EP1188021B1 - Fossilbeheizter dampferzeuger mit einer entstickungseinrichtung für heizgas - Google Patents

Fossilbeheizter dampferzeuger mit einer entstickungseinrichtung für heizgas Download PDF

Info

Publication number
EP1188021B1
EP1188021B1 EP00949097.0A EP00949097A EP1188021B1 EP 1188021 B1 EP1188021 B1 EP 1188021B1 EP 00949097 A EP00949097 A EP 00949097A EP 1188021 B1 EP1188021 B1 EP 1188021B1
Authority
EP
European Patent Office
Prior art keywords
steam generator
combustion chamber
gas
tubes
evaporator tubes
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.)
Expired - Lifetime
Application number
EP00949097.0A
Other languages
German (de)
English (en)
French (fr)
Other versions
EP1188021A1 (de
Inventor
Josef Pulec
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
Publication of EP1188021A1 publication Critical patent/EP1188021A1/de
Application granted granted Critical
Publication of EP1188021B1 publication Critical patent/EP1188021B1/de
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • 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
    • F22B21/34—Water-tube boilers of vertical or steeply-inclined type, i.e. the water-tube sets being arranged vertically or substantially vertically built-up from water tubes grouped in panel form surrounding the combustion chamber, i.e. radiation boilers
    • 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
    • F22B37/008—Adaptations for flue gas purification in steam generators
    • 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
    • F22B21/34—Water-tube boilers of vertical or steeply-inclined type, i.e. the water-tube sets being arranged vertically or substantially vertically built-up from water tubes grouped in panel form surrounding the combustion chamber, i.e. radiation boilers
    • F22B21/346—Horizontal radiation boilers

Definitions

  • the invention relates to a steam generator with a denitrification device for heating gas and with a combustion chamber for fossil fuel, the hot gas side via a horizontal gas train and a vertical gas train denitrification is followed by heating gas.
  • the fuel gas generated during the combustion of a fossil fuel is used for the evaporation of a flow medium in the steam generator.
  • the steam generator has evaporator tubes for the evaporation of the flow medium, the heating of which leads with heating gas to an evaporation of the flow medium guided therein.
  • the steam provided by the steam generator can in turn be provided, for example, for a connected external process or else for the drive of a steam turbine. If the steam drives a steam turbine, usually a generator or a working machine is operated via the turbine shaft of the steam turbine.
  • the power generated by the generator may be provided for feeding into a composite and / or island grid.
  • the steam generator can be designed as a continuous steam generator.
  • a continuous steam generator is from the article " Evaporator Concepts for Benson Steam Generators "by J. Franke, W. Köhler and E. Wittchow, published in VGB Kraftwerkstechnik 73 (1993), No. 4, pp. 352-360 , known.
  • the heating of steam generator tubes provided as evaporator tubes leads to an evaporation of the flow medium in the steam generator tubes in a single pass.
  • Steam generators are usually designed with a combustion chamber in a vertical construction. This means that the combustion chamber is designed for a flow through the heating medium or heating gas in approximately vertical direction.
  • the combustion chamber can be followed by a horizontal gas train, wherein the transition from the combustion chamber in the horizontal gas train, a deflection of the Schugasstroms takes place in an approximately horizontal flow direction.
  • Such combustors generally require due to the temperature-induced changes in length of the combustion chamber, a scaffold on which the combustion chamber is suspended. This requires a considerable technical effort in the production and installation of the steam generator, which is the greater, the greater the height of the steam generator.
  • a particular problem is the design of the enclosure wall of the gas flue or combustion chamber of the steam generator with respect to the pipe wall or material temperatures occurring there.
  • the temperature of the peripheral wall of the combustion chamber is essentially determined by the height of the saturation temperature of the water , This is achieved, for example, by the use of evaporator tubes which have a surface structure on their inside.
  • evaporator tubes which have a surface structure on their inside.
  • finned tubes i. Tubes with a ribbed inner surface have a particularly good heat transfer from the tube inner wall to the flow medium.
  • the process of selective catalytic reduction can be used.
  • nitrogen oxides (NO x ) are reduced to nitrogen (N 2 ) and water (H 2 O) by means of a reducing agent, such as ammonia, and a catalyst.
  • a reducing agent such as ammonia
  • a denitrification device for heating gas with a catalytic converter is usually arranged after the heating gas duct designed as convection draft, where usually the heating gas has a temperature of about 320 to 400 ° C.
  • the catalyst of the denitration device for heating gas serves to initiate and / or maintain a reaction between the reducing agent introduced in the heating gas and the nitrogen oxides of the heating gas.
  • the reducing agent required for the SCR process is usually injected with air as a carrier stream into the hot gas flowing through the gas train.
  • the nitrogen oxide emission of the steam generator is usually dependent on the type of fossil fuel burned. In order to comply with the statutory limits, therefore, usually the directedüsende amount of reducing agent is varied depending on the fossil fuel used.
  • a denitrification device for heating gas arranged on the output side after the convection pass requires considerable design and production effort for the respective steam generator. Because the denitrification must be placed there in the steam generator, where it can exert a particularly high cleaning effect on the fuel gas at all operating conditions of the steam generator. This is usually the case where the heating gas has a temperature in the range of about 320 to 400 ° C. In addition, the production cost of a steam generator increases when this addition to conventional components additionally has a denitrification.
  • the invention is therefore an object of the invention to provide a fossil-fired steam generator of the type mentioned above, which requires a particularly low design and manufacturing costs, and in the particularly reliable cleaning of the fuel gas of the fossil fuel is guaranteed before they leave the steam generator on the output side.
  • combustion chamber of the steam generator comprises a number of arranged in the height of the horizontal flue burners, the vertical gas flue for an approximately vertical flow of the heating gas from bottom to top and denitrification of heating gas for an approximately vertical flow of the fuel gas top down is designed.
  • the invention is based on the consideration that a producible with particularly low manufacturing and assembly costs steam generator should have a executable with simple means suspension structure.
  • a scaffold for the suspension of the combustion chamber to be created with comparatively little technical effort can be accompanied by a particularly low overall height of the steam generator.
  • a particularly low height of the steam generator can be achieved by the combustion chamber is designed in a horizontal design.
  • the burners are arranged in the height of the horizontal gas flue in the combustion chamber wall.
  • the combustion chamber is flowed through during operation of the steam generator in approximately horizontal direction of the heating gas.
  • the denitrification device for heating gas should be arranged on the output side after the vertical gas train. On the output side after the vertical gas train, namely, the heating gas to temperatures at which a cleaning of the fuel gas is particularly effective with little technical effort. It should be noted that for a particularly low height of the steam generator Entstickungs adopted for heating gas should be designed for an approximately vertical flow of the fuel gas from top to bottom. This results in an injection of the liquid required in the SCR process with ammonia components along the main flow direction of the fuel gas possible, whereby the vertical extent of the denitrification precipitates particularly low.
  • the purified fuel gas leaving the denitrification device for heating gas can be used to heat air in an air preheater.
  • the air preheater should be arranged in a particularly space-saving manner directly below the Entstickungs learned for heating gas.
  • the preheated air is to be supplied to the burners of the steam generator for the combustion of the fossil fuel. If warm air is supplied to the burners as opposed to cold air during combustion of the fossil fuel, the overall efficiency of the steam generator increases.
  • the denitrification device for heating gas advantageously comprises a DeNO x catalyst.
  • a reduction in nitrogen oxide of the hot gas leaving the steam generator can be carried out in a particularly simple manner, for example with the method of Selective Catalytic Reduction.
  • the enclosing walls of the combustion chamber are advantageously formed of gas-tight welded together, vertically arranged evaporator tubes, each of which a number can be acted upon in parallel with flow medium.
  • a peripheral wall of the combustion chamber is the end wall and two surrounding walls of the combustion chamber are the side walls, wherein the side walls are each subdivided into a first group and a second group of Verdamperrohre, the end wall and the first group of Verdamperrohre be acted upon in parallel with flow medium and the be acted upon in parallel flow medium, the second group of evaporator tubes upstream of the flow medium.
  • This ensures a particularly favorable cooling of the end wall.
  • each of the evaporator tubes which can be acted upon in parallel with flow medium, is preceded by a common inlet collector system on the flow medium side and a common outlet collector system connected downstream.
  • a designed in this embodiment steam generator allows reliable pressure equalization between the parallel connected evaporator tubes and thus a particularly favorable distribution of the flow medium in the flow through the evaporator tubes.
  • the tube inner diameter of a number of evaporator tubes of the combustion chamber is selected depending on the respective position of the evaporator tubes in the combustion chamber.
  • the evaporator tubes in the combustion chamber can be adapted to a gas-side predefinable heating profile. With the effect thereby effected on the flow through the evaporator tubes, temperature differences at the outlet of the evaporator tubes of the combustion chamber are kept particularly low.
  • flow medium advantageously has a number of evaporator tubes on its inner side in each case a Herzoges thread forming ribs.
  • a pitch angle ⁇ between a plane perpendicular to the tube axis and the flanks of the arranged on the tube inside ribs is advantageously less than 60 °, preferably less than 55 °.
  • a so-called smooth tube, evaporator tube can namely no longer be maintained by a certain vapor content of the required for a particularly good heat transfer wetting the tube wall. If there is no wetting, there may be a partially dry pipe wall. The transition to such a dry pipe wall leads to a kind of heat transfer crisis with deteriorated heat transfer behavior, so that in general increase the pipe wall temperatures at this point particularly strong. In an internally ribbed pipe, however, this crisis of heat transfer now occurs only at a steam mass content> 0.9, ie shortly before the end of the evaporation, compared to a smooth pipe. This is due to the spin experienced by the flow through the spiral ribs.
  • a number of the evaporator tubes of the combustion chamber advantageously has means for reducing the flow of the flow medium. It proves to be particularly advantageous if the means are designed as throttle devices. Throttling devices, for example, internals in be the evaporator tubes, which reduce the pipe inside diameter at a point inside the respective evaporator tube.
  • the line system can also be connected upstream of an inlet collector system of evaporator tubes which can be acted upon in parallel with flow medium.
  • throttle valves can be provided.
  • the side walls of the horizontal gas flue and / or the vertical gas flue are advantageously formed of gas-tight welded together, vertically arranged steam generator tubes, each of which a number can be acted upon in parallel with flow medium.
  • Adjacent evaporator or steam generator tubes are advantageously welded together via metal bands, so-called fins, gas-tight.
  • the fin width affects the heat input into the steam generator tubes. Therefore, the fin width is preferably adapted depending on the position of the respective evaporator or steam generator tubes in the steam generator to a gas-side prescribable heating and / or temperature profile.
  • a heating and / or temperature profile a typical heating and / or temperature profile determined from empirical values or else a rough estimate, such as a step-shaped heating and / or temperature profile, be given.
  • heat input into all evaporator or steam generator tubes is achievable even with very different heating of different evaporator or steam generator tubes, so that temperature differences at the outlet of the evaporator or steam generator tubes are kept particularly low. In this way, premature material fatigue is reliably prevented. As a result, the steam generator on a particularly long life.
  • a number of superheater heating surfaces are advantageously arranged, whose tubes are arranged approximately transversely to the main flow direction of the heating gas and connected in parallel for a flow through the flow medium.
  • superheater heating surfaces are heated predominantly convective and downstream of the evaporator tubes of the combustion chamber downstream of the combustion chamber.
  • the vertical gas train has a number of convection heating surfaces, which are formed from tubes arranged approximately transversely to the main flow direction of the heating gas.
  • the tubes of a convection heating surface are connected in parallel for a flow through the flow medium. These convection heating surfaces are heated predominantly convection.
  • the vertical gas train advantageously has an economizer.
  • the burners are arranged on the end wall of the combustion chamber, that is on that surrounding wall of the combustion chamber, which is opposite to the outflow opening to the horizontal gas flue.
  • a trained steam generator can be adapted in a particularly simple manner to the Ausbrandin of the fuel.
  • the maximum burn-out length for the respective steam generator results in the steam output of the steam generator at full load, the so-called full-load operation of the steam generator.
  • the burn-out time t A is the time that, for example, a pulverized coal particle needs to completely burn out at a certain average heating gas temperature.
  • the defined by the distance from the end wall to the inlet region of the horizontal flue length L of the combustion chamber is advantageously at least equal to the burn-out length of the fuel Full load operation of the steam generator.
  • This length L of the combustion chamber will generally be greater than the height of the combustion chamber, measured from the funnel upper edge to the combustion chamber ceiling.
  • the advantages achieved by the invention are in particular that has a particularly small footprint through the horizontal combustion chamber and designed for an approximately vertical flow direction of the fuel gas from bottom to top vertical gas train of the steam generator.
  • This particularly compact design of the steam generator allows for integration of the steam generator in a steam turbine plant particularly short connecting pipes from the steam generator to the steam turbine.
  • the steam generator 2 according to FIG. 1 is associated with a power plant not shown, which also includes a steam turbine plant.
  • the steam generated in the steam generator 2 is used to drive the steam turbine, which in turn drives a generator for generating electricity.
  • the electricity generated by the generator is provided for feeding into a network or an island network.
  • a diversion of a subset of the steam for feeding into an external process connected to the steam turbine plant may be provided, which may also be a heating process.
  • the fossil-heated steam generator 2 is advantageously designed as a continuous steam generator. It comprises a horizontally constructed combustion chamber 4, the heating gas side via a horizontal gas train 6 a vertical gas train 8 is connected downstream.
  • the lower region of the combustion chamber 4 is formed by a funnel 5 with an upper edge corresponding to the auxiliary line with the end points X and Y.
  • ash from the fossil fuel B can be discharged into a deashing device 7 arranged below it.
  • the enclosure walls 9 of the combustion chamber 4 are formed from gas-tight welded together, vertically arranged evaporator tubes 10.
  • a surrounding wall 9, the end wall 9A and two enclosing walls 9 are the side walls 9B of the combustion chamber 4 of the steam generator 2.
  • the evaporator tubes 10 of the side walls 9B of the combustion chamber 4 are divided into a first group 11A and a second group 11B.
  • the evaporator tubes 10 of the end wall 9A and the first group 11A of the evaporator tubes 10 are acted upon in parallel with flow medium S.
  • the second group 11B of the evaporator tubes 10 can be acted upon in parallel with flow medium S.
  • the evaporator tubes 10 of the end wall 9A and the first group 11A strömungsmediumsseitg the evaporator tubes 10 of the second group 11B upstream.
  • the side walls 12 of the horizontal gas flue 6 and / or the side walls 14 of the vertical gas flue 8 are formed from gas-tight welded together, vertically arranged steam generator tubes 16 and 17, respectively. Of the steam generator tubes 16, 17 while a number in parallel with flow medium S can be acted upon.
  • the second group 11B of the side walls 9B of the evaporator tubes 10 is preceded by a common inlet header system 18B for flow medium S downstream of an outlet header system 20B and downstream of an outlet header system 20B.
  • the entry collector systems 18A and 18B each comprise a number of parallel entry collectors.
  • a piping 19A For supplying flow medium S into the inlet header system 18A of the end face 9A of the combustion chamber 4 and the first group 11A of the evaporator tubes 10 of the side walls 9B of the combustion chamber 4, a piping 19A is provided.
  • the conduit system 19A includes a plurality of parallel-connected conduits, each connected to one of the inlet header of the inlet header system 18A.
  • the outlet header system 20A is connected on the output side to a line system 19B, which is suitable for feeding flow medium S into the Intake collector of the inlet header system 18B of the second group 11B of the evaporator tubes 10 of the side walls 9B of the combustion chamber 4 is provided.
  • the steam generator tubes 16, which can be acted upon in parallel with flow medium S, of the side walls 12 of the horizontal gas flue 6 are preceded by a common inlet header system 21 and are followed by a common outlet header system 22.
  • a line system 25 is provided for supplying flow medium S into the inlet header system 21 of the steam generator tubes 16.
  • the line system 25 also includes a plurality of parallel lines, which are each connected to one of the inlet header of the inlet header system 21.
  • the line system 25 is connected to the outlet header system 20B of the second group 11B of the evaporator tubes 10 of the side walls 9A of the combustion chamber 4. The heated flow medium S leaving the combustion chamber 4 is thus guided into the side walls 12 of the horizontal gas flue 6.
  • This embodiment of the continuous-flow steam generator 2 with inlet collector systems 13A, 18B and 21 and outlet collector systems 20A, 20B and 22 provides a particularly reliable pressure equalization between the parallel-connected evaporator tubes 10 of the combustion chamber 4 and the parallel steam generator tubes 16 of the horizontal gas flue 6 in FIG the way possible that each parallel-connected evaporator or steam generator tubes 10 and 16 have the same total pressure loss. This means that in a more heated evaporator tube 10 or steam generator tube 16 compared to a less heated evaporator tube 10 or steam generator tube 16, the throughput must increase.
  • the evaporator tubes 10 have - as in FIG. 2 shown on its inside ribs 40, which form a kind multi-threaded and have a rib height R.
  • the pitch angle ⁇ between a perpendicular to the tube axis Level 42 and the flanks 44 of the arranged on the tube inside ribs 40 is less than 55 °.
  • the tube inner diameter D of the evaporator tubes 10 of the combustion chamber 4 is selected depending on the respective position of the evaporator tubes 10 in the combustion chamber 4. In this way, the steam generator 2 is adapted to the different degrees of heating of the evaporator tubes 10.
  • This design of the evaporator tubes 10 of the combustion chamber 4 ensures particularly reliable that temperature differences at the outlet of the evaporator tubes 10 are kept particularly low.
  • Adjacent evaporator or steam generator tubes 10, 16, 17 are gas-tight welded together in a manner not shown by fins.
  • the respective fin width namely the heating of the evaporator or steam generator tubes 10, 16, 17 can be influenced. Therefore, the respective fin width is adapted to a gas side specifiable heating profile, which depends on the position of the respective evaporator or steam generator tubes 10, 16, 17 in the steam generator.
  • the heating profile can be a typical heating profile determined from empirical values or else a rough estimate.
  • throttling devices As means for reducing the flow rate of the flow medium S, a part of the evaporator tubes 10 are equipped with throttling devices which are not closer in the drawing are shown.
  • the throttling devices are embodied as pinhole diaphragms reducing the inner diameter of the pipe D and, during operation of the steam generator 2, reduce the throughput of the flow medium S in underheated evaporator tubes 10, whereby the flow rate of the flow medium S is adapted to the heating.
  • the internal ribbing is designed such that a sufficient cooling of Evaporator pipe walls is ensured.
  • all the evaporator tubes 10 have approximately the same exit temperatures of the flow medium S with the above-mentioned measures.
  • the horizontal gas flue 6 has a number of Matterhitzersammlung inhabit designed as Schottsammlung lake 23, which are arranged in a hanging construction approximately perpendicular to the main flow direction 24 of the fuel gas G and whose tubes are connected in parallel for a flow of the flow medium S.
  • the superheater heating surfaces 23 are predominantly heated convectively and are downstream of the evaporator tubes 10 of the combustion chamber 4 on the flow medium side.
  • the vertical gas flow 8 which can be flowed through from bottom to top by heating gas G, has a number of convection heating surfaces 26 which can be heated predominantly convectively and which are formed from tubes arranged approximately perpendicular to the main flow direction 24 of the heating gas G. These tubes are each connected in parallel for flow through the flow medium S and integrated into the path of the flow medium S, which is not shown in detail in the drawing.
  • an economizer 28 is disposed in the vertical gas train 8 above the convection heating surfaces 26.
  • the economizer 28 is connected on the output side via a line system 19 to the evaporator tubes 10 associated with the inlet collector system 18.
  • one or more lines (not shown in detail in the drawing) of the line system 54 may have throttle bodies for reducing the flow rate of the flow medium S.
  • the vertical gas train 8 On the output side, the vertical gas train 8, which can be traversed from bottom to top in approximately vertical main flow direction 24 with heating gas G, is followed by a short connecting duct 50.
  • the connecting channel 50 connects the vertical gas train 8 with a housing 52.
  • a denitrification 54 for heating gas G is arranged on the input side.
  • the denitrification device 54 for heating gas G is connected via a feed 56 to an air preheater 60.
  • the air preheater 60 in turn is connected via a flue gas channel 62 to an electronic filter 62.
  • the denitrification device 54 for heating gas G is operated by the selective catalytic reduction process, the so-called SCR process.
  • SCR process nitrogen oxides (NO x ) are reduced to nitrogen (N 2 ) and water (H 2 O) by means of a catalyst and a reducing agent, for example ammonia.
  • the denitrification device 54 for heating gas G comprises a catalyst designed as DeNO x catalyst 64.
  • the DeNO x catalyst is arranged in the flow region of the heating gas G.
  • the denitrification device 54 for heating gas G has a metering system 66.
  • the dosing 66 comprises a reservoir 68 for ammonia water and a compressed air system 69.
  • the dosing system 66 is disposed above the DeNO x catalyst 64 in the denitrification 54.
  • the steam generator 2 is designed with a horizontal combustion chamber 4 with a particularly low height and thus can be built with very low production and assembly costs.
  • the combustion chamber 4 of the steam generator 2 to a number of burners 70 for fossil fuel B, which are arranged on the end wall 11 of the combustion chamber 4 in the height of the horizontal gas flue 6.
  • the length L of the combustion chamber 4 is selected such that it exceeds the burn-out length of the fuel B at full load operation of the steam generator 2.
  • the length L is the distance from the end wall 9A of the combustion chamber 4 to the inlet region 72 of the horizontal gas flue 6.
  • the burn-out length of the fuel B is defined as the fuel gas velocity in the horizontal direction at a certain mean heating gas temperature multiplied by the burn-out time t A of the fossil fuel B.
  • the maximum burn-out length for the respective steam generator 2 results during the full-load operation of the steam generator 2.
  • the burn-out time t A of the fuel B is the time required, for example, by a pulverized coal grain of medium size to completely burn out at a specific average heating gas temperature.
  • the burners 70 are supplied with fossil fuel B and air.
  • the air is preheated in the air preheater with the residual heat of the fuel gas G, and then, which is not shown in detail in the drawing, compressed and fed to the burners 70.
  • the flames F of the burner 70 are aligned horizontally.
  • a flow of the heating gas G produced during combustion is generated in an approximately horizontal main flow direction 24.
  • the heating gas G passes through the horizontal gas flue 6 in the vertical gas fl ow from bottom to top with hot gas G. 8. On the output side after the vertical gas train 8, the heating gas G passes through the connecting channel 50 in the denitration 54 for fuel G.
  • About the denitrification 54 for fuel gas G is a function of the fuel type of the steam generator 2 operating fuel B, a certain amount of ammonia water as reducing agent M injected by means of compressed air into the fuel gas G. This is necessary since the degree of separation of the nitrogen oxides (NO x ) depends on the type of fuel of the fossil fuel B operating the steam generator 2. In this way, a particularly reliable denitrification of the hot gas G is ensured under all operating conditions of the steam generator 2.
  • the purified fuel gas G1 leaves the denitrification 54 for fuel gas G via a feed 56, which opens into the air preheater 58.
  • the heating gas G leaves the air preheater 58 via the flue gas channel 60 and passes through the electronic filter 62 into the environment.
  • Flow medium S entering the economizer 28 passes via the line system 19A into the inlet header system 18A, which is assigned to the end wall 9A and the evaporator tubes 10 of the first group 11A of the side walls 9B of the combustion chamber 4 of the steam generator 2.
  • the resulting in the vertically arranged, gas-tight welded together evaporator tubes 10 of the combustion chamber 4 of the steam generator 2 steam or a water-steam mixture is collected in the outlet collector system 20A for flow medium S.
  • the steam or the water-vapor mixture passes via the line system 19B in the inlet header system 18B, which is associated with the second group 11B of the evaporator tubes 10 of the side walls 9B of the combustion chamber 4.
  • the resulting in the vertically arranged, gas-tight welded together evaporator tubes 10 of the combustion chamber 4 of the steam generator 2 steam or a water-steam mixture is in the outlet collector system 20B collected for flow medium S. From there, the steam or the water-vapor mixture passes through the line system 25 in the steam generator tubes 16 of the side walls 12 of the horizontal gas train associated with inlet collector system 21.
  • the resulting in the evaporator tubes 16 steam or water-steam mixture passes the outlet collector system 22 into the walls of the vertical gas flue 8 and from there in turn into the superheater heating surfaces 23 of the horizontal flue 6. In the superheater heating 23 further overheating of the steam, which is then a use, for example, the drive of a steam turbine is supplied.
  • the steam generator 2 is ensured by the choice of the length L of the combustion chamber 4 in response to the BMCR value W of the steam generator 2 that the heat of combustion of the fossil fuel B is utilized particularly reliable.
  • the steam generator 2 by its horizontal combustion chamber 4 and the denitrification device 54 immediately downstream of the vertical gas train 8 has a particularly small footprint. In this case, a particularly reliable denitration of the heating gas G is ensured in a particularly simple manner in all operating states of the steam generator 2.

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Control Of Steam Boilers And Waste-Gas Boilers (AREA)
  • Chimneys And Flues (AREA)
  • Engine Equipment That Uses Special Cycles (AREA)
EP00949097.0A 1999-06-24 2000-06-13 Fossilbeheizter dampferzeuger mit einer entstickungseinrichtung für heizgas Expired - Lifetime EP1188021B1 (de)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
DE19929088A DE19929088C1 (de) 1999-06-24 1999-06-24 Fossilbeheizter Dampferzeuger mit einer Entstickungseinrichtung für Heizgas
DE19929088 1999-06-24
PCT/DE2000/001941 WO2001001040A1 (de) 1999-06-24 2000-06-13 Fossilbeheizter dampferzeuger mit einer entstickungseinrichtung für heizgas

Publications (2)

Publication Number Publication Date
EP1188021A1 EP1188021A1 (de) 2002-03-20
EP1188021B1 true EP1188021B1 (de) 2013-05-29

Family

ID=7912477

Family Applications (1)

Application Number Title Priority Date Filing Date
EP00949097.0A Expired - Lifetime EP1188021B1 (de) 1999-06-24 2000-06-13 Fossilbeheizter dampferzeuger mit einer entstickungseinrichtung für heizgas

Country Status (9)

Country Link
US (1) US6536380B1 (ko)
EP (1) EP1188021B1 (ko)
JP (1) JP3806350B2 (ko)
KR (1) KR100472111B1 (ko)
CN (1) CN1126904C (ko)
CA (1) CA2377681C (ko)
DE (1) DE19929088C1 (ko)
RU (1) RU2214555C1 (ko)
WO (1) WO2001001040A1 (ko)

Families Citing this family (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA2501086A1 (en) * 2002-10-04 2004-04-22 Nooter/Eriksen, Inc. Once-through evaporator for a steam generator
US6718915B1 (en) * 2002-12-16 2004-04-13 The Babcock & Wilcox Company Horizontal spiral tube boiler convection pass enclosure design
US7878157B2 (en) 2004-09-23 2011-02-01 Siemens Aktiengesellschaft Fossil-fuel heated continuous steam generator
EP1701090A1 (de) * 2005-02-16 2006-09-13 Siemens Aktiengesellschaft Dampferzeuger in liegender Bauweise
EP1793163A1 (de) * 2005-12-05 2007-06-06 Siemens Aktiengesellschaft Dampferzeugerrohr, zugehöriges Herstellungsverfahren sowie Durchlaufdampferzeuger
EP1793164A1 (de) * 2005-12-05 2007-06-06 Siemens Aktiengesellschaft Dampferzeugerrohr, zugehöriges Herstellungsverfahren sowie Durchlaufdampferzeuger
US7387090B2 (en) * 2005-12-23 2008-06-17 Russoniello Fabio M Method for control of steam quality on multipath steam generator
US7533632B2 (en) * 2006-05-18 2009-05-19 Babcock & Wilcox Canada, Ltd. Natural circulation industrial boiler for steam assisted gravity drainage (SAGD) process
WO2008004281A1 (fr) * 2006-07-04 2008-01-10 Miura Co., Ltd. Appareil de combustion
EP2180251A1 (de) * 2008-09-09 2010-04-28 Siemens Aktiengesellschaft Durchlaufdampferzeuger
EP2180250A1 (de) * 2008-09-09 2010-04-28 Siemens Aktiengesellschaft Durchlaufdampferzeuger
EP2182278A1 (de) * 2008-09-09 2010-05-05 Siemens Aktiengesellschaft Durchlaufdampferzeuger
ES2400594B1 (es) * 2009-05-18 2014-04-15 Inerco, Ingenieria , Tecnologia Y Consultoria, S.A. Caldera equipada con sistema integrado de abatimiento catalitico de oxidos de nitrogeno
GB201010038D0 (en) 2010-06-16 2010-07-21 Doosan Power Systems Ltd Steam generator
US10215399B2 (en) * 2013-03-14 2019-02-26 The Babcock & Wilcox Company Small supercritical once-thru steam generator
US9939149B2 (en) * 2013-07-30 2018-04-10 Pcl Industrial Services, Inc. Radiant to convection transition for fired equipment
CN109416172B (zh) * 2016-07-07 2021-06-08 西门子股份公司 具有涡旋式安装体的蒸汽发生器管
CN111539160B (zh) * 2020-04-14 2022-10-04 龙净科杰环保技术（上海）有限公司 燃煤机组尿素脱硝系统喷氨管道流速的计算方法

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3527261A (en) 1968-11-12 1970-09-08 Babcock & Wilcox Co Tube guide apparatus
US3556059A (en) * 1969-01-28 1971-01-19 Foster Wheeler Corp Two-pass furnace circuit arrangement for once-through vapor generator
US3872836A (en) * 1973-09-18 1975-03-25 Foster Wheeler Corp Coal-fired generator of medium to large capacity
DE2557427A1 (de) * 1975-12-19 1977-06-30 Kraftwerk Union Ag Schaltung einer feuerraumnase bei einem durchlaufkessel mit gasdicht verschweissten waenden in zweizugbauweise
JPS61130705A (ja) * 1984-11-30 1986-06-18 三菱重工業株式会社 ボイラ装置
DK154731C (da) * 1985-05-21 1989-05-08 Burmeister & Wains Energi Dampkedel med katalytisk roeggasbehandling samt fremgangsmaade ved drift af kedelen
DK0745807T3 (da) * 1995-05-31 2000-02-21 Asea Brown Boveri Dampgenerator
JPH0926105A (ja) * 1995-07-12 1997-01-28 Mitsubishi Heavy Ind Ltd ボイラ

Also Published As

Publication number Publication date
RU2214555C1 (ru) 2003-10-20
CA2377681C (en) 2008-04-01
DE19929088C1 (de) 2000-08-24
WO2001001040A1 (de) 2001-01-04
CA2377681A1 (en) 2001-01-04
EP1188021A1 (de) 2002-03-20
KR20020015994A (ko) 2002-03-02
CN1364226A (zh) 2002-08-14
JP2003503670A (ja) 2003-01-28
CN1126904C (zh) 2003-11-05
JP3806350B2 (ja) 2006-08-09
KR100472111B1 (ko) 2005-03-08
US6536380B1 (en) 2003-03-25

Similar Documents

Publication Publication Date Title
EP1188021B1 (de) Fossilbeheizter dampferzeuger mit einer entstickungseinrichtung für heizgas
EP0944801B1 (de) Dampferzeuger
EP0617778B1 (de) Fossil befeuerter durchlaufdampferzeuger
EP2324285B1 (de) Abhitzedampferzeuger
EP1086339B1 (de) Fossilbeheizter dampferzeuger
EP1166014B1 (de) Fossilbeheizter durchlaufdampferzeuger
EP1166015B1 (de) Fossilbeheizter durchlaufdampferzeuger
EP1141625B1 (de) Fossilbeheizter durchlaufdampferzeuger
EP1144910B1 (de) Fossilbeheizter dampferzeuger
EP1144911B1 (de) Fossilbeheizter dampferzeuger
WO2006032556A1 (de) Fossil beheizter durchlaufdampferzeuger
DE102010038883B4 (de) Zwangdurchlaufdampferzeuger
EP1554522B1 (de) Verfahren zum betreiben eines dampferzeugers in liegender bauweise
WO2005050089A1 (de) Durchlaufdampferzeuger
EP2601442A2 (de) Zwangdurchlaufdampferzeuger
DE381001C (de) Wasserrohrkessel
DE19851809A1 (de) Fossilbeheizter Dampferzeuger
DE19825800A1 (de) Fossilbeheizter Dampferzeuger
WO1994005950A1 (de) Dampferzeuger

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: 20011122

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AT BE CH CY DE DK ES FI FR GB GR IE IT LI LU MC NL PT SE

17Q First examination report despatched

Effective date: 20071029

REG Reference to a national code

Ref country code: DE

Ref legal event code: R079

Ref document number: 50016316

Country of ref document: DE

Free format text: PREVIOUS MAIN CLASS: F22B0021340000

Ipc: F22B0037000000

GRAP Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOSNIGR1

RIC1 Information provided on ipc code assigned before grant

Ipc: F22B 21/34 20060101ALI20121205BHEP

Ipc: F22B 37/00 20060101AFI20121205BHEP

RAP1 Party data changed (applicant data changed or rights of an application transferred)

Owner name: SIEMENS AKTIENGESELLSCHAFT

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 CH CY DE DK ES FI FR GB GR IE IT LI LU MC NL PT SE

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: CH

Ref legal event code: EP

REG Reference to a national code

Ref country code: AT

Ref legal event code: REF

Ref document number: 614652

Country of ref document: AT

Kind code of ref document: T

Effective date: 20130615

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: 50016316

Country of ref document: DE

Effective date: 20130725

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

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: 20130930

Ref country code: ES

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: 20130909

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: 20130529

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: 20130830

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: 20130529

REG Reference to a national code

Ref country code: NL

Ref legal event code: VDEP

Effective date: 20130529

BERE Be: lapsed

Owner name: SIEMENS A.G.

Effective date: 20130630

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: 20130529

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: 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: 20130529

Ref country code: IT

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: 20130529

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: 20130529

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: BE

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

Effective date: 20130630

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

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

Ref country code: CH

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

Effective date: 20130630

Ref country code: LI

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

Effective date: 20130630

Ref country code: IE

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

Effective date: 20130613

26N No opposition filed

Effective date: 20140303

REG Reference to a national code

Ref country code: FR

Ref legal event code: ST

Effective date: 20140416

REG Reference to a national code

Ref country code: DE

Ref legal event code: R097

Ref document number: 50016316

Country of ref document: DE

Effective date: 20140303

REG Reference to a national code

Ref country code: AT

Ref legal event code: MM01

Ref document number: 614652

Country of ref document: AT

Kind code of ref document: T

Effective date: 20130613

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: 20130729

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: 20130613

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 FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20130529

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: 20130613

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

Ref country code: GB

Payment date: 20160610

Year of fee payment: 17

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

Ref country code: DE

Payment date: 20160819

Year of fee payment: 17

REG Reference to a national code

Ref country code: DE

Ref legal event code: R119

Ref document number: 50016316

Country of ref document: DE

GBPC Gb: european patent ceased through non-payment of renewal fee

Effective date: 20170613

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

Ref country code: DE

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

Effective date: 20180103

Ref country code: GB

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

Effective date: 20170613