EP1288567A1 - Verfahren zum Anfahren eines Dampferzeugers mit einem in einer annähernd horizontalen Heizgasrichtung durchströmbaren Heizgaskanal und Dampferzeuger - Google Patents

Verfahren zum Anfahren eines Dampferzeugers mit einem in einer annähernd horizontalen Heizgasrichtung durchströmbaren Heizgaskanal und Dampferzeuger Download PDF

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Publication number
EP1288567A1
EP1288567A1 EP01121027A EP01121027A EP1288567A1 EP 1288567 A1 EP1288567 A1 EP 1288567A1 EP 01121027 A EP01121027 A EP 01121027A EP 01121027 A EP01121027 A EP 01121027A EP 1288567 A1 EP1288567 A1 EP 1288567A1
Authority
EP
European Patent Office
Prior art keywords
evaporator tubes
evaporator
flow medium
steam generator
flow
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Withdrawn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
EP01121027A
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 EP01121027A priority Critical patent/EP1288567A1/de
Priority to PL367786A priority patent/PL199757B1/pl
Priority to EP02797600A priority patent/EP1421317B1/de
Priority to RU2004109587/06A priority patent/RU2290563C2/ru
Priority to SK155-2004A priority patent/SK1552004A3/sk
Priority to CA002458390A priority patent/CA2458390C/en
Priority to US10/488,328 priority patent/US7281499B2/en
Priority to CNB028162439A priority patent/CN1289854C/zh
Priority to KR1020047002993A priority patent/KR100742407B1/ko
Priority to ES02797600T priority patent/ES2395897T3/es
Priority to PCT/EP2002/009312 priority patent/WO2003021148A2/de
Priority to JP2003525187A priority patent/JP2005523410A/ja
Priority to CZ2004403A priority patent/CZ2004403A3/cs
Publication of EP1288567A1 publication Critical patent/EP1288567A1/de
Priority to JP2008061279A priority patent/JP4970316B2/ja
Withdrawn legal-status Critical Current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
    • F22B35/00—Control systems for steam boilers
    • F22B35/06—Control systems for steam boilers for steam boilers of forced-flow type
    • F22B35/14—Control systems for steam boilers for steam boilers of forced-flow type during the starting-up periods, i.e. during the periods between the lighting of the furnaces and the attainment of the normal operating temperature of the steam boilers
    • 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

Definitions

  • the invention relates to a method for starting a Steam generator with one in an approximately horizontal Hot gas flow through the hot gas channel, in which at least one of a number of approximately vertically arranged, connected in parallel to flow through a flow medium Evaporator tubes formed flow heating surface arranged is. It further relates to such a steam generator.
  • the In a gas and steam turbine plant, the is relaxed Work equipment or heating gas contained in the gas turbine Heat used to generate steam for the steam turbine.
  • the heat transfer takes place in a downstream of the gas turbine Heat recovery steam generator, in which usually a Number of heating surfaces for water preheating, for steam generation and is arranged for steam superheating.
  • the heating surfaces are connected to the water-steam cycle of the steam turbine.
  • the water-steam cycle usually comprises several e.g. three, pressure levels, each pressure level an evaporator heating surface can have.
  • 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 live steam pressures far above the critical pressure of water (P Kri ⁇ 221 bar) - where there are only slight differences in density between liquid-like and steam-like medium - are possible.
  • a high live steam pressure promotes high thermal efficiency and thus low CO 2 emissions from a fossil-fired power plant.
  • a continuous steam generator has a simple construction in comparison to a circulation steam generator and can therefore be produced with particularly little effort.
  • the use of a steam generator designed according to the continuous flow principle as waste heat steam generator of a gas and steam turbine system is therefore particularly favorable in order to achieve a high overall efficiency of the gas and steam turbine system with a simple construction.
  • the invention is therefore based on the object of a method to start up a steam generator of the type mentioned above, with which even with a particularly simple design high operational security is guaranteed.
  • a particularly suitable one for carrying out the method Steam generator can be specified.
  • this object is achieved according to the invention solved by at least some of the continuous heating surface forming evaporator tubes before loading the heating gas duct with heating gas up to a predefinable target level partially filled with unevaporated flow medium.
  • the invention is based on the consideration that compliance a high level of operational security even during the Start-up of the steam generator must be excluded that unevaporated flow medium in the the evaporator tubes downstream superheater can reach. For one particularly simple construction, this should be avoided to those usually provided in continuous steam generators Water-steam separation device can be ensured. To should be used for a steam generator in a horizontal construction, in which one of the evaporator tubes forming the continuous heating surface outlet collector connected downstream on the outlet side is connected to an inlet manifold of the superheater the start-up only partially filling the evaporator tubes be carried out with unevaporated flow medium.
  • the filling quantity and thus the target level for this First filling before the heating gas duct is started with heating gas should be chosen such that on the one hand a water emission due to the first steam formation is avoided, and that, on the other hand, insufficient cooling the evaporator tubes are avoided when starting up.
  • the target fill level is expediently selected in such a way that that at the beginning of the start-up process a feed of the Evaporator tubes with flow medium can be omitted. Consequently takes place during the start-up process, i.e. after loading of the heating gas duct with the heating gas, initially one Evaporation of what is already in the evaporator tubes Flow medium.
  • the unevaporated flow medium, that within the respective evaporator tube downstream of the respective location of the start of evaporation is not due to the vapor bubble forming in the in advance filled zone of the respective evaporator tube pushed.
  • the undevaporated flow medium can evaporate or falls if the mass flow densities are sufficiently low in the evaporator tubes again in the lower ones Space area of the respective evaporator tube.
  • the choice of the target level can thus be in the upper range of the respective evaporator tube, initially not filled with flow medium and as compensation space for the underlying column serving as a flow medium of the respective evaporator tube are sufficiently large can be chosen so that an exit is not evaporated Flow medium from the respective evaporator tube also beginning evaporation can be safely excluded.
  • Heating gas is advantageously the actual level of the respective Evaporator tubes adjusted to the specified target level.
  • the respective actual fill level is advantageously by means of a differential pressure measurement between the lower pipe inlet and top pipe outlet of the respective evaporator pipe determined, the measurement value obtained thereby expediently as the basis for feeding the respective evaporator tube with unevaporated flow medium becomes.
  • the start-up phase varies a particularly reliable compliance with the boundary conditions ensure that on the one hand an exit when starting of unevaporated flow medium from the evaporator tubes reliably excluded and on the other hand in everyone If sufficient cooling of all evaporator tubes is guaranteed should be the one for the first filling of the evaporator tubes relevant target level advantageously in Dependency on the intended start-up heating process specified.
  • the start-up heating process will expediently based on characteristic values for the boiler geometry and / or the course of the heat supply over time the heating gas is determined. It can be used for a variety of such Parameter combinations, each adapted start-up heating process in a database assigned to the steam generator be deposited, in particular also the current one Heating cycle previous heating cycles taken into account could be.
  • a particularly high operational stability of the steam generator to ensure, is advantageous when feeding the evaporator tubes with flow medium whose mass flow density set so that a compared to another evaporator tube of the same continuous heating surface multi-heated evaporator tube one compared to the other Evaporator tube has higher throughput of the flow medium.
  • the continuous heating surface of the steam generator thus shows in the type of flow characteristic of a natural circulation evaporator heating surface (Natural circulation characteristic) when occurring different heating of individual evaporator tubes self-stabilizing behavior without the requirement external influence to align the exit side Temperatures also on differently heated, fluid medium side evaporator tubes connected in parallel leads. To ensure this characteristic is an application of the evaporator tubes with comparatively less Mass flow density provided.
  • the stated object is achieved by a distributor upstream of the evaporator tubes and an outlet header downstream of the evaporator tubes a common differential pressure measuring device assigned.
  • a common differential pressure measuring device assigned to the differential pressure measuring device.
  • the level in the evaporator tubes is particularly favorable Way can be monitored so that a characteristic Characteristic value as a suitable reference variable for feeding the Evaporator tubes can be used.
  • the advantages achieved with the invention are in particular in that by only partially filling the Evaporator tubes with unevaporated flow medium in front of one first application of heating gas to the heating gas duct
  • a particularly safe and stable Operating behavior can be achieved in particular by the evaporator tubes with a comparatively low mass flow density be applied so that in the evaporator tubes located undevaporated flow medium even when it starts Vapor formation remains in the respective evaporator tube and ultimately evaporates there too.
  • An embodiment of the invention is based on a Drawing explained in more detail. In it the figure shows in simplified Representation in longitudinal section of a steam generator in horizontal construction.
  • the steam generator 1 is in the manner of a heat recovery steam generator a gas turbine, not shown downstream on the exhaust gas side.
  • the steam generator 1 has a surrounding wall 2, one in an approximately horizontal, by the arrows 4 indicated heating gas direction x flow-through heating gas channel 6 for the exhaust gas from the gas turbine forms.
  • heating gas channel 6 is a number of after Continuous flow evaporator heating surface, also as Pass-through heating surface 8, 10, arranged.
  • two continuous heating surfaces 8, 10 are shown, but it can also be only one or a larger number be provided by continuous heating surfaces.
  • the continuous heating surfaces 8, 10 of the steam generator 1 include a plurality of each in the manner of a tube bundle Flow through a flow medium W connected in parallel Evaporator tubes 14 and 15.
  • the evaporator tubes 14, 15 are each aligned approximately vertically, with each a plurality of evaporator tubes 14 and 15 in the heating gas direction x seen is arranged side by side. It is in each case only one of the evaporator tubes arranged side by side in this way 14 or 15 visible.
  • the evaporator tubes 14 of the first continuous heating surface 8 A common distributor 16 on the flow medium side upstream and a common outlet header 18 connected.
  • the outlet header 18 of the first continuous heating surface 8 is in turn on the outlet side via a downpipe system 20 with a the second continuous heating surface 10 associated distributor 22 connected.
  • On the output side is the second continuous heating surface 10 downstream of an outlet header 24.
  • the evaporator system formed by the continuous heating surfaces 8, 10 can be acted upon with flow medium W, the one Passes through the evaporator system and evaporates dissipated as steam D after leaving the evaporator system and one of the outlet collector 24 of the second continuous heating surface 10 downstream superheater heating surface 26 is fed. That from the continuous heating surfaces 8, 10 and that formed after this superheater heating surface 26 Pipe system is in the water-steam cycle, not shown switched to a steam turbine. In addition, in the steam turbine water-steam cycle a number of others, in the figure schematically indicated heating surfaces 28 switched. With the heating surfaces 28, for example around medium pressure evaporators, low pressure evaporators and / or act as preheaters.
  • the evaporator system formed by the continuous heating surfaces 8, 10 is designed in such a way that it is suitable for feeding the Evaporator tubes 14, 15 with a comparatively low mass flow density is suitable, the evaporator tubes 14, 15 have a natural circulation characteristic. With this natural circulation characteristic has one compared to another Evaporator tube 14 or 15 of the same continuous heating surface 8 or 10 more heated evaporator tubes 14 or 15 in comparison to the further evaporator tube 14 or 15 higher throughput of the flow medium W.
  • the steam generator 1 is in comparison kept simple construction. This includes the second continuous heating surface 10 without a comparatively elaborate water-steam separation system or separation system directly with the superheater heating surface downstream 26 connected so that the outlet manifold 24th the second continuous heating surface 10 directly over a Overflow line and without the interposition of other components connected to a distributor of the superheater heating surface 26 is.
  • the steam generator 1 In order to be comparatively structural in this, too simple design in all operating conditions to maintain a comparatively high level of operational security, is the steam generator 1 when starting with regard to operated these constraints.
  • the filling the evaporator tubes 14 with undevaporated flow medium W before the start of heating takes place via the anyway existing feed water line and the distributor 16.
  • a common differential pressure measuring device 32 is assigned. Based on the actual level determined in each evaporator tube 14 is the further filling with unevaporated flow medium W controlled such that the predetermined target level taken within a specified tolerance band becomes.
  • any remaining unevaporated flow medium W is via the downpipe system 20 in the downstream second Pass-through heating surface 10 transferred and completely evaporated there.
  • the second continuous heating surface 10 thus takes in each Drop the remaining water output from the first Pass-through heating surface 8. Because of the only partial Filling the evaporator tubes 14 before the start of the actual one The start-up process therefore occurs with little or no vaporization Flow medium W in the second continuous heating surface 10 downstream outlet header 24 or in the this downstream superheater heating surface 26.
  • the filling is only partial of the evaporator tubes forming the first continuous heating surface 8 14 provided; the second continuous heating surface 10 initially remains unfilled.
  • a partial filling the evaporator tubes forming the second continuous heating surface 10 15 can be provided with an analogous procedure.
  • a pressure measurement of the flow medium W or Vapor D particularly at the outlet header 24 or at the outlet the superheater heating surface 26.
  • Via one accordingly arranged pressure sensor is a for the pressure of the evaporated flow medium or vapor D in the outlet header 24 or more characteristic at the outlet of the superheater heating surface Measured value recorded and monitored. At the beginning of steam production is closed based on the onset of pressure increase, of values of a few when steam formation begins bar per minute.
  • the operational Conveying feed water or unevaporated flow medium W in the distributor assigned to the continuous heating surface 8 16 added.
  • the supply of feed water or unevaporated Flow medium W in the evaporator tubes 14 regulated in such a way that at the upper tube outlet 34 of the evaporator tubes 14 superheated steam D, i.e. Steam D without wet components, exit.
  • the evaporator tubes 14 are supplied with Flow medium W whose mass flow density is set in such a way that one compared to another evaporator tube 14 more heated evaporator tube 14 compared to another evaporator tube 14 higher throughput of the flow medium W. This ensures that the continuous heating surface 8 even if different heating occurs individual evaporator tubes 14 in the manner of the flow characteristic a natural circulation evaporator heating surface shows self-stabilizing behavior.

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • General Engineering & Computer Science (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Development (AREA)
  • Sustainable Energy (AREA)
  • Control Of Steam Boilers And Waste-Gas Boilers (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
EP01121027A 2001-08-31 2001-08-31 Verfahren zum Anfahren eines Dampferzeugers mit einem in einer annähernd horizontalen Heizgasrichtung durchströmbaren Heizgaskanal und Dampferzeuger Withdrawn EP1288567A1 (de)

Priority Applications (14)

Application Number Priority Date Filing Date Title
EP01121027A EP1288567A1 (de) 2001-08-31 2001-08-31 Verfahren zum Anfahren eines Dampferzeugers mit einem in einer annähernd horizontalen Heizgasrichtung durchströmbaren Heizgaskanal und Dampferzeuger
CNB028162439A CN1289854C (zh) 2001-08-31 2002-08-20 带有沿水平燃气方向穿过的通道的蒸汽发生器及起动方法
KR1020047002993A KR100742407B1 (ko) 2001-08-31 2002-08-20 증기 발생기 및 거의 수평인 가열 가스 방향으로횡단가능한 가열 가스 채널을 포함하는 증기 발생기 시동방법
RU2004109587/06A RU2290563C2 (ru) 2001-08-31 2002-08-20 Способ запуска парогенератора и парогенератор
SK155-2004A SK1552004A3 (en) 2001-08-31 2002-08-20 Method for starting a steam generator comprising a heating gas channel that can be traversed in an approximately horizontal heating gas direction and a steam generator
CA002458390A CA2458390C (en) 2001-08-31 2002-08-20 Method for starting a steam generator comprising a heating gas channel that can be traversed in an approximately horizontal heating gas direction and a steam generator
US10/488,328 US7281499B2 (en) 2001-08-31 2002-08-20 Method for starting a steam generator comprising a heating gas channel that can be traversed in an approximately horizontal heating gas direction and a steam generator
PL367786A PL199757B1 (pl) 2001-08-31 2002-08-20 Sposób rozruchu wytwornicy pary z kanałem gazu grzejnego przepływanym w zbliżonym do poziomego kierunku przepływu gazu grzejnego i wytwornica pary
EP02797600A EP1421317B1 (de) 2001-08-31 2002-08-20 Verfahren zum anfahren eines dampferzeugers mit einem in einer annähernd horizontalen heizgasrichtung durchströmbaren heizgaskanal und dampferzeuger
ES02797600T ES2395897T3 (es) 2001-08-31 2002-08-20 Procedimiento para el arranque de un generador de vapor con un canal de gas que puede circular en una dirección de gas caliente aproximadamente horizontal y generador de vapor
PCT/EP2002/009312 WO2003021148A2 (de) 2001-08-31 2002-08-20 Verfahren zum anfahren eines dampferzeugers mit einem in einer annähernd horizontalen heizgasrichtung durchströmbaren heizgaskanal und dampferzeuger
JP2003525187A JP2005523410A (ja) 2001-08-31 2002-08-20 ボイラとその起動方法
CZ2004403A CZ2004403A3 (cs) 2001-08-31 2002-08-20 Název neuveden
JP2008061279A JP4970316B2 (ja) 2001-08-31 2008-03-11 廃熱ボイラとその起動方法

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP01121027A EP1288567A1 (de) 2001-08-31 2001-08-31 Verfahren zum Anfahren eines Dampferzeugers mit einem in einer annähernd horizontalen Heizgasrichtung durchströmbaren Heizgaskanal und Dampferzeuger

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EP1288567A1 true EP1288567A1 (de) 2003-03-05

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EP01121027A Withdrawn EP1288567A1 (de) 2001-08-31 2001-08-31 Verfahren zum Anfahren eines Dampferzeugers mit einem in einer annähernd horizontalen Heizgasrichtung durchströmbaren Heizgaskanal und Dampferzeuger
EP02797600A Expired - Lifetime EP1421317B1 (de) 2001-08-31 2002-08-20 Verfahren zum anfahren eines dampferzeugers mit einem in einer annähernd horizontalen heizgasrichtung durchströmbaren heizgaskanal und dampferzeuger

Family Applications After (1)

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EP02797600A Expired - Lifetime EP1421317B1 (de) 2001-08-31 2002-08-20 Verfahren zum anfahren eines dampferzeugers mit einem in einer annähernd horizontalen heizgasrichtung durchströmbaren heizgaskanal und dampferzeuger

Country Status (12)

Country Link
US (1) US7281499B2 (ja)
EP (2) EP1288567A1 (ja)
JP (2) JP2005523410A (ja)
KR (1) KR100742407B1 (ja)
CN (1) CN1289854C (ja)
CA (1) CA2458390C (ja)
CZ (1) CZ2004403A3 (ja)
ES (1) ES2395897T3 (ja)
PL (1) PL199757B1 (ja)
RU (1) RU2290563C2 (ja)
SK (1) SK1552004A3 (ja)
WO (1) WO2003021148A2 (ja)

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EP1512907A1 (de) * 2003-09-03 2005-03-09 Siemens Aktiengesellschaft Verfahren zum Anfahren eines Durchlaufdampferzeugers und Durchlaufdampferzeuger zur Durchführung des Verfahrens
WO2009100742A2 (de) * 2008-02-12 2009-08-20 Man Turbo Ag Kondensationsdampfturbine mit füllstandsfassungseinrichtung und verfahren zur regelung des füllstandes
DE102009012322A1 (de) * 2009-03-09 2010-09-16 Siemens Aktiengesellschaft Durchlaufverdampfer
DE102009012321A1 (de) * 2009-03-09 2010-09-16 Siemens Aktiengesellschaft Durchlaufverdampfer
DE102009024587A1 (de) * 2009-06-10 2010-12-16 Siemens Aktiengesellschaft Durchlaufverdampfer

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CN101310146B (zh) * 2005-07-19 2010-08-18 塞拉米克燃料电池有限公司 蒸汽发生器
JP4847213B2 (ja) * 2006-05-29 2011-12-28 バブコック日立株式会社 貫流型排熱回収ボイラ
CN101981373A (zh) * 2008-03-27 2011-02-23 阿尔斯托姆科技有限公司 带有均衡室的连续蒸汽发生器
EP2194320A1 (de) * 2008-06-12 2010-06-09 Siemens Aktiengesellschaft Verfahren zum Betreiben eines Durchlaufdampferzeugers sowie Zwangdurchlaufdampferzeuger
EP2180250A1 (de) * 2008-09-09 2010-04-28 Siemens Aktiengesellschaft Durchlaufdampferzeuger
DE102009012320A1 (de) * 2009-03-09 2010-09-16 Siemens Aktiengesellschaft Durchlaufverdampfer
NL2003596C2 (en) * 2009-10-06 2011-04-07 Nem Bv Cascading once through evaporator.
CN103090345A (zh) * 2011-10-28 2013-05-08 西安科弘厨房工程设备有限责任公司 太阳能/复合能源封闭循环相变供热系统
US9151488B2 (en) 2012-01-17 2015-10-06 Alstom Technology Ltd Start-up system for a once-through horizontal evaporator
EP2805108B1 (en) 2012-01-17 2020-11-25 General Electric Technology GmbH A method and apparatus for connecting sections of a once-through horizontal evaporator
US9739478B2 (en) 2013-02-05 2017-08-22 General Electric Company System and method for heat recovery steam generators
US9097418B2 (en) * 2013-02-05 2015-08-04 General Electric Company System and method for heat recovery steam generators
CN104896500B (zh) * 2014-11-18 2017-12-08 郭志男 一种固体燃料燃烧去烟降尘装置
EP3495730B1 (en) 2017-12-08 2024-01-24 General Electric Technology GmbH Once-through evaporator systems
EP3495729B1 (en) 2017-12-08 2020-11-25 General Electric Technology GmbH Once-through evaporator systems
EP3495732B1 (en) 2017-12-08 2024-02-14 General Electric Technology GmbH Once-through evaporator systems
EP3495731B1 (en) 2017-12-08 2022-02-16 General Electric Technology GmbH Once-through evaporator systems
EP3842723A1 (en) * 2019-12-23 2021-06-30 Hamilton Sundstrand Corporation Two-stage fractal heat exchanger

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Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1512907A1 (de) * 2003-09-03 2005-03-09 Siemens Aktiengesellschaft Verfahren zum Anfahren eines Durchlaufdampferzeugers und Durchlaufdampferzeuger zur Durchführung des Verfahrens
WO2005028957A1 (de) * 2003-09-03 2005-03-31 Siemens Aktiengesellschaft Verfahren zum anfahren eines durchlaufdampferzeugers und durchlaufdampferzeuger zur durchführung des verfahrens
JP2007504426A (ja) * 2003-09-03 2007-03-01 シーメンス　アクチエンゲゼルシヤフト 貫流ボイラとその始動方法
US7587133B2 (en) 2003-09-03 2009-09-08 Siemens Aktiengesellschaft Method for starting a continuous steam generator and continuous steam generator for carrying out said method
AU2004274586B2 (en) * 2003-09-03 2010-09-02 Siemens Aktiengesellschaft Method for starting a continuous steam generator and continuous steam generator for carrying out said method
CN1856680B (zh) * 2003-09-03 2011-01-26 西门子公司 起动直流式蒸汽发生器的方法和实施该方法的直流式蒸汽发生器
WO2009100742A2 (de) * 2008-02-12 2009-08-20 Man Turbo Ag Kondensationsdampfturbine mit füllstandsfassungseinrichtung und verfahren zur regelung des füllstandes
WO2009100742A3 (de) * 2008-02-12 2012-04-26 Man Diesel & Turbo Se Kondensationsdampfturbine mit füllstandsfassungseinrichtung und verfahren zur regelung des füllstandes
DE102009012322A1 (de) * 2009-03-09 2010-09-16 Siemens Aktiengesellschaft Durchlaufverdampfer
DE102009012321A1 (de) * 2009-03-09 2010-09-16 Siemens Aktiengesellschaft Durchlaufverdampfer
DE102009012322B4 (de) * 2009-03-09 2017-05-18 Siemens Aktiengesellschaft Durchlaufverdampfer
DE102009024587A1 (de) * 2009-06-10 2010-12-16 Siemens Aktiengesellschaft Durchlaufverdampfer

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US7281499B2 (en) 2007-10-16
CZ2004403A3 (cs) 2004-06-16
CN1543551A (zh) 2004-11-03
CA2458390A1 (en) 2003-03-13
KR20040029105A (ko) 2004-04-03
WO2003021148A3 (de) 2003-04-17
CN1289854C (zh) 2006-12-13
RU2290563C2 (ru) 2006-12-27
ES2395897T3 (es) 2013-02-15
WO2003021148A2 (de) 2003-03-13
US20060192023A1 (en) 2006-08-31
PL199757B1 (pl) 2008-10-31
CA2458390C (en) 2008-12-30
RU2004109587A (ru) 2005-05-20
EP1421317B1 (de) 2012-11-28
SK1552004A3 (en) 2004-11-03
JP2005523410A (ja) 2005-08-04
EP1421317A2 (de) 2004-05-26
WO2003021148A8 (de) 2004-03-04
JP4970316B2 (ja) 2012-07-04
KR100742407B1 (ko) 2007-07-24
JP2008180501A (ja) 2008-08-07
PL367786A1 (en) 2005-03-07

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