EP0195443A1 - Apparatus for separating moisture from and for reheating steam by heat exchange - Google Patents

Apparatus for separating moisture from and for reheating steam by heat exchange Download PDF

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Publication number
EP0195443A1
EP0195443A1 EP86103774A EP86103774A EP0195443A1 EP 0195443 A1 EP0195443 A1 EP 0195443A1 EP 86103774 A EP86103774 A EP 86103774A EP 86103774 A EP86103774 A EP 86103774A EP 0195443 A1 EP0195443 A1 EP 0195443A1
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EP
European Patent Office
Prior art keywords
steam
superheaters
shell
bundles
channels
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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.)
Ceased
Application number
EP86103774A
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German (de)
French (fr)
Inventor
Pascal Alias
Olivier Lacoste
Jacques Marjollet
Pierre Pouderoux
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Stein Industrie SA
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Stein Industrie SA
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Application filed by Stein Industrie SA filed Critical Stein Industrie SA
Publication of EP0195443A1 publication Critical patent/EP0195443A1/en
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22STEAM GENERATION
    • F22BMETHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B37/00Component parts or details of steam boilers
    • F22B37/02Component parts or details of steam boilers applicable to more than one kind or type of steam boiler
    • F22B37/26Steam-separating arrangements
    • F22B37/266Separator reheaters

Definitions

  • Patent EP-B-005225 of the Applicant relates to a device of this kind, in which the channels allow the humid vapor to rise on either side of the superheaters in the vicinity of the internal surface of the shell, then to descend between two groups of superheaters to lead to the inlet of the separators in the vicinity of the plane of symmetry.
  • Such a device requires that the superheaters be divided into two groups separated by a central space allowing the descent of the wet steam. This requires giving the device a larger diameter, to the detriment of its size and its cost.
  • the object of the present invention is to provide a device for drying and overheating vapor of reduced bulk and weight than the known device, while ensuring cooling of the internal wall of the shell as effectively.
  • the device according to the invention is characterized in that its channels for the circulation of wet steam are separated from the chamber intake by a partition arranged on one side of the superheaters only, so that the humid vapor rises in the vicinity of the internal surface of the shell only on one side of the superheaters, then descends from the on the other side towards admission to separating bodies.
  • the figure shows the device in section through a plane perpendicular to its axis, in line with the pipes for the admission of wet steam and the discharge of superheated steam.
  • a distribution member 3 such as that which was the subject of patent FR-B-2442069 of the Applicant, distributes the wet steam in two lateral flows represented by the arrows 4 and 5 , and an axial flow represented by the arrow 6. From the left lateral flow, a first part penetrates into the blocks of separating members 7, formed for example by stacks of parallel corrugated sheets, on which the water droplets are deposited, then run off, before being evacuated by gutters and evacuation pipes, not shown.
  • the right lateral flow of wet steam enters the separator member blocks 8.
  • the axial flow represented by arrow 6, enters the separator member blocks 9 and 10.
  • a fraction of the wet steam does not pass directly into the separating members, but rises along the shell 1, as shown by the arrow 14, in a channel 15 disposed between the shell 1 and an internal envelope 16 delimiting the flow of steam to be superheated.
  • This fraction keeps the shell 1 at a relatively low temperature. It then descends on the other side of the internal envelope 16 by a channel 17 along the right side of the shell 1, as shown by the arrow 18. It is then directed by a partition 19 in a channel 20 towards the admission to separating bodies 21, where it gets rid of its residual moisture.
  • This dried fraction then joins the main dried vapor fraction to go to the overheating exchangers.

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Drying Of Solid Materials (AREA)

Abstract

Dispositif de séchage et de surchauffe de vapeur d'axe horizontal, comportant à l'intérieur d'une virole cylindrique a) dans sa partie inférieure, une chambre d'admission de la vapeur humide, b) au-dessus, des organes séparateurs (7, 8, 9, 10, 21) d'élimination de l'eau, c) dans sa partie supérieure, des faisceaux de tubes surchauffeurs 11 et d) de part et d'autre de ces faisceaux, des canaux 15, 17 de circulation de la vapeur humide. Ces canaux sont séparés de la chambre d'admission par une cloison (19) disposée de l'un des côtés des surchauffeurs seulement, de façon que la vapeur humide ne s'élève au voisinage de la surface de la virole que de l'un des côtés des surchauffeurs, puis redescende de l'autre côté vers l'admission à des organes séparateurs (21).Steam drying and superheating device with a horizontal axis, comprising inside a cylindrical shell a) in its lower part, a chamber for the admission of wet steam, b) above, separating members ( 7, 8, 9, 10, 21) for removing water, c) in its upper part, bundles of superheater tubes 11 and d) on either side of these bundles, channels 15, 17 of circulation of wet steam. These channels are separated from the intake chamber by a partition (19) arranged on one side of the superheaters only, so that the humid vapor rises in the vicinity of the surface of the shell only from one on the sides of the superheaters, then descends on the other side towards the admission to separating members (21).

Description

La présente invention concerne un dispositif de séchage puis de surchauffe par échange de chaleur, d'axe horizontal, notamment pour l'alimentation en vapeur d'eau d'une turbine de détente, comportant à l'intérieur d'une virole cylindrique, disposés parallèlement à son axe et symétriquement par rapport à son plan de symétrie longitudinal,

  • a) dans sa partie inférieure, une chambre d'admission de la vapeur humide à sécher et surchauffer,
  • b) au-dessus de la chambre d'admission, des organes séparateurs éliminant l'eau de la vapeur humide à surchauffer,
  • c) dans sa partie supérieure, des faisceaux de tubes constituant les surchauffeurs, dans lesquels de la vapeur surchauffée sous pression est refroidie, puis condensée en échange de chaleur avec la vapeur séchée à surchauffer,

et d) de part et d'autre des faisceaux de tubes surchauffeurs, des canaux de circulation de la vapeur humide permettant à une partie de celle-ci de s'élever au voisinage de la surface interne de la virole, avant de revenir vers les organes séparateurs,The present invention relates to a device for drying and then overheating by heat exchange, with a horizontal axis, in particular for supplying water vapor to an expansion turbine, comprising inside a cylindrical shell, arranged parallel to its axis and symmetrically with respect to its longitudinal plane of symmetry,
  • a) in its lower part, a humid steam inlet chamber to be dried and overheated,
  • b) above the intake chamber, separating members eliminating the water from the humid steam to be overheated,
  • c) in its upper part, bundles of tubes constituting the superheaters, in which superheated steam under pressure is cooled, then condensed in exchange for heat with the dried steam to be superheated,

and d) on either side of the bundles of superheater tubes, channels for the circulation of wet steam allowing part of it to rise in the vicinity of the internal surface of the shell, before returning to the separating bodies,

Le brevet EP-B-005225 de la Demanderesse porte sur un dispositif de ce genre, dans lequel les canaux permettent à la vapeur humide de s'élever de part et d'autre des surchauffeurs au voisinage de la surface interne de la virole, puis de redescendre entre deux groupes de surchauffeurs pour déboucher à l'entrée des séparateurs au voisinage du plan de symétrie.Patent EP-B-005225 of the Applicant relates to a device of this kind, in which the channels allow the humid vapor to rise on either side of the superheaters in the vicinity of the internal surface of the shell, then to descend between two groups of superheaters to lead to the inlet of the separators in the vicinity of the plane of symmetry.

Un tel dispositif nécessite que les surchauffeurs soient divisés en deux groupes séparés par un espace central permettant la descente de la vapeur humide. Ceci oblige à donner au dispositif un diamètre plus important, au détriment de son encombrement et de son coût.Such a device requires that the superheaters be divided into two groups separated by a central space allowing the descent of the wet steam. This requires giving the device a larger diameter, to the detriment of its size and its cost.

La présente invention a pour but de procurer un dispositif de séchage et de surchauffe de vapeur d'encombrement et de poids plus réduits que le dispositif connu, tout en assurant un refroidissement de la paroi interne de la virole aussi efficace.The object of the present invention is to provide a device for drying and overheating vapor of reduced bulk and weight than the known device, while ensuring cooling of the internal wall of the shell as effectively.

Le dispositif selon l'invention est caractérisé en ce que ses canaux de circulation de la vapeur humide sont séparés de la chambre d'admission par une cloison disposée de l'un des côtés des surchauffeurs seulement, de façon que la vapeur humide ne s'élève au voisinage de la surface interne de la virole que de l'un des côtés des surchauffeurs, puis redescende de l'autre côté vers l'admission à des organes séparateurs.The device according to the invention is characterized in that its channels for the circulation of wet steam are separated from the chamber intake by a partition arranged on one side of the superheaters only, so that the humid vapor rises in the vicinity of the internal surface of the shell only on one side of the superheaters, then descends from the on the other side towards admission to separating bodies.

Il est décrit ci-après, à titre d'exemple et en référence à la figure unique du dessin annexé, un dispositif de séchage et de surchauffe de vapeur d'eau selon l'invention, adjoint à une installation de production d'énergie par détente de vapeur d'eau dans des turbines.It is described below, by way of example and with reference to the single figure of the accompanying drawing, a device for drying and superheating water vapor according to the invention, associated with an installation for producing energy by water vapor expansion in turbines.

La figure représente le dispositif en coupe par un plan perpendiculaire à son axe, au droit de tubulures d'admission de vapeur humide et d'évacuation de vapeur surchauffée.The figure shows the device in section through a plane perpendicular to its axis, in line with the pipes for the admission of wet steam and the discharge of superheated steam.

Il comporte une virole externe 1, munie de tubulures d'admission de vapeur humide (émulsion d'eau et de vapeur) telles que 2.It has an external shroud 1, fitted with wet steam intake pipes (water and steam emulsion) such as 2.

Au-dessus d'une tubulure 2, un organe de répartition 3, tel que celui qui a fait l'objet du brevet FR-B-2442069 de la Demanderesse, répartit la vapeur humide en deux flux latéraux représentés par les flèches 4 et 5, et un flux axial représenté par la flèche 6. Du flux latéral gauche, une première partie pénètre dans les blocs d'organes séparateurs 7, formés par exemple par des empilements de tôles ondulées parallèles, sur lesquelles les gouttelettes d'eau se déposent, puis ruissellent, avant d'être évacuées par des gouttières et des tuyauteries d'évacuation, non représentées.Above a pipe 2, a distribution member 3, such as that which was the subject of patent FR-B-2442069 of the Applicant, distributes the wet steam in two lateral flows represented by the arrows 4 and 5 , and an axial flow represented by the arrow 6. From the left lateral flow, a first part penetrates into the blocks of separating members 7, formed for example by stacks of parallel corrugated sheets, on which the water droplets are deposited, then run off, before being evacuated by gutters and evacuation pipes, not shown.

Le flux latéral droit de vapeur humide, représenté par la flèche 5, pénètre dans les blocs d'organes séparateurs 8. Le flux axial, représenté par la flèche 6, pénètre dans les blocs d'organes séparateurs 9 et 10.The right lateral flow of wet steam, represented by arrow 5, enters the separator member blocks 8. The axial flow, represented by arrow 6, enters the separator member blocks 9 and 10.

La vapeur séchée issue des différents blocs d'organes séparateurs, à laquelle se réunit une autre fraction de vapeur séchée ayant servi à assurer le refroidissement de la virole, comme il sera décrit ci-après, s'élève vers les échangeurs de surchauffe 11, formés par des faisceaux tubulaires à l'intérieur desquels circule de la vapeur à pression plus élevée. Elle traverse ces échangeurs comme représentée par les flèches 12, et se rend à l'utilisation par des tubulures de sortie telles que 13.The dried steam coming from the different blocks of separating members, to which another fraction of dried steam which has served to cool the shell meets, as will be described below, rises to the overheating exchangers 11, formed by tubular bundles inside which higher pressure steam circulates. It crosses these exchangers as shown by the arrows 12, and goes to use by outlet pipes such as 13.

Une fraction de la vapeur humide ne passe pas directement dans les organes séparateurs, mais s'élève le long de la virole 1, comme représenté par la flèche 14, dans un canal 15 disposé entre la virole 1 et une enveloppe interne 16 délimitant l'écoulement de la vapeur à surchauffer. Cette fraction maintient la virole 1 à une température relativement basse. Elle redescend ensuite de l'autre côté de l'enveloppe interne 16 par un canal 17 le long du côté droit de la virole 1, comme représenté par la flèche 18. Elle est alors dirigée par une cloison 19 dans un canal 20 vers l'admission à des organes séparateurs 21, où elle se débarasse de son humidité résiduelle. Cette fraction séohée se réunit alors à la fraction principale de vapeur séchée pour se rendre aux échangeurs de surchauffe.A fraction of the wet steam does not pass directly into the separating members, but rises along the shell 1, as shown by the arrow 14, in a channel 15 disposed between the shell 1 and an internal envelope 16 delimiting the flow of steam to be superheated. This fraction keeps the shell 1 at a relatively low temperature. It then descends on the other side of the internal envelope 16 by a channel 17 along the right side of the shell 1, as shown by the arrow 18. It is then directed by a partition 19 in a channel 20 towards the admission to separating bodies 21, where it gets rid of its residual moisture. This dried fraction then joins the main dried vapor fraction to go to the overheating exchangers.

Claims (1)

Dispositif de séchage et de surchauffe de vapeur par échange de chaleur, d'axe horizontal, notamment pour l'alimentation en vapeur d'eau d'une turbine de détente, comportant à l'intérieur d'une virole cylindrique, disposés parallèlement à son axe et symétriquement par rapport à son plan de symétrie longitudinal, a) dans sa partie inférieure, une chambre d'admission de la vapeur humide à sécher et surchauffer, b) au-dessus de la chambre d'admissionjdes organes séparateurs (7, 8, 9, 10, 21) éliminant l'eau de la vapeur humide à surchauffer, c) dans sa partie supérieure, des faisceaux de tubes (11) constituant les surchauffeurs, dans lesquels de la vapeur surchauffée sous pression est refroidie, puis condensée en échange de chaleur avec la vapeur séchée à surchauffer,
et d) de part et d'autre des faisceaux de tubes surchauffeurs, des canaux (15, 17) de circulation de la vapeur humide permettant à une partie de celle-ci de s'élever au voisinage de la surface interne de la virole, avant de revenir vers les organes séparateurs,
caractérisé en ce que les canaux sont séparés de la chambre d'admission par une cloison (19) disposée de l'un des côtés des surchauffeurs seulement, de façon que la vapeur humide ne s'élève au voisinage de la surface interne de la virole que de l'un des côtés des surchauffeurs, puis redescende de l'autre côté vers l'admission à des organes séparateurs (21).
Device for drying and superheating steam by heat exchange, with a horizontal axis, in particular for supplying water vapor to an expansion turbine, comprising inside a cylindrical shell, arranged parallel to its axis and symmetrically with respect to its longitudinal plane of symmetry, a) in its lower part, a humid steam inlet chamber to be dried and overheated, b) above the inlet chamber j of the separating members (7, 8, 9, 10, 21) eliminating the water from the wet steam to be overheated, c) in its upper part, bundles of tubes (11) constituting the superheaters, in which superheated steam under pressure is cooled, then condensed in exchange for heat with the dried steam to be superheated,
and d) on either side of the bundles of superheater tubes, channels (15, 17) for circulation of the humid vapor allowing a part of it to rise in the vicinity of the internal surface of the shell, before returning to the separating bodies,
characterized in that the channels are separated from the intake chamber by a partition (19) arranged on one side of the superheaters only, so that the humid vapor does not rise in the vicinity of the internal surface of the shell on one side of the superheaters, then down on the other side towards the admission to separating members (21).
EP86103774A 1985-03-22 1986-03-20 Apparatus for separating moisture from and for reheating steam by heat exchange Ceased EP0195443A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR8504300A FR2579298B1 (en) 1985-03-22 1985-03-22 DEVICE FOR DRYING AND OVERHEATING VAPOR BY HEAT EXCHANGE
FR8504300 1985-03-22

Publications (1)

Publication Number Publication Date
EP0195443A1 true EP0195443A1 (en) 1986-09-24

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EP86103774A Ceased EP0195443A1 (en) 1985-03-22 1986-03-20 Apparatus for separating moisture from and for reheating steam by heat exchange

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US (1) US4671214A (en)
EP (1) EP0195443A1 (en)
JP (1) JPS61223407A (en)
CA (1) CA1274734A (en)
FR (1) FR2579298B1 (en)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4856461A (en) * 1988-02-01 1989-08-15 Combustion Engineering, Inc. Multiple tube steam dryer for moisture separator reheater
US5049171A (en) * 1988-04-24 1991-09-17 Ingersoll-Rand Company Oil/air separator
FR2640727B1 (en) * 1988-12-15 1991-08-16 Stein Industrie OVERHEATER BEAM FOR HORIZONTAL STEAM SEPARATOR-SUPERHEATER
FR2641848B1 (en) * 1989-01-19 1991-08-16 Stein Industrie OVERHEATING HARNESS FOR VAPOR SEPARATOR-SUPERHEATER WITH HORIZONTAL TUBES
US5989302A (en) * 1996-02-13 1999-11-23 Dltk, Inc. Steam separator including an interior baffle with openings defining steam ports and a water flow surface
WO2008026325A1 (en) * 2006-08-28 2008-03-06 Mitsubishi Heavy Industries, Ltd. Moisture separator
JP5456107B2 (en) * 2012-07-27 2014-03-26 三菱重工業株式会社 Moisture separator
KR102210811B1 (en) * 2019-03-28 2021-02-02 한국에너지기술연구원 Decompression apparatus for superheated steam

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0005225A1 (en) * 1978-04-28 1979-11-14 STEIN INDUSTRIE Société anonyme dite: Apparatus for extracting moisture from and for reheating steam

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1177793A (en) * 1915-08-27 1916-04-04 Forest Products Company Combined boiler, retort, and superheater.
NL6812147A (en) * 1967-09-06 1969-03-10
US3532160A (en) * 1968-09-06 1970-10-06 American Precision Ind Heat exchanger of the tube and plate type
US4123237A (en) * 1977-03-25 1978-10-31 Foster Wheeler Energy Corporation Low pressure drop girth baffle steam separator
FR2442069A1 (en) * 1978-11-24 1980-06-20 Stein Industrie DEVICE FOR DISTRIBUTING A MIXTURE OF VAPOR AND LIQUID IN A HORIZONTAL AXIS SEPARATOR
US4302227A (en) * 1980-05-27 1981-11-24 General Electric Company Baffled moisture separator
FR2553867B1 (en) * 1983-10-19 1985-12-27 Stein Industrie STEAM SUPERHEATER SEPARATOR AND MOUNTING METHOD THEREOF

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0005225A1 (en) * 1978-04-28 1979-11-14 STEIN INDUSTRIE Société anonyme dite: Apparatus for extracting moisture from and for reheating steam

Also Published As

Publication number Publication date
CA1274734A (en) 1990-10-02
JPS61223407A (en) 1986-10-04
FR2579298B1 (en) 1987-05-07
FR2579298A1 (en) 1986-09-26
US4671214A (en) 1987-06-09

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