EP0045034A1 - Dispositif pour éviter la formation de fissures sur les faces internes des ajutages d'admission de l'eau d'alimentation dans un récipient sous pression - Google Patents
Dispositif pour éviter la formation de fissures sur les faces internes des ajutages d'admission de l'eau d'alimentation dans un récipient sous pression Download PDFInfo
- Publication number
- EP0045034A1 EP0045034A1 EP81105706A EP81105706A EP0045034A1 EP 0045034 A1 EP0045034 A1 EP 0045034A1 EP 81105706 A EP81105706 A EP 81105706A EP 81105706 A EP81105706 A EP 81105706A EP 0045034 A1 EP0045034 A1 EP 0045034A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- line
- water
- pressure vessel
- feed water
- steam
- 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
- F22B37/228—Headers for distributing feedwater into steam generator vessels; Accessories therefor
Definitions
- the invention relates to a device for avoiding the formation of cracks on the inner surfaces of feed water line nozzles opening into pressure vessels, in particular nuclear reactor pressure vessels or steam generators.
- cooler medium is replenished in a system (container, pipeline) that is filled with an elevated temperature medium, i.e. a feed water pipe socket
- the horizontal connecting piece will be stratified by colder and warmer medium if the Feeding with 'in relation to the size of the connection cross-section low volume throughput, ie low flow rates, takes place.
- the stratification occurs because the lighter (warmer) medium can flow back into the upper part of the flow cross-section of the nozzle due to its buoyancy against the colder water to be fed.
- the respective temperature differences between the two media lead to thermal stresses in the connecting piece or in the connecting line, which as a rule are already highly stressed by the internal pressure of the system, so that material fatigue and thus cracking occur when the supply processes are sufficiently high education can occur.
- the phenomenon of temperature stratification could be demonstrated by temperature measurements on the feed water pipe socket of a steam generator for pressurized water reactors.
- the feeding takes place with horizontal and / or downward flow guidance within the container. Even though the inside of the feed pipe is lined with so-called thermosleeve pipes, the thermal stress problems mentioned at the beginning can still occur in some areas of the pipe.
- the invention has for its object to provide the device of the type mentioned in such a way that with weak feeding of the feed water pipe connection, as occurs in part-load or no-load operation of a system, material fatigue and thus crack formation on the load cycles even under higher load cycles Trim is excluded with certainty.
- the object is achieved by the features listed in the characterizing part of claim 1.
- An advantageous development of the subject matter of claim 1 is described in sub-claim 2.
- the advantages achievable with the invention can be seen above all in the fact that a backflow of the specifically lighter medium in the fed system against the heavier (still cold) medium to be fed in is prevented.
- the invention solves not only the problems of thermal stresses and cracking that occur in particular under no-load and low-load operation, but also the problems that arise during start-up and shutdown operation.
- Fig. 1 (hereinafter abbreviated as DE) has a pressure vessel housing 1 with a primary chamber area 1.1, an evaporator area 1.2 having the U-shaped heat-exchanging tubes 2 and a separator area 1.4 adjoining via a conically widening housing transition area 1.3.
- the tube sheet 3 welded into the housing 1 and the heat exchanger tubes 2 welded into it and held by it separate the primary chamber 1 from the secondary chamber II in a gas-tight manner.
- the primary chamber I is formed by a base cap 4 welded to the tube sheet 3 and having an inlet connection E and an outlet connection A, wherein the inflow space e1 of the primary chamber is separated from the outflow space a1 by an arched partition 5.
- the tubes 2 of the tube bundle 2 ' only the outer and inner are indicated by lines; the pipe bends are marked 2.1, the inner pipe lane is marked 2.2.
- the primary medium (water) heated in the core of the pressurized water reactor (not shown) is supplied to the primary chamber I via the inlet connection E at a temperature of approx the outlet port A is fed back to the reactor pressure vessel at a temperature of approx. 290 ° C.
- the tube bundle from the heat-exchanging tubes 2 is held in a vibration-proof manner by means of axially spaced tube holding grids 6; it is surrounded by a hollow cylindrical jacket 7 which, together with the wall 1, forms an annular fall space 8. Since the jacket 7 is arranged at a distance a2 from the tube sheet 3, the drop chamber 8 is in flow connection at its lower end via the flow passages 8.1 with the evaporation chamber inside the jacket 7.
- the jacket 7 is closed at its upper end by an attachment 9, which carries on its top a battery of water separators 10, into which the water-steam mixture from the evaporation chamber II enters through appropriate flow channels.
- the ejected water, the water level of the circulating water is indicated at 11, is fed directly to the drop room 8.
- the ring line 12 which is arranged at the upper end of the drop space, is used via openings (not shown) for introducing the feed water from a feed water line connection piece 13 via a substantially perpendicular connecting pipeline 14.
- the largely dewatered steam emerging from the water separators 10 on the upper side then passes still in fine separator 15 and from these via the live steam line connector 16 of the steam dome 17 to the steam turbines, not shown.
- the DE works according to the natural circulation principle.
- the feed water and the separated water flow mixed in the fall chamber 8 down into the evaporation chamber-II and rise in this under evaporation (wet steam).
- the water-steam mixture then passes into the coarse separator 10 and then into the fine separator 15, as already explained.
- a very specific flow guide is provided, which is explained in more detail with reference to FIGS. 2 and 3.
- the feed water is introduced into the water-steam space of the DE via an essentially horizontally running line part 140 and a subsequent rising line part 141, which is designed as a pipe bend, up to overflow edges Ü at the end of the flow path of the rising line part 141. From there the feed water, see flow arrows f1, via a downward line piece 142 and the feed ring line 12 connected thereto (FIG. 1) to the water-steam space, ie in this case, the drop room 8 of the DE, mixed.
- the line part 142 is dome-shaped and comprises the line part 141 as a kind of bell.
- the line part 140 can be held in the connection piece 13 (FIG. 1) in the manner of a thermosleeve pipe.
- the rising line part is formed by a trough 141 'which is rectangular in cross section and which is flat and box-shaped, that is to say forms a water tank, on the two narrow side upper edges of which the overflow edges U are arranged.
- This water box 141 ' is surrounded by a likewise box-shaped structure 142, rounded at its upper edge, for the downward line piece, which can also be curved in accordance with the inner circumferential curvature of the pressure vessel, and opens into the ring line 12 at its lower end via a narrowed neck piece 143 .
- thermosleeve pipe can be of a conventional design or configured as shown in FIG. 2 of DE-OS 23 46 411.
- Fig. 8 it is also shown that an essentially horizontally extending line part 140 can be followed by a substantially downwardly extending line part 145, which opens into a collecting cup 141 ", which opens the ascending flow paths up to the overflow edges Ü has.
- a n / D i means the horizontal distance of the pressure vessel inner wall 1i from the center line M ü running through the center of gravity of the cross-sectional area F ü spanned by the overflow edges Ü.
- D i means the inside diameter of the feed water line 140 opening into the pressure vessel DE.
- the stated ratio A n / D i should be as small as possible and is approximately between 0.5 and 2.
- the embodiment according to FIG. 8 shows in connection with FIG. 9 that the ratio A n / D i is in the range of the upper limit value of 2.
- An advantage of this example is the relatively high flow cross cut and to mention the cylindrical symmetrical shape, which latter is also given in the embodiment of FIGS. 2 and 3.
- cylindrical symmetrical forms allow a higher pressure load; box-shaped cross-sections, on the other hand, are lower in compressive strength for a given wall thickness, but the extension in direction A n is lower. 1 to 3, where a relatively low ratio A n / D i of 1.27 is achieved and a relatively high compressive strength with a sufficient flow cross-section are given.
- the other exemplary embodiments can be regarded as special designs in which either the ratio A n / D i is kept particularly low (FIGS. 4 to 7) or the flow cross section in the overflow area is particularly large (FIG. 8).
- the table according to FIG. 9 is based on the cm values for A n and D i , as can be seen from the approximately true-to-scale drawing.
- the pressure vessel of the steam generator DE according to FIG. 1 has an outer diameter of approximately 4800 mm in its separator area 1.4 (steam dome), so that it can be used for enlargement 2 and 3 entered sizes
- a 1 and D i give values of / 500 mm and 400 mm.
- the steam generator shown in FIG. 1 is used, for example, together with three further steam generators in a 4-loop arrangement to generate the working steam in a 1200 MW e i pressurized water nuclear power plant.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE3027630 | 1980-07-21 | ||
DE3027630 | 1980-07-21 |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0045034A1 true EP0045034A1 (fr) | 1982-02-03 |
EP0045034B1 EP0045034B1 (fr) | 1983-04-13 |
Family
ID=6107750
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP81105706A Expired EP0045034B1 (fr) | 1980-07-21 | 1981-07-20 | Dispositif pour éviter la formation de fissures sur les faces internes des ajutages d'admission de l'eau d'alimentation dans un récipient sous pression |
Country Status (5)
Country | Link |
---|---|
US (1) | US4462340A (fr) |
EP (1) | EP0045034B1 (fr) |
JP (1) | JPH0147681B2 (fr) |
ES (1) | ES8704251A1 (fr) |
WO (1) | WO1982000330A1 (fr) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2562639A1 (fr) * | 1984-04-09 | 1985-10-11 | Westinghouse Electric Corp | Systeme d'eau d'alimentation de generateur de vapeur a conduit ouvert |
EP0297968A1 (fr) * | 1987-06-30 | 1989-01-04 | Framatome | Générateur de vapeur à tuyau d'alimentation muni d'un dispositif anti-strtification thermique |
WO1993020386A1 (fr) * | 1992-04-03 | 1993-10-14 | Vítkovice A.S. | Systeme d'alimentation pour echangeur de chaleur |
FR2700383A1 (fr) * | 1993-01-11 | 1994-07-13 | Framatome Sa | Echangeur de chaleur dans lequel l'alimentation en fluide secondaire s'effectue en partie haute par un boîtier d'alimentation ouvert vers le bas. |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
ES2001332A6 (es) * | 1985-07-02 | 1988-05-16 | Framatome Sa | Generador de vapor |
US5698390A (en) * | 1987-11-18 | 1997-12-16 | Chiron Corporation | Hepatitis C immunoassays |
JP2013160695A (ja) * | 2012-02-07 | 2013-08-19 | Mitsubishi Heavy Ind Ltd | 蒸気発生器用給水管 |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2259629A1 (de) * | 1972-12-06 | 1974-06-20 | Gutehoffnungshuette Sterkrade | Dampferzeuger |
DE2346411A1 (de) * | 1973-09-14 | 1975-04-03 | Kraftwerk Union Ag | Dampferzeuger |
DE2600032A1 (de) * | 1975-01-29 | 1976-08-05 | Westinghouse Electric Corp | Dampferzeuger |
FR2425611A1 (fr) * | 1978-05-12 | 1979-12-07 | Commissariat Energie Atomique | Generateur de vapeur surchauffee |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3661123A (en) * | 1970-12-31 | 1972-05-09 | Combustion Eng | Steam generator feedwater preheater |
-
1981
- 1981-07-20 ES ES504105A patent/ES8704251A1/es not_active Expired
- 1981-07-20 EP EP81105706A patent/EP0045034B1/fr not_active Expired
- 1981-07-21 JP JP56502568A patent/JPH0147681B2/ja not_active Expired
- 1981-07-21 WO PCT/EP1981/000103 patent/WO1982000330A1/fr unknown
- 1981-07-21 US US06/359,666 patent/US4462340A/en not_active Expired - Fee Related
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2259629A1 (de) * | 1972-12-06 | 1974-06-20 | Gutehoffnungshuette Sterkrade | Dampferzeuger |
FR2210273A5 (fr) * | 1972-12-06 | 1974-07-05 | Gutehoffnungshuette Sterkrade | |
DE2346411A1 (de) * | 1973-09-14 | 1975-04-03 | Kraftwerk Union Ag | Dampferzeuger |
DE2600032A1 (de) * | 1975-01-29 | 1976-08-05 | Westinghouse Electric Corp | Dampferzeuger |
FR2425611A1 (fr) * | 1978-05-12 | 1979-12-07 | Commissariat Energie Atomique | Generateur de vapeur surchauffee |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2562639A1 (fr) * | 1984-04-09 | 1985-10-11 | Westinghouse Electric Corp | Systeme d'eau d'alimentation de generateur de vapeur a conduit ouvert |
EP0297968A1 (fr) * | 1987-06-30 | 1989-01-04 | Framatome | Générateur de vapeur à tuyau d'alimentation muni d'un dispositif anti-strtification thermique |
FR2617570A1 (fr) * | 1987-06-30 | 1989-01-06 | Framatome Sa | Dispositif anti-stratification thermique pour tuyau d'alimentation de generateur de vapeur |
US4870927A (en) * | 1987-06-30 | 1989-10-03 | Framatome | Device for preventing thermal stratification in a steam generator feed pipe |
WO1993020386A1 (fr) * | 1992-04-03 | 1993-10-14 | Vítkovice A.S. | Systeme d'alimentation pour echangeur de chaleur |
FR2700383A1 (fr) * | 1993-01-11 | 1994-07-13 | Framatome Sa | Echangeur de chaleur dans lequel l'alimentation en fluide secondaire s'effectue en partie haute par un boîtier d'alimentation ouvert vers le bas. |
EP0607071A1 (fr) * | 1993-01-11 | 1994-07-20 | Framatome | Echangeur de chaleur dans lequel l'alimentation en fluide secondaire s'effectue en partie haute par un déversoir |
US5396948A (en) * | 1993-01-11 | 1995-03-14 | Framatome | Heat exchanger, in which the supply of secondary fluid takes place in the upper part by means of an overflow |
Also Published As
Publication number | Publication date |
---|---|
JPH0147681B2 (fr) | 1989-10-16 |
EP0045034B1 (fr) | 1983-04-13 |
WO1982000330A1 (fr) | 1982-02-04 |
JPS57501143A (fr) | 1982-07-01 |
ES504105A0 (es) | 1987-03-16 |
US4462340A (en) | 1984-07-31 |
ES8704251A1 (es) | 1987-03-16 |
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