Compact mixing condenser with enhanced heat exchange

Abstract

The present invention provides a compact mixing condenser with enhanced heat exchange, comprising a condenser shell, a water chamber, a first condensation structure, and a second condensation structure; the condenser shell is provided with a main inlet and a main outlet, and the water chamber is provided with a plurality of condensation nozzles for forming a cooling liquid film; the first condensation structure has a first steam inlet and a first steam outlet, a first steam flow channel is formed between the first steam inlet and the first steam outlet, and a liquid film channel is further provided between the first steam inlet and the first steam outlet, and the liquid film channel and each condensation nozzle are arranged in sequence; the second condensation structure has a second steam inlet and a second steam outlet, a second steam flow channel is formed between the second steam inlet and the second steam outlet, and a plurality of water spraying channels are further provided between the second steam inlet and the second steam outlet. The compact mixing condenser with enhanced heat exchange provided by the present invention is intended to solve the problems of low condensation efficiency and large size of traditional mixing condensers.

Description

Technical Field

[0001] The present invention relates to the technical field of condensing devices, and in particular to a compact mixing condenser with enhanced heat exchange. Background Art

[0002] As the power generation of power plants gradually increases, the size of their steam condensers also gradually increases. Therefore, there is an urgent need to improve the heat exchange capacity of steam condensers. Traditional steam condensers can be divided into shell and tube indirect condensers and hybrid condensers. Among them, the shell and tube indirect condenser adopts an indirect heat exchange method in which steam flows through the shell side and cooling water flows through the tube side. The total heat transfer coefficient is low and the volume is large. The hybrid condenser adopts a phase change heat transfer method in which steam and cooling water are directly contacted and condensed. The heat transfer coefficient is very high and can effectively reduce the volume of the condenser. In order to form a stable water film, the hybrid condenser currently used in power plants will be equipped with a water chamber in the middle position inside the condenser. Water is replenished inside the condenser through an external pump device. A nozzle is installed on the water chamber. The function of the nozzle is to form a water film with the sprayed water so that it can exchange heat with the steam efficiently. However, since the steam in the current hybrid condenser flows in a one-way manner from top to bottom, the contact time with the liquid film is relatively short. Moreover, after the steam enters the large space inside the condenser from the inlet, the flow rate will decrease, and the convective heat transfer coefficient will also decrease accordingly, thereby affecting the overall heat transfer coefficient. In order to ensure that the steam can be fully condensed, in addition to increasing the amount of liquid film, the height of the hybrid condenser needs to be increased to extend the contact heat exchange time between the steam and the liquid film. This results in the hybrid condenser being unable to be effectively reduced in height, which is not conducive to its application in certain scenarios with limited height space. Summary of the Invention

[0003] The present invention provides a compact mixing condenser with enhanced heat exchange, aiming to solve the problems of low condensation efficiency and large volume of traditional mixing condensers.

[0004] In view of the problems existing in the prior art, the present invention provides a compact mixing condenser with enhanced heat exchange, comprising:

[0005] A condenser housing, wherein the condenser housing has an installation cavity therein and is provided with a main inlet and a main outlet communicating with the installation cavity;

[0006] a water chamber disposed in the mounting cavity and extending along the axial direction of the condenser shell, wherein the water chamber is provided with a plurality of condensation nozzles, each of the condensation nozzles being used to spray water to form a cooling liquid film;

[0007] A first condensation structure is arranged near the main inlet, the first condensation structure has a first steam inlet and a first steam outlet, a first steam flow channel is formed between the first steam inlet and the first steam outlet, the first steam inlet is connected to the main inlet, and a plurality of liquid film channels are provided between the first steam inlet and the first steam outlet, each of the liquid film channels is arranged corresponding to each of the condensation nozzles in sequence; and

[0008] The second condensation structure is arranged between the first condensation structure and the main outlet. The second condensation structure has a second steam inlet and a second steam outlet. A reciprocating second steam flow channel is formed between the second steam inlet and the second steam outlet. The second steam inlet is connected to the first steam outlet, and the second steam outlet is connected to the main outlet. There are also multiple water sprinkling channels set through the second steam flow channel between the second steam inlet and the second steam outlet. One end of the water sprinkling channel is connected to the first steam flow channel, and the other end of the water sprinkling channel is connected to the main outlet.

[0009] According to the compact mixing condenser with enhanced heat exchange provided by the present invention, a plurality of condensation nozzles are provided on both side walls of the water chamber that are axially opposite to each other, and a plurality of the first condensation structures and the second condensation structures are provided on both sides of the water chamber.

[0010] According to the enhanced heat exchange compact mixing condenser provided by the present invention, the first condensing structure includes a guide plate, a first water sprinkling plate, and a plurality of first baffles, one end of the guide plate is connected to the side wall of the water chamber, and the other end extends toward the condenser shell;

[0011] The first water spray plate is separated from the guide plate. One end of the first water spray plate is connected to the condenser shell, and the other end extends toward the side wall of the water chamber. Each first deflector extends along the height direction of the condenser shell and is arranged in sequence on the guide plate or the first water spray plate at intervals to form the first steam flow channel that is reciprocating and circuitous.

[0012] According to a compact mixing condenser with enhanced heat exchange provided by the present invention, a plurality of groups of liquid film through holes are correspondingly provided on the plurality of first baffles, a group of the liquid film through holes includes a liquid film through hole provided on each of the first baffles, and a group of the liquid film through holes is provided corresponding to one of the condensation nozzles to form a liquid film channel.

[0013] According to the present invention, a compact mixing condenser with enhanced heat exchange is provided, wherein the end of the guide plate away from the water chamber is smoothly connected to the nearest first baffle, and the guide plate, the first baffle and the condenser shell together enclose the first steam inlet;

[0014] One end of the first water sprinkling plate away from the water chamber is smoothly connected to the nearest first baffle plate, and the first water sprinkling plate, the first baffle plate and the side wall of the water chamber together enclose the first steam outlet.

[0015] According to the present invention, the second condensing structure includes a second water sprinkling plate and a second baffle. The second water sprinkling plate is separated from the first water sprinkling plate. One end of the second water sprinkling plate is connected to the side wall of the water chamber, and the other end extends toward the condenser shell.

[0016] Each of the second baffles extends along the height direction of the condenser shell and is sequentially and alternately arranged on the first water spray plate or the second water spray plate to form a reciprocating and circuitous second steam flow channel.

[0017] According to the compact mixing condenser with enhanced heat exchange provided by the present invention, a plurality of water sprinkling holes are correspondingly provided on the first water sprinkling plate and the second water sprinkling plate, and two water sprinkling holes correspondingly provided in the height direction of the shell are used to form a water sprinkling channel.

[0018] According to a compact mixing condenser with enhanced heat exchange provided by the present invention, the second water sprinkling plate, the second baffle and the side wall of the water chamber are enclosed to form the second steam inlet, and the second water sprinkling plate, the second baffle and the condenser shell are enclosed to form the second steam outlet. From the second steam inlet to the second steam outlet, the distance between the first water sprinkling plate and the second water sprinkling plate is gradually reduced.

[0019] According to a compact mixing condenser with enhanced heat exchange provided by the present invention, the distance between two adjacent first baffles is gradually reduced from the first steam inlet to the first steam outlet, and the distance between two adjacent second baffles is gradually reduced from the second steam inlet to the second steam outlet.

[0020] According to the compact mixing condenser with enhanced heat exchange provided by the present invention, the end of the first baffle is connected to the condenser shell in a curved and smooth transition.

[0021] According to a compact mixing condenser with enhanced heat exchange provided by the present invention, an exhaust zone is provided at one end of the water chamber close to the main outlet, the exhaust zone has an exhaust inlet and an exhaust outlet, the exhaust inlet is connected to the installation cavity, and the exhaust outlet is connected to the exhaust pump.

[0022] The compact mixing condenser with enhanced heat exchange provided by the present invention, by arranging a reciprocating and circuitous first steam flow channel and a liquid film channel running through the first steam flow channel, does not affect the film formation quality of the liquid film, but can also increase the contact time between the steam and the liquid film, so that the steam and the liquid film present a nearly countercurrent heat exchange mode, which can greatly improve the steam condensation effect, thereby reducing the size of the condensation zone in the height direction and thus reducing the size of the condenser; in addition, by arranging the second steam flow channel and the water sprinkling channel, on the one hand, the contact time between the steam and the water sprinkling can be increased, thereby improving the steam condensation effect, and on the other hand, the size of the water sprinkling zone in the height direction can be reduced, thereby reducing the size of the condenser. BRIEF DESCRIPTION OF THE DRAWINGS

[0023] In order to more clearly illustrate the technical solutions in the present invention or the prior art, the following briefly introduces the drawings required for use in the embodiments or the description of the prior art. Obviously, the drawings described below are some embodiments of the present invention. For ordinary technicians in this field, other drawings can be obtained based on these drawings without paying any creative work.

[0024] Figure 1 This is a front view structural diagram of the compact mixing condenser with enhanced heat exchange provided by the present invention;

[0025] Figure 2 for Figure 1 A side view structural diagram of the invention;

[0026] Figure 3 for Figure 1 A cross-sectional structural diagram of ;

[0027] Figure markings: 1: Compact mixing condenser with enhanced heat exchange; 2: Condenser shell; 3: Water chamber; 4: First condensation structure; 5: Second condensation structure; 6: Exhaust area; 7: Mounting cavity; 8: Main inlet; 9: Main outlet; 10: Condensation nozzle; 11: First steam inlet; 12: First steam outlet; 13: First steam flow channel; 14: Liquid film channel; 15: First deflector; 16: Liquid film through hole; 17: Guide plate; 18: First water spraying plate; 19: Second steam inlet; 20: Second steam outlet; 21: Second steam flow channel; 22: Water spraying channel; 23: Second water spraying plate; 24: Second deflector; 25: Water spraying hole; 26: Exhaust inlet; 27: Exhaust outlet. DETAILED DESCRIPTION

[0028] To make the objectives, technical solutions, and advantages of the present invention more clear, the technical solutions of the present invention will be clearly and completely described below in conjunction with the accompanying drawings. Obviously, the embodiments described are only some embodiments of the present invention, not all embodiments. Based on the embodiments of the present invention, all other embodiments obtained by ordinary technicians in this field without making creative efforts shall fall within the scope of protection of the present invention.

[0029] In the description of the embodiments of the present invention, it should be noted that the terms "center", "longitudinal", "lateral", "up", "down", "front", "back", "left", "right", "vertical", "horizontal", "top", "bottom", "inside", "outside", etc., indicating the orientation or positional relationship, are based on the orientation or positional relationship shown in the accompanying drawings, and are only for the convenience of describing the embodiments of the present invention and simplifying the description, and do not indicate or imply that the device or element referred to must have a specific orientation, be constructed and operate in a specific orientation, and therefore should not be understood as limiting the embodiments of the present invention. In addition, the terms "first", "second", and "third" are used for descriptive purposes only and should not be understood as indicating or implying relative importance.

[0030] In the description of the embodiments of the present invention, it should be noted that, unless otherwise specified or limited, the terms "connected" and "connection" should be understood in a broad sense. For example, they can refer to fixed connections, detachable connections, or integral connections; mechanical connections, electrical connections; and direct connections or indirect connections through an intermediary. Those skilled in the art will understand the specific meanings of the above terms in the embodiments of the present invention based on the specific circumstances.

[0031] In the embodiments of the present invention, unless otherwise expressly specified or limited, a first feature being "above" or "below" a second feature may mean that the first and second features are in direct contact, or that the first and second features are in indirect contact through an intermediate medium. Furthermore, a first feature being "above," "above," or "above" a second feature may mean that the first feature is directly above or diagonally above the second feature, or simply means that the first feature is at a higher level than the second feature. A first feature being "below," "below," or "below" a second feature may mean that the first feature is directly below or diagonally below the second feature, or simply means that the first feature is at a lower level than the second feature.

[0032] In the description of this specification, the reference terms "one embodiment", "some embodiments", "example", "specific example", or "some examples" mean that the specific features, structures, materials or characteristics described in conjunction with the embodiment or example are included in at least one embodiment or example of the embodiment of the present invention. In this specification, the schematic representations of the above terms do not necessarily refer to the same embodiment or example. Moreover, the specific features, structures, materials or characteristics described can be combined in any one or more embodiments or examples in a suitable manner. In addition, those skilled in the art can combine and combine different embodiments or examples described in this specification and features of different embodiments or examples without contradiction.

[0033] The following combination Figure 1-Figure 3 The enhanced heat exchange compact mixing condenser 1 provided by the present invention is described.

[0034] In order to solve the problems of low condensation efficiency and large size of the mixing condenser in traditional technology, an embodiment of the present invention provides an enhanced heat exchange compact mixing condenser 1, including a condenser shell 2, a water chamber 3, a first condensation structure 4 and a second condensation structure 5.

[0035] The condenser housing 2 has a mounting cavity 7 therein. A main inlet 8 and a main outlet 9 are provided on the condenser housing 2, which are in communication with the mounting cavity 7. Steam to be cooled enters through the main inlet 8, and condensed water flows out through the main outlet 9. A water chamber 3 is provided within the mounting cavity 7 and extends axially along the condenser housing 2. The water chamber 3 has a cooling water inlet and a cooling water outlet. The water chamber 3 is also provided with a plurality of condensation nozzles 10. Cooling water flows through the condensation nozzles 10 to form a cooling liquid film, and the steam is cooled by contact with the cooling liquid film.

[0036] The first condensation structure 4 is arranged near the main inlet 8. The first condensation structure 4 has a first steam inlet 11 and a first steam outlet 12. A reciprocating first steam flow channel 13 is formed between the first steam inlet 11 and the first steam outlet 12. The first steam inlet 11 is connected to the main inlet 8. The provision of the first steam flow channel 13 lengthens the flow path of the steam and increases the contact time between the steam and the liquid film, which is beneficial to improving the condensation efficiency of the steam. Correspondingly, a plurality of liquid film channels 14 are provided between the first steam inlet 11 and the first steam outlet 12, and each liquid film channel 14 is arranged corresponding to each condensation nozzle 10 in sequence. The liquid film sprayed from the nozzle will pass through the liquid film channel 14 and produce sufficient contact condensation with the steam in the first steam flow channel 13. The provision of the liquid film channel 14 and the first steam flow channel 13 does not affect the film formation quality of the liquid film, but can also increase the contact time between the steam and the liquid film, so that the steam and the liquid film present a nearly countercurrent heat exchange mode, which can greatly improve the steam condensation effect, thereby reducing the size of the condensation area in the height direction and thus reducing the size of the condenser.

[0037] The second condensation structure 5 is provided between the first condensation structure 4 and the main outlet 9. The second condensation structure 5 has a second steam inlet 19 and a second steam outlet 20. A reciprocating second steam flow channel 21 is formed between the second steam inlet 19 and the second steam outlet 20. The second steam inlet 19 is connected to the first steam outlet 12, and the second steam outlet 20 is connected to the main outlet 9. There are also multiple water sprinkling channels 22 provided between the second steam inlet 19 and the second steam outlet 20, which are provided through the second steam flow channel 21. One end of the water sprinkling channel 22 is connected to the first steam flow channel 13, and the other end of the water sprinkling channel 22 is connected to the main outlet 9. The condensed water generated in the first condensation structure 4 continues to condense the steam in the second steam flow channel 21 through the water sprinkling channel 22. The provision of the second steam flow channel 21 and the water sprinkling channel 22 can, on the one hand, increase the contact time between the steam and the water sprinkling, thereby improving the steam condensation effect, and on the other hand, can reduce the height dimension of the water sprinkling area, thereby reducing the size of the condenser.

[0038] See Figure 1 In the technical solution provided by the present invention, a plurality of condensation nozzles 10 are provided on both side walls of the water chamber 3 that are axially opposite to each other, and a plurality of the first condensation structures 4 and the second condensation structures 5 are provided on both sides of the water chamber 3. It should be noted that the condensation nozzles 10 can be set as multiple groups along the axial intervals of the condenser shell 2, and each group of condensation nozzles 10 includes a plurality of condensation nozzles 10 spaced apart along the height direction of the condenser shell 2, so that the space can be utilized to the maximum extent and the condensation efficiency can be improved. In addition, in this embodiment, the first condensation structures 4 are set as two, which are symmetrically arranged along the two sides of the water chamber 3, and of course they can also be asymmetrically arranged; the second condensation structures 5 are also set as two, which are arranged along the two sides of the water chamber 3. It should be noted that the second condensation structures 5 can be set as four, six or eight according to actual applications to meet the steam condensation needs under high working conditions. The present invention is not limited to this.

[0039] Specifically, see Figure 1-Figure 2 The first condensation structure 4 covers the entire liquid film area and includes a guide plate 17, a first water sprinkling plate 18, and a plurality of first baffles 15. One end of the guide plate 17 is connected to the side wall of the water chamber 3, and the other end extends toward the condenser shell 2. The first water sprinkling plate 18 is separated from the guide plate 17. One end of the first water sprinkling plate 18 is connected to the condenser shell 2, and the other end extends toward the side wall of the water chamber 3. The first baffles 15 extend along the height direction of the condenser shell 2. The first baffles 15 are staggered on the guide plate 17 or the first water sprinkling plate 18 in sequence. A steam flow channel is formed between two adjacent first baffles 15. All steam flow channels are connected end to end in sequence to form a reciprocating first steam flow channel 13. Please refer to Figure 2In this embodiment, steam enters from both sides of the condenser shell 2, flows toward the middle through the first steam inlet 11 along the flow space formed by the first baffle 15, and finally flows downward from the side wall of the water chamber 3 structure into the second condensation structure 5. It should be noted that in this embodiment, the first baffles 15 are arranged in parallel, and the steam flow channels formed are also arranged in parallel. Of course, the first baffles 15 can also be arranged to be inclined to each other, and the present invention is not limited to this. It should also be noted that more guide plates 17 structures can also be set in the space between the main inlet 8 and the water chamber 3 structure to better guide the steam to flow to both sides.

[0040] Furthermore, a plurality of groups of liquid film through holes 16 are correspondingly provided on the first baffle 15, and each group of liquid film through holes 16 includes a liquid film through hole 16 provided on each first baffle 15. A group of liquid film through holes 16 is provided corresponding to a condensation nozzle 10, and a sheet-like liquid film is sprayed out from each condensation nozzle 10, passing through the liquid film through holes 16 on each first baffle 15 successively, and finally forming a complete liquid film to condense and contact with the steam in the first steam flow channel 13.

[0041] Furthermore, the end of the guide plate 17 facing away from the water chamber 3 smoothly transitions to the nearest first baffle 15. The guide plate 17, the first baffle 15, and the condenser housing 2 together form a first steam inlet 11. The end of the first water spray plate 18 facing away from the water chamber 3 smoothly transitions to the nearest first baffle 15. The first water spray plate 18, the first baffle 15, and the sidewall of the water chamber 3 together form a first steam outlet 12. This arrangement ensures smooth steam flow through the aforementioned corners, thereby reducing adverse factors such as steam flow separation. Similarly, the end of the first baffle 15 is curved and smoothly transitions to the condenser housing 2, thereby ensuring smooth steam flow.

[0042] See Figure 1Specifically, the second condensation structure 5 includes a second water sprinkling plate 23 and a second baffle 24. The second water sprinkling plate 23 is separated from the first water sprinkling plate 18. One end of the second water sprinkling plate 23 is connected to the side wall of the water chamber 3, and the other end extends toward the condenser shell 2. Each second baffle 24 extends along the height of the condenser shell 2. The second baffles 24 are alternately arranged on the first water sprinkling plate 18 or the second water sprinkling plate 23. A steam flow channel is formed between two adjacent second baffles 24. All steam flow channels are connected end to end to form a reciprocating and circuitous second steam flow channel 21. Multiple water sprinkling holes 25 are correspondingly formed on the first water sprinkling plate 18 and the second water sprinkling plate 23. Two water sprinkling holes 25 correspondingly arranged along the height of the shell form a water sprinkling channel 22. It should be noted that the size of the water sprinkling holes 25 can be changed according to the situation and does not have to be exactly the same size. It can be a combination of water sprinkling holes 25 of multiple sizes. Condensed water and cooling water can flow downward through the water sprinkling holes 25 to form sprinkling water. The steam is further in contact with the sprinkling water when flowing through the second steam flow channel 21, thereby achieving further condensation of uncondensed steam and heat recovery of the sprinkling water. The second condensation structure 5 can increase the contact time between steam and sprinkling water, improve the steam condensation effect, thereby reducing the size of the sprinkling area in the height direction, and further reducing the size of the condenser.

[0043] Furthermore, the second water sprinkling plate 23, the second baffle plate 24 and the side wall of the water chamber 3 are enclosed to form a second steam inlet 19, and the second water sprinkling plate 23, the second baffle plate 24 and the condenser shell 2 are enclosed to form a second steam outlet 20. From the second steam inlet 19 to the second steam outlet 20, the distance between the first water sprinkling plate 18 and the second water sprinkling plate 23 is gradually reduced. Since the steam content is the highest when the steam just enters the second baffle plate 24 area, and the condensation amount is the largest after contacting the cooling water, more space is needed below it to store condensed water to prevent the condensed water from being too high and submerging the second steam flow channel 21.

[0044] Furthermore, from the first steam inlet 11 to the first steam outlet 12, the distance between two adjacent first baffles 15 is gradually reduced, and from the second steam inlet 19 to the second steam outlet 20, the distance between two adjacent second baffles 24 is gradually reduced. In this way, the steam can have approximately the same flow rate in each steam flow channel, ensuring an efficient convective heat transfer coefficient between steam and water.

[0045] See also Figure 1The end of the water chamber 3 near the main outlet 9 is provided with an air extraction zone 6. The air extraction zone 6 has an air extraction inlet 26 and an air extraction outlet 27. The air extraction inlet 26 is connected to the mounting cavity 7, and the air extraction outlet 27 is connected to the air extraction pump. The condensed water is finally collected into the water tank at the bottom of the condenser through the main outlet 9. There is still a gas space above. The uncondensed gas enters the air extraction zone 6 through the air extraction inlet 26 and is eventually pumped out by the external air extraction pump. The condensed water is then pumped away by an external circulating water pump and provided to users in need, ensuring that the water level in the water tank remains relatively stable.

[0046] The enhanced heat exchange compact mixing condenser 1 provided by the present invention has an intermittent first baffle 15 that does not affect the quality of liquid film formation, but can also increase the contact time between steam and liquid film, so that the steam and liquid film present a nearly countercurrent heat exchange mode, which can greatly improve the steam condensation effect, thereby reducing the height size of the condensation area; the second baffle 24 can increase the contact time between steam and water, improve the steam condensation effect, and thus reduce the height size of the water spraying area. The multi-layer water spraying plate structure can not only achieve further condensation of steam, but also reheat the cooling water and reduce the supercooling of the condensed water, thereby achieving efficient and reasonable use of cooling water, avoiding the problem of excessive power consumption of the circulating water pump caused by a large deviation between the actual cooling water demand and the theoretical demand.

[0047] Finally, it should be noted that the above embodiments are only used to illustrate the technical solutions of the present invention, rather than to limit it. Although the present invention has been described in detail with reference to the aforementioned embodiments, those skilled in the art should understand that they can still modify the technical solutions described in the aforementioned embodiments, or make equivalent replacements for some of the technical features therein. However, these modifications or replacements do not deviate the essence of the corresponding technical solutions from the spirit and scope of the technical solutions of the various embodiments of the present invention.

Claims

1. A compact mixing condenser with enhanced heat exchange, characterized in that: include: A condenser housing, wherein the condenser housing has an installation cavity therein and is provided with a main inlet and a main outlet communicating with the installation cavity; a water chamber disposed in the mounting cavity and extending along the axial direction of the condenser shell, wherein the water chamber is provided with a plurality of condensation nozzles, each of the condensation nozzles being used to spray water to form a cooling liquid film; A first condensation structure is arranged near the main inlet, the first condensation structure has a first steam inlet and a first steam outlet, a first steam flow channel is formed between the first steam inlet and the first steam outlet, the first steam inlet is connected to the main inlet, and a plurality of liquid film channels are provided between the first steam inlet and the first steam outlet, each of the liquid film channels is arranged corresponding to each of the condensation nozzles in sequence; and The second condensation structure is arranged between the first condensation structure and the main outlet. The second condensation structure has a second steam inlet and a second steam outlet. A reciprocating second steam flow channel is formed between the second steam inlet and the second steam outlet. The second steam inlet is connected to the first steam outlet, and the second steam outlet is connected to the main outlet. There are also multiple water sprinkling channels set through the second steam flow channel between the second steam inlet and the second steam outlet. One end of the water sprinkling channel is connected to the first steam flow channel, and the other end of the water sprinkling channel is connected to the main outlet.

2. The compact mixing condenser with enhanced heat exchange according to claim 1, characterized in that: The two side walls of the water chamber that are axially opposite to each other are each provided with a plurality of the condensation nozzles, and the first condensation structure and the second condensation structure are each provided with a plurality of them on both sides of the water chamber.

3. The compact mixing condenser with enhanced heat exchange according to claim 2, characterized in that: The first condensation structure includes a guide plate, a first water spray plate and a plurality of first baffles, one end of the guide plate is connected to the side wall of the water chamber, and the other end extends toward the condenser shell; The first water spray plate is separated from the guide plate. One end of the first water spray plate is connected to the condenser shell, and the other end extends toward the side wall of the water chamber. Each first deflector extends along the height direction of the condenser shell and is arranged in sequence on the guide plate or the first water spray plate at intervals to form the first steam flow channel that is reciprocating and circuitous.

4. The compact mixing condenser with enhanced heat exchange according to claim 3, characterized in that: Multiple groups of liquid film through holes are correspondingly provided on the multiple first baffles, and a group of the liquid film through holes includes a liquid film through hole arranged on each of the first baffles. A group of the liquid film through holes corresponds to a condensation nozzle and is used to form a liquid film channel.

5. The compact mixing condenser with enhanced heat exchange according to claim 4, characterized in that: One end of the guide plate away from the water chamber is smoothly connected to the nearest first baffle, and the guide plate, the first baffle and the condenser shell together enclose the first steam inlet; One end of the first water sprinkling plate away from the water chamber is smoothly connected to the nearest first baffle plate, and the first water sprinkling plate, the first baffle plate and the side wall of the water chamber together enclose the first steam outlet.

6. The compact mixing condenser with enhanced heat exchange according to claim 3, characterized in that: The second condensing structure includes a second water sprinkling plate and a second baffle, the second water sprinkling plate is separated from the first water sprinkling plate, one end of the second water sprinkling plate is connected to the side wall of the water chamber, and the other end extends toward the condenser shell; Each of the second baffles extends along the height direction of the condenser shell and is sequentially and alternately arranged on the first water spray plate or the second water spray plate to form a reciprocating and circuitous second steam flow channel.

7. The compact mixing condenser with enhanced heat exchange according to claim 6, characterized in that: A plurality of water sprinkling holes are correspondingly provided on the first water sprinkling plate and the second water sprinkling plate, and two water sprinkling holes correspondingly provided in the height direction of the shell are used to form a water sprinkling channel.

8. The compact mixing condenser with enhanced heat exchange according to claim 6, characterized in that: The second water sprinkling plate, the second baffle and the side wall of the water chamber together form the second steam inlet, and the second water sprinkling plate, the second baffle and the condenser shell together form the second steam outlet. From the second steam inlet to the second steam outlet, the distance between the first water sprinkling plate and the second water sprinkling plate is gradually reduced.

9. The compact mixing condenser with enhanced heat exchange according to claim 6, characterized in that: From the first steam inlet to the first steam outlet, the distance between two adjacent first baffles is gradually reduced, and from the second steam inlet to the second steam outlet, the distance between two adjacent second baffles is gradually reduced.

10. The compact mixing condenser with enhanced heat exchange according to claim 6, characterized in that: The end of the first baffle is connected to the condenser shell in a curved and smooth transition.

11. The compact mixing condenser with enhanced heat exchange according to claim 1, characterized in that: An air extraction zone is provided at one end of the water chamber close to the main outlet. The air extraction zone has an air extraction inlet and an air extraction outlet. The air extraction inlet is communicated with the installation cavity, and the air extraction outlet is communicated with an air extraction pump.

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