relatively greater inertia at a branch point preferably continues to flow straight in its flow direction, whereas the vapor content of a forced deflection is relatively easier to follow due to its relatively lower inertia.
  • the outlet headers 20 are each embodied in the form of T-pieces, wherein an outlet pipe piece 34 for flow medium branches off from a main body designed substantially as a cylinder body 32.
  • the designed as a cylinder body 32 main body of the respective outlet header 20 is connected at its not connected to the steam generator tubes 12 end 36 with a Wasserableitrohr Gi 38.
  • this construction thus flows the water content of the water-steam mixture in the outlet header 20 at which the respective integrated Wasserabscheiderelement 28 forming branch point of Abströmrohr ceremoniess 34 preferably in the axial direction and passes
  • the steam content of the water-steam mixture flowing in the cylinder body 32 can better follow an imposed deflection because of its comparatively lower inertia and thus preferably flows via the outflow pipe section 34 and the further intermediate components to the downstream superheater pipes 22 too.
  • the cylinder body 32 can be arranged with its longitudinal direction opposite the horizontal in the flow direction inclined downwards.
  • Water outlet side, so on the Wasserableitrohr Communitye 38, the integrated into the outlet header 20 Wasserabscheiderieri 28 are connected in groups with a respective common outlet header 40.
  • This is a water collection tank 42, in particular a separation bottle, downstream.
  • the water collecting container 42 is connected via a connected outflow line 44, from which also a discharge line 45 connected to a sewage system, to the water supply system 18 of the continuous evaporator heating surface 8, so that a closed circulation circuit can be operated.
  • This circulation can be superimposed in the start, low or partial load operation flowing into the steam generator tubes 12 evaporable flow medium, an additional circulation to increase the operational safety.
  • the separating system formed by the integrated water separator elements 28 can be operated in such a way that all water still entrained at the outlet of the steam generator tubes 12 is separated from the flow medium and only evaporated flow medium is passed on to the superheater tubes 22.
  • the Wasserabscheidesystem can also be operated in the so-called over-flow mode, in which not all water is separated from the flow medium, but together with the steam, a partial flow of entrained water is passed on to the superheater tubes 22.
  • the evaporation end point shifts into the superheater tubes 22.
  • over-fed mode first both the water collecting container 42 and the upstream outlet header 40 completely fill with water, so that a backflow forms up to the transition region respective water separator 28, at which the Abströmrohr Schi 34 branches off. Due to this backwater also experiences the water content of the water separator elements 28 incoming flow medium at least partially a deflection and thus passes together with the steam in the Abströmrohr sang 34.
  • the height of the partial flow, which is supplied to the superheater tubes 22 together with the steam results in the process on the one hand, from the total water mass flow supplied to the respective water separator element 28 and, on the other hand, from the partial mass flow discharged via the water drainage pipe section 38.
  • suitable variation of the supplied water mass flow and / or the water mass flow discharged via the Wasserableitrohr choir 38 of the passed into the superheater tubes 22 mass flow can be adjusted to non-vaporized flow medium.
  • the water separation system 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 22.
  • the control device 60 acts, on the one hand, on a control valve 64 connected in the outflow line 44 of the water collecting container 42. This can be specified by selective control of the control valve 64, the water flow, the off taken from the separation system. This mass flow can in turn be withdrawn from the flow medium in the water separator elements 28 and forwarded to the subsequent collection systems.
  • control valve 64 influencing the Wasserabscheiderelement 28 respectively branched off water flow and thus influencing the after the deposition still passed in the flow medium to the Matterhitzersammlung vom 22 water content possible.
  • control device 60 can still act on a circulating pump 66 connected in the outflow line 44, so that the inflow rate of the medium into the water separation system can also be adjusted accordingly.

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  • Engineering & Computer Science (AREA)
  • General Engineering & Computer Science (AREA)
  • Thermal Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Mechanical Engineering (AREA)
  • Combustion & Propulsion (AREA)
  • Physics & Mathematics (AREA)
  • Sustainable Energy (AREA)
  • Sustainable Development (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Control Of Steam Boilers And Waste-Gas Boilers (AREA)
  • Engine Equipment That Uses Special Cycles (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Central Heating Systems (AREA)
EP05003268A 2005-02-16 2005-02-16 Dampferzeuger in liegender Bauweise Withdrawn EP1701090A1 (de)

Priority Applications (17)

Application Number Priority Date Filing Date Title
EP05003268A EP1701090A1 (de) 2005-02-16 2005-02-16 Dampferzeuger in liegender Bauweise
PL06708193T PL1848925T3 (pl) 2005-02-16 2006-02-10 Wytwornica pary o konstrukcji poziomej
CNB2006800050837A CN100572911C (zh) 2005-02-16 2006-02-10 水平构造形式的蒸汽发生器
RU2007134409/06A RU2382936C2 (ru) 2005-02-16 2006-02-10 Парогенератор горизонтального типа
US11/884,284 US7628124B2 (en) 2005-02-16 2006-02-10 Steam generator in horizontal constructional form
EP06708193.5A EP1848925B1 (de) 2005-02-16 2006-02-10 Dampferzeuger in liegender bauweise
BRPI0608082-0A BRPI0608082A2 (pt) 2005-02-16 2006-02-10 gerador de vapor em técnica de construção deitada
AU2006215685A AU2006215685B2 (en) 2005-02-16 2006-02-10 Horizontally positioned steam generator
CA2597936A CA2597936C (en) 2005-02-16 2006-02-10 Steam generator in horizontal constructional form
ES06708193.5T ES2609410T3 (es) 2005-02-16 2006-02-10 Generador de vapor de tipo horizontal
PCT/EP2006/050851 WO2006087299A2 (de) 2005-02-16 2006-02-10 Dampferzeuger in liegender bauweise
JP2007554565A JP4781370B2 (ja) 2005-02-16 2006-02-10 横形ボイラ
TW095104819A TWI357965B (en) 2005-02-16 2006-02-14 Steam generator in horizontally situated construct
ARP060100530A AR052290A1 (es) 2005-02-16 2006-02-15 Generador de vapor
MYPI20060678A MY145953A (en) 2005-02-16 2006-02-16 Steam generator of horizontal construction type
UAA200709315A UA88350C2 (ru) 2005-02-16 2006-10-02 Парогенератор горизонтального типа конструкции
ZA200705853A ZA200705853B (en) 2005-02-16 2007-07-16 Horizontally positioned steam generator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP05003268A EP1701090A1 (de) 2005-02-16 2005-02-16 Dampferzeuger in liegender Bauweise

Publications (1)

Publication Number Publication Date
EP1701090A1 true EP1701090A1 (de) 2006-09-13

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Family Applications (2)

Application Number Title Priority Date Filing Date
EP05003268A Withdrawn EP1701090A1 (de) 2005-02-16 2005-02-16 Dampferzeuger in liegender Bauweise
EP06708193.5A Active EP1848925B1 (de) 2005-02-16 2006-02-10 Dampferzeuger in liegender bauweise

Family Applications After (1)

Application Number Title Priority Date Filing Date
EP06708193.5A Active EP1848925B1 (de) 2005-02-16 2006-02-10 Dampferzeuger in liegender bauweise

Country Status (16)

Country Link
US (1) US7628124B2 (zh)
EP (2) EP1701090A1 (zh)
JP (1) JP4781370B2 (zh)
CN (1) CN100572911C (zh)
AR (1) AR052290A1 (zh)
AU (1) AU2006215685B2 (zh)
BR (1) BRPI0608082A2 (zh)
CA (1) CA2597936C (zh)
ES (1) ES2609410T3 (zh)
MY (1) MY145953A (zh)
PL (1) PL1848925T3 (zh)
RU (1) RU2382936C2 (zh)
TW (1) TWI357965B (zh)
UA (1) UA88350C2 (zh)
WO (1) WO2006087299A2 (zh)
ZA (1) ZA200705853B (zh)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2007133071A2 (en) * 2007-04-18 2007-11-22 Nem B.V. Bottom-fed steam generator with separator and downcomer conduit
WO2010029022A2 (de) * 2008-09-09 2010-03-18 Siemens Aktiengesellschaft Durchlaufdampferzeuger
WO2010029033A2 (de) 2008-09-09 2010-03-18 Siemens Aktiengesellschaft Abhitzedampferzeuger
WO2015028378A3 (de) * 2013-08-28 2015-05-28 Siemens Aktiengesellschaft Betriebsverfahren insbesondere zum anfahren eines solarthermisch beheizten zwangdurchlaufdampferzeugers

Families Citing this family (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1710498A1 (de) * 2005-04-05 2006-10-11 Siemens Aktiengesellschaft Dampferzeuger
EP2065641A3 (de) * 2007-11-28 2010-06-09 Siemens Aktiengesellschaft Verfahren zum Betrieben eines Durchlaufdampferzeugers sowie Zwangdurchlaufdampferzeuger
EP2180250A1 (de) * 2008-09-09 2010-04-28 Siemens Aktiengesellschaft Durchlaufdampferzeuger
DE102009012321A1 (de) * 2009-03-09 2010-09-16 Siemens Aktiengesellschaft Durchlaufverdampfer
NL2003596C2 (en) 2009-10-06 2011-04-07 Nem Bv Cascading once through evaporator.
US9273865B2 (en) * 2010-03-31 2016-03-01 Alstom Technology Ltd Once-through vertical evaporators for wide range of operating temperatures
ITMI20102463A1 (it) * 2010-12-30 2012-07-01 Stamicarbon Metodo per l'avviamento e la gestione di un impianto termico a ciclo combinato per la produzione di energia e relativo impianto
CN103688606B (zh) * 2011-07-15 2016-05-11 日本电气株式会社 冷却系统和使用该冷却系统的装置安放设备
WO2013108218A2 (en) 2012-01-17 2013-07-25 Alstom Technology Ltd Tube arrangement in a once-through horizontal evaporator
EP2839213B1 (en) 2012-01-17 2018-09-05 General Electric Technology GmbH Tube and baffle arrangement in a once-through horizontal evaporator
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BRPI0608082A2 (pt) 2009-11-10
CN101120206A (zh) 2008-02-06
EP1848925B1 (de) 2016-09-28
US7628124B2 (en) 2009-12-08
CA2597936C (en) 2013-10-29
CA2597936A1 (en) 2006-08-24
TWI357965B (en) 2012-02-11
MY145953A (en) 2012-05-31
CN100572911C (zh) 2009-12-23
JP4781370B2 (ja) 2011-09-28
TW200634258A (en) 2006-10-01
JP2008530494A (ja) 2008-08-07
ES2609410T3 (es) 2017-04-20
RU2007134409A (ru) 2009-03-27
PL1848925T3 (pl) 2017-03-31
AU2006215685B2 (en) 2010-09-30
WO2006087299A3 (de) 2006-11-16
UA88350C2 (ru) 2009-10-12
RU2382936C2 (ru) 2010-02-27
ZA200705853B (en) 2008-09-25
AU2006215685A1 (en) 2006-08-24

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