EP2324285A2 - Générateur de vapeur à récupération de chaleur - Google Patents

Générateur de vapeur à récupération de chaleur

Info

Publication number
EP2324285A2
EP2324285A2 EP09782665A EP09782665A EP2324285A2 EP 2324285 A2 EP2324285 A2 EP 2324285A2 EP 09782665 A EP09782665 A EP 09782665A EP 09782665 A EP09782665 A EP 09782665A EP 2324285 A2 EP2324285 A2 EP 2324285A2
Authority
EP
European Patent Office
Prior art keywords
tubes
steam generator
heat recovery
recovery steam
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.)
Granted
Application number
EP09782665A
Other languages
German (de)
English (en)
Other versions
EP2324285B1 (fr
Inventor
Jan BRÜCKNER
Joachim Franke
Holger Schmidt
Frank Thomas
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 PL09782665T priority Critical patent/PL2324285T3/pl
Priority to EP09782665.5A priority patent/EP2324285B1/fr
Publication of EP2324285A2 publication Critical patent/EP2324285A2/fr
Application granted granted Critical
Publication of EP2324285B1 publication Critical patent/EP2324285B1/fr
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22—STEAM GENERATION
    • F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B15/00—Water-tube boilers of horizontal type, i.e. the water-tube sets being arranged horizontally
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22—STEAM GENERATION
    • F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B21/00—Water-tube boilers of vertical or steeply-inclined type, i.e. the water-tube sets being arranged vertically or substantially vertically
    • 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 heat recovery steam generator with a number of evaporator tubes connected in parallel on the flow medium side, through which a number of superheater tubes are connected via a water separation system, wherein the water separation system comprises a number of water separation elements, each of which downstream of a number of evaporator tubes and / or a number of superheater tubes upstream, wherein each of the Wasserabscheideieri comprises a connected to the respective upstream evaporator tubes Einströmrohr mosaic, seen in its longitudinal direction merges into a Wasserableitrohr voting, wherein in the transition region a number of Abströmrohr structurien branches, which are connected to an inlet header of the respective downstream superheater tubes.
  • a heat recovery steam generator is a heat exchanger that recovers heat from a hot gas stream.
  • Heat recovery steam generators are used, for example, in gas and steam turbine power plants, in which the hot exhaust gases of one or more gas turbines are conducted into a heat recovery steam generator. The steam generated therein is then used to drive a steam turbine. This combination produces electrical energy much more efficiently than gas or steam turbine alone.
  • Heat recovery steam generators can be categorized by a variety of criteria: based on the flow direction of the gas flow, heat recovery steam generators can be classified, for example, into vertical and horizontal types. Furthermore, there are steam generator with a plurality of pressure stages with different thermal states of the water-steam mixture contained in each case. Steam generators can generally be designed as natural circulation, forced circulation or continuous steam generators. In a continuous steam generator, the heating 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 point of transition from a flow with residual moisture to pure steam flow, is variable and mode-dependent.
  • the evaporation end point is located, for example, in an end region of the evaporator tubes, so that the overheating of the vaporized flow medium already begins in the evaporator tubes.
  • such a continuous steam generator is normally operated with a minimum flow of flow medium in the evaporator tubes during low-load operation or during start-up.
  • the operationally provided minimum flow of flow medium in the evaporator tubes is thus when starting or in the
  • the superheater tubes connected downstream of the evaporator tubes of the continuous-flow steam generator are usually not suitable for a relatively large flow of unvaporized flow. are designed medium, continuous steam generators are usually designed so that even when starting and during low load operation excessive water ingress into the superheater tubes is safely avoided.
  • the evaporator tubes are usually connected to the superheater tubes connected downstream via a water separation system.
  • the water separator causes a separation of the emerging during the start or in low load operation of the evaporator tubes water-steam mixture in water and in steam.
  • the steam is downstream of the Wasserabscheidesystem
  • Superheater tubes supplied whereas the separated water can be supplied to the evaporator tubes again, for example via a circulation pump or discharged via a decompressor.
  • the Wasserabscheidesystem may include a plurality of Wasserabscheidemaschinen that are integrated directly into the tubes.
  • each of the evaporator tubes connected in parallel can be assigned a water separation element.
  • the Wasserabscheideetic can continue to be designed as a so-called T-piece Wasserabscheideimplantation.
  • each T-piece water separation element in each case comprises an inflow pipe piece connected to the upstream evaporator pipe, which, viewed in its longitudinal direction, merges into a water drainage pipe piece, wherein an outflow pipe piece connected to the downstream superheater pipe branches off in the transition region.
  • the T-piece Wasserabscheideelement for inertial separation of the flowing from the upstream evaporator tube in the Einströmrohr choir water-steam mixture is designed. Because of its comparatively higher inertia, namely, the water content of the flow medium flowing in the inflow pipe section at the transition point preferably continues in the axial extension of the inflow pipe section and thus enters the water diverter pipe section and from there usually further into a connected collecting tank. The vapor content of the inflow pipe section flowing water-steam mixture, however, can better follow a forced deflection due to its relatively lower inertia and thus flows through the Abströmrohr conducted to the downstream superheater pipe section.
  • a waste heat steam generator of this design designed for continuous operation is known, for example, from EP 1 701 090.
  • the transfer of flow medium to the superheater tubes is not only limited to steam, but now a water-steam mixture can be continued to the superheater tubes by the water separation elements are over-fed. As a result, the evaporation end point can be pushed into the superheater tubes as needed.
  • a particularly high operational flexibility can be achieved even in start-up or low load operation of the continuous steam generator.
  • the live steam temperature can be controlled in comparatively large limits by influencing the feedwater quantity.
  • the invention is therefore based on the object to provide a heat recovery steam generator of the type mentioned above, while maintaining a particularly high operational flexibility a comparatively low design and repair costs brings with it.
  • This object is achieved according to the invention by arranging a distributor element on the steam side between the respective water separation element and the inlet header of the subsequent heating surface.
  • the invention is based on the consideration that the decentralized separation of water, which takes place separately in each of the parallel-connected evaporator tubes in the construction described above, a comparatively large number of T-piece Wasserabscheideijnn can lead to design problems in large-scale application. Due to the space problems that may be associated with the need to accommodate such a large number of water separation elements, such a construction may also entail significant additional costs and restrictions on the heat recovery steam generator's geometric parameters due to the high design effort involved.
  • a reduction in the design cost of the heat recovery steam generator could be achieved by simplifying the design of the water separation system. For this purpose, the number of Wasserabscheideieri used can be reduced. However, in order to obtain the advantages of decentralized water separation, such as the possibility of feeding with water-steam mixture, the basic design in the form of T-piece water separation elements should be maintained. The combination of the two aforementioned concepts can be achieved by a collection of the flow medium from a plurality of evaporator tubes in each case a Wasserabscheideelement.
  • the geometric parameters of a number of outlet pipes are chosen such that a homogeneous flow distribution is ensured on the inlet header of the respectively downstream superheater pipes.
  • a homogeneous entry is already achieved in the inlet header, which continues accordingly in the downstream superheater tubes.
  • the outlet tubes can, for example, have the same diameter and be guided at equal intervals parallel to one another in the inlet header.
  • the distributor element is designed as a star distributor, d. H. it comprises a baffle plate, an inlet tube arranged perpendicular to the baffle plate, and a number of outlet tubes arranged in a star shape around the baffle plate in the plane thereof.
  • the inflowing water impinges on the baffle plate and is distributed in a symmetrical manner perpendicular to the inflow direction and directed into the outlet tubes.
  • the baffle plate in a particularly advantageous embodiment is circular and the exit tubes arranged concentrically to the center of the baffle plate at equal intervals to the respective adjacent outlet tubes. In this way, a particularly homogeneous distribution is ensured on the different outlet pipes.
  • the water separation system as a T-piece separator there is the possibility of overfeeding, d. H. Forwarding of water-steam mixture in the superheater pipes. Any irregular flow created in the evaporation process will thus continue in the T-piece water separator elements and the downstream superheater tubes.
  • Such turbulent flows can occur in particular in the form of so-called slugs, which are caused by the different flow velocities of vaporized and unevaporated flow medium in the tubes.
  • the result is a wave-like movement that causes a pulsating mass flow, which can lead to mechanical and thermal loads on the Wasserabscheideimplantation and also the downstream superheater tubes.
  • measures should be taken against the further propagation of the turbulence from the evaporator tubes into the T-piece water separator elements and the downstream superheater tubes. This should be done before the water-steam mixture in the T-piece Wasserabscheideetic.
  • a flow turbulence damper is provided in the inflow pipe sections of a number of water separation elements in an advantageous embodiment.
  • the turbulences in the pipe system are caused, among other things, by two different phases of the flow medium flowing parallel to one another through the pipe system. At the interface of the two phases, vortices occur at widely differing flow velocities, resulting in a rapid local displacement of the interface between the two phases in the form of a wave-like motion.
  • the flow turbulence dampers in an advantageous embodiment each comprise a number of bulkheads, each of which closes a part of the pipe cross section. The slugs break at the bulkheads, some of the water is held back and distributed to the area following the slug, mainly dominated by steam.
  • the waves are smoothed and pulsation-free operation is achieved by smoothing the wave movements.
  • the direction of oscillation of the wave movements entering the flow turbulence absorbers should be known and predictable.
  • possible swirling movements of the inflowing water-vapor mixture should be suppressed, as these could hinder the operation of the flow turbulence damper.
  • the flow turbulence dampers on the tube inner wall advantageously comprise a number of guide profiles aligned in the main flow direction of the flow medium. Through the guide profiles a possible swirling motion of the water vapor mixture is stopped and the water vapor mixture is introduced in such a geometric position in the flow turbulence damper that they can fulfill their task appropriately.
  • the flow turbulence dampers can be introduced directly during the production of the pipes.
  • the flow turbulence dampers are advantageously made of a material having the same material as the tube or similar composition. This also prevents too high a mechanical stress on the pipes, which would arise in the case of different materials for pipes and flow turbulence dampers and / or the guide profiles as a result of the different thermal expansion properties.
  • FIG. 3 shows the evaporator of a heat recovery steam generator from FIGS. 1 and 2 in the direction of the flue gas path
  • FIG. 1 shows the schematic representation of a heat recovery steam generator 1 with horizontal flue gas path.
  • the flow medium M is fed into the pipe system by an upstream feed pump not shown in detail. Initially, it flows into a number of evaporator inlet collectors 2, which provide for the distribution of the flow medium M to four evaporator heating surfaces with evaporator tubes 4, in which then an evaporation of the flow medium takes place.
  • further evaporator heating surfaces can also be connected upstream or the heating surfaces can be arranged in different geometrical configurations in the heating gas duct.
  • a number of evaporator tubes 4 opens into a via a first evaporator outlet header 6 and a second outlet header 8 in a common transition pipe section 10, which is the T-piece Wasserabscheideelement 12 downstream.
  • the T-piece Wasserabscheideelement comprises a Einströmrohr laminate 14, which is seen in its longitudinal direction merges into a Wasserableitrohr laminate 16, wherein in the transition region, a Abströmrohr lenders 18 branches off.
  • the Wasserableitrohr lenders 16 opens into a Abschlämmtechnisch 20, which is arranged downstream of a collecting tank 22 arranged outside the flue gas duct.
  • An outlet valve 24 is connected to the collection container 22, via which the separated water can either be discarded or re-supplied to the evaporation circulation.
  • flow medium M enters through the inflow pipe piece 14. Due to its inertia, the proportionate water W flows into the water drainage pipe piece 16 which follows in the longitudinal direction.
  • the steam D follows the diversion into the outflow pipe piece 18 due to its lower mass.
  • the overflow pipe piece 18 is superposed in two superheater heating surfaces downstream of a superheater inlet collector 28.
  • the superheater tubes 26 eventually open in a superheater outlet header 30.
  • the vapor D is collected there and fed through the steam outlet 32 for its further use;
  • a device not shown in detail in FIG. 1, for example a steam turbine, is provided.
  • the outlet valve 24 can be closed and thus an overfeed of the T-piece Wasserabscheideieri 12 be brought about.
  • unevaporated water W enters the superheater tubes 26 so that they can still be used for further evaporation, ie. h.,
  • the evaporation end point can be moved into the superheater tubes, which allows a relatively higher flexibility in the operation of the heat recovery steam generator 1.
  • T-piece water separation elements 12 In order to allow a particularly simple construction of the heat recovery steam generator 1, a comparatively smaller number of T-piece water separation elements 12 should be used. In order to compensate for the resulting inhomogeneities with regard to the distribution to the superheater tubes and thus to enable such an embodiment in the first place, distribution elements 34 are interposed in the manner of star distributors to the T-piece water separation elements. These provide for a pre-distribution of the flow medium M in the event of over-feeding of the T-piece Wasserabscheideieri 12 to the superheater inlet collector ⁇ O QO.
  • the mode of operation of the distributor elements 34 in the form of star distributors can be seen in the plan view of the heat recovery steam generator 1 according to FIG. Also recognizable are the first and second evaporator outlet collectors 6, 8, furthermore the T-piece water separation elements 12, the drainage line 20 and the collecting container 22.
  • the flow medium M impinges on a circular baffle plate and bounces from there into star-shaped, concentrically-symmetrically arranged outlet tubes 36 Arrangement of the output shown in the embodiment eight output tubes 36 is assigned to each output tube 36 about the same amount of flow medium M. These open at equal intervals in the superheater inlet header 28, so that there is already a pre-distribution of the flow medium M to the entire width of the superheater inlet header 28.
  • FIG. 3 shows the heat recovery steam generator 1 from the direction of the flue gas inlet. Visible are the second evaporator outlet header 8, further the T-piece Wasserabscheide institute 12, the Abschlämmtechnisch 20, the sump 22 with the outlet valve 24, further the distributor elements 34 with the discharge pipes 36, which open into the superheater inlet header 28.
  • FIG. 3 clearly shows the advantages of the pre-distribution:
  • the flow medium M is already distributed homogeneously over the entire width of each superheater inlet collector 28 via the respective eight outlet tubes.
  • the flow medium M in the superheater inlet collectors 28 could not be evenly distributed, as these due to the width of the superheater heating not for such a homogeneous distribution of, for example, a single supply are suitable.
  • FIG. 4 shows an alternative embodiment, namely a heat recovery steam generator 1 with a vertical flue gas direction in a side view.
  • the components and their function are essentially identical to the steam generator shown in FIGS. 1 to 3, only the evaporator tubes 4 and the superheater tubes 26 are arranged horizontally.
  • the evaporator tubes 4 are repeatedly guided in turns through the Schugaskanal. Due to the smaller number of T-piece Wasserabscheideijnn 12 each of these elements is relatively larger dimensions.
  • flow turbulence dampers 38 are provided in an area upstream of the T-piece water separation elements 12. These can be mounted, for example, in an outlet region of the evaporator tube 4, in the exemplary embodiment shown they are introduced into the inflow pipe section 14 of the tee water separation element 12, which is shown separately in FIG.
  • the flow turbulence dampers 38 may include a number of bulkheads or guide profiles that may be fabricated from the same material as the inflow tubing 14. With regard to their geometric parameters, they can furthermore be adapted to the local flow conditions provided during operation.

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Drying Of Solid Materials (AREA)
  • Engine Equipment That Uses Special Cycles (AREA)
  • Separating Particles In Gases By Inertia (AREA)

Abstract

L'invention concerne un générateur de vapeur à récupération de chaleur (1) comportant une pluralité de tuyaux d'évaporateur (4) montés parallèlement sur le côté du fluide circulant, une pluralité de tuyaux de surchauffeur (26) étant montés en aval des tuyaux d'évaporateur au moyen d'un système de séparation d'eau. Le système de séparation d'eau comporte une pluralité d'éléments de séparation d'eau (12), chaque élément de séparation d'eau étant respectivement monté en aval d'une pluralité de tuyaux d'évaporateur (4) et/ou en amont d'une pluralité de tuyaux de surchauffeur (26). Chaque élément de séparation d'eau (12) comporte une tubulure d'entrée (14) respectivement reliée aux tuyaux d'évaporateur (4) respectivement montés en amont, se prolongeant sous forme de tubulure d'évacuation d'eau (16) dans sa direction longitudinale, une pluralité de tubulures d'écoulement (18) se détachant dans la zone de transition, celles-ci étant reliées à un collecteur d'entrée (28) des tuyaux de surchauffeur (26) respectivement montés en aval. L'invention vise à mettre en oeuvre un tel générateur de vapeur à récupération de chaleur caractérisé par une grande flexibilité de fonctionnement et des moyens de construction et de réparation réduits. A cet effet, un élément distributeur (34) est disposé côté vapeur entre l'élément de séparation d'eau respectif (12) et le collecteur d'entrée (28).
EP09782665.5A 2008-09-09 2009-09-07 Générateur de vapeur à récupération de chaleur Active EP2324285B1 (fr)

Priority Applications (2)

Application Number Priority Date Filing Date Title
PL09782665T PL2324285T3 (pl) 2008-09-09 2009-09-07 Kocioł odzyskowy
EP09782665.5A EP2324285B1 (fr) 2008-09-09 2009-09-07 Générateur de vapeur à récupération de chaleur

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
EP08015864A EP2204611A1 (fr) 2008-09-09 2008-09-09 Générateur de vapeur à récupération de chaleur
PCT/EP2009/061521 WO2010029033A2 (fr) 2008-09-09 2009-09-07 Générateur de vapeur à récupération de chaleur
EP09782665.5A EP2324285B1 (fr) 2008-09-09 2009-09-07 Générateur de vapeur à récupération de chaleur

Publications (2)

Publication Number Publication Date
EP2324285A2 true EP2324285A2 (fr) 2011-05-25
EP2324285B1 EP2324285B1 (fr) 2016-11-02

Family

ID=42005552

Family Applications (2)

Application Number Title Priority Date Filing Date
EP08015864A Withdrawn EP2204611A1 (fr) 2008-09-09 2008-09-09 Générateur de vapeur à récupération de chaleur
EP09782665.5A Active EP2324285B1 (fr) 2008-09-09 2009-09-07 Générateur de vapeur à récupération de chaleur

Family Applications Before (1)

Application Number Title Priority Date Filing Date
EP08015864A Withdrawn EP2204611A1 (fr) 2008-09-09 2008-09-09 Générateur de vapeur à récupération de chaleur

Country Status (7)

Country Link
US (1) US8701602B2 (fr)
EP (2) EP2204611A1 (fr)
CN (1) CN102171513B (fr)
ES (1) ES2614155T3 (fr)
PL (1) PL2324285T3 (fr)
RU (1) RU2011113827A (fr)
WO (1) WO2010029033A2 (fr)

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1629677B1 (fr) 2003-06-05 2014-12-31 Meshnetworks, Inc. Optimisation de l'acheminement dans des reseaux de radiocommunication ad hoc
US9273865B2 (en) * 2010-03-31 2016-03-01 Alstom Technology Ltd Once-through vertical evaporators for wide range of operating temperatures
DE102010040216A1 (de) * 2010-09-03 2012-03-08 Siemens Aktiengesellschaft Solarthermischer Druchlaufdampferzeuger mit einem Dampfabscheider und nachgeschaltetem Sternverteiler für Solarturm-Kraftwerke mit direkter Verdampfung
DE102011004278A1 (de) * 2011-02-17 2012-08-23 Siemens Aktiengesellschaft Solarthermisches Kraftwerk
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
EP2839213B1 (fr) * 2012-01-17 2018-09-05 General Electric Technology GmbH Configuration de tubes et de déflecteurs dans un évaporateur horizontal à passage unique
CN107110489B (zh) * 2014-11-04 2019-07-16 尚科宁家运营有限公司 蒸汽发生器
CN106838852B (zh) * 2017-03-10 2023-02-28 高峰 一种膜式蒸汽发生器
CN117185391B (zh) * 2023-09-08 2024-05-10 山东迈沃净水科技有限公司 一种高效多效蒸馏水机及其模块化设计方法

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19717158C2 (de) * 1997-04-23 1999-11-11 Siemens Ag Durchlaufdampferzeuger und Verfahren zum Anfahren eines Durchlaufdampferzeugers
DE10228335B3 (de) * 2002-06-25 2004-02-12 Siemens Ag Abhitzedampferzeuger mit Hilfsdampferzeugung
EP1701091A1 (fr) * 2005-02-16 2006-09-13 Siemens Aktiengesellschaft Générateur de vapeur à passage unique
EP1701090A1 (fr) 2005-02-16 2006-09-13 Siemens Aktiengesellschaft Générateur de vapeur à construction horizontale
EP1710498A1 (fr) * 2005-04-05 2006-10-11 Siemens Aktiengesellschaft Générateur de vapeur
NL2003596C2 (en) * 2009-10-06 2011-04-07 Nem Bv Cascading once through evaporator.

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See references of WO2010029033A2 *

Also Published As

Publication number Publication date
RU2011113827A (ru) 2012-10-20
PL2324285T3 (pl) 2017-04-28
US8701602B2 (en) 2014-04-22
WO2010029033A3 (fr) 2010-06-10
EP2324285B1 (fr) 2016-11-02
WO2010029033A2 (fr) 2010-03-18
EP2204611A1 (fr) 2010-07-07
US20110162594A1 (en) 2011-07-07
CN102171513A (zh) 2011-08-31
CN102171513B (zh) 2013-11-20
ES2614155T3 (es) 2017-05-29

Similar Documents

Publication Publication Date Title
EP2324285B1 (fr) Générateur de vapeur à récupération de chaleur
EP0944801B1 (fr) Chaudiere a vapeur
EP1848925B1 (fr) Générateur de vapeur de type horizontal
EP1710498A1 (fr) Générateur de vapeur
DE102009012322B4 (de) Durchlaufverdampfer
EP1390606B2 (fr) Dispositif de refroidissement du fluide de refroidissement d'une turbine a gaz et ensemble turbine a gaz et turbine a vapeur comportant un tel dispositif
EP1701091A1 (fr) Générateur de vapeur à passage unique
EP2321578B1 (fr) Générateur de vapeur en continu
WO2015039831A2 (fr) Centrale à cycle combiné gaz-vapeur munie d'un générateur de vapeur à récupération de chaleur
EP1512905A1 (fr) Générateur de vapeur à passage unique et méthode pour faire fonctionner ledit générateur de vapeur à passage unique
EP3014177B1 (fr) Générateur de vapeur en continu en construction de type chaudière à deux passages
EP1537358B1 (fr) Generateur de vapeur construit horizontalement
DE102010038883B4 (de) Zwangdurchlaufdampferzeuger
EP1554522B1 (fr) Procede pour exploiter un generateur de vapeur de conception horizontale
DE102009015260B4 (de) Vorrichtung zur Phasenseparation eines Mehrphasen-Fluidstroms, Dampfturbinenanlage mit einer derartigen Vorrichtung und zugehöriges Betriebsverfahren
DE69004929T2 (de) Dampferzeugungssystem.
DE102010038885B4 (de) Zwangdurchlaufdampferzeuger
EP2564117B1 (fr) Générateur de vapeur
EP3048366A1 (fr) Générateur de vapeur à récupération de chaleur
DE102010040216A1 (de) Solarthermischer Druchlaufdampferzeuger mit einem Dampfabscheider und nachgeschaltetem Sternverteiler für Solarturm-Kraftwerke mit direkter Verdampfung
DE102011004262A1 (de) Verdampfer eines solarthermischen Dampferzeugers mit T-Abscheider
DE102010040214A1 (de) Berohrung einer Verdampferheizfläche für Durchlaufdampferzeuger in Solarturm-Kraftwerken mit direkter Verdampfung und Naturumlauf-Charakteristik

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

17P Request for examination filed

Effective date: 20101112

AK Designated contracting states

Kind code of ref document: A2

Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO SE SI SK SM TR

DAX Request for extension of the european patent (deleted)
RAP1 Party data changed (applicant data changed or rights of an application transferred)

Owner name: SIEMENS AKTIENGESELLSCHAFT

GRAP Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOSNIGR1

INTG Intention to grant announced

Effective date: 20160506

GRAS Grant fee paid

Free format text: ORIGINAL CODE: EPIDOSNIGR3

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO SE SI SK SM TR

REG Reference to a national code

Ref country code: GB

Ref legal event code: FG4D

Free format text: NOT ENGLISH

REG Reference to a national code

Ref country code: AT

Ref legal event code: REF

Ref document number: 842219

Country of ref document: AT

Kind code of ref document: T

Effective date: 20161115

Ref country code: CH

Ref legal event code: EP

REG Reference to a national code

Ref country code: IE

Ref legal event code: FG4D

Free format text: LANGUAGE OF EP DOCUMENT: GERMAN

REG Reference to a national code

Ref country code: DE

Ref legal event code: R096

Ref document number: 502009013320

Country of ref document: DE

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LV

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20161102

REG Reference to a national code

Ref country code: NL

Ref legal event code: MP

Effective date: 20161102

REG Reference to a national code

Ref country code: LT

Ref legal event code: MG4D

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SE

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20161102

Ref country code: NO

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20170202

Ref country code: NL

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20161102

Ref country code: GR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20170203

Ref country code: LT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20161102

REG Reference to a national code

Ref country code: ES

Ref legal event code: FG2A

Ref document number: 2614155

Country of ref document: ES

Kind code of ref document: T3

Effective date: 20170529

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: HR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20161102

Ref country code: FI

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20161102

Ref country code: PT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20170302

Ref country code: IS

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20170302

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: DK

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20161102

Ref country code: CZ

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20161102

Ref country code: EE

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20161102

Ref country code: SK

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20161102

Ref country code: RO

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20161102

REG Reference to a national code

Ref country code: DE

Ref legal event code: R097

Ref document number: 502009013320

Country of ref document: DE

RAP2 Party data changed (patent owner data changed or rights of a patent transferred)

Owner name: SIEMENS AKTIENGESELLSCHAFT

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: BG

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20170202

Ref country code: SM

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20161102

PLBE No opposition filed within time limit

Free format text: ORIGINAL CODE: 0009261

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT

REG Reference to a national code

Ref country code: CH

Ref legal event code: NV

Representative=s name: SIEMENS SCHWEIZ AG, CH

Ref country code: CH

Ref legal event code: PCOW

Free format text: NEW ADDRESS: WERNER-VON-SIEMENS-STRASSE 1, 80333 MUENCHEN (DE)

26N No opposition filed

Effective date: 20170803

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SI

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20161102

REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: MC

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20161102

REG Reference to a national code

Ref country code: IE

Ref legal event code: MM4A

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LU

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20170907

REG Reference to a national code

Ref country code: FR

Ref legal event code: ST

Effective date: 20180531

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: IE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20170907

Ref country code: LI

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20170930

Ref country code: CH

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20170930

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: FR

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20171002

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: MT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20161102

REG Reference to a national code

Ref country code: AT

Ref legal event code: MM01

Ref document number: 842219

Country of ref document: AT

Kind code of ref document: T

Effective date: 20170907

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: AT

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20170907

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: HU

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT; INVALID AB INITIO

Effective date: 20090907

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: CY

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20161102

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: MK

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20161102

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: TR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20161102

REG Reference to a national code

Ref country code: DE

Ref legal event code: R081

Ref document number: 502009013320

Country of ref document: DE

Owner name: SIEMENS ENERGY GLOBAL GMBH & CO. KG, DE

Free format text: FORMER OWNER: SIEMENS AKTIENGESELLSCHAFT, 80333 MUENCHEN, DE

REG Reference to a national code

Ref country code: GB

Ref legal event code: 732E

Free format text: REGISTERED BETWEEN 20220811 AND 20220817

REG Reference to a national code

Ref country code: BE

Ref legal event code: PD

Owner name: SIEMENS ENERGY GLOBAL GMBH & CO. KG; DE

Free format text: DETAILS ASSIGNMENT: CHANGE OF OWNER(S), ASSIGNMENT; FORMER OWNER NAME: SIEMENS AKTIENGESELLSCHAFT

Effective date: 20221214

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: IT

Payment date: 20230920

Year of fee payment: 15

Ref country code: GB

Payment date: 20230926

Year of fee payment: 15

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: DE

Payment date: 20230928

Year of fee payment: 15

Ref country code: BE

Payment date: 20230926

Year of fee payment: 15

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: ES

Payment date: 20231018

Year of fee payment: 15

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: PL

Payment date: 20230831

Year of fee payment: 15

REG Reference to a national code

Ref country code: ES

Ref legal event code: PC2A

Owner name: SIEMENS ENERGY GLOBAL GMBH & CO. KG

Effective date: 20240409