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EP1695007A1 - Generateur de vapeur en continu - Google Patents

Generateur de vapeur en continu

Info

Publication number
EP1695007A1
EP1695007A1 EP04790884A EP04790884A EP1695007A1 EP 1695007 A1 EP1695007 A1 EP 1695007A1 EP 04790884 A EP04790884 A EP 04790884A EP 04790884 A EP04790884 A EP 04790884A EP 1695007 A1 EP1695007 A1 EP 1695007A1
Authority
EP
European Patent Office
Prior art keywords
steam generator
side walls
region
tubes
generator 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.)
Withdrawn
Application number
EP04790884A
Other languages
German (de)
English (en)
Inventor
Rudolf Kral
Andre Schrief
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
Siemens Corp
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, Siemens Corp filed Critical Siemens AG
Priority to EP04790884A priority Critical patent/EP1695007A1/fr
Publication of EP1695007A1 publication Critical patent/EP1695007A1/fr
Withdrawn legal-status Critical Current

Links

Classifications

    • 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
    • F22B37/10—Water tubes; Accessories therefor
    • F22B37/14—Supply mains, e.g. rising mains, down-comers, in connection with water tubes
    • F22B37/146—Tube arrangements for ash hoppers and grates and for combustion chambers of the cyclone or similar type out of the flues
    • 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
    • F22B37/10—Water tubes; Accessories therefor
    • F22B37/14—Supply mains, e.g. rising mains, down-comers, in connection with water tubes

Definitions

  • the invention relates to a steam generator with a combustion chamber, which has funnel side walls in its bottom region, and with a peripheral wall formed from gas-tightly welded steam generator pipes.
  • a steam generator can be designed according to various design principles.
  • the heating of a number of steam generator tubes which together form the gas-tight peripheral wall of the combustion chamber, leads to complete evaporation of a flow medium in the steam generator tubes in one pass.
  • the flow medium - usually water - is fed to the superheater tubes connected downstream of the steam generator tubes and overheated there.
  • a high live steam pressure promotes high thermal efficiency and thus lower CO 2 emissions from a fossil-fired power plant.
  • the steam generator pipes are usually connected to one another by fins.
  • the surrounding wall is thus formed from a number of approximately parallel steam generator tubes which are connected to one another via fins and welded in a gas-tight manner.
  • the steam generator tubes of the steam generator can be arranged vertically or spirally and thus inclined.
  • funnel side walls of the combustion chamber are usually arranged, the shape of which allows the uncomplicated removal of ash that has arisen during the combustion process.
  • the combustion chamber wall is usually made of vertical steam generator tubes and fins.
  • the steam generator tubes In the lower section in the area of the funnel, the steam generator tubes usually also run in the manner of a vertical pipe in the same direction as in their upper section forming the combustion chamber wall.
  • the parallel tubes enter the funnels via inlet collectors and then form the parallel tubes of the combustion chamber.
  • the heat generated during the combustion of a fuel gas within the combustion chamber is introduced both directly through the walls of the steam generator tubes and via the fins into the flow medium flowing through the steam generator tubes.
  • the heating of each steam generator tube determines the weight of the water column in the respective tube. Since the flow of flow medium through a steam generator tube and thus the outlet temperature of the flow medium depends on the pressure of the water column in the corresponding tube, the outlet temperature through a steam generator tube is decisively influenced by the heating of the corresponding steam generator tube.
  • the invention is therefore based on the object of specifying a steam generator of the type mentioned above, in which it is ensured in every operating state that the differences in the temperatures of the flow medium at the outlet of individual steam generator pipes do not exceed a critical value.
  • This object is achieved according to the invention in that a number of steam generator tubes in the area of the funnel side walls have a different tube outer diameter and / or a different fin width than in the area of the peripheral wall of the combustion chamber.
  • the invention is based on the consideration that high material loads on the steam generator tubes can be avoided by ensuring that the temperature differences of the flow medium at the outlet of individual steam generator tubes do not exceed a critical value. Therefore, the heating of a steam generator tube should not deviate significantly from the heating of the other steam generator tubes at any point of the steam generator.
  • the length of the steam generator tubes has to be varied with increasing tapering of the funnel in the case of a conventional design. Some steam generator tubes are therefore shorter than others and are therefore exposed to weaker heating in the area of the funnel side walls. With the conventional design Different heating of the steam generator tubes and fins can therefore not be avoided due to the geometric conditions in their lower section arranged in the region of the funnel side walls.
  • the lengths of the individual steam generator tubes should not deviate too much from one another.
  • the steam generator tubes should be guided along the side faces of the funnel side walls. This is made possible by a suitable choice of pipe geometries.
  • the steam generator is advantageously designed as a once-through steam generator.
  • a number of steam generator tubes have a smaller tube diameter in the lower section forming the funnel side walls than in the upper section forming the combustion chamber wall.
  • the reduction in the pipe diameter in the funnel side walls allows the pipes to be piped with the same number of steam generator pipes as in the upper section forming the combustion chamber wall.
  • the tapering of the funnel side walls is not taken into account by reducing the number of steam generator tubes, but by reducing the tube diameter. This means that all steam generator tubes run over approximately the same length in the heated area and comparable heating of all steam generator tubes is ensured.
  • the heat input into the flow medium occurs not only through the tube walls, but also through the fins connecting the individual steam generator tubes together.
  • the width of the combustion chamber wall and the funnel side walls results from the number of steam generator tubes multiplied by the distance from the tube axis to the tube axis, the distance from the tube axis to the tube axis being equal to the tube diameter added to the width of a fin.
  • the width of the fins in the lower section of the steam generator tubes forming the funnel side walls can therefore advantageously also be changed and in particular reduced.
  • the pipe outer diameter in the lower section is advantageously reduced by 5 to 15 percent compared to the pipe diameter in the upper section.
  • the fin width is advantageously reduced in the lower section by 30 to 70 percent compared to the width in the upper section.
  • a number of steam generator tubes are advantageously arranged at least partially parallel to the direction of inclination of the funnel side walls.
  • Such an arrangement allows a particularly good adaptation of the length of each individual steam generator tube to the heating conditions and thus a particularly uniform heating.
  • the advantages achieved by the invention are, in particular, that when the steam generator is designed as a once-through steam generator, the occurrence of impermissibly large temperature differences of the flow medium in individual steam generator pipes can be effectively avoided with comparatively little structural effort. Because, in particular in the lower section of the steam generator tubes forming the funnel side walls, all steam generator tubes are exposed to a similarly strong heating, this can also occur when feeding of the steam generator with a low mass flow density do not lead to greatly differing flow rates and therefore also not to impermissibly high temperature differences of the flow medium at the outlet of the steam generator pipes.
  • Fig. Lb an alternative embodiment of the continuous steam generator
  • FIG. 2 shows a further alternative embodiment of the once-through steam generator according to FIG. 1.
  • FIG. 1 a schematically shows a steam generator 1 designed as a continuous steam generator, the vertical throttle cable of which is surrounded by a surrounding wall 4 and forms a combustion chamber which merges at the lower end into a floor formed by funnel side walls 6.
  • the bottom comprises a discharge opening 8 for ashes, not shown.
  • the vertical steam generator tubes 12 In the area of the throttle cable, there are a number of burners (not shown) in the vertical steam generator tubes 12 formed surrounding wall 4 of the combustion chamber attached.
  • the vertically extending steam generator tubes 12 are welded together via fins 14 and together with the fins 14 form the peripheral wall 4 of the combustion chamber in their upper section.
  • An inlet header 16 is arranged below the floor, from which the steam generator tubes 12 are supplied with flow medium.
  • the flow rate of the flow medium through the individual steam generator tubes 12 or the division of the flow rate among the individual steam generator tubes 12 is strongly determined by the respective weights of the water columns in the individual steam generator tubes 12. This has the consequence that heating, which is in the lower part of the combustion chamber, especially in the area of the funnel side walls 6, has a great influence on the flow through the steam generator tubes 12. If individual steam generator tubes 12 are heated comparatively strongly, the weight of their water column and thus also the resistance in the steam generator tube 12 in question decreases. This increases the flow rate in this steam generator tube 12 in comparison to other, less strongly heated steam generator tubes 12. If a steam generator tube 12 becomes comparatively weak heated, the flow rate is reduced accordingly.
  • a steam generator tube 12 is heated comparatively weakly in the area of the funnel side walls, for example because it only enters the heated side walls 6 at the upper edge of the funnel. th area occurs and thus has a comparatively short length within the heated area, it has a lower flow rate compared to other, comparatively strongly heated steam generator tubes 12 which have a greater length within the heated area.
  • all steam generator tubes 12 are exposed to similar heating. Under these conditions, a steam generator tube 12 with a comparatively low flow rate will absorb more heat than one with a comparatively high throughput, so that the different heating of the steam generator tubes 12 in the region of the funnel side walls 6 may result in considerable differences in the outlet temperature of the flow medium.
  • the steam generator tubes 12 of the steam generator 1 in FIG. 1 a have a smaller diameter in the lower section forming the funnel side walls 6 than in the upper section forming the peripheral wall 4 of the combustion chamber.
  • the fins 14 also have a smaller width in the lower section than in the upper section.
  • the width of the base which is determined by the number of parallel steam generator tubes 12 and by the tube diameter added to the width of a fin 14, can thus be reduced by a smaller tube diameter and a smaller width of the fins 14 instead of by reducing tion of the number of parallel steam generator tubes 12. This achieves the required tapering of the floor in the manner of at least partially guiding the steam generator pipes along the floor.
  • each steam generator tube 12 in the lower section is 5 to 15 percent compared to the tube diameter in the upper section and the width of the fins 14 in the lower section are reduced by 30 to 70 percent compared to the width in the upper section.
  • a normal tube diameter of 34 mm and a fin width of 16 mm this results in a tube diameter of approximately 32 mm and a fin width of approximately 6 mm in the lower section.
  • a particularly uniform heating of the steam generator tubes 12 in the region of the funnel side walls 6 can be achieved by the steam generator tubes 12 in their lower section, as shown in FIG.
  • This oblique arrangement allows the strength of the heating of each steam generator tube 12 to be largely adapted to its length within the heated area. In other words, the comparatively weak heating of a steam generator tube 12 is compensated for by a longer length in the heated area made possible by the oblique arrangement of the steam generator tubes 12.
  • FIG. 1 a shows an arrangement in which the steam generator tubes 12 are arranged obliquely in their lower section, in which the tube diameter is reduced, that is to say not parallel to the direction of inclination of the base.
  • this arrangement up to a certain height H determined by the geometry and dimensions of the bottom, fins 14 and steam generator tubes 12, an arrangement of the steam generator tubes 12 is provided parallel to the direction of inclination of the base. Above this height H, the described oblique arrangement is provided.
  • the steam generator tubes 12 can also be arranged as shown in FIG. 1b.
  • a pipe diameter that is reduced compared to the diameter in the upper section up to a certain height H there is also a pipe with steam generator pipes 12 arranged parallel to the direction of inclination of the floor and with a pipe diameter that is reduced compared to the diameter in the upper section.
  • an oblique arrangement of the steam generator tubes 12 is provided, but the angle of inclination of the steam generator tubes 12 relative to their original direction in the plane of the floor is selected such that the steam generator tubes 12 as well as the fins 14 in their oblique section have the same tube diameter or the same width as in the upper section.
  • the tube diameter and fin width are only reduced to height H.
  • the steam generator tubes 12 can be arranged as shown in FIG. 2.
  • the outermost steam generator tubes 12, that is to say those steam generator tubes 12 which are at the greatest distance from the central axis A are designed over the entire height of the funnel side walls 6 both with a non-reduced tube diameter and a non-reduced fin width, and are arranged obliquely.
  • the innermost steam generator tubes 12 with the smallest distance from the central axis A are designed with a reduced tube diameter and fin width over their entire length and arranged parallel to the central axis A and thus to the direction of inclination of the floor.
  • the respective steam generator pipes 12 lying between the outermost and the innermost steam generator pipe 12 form the transition and each have a first section with a reduced pipe diameter and a fin width, in which they are arranged parallel to the central axis, and a second section with a non-reduced pipe diameter and a non-reduced fin width , in which they are arranged obliquely and thus parallel to the outermost steam generator tube 12.

Landscapes

  • Engineering & Computer Science (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • Combustion & Propulsion (AREA)
  • Chemical & Material Sciences (AREA)
  • Control Of Steam Boilers And Waste-Gas Boilers (AREA)
  • Hydrogen, Water And Hydrids (AREA)
  • Combustion Of Fluid Fuel (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Devices For Medical Bathing And Washing (AREA)
  • Gas Burners (AREA)

Abstract

L'invention concerne un générateur de vapeur (1) présentant une chambre de combustion, pourvue de parois latérales en entonnoir (6) dans sa zone inférieure, et une paroi extérieure (4) constituée d'une pluralité de conduits (12) de générateur de vapeur traversés par un fluide. L'objectif de cette invention est d'obtenir des écarts de température les plus faibles possibles dans le fluide à la sortie des conduits (12) du générateur de vapeur. A cet effet, les conduits (12) du générateur de vapeur sont agencés en particulier dans la section inférieure constituant les parois latérales en entonnoir (6), de façon à être exposés à un chauffage le plus régulier possible. De plus, un certain nombre de conduits (12) du générateur de vapeur présentent un diamètre au niveau des parois latérales en entonnoir (6) qui est différent de celui au niveau de la paroi extérieure (4).
EP04790884A 2003-11-19 2004-10-26 Generateur de vapeur en continu Withdrawn EP1695007A1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
EP04790884A EP1695007A1 (fr) 2003-11-19 2004-10-26 Generateur de vapeur en continu

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
EP03026647A EP1533565A1 (fr) 2003-11-19 2003-11-19 Générateur de vapeur à passage unique
EP04790884A EP1695007A1 (fr) 2003-11-19 2004-10-26 Generateur de vapeur en continu
PCT/EP2004/012102 WO2005050089A1 (fr) 2003-11-19 2004-10-26 Generateur de vapeur en continu

Publications (1)

Publication Number Publication Date
EP1695007A1 true EP1695007A1 (fr) 2006-08-30

Family

ID=34429402

Family Applications (2)

Application Number Title Priority Date Filing Date
EP03026647A Withdrawn EP1533565A1 (fr) 2003-11-19 2003-11-19 Générateur de vapeur à passage unique
EP04790884A Withdrawn EP1695007A1 (fr) 2003-11-19 2004-10-26 Generateur de vapeur en continu

Family Applications Before (1)

Application Number Title Priority Date Filing Date
EP03026647A Withdrawn EP1533565A1 (fr) 2003-11-19 2003-11-19 Générateur de vapeur à passage unique

Country Status (14)

Country Link
US (1) US7516719B2 (fr)
EP (2) EP1533565A1 (fr)
JP (1) JP4463825B2 (fr)
KR (1) KR101177143B1 (fr)
CN (1) CN1902438B (fr)
AR (1) AR047127A1 (fr)
AU (1) AU2004291619B2 (fr)
BR (1) BRPI0416776A (fr)
CA (1) CA2546375A1 (fr)
MY (1) MY140359A (fr)
RU (1) RU2382938C2 (fr)
TW (1) TWI341914B (fr)
WO (1) WO2005050089A1 (fr)
ZA (1) ZA200603389B (fr)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5193007B2 (ja) * 2008-12-03 2013-05-08 三菱重工業株式会社 ボイラ構造
FI124376B (fi) 2010-01-15 2014-07-31 Foster Wheeler Energia Oy Höyrykattila
WO2012149080A2 (fr) 2011-04-27 2012-11-01 Bp Corporation North America Inc. Systèmes et procédés pour tube prolongateur sous-marin en mer
CN108072026A (zh) * 2016-11-17 2018-05-25 华北电力大学（保定） 一种新型超临界直流三压再热余热锅炉
KR102775502B1 (ko) * 2022-11-30 2025-03-05 한국기계연구원 벽체의 열관류율 측정방법 및 시스템

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US3662716A (en) * 1970-12-14 1972-05-16 Foster Wheeler Corp Furnance enclosure for natural circulation generator
US3872836A (en) * 1973-09-18 1975-03-25 Foster Wheeler Corp Coal-fired generator of medium to large capacity
PL204072A1 (pl) * 1978-01-17 1979-09-24 Katowice Metalurgiczny Huta Kociol odzysknicowy,zwlaszcza dla konwertora stalowniczego
US4465023A (en) * 1982-09-30 1984-08-14 Rockwell International Corporation Programmed combustion steam generator
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CN1016532B (zh) * 1985-09-23 1992-05-06 劳舍兄弟有限公司 燃烧矿物燃料的蒸汽发生器
IN165916B (fr) * 1985-12-04 1990-02-10 Sulzer Ag
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EP0349834B1 (fr) * 1988-07-04 1996-04-17 Siemens Aktiengesellschaft Chaudière à vapeur à passage unique
US4944250A (en) * 1989-03-30 1990-07-31 Foster Wheeler Energy Corporation Cyclone separator including a hopper formed by water-steam cooled walls
DE59009015D1 (de) * 1990-01-31 1995-06-08 Siemens Ag Dampferzeuger.
CA2082096A1 (fr) * 1991-11-21 1993-05-22 Michael Garkawe Separateur cyclonique refroidi a l'eau
US5226936A (en) * 1991-11-21 1993-07-13 Foster Wheeler Energy Corporation Water-cooled cyclone separator
DE4227457A1 (de) * 1992-08-19 1994-02-24 Siemens Ag Dampferzeuger
DE4431185A1 (de) * 1994-09-01 1996-03-07 Siemens Ag Durchlaufdampferzeuger
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DE19600004C2 (de) * 1996-01-02 1998-11-19 Siemens Ag Durchlaufdampferzeuger mit spiralförmig angeordneten Verdampferrohren
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WO2006032556A1 (fr) * 2004-09-23 2006-03-30 Siemens Aktiengesellschaft Generateur de vapeur en continu chauffe a l'aide d'un combustible fossile

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See references of WO2005050089A1 *

Also Published As

Publication number Publication date
MY140359A (en) 2009-12-31
CN1902438A (zh) 2007-01-24
AU2004291619A1 (en) 2005-06-02
TW200519324A (en) 2005-06-16
TWI341914B (en) 2011-05-11
JP2007534911A (ja) 2007-11-29
US20070144456A1 (en) 2007-06-28
CA2546375A1 (fr) 2005-06-02
BRPI0416776A (pt) 2007-02-27
EP1533565A1 (fr) 2005-05-25
KR101177143B1 (ko) 2012-08-24
ZA200603389B (en) 2007-09-26
KR20070026344A (ko) 2007-03-08
CN1902438B (zh) 2010-06-16
AU2004291619B2 (en) 2009-09-10
JP4463825B2 (ja) 2010-05-19
RU2382938C2 (ru) 2010-02-27
AR047127A1 (es) 2006-01-11
WO2005050089A1 (fr) 2005-06-02
US7516719B2 (en) 2009-04-14
RU2006121455A (ru) 2007-12-27

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