Classifications

• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F28—HEAT EXCHANGE IN GENERAL
  • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
  • F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
  • F28D7/0066—Multi-circuit heat-exchangers, e.g. integrating different heat exchange sections in the same unit or heat-exchangers for more than two fluids
  • F28D7/0083—Multi-circuit heat-exchangers, e.g. integrating different heat exchange sections in the same unit or heat-exchangers for more than two fluids with units having particular arrangement relative to a supplementary heat exchange medium, e.g. with interleaved units or with adjacent units arranged in common flow of supplementary heat exchange medium
• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F28—HEAT EXCHANGE IN GENERAL
  • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
  • F28D9/00—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
  • F28D9/0006—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the plate-like or laminated conduits being enclosed within a pressure vessel
• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F28—HEAT EXCHANGE IN GENERAL
  • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
  • F28D9/00—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
  • F28D9/0093—Multi-circuit heat-exchangers, e.g. integrating different heat exchange sections in the same unit or heat-exchangers for more than two fluids
• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F28—HEAT EXCHANGE IN GENERAL
  • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
  • F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
  • F28F9/007—Auxiliary supports for elements
  • F28F9/0075—Supports for plates or plate assemblies
• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F28—HEAT EXCHANGE IN GENERAL
  • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
  • F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
  • F28F9/02—Header boxes; End plates
  • F28F9/026—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits
  • F28F9/027—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits in the form of distribution pipes
• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F28—HEAT EXCHANGE IN GENERAL
  • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
  • F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
  • F28F9/02—Header boxes; End plates
  • F28F9/026—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits
  • F28F9/027—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits in the form of distribution pipes
  • F28F9/0275—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits in the form of distribution pipes with multiple branch pipes
• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F28—HEAT EXCHANGE IN GENERAL
  • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
  • F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
  • F28F9/26—Arrangements for connecting different sections of heat-exchange elements, e.g. of radiators
• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F28—HEAT EXCHANGE IN GENERAL
  • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
  • F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
  • F28D2021/0019—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
  • F28D2021/0054—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for nuclear applications

Definitions

• the present invention relates to the exchange of heat between two fluids.
• the invention relates more particularly to the realization of a new type of compact heat exchanger and high thermal power.
• the invention thus relates to a heat exchanger integrating one or more plate type heat exchanger modules in a pressure shell.
• the main use of the exchanger between two fluids according to the invention is its use with liquid metal and gas.
• This may advantageously be liquid sodium and nitrogen.
• the main application targeted by the exchanger according to the invention is the exchange of heat between a liquid metal, such as liquid sodium, of the secondary loop and nitrogen as a gas of the tertiary loop of a reactor.
• a liquid metal such as liquid sodium
• fast neutrons cooled with the liquid metal such as liquid sodium called RNR-Na or SFR (acronym for "Sodium Fast Reactor") and which is part of the family of so-called fourth generation reactors.
• a heat exchanger according to the invention can also be implemented in any other application requiring exchange between two fluids, such as a liquid and a gas, preferably when it is necessary. to have a compact exchanger and high thermal power.
• primary fluid means the usual thermal meaning, namely the hot fluid which transfers its heat to the secondary fluid which is the cold fluid,
• secondary fluid in the context of the invention, the usual thermal sense, namely the cold fluid to which is transferred the heat of the primary fluid.
• the primary fluid is the sodium that circulates in the so-called secondary loop of the thermal conversion cycle of a reactor RNR-Na, while the secondary fluid is the nitrogen that circulates in the tertiary loop of said cycle.
• the heat exchangers have significant advantages over heat exchangers, known as tube heat exchangers, in particular their thermal performance and their compactness thanks to a ratio of the surface area to the heat exchange volume favorably. Student. Compact plate heat exchangers are used in many industrial fields.
• the known tube exchangers are, for example, tube and shell exchangers, in which a bundle of straight or bent tubes. U-shaped or helically shaped is fixed on drilled plates and disposed inside a sealed enclosure called calender. In these tube and shell exchangers, one of the fluids circulates inside the tubes while the other fluid circulates inside the shell. These tube and shell exchangers have a large volume and are therefore of low compactness.
• AREVA has proposed, in the framework of studies carried out on high- or high-temperature gas reactors, called HTR or VHTR (for "High Temperature Reactor” or “Very High Temperature Reactor”), a design solution. in a calender of a series of plate heat exchanger modules by pooling a portion of the fluid supply and distribution manifolds.
• This solution for example described in patent FR 2887618, is advantageous insofar as the unit heat power of the exchanger can be increased by increasing the number of heat exchanger modules in series.
• the radial orientation of the exchanger modules and the relative arrangement of the collectors with respect to the sealed enclosure forming the shell limit the use of a heat exchanger to an exchange between gas and gas because, a liquid is not possible and, on the other hand do not allow to have a really compact exchanger.
• the volume occupied by the structures (sealed enclosure, support, etc.) and the collectors is much greater than the intrinsic volume of the exchanger modules.
• the inventors of the present invention were faced with the need to find a heat exchanger between a liquid metal, such as liquid sodium, and a gas, with the need to be able to perform a gravity drain of the liquid metal circuit and thus an elimination of the retention zones in this circuit.
• FIGS. 1 to 1C show the views of the heat exchanger as disclosed in this publication [1],
• the heat exchanger 1 is intended to transfer heat between a first fluid, which is nitrogen (N 2 ) (cold fluid) and a second fluid which is liquid sodium (Na).
• a first fluid which is nitrogen (N 2 ) (cold fluid)
• a second fluid which is liquid sodium (Na).
• FIGS. 1 to 1C also show the characteristic temperatures and pressures of nitrogen and sodium, respectively, as they are provided at their inlet and at their exit from exchanger 1.
• the pressure of 180 bars is that of nitrogen and therefore, that prevailing inside the sealed enclosure 2.
• the heat exchanger 1 of the central axis X 2 comprises a sealed enclosure in which is housed a plurality of 3 exchanger modules 3.1, 3.2, 3.3, 3.4, arranged vertically and parallel to the axis X. As best illustrated in Figure 1A. the number of identical exchanger modules is equal to four.
• the sealed enclosure 2 is of substantially cylindrical general shape and consists essentially of a cover 20 assembled with a bottom 21. The cover 20 has no opening.
• the sealed enclosure 2 comprises at one of its longitudinal ends, both an inlet 10 and an outlet 11 of the nitrogen and an inlet 12 and an outlet 13 of the liquid sodium.
• Each exchanger module 3.1, 3.2, 3.3, 3.4 integrates two fluid circuits including one dedicated to the circulation of sodium (Na) from a nuclear reactor RN11-Na. as the primary fluid of the exchanger module, and the other dedicated to the circulation of nitrogen (N2) as a secondary fluid.
• Na sodium
• N2 nitrogen
• the plurality of exchanger modules 3.1, 3.2, 3.3, 3.4 is supported by a support structure 4.
• the support structure 4 is flexibly fixed in the sealed enclosure 2.
• the exchanger modules 3.1, 3.2, 3.3, 3.4 are placed on a perforated support plate 40 which is suspended in the chamber 2 by means of flexible arms 40a, 40b, 40c ( Figure 1C).
• a nitrogen inlet chamber 5 is formed axially on the top of the chamber 2, at its upper longitudinal end 2b, between the exchanger modules 3.1. to 3.4 and the cover 20 of the enclosure 2.
• this chamber 5 communicates with each unrepresented input of the integrated nitrogen circuit in one of the exchanger modules 3.1 to 3.4.
• a first central collector 6 is arranged axially around the central axis (X). This first central collector 6 has the function of recovering the hot nitrogen to which the heat of the sodium has been transferred in the exchanger modules 3.1 to 3.4.
• This central collector 6 therefore communicates upstream with each unrepresented output of the integrated nitrogen circuit in one of the exchanger modules 3.1 to 3.4. Downstream, this central collector 6 communicates with the outlet 11 of the nitrogen of the enclosure 2.
• annular collector 7 is arranged around the central collector 6 and exchanger modules 3.1 to 3.4 forming a nitrogen guide space.
• This annular collector 7 serves to bring the cold nitrogen into the chamber 5. More precisely, this annular manifold 7 consists essentially of a flared deflector 70 and a cylindrical shell 71.
• the nitrogen guiding space is delimited from upstream to downstream, at the outside by the chamber 2 and inside, by the first central collector 6 and then by the deflector 70 and the shell 71.
• the annular collector 7 is arranged coaxially around the first central collector 6.
• the annular collector 7 thus communicates upstream with the inlet 10 of the nitrogen of the enclosure 2 and downstream with the chamber 5.
• a plurality 8 of inlet pipes 81, 82, 83, 84 is arranged to bring the hot sodium into each of the unrepresented inputs of the sodium circuit integrated in one of the exchanger modules 3.1 to 3.4.
• each inlet pipe 81 to 84 communicates upstream with the inlet 12 of the sodium of the enclosure 2, and downstream with each inlet 31 to 34 of the sodium circuit integrated in one of the exchanger modules 3.1 to 3.4 .
• each inlet 31 to 34 is made on a lateral side of the underside of a module 3.1 to 3.4: the plurality 8 of inlet pipes 81 to 84 is thus curved in order to be able to reach these entrances lateral 31 to 34.
• a plurality 9 of outlet pipes 91, 92, 93, 94 are arranged to extract the cold sodium from each of the outlets. integrated sodium circuit in one of the exchanger modules 3.1 to 3.4.
• each outlet pipe 91 to 94 communicates upstream with an output of the sodium circuit integrated in one of the exchanger modules 3.1 to 3.4 and downstream with the outlet 13 of the sodium of the enclosure 2.
• the outlet 13 of the sodium cold takes place laterally and upwards of the enclosure 2.
• each sodium outlet is produced on a lateral side of the top of a module 3.1 to 3.4: the plurality of outlet pipes 91 to 94 is thus curved in order to be able to emerge on these lateral outlets.
• the plurality of pipes 8 input 81-84 communicates with a second central manifold 14 which thus causes the hot liquid sodium through the inlet 12 of the enclosure 2.
• the first manifold central 6 is coaxial with the second central collector 14 and disposed between the annular collector 7 and the second central collector 14.
• the cold nitrogen arrives, at a temperature of the order of 330 ° C. and at a pressure of the order of 180 bar, through the inlet 10 and is then fed through the annular manifold 7 at the top of the enclosure 2 and is redirected to, the. inlet chamber 5 by the cover 20, as illustrated by the rising and descending side arrows in FIG.
• the nitrogen then flows through the heat exchanger modules 3.1 to 3.4 in which heat from the hot sodium is transferred thereto.
• the nitrogen which has become hot at a temperature of the order of 515 ° C., emerges from the modules 3.1 to 3.4 and is extracted from the enclosure through the outlet 11 via the first central collector 6.
• the hot sodium is brought, at a temperature of the order of 530 ° C, by the second central collector 14 through the inlet 12 and is distributed in each exchanger module 3.1 to 3.4 by the pipes 81 to 84.
• the hot sodium then passes through the heat exchanger modules 3.1 to 3.4 in which it transfers its heat to the nitrogen.
• the heat exchanger 1 which has just been described has the advantages of being able to be of high unit thermal power and of being compact.
• the arrangement of the exchanger modules 3.1 to 3.4, the plurality of inlet and outlet pipes 9 and the second central manifold 14 allows gravity drainage of sodium but only hot sodium. Indeed, with regard to cold sodium, given the curved shape of the outlet pipes, it is very likely that there is a retention of cold sodium.
• this heat exchanger presents as a major disadvantage that the distribution of the fluids can be difficult to guarantee in an industrial way taking into account the temperature levels required for the operation.
• it is first necessary to ensure the perfect sliding seal between the supply manifold 14 of the sodium and the output manifold 6 of the nitrogen which is coaxial, with the aid of a bellows 15.
• the hot nitrogen coming out of the modules Exchanger 3.1 to 3.4 is recovered by the deflector 70, as shown by the downward curved arrows, which therefore thermally urges the suspended support structure 4, 40 of the exchanger modules 3.1 to 3.4.
• the support part itself 40 must also seal between the hot nitrogen present in the chamber 5 and the cold nitrogen recovered downstream.
• it is necessary to ensure both the good mechanical and thermal strength of the flexibility of the arms 40a to 40c and good flexibility in the inlet pipes 81 to 84 of the sodium passing through the support 40 by means of metal bellows 16 .
• the object of the invention is to at least partially meet this need.
• the subject of the invention is a heat exchanger between a first and a second fluid, comprising:
• a étanehe enclosure having a central axis and comprising, at one of its longitudinal ends, at least one inlet and an outlet of the first fluid and, at the other of its longitudinal ends, at least one inlet and one outlet of the second fluid, the sealed enclosure being adapted to be pressurized,
• At least one heat exchanger module integrating a first and second fluid circuit, extending parallel to the central axis and arranged inside the enclosure,
• first fluid formed axially between the support and the enclosure, and communicating with one of the inlet and the outlet of the first fluid circuit,
• a first central collector extending around the central axis, arranged axially opposite the chamber and communicating on the one hand with one of the inlet and the outlet of the first fluid of the enclosure; and on the other hand with the other of the inlet and the outlet of the first fluid circuit.
• an annular collector arranged around the first central collector and the at least one exchanger module, to the support, by forming a guiding space for the first fluid and communicating on the one hand with the other of the inlet and of the output of the first fluid of the enclosure and secondly with the chamber,
• At least one inlet pipe communicating on the one hand with the inlet of the second fluid of the enclosure, and on the other hand with the inlet of the second fluid circuit,
• At least one outlet pipe communicating on the one hand with the outlet of the second fluid of the enclosure, and on the other hand with the outlet of the second fluid circuit, the pipes being not supported by the support structure and keeping.
• collector means here and in the context of the invention a device for dispensing or collecting a fluid, respectively to or from one or more channels.
• piping is meant here and in the context of the invention, a conduit for dispensing or collecting a fluid to and from a single channel.
• the support structure does not serve to support the pipes and that it receives no mechanical stress or adverse thermal stress through the pipes.
• the pipes are arranged at a distance from the support and holding structure.
• the pipes and the supporting and holding structure are mechanically and thermally decoupled from each other.
• the invention consists first and foremost in defining an exchange structure of heat which makes it possible to bring and recover the primary fluid, such as sodium, at the same longitudinal end and away from the longitudinal end through which the secondary fluid, such as nitrogen, is fed and recovered.
• the primary fluid such as sodium
• the secondary fluid such as nitrogen
• the invention consists in rigidly fixing the support structure of the exchanger modules to the sealed enclosure and in bringing the coldest fluid (secondary fluid) to the support side. Thanks to this, the support structure is subjected to relatively low temperatures, and therefore it is less thermally constrained.
• the heat exchanger allows the gravity draining of the primary fluid from the bottom of the sealed enclosure, away from the first central manifold through which the secondary fluid, which is disposed in the upper part of the sealed enclosure, is extracted.
• a compact heat exchanger with a high unit thermal power is obtained for a liquid-gas metal exchange and whose industrial production can be guaranteed easily and reliably.
• the heat exchanger comprises:
• the unit thermal power of such an exchanger is high.
• the plurality of inlet pipes communicates with a second central collector.
• the plurality of outlet pipes communicates with a third central collector.
• the third central collector is arranged coaxially around the second central collector.
• the inlet of the first and / or second fluid circuit of each exchanger module is arranged at a longitudinal end of each module.
• the output of the first and / or the second fluid circuit being arranged at a longitudinal end of each module.
• the inlet of the first fluid circuit and the outlet of the second fluid circuit of each exchanger module being arranged at the same longitudinal end and the inlet of the second fluid circuit and the outlet of the first fluid circuit of each exchanger module being arranged at the same opposite longitudinal end.
• the invention also relates, in another of its aspects, to a method of operating the heat exchanger which has just been described, the sealed chamber being arranged substantially vertically with the inlet and the outlet of the first fluid. top and the inlet and the outlet of the second fluid at the bottom.
• the invention also relates to the use of the heat exchanger which has just been described, the first fluid being a secondary fluid being a gas or a mixture of gases and the second fluid as the primary fluid being a liquid metal.
• the first fluid mainly comprises nitrogen and the second fluid is liquid sodium.
• the first or the second fluid can come from a nuclear reactor.
• the invention relates to a nuclear installation comprising a fast neutron nuclear reactor cooled with liquid metal, especially liquid sodium said RNR-Na or SFR and a heat exchanger described above.
• FIG. 1 is a longitudinal sectional view and perspective of a heat exchanger according to the state of the art
• FIG. 1A is a perspective view and cut away of the heat exchanger according to Figure 1;
• FIGS. 1B and 1C are detailed views of a heat exchanger according to FIG.
• FIG. 2 is a perspective and cutaway view of a heat exchanger according to the invention.
• FIG. 2A is a perspective and cutaway view of the upper part of a heat exchanger according to FIG. 2;
• FIG. 2B is a perspective and cut away view of the lower part of a heat exchanger according to FIG. 2;
• FIG. 3 is a perspective view of the plurality of exchanger modules and a part of the support structure of the heat exchanger according to FIG. 2;
• FIG. 4 is a perspective view of the plurality of exchanger modules and of an additional part of the support structure of the heat exchanger according to FIG. 2;
• FIG. 5 is a perspective view of the plurality of exchanger modules and an additional portion of the support structure of the heat exchanger according to FIG. 2;
• Figure 5A is a detail view of Figure 5;
• FIG. 6 shows Figure 5 and further illustrates in perspective the first central collector of the heat exchanger according to the invention
• FIG. 7 shows Figure 6 and further illustrates in perspective the inlet and outlet pipes of one of the fluids and their central collectors of the heat exchanger according to the invention
• FIG. 8 is an isolated perspective view of the inlet and outlet pipes of one of the fluids and of their central collectors shown in FIG. 7;
• FIG. 8A shows FIG. 7 and further illustrates in perspective the arrangement of a portion of the annular collector and the arrangement of the inlet and outlet pipes and their central collectors in the bottom of the sealed enclosure. of the exchanger according to the invention
• FIG. 9 is a perspective view and cut away of the relative arrangement between the lid of the sealed chamber and another part of the annular collector.
• the inventors of the present invention have sought to retain the advantages of the heat exchanger I according to this publication, namely essentially a good compactness and a high unit thermal power, while avoiding its major disadvantage. In this way, they sought to guarantee the distribution of fluids industrially.
• the heat exchanger 1 is shown in its vertical operating configuration with the lid 20 of the sealed enclosure on top.
• the heat exchanger 1 of central axis X comprises a sealed enclosure 2 in which is housed a plurality of 3 exchanger modules 3.1, 3.2, 3.3, 3.4, 3.5, 3.6, 3.7, 3.8 arranged vertically and parallel to the X axis.
• the number of identical exchanger modules is equal to eight.
• the sealed enclosure 2 is of substantially cylindrical general shape and consists essentially of a cover 20, a bottom 21 and a side shell 22 in the form of a ferrule.
• the lid 20 and the ferrule 22 are assembled together at means of a first group of bolts 23.
• the bottom 21 and the ferrule 22 are also assembled together by means of a second group of bolts 23.
• the sealed enclosure 2 comprises at one of its longitudinal ends 2a, an inlet 10 and an outlet 1 1 of the nitrogen
• Each exchanger module 3.1 to 3.8 integrates two fluid circuits, one of which is dedicated to the circulation of sodium (Na) coming from a nuclear reactor RNR-Ma, as the primary fluid of the exchanger module, and the other dedicated to the circulation of nitrogen (N2) as a secondary fluid.
• the plurality of heat exchanger modules 3.1 to 3.8 is supported by a supporting and holding structure 4.
• the support and holding structure 4 is thus fixed rigidly to the external enclosure 2.
• a nitrogen inlet chamber 5 is formed axially on the underside of the enclosure 2, at its lower longitudinal end 2b, between the support structure 4 and the bottom 21 of the enclosure 2. In other words, this chamber 5 is the space available between the support structure 4 and the bottom 21 of the enclosure 2.
• This chamber 5 communicates with each unrepresented input of the integrated nitrogen circuit in one of the exchanger modules 3.1 to 3.8.
• a first central collector 6 is arranged axially around the central axis (X).
• This first central collector 6 has the function of recovering the hot nitrogen to which the heat of the sodium has been transferred in the exchanger modules 3.1 to 3.8.
• This hot collector 6 is thus common to the modules 3.1 to 3.8 but each of them independently supplies this collector through the outlet 30.
• This central collector 6 thus communicates upstream with each output 30 of the integrated nitrogen circuit in one of the exchanger modules 3.1 to 3.4. Downstream, this central collector communicates with the outlet 11 of the nitrogen of the enclosure 2, i.e. through the cover 20.
• annular collector 7 is arranged coaxially around the central collector 6 and exchanger modules 3.1 to 3.8 forming a nitrogen guide space.
• This annular collector 7 serves to bring the cold nitrogen into the chamber 5. More specifically, this annular manifold 7 consists essentially of a deflector of flared shape 70 and a cylindrical shell 71.
• the annular collector 7 can be constituted in one piece made by boiler.
• FIG. 1 A relative arrangement between the deflector 70 and the cover 20 of the enclosure is shown in FIG.
• the guiding space 72 of the cold nitrogen coming from the inlet 10 is delimited from upstream to downstream, outside by the enclosure 2 and inside, only by the annular collector 7, it is that is to say by the deflector 70 and the shell 71.
• the function of the shell 71 is to guide the cold nitrogen along the wall of the sealed enclosure 2, in order to distribute it through the lower ends of the modules 3.1 to 3.8.
• the cold nitrogen distributed in the annular space 72 sets the temperature of the wall of the sealed enclosure 2, typically at about 330 ° C.
• the annular collector 7 therefore communicates upstream with the return of nitrogen from the enclosure 2 and downstream with the chamber 5.
• a plurality 8 of inlet pipes 81, 82, 83, 84, 85, 86, 87, 88 are arranged to bring the hot sodium into each of the inlets 31, 32, 33, 34, 35, 36, 37, 38 of the integrated sodium circuit in one of the exchanger modules 3.1 to 3.8.
• each inlet pipe 81 to 88 communicates upstream with the inlet 12 of the sodium of the enclosure 2, and downstream with each inlet 31 to 38 of the sodium circuit integrated in one of the exchanger modules 3.1 to 3.8 .
• the plurality 8 of inlet pipes communicates with a second central collector 14.
• each inlet 31 to 38 is formed on the top of a module 3.1 to 3.8: the plurality 8 of inlet pipes 81 to 88 is thus curved in order to be able to lead to these longitudinal inlets 31 to 38 .
• each input 31 to 38 is made on a longitudinal side in the upper part of a module 3.1 to 3.8.
• a plurality 9 of outlet pipes 91, 92, 93, 94, 95, 96, 7, 98 is arranged to extract the cold sodium from each of the outputs of the integrated sodium circuit in one of the exchanger modules 3.1 to 3.8.
• each outlet pipe 91 to 98 communicates upstream with an outlet of the sodium circuit integrated in one of the exchanger modules 3.1 to 3.8 and downstream with the outlet 13 of the sodium of the enclosure 2.
• the outlet 13 of the cold sodium takes place bottom of the chamber 2 through the bottom 21.
• the plurality 9 of output pipes communicates with a third central collector 17.
• FIG. 7A An advantageous embodiment of the plurality of inlet and outlet pipes 9 and their relative arrangement is shown in FIG. 7A: the coaxial arrangement of the third central collector 17 is clearly seen around the second central collector 14.
• the support and holding structure 4 comprises a support platform 40 which bears against a peripheral shoulder inside the bottom 21 of the enclosure 2. According to the invention, no function of relative sealing between the supply of cold nitrogen and the recovery of hot nitrogen is not to be realized for the platform 40. Thus, as it appears better later, no flexibility by metal bellows between the inlet piping 8 and sodium 9 output is to achieve.
• the platform 40 can thus be perforated, in particular to reduce the weight.
• the platform 40 may be a beam assembly made in welded mechanics.
• the modules 3.1 to 3.8 are placed on the platform 40 and are held in position by brackets fixed on the platform 40 ( Figure 3).
• the supporting and holding structure 4 also comprises means 41 for lateral holding of the exchanger modules 3.1 to 3.8, also fixed on the platform 40 (FIG. 4), by way of example, the lateral holding means 41 can be a welded welded beam assembly that conforms to the outer shape of the modules, it may be two groups of beams at 90 ° from each other and dividing the modules 3.1 to 3.8 into four equal groups ( Figure 4).
• a sealing plate 42 is screwed onto the holding structure 41 (FIG. 5). Its function is to seal the cold nitrogen fed into the heat exchanger and the hot nitrogen leaving each exchanger module 3.1 to 3.8 is recovered by the first central collector 6.
• the first central collector 6 or hot collector, nitrogen is fixed directly on the sealing plate 42.
• An advantageous embodiment of realization of the sliding sealing system between central collector 6 and modules 3.1 to 3.8 is shown in FIG. 5A: a flange 43 is fixed on the sealing plate 42 by means of screws 44 and segment joints 45 between the output 30 of the modules and the collector 6 are arranged. Seals 46 are also arranged between flange 43 and sealing plate 42. Alternatively, metal bellows could be provided.
• heat exchanger 1 which has just been described will now be briefly explained in relation to the path of nitrogen and sodium.
• the cold nitrogen arrives, at a temperature of the order of 330 ° C. and at a pressure of the order of 180 bar, through the inlet 10 and is then fed through the annular manifold 7 at the bottom of the enclosure 2 until to the inlet chamber 5 above the bottom 21, as illustrated by the lateral arrows in FIG.
• the nitrogen then flows through the heat exchanger modules 3.1 to 3.8 in which the heat from the hot sodium is transferred thereto.
• the nitrogen which has become hot at a temperature of the order of 515 ° C., emerges from the modules 3.1 to 3.8 and is then withdrawn from the enclosure through the outlet 11 via the first central collector 6.
• the hot sodium is brought, at a temperature of the order of 530 ° C, by the second central collector 14 through the inlet 12 and is distributed in each exchanger module 3.1 to 3.8 by the pipes 81 to 88, as illustrated by the rising vertical arrows in FIG.
• the sodium then passes through the heat exchanger modules 3.1 to 3.8 in which it transfers its heat to the nitrogen.
• the sodium which has become cold at a temperature of the order of 345 ° C., emerges from the modules 3.1 to 3.8 at their lower ends and is then extracted from the enclosure 2 through the outlet 13 via the outlet pipes 91 to 98. .
• the cold gas (cold N2) flows from top to bottom and counteracts with the hot sodium.
• the cold gas (cold N2) reaches the chamber 5, enters at the bottom of the modules 3.1 to 3.8 and then hot spring through the module outlets 30 to supply the collector 6 and finally the heat exchanger outlet 1 via outlet 1.
• FIG. 2A in the heat exchanger 1 according to the invention, there is no gas inlet manifold by module: the gas channels defined between the deflector 7 and the chamber 2 open directly into the latter, at the chamber 5.
• the chamber 5 defmed by the chamber 2 acts as an inlet manifold gas.
• the circulation of the fluids is compatible with a circulation in natural convection.
• the cold gas (N2) meanwhile descends along the wall of the sealed chamber 2 and it rises at the same time as it is heated to be extracted by the central collector 6. The heat promotes its progression upwards. the exchanger 1.

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• Engineering & Computer Science (AREA)
• Physics & Mathematics (AREA)
• Thermal Sciences (AREA)
• Mechanical Engineering (AREA)
• General Engineering & Computer Science (AREA)
• Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
• Manufacture And Refinement Of Metals (AREA)

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• 2013
  • 2013-08-26 FR FR1358178A patent/FR3009862B1/fr not_active Expired - Fee Related
• 2014
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  • 2014-08-22 TN TN2016000074A patent/TN2016000074A1/fr unknown
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