EP0250319B1 - Dampferzeuger mit verbesserten Trocknungsmitteln - Google Patents
Dampferzeuger mit verbesserten Trocknungsmitteln Download PDFInfo
- Publication number
- EP0250319B1 EP0250319B1 EP19870401361 EP87401361A EP0250319B1 EP 0250319 B1 EP0250319 B1 EP 0250319B1 EP 19870401361 EP19870401361 EP 19870401361 EP 87401361 A EP87401361 A EP 87401361A EP 0250319 B1 EP0250319 B1 EP 0250319B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- elementary
- dryers
- steam
- layers
- dryer
- 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
Links
- 238000001035 drying Methods 0.000 title claims description 21
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 49
- 238000004519 manufacturing process Methods 0.000 claims description 8
- 230000002093 peripheral effect Effects 0.000 claims description 7
- 230000000149 penetrating effect Effects 0.000 claims description 3
- 239000012530 fluid Substances 0.000 description 9
- 230000005484 gravity Effects 0.000 description 5
- 238000000926 separation method Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 238000009835 boiling Methods 0.000 description 2
- 230000001174 ascending effect Effects 0.000 description 1
- 230000002301 combined effect Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000004992 fission Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 230000000284 resting effect Effects 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
Images
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
- F22B37/26—Steam-separating arrangements
- F22B37/28—Steam-separating arrangements involving reversal of direction of flow
- F22B37/286—Steam-separating arrangements involving reversal of direction of flow specially adapted for steam generators of nuclear power plants
Definitions
- the present invention relates to a steam generator equipped with drying means of a new type, with increased efficiency.
- the steam used to drive the turbines of the electric generator is created in a steam generator.
- steam generator designates here any component in which water penetrating in the liquid state emerges in the vapor state under the effect of its heating.
- a component can therefore be a heat exchanger in which a primary fluid, heated for example in the core of a nuclear reactor, in turn heats the water in the secondary circuit. It can also be the main tank of a boiling water nuclear reactor, in which the water heats up directly by passing through the reactor core.
- the separators are constituted by juxtaposed vertical tubes, in which are placed helical fins centrifuging the water-vapor mixture, and allowing thus to separate most of the water entrained by the vapor.
- the steam always charged with humidity leaving through the upper end of the tubes passes through then the drying device, consisting of chicane passages formed between lamellae in the form of rafters.
- the shape of the baffles is such that a part of the water droplets entrained by the vapor is separated from the latter and descends towards the steam production zone.
- the poor efficiency of this drying device is mainly explained by the fact that the separation of the water droplets is obtained by circulating the steam horizontally inside the baffles.
- the force of inertia due to the change in curvature and the force of gravity, which act simultaneously on each water droplet are therefore directed in two different directions, approximately perpendicular.
- the modulus of the resultant of these two forces, which determines the separating power of the device is therefore much lower than the sum of the modules of these two forces, which corresponds to the maximum theoretical separating power.
- the water droplets are not immediately withdrawn from the action of the surrounding vapor, so that part of them can be again entrained by the vapor.
- the effectiveness of the device is also limited by this phenomenon.
- drying means intended for a steam generator, consisting of elementary dryers arranged in several layers superposed according to a regular network offset from one layer to another.
- Each elementary dryer is formed by two curved plates forming an upper part flared upwards and a central part separated by a clearance from the edges of the upper parts of the adjacent elementary dryers of the immediately lower layer. Drainage channels are placed below the dryer layers.
- the invention specifically relates to a steam generator equipped with improved dryers in which the separation of the water droplets is obtained by subjecting the steam to successive changes of direction at 180 ° and by circulating the steam from bottom to top , so that the force of gravity acting on each water droplet is added to the force of inertia due to the change of direction, to give the separation maximum efficiency.
- the invention also relates to a steam generator, the dryers of which are designed so as to immediately remove the water droplets from the action of steam.
- the drying means comprise juxtaposed interchangeable baskets, each containing several layers of elementary dryers.
- the interchangeable baskets then have a horizontal hexagonal section.
- the separation means comprising in known manner helical fins arranged in vertical tubes, the interchangeable baskets also contain elementary drainage channels and extend downward so as to surround and support the upper end of one of the tubes, delimiting therewith an annular space for the return of water, into which the elementary drainage channels open.
- This steam generator is intended in particular to be used for ensuring the exchange of heat between a primary fluid previously heated in a nuclear reactor and a secondary fluid consisting of water.
- the invention is not limited to this type of steam generator and also covers the case where the primary fluid is removed, the heat source constituted for example by the core of a reactor with boiling water being placed directly inside the outer casing of the steam generator, which then constitutes the main tank of the reactor.
- the steam generator shown in Figure 1 conventionally comprises an outer casing 10 having a symmetry of revolution about a vertical axis.
- a bundle of inverted U-shaped tubes 12 In the lower part of the enclosed volume delimited by the envelope 10 is housed a bundle of inverted U-shaped tubes 12, the ends of which are fixed in a sealed manner on a horizontal tube plate 14, itself fixed in a sealed manner to the envelope 10 near the hemispherical bottom 10a thereof.
- the ends of the tubes 12 open respectively into an inlet chamber 16 and into an outlet chamber 18 of primary fluid, these two chambers being formed between the tube plate 14 and the hemispherical bottom 10a, and separated by a partition 20.
- the entry of the primary fluid into the chamber 16 and the exit of this fluid from the chamber 18 are done respectively by an inlet pipe 22 and by an outlet pipe 24 formed in the bottom 10a of the envelope.
- Tubing 22 and 24 are designed to be connected to an external circuit in which there is for example a tank containing the core of a nuclear reactor.
- the relatively hot primary fluid entering the chamber 16 circulates in the bundle of tubes 12 before being evacuated by the outlet chamber 18.
- the bundle of tubes 12 therefore constitutes inside the outer envelope 10 a source of heat used to vaporize the water in the secondary circuit.
- the admission of the water from the secondary circuit in the liquid state to the inside of the envelope 10 of the steam generator is done by an inlet pipe 26 located immediately above the tube plate 14.
- L water in the liquid state penetrating through the tubing 26 travels from bottom to top around the tubes 12, taking part of the heat of the water conveyed by the primary fluid circulating in these tubes.
- the bundle of tubes 12 thus constitutes a zone for producing steam.
- the vapor thus formed then circulates successively from bottom to top in a separating device 28, then in a drying device 30, before escaping at the upper end of the casing 10 by a steam outlet pipe 32.
- a water / steam circuit comprising in particular a turbo-alternator assembly producing the desired electrical energy.
- the bundle of tubes 12 is housed in a cylindrical inner envelope 34 defining with the outer envelope 10 an annular space 36.
- the separator device 28 comprises vertical tubes 38 connected directly to the upper part of the inner envelope 34. Inside the tubes 38, part of the water droplets is separated from the vapor by helical fins . The water thus separated from the steam returns directly to the steam production zone delimited by the inner envelope 34.
- the drying device 30 mainly comprises several horizontal layers of elementary dryers 40, the elemental dryers of each layer being arranged in a regular network, preferably with triangular or square meshes.
- the elementary dryers are offset so that the dryers of a given layer are vertical to the center of the mesh of the dryers of the two immediately adjacent layers.
- the elementary dryers of the successive layers are nested one inside the other, as clearly shown in FIG. 2.
- each of the elementary dryers 40 has approximately the shape of a funnel with a vertical axis.
- each elementary dryer 40 comprises an upper portion 40a approximately frustoconical, an outer peripheral edge 40b facing downwards and a central portion 40c approximately tubular.
- the upper part 40a very flared, drains on its upper face the water droplets towards the central part 40c, which borders it internally.
- the lower face of the part 40a extended externally by the edge 40b, forces the current of steam rising in the steam generator to effect a change of direction at 180 °.
- the length of the central tubular part 40c of each elementary separator 40 is such that its lower end penetrates into the upper end of the corresponding part 40c of the elementary dryer 40 with which it is vertically aligned, two layers below. To this end, the diameter of the part 40c gradually decreases downward, so as to leave a clearance between the lower end of the part. 40c of a given elementary dryer and the upper end of the part 40c of the dryer into which this lower end penetrates.
- This game makes it possible to drain the drops of water collected by the parts 40c, as illustrated by the arrows F1 in FIG. 2.
- each of the elemental dryers 40 and the size of the meshes according to which these dryers are arranged in each of the layers are such that there is also a certain clearance between the tubular part 40c of each elementary dryer and the peripheral edge. outside 40b of the elementary dryers of the immediately lower layer.
- the length of the outer peripheral edge 40b of the elementary dryers is such that there is also a clearance between the lower end of these edges and the parts 40a of the elementary dryers of the layer of dryers situated immediately below.
- this result is obtained by simply resting by gravity the elementary dryers of a given layer on the dryers of the adjacent lower layer, by virtue of the approximately frustoconical character of the parts 40a.
- the water vapor coming from the separator assembly 28 and flowing from bottom to top undergoes a change of direction approximately 180 ° each time it strikes the upper part 40a extended by the edge 40b d 'an elementary dryer.
- the slightly flared shape of the part 40a deflects the vapor radially outwards relative to the vertical axis of the corresponding elementary dryer, towards the inverted edge 40b. The latter then forces the vapor to descend before resuming its upward path to the elemental dryers of the upper layer.
- the water droplets separated from the vapor by each of the elementary dryers 40 fall on the upper part 40a of the elementary dryers of the adjacent lower layer by subtracting the separated water droplets steam entrainment.
- the water separated from the steam is then conveyed by the tubular central parts 40c of the elementary dryers to drainage channels 42 extending horizontally over the entire width of the steam generator (FIG. 1) and into which the lower ends penetrate. tubular parts 40c of the elemental dryers forming the two lower layers of the stack.
- the drainage channels 42 are fitted with pipes 44 (FIG. 1) making it possible to convey the water thus drained to above the annular space 36 delimited between the envelopes 34 and 10.
- the separated water steam thus descends to the lower part of the steam generator to be mixed with the feed water entering through the pipe 26.
- each of the drainage channels 42 is inclined radially towards the outside of the exchanger to facilitate the flow of water to the pipes 44 forming the return passages. water to the steam generator area.
- the drying assembly 30 can consist of interchangeable modular baskets 46 in each of which is housed a certain number of elementary dryers 40.
- the baskets 46 preferably have a hexagonal shape in horizontal section.
- the drainage channels 42 remain fixedly mounted inside the casing 10 of the generator.
- each of the interchangeable modular baskets comprises both a stack of several layers of elementary dryers 40, a set of elementary drainage channels 42 and a tube 38 of the separator device 28.
- the dryers 40 are here again housed in a basket 46 having a horizontal hexagonal section, this basket extending downward so that there are housed drainage channels 42 of reduced length ( Figure 5) , as well as the upper end of one of the tubes 38.
- the diameter of the tube 38 is such that it fits entirely inside the lower part of the basket 46, delimiting therewith an annular space 44a in which the ends of the drainage channels 42 open out through holes 42a.
- This annular space 44a then constitutes the return passage of the water towards the steam production zone and thus replaces the pipes 44 of FIG. 1.
- each of the tubes 38 is fixed to the corresponding basket 46, so that the removal of the latter makes it possible to maintain the dryers and the corresponding separator.
- the particular shape of the elementary dryers 40 described above should not be considered as limiting, the only double condition that must meet these dryers being to ensure a return to about 180 ° of the ascending steam flow as well as a return of the water separated from the steam in the drainage channels 42.
- the upper part 40a of the elementary dryers can have a circular arc section allowing the tubular part 40c to be connected to the peripheral edge 40b.
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Drying Of Solid Materials (AREA)
Claims (4)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR8608804A FR2600403B1 (fr) | 1986-06-18 | 1986-06-18 | Generateur de vapeur a moyens de sechage perfectionnes |
FR8608804 | 1986-06-18 |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0250319A1 EP0250319A1 (de) | 1987-12-23 |
EP0250319B1 true EP0250319B1 (de) | 1991-02-20 |
Family
ID=9336456
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP19870401361 Expired - Lifetime EP0250319B1 (de) | 1986-06-18 | 1987-06-17 | Dampferzeuger mit verbesserten Trocknungsmitteln |
Country Status (3)
Country | Link |
---|---|
EP (1) | EP0250319B1 (de) |
DE (1) | DE3768054D1 (de) |
FR (1) | FR2600403B1 (de) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112054416B (zh) * | 2020-09-03 | 2022-03-01 | 福建腾力电力发展有限公司 | 正压空间开关柜 |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2004498A1 (de) * | 1970-01-31 | 1971-08-05 | Licentia Gmbh | Abscheider |
FR2507742A1 (fr) * | 1981-06-16 | 1982-12-17 | Commissariat Energie Atomique | Generateur de vapeur muni d'un dispositif de purge dynamique |
-
1986
- 1986-06-18 FR FR8608804A patent/FR2600403B1/fr not_active Expired
-
1987
- 1987-06-17 DE DE8787401361T patent/DE3768054D1/de not_active Expired - Lifetime
- 1987-06-17 EP EP19870401361 patent/EP0250319B1/de not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
EP0250319A1 (de) | 1987-12-23 |
DE3768054D1 (de) | 1991-03-28 |
FR2600403A1 (fr) | 1987-12-24 |
FR2600403B1 (fr) | 1988-08-26 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CA1260410A (fr) | Separateur de melanges par centrifugation | |
EP0067739B1 (de) | Verfahren und Vorrichtung zum Entfernen von Schlamm von der Oberfläche des Rohrbodens eines Dampferzeugers | |
EP0246151B1 (de) | Abscheider mit Flügelflächen zur Abscheidung von Flüssigkeitsteilchen | |
EP0068913B1 (de) | Schneller Brüter mit Einrichtung zur Abführung von Restwärme | |
EP0176420B1 (de) | Vorrichtung zur Abtrennung von Wasser und Dampf zur Trocknung eines feuchten Dampfes | |
EP0250319B1 (de) | Dampferzeuger mit verbesserten Trocknungsmitteln | |
EP0389361B1 (de) | Dampferzeuger mit Vorwärmung | |
FR2616883A1 (fr) | Bac d'epuration d'eau de generateur de vapeur | |
CH628969A5 (fr) | Generateur de vapeur comprenant un dispositif d'evacuation des contaminants du fluide de chauffe du generateur de vapeur. | |
EP0043760B1 (de) | Dampftrockneranlage für Dampferzeuger, insbesondere für Kernreaktor-Dampferzeuger | |
EP0607071B1 (de) | Wärmetauscher mit oben durch einen Überlauf gespeistes Sekundärfluid | |
EP0634607A1 (de) | Dampferzeuger mit abnehmbarem Zyklonabscheidersystem | |
EP0032088B1 (de) | Vorrichtung zum Trennen von Flüssigkeit und Dampf aus einem Fluid-Strom und Dampferzeuger mit solchen Vorrichtungen | |
EP0566477B1 (de) | Dampferzeuger mit einer Wasserablenkungvorrichtung und einer Schlammentleerungsbahn | |
EP0568434B1 (de) | Vorrichtung zur Abgabe und Verteilung von Speise- und Rezirkulationswasser in der Sekundärseite eines Dampferzeugers | |
EP0002235B1 (de) | Senkrechter Abscheider für eine Dampfflüssigkeitsmischung | |
FR2597577A1 (fr) | Echangeur de chaleur pour generateur de vapeur, notamment de centrale nucleaire | |
FR2480905A1 (fr) | Dispositif de separation d'eau et de vapeur a la sortie d'enceinte de vaporisation d'un generateur de vapeur | |
FR2593718A1 (fr) | Evaporateur a film descendant | |
EP0005225A1 (de) | Einrichtung zum Trocknen und Überhitzen von Dampf | |
FR2561123A3 (fr) | Evaporateur a cascade | |
CH384590A (fr) | Générateur de vapeur vertical | |
FR2541441A1 (fr) | Dispositif de degazage de condensats installe dans un puits de condenseur de centrale electrique | |
BE566747A (de) | ||
EP0557173A1 (de) | Dampferzeuger mit Speisewasserzuführungsleitung im niedrigen Teil |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): BE CH DE GB IT LI NL |
|
17P | Request for examination filed |
Effective date: 19880530 |
|
17Q | First examination report despatched |
Effective date: 19900115 |
|
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): BE CH DE GB IT LI NL |
|
REF | Corresponds to: |
Ref document number: 3768054 Country of ref document: DE Date of ref document: 19910328 |
|
ITF | It: translation for a ep patent filed | ||
GBT | Gb: translation of ep patent filed (gb section 77(6)(a)/1977) | ||
PLBE | No opposition filed within time limit |
Free format text: ORIGINAL CODE: 0009261 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT |
|
26N | No opposition filed | ||
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: DE Payment date: 19920526 Year of fee payment: 6 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: GB Payment date: 19920609 Year of fee payment: 6 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: BE Payment date: 19920618 Year of fee payment: 6 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: NL Payment date: 19920630 Year of fee payment: 6 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: CH Payment date: 19920702 Year of fee payment: 6 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: GB Effective date: 19930617 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: LI Effective date: 19930630 Ref country code: CH Effective date: 19930630 Ref country code: BE Effective date: 19930630 |
|
BERE | Be: lapsed |
Owner name: COMMISSARIAT A L'ENERGIE ATOMIQUE ETABLISSEMENT D Effective date: 19930630 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: NL Effective date: 19940101 |
|
GBPC | Gb: european patent ceased through non-payment of renewal fee |
Effective date: 19930617 |
|
NLV4 | Nl: lapsed or anulled due to non-payment of the annual fee | ||
REG | Reference to a national code |
Ref country code: CH Ref legal event code: PL |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: DE Effective date: 19940301 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IT Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20050617 |