EP2141411A1 - Header distributor for two-phase flow in a single pass evaporator - Google Patents
Header distributor for two-phase flow in a single pass evaporator Download PDFInfo
- Publication number
- EP2141411A1 EP2141411A1 EP08447033A EP08447033A EP2141411A1 EP 2141411 A1 EP2141411 A1 EP 2141411A1 EP 08447033 A EP08447033 A EP 08447033A EP 08447033 A EP08447033 A EP 08447033A EP 2141411 A1 EP2141411 A1 EP 2141411A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- header
- section
- inlet header
- evaporator
- distributor
- 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
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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
- F22B37/22—Drums; Headers; Accessories therefor
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B1/00—Methods of steam generation characterised by form of heating method
- F22B1/02—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers
- F22B1/18—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being a hot gas, e.g. waste gas such as exhaust gas of internal-combustion engines
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B29/00—Steam boilers of forced-flow type
- F22B29/06—Steam boilers of forced-flow type of once-through type, i.e. built-up from tubes receiving water at one end and delivering superheated steam at the other end of the tubes
-
- 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
-
- 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
- F22B37/62—Component parts or details of steam boilers specially adapted for steam boilers of forced-flow type
- F22B37/70—Arrangements for distributing water into water tubes
- F22B37/74—Throttling arrangements for tubes or sets of tubes
Definitions
- the present invention is applicable to any steam generator, but more particularly to horizontal once-through heat recovery steam generators, where a two-phases flow has to be equally distributed inside all heating tubes through an inlet header.
- the evaporators bundles are usually formed with multiple parallel tubes arranged in successive rows perpendicular to the gas flow direction. Each row of tubes is connected at its lower side to an inlet header and at its upper side to an outlet header.
- Horizontal heat recovery steam generators which are designed with a once-through evaporator may have this heat exchanger split in two sections in series.
- the heating tubes of the first section once-through evaporator are fed with hot water coming from an economizer and discharge water-steam mixture with a partial steam fraction.
- That fluid is transferred from the first to the second section by means of manifolds, pipes, distributors and feeders.
- the heating tubes of the second section once-through evaporator are then fed with two-phases fluid and discharge superheated steam.
- heated water flows through the tubes of a once-through section at a rate sufficient to maintain the interiors of its tubes fully wetted while enabling steam to develop in that water.
- This is possible because the once-through section is followed by a circulation section delivering saturated steam to the superheater, while in a steam generator comprising only a once-through evaporator, no liquid water should leave the evaporator. In this case, as the fraction of steam remains always below 100%, the tubes of the once-through section remain fully wetted.
- a steam generator has a once-through evaporator which converts liquid water into steam in tubes over which hot gases flow.
- each tube contains a metal tape which is twisted into a helical configuration to induce turbulence in the mist produced by the boiling, and these turbulences insure that the mist wets the inside surfaces of the tubes, thus producing good heat transfer and moderate temperatures in the tubes.
- Document JP-A-2007/298245 is related to an economizer designed to pass almost evenly liquid water, i.e. a monophasic fluid, through a row of heat transfer pipes.
- an appropriate distributor device should be installed in the interconnecting pipes in order to supply an identical steam fraction inside each feeder.
- a feeder is connected on an inlet header for feeding several heating tubes.
- a specific distributor device must be installed either inside the inlet header or in each feeder nozzle to facilitate the equalization of the distribution.
- the main object of the present invention is to drastically improve the distribution equalization of the water-steam flow inside all the heating tubes of the second evaporator section.
- the invention intends to allow achieving a more uniform steam temperature profile at the outlet of the heating tubes and then to improve the lifetime of the components.
- the invention aims at accommodating with different geometries and dimensions of the heating tubes and the inlet headers.
- the invention also intends to easily eliminate the stratification effect existing in the feeder nozzles due to water centrifugation induced by the feeder pipe routing.
- a further goal of the invention is to permit its use as a retrofit in existing exchangers in order to restore acceptable operating conditions.
- a first object of the present invention is related, as indicated in Claim 1, to an evaporator sections in a steam generator comprising an inlet header, an outlet header, a plurality of heating tubes connected in parallel at a first end to said inlet header and at a second end to said outlet header, at least a feeder pipe terminated by a feeder nozzle connected to said inlet header and a header distributor for conveying a two-phases or biphasic fluid through the inlet header from the feeder pipe, characterized in that said header distributor comprises means to perform an equalization of the biphasic fluid distribution inside said plurality of heating tubes.
- Preferred embodiments of the invention further contain, in combination with the features of Claim 1, one or several of the following features disclosed in the secondary claims :
- Still another object of the present invention concerns, as indicated in Claim 11, concerns a heat recovery steam generator (HRSG) comprising an exhaust gas duct connected to a hot gas source, an economizer, a first section and a second section of a once-through evaporator and a superheater, means comprising manifolds, pipes, distributors and feeder pipes for transferring a water-steam mixture, i.e. a biphasic flow, from said first section to said second section of the evaporator, said distributors being configured for equally spreading the biphasic flow into the feeder pipes, characterized in that said second evaporator section is an evaporator section as in Claim 1.
- HRSG heat recovery steam generator
- FIG.1 is a schematic cross-sectional view of a horizontal once-through heat recovery steam generator (HRSG) constructed in accordance with and embodying the present invention.
- HRSG horizontal once-through heat recovery steam generator
- FIG.2 is a schematic perspective view of the second section of the evaporator with vertical heating tubes and embodying the present invention.
- FIG.3 is a schematic cross-sectional side view of the inlet header embodying the present invention.
- FIG.4 is a fragmentary schematic cross-sectional front view of the inlet header embodying a tubular distributor.
- FIG.5 is a fragmentary schematic cross-sectional plan view of the inlet header embodying a tubular distributor.
- FIG.6 is a fragmentary schematic cross-sectional plan view of the inlet header and the feeder pipe which could have a non-perpendicular orientation in regards of the inlet header axis.
- FIG.7 is a fragmentary schematic cross-sectional front view of the inlet header embodying a conical-type distributor.
- a steam generator includes an exhaust gas duct 1 connected to a hot gas source such as a gas turbine.
- the hot gas flows in series respectively through a superheater 2, a second section 3 of a once-through evaporator, a first section 4 of said once-through evaporator and an economizer 5.
- the water flows in the opposite direction and is forced by the feedwater pump 6 to the cold side of the economizer 5.
- the heat extracted from the hot gas elevates the temperature of the water which leaves the first exchanger hotter than when entering.
- the liquid water then flows to the first section of the evaporator 4 which converts part of the water into steam at saturated conditions after further extraction of heat from the hot gas.
- the water-steam mixture (i.e. a two-phases fluid) is transferred from said first section 4 to said second section 3 by means of manifolds 7, pipes 8, distributors 9 and feeders 10.
- the two-phases flow is equally spread into the feeders 10 by means of the distributors 9.
- the extracted heat from the hot gas terminates the evaporation and slightly superheats the steam.
- the second section 3 of the once-through evaporator includes a plurality of heating tubes 12 arranged along a single row - however a multiple tube rows arrangement is also possible - connected on the inlet header 11 at the lower side and on the outlet header 13 at the upper side.
- the inlet header 11 has one or several feeder nozzles 14 onto which the feeders 10 are connected and receiving the two-phases flow from the distributors 9.
- the outlet header 13 has one or several connector nozzles 15 for conveying the superheated steam to the superheater 2.
- FIG.3 to FIG.7 illustrate preferred embodiments of the device of the invention which is called a "two-phases flow header distributor" for a tubular-type 16 or a conical-type distributor 20 respectively, where said two-phases flow is passing through the feeder nozzle 14 and entering partly inside the inlet header 11.
- the tubular distributor is fitted with an end cap 17 in order to eliminate any water jet effect impacting the distribution equalization, especially in the nearby heating tubes 12 and more generally in all other heating tubes.
- the distributor 16 is fitted in this example with two opposite main orifices or openings 18 located along the inlet header 11 axis.
- the purpose is to spread equally the water onto the sides of the inlet header 11 regardless of the possible water stratification in the feeder pipe 10 and feeder nozzle 14 sections.
- the type, number, dimensions and position of those openings 18 may vary according to the heating tubes-inlet header 11, 12 configuration, to the feeder pipe 10 routing and to the real operating conditions.
- two small holes or orifices 19 are fitted on the distributor end cap 17 along the inlet header 11 axis.
- the purpose is to allow a direct and controlled water feeding of the nearby heating tubes 12 if they are partially hidden by the distributor according to the arrangement.
- the type, number, dimensions and position of those openings 19 may also vary according to the heating tubes-inlet header 11, 12 configuration, to the feeder pipe 10 routing and to the real operating conditions.
- the orientation of the feeder pipe 10 has a direct impact on the water stratification inside the pipe due to the centrifugation effect taking place in the last pipe elbow.
- the header distributor 16 shall be preferably oriented for having the lateral openings 18 perpendicular to the last elbow in order to force the water film present on the extrados side of the upstream elbow to remix in the pipe end cap before being equally spread through the openings.
- the type, number, dimensions and position of those openings 18 may also vary according to the heating tubes-inlet header 11, 12 configuration and to the real operating conditions.
- a conical-type distributor 20 is an alternate design for the same purpose. It consists substantially in an inverted cone 21 passing through the feeder nozzle 14.
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- 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)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
Description
- The present invention is applicable to any steam generator, but more particularly to horizontal once-through heat recovery steam generators, where a two-phases flow has to be equally distributed inside all heating tubes through an inlet header.
- In horizontal heat recovery steam generators, the evaporators bundles are usually formed with multiple parallel tubes arranged in successive rows perpendicular to the gas flow direction. Each row of tubes is connected at its lower side to an inlet header and at its upper side to an outlet header.
- Horizontal heat recovery steam generators which are designed with a once-through evaporator may have this heat exchanger split in two sections in series.
- In this case, the heating tubes of the first section once-through evaporator are fed with hot water coming from an economizer and discharge water-steam mixture with a partial steam fraction.
- That fluid is transferred from the first to the second section by means of manifolds, pipes, distributors and feeders.
- The heating tubes of the second section once-through evaporator are then fed with two-phases fluid and discharge superheated steam.
- It is very important to assure that the feeding of the two-phases flow is equally distributed over all heating tubes of the second evaporator section in order to achieve an uniform temperature profile of the steam over all heating tubes outlets. If a particular tube receives more water than the average, the steam temperature at its outlet shall be lower than in the other tubes and its mean metal temperature shall also be lower inducing unexpected specific tensile thermal stress in said tube. The opposite behavior (so receiving less water than the average) also induces unexpected specific compressive thermal stress. Depending upon the tube configurations, those thermal stresses could also generate at the tubes-to-headers connections high bending stresses with detrimental effects in respect of lifetime.
- In steam generators as described in document
WO-A-2006/107315 , once-through evaporator sections are usually provided under the form of multiple single-row header-and-tube assemblies. As in such assemblies, each row of tubes is connected to a linear inlet header with a central water inlet tube, there is a risk that portions of the tubes where steam is created run dry. It may also occur in such a configuration that water is segregated in the outlet sections of the central tubes of the row, while steam is segregated in the outlet sections of the external tubes of the row. This produces higher temperatures in some tube walls and less efficient heat transfer. The higher temperatures require then the use of tubes made of expensive high alloy steels - In document
WO-A-03/048638 - In document
US-A-2004/0069244 , a steam generator has a once-through evaporator which converts liquid water into steam in tubes over which hot gases flow. To overcome the drawback of tubes running dry, each tube contains a metal tape which is twisted into a helical configuration to induce turbulence in the mist produced by the boiling, and these turbulences insure that the mist wets the inside surfaces of the tubes, thus producing good heat transfer and moderate temperatures in the tubes. - Document
JP-A-2007/298245 - Considering the properties of the two-phases flow, it is very difficult to easily achieve an equal distribution inside all the heating tubes because the water and the steam have highly different densities.
- In that respect an appropriate distributor device should be installed in the interconnecting pipes in order to supply an identical steam fraction inside each feeder.
- A feeder is connected on an inlet header for feeding several heating tubes. A specific distributor device must be installed either inside the inlet header or in each feeder nozzle to facilitate the equalization of the distribution.
- The main object of the present invention is to drastically improve the distribution equalization of the water-steam flow inside all the heating tubes of the second evaporator section.
- More particularly for a once-through evaporator, the invention intends to allow achieving a more uniform steam temperature profile at the outlet of the heating tubes and then to improve the lifetime of the components.
- Among other objectives, the invention aims at accommodating with different geometries and dimensions of the heating tubes and the inlet headers.
- The invention also intends to easily eliminate the stratification effect existing in the feeder nozzles due to water centrifugation induced by the feeder pipe routing.
- A further goal of the invention is to permit its use as a retrofit in existing exchangers in order to restore acceptable operating conditions.
- A first object of the present invention is related, as indicated in Claim 1, to an evaporator sections in a steam generator comprising an inlet header, an outlet header, a plurality of heating tubes connected in parallel at a first end to said inlet header and at a second end to said outlet header, at least a feeder pipe terminated by a feeder nozzle connected to said inlet header and a header distributor for conveying a two-phases or biphasic fluid through the inlet header from the feeder pipe, characterized in that said header distributor comprises means to perform an equalization of the biphasic fluid distribution inside said plurality of heating tubes.
- Preferred embodiments of the invention further contain, in combination with the features of Claim 1, one or several of the following features disclosed in the secondary claims :
- said header distributor is tubular, passing through the feeder nozzle at the connection of the feeder pipe to the inlet header, and having a protruding section inside said inlet header, said protruding section being provided with an end cap and having at least two diametrically-opposed main orifices located on the lateral surface of the distributor ;
- said main orifices are partly located in the protruding section of the distributor inside the inlet header and partly inside the feeder nozzle ;
- said end cap is provided with at least two secondary orifices aligned along the inlet header axis ;
- the size of the secondary orifices is smaller than the size of the main orifices ;
- the line joining the centres of the main orifices is perpendicular to the axis of the feeder pipe at the location the latter is entering the inlet header ;
- said header distributor is a conical or plug-like distributor, substantially comprising an inverted plug passing through the feeder nozzle connecting the feeder pipe and the inlet header and having a terminal part protruding into the inlet header ;
- said evaporator is a once-through evaporator ;
- the plurality of heating tubes is arranged along a single row of tubes connected to the inlet header and to the outlet header ;
- said biphasic fluid is a mixture of steam and water.
- Still another objet of the present invention concerns, as indicated in
Claim 11, concerns a heat recovery steam generator (HRSG) comprising an exhaust gas duct connected to a hot gas source, an economizer, a first section and a second section of a once-through evaporator and a superheater, means comprising manifolds, pipes, distributors and feeder pipes for transferring a water-steam mixture, i.e. a biphasic flow, from said first section to said second section of the evaporator, said distributors being configured for equally spreading the biphasic flow into the feeder pipes, characterized in that said second evaporator section is an evaporator section as in Claim 1. -
FIG.1 is a schematic cross-sectional view of a horizontal once-through heat recovery steam generator (HRSG) constructed in accordance with and embodying the present invention. -
FIG.2 is a schematic perspective view of the second section of the evaporator with vertical heating tubes and embodying the present invention. -
FIG.3 is a schematic cross-sectional side view of the inlet header embodying the present invention. -
FIG.4 is a fragmentary schematic cross-sectional front view of the inlet header embodying a tubular distributor. -
FIG.5 is a fragmentary schematic cross-sectional plan view of the inlet header embodying a tubular distributor. -
FIG.6 is a fragmentary schematic cross-sectional plan view of the inlet header and the feeder pipe which could have a non-perpendicular orientation in regards of the inlet header axis. -
FIG.7 is a fragmentary schematic cross-sectional front view of the inlet header embodying a conical-type distributor. - Referring to
FIG. 1 , a steam generator according to a preferred embodiments of the present invention includes an exhaust gas duct 1 connected to a hot gas source such as a gas turbine. The hot gas flows in series respectively through asuperheater 2, asecond section 3 of a once-through evaporator, afirst section 4 of said once-through evaporator and aneconomizer 5. - The water flows in the opposite direction and is forced by the feedwater pump 6 to the cold side of the
economizer 5. The heat extracted from the hot gas elevates the temperature of the water which leaves the first exchanger hotter than when entering. - The liquid water then flows to the first section of the
evaporator 4 which converts part of the water into steam at saturated conditions after further extraction of heat from the hot gas. - The water-steam mixture (i.e. a two-phases fluid) is transferred from said
first section 4 to saidsecond section 3 by means of manifolds 7, pipes 8, distributors 9 andfeeders 10. The two-phases flow is equally spread into thefeeders 10 by means of the distributors 9. - In the
second section 3 of the evaporator, the extracted heat from the hot gas terminates the evaporation and slightly superheats the steam. - Finally the heat extracted inside the
superheater 2 raises the temperature of the superheated steam up to the live steam conditions needed for powering a steam turbine or any other process. - Referring to
FIG.2 , thesecond section 3 of the once-through evaporator includes a plurality ofheating tubes 12 arranged along a single row - however a multiple tube rows arrangement is also possible - connected on theinlet header 11 at the lower side and on theoutlet header 13 at the upper side. - The
inlet header 11 has one orseveral feeder nozzles 14 onto which thefeeders 10 are connected and receiving the two-phases flow from the distributors 9. - The
outlet header 13 has one orseveral connector nozzles 15 for conveying the superheated steam to thesuperheater 2. -
FIG.3 to FIG.7 illustrate preferred embodiments of the device of the invention which is called a "two-phases flow header distributor" for a tubular-type 16 or a conical-type distributor 20 respectively, where said two-phases flow is passing through thefeeder nozzle 14 and entering partly inside theinlet header 11. - Referring to
FIG.3 to FIG.5 , the tubular distributor is fitted with anend cap 17 in order to eliminate any water jet effect impacting the distribution equalization, especially in thenearby heating tubes 12 and more generally in all other heating tubes. - The
distributor 16 is fitted in this example with two opposite main orifices oropenings 18 located along theinlet header 11 axis. The purpose is to spread equally the water onto the sides of theinlet header 11 regardless of the possible water stratification in thefeeder pipe 10 andfeeder nozzle 14 sections. The type, number, dimensions and position of thoseopenings 18 may vary according to the heating tubes-inlet header feeder pipe 10 routing and to the real operating conditions. - Moreover two small holes or
orifices 19 are fitted on thedistributor end cap 17 along theinlet header 11 axis. The purpose is to allow a direct and controlled water feeding of thenearby heating tubes 12 if they are partially hidden by the distributor according to the arrangement. The type, number, dimensions and position of thoseopenings 19 may also vary according to the heating tubes-inlet header feeder pipe 10 routing and to the real operating conditions. - Referring to
FIG.6 , the orientation of thefeeder pipe 10 has a direct impact on the water stratification inside the pipe due to the centrifugation effect taking place in the last pipe elbow. Theheader distributor 16 shall be preferably oriented for having thelateral openings 18 perpendicular to the last elbow in order to force the water film present on the extrados side of the upstream elbow to remix in the pipe end cap before being equally spread through the openings. The type, number, dimensions and position of thoseopenings 18 may also vary according to the heating tubes-inlet header - Referring to
FIG.7 , a conical-type distributor 20 is an alternate design for the same purpose. It consists substantially in aninverted cone 21 passing through thefeeder nozzle 14.
Claims (11)
- Evaporator section (3) in a steam generator comprising an inlet header (11), an outlet header (13), a plurality of heating tubes (12) connected in parallel at a first end to said inlet header (11) and at a second end to said outlet header (13), at least a feeder pipe (10) terminated by a feeder nozzle (14) connected to said inlet header (11) and a header distributor (16, 20) for conveying a biphasic fluid through the inlet header (11) from the feeder pipe (10), characterized in that said header distributor (16, 20) comprises means (17, 18, 19, 21) to perform an equalization of the biphasic fluid distribution inside said plurality of heating tubes (12).
- Evaporator section (3) according to Claim 1, characterized in that said header distributor (16) is tubular, passing through the feeder nozzle (14) at the connection of the feeder pipe (10) to the inlet header (11), and having a protruding section inside said inlet header (11), said protruding section being provided with an end cap (17) and having at least two diametrically-opposed main orifices (18) located on the lateral surface of the distributor (16).
- Evaporator section (3) according to Claim 2, characterized in that said main orifices (18) are partly located in the protruding section of the distributor (16) inside the inlet header (11) and partly inside the feeder nozzle (14).
- Evaporator section (3) according to Claim 2, characterized in that said end cap is provided with at least two secondary orifices (19) aligned along the inlet header axis.
- Evaporator section (3) according to Claim 4, characterized in that the size of the secondary orifices (19) is smaller than the size of the main orifices (18).
- Evaporator section (3) according to Claim 2, characterized in that the line joining the centres of the main orifices (18) is perpendicular to the axis of the feeder pipe (10) at the location the latter is entering the inlet header (11).
- Evaporator section (3) according to Claim 1, characterized in that said header distributor (20) is a conical or plug-like distributor, substantially comprising an inverted plug (21) passing through the feeder nozzle (14) connecting the feeder pipe (10) and the inlet header (11) and having a terminal part protruding into the inlet header (11).
- Evaporator section (3) according to Claim 1, characterized in that said evaporator is a once-through evaporator.
- Evaporator section (3) according to Claim 1, characterized in that the plurality of heating tubes (12) is arranged along a single row of tubes connected to the inlet header (11) and to the outlet header (13).
- Evaporator section (3) according to Claim 1, characterized in that said biphasic fluid is a mixture of steam and water.
- Heat recovery steam generator comprising an exhaust gas duct (1) connected to a hot gas source, an economizer (5), a first section (4) and a second section (3) of a once-through evaporator and a superheater (2), means comprising manifolds (7), pipes (8), distributors (9) and feeder pipes (10) for transferring a water-steam mixture, i.e. a biphasic flow, from said first section (4) to said second section (3) of the evaporator, said distributors (9) being configured for equally spreading the biphasic flow into the feeder pipes (10), characterized in that said second evaporator section (3) is an evaporator section (3) as in Claim 1.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PL08447033T PL2141411T3 (en) | 2008-06-30 | 2008-06-30 | Header distributor for two-phase flow in a single pass evaporator |
EP08447033.5A EP2141411B1 (en) | 2008-06-30 | 2008-06-30 | Header distributor for two-phase flow in a single pass evaporator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP08447033.5A EP2141411B1 (en) | 2008-06-30 | 2008-06-30 | Header distributor for two-phase flow in a single pass evaporator |
Publications (2)
Publication Number | Publication Date |
---|---|
EP2141411A1 true EP2141411A1 (en) | 2010-01-06 |
EP2141411B1 EP2141411B1 (en) | 2013-08-21 |
Family
ID=40364430
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP08447033.5A Not-in-force EP2141411B1 (en) | 2008-06-30 | 2008-06-30 | Header distributor for two-phase flow in a single pass evaporator |
Country Status (2)
Country | Link |
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EP (1) | EP2141411B1 (en) |
PL (1) | PL2141411T3 (en) |
Citations (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB770589A (en) * | 1954-04-28 | 1957-03-20 | Siemens Ag | Improvements in or relating to means for regulating flow inside the headers of steamgenerators |
GB949027A (en) * | 1962-07-28 | 1964-02-05 | Vorkauf Heinrich | Improvements in forced recirculation steam generators |
FR1549058A (en) * | 1967-01-19 | 1968-12-06 | ||
JPS57101296A (en) * | 1980-12-17 | 1982-06-23 | Mitsubishi Heavy Ind Ltd | Header |
JPS58173393A (en) * | 1982-04-02 | 1983-10-12 | Mitsubishi Heavy Ind Ltd | Distributing header for two (vapor-liquid) phase fluid |
US5806586A (en) * | 1993-07-03 | 1998-09-15 | Ernst Flitsch Gmbh & Co. | Plate heat exchanger with a refrigerant distributor |
WO2003048638A1 (en) | 2001-12-05 | 2003-06-12 | Nooter/Eriksen, Inc. | Evaporator and evaporative process for generating saturated steam |
US20040069244A1 (en) | 2002-10-04 | 2004-04-15 | Schroeder Joseph E. | Once-through evaporator for a steam generator |
US6957630B1 (en) * | 2005-03-31 | 2005-10-25 | Alstom Technology Ltd | Flexible assembly of once-through evaporation for horizontal heat recovery steam generator |
JP2007298245A (en) | 2006-05-02 | 2007-11-15 | Babcock Hitachi Kk | Economizer and exhaust heat recovery boiler provided therewith |
-
2008
- 2008-06-30 PL PL08447033T patent/PL2141411T3/en unknown
- 2008-06-30 EP EP08447033.5A patent/EP2141411B1/en not_active Not-in-force
Patent Citations (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB770589A (en) * | 1954-04-28 | 1957-03-20 | Siemens Ag | Improvements in or relating to means for regulating flow inside the headers of steamgenerators |
GB949027A (en) * | 1962-07-28 | 1964-02-05 | Vorkauf Heinrich | Improvements in forced recirculation steam generators |
FR1549058A (en) * | 1967-01-19 | 1968-12-06 | ||
JPS57101296A (en) * | 1980-12-17 | 1982-06-23 | Mitsubishi Heavy Ind Ltd | Header |
JPS58173393A (en) * | 1982-04-02 | 1983-10-12 | Mitsubishi Heavy Ind Ltd | Distributing header for two (vapor-liquid) phase fluid |
US5806586A (en) * | 1993-07-03 | 1998-09-15 | Ernst Flitsch Gmbh & Co. | Plate heat exchanger with a refrigerant distributor |
WO2003048638A1 (en) | 2001-12-05 | 2003-06-12 | Nooter/Eriksen, Inc. | Evaporator and evaporative process for generating saturated steam |
US20040069244A1 (en) | 2002-10-04 | 2004-04-15 | Schroeder Joseph E. | Once-through evaporator for a steam generator |
US6957630B1 (en) * | 2005-03-31 | 2005-10-25 | Alstom Technology Ltd | Flexible assembly of once-through evaporation for horizontal heat recovery steam generator |
WO2006107315A1 (en) | 2005-03-31 | 2006-10-12 | Alstom Technology Ltd | Flexible assembly of once-through evaporation for horizontal heat recovery steam generator |
JP2007298245A (en) | 2006-05-02 | 2007-11-15 | Babcock Hitachi Kk | Economizer and exhaust heat recovery boiler provided therewith |
Also Published As
Publication number | Publication date |
---|---|
PL2141411T3 (en) | 2014-01-31 |
EP2141411B1 (en) | 2013-08-21 |
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