EP1327819B1 - Steam pressure reducing and conditioning system - Google Patents
Steam pressure reducing and conditioning system Download PDFInfo
- Publication number
- EP1327819B1 EP1327819B1 EP02007253.4A EP02007253A EP1327819B1 EP 1327819 B1 EP1327819 B1 EP 1327819B1 EP 02007253 A EP02007253 A EP 02007253A EP 1327819 B1 EP1327819 B1 EP 1327819B1
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- EP
- European Patent Office
- Prior art keywords
- valve
- steam
- nozzle
- moisture
- lower discharge
- 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
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Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22G—SUPERHEATING OF STEAM
- F22G5/00—Controlling superheat temperature
- F22G5/12—Controlling superheat temperature by attemperating the superheated steam, e.g. by injected water sprays
- F22G5/123—Water injection apparatus
- F22G5/126—Water injection apparatus in combination with steam-pressure reducing valves
Definitions
- the present invention concerns a steam pressure reducing and conditioning system.
- a steam pressure reducing and conditioning system comprising a steam source 24 (such as boiler) for generating superheated steam S, a pressure reducing and conditioning valve 21 for depressurizing and desuperheating steam S generated by this steam source 24, and a discharge pipe 23 connected to an outlet of steam pressure reducing and conditioning valve 21, and connected to a steam work section 22, downstream of valve 21.
- a steam source 24 such as boiler
- a pressure reducing and conditioning valve 21 for depressurizing and desuperheating steam S generated by this steam source 24
- a discharge pipe 23 connected to an outlet of steam pressure reducing and conditioning valve 21, and connected to a steam work section 22, downstream of valve 21.
- steam pressure and conditioning valve 21 receives superheated and pressurized steam S inflowing in inlet 21a.
- Steam S is desuperheated and depressurized by passing steam S valve 21 and injecting subcooled water mist W (not shown) from one or more nozzles 25 in the lower portion of valve 21.
- the desuperheated and depressurized steam S 1 discharged from the valve 21 and the subcooled water mist W injected in valve 21, flow into the discharge pipe 23 and are conveyed to the steam work section 22.
- a portion of discharge pipe 23 is arranged horizontally 23a. Some of the subcooled water mist W condenses and clings to the discharge pipe at 23a and flows along the bottom of the horizontal section. Steam S 1 flows past these areas of condensation creating temperature differentials in the interior surface of the pipe 23.
- the pipe 23 deforms (bends upward) and possibly breaks due to expansion and stress due to the temperature difference in horizontal section of pipe 23, and moreover, the condensed moisture W 1 , flowing at the bottom of the pipe 23 is enrolled up by the high speed flow of steam S 1 (jumping phenomenon).
- the jumping phenomenon erroneous temperature measurements in temperature sensors in the pipe 23 for detecting the heat of the steam S 1 .
- GB 772,058 relates to a desuperheater for steam or other superheated vapor and teaches a desuperheater containing a venturi nozzle, a vessel, and a pipe connecting the vessel to venturi nozzle.
- GB 772,058 has no disclosure or teaching of a steam conditioning valve for controlling the flow of steam with a lower discharge end having a reduced cross-sectional area with a discharge opening from an injection nozzle disposed in the reduced cross-sectional area.
- U.S. Patent No. 3,496,724 discloses a desuperheater system and related method which generally correspond to the preamble of claims 1 and 3 herein.
- the present invention provides a system and method in accordance with the appended claims.
- the present invention concerns a steam pressure reducing and conditioning system comprising a steam reducing and conditioning valve 1 for desuperheating and depressurizing superheated steam S by injecting subcooled water mist W in the lower portion of valve 1.
- a discharge pipe 3 is connected at its proximal end to the exit of valve 1.
- a steam work section 2 is connected at the distal end of pipe 3.
- the discharge pipe 3 has a horizontal portion 3a, and said horizontal portion 3a is provided with a moisture drain 4 at the bottom portion or at a portion near the bottom of the horizontal portion 3a of pipe 3.
- Condensed subcooled water mist (“moisture”) W 1 is extracted from discharge pipe 23 by drain 4 and is recycled and reinjected as moisture W to be supplied to the vapor S in said conditioning valve 1.
- Moisture drain 4 is directly connected by a moisture transport conduit 5 to the conditioning valve 1.
- the steam conditioning valve 1 further includes a reduced annular section 9 with a nozzle 5a disposed therein for injecting subcooled water mist W into the reduced annular section 9 of conditioning valve 1.
- Moisture W is drawn into steam flow S due to the Venturi effect caused by the pressure drop through the reduced annular section.
- a superheated steam S is desuperheated by supplying subcooled water mist ("moisture”) W to steam conditioning valve 1.
- the desuperheated steam S 1 flowing out from the conditioning valve 1 and the moisture W used for cooling in discharge valve 1 flows into discharge pipe 3, and is introduced in the steam work section 2 connected to the downstream area of the discharge pipe 3.
- the condensed moisture W 1 is drained from a moisture drain 4 disposed at the bottom portion 3a of this pipe 3, and the moisture W 1 extracted from the moisture drain 4 is recycled as part of moisture W to be supplied to the steam S in the steam conditioning valve 1.
- moisture W 1 can be removed from the horizontal section 3a of the pipe 3, preventing the moisture W 1 from stagnating at the bottom of the pipe, solving the aforementioned problem of the prior art discussed in the background section, and further, the recycling of moisture W 1 used for cooling the vapor S again in the conditioning valve 1 saves energy.
- This embodiment of the present invention comprises, as shown in Figs. 1 and 2 , a steam desuperheating and conditioning valve 1 wherein a superheated and pressurized steam S generated in a steam generation source 8 (for instance, boiler) flows into a first port 1a of conditioning valve 1.
- Steam S is desuperheated and depressurized by passing through a small hole section 6 (diffuser) having scattered small holes 6a, and the steam S 1 is discharged from a second port 1b of conditioning valve 1.
- Steam S 1 is desuperheated by injecting a subcooled water mist "moisture" W from one or more nozzles 7.
- a discharge pipe 3 is connected at its proximal end to the exit of conditioning valve 1, and at its distal end to a steam work section 2 (for instance, condenser for a nuclear reactor).
- the discharge pipe 3 is provided with a horizontal section 3a extending from the conditioning valve 1 and disposed horizontally with an elbow section 3b (bent section) .
- the discharge pipe 3 is so composed that the condensed moisture W 1 flowing in this horizontal section 3a is part of the moisture W to be supplied to the vapor S in the conditioning valve 1.
- said discharge pipe 3 is provided with a moisture drain 4 having a drain hole 4a at or near the bottom portion of the horizontal section 3a, said moisture drain 4 is provided with a moisture transport conduit 5 for directly conveying moisture W 1 extracted from the moisture drain 4 to the vapor cooler 1.
- This moisture transport conduit 5 is a tubular element having a predetermined diameter, and connected to a reduced annular area 9 constituting a predetermined area of the conditioning valve 1, where a steam S 1 flowing in the conduit will flow faster than the steam flowing in the larger diameter discharge pipe 3.
- annular reduced diameter section 9 is disposed in the lower portion of conditioning valve 1 at a position near the jet nozzle 7 of the conditioning valve 1.
- a nozzle 5a of the moisture conduit 5 exits into this reduced diameter section 9, and it is so configured that the moisture W 1 in the moisture conduit 5 is injected into depressurized steam S 1 path, in this reduced diameter section 9.
- This reduced diameter section 9 obtains improved cooling effect by maintaining the steam S 1 flow rate immediately passing through the reduced diameter section 9 faster than the vapor S 1 passing through the discharge pipe 3, thereby reducing the pressure at the position of the reduced diameter section 9 below the pressure in the discharge pipe 3.
- This pressure drop in a reduced diameter section 9 is due to the increased velocity of a constant flow volume.
- Such an effect is well known in the art and is referred to as a Venturi effect. Consequently, this embodiment of the present invention allows return of the moisture W 1 from the discharge pipe 3 to the conditioning valve 1 by connecting the nozzle 5a of moisture transport conduit 5 to this reduced diameter section 9, and drawing the moisture W 1 from the nozzle 5a into the conditioning valve 1 using the differential pressure generated by the Venturi negative pressure phenomenon.
- this level difference it is preferable to set this level difference to 10 meters or less, in the case where the moisture drain 4 is placed lower than the nozzle 5a (no limitation in the case where the moisture drain section 4 is placed higher than the nozzle 5a).
- the vapor S 1 differential pressure is used as mentioned before, as a means for recycling the moisture W 1 flowing from the conditioning valve 1 back to the conditioning valve 1.
- a forced delivery apparatus for instance a pump or the like
- the moisture transport conduit 5 would be outside of and contrary to the scope of the claimed invention.
- this embodiment desuperheats the steam S in the conditioning valve 1, and the desuperheated and depressurized steam S 1 is discharged from the conditioning valve 1 together with moisture W into the discharge pipe 3.
- the steam S 1 flowing through discharge pipe 3 is introduced into the steam work section 2 connected to the distal end of the discharge pipe 3.
- the moisture W 1 flowing at the bottom of the discharge pipe 3 is extracted by the moisture drain 4, transferred by the moisture transport conduit 5 and recycled as moisture W for cooling in the steam conditioning valve 1.
- this embodiment provides for an energy efficient removal of the moisture W 1 from the horizontal section 3a of the discharge pipe 3, thereby preventing the moisture W 1 from stagnating at the bottom of the discharge pipe 3, avoiding as much as possible the pipe 3 deformation (damage) and the detrimental effect to the temperature detection sensor and other problems of the prior art. Additionally, the present invention provides for recycling the moisture W 1 used for cooling the vapor S 1 in the conditioning valve 1 providing for energy efficient cooling.
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Cleaning By Liquid Or Steam (AREA)
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Description
- The present invention concerns a steam pressure reducing and conditioning system.
- The present description includes common subject matter disclosed in
U.S. Application Serial No. 10/039,343, entitled Steam Pressure Reducing and Conditioning Valve by the same inventor Hiroyuki Higuchi filed concurrently on January 4, 2002, nowU.S. Patent No. 6, 715, 505 . - Referring to Prior Art
Figure 3 , it has been known to have a steam pressure reducing and conditioning system comprising a steam source 24 (such as boiler) for generating superheated steam S, a pressure reducing andconditioning valve 21 for depressurizing and desuperheating steam S generated by thissteam source 24, and adischarge pipe 23 connected to an outlet of steam pressure reducing andconditioning valve 21, and connected to asteam work section 22, downstream ofvalve 21. - As illustrated in Prior Art
Figure 3 , steam pressure andconditioning valve 21 receives superheated and pressurized steam S inflowing ininlet 21a. Steam S is desuperheated and depressurized by passingsteam S valve 21 and injecting subcooled water mist W (not shown) from one ormore nozzles 25 in the lower portion ofvalve 21. - The desuperheated and depressurized steam S1, discharged from the
valve 21 and the subcooled water mist W injected invalve 21, flow into thedischarge pipe 23 and are conveyed to thesteam work section 22. A portion ofdischarge pipe 23 is arranged horizontally 23a. Some of the subcooled water mist W condenses and clings to the discharge pipe at 23a and flows along the bottom of the horizontal section. Steam S1 flows past these areas of condensation creating temperature differentials in the interior surface of thepipe 23. - Consequently, the
pipe 23 deforms (bends upward) and possibly breaks due to expansion and stress due to the temperature difference in horizontal section ofpipe 23, and moreover, the condensed moisture W1, flowing at the bottom of thepipe 23 is enrolled up by the high speed flow of steam S1 (jumping phenomenon). The jumping phenomenon erroneous temperature measurements in temperature sensors in thepipe 23 for detecting the heat of the steam S1. - It is an object of the present invention to provide a steam pressure reducing and conditioning system that can solve the aforementioned problems.
-
GB 772,058 GB 772,058 -
U.S. Patent No. 3,496,724 discloses a desuperheater system and related method which generally correspond to the preamble ofclaims - The disclosed invention will be described with reference to the accompanying drawings, which show important sample embodiments of the invention and which are incorporated in the specification hereof by reference. A more complete understanding of the present invention may be had by reference to the following Detailed Description when taken in conjunction with the accompanying drawings, wherein:
-
Fig. 1 is a partial side view with schematic elements illustrating the operation of the steam pressure reducing and conditioning system of the present invention; -
Fig. 2 is a partial cross-section view illustrating a portion of the pressure reducing and conditioning valve used in the system of the present invention ofFigure 1 ; and -
Fig. 3 is a partial side view with schematic elements illustrating the operation of a prior art steam pressure reducing and conditioning system. - Reference is now made to the Drawings wherein like reference characters denote like or similar parts throughout the Figures.
- The present invention provides a system and method in accordance with the appended claims.
- The present invention concerns a steam pressure reducing and conditioning system comprising a steam reducing and
conditioning valve 1 for desuperheating and depressurizing superheated steam S by injecting subcooled water mist W in the lower portion ofvalve 1. Adischarge pipe 3 is connected at its proximal end to the exit ofvalve 1. Asteam work section 2 is connected at the distal end ofpipe 3. Thedischarge pipe 3 has ahorizontal portion 3a, and saidhorizontal portion 3a is provided with amoisture drain 4 at the bottom portion or at a portion near the bottom of thehorizontal portion 3a ofpipe 3. Condensed subcooled water mist ("moisture") W1 is extracted fromdischarge pipe 23 bydrain 4 and is recycled and reinjected as moisture W to be supplied to the vapor S in saidconditioning valve 1. Moisturedrain 4 is directly connected by amoisture transport conduit 5 to theconditioning valve 1. - The
steam conditioning valve 1 further includes a reducedannular section 9 with anozzle 5a disposed therein for injecting subcooled water mist W into the reducedannular section 9 ofconditioning valve 1. Moisture W is drawn into steam flow S due to the Venturi effect caused by the pressure drop through the reduced annular section. - A superheated steam S is desuperheated by supplying subcooled water mist ("moisture") W to
steam conditioning valve 1. The desuperheated steam S1 flowing out from theconditioning valve 1 and the moisture W used for cooling indischarge valve 1 flows intodischarge pipe 3, and is introduced in thesteam work section 2 connected to the downstream area of thedischarge pipe 3. - In the present invention, when the moisture W discharged from the
conditioning valve 1 flows through thehorizontal section 3a of thedischarge pipe 3, the condensed moisture W1 is drained from amoisture drain 4 disposed at thebottom portion 3a of thispipe 3, and the moisture W1 extracted from themoisture drain 4 is recycled as part of moisture W to be supplied to the steam S in thesteam conditioning valve 1. - Consequently, moisture W1 can be removed from the
horizontal section 3a of thepipe 3, preventing the moisture W1 from stagnating at the bottom of the pipe, solving the aforementioned problem of the prior art discussed in the background section, and further, the recycling of moisture W1 used for cooling the vapor S again in theconditioning valve 1 saves energy. - The attached drawings show an embodiment of the present invention, which will be described below.
- This embodiment of the present invention comprises, as shown in
Figs. 1 and2 , a steam desuperheating andconditioning valve 1 wherein a superheated and pressurized steam S generated in a steam generation source 8 (for instance, boiler) flows into a first port 1a ofconditioning valve 1. Steam S is desuperheated and depressurized by passing through a small hole section 6 (diffuser) having scatteredsmall holes 6a, and the steam S1 is discharged from asecond port 1b ofconditioning valve 1. Steam S1 is desuperheated by injecting a subcooled water mist "moisture" W from one ormore nozzles 7. Adischarge pipe 3 is connected at its proximal end to the exit ofconditioning valve 1, and at its distal end to a steam work section 2 (for instance, condenser for a nuclear reactor). - Also, in this embodiment, the
discharge pipe 3 is provided with ahorizontal section 3a extending from theconditioning valve 1 and disposed horizontally with anelbow section 3b (bent section) . Thedischarge pipe 3 is so composed that the condensed moisture W1 flowing in thishorizontal section 3a is part of the moisture W to be supplied to the vapor S in theconditioning valve 1. - To be more specific, as shown in
Fig. 1 , saiddischarge pipe 3 is provided with amoisture drain 4 having adrain hole 4a at or near the bottom portion of thehorizontal section 3a, saidmoisture drain 4 is provided with amoisture transport conduit 5 for directly conveying moisture W1 extracted from themoisture drain 4 to thevapor cooler 1. - This
moisture transport conduit 5 is a tubular element having a predetermined diameter, and connected to a reducedannular area 9 constituting a predetermined area of theconditioning valve 1, where a steam S1 flowing in the conduit will flow faster than the steam flowing in the largerdiameter discharge pipe 3. - Referring to
Figure 2 , an annular reduceddiameter section 9 is disposed in the lower portion ofconditioning valve 1 at a position near thejet nozzle 7 of theconditioning valve 1. Anozzle 5a of the moisture conduit 5 exits into this reduceddiameter section 9, and it is so configured that the moisture W1 in themoisture conduit 5 is injected into depressurized steam S1 path, in this reduceddiameter section 9. - This reduced
diameter section 9 obtains improved cooling effect by maintaining the steam S1 flow rate immediately passing through the reduceddiameter section 9 faster than the vapor S1 passing through thedischarge pipe 3, thereby reducing the pressure at the position of the reduceddiameter section 9 below the pressure in thedischarge pipe 3. This pressure drop in a reduceddiameter section 9 is due to the increased velocity of a constant flow volume. Such an effect is well known in the art and is referred to as a Venturi effect. Consequently, this embodiment of the present invention allows return of the moisture W1 from thedischarge pipe 3 to theconditioning valve 1 by connecting thenozzle 5a ofmoisture transport conduit 5 to this reduceddiameter section 9, and drawing the moisture W1 from thenozzle 5a into theconditioning valve 1 using the differential pressure generated by the Venturi negative pressure phenomenon. - Considering the optimal conditions for the circulation method using this differential pressure, it is preferable to set this level difference to 10 meters or less, in the case where the
moisture drain 4 is placed lower than thenozzle 5a (no limitation in the case where themoisture drain section 4 is placed higher than thenozzle 5a). - In this embodiment, the vapor S1 differential pressure is used as mentioned before, as a means for recycling the moisture W1 flowing from the
conditioning valve 1 back to theconditioning valve 1. The disposing of a forced delivery apparatus (for instance a pump or the like), in themoisture transport conduit 5 would be outside of and contrary to the scope of the claimed invention. - Composed as described above, this embodiment desuperheats the steam S in the
conditioning valve 1, and the desuperheated and depressurized steam S1 is discharged from theconditioning valve 1 together with moisture W into thedischarge pipe 3. The steam S1 flowing throughdischarge pipe 3 is introduced into thesteam work section 2 connected to the distal end of thedischarge pipe 3. The moisture W1 flowing at the bottom of thedischarge pipe 3 is extracted by themoisture drain 4, transferred by themoisture transport conduit 5 and recycled as moisture W for cooling in thesteam conditioning valve 1. - Therefore, this embodiment provides for an energy efficient removal of the moisture W1 from the
horizontal section 3a of thedischarge pipe 3, thereby preventing the moisture W1 from stagnating at the bottom of thedischarge pipe 3, avoiding as much as possible thepipe 3 deformation (damage) and the detrimental effect to the temperature detection sensor and other problems of the prior art. Additionally, the present invention provides for recycling the moisture W1 used for cooling the vapor S1 in theconditioning valve 1 providing for energy efficient cooling.
Claims (5)
- A steam conditioning system having:a steam conditioning valve (1) for depressurizing and desuperheating superheated inlet steam (S) by supplying a water mist (W) thereto, said valve (1) oriented wherein flow is discharged from said valve (1) through a lower discharge end (1b) oriented in a downward substantially vertical direction, said valve (1) having a reduced annular section (9) having a reduced flow section relative to a flow section of a discharge pipe (3) connected to the lower discharge end of said valve (1), whereby steam (S1) flowing through the reduced annular section of said valve (1) will flow faster than steam (S1) through the discharge pipe (3), thereby creating a pressure drop in the reduced annular section (9) disposed in a lower discharge portion of said valve (1), said pressure drop known as a Venturi effect;said steam conditioning system further comprising:characterized in that:said discharge pipe (3) having:a substantially horizontal section (3a) being provided with a moisture drain (4) in proximity to the bottom of the horizontal section;a substantially vertical section between the lower discharge end of the steam conditioning valve and the horizontal section;a nozzle (5a) for injecting a water mist (W) into the lower discharge portion of said steam conditioning valve (1), wherein said nozzle (5a) has a discharge opening exiting into the reduced annular section (9) of the lower discharge portion of said valve (1); anda transport conduit (5) connecting said nozzle (5a) to said moisture drain (4) for transporting collected condensed water (W1) to said nozzle, wherein the collected condensed water (W1) is drawn from said moisture drain (4) of the discharge pipe (3) through the transport conduit (5) and discharged as a water mist (W) out the nozzle (5a) discharge opening into the lower discharge portion of said steam conditioning valve due to the Venturi effect pressure drop in the reduced annular section (9) of the lower discharge portion of said valve;the transport conduit (5) is configured to directly convey the collected condensed water (W1) from the moisture drain (4) to the nozzle (5a)
- The system of claim 1, wherein:i) the moisture drain (4) is placed at a level which is 10 metres or less lower than a level of the nozzle (5a); orii) the moisture drain (4) is placed at a level which is higher than a level of the nozzle (5a).
- A method of operating a steam pressure reducing and conditioning system, the method comprising:providing a steam conditioning valve (1) having an inlet (1a) and a lower discharge end (1b), the inlet receiving superheated steam (S) from a steam source (8), said steam conditioning valve (1) oriented wherein flow is discharged from said valve through the lower discharge end (1b) oriented in a downward substantially vertical direction, a lower discharge portion of said steam conditioning valve having a reduced annular section (9) with a reduced flow section relative to a flow section of a discharge pipe (3) and having a discharge opening of a nozzle (5a) being disposed in the reduced annular section (9) of the lower discharge portion of the steam conditioning valve, further characterized by:characterized in that:providing the discharge pipe (3) having a proximal end, a distal end, a substantially vertical portion between the ends, and a substantially horizontal portion (3a) between the vertical portion and the distal end, the proximal end being connected to the lower discharge end (1b) of said valve (1) and the distal end supplying steam (S1) to the steam work section (2); andproviding a transport conduit (5) connecting the horizontal portion (3a) of the discharge pipe (3) to the nozzle (5a);receiving in the inlet of said valve (1) superheated steam (S);cooling the superheated steam passing through the lower discharge portion of said valve (1) with the steps of:collecting condensed moisture (W1) in the horizontal portion (3a) of the discharge pipe (3);removing at least a portion of the collected condensed moisture (W1) from the horizontal portion (3a) of the discharge pipe (3) due to a reduced pressure in the reduced annular section (9) in the lower discharge portion (1b) of said valve (1) when steam is flowing through the lower discharge portion of said valve and out through the discharge pipe;transporting the removed collected condensed moisture (W1) through the transport conduit (5) to the discharge opening of the nozzle (5a) due to a reduced pressure in the reduced annular section (9) in the lower discharge portion of said valve (1) when steam (S1) is flowing through the lower discharge portion of said valve and out through the discharge pipe; andinjecting the removed collected condensed moisture (W) through the discharge opening of the nozzle (5a) into the lower discharge portion of said valve (1) to cool the superheated steam (S1) passing therethrough;the transporting the removed collected condensed moisture (W1) through the transport conduit comprises directly conveying the removed collected condensed moisture (W1) from a moisture drain (4) in proximity to the bottom of the horizontal section (3a) to the nozzle (5a).
- The method of Claim 3, comprising:i) placing the moisture drain (4) at a level which is 10 metres or less lower than a level of the nozzle (5a) ; orii) placing said moisture drain (4) at a level which is higher than a level of the nozzle (5a).
- The method of either of Claim 3 or 4, wherein supplying the removed condensed moisture (W1) to the superheated steam (S) passing through said steam conditioning valve (1) is characterized by misting the superheated steam with the removed condensed moisture (W1).
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US39343 | 2002-01-04 | ||
US10/039,343 US6758232B2 (en) | 2000-11-30 | 2002-01-04 | Steam pressure reducing and conditioning system |
Publications (2)
Publication Number | Publication Date |
---|---|
EP1327819A1 EP1327819A1 (en) | 2003-07-16 |
EP1327819B1 true EP1327819B1 (en) | 2015-07-29 |
Family
ID=21904964
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP02007253.4A Expired - Lifetime EP1327819B1 (en) | 2002-01-04 | 2002-03-28 | Steam pressure reducing and conditioning system |
Country Status (2)
Country | Link |
---|---|
EP (1) | EP1327819B1 (en) |
CA (1) | CA2405397C (en) |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR595499A (en) * | 1925-03-20 | 1925-10-03 | Steam saturator by mixing | |
GB772058A (en) * | 1954-08-10 | 1957-04-10 | Alfred Kenneth Porter | De-superheater for steam or other superheated vapour |
US3034771A (en) * | 1958-11-06 | 1962-05-15 | Schutte & Koerting Co | Desuperheater |
US3496724A (en) * | 1967-11-30 | 1970-02-24 | Allis Chalmers Mfg Co | Main steam line desuperheater systems,apparatus and method |
FR2082083A5 (en) * | 1970-03-03 | 1971-12-10 | App Precision Cont | |
US4887431A (en) * | 1989-04-05 | 1989-12-19 | The Babcock & Wilcox Company | Superheater outlet steam temperature control |
-
2002
- 2002-03-28 EP EP02007253.4A patent/EP1327819B1/en not_active Expired - Lifetime
- 2002-09-27 CA CA 2405397 patent/CA2405397C/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
CA2405397C (en) | 2009-08-04 |
EP1327819A1 (en) | 2003-07-16 |
CA2405397A1 (en) | 2003-07-04 |
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