High-flux heat exchanger for fluid separation

Abstract

The invention discloses a high-flux heat exchanger for fluid separation, and belongs to the field of heat exchangers, the high-flux heat exchanger comprises a shell, one side of the shell is fixedly connected with a partition bin, the middle of the interior of the partition bin is fixedly connected with a partition plate, and the outer surface of the partition bin is symmetrically provided with a first liquid inlet and a first liquid outlet respectively. The two stirring wheels can rotate to stir liquid flowing in the heat exchange tube and high-flow-speed liquid, turbulent flow or local vortex generated by stirring washes the inner wall of the tube, static thermal boundary layers originally attached to the tube wall are mixed, the fluid in the tube is converted into the turbulent flow state from the laminar flow state, and the heat exchange effect is improved. The stirring wheel continuously scrapes the inner wall of the heat exchange tube, dirt on the inner wall of the heat exchange tube is scraped away, the situation that the heat exchange efficiency is low due to dirt accumulation is avoided, the worm wheel can convert potential energy of water flow into mechanical energy, and energy consumption is effectively reduced.

Description

TECHNICAL FIELD

[0001] The present application relates to the field of heat exchangers, more particularly to a high-flux heat exchanger for fluid separation. BACKGROUND

[0002] A heat exchanger is an energy-saving device that transfers heat between two or more fluids at different temperatures, and is one of the main devices for improving energy utilization. It is also known as a heat exchanger and plays an important role in chemical, petroleum, and power industries. It is generally divided into jacketed, plate, shell-and-tube, and double-tube plate types. Among them, the double-tube plate heat exchanger refers to a heat exchanger with two tube plates with a certain gap at one end, which can effectively prevent leakage and material pollution.

[0003] Although the existing heat exchanger can adjust the flow rate of the fluid by rotating the guide vane, the heat exchange tubes on the existing heat exchanger are fixedly distributed on the tank body, so that the heat inside the heat exchange tube can only be quickly exchanged with the surrounding heat exchange fluid during heat exchange. This will cause heat to accumulate around the heat exchange tube, which will cause local overheating or overcooling in the tank body to some extent, thereby affecting the heat exchange quality and efficiency of the heat exchanger. SUMMARY

[0004] In view of the problems in the prior art, the purpose of the present application is to provide a high-flux heat exchanger for fluid separation.

[0005] To solve the above problems, the technical scheme adopted by the present application is as follows.

[0006] A high-flux heat exchanger for fluid separation, comprising a shell, a partition bin fixedly connected to one side of the shell, a partition plate fixedly connected to the inside middle of the partition bin, a first liquid inlet and a first liquid outlet symmetrically arranged on the outer surface of the partition bin, a second liquid inlet fixedly connected to one side of the outer surface of the shell, a second liquid outlet fixedly connected to the other side of the bottom of the outer surface of the shell, a confluence bin fixedly connected to the side of the shell away from the partition bin, a heat exchange tube arranged in the inside of the shell, and an agitating assembly arranged on the top and bottom of the partition plate for fluid agitation.

[0007] The agitating assembly comprises a rotating shaft rotating on one side of the inside of the partition bin, a driving gear rotating on the other side of the inside of the partition bin, and a driving component arranged on the top of the partition plate. One side of the outer surface of the rotating shaft is fixedly connected with a driven gear, both sides of the outer surface of the rotating shaft are fixedly connected with agitating wheels, and the middle of the outer surface of the rotating shaft is fixedly connected with first scrapers. A scraping assembly is arranged in the inside of the shell.

[0008] Further, the driving component comprises a support shaft rotating on the top of the partition plate and a first gear fixed on one side of the driving gear, the top of the support shaft is fixedly connected with a worm gear, the middle of the outer surface of the support shaft is fixedly connected with a crown gear, the crown gear and the first gear are perpendicular to each other, and the crown gear and the first gear are meshed with each other.

[0009] Further, the driving gear is located between the two driven gears, the driving gear and the driven gears are meshed with each other, the worm gear is located directly below the first liquid inlet, and the other worm gear is located above the first liquid outlet.

[0010] Further, the rotating shaft is located in the inside of the heat exchange pipe, the first scraper is attached to the inner wall of the heat exchange pipe, and the first scraper is located between the two stirring wheels.

[0011] Further, the scraping assembly comprises a servo motor fixed on the outer surface of the converging warehouse, a threaded rod fixedly connected to the output end of the servo motor, a moving plate threadedly connected to the outer surface of the threaded rod, four annular rings uniformly arranged on one side of the moving plate, an annular rack fixedly connected to the outer surface of the annular ring, a second scraper fixedly connected to the inner surface of the annular ring, and a rotating component arranged on one side of the moving plate.

[0012] Further, the rotating component comprises a rotating sleeve rotating on one side of the middle of the moving plate and a horizontal shaft fixed on one side of the inside of the shell, a spiral groove is formed in the outer surface of the horizontal shaft, a driving block is fixedly connected to the inside of the rotating sleeve, and a central gear is fixedly connected to one side of the rotating sleeve.

[0013] Further, one side of the threaded rod extends to the inside of the shell, the central gear is meshed with the annular rack, the moving plate is simultaneously sleeved on the outside of the heat exchange pipe, a plurality of flow channels are formed in the inside of the moving plate, and the second scraper is attached to the outer surface of the heat exchange pipe.

[0014] Further, a through hole is formed in the middle of the inside of the driving block, the horizontal shaft is located in the inside of the through hole, the driving block is located in the inside of the spiral groove, and the driving block and the spiral groove are slidably matched with each other.

[0015] Further, the shell is provided with a mixing assembly away from one side of the partition warehouse, the mixing assembly comprises a stirring shaft rotating on the bottom of one side of the shell and a second synchronous gear fixed on the outer surface of the threaded rod, the outer surfaces of the second synchronous gear and the first synchronous gear are sleeved with a synchronous belt, and the outer surface of the stirring shaft is uniformly fixedly connected with stirring vanes.

[0016] Further, the stirring vanes are located in the inside of the converging warehouse, and the stirring shaft is connected with the shell through a bearing.

[0017] Compared with the prior art, the present application has the following advantages:

[0018] 1. The present application has the following advantages:

[0019] 2. The present application has the following advantages:

[0020] 3. The present application has the following advantages: BRIEF DESCRIPTION OF DRAWINGS

[0021] Figure 1 The present application has the following advantages:

[0022] Figure 2 The present application has the following advantages: Figure 1 ;

[0023] Figure 3 The present application has the following advantages: Figure 2 ;

[0024] Figure 4 The present application has the following advantages:

[0025] Figure 5 The present application has the following advantages:

[0026] Figure 6 The present application has the following advantages: Figure 1 ;

[0027] Figure 7Structure diagram of the scraping assembly of the present application Figure 2 ;

[0028] Figure 8 Structure diagram of the scraping assembly of the present application Figure 3 ;

[0029] Figure 9 Structure diagram of the mixing assembly of the present application

[0030] Explanation of the reference numerals in the drawings:

[0031] 1, housing; 2, converging chamber; 3, partition chamber; 4, first liquid inlet; 5, second liquid inlet; 6, second liquid outlet; 7, first liquid outlet;

[0032] 8, stirring assembly; 81, support shaft; 82, crown gear; 83, worm gear; 84, first gear; 85, driven gear; 86, rotating shaft; 87, driving gear;

[0033] 88, scraping assembly; 881, servo motor; 882, threaded rod; 883, moving plate; 884, cross shaft; 885, central gear; 886, annular rack; 887, second scraper; 888, driving block; 889, helical groove; 8810, rotating sleeve; 8811, ring;

[0034] 89, mixing assembly; 891, first synchronous gear; 892, stirring shaft; 893, stirring fan blade; 894, synchronous belt; 895, second synchronous gear;

[0035] 810, stirring wheel; 811, first scraper;

[0036] 9, partition plate; 10, heat exchange pipe. DETAILED DESCRIPTION

[0037] The technical solutions in the embodiments of the present application will be clearly and completely described below with reference to the drawings in the embodiments of the present application. Obviously, the described embodiments are only a part of the embodiments of the present application, rather than all the embodiments of the present application. Based on the embodiments in the present application, all the other embodiments obtained by those of ordinary skill in the art without any creative work fall within the protection scope of the present application.

[0038] Please refer to Figures 1 to 9The utility model provides a high flux heat exchanger for fluid separation, which comprises a shell 1, a partition bin 3 fixedly connected to one side of the shell 1, a partition plate 9 fixedly connected to the middle of the interior of the partition bin 3, a first liquid inlet 4 and a first liquid outlet 7 symmetrically arranged on the outer surface of the partition bin 3, a second liquid inlet 5 fixedly connected to one side of the outer surface of the shell 1, a second liquid outlet 6 fixedly connected to the other side of the bottom of the outer surface of the shell 1, a converging bin 2 fixedly connected to the side of the shell 1 away from the partition bin 3, a heat exchange pipe 10 arranged in the interior of the shell 1, and an agitating assembly 8 arranged on the top and bottom of the partition plate 9 for fluid agitation.

[0039] As shown in the figure, the agitating assembly 8 comprises a rotating shaft 86 rotating on one side of the interior of the partition bin 3, a driving gear 87 rotating on the other side of the interior of the partition bin 3, a driving component arranged on the top of the partition plate 9, a driven gear 85 fixedly connected to one side of the outer surface of the rotating shaft 86, agitating wheels 810 fixedly connected to both sides of the outer surface of the rotating shaft 86, and first scrapers 811 fixedly connected to the middle of the outer surface of the rotating shaft 86 symmetrically, and a scraping assembly 88 arranged in the interior of the shell 1. Figures 2-4

[0040] The driving component comprises a support shaft 81 rotating on the top of the partition plate 9 and a first gear 84 fixedly connected to one side of the driving gear 87, a worm gear 83 fixedly connected to the top of the support shaft 81, and a crown gear 82 fixedly connected to the middle of the outer surface of the support shaft 81, wherein the crown gear 82 and the first gear 84 are perpendicular to each other, and the crown gear 82 and the first gear 84 are engaged with each other.

[0041] The driving gear 87 is located between the two driven gears 85, the driving gear 87 and the driven gears 85 are engaged with each other, one worm gear 83 is located directly below the first liquid inlet 4, and the other worm gear 83 is located above the first liquid outlet 7.

[0042] The rotating shaft 86 is located in the interior of the heat exchange pipe 10, the first scrapers 811 are in close contact with the inner wall of the heat exchange pipe 10, and the first scrapers 811 are located between the two agitating wheels 810.

[0043] During heat exchange, a first group of liquid is introduced into the interior of the partition bin 3 through the first liquid inlet 4, and a second group of liquid is delivered into the interior of the shell 1 through the second liquid inlet 5, the first group of liquid enters the interior of the partition bin 3, flows into the interior of the heat exchange pipe 10, and then flows into the interior of the converging bin 2, and then enters the lower part of the partition bin 3 through the lower heat exchange pipe 10, and is discharged through the first liquid outlet 7, and the second group of liquid is discharged through the second liquid outlet 6, and in this process, the two groups of liquid are subjected to heat exchange.

[0044] ​In the process of heat exchange, the liquid flushes the blades of the worm wheel 83, causing the worm wheel 83 to rotate, the worm wheel 83 drives the crown gear 82 to rotate through the support shaft 81, the crown gear 82 drives the driving gear 87 to rotate at high speed through the first gear 84, the driving gear 87 simultaneously drives the two driven gears 85 to rotate, the driven gears 85 drive the two stirring wheels 810 to rotate through the rotating shaft 86, which can stir the liquid flowing inside the heat exchange pipe 10, can stir the liquid with high flow rate, the turbulence or local vortex generated by stirring can flush the inner wall of the pipe, mix the static thermal boundary layer attached to the pipe wall, and convert the fluid in the pipe from laminar flow to turbulent flow, so that the liquid is in full contact with the inner wall of the heat exchange pipe 10, improving the efficiency of heat exchange, and the stirring wheels 810 continuously scrape the inner wall of the heat exchange pipe 10, which can remove the dirt on the inner wall of the heat exchange pipe 10, avoiding dirt accumulation and causing low heat exchange efficiency. The worm wheel 83 can convert the potential energy of the water flow into mechanical energy, which can effectively save energy consumption.

[0045] As shown in Figures 5-8 The scraping assembly 88 includes a servo motor 881 fixed to the outer surface of the converging bin 2, a threaded rod 882 fixedly connected to the output end of the servo motor 881, a moving plate 883 threadedly connected to the outer surface of the threaded rod 882, four circular rings 8811 uniformly arranged on one side of the moving plate 883, an annular rack 886 fixedly connected to the outer surface of the circular ring 8811, and a second scraper 887 fixedly connected to the inner surface of the circular ring 8811. A rotating part is arranged on one side of the moving plate 883.

[0046] The rotating part includes a rotating sleeve 8810 rotating on one side of the moving plate 883 and a horizontal shaft 884 fixed to one side of the inside of the shell 1, the horizontal shaft 884 has a spiral groove 889 formed on the outer surface, the inside of the rotating sleeve 8810 is fixedly connected with a driving block 888, and one side of the rotating sleeve 8810 is fixedly connected with a central gear 885.

[0047] One side of the threaded rod 882 extends to the inside of the shell 1, the central gear 885 is engaged with the annular rack 886, the moving plate 883 is sleeved on the outside of the heat exchange pipe 10, a plurality of flow channels are formed in the inside of the moving plate 883, and the second scraper 887 is in close contact with the outer surface of the heat exchange pipe 10.

[0048] A through hole is formed in the middle of the inside of the driving block 888, the horizontal shaft 884 is located in the through hole, the driving block 888 is located in the spiral groove 889, and the driving block 888 and the spiral groove 889 are slidably matched.

[0049] In the process of heat exchange, not only the inner wall of the heat exchange pipe 10 is easy to scale, but also the outer surface of the heat exchange pipe 10 in contact with the liquid is easy to scale, which will also reduce the efficiency of heat exchange. At the same time of heat exchange, the servo motor 881 is started to drive the threaded rod 882 to rotate, the threaded rod 882 drives the moving plate 883 to move back and forth in the inside of the shell 1, the moving plate 883 drives the driving block 888 to move through the rotating sleeve 8810. Since the driving block 888 is located in the inside of the spiral groove 889, the driving block 888 slides along the inside of the spiral groove 889, so that the driving block 888 drives the rotating sleeve 8810 to rotate when moving, thereby the rotating sleeve 8810 drives the center gear 885 to rotate, the center gear 885 synchronously drives the four annular racks 886 to rotate, the annular rack 886 drives the plurality of second scrapers 887 to rotate through the circular ring 8811. The second scraper 887 performs circular motion while moving horizontally on the outer surface of the heat exchange pipe 10, and the second scraper 887 scrapes the outer surface of the heat exchange pipe 10, which can remove the dirt on the surface of the heat exchange pipe 10, so that the liquid fully contacts the outer surface of the heat exchange pipe 10. When the moving plate 883 moves in the inside of the shell 1, it can agitate the liquid in the inside of the shell 1, so that the liquid in the inside of the shell 1 fully contacts the heat exchange pipe 10, avoiding the liquid from stratifying due to too fast flow rate, thereby further improving the heat exchange efficiency of the two liquids. The moving plate 883 moves back and forth in the inside of the shell 1, so that the second scraper 887 repeatedly scrapes the surface of the heat exchange pipe 10, effectively increasing the wiping area, thereby ensuring the cleaning effect.

[0050] As shown in Figure 9 The shell 1 away from the side of the partition bin 3 is provided with a mixing assembly 89, the mixing assembly 89 includes a stirring shaft 892 rotating at the bottom of one side of the shell 1 and a second synchronous gear 895 fixed on the outer surface of the threaded rod 882. The outer surface of the second synchronous gear 895 and the outer surface of the first synchronous gear 891 are sleeved with a synchronous belt 894, and the outer surface of the stirring shaft 892 is uniformly fixedly connected with stirring blades 893 on one side.

[0051] The stirring blades 893 are located in the inside of the converging bin 2, and the stirring shaft 892 is connected with the shell 1 through a bearing.

[0052] When the dirt scraped down in the inside of the heat exchange pipe 10 flows synchronously with the liquid, when the liquid enters the inside of the converging bin 2, the dirt will deposit at the bottom of the converging bin 2 due to the action of gravity. If it is not removed in time, it will accumulate more and more, causing the dirt to deposit and accumulate, increasing the difficulty of subsequent cleaning;

[0053] When the threaded rod 882 rotates, the second synchronous gear 895 rotates, the second synchronous gear 895 drives the first synchronous gear 891 to rotate at high speed through the synchronous belt 894, and the first synchronous gear 891 drives the three stirring fans 893 to rotate through the stirring shaft 892. When the liquid carrying dirt inside the heat exchange pipe 10 enters the inside of the collecting bin 2, the dirt cannot be deposited at the bottom of the collecting bin 2 due to the continuous stirring of the stirring fan 893, and also continues to flow with the liquid, so that the dirt cannot stay in the equipment, and the subsequent liquid dirt treatment is more convenient.

[0054] Method for use: when heat exchange, the first group of liquid enters the inside of the separation bin 3 through the first liquid inlet 4, and the second group of liquid is transported into the inside of the shell 1 through the second liquid inlet 5, the first group of liquid enters the inside of the separation bin 3, the liquid enters the inside of the heat exchange pipe 10, and then flows into the inside of the collecting bin 2, and then enters the lower part of the separation bin 3 through the lower heat exchange pipe 10, and is discharged through the first liquid outlet 7, and the second group of liquid is discharged through the second liquid outlet 6, in the process, the two groups of liquid are heat exchanged;

[0055] In the process of heat exchange, the liquid flushes the blades of the worm gear 83, so that the worm gear 83 rotates, the worm gear 83 drives the crown gear 82 to rotate through the support shaft 81, the crown gear 82 drives the driving gear 87 to rotate at high speed through the first gear 84, and the driving gear 87 drives the two driven gears 85 to rotate at the same time, the driven gears 85 drive the two stirring wheels 810 to rotate through the rotating shaft 86, the liquid flowing in the heat exchange pipe 10 can be stirred, the liquid with high flow rate can be stirred, the turbulence or local vortex generated by stirring flushes the inner wall of the pipe, mixes the static thermal boundary layer attached to the pipe wall, and makes the fluid in the pipe from laminar flow to turbulent flow, so that the liquid fully contacts with the inner wall of the heat exchange pipe 10, improves the heat exchange efficiency, and the stirring wheel 810 continuously scrapes the inner wall of the heat exchange pipe 10, which can scrape off the dirt on the inner wall of the heat exchange pipe 10, avoid dirt accumulation, and cause low heat exchange efficiency. At the same time, the potential energy of the water flow is converted into mechanical energy, which can effectively save energy consumption;

[0056] The starting servo motor 881 drives the threaded rod 882 to rotate, and the threaded rod 882 drives the moving plate 883 to move back and forth in the inside of the shell 1. The moving plate 883 drives the driving block 888 to move through the rotating sleeve 8810. Since the driving block 888 is located in the inside of the spiral groove 889, the driving block 888 slides along the spiral groove 889, so that the driving block 888 drives the rotating sleeve 8810 to rotate when moving, thereby the rotating sleeve 8810 drives the center gear 885 to rotate, and the center gear 885 synchronously drives the four annular racks 886 to rotate. The annular rack 886 drives the plurality of second scrapers 887 to rotate through the circular ring 8811. The second scraper 887 moves horizontally on the outer surface of the heat exchange pipe 10 while performing circular motion, and the second scraper 887 scrapes the outer surface of the heat exchange pipe 10, so that the dirt on the surface of the heat exchange pipe 10 is removed, and the liquid fully contacts the outer surface of the heat exchange pipe 10. When the moving plate 883 moves in the inside of the shell 1, the liquid in the inside of the shell 1 is stirred, so that the liquid in the inside of the shell 1 fully contacts the heat exchange pipe 10, and the stratification of the liquid due to too high flow rate is avoided.

[0057] The threaded rod 882 drives the second synchronous gear 895 to rotate at the same time, the second synchronous gear 895 drives the first synchronous gear 891 to rotate at high speed through the synchronous belt 894, and the first synchronous gear 891 drives the three stirring fans 893 to rotate through the stirring shaft 892. When the liquid in the heat exchange pipe 10 enters the inside of the collecting bin 2, and the liquid carrying dirt enters the inside of the collecting bin 2 to gather, the dirt cannot be deposited at the bottom of the collecting bin 2 due to the continuous stirring of the stirring fan 893, and the dirt also continues to flow with the liquid, so that the dirt cannot stay in the equipment, and the subsequent treatment of the dirt in the liquid is more convenient.

[0058] The above describes only the preferred embodiments of the present application; however, the protection scope of the present application is not limited to this. Any person skilled in the art can make equivalent replacements or changes to the technical solution of the present application and the improved concept thereof within the technical range disclosed by the present application, which should be covered in the protection scope of the present application.

Claims

1. A high-throughput heat exchanger for fluid separation, comprising a shell (1), a partition chamber (3) fixedly connected to one side of the shell (1), a partition plate (9) fixedly connected to the middle of the interior of the partition chamber (3), a first liquid inlet (4) and a first liquid outlet (7) symmetrically arranged on the outer surface of the partition chamber (3), a second liquid inlet (5) fixedly connected to one side of the outer surface of the shell (1), a second liquid outlet (6) fixedly connected to the other side of the bottom of the outer surface of the shell (1), a manifold (2) fixedly connected to the side of the shell (1) away from the partition chamber (3), and a heat exchange tube (10) arranged inside the shell (1); Its features are: The top and bottom of the partition plate (9) are provided with agitation components (8) for fluid agitation; The agitation assembly (8) includes a rotating shaft (86) that rotates on one side inside the partition chamber (3), a drive gear (87) that rotates on the other side inside the partition chamber (3), and a drive component set on the top of the partition plate (9). A driven gear (85) is fixedly connected to one side of the outer surface of the rotating shaft (86), and agitation wheels (810) are fixedly connected to both sides of the outer surface of the rotating shaft (86). A first scraper (811) is symmetrically fixedly connected to the middle of the outer surface of the rotating shaft (86), and a scraping assembly (88) is provided inside the housing (1).

2. The high-throughput heat exchanger for fluid separation according to claim 1, characterized in that: The driving component includes a support shaft (81) that rotates on the top of the partition plate (9) and a first gear (84) fixed on one side of the drive gear (87). A worm gear (83) is fixedly connected to the top of the support shaft (81), and a crown gear (82) is fixedly connected to the middle of the outer surface of the support shaft (81). The crown gear (82) and the first gear (84) are perpendicular to each other and mesh with each other.

3. A high-throughput heat exchanger for fluid separation according to claim 2, characterized in that: The driving gear (87) is located between two driven gears (85), and the driving gear (87) and driven gears (85) mesh with each other. The worm gear (83) is located directly below the first liquid inlet (4), and the other worm gear (83) is located above the first liquid outlet (7).

4. A high-throughput heat exchanger for fluid separation according to claim 3, characterized in that: The rotating shaft (86) is located inside the heat exchange tube (10), the first scraper (811) is in contact with the inner wall of the heat exchange tube (10), and the first scraper (811) is located between the two stirring wheels (810).

5. A high-throughput heat exchanger for fluid separation according to claim 4, characterized in that: The scraping assembly (88) includes a servo motor (881) fixed on the outer surface of the manifold (2). The output end of the servo motor (881) is fixedly connected to a threaded rod (882). A movable plate (883) is threadedly connected to the outer surface of the threaded rod (882). Four rings (8811) are evenly rotatably arranged on one side of the movable plate (883). A ring rack (886) is fixedly connected to the outer surface of the rings (8811). A second scraper (887) is evenly fixedly connected to the inner surface of the rings (8811). A rotating component is arranged in the middle of one side of the movable plate (883).

6. A high-throughput heat exchanger for fluid separation according to claim 5, characterized in that: The rotating component includes a rotating sleeve (8810) rotating at the middle of one side of the moving plate (883) and a horizontal shaft (884) fixed inside the housing (1). The outer surface of the horizontal shaft (884) is provided with a spiral groove (889). A driving block (888) is fixedly connected inside the rotating sleeve (8810). A central gear (885) is fixedly connected to one side of the rotating sleeve (8810).

7. A high-throughput heat exchanger for fluid separation according to claim 6, characterized in that: The threaded rod (882) extends into the interior of the housing (1) on one side. The central gear (885) meshes with the annular rack (886). The moving plate (883) is simultaneously sleeved on the outside of the heat exchange tube (10). Multiple flow channels are opened inside the moving plate (883). The second scraper (887) is in contact with the outer surface of the heat exchange tube (10).

8. A high-throughput heat exchanger for fluid separation according to claim 7, characterized in that: A through hole is provided in the middle of the drive block (888), the horizontal axis (884) is located inside the through hole, the drive block (888) is located inside the spiral groove (889), and the drive block (888) and the spiral groove (889) slide and adapt to each other.

9. A high-throughput heat exchanger for fluid separation according to claim 1, characterized in that: A mixing assembly (89) is provided on the side of the housing (1) away from the partition chamber (3). The mixing assembly (89) includes an agitator (892) rotating at the bottom of one side of the housing (1) and a second synchronous gear (895) fixed on the outer surface of the threaded rod (882). A synchronous belt (894) is sleeved on the outer surface of the second synchronous gear (895) and the first synchronous gear (891). Agitator blades (893) are uniformly fixedly connected to one side of the outer surface of the agitator (892).

10. A high-throughput heat exchanger for fluid separation according to claim 9, characterized in that: The agitator blade (893) is located inside the manifold (2), and the agitator shaft (892) is connected to the housing (1) via a bearing.

Images