Any and all applications for which a foreign or domestic priority claim is identified in the Application Data Sheet as filed with the present application are hereby incorporated by reference under 37 CFR 1.57.
The present invention relates to an evaporator of a working fluid for an OTEC plant.
In a manner known per se, an OTEC (for Ocean Thermal Energy Conversion) plant uses the temperature difference between the surface water and the deep water of the oceans to produce electricity.
Typically, such an OTEC plant comprises an evaporator, in which a working fluid is evaporated by the warm surface waters to drive a turbine, and a condenser, in which this working fluid is then condensed by the cold waters of the ocean floor.
The evaporator of an OTEC plant generally has an elongated body through which a bundle of evaporators extends. This bundle of evaporators, in the form of a plurality of pipes or plates, circulates hot water along the evaporator. A sprinkling system consisting of pipes and nozzles mounted on the pipes is provided along this bundle in order to sprinkle working fluid, in a liquid state, onto it. The nozzles are generally arranged homogeneously along the corresponding pipes.
The evaporator body, also known as the shell in the state of the art, not only acts as a pressurized container but also guides the working fluid evaporated by the bundle of evaporators to an evacuation system.
In horizontal falling film evaporator applications, the sprinkling system is located below the evacuation system. Thus, the fluid in liquid state, falling by gravity on the bundle of evaporators, rises again after its evaporation to the evacuation system.
In such a case, the shell alone is insufficient to guide the steam efficiently, and a specific guide system is therefore provided.
This guide system generally comprises a component covering the bundle of evaporators and isolating the working fluid, still in liquid state, from the steam. This component, known in the state of the art as a “casing”, is fixed to the shell at a distance from it to form a sealed channel for the passage of the steam.
However, due to different thermal expansions between the casing and the shell, the channel formed between them is not perfectly sealed. Thus, some working fluid can pass through these imperfections, which decreases the efficiency of the OTEC plant. Furthermore, this can lead to droplets forming and driving on the turbine.
The object of the present invention is to provide an evaporator whose casing ensures a particularly effective isolation between the fluid in liquid state and the steam, and thus increases the efficiency of the OTEC plant.
To this end, the subject matter of the invention is an evaporator of a working fluid for an OTEC plant, comprising:
The guide system comprises:
According to further advantageous aspects of the invention, the evaporator comprises one or more of the following features, taken alone or in any technically possible combination:
These features and advantages of the invention will become apparent from the following description, given only as a non-limiting example, and made with reference to the appended drawings, in which:
In fact, an evaporator 10 for an OTEC plant has been shown in
With reference to
At the first end 12, the evaporator body 11 has a substantially conical shape 14 opening into a substantially cylindrical shape 15 defining the second end 13.
The evaporator body 11 is pressurized, for example, and may also be referred to in the terminology used in the prior art as a shell.
In each cross-section of the cylindrical part 15 (one of which is visible in
The evaporator body 11 further defines an inner surface 16 delimiting the interior of said body and two side walls 17A, 17B.
As visible in
Referring again to
The sprinkling system 24 is arranged in the upper part PS of the evaporator body 11 and comprises a supply network and a plurality of sprinkling nozzles arranged on this supply network.
In particular, in the example of
Within the evaporator body 11, each supply pipe 30 extends along the main axis X above the bundle of evaporators 25. Thus, in
Furthermore, as can be seen in cross-section in
The opening of this arc of a circle 31 is between 80° and 160°, for example.
In addition, the supply pipes 30 are evenly distributed along this arc, for example.
Thus, in the example shown in
The bundle of evaporators 25 takes the form of a plurality of pipes passing through the cylindrical part 15 of the body 11 along the main axis X. These pipes are a few thousand in number, for example, such as 3000 in number. Thus, for reasons of legibility of
The pipes of the bundle of evaporators 25 transport water, called warm water, i.e. surface water. This water circulates in the bundle of evaporators 25 along the main axis X, from left to right in the example of
Thus, when a working fluid sprinkled via the sprinkling system 24 comes into contact with the pipes of the bundle 25, it vaporizes.
The channeling system 26 allows the non-vaporized working fluid to be channeled back into the evaporator 10 via the sprinkling system 24, for example.
This channeling system 26 is arranged in the lower part PI of the evaporator body 11, below the bundle of evaporators 25.
The evacuation system 27 is used to evacuate steam produced by the bundle of evaporators 25 and to guide it to a (non-illustrated) turbine, for rotation.
This evacuation system 27 is arranged in the upper part PS of the evaporator body 11, above the sprinkler system 24 and thus above the bundle of evaporators 25.
The evacuation system 27 takes the form of a plurality of channels passing through the evaporator body 11 in the upper part thereof, for example.
The guide system 28 is used to guide the working fluid in a gaseous state to the evacuation system 27.
For this purpose, the guide system 28 comprises a cover 40 and at least two partitioning means 42, 43, as can be seen in
The cover 40 is elongated, extends along the main axis X and covers the bundle of evaporators 25 and the sprinkling system 24 in the upper part PS and intermediate part PM of the evaporator body 11.
In particular, in the illustrated example, the cover 40 has a “U”-shaped bent sheet metal. This sheet metal defines an outer surface 46 which, in turn, defines at least two substantially planar parts 47A, 47B, visible in
More generally, according to other embodiments, the cover 40 has any other shape covering the sprinkling system 24 and the evaporator bundle 25.
Each of these planar parts 47A, 47B is arranged opposite one of the side walls 17A, 17B of the evaporator body 11.
In the simplified example of
According to other embodiments, these parts 47A, 47B may have any other shape chosen in particular depending on the shape of the evaporator body 11. Thus, for example, when the evaporator body 11 has a conical shape at its ends, the parts 47A, 47B may follow this shape.
The cover 40 is arranged away from the inner surface 16 of the evaporator body 11 so as to form a channel for the passage of steam.
This channel opens in the lower part PI of the evaporator body 11 onto two longitudinal openings 49A, 49B, formed between the cover 40 and the side walls 17A, 17B, and in the upper part PS of the evaporator body 11, on the evacuation system 27.
In particular, each longitudinal opening 49A, 49B is formed between one of the side walls 17A, 17B and the planar part 47A, 47B of the cover 40 corresponding to that side wall 17A, 17B.
Each of the partitioning means 42, 43 takes the form of a plate cut out in a “U” shape, defining an inner contour 52, 53 respectively, an outer contour 62, 63 respectively and a partition 72, 73 respectively.
Each inner contour 52, 53 is in sealed contact with the outer surface 46 of the cover 40 and each outer contour 62, 63 is in sealed contact with the inner surface 16 of the evaporator body 11.
Each wall 72, 73 extends between the corresponding inner contour 52, 53 and outer contour 62, 63, substantially perpendicular to the main axis X, for example.
Thus, the walls 72, 73 define and complete the channel for passage of steam formed between the outer surface 46 of the cover 40 and the inner surface 16 of the evaporator body 11.
The cover 40 is held away from the inner surface 16 of the evaporator body 11 by the partition means 43.
In particular, this partitioning means 43 corresponding to the end 13 of the evaporator body 11 is sealed between the cover 40 and the evaporator body 11, for example.
In other words, in this case, the inner contour 53 of this means 43 is sealed to the outer surface 46 of the cover 40 and the outer contour 63 is sealed to the inner surface 16 of the evaporator body 11. This attachment is made by angle welding, for example.
The partition means 42 corresponding to the end 12 of the evaporator body 11 is sealed to the evaporator body 11 and is in free contact with the cover 40.
In this case, the outer contour 62 is sealed by welding, for example, to the inner surface 16 of the evaporator body 11 and the inner contour 52 is in free contact with the outer surface 46 of the cover 40. In this case, the inner contour 52 is said to be free contour.
Thus, during longitudinal expansions of the cover 40, the inner contour 52 is able to slide along the outer surface 46 of the cover 40 along the main axis X.
The seal between the inner contour 52 and the outer surface 46 of the cover 42 is ensured by a metal-to-metal type sealing contact, for example, or by a seal provided for this purpose between these parts.
In a variant, the inner contour 52 of the partitioning means 42 is fixed to the outer surface 46 of the cover 40 and the outer contour 62 is thus in free contact with the inner surface 16 of the evaporator body 11.
In this case, the outer contour 62 is thus said to be a free contour, capable of sliding along the inner surface 16 of the evaporator body 11 and ensuring sealing either by metal-to-metal contact or through a seal provided for this purpose with this surface 16.
Of course, it is possible to provide a partitioning means with a free contour (analogous to the partitioning means 42) at the end 13 of the evaporator body 11 and a partitioning means with the two contours fixed (analogous to the partitioning means 43) at the end 12 of the evaporator body 11. It is also possible to arrange these partitioning means in different parts of the evaporator body 11 than the ends 12, 13.
It is then conceivable that the present invention has a number of advantages.
Indeed, in the evaporator according to the invention, the partitioning means of the cover, used to isolate the fluid in a liquid state with the steam makes it possible for the cover to expand along the main axis independently of the evaporator body.
Thus, the seal of the steam guide channel is not broken, which allows the fluid in liquid state to be effectively isolated from the fluid in gaseous state.
It is thus clear that the guidance system within the meaning of the invention makes it possible to decorrelate the sealing function with expansion of the intersection function of the shapes of the cover and the evaporator body, particularly in its conical part.
This then makes it possible to increase the efficiency of the turbine and more generally, the efficiency of the OTEC plant.
Number | Date | Country | Kind |
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FR1906457 | Jun 2019 | FR | national |
Filing Document | Filing Date | Country | Kind |
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PCT/EP2020/066759 | 6/17/2020 | WO |