Low-vibration spiral turbulent flow and two-heat-flow synchronous uniform cooling type heat exchange device

By designing a low vibration, spiral spoiler and the synchronous uniform cold heat exchange device of both heat flows, the problem of two heat flows in the existing heat exchange device cannot be heat exchanged and vibration simultaneously, and the synchronous uniform cold heat exchange of the two heat flows and the vibration damping effect of the device is achieved, improving the heat exchange efficiency and stability.

CN120368749APending Publication Date: 2025-07-25SHANDONG QINGLEI ENVIRONMENTAL SCI & TECH CO LTD
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Patent Information

Application Number
CN202510762210.2
Authority / Receiving Office
CN · China
Patent Type
Applications(China)
Current Assignee / Owner
Filing Date
2025-06-09
Publication Date
2025-07-25

AI Technical Summary

Technical Problem

The existing heat exchange devices have problems such as two types of heat flows that cannot be heat exchanged at the same time, and the two types of heat flows are not easy to control the heat exchange temperature and vibration during operation.

Method used

A low-vibration, spiral spoiler and two heat flows are designed to synchronously uniformly cold heat exchange device, including two heat conveying devices, three-cold heat transfer devices, intercool heat exchange devices, spiral heat exchange devices, turbulent flow generation devices, three-cold mixing devices, and vibration-absorbing support devices. Through the combination of these components, the synchronous heat exchange of the two heat flows, the branch conveying of the cold flow, the efficient heat exchange of the cold and hot flow, the turbulent flow of the heat flow and the vibration-absorbing support of the device are achieved.

Benefits of technology

Synchronous heat exchange between the two heat flows is achieved, cost reduction, consistency of the temperature of the two heat flows is ensured, and vibration of the device is reduced, improving heat exchange efficiency and stability.

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Abstract

The invention provides a low-vibration, spiral turbulent flow and two-heat-flow synchronous uniform cooling type heat exchange device, which belongs to the technical field of heat exchange devices and comprises a two-heat conveying device, a three-cold separate conveying device, an intercooling heat exchange device, a spiral heat exchange device, a turbulent flow generation device, a three-cold uniform mixing device and a vibration reduction supporting device. The device is characterized in that two heat flows exchange heat simultaneously, cold flow is divided into three branches to exchange heat with the heat flows firstly and then exchange heat with each other in a mixed manner, isothermal output participates in heat exchange again, and synchronous and uniform cold heat exchange of the two heat flows is realized. Efficient heat exchange conveying of two heat flows is achieved through the two heat conveying devices, branch conveying of cold flows is achieved through the three cold branch conveying devices, simultaneous heat exchange of the two heat flows of the heat exchanger is achieved through the intercooling heat exchange device, efficient heat exchange of the cold and hot flows is achieved through the spiral heat exchange device, and turbulent flow of the heat flows is achieved through the turbulent flow generating device. Mixing and temperature equalizing of three cold flows are achieved through the three-cold uniform mixing device, and vibration reduction supporting of the heat exchange device is achieved through the vibration reduction supporting device.
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Description

Technical Field

[0001] The present invention relates to a low-vibration, spiral flow disturbance and two-heat-flow synchronous uniform cooling heat exchange device, and particularly to a device that realizes efficient heat exchange and transportation of two heat flows through two heat transportation devices, realizes branched transportation of cold flow through a three-coolant branched transportation device, realizes simultaneous heat exchange of two heat flows in a heat exchanger through an intermediate cooling heat exchange device, realizes efficient heat exchange between hot and cold flows through a spiral heat exchange device, realizes turbulent flow of the heat flow through a turbulent flow generation device, realizes mixing and equalizing of three cold flows through a three-coolant mixing and equalizing device, and realizes vibration damping and support of the heat exchange device through a vibration damping support device, belonging to the technical field of heat exchange devices. Background Art

[0002] A heat exchange device transfers heat from a fluid with a higher temperature to a fluid with a lower temperature, so that the temperature of the fluid reaches the specified index of the process to meet the requirements of process conditions. It is also one of the main devices for improving energy utilization efficiency. However, the currently used heat exchange devices still have the following problems: First, two heat flows cannot be heat-exchanged simultaneously. For example, when heat-exchanging gas-liquid two-phase flows, two sets of heat exchange equipment are required, increasing the cost of heat exchange equipment; Second, it is difficult to control the heat exchange temperature of two heat flows. For example, when heat-exchanging gas-liquid two-phase flows as mentioned in the first problem, due to the different physical properties of gas and liquid in two forms of fluid, it is not easy to make the temperatures of gas-liquid two-phase flows the same after heat exchange through two sets of heat exchange equipment, which will affect the use effect of some special equipment; Third, the vibration during operation is likely to damage the heat exchange equipment.

[0003] Therefore, in view of the problems commonly existing in the current heat exchange devices during use, such as the inability to simultaneously heat-exchange two heat flows, the difficulty in controlling the heat exchange temperature of two heat flows, and the vibration during operation, etc., comprehensive consideration should be given to the working mode and structure of the heat exchange device, and a heat exchange device with two-heat-flow synchronous heat exchange, uniform cooling heat exchange, and low vibration should be designed. Summary of the Invention

[0004] The present invention aims at the problems commonly existing in the current heat exchange devices during use, such as the inability to simultaneously heat-exchange two heat flows, the difficulty in controlling the heat exchange temperature of two heat flows, and the vibration during operation, etc., and provides a low-vibration, spiral flow disturbance and two-heat-flow synchronous uniform cooling heat exchange device that can effectively solve the above problems.

[0005] The following technical solutions are adopted for the low-vibration, spiral flow disturbance and two-heat-flow synchronous uniform cooling heat exchange device of the present invention: A low-vibration, spiral flow-disturbing and two-heat-flow synchronous uniform-cooling heat exchange device, comprising two heat delivery devices, three cold flow distribution devices, a middle cold heat exchange device, a spiral heat exchange device, a turbulence generation device, a three-cold mixing and uniforming device, and a vibration damping and support device. The middle cold heat exchange device is located in the middle of the two heat delivery devices. The spiral heat exchange device, the turbulence generation device and the three-cold mixing and uniforming device are installed in the two heat delivery devices. The three cold flow distribution devices are located at both ends of the two heat delivery devices. The vibration damping and support device is located below the two heat delivery devices. The two heat delivery devices are composed of heat flow pipes, end covers, heat flow inlet A, heat flow inlet B, heat flow outlet A and heat flow outlet B. The end covers are welded to both ends of the heat flow pipes. The heat flow inlet A and the heat flow inlet B are located on the left end cover of the heat flow pipe. The heat flow outlet A and the heat flow outlet B are located on the right end cover of the heat flow pipe. The three cold flow distribution devices are composed of cold flow inlets, shunt pipes, guide pipes, connecting pipes and cold flow outlets. The guide pipes and the connecting pipes are welded to the inner side of the shunt pipes. The cold flow inlets and the cold flow outlets are respectively welded to the outer side of the shunt pipes. The middle cold heat exchange device is composed of cold flow pipes, turbulence plates E and baffles A. The turbulence plates E and the baffles A are welded inside the cold flow pipes. The turbulence plates E are provided with round holes. The spiral heat exchange device is composed of spiral pipes and connecting pipes thereon. The spiral pipes are fixed to the inner wall of the heat flow pipes through support rods A and support rods B. Connecting pipes are respectively welded to the inlet and outlet of the spiral pipes. The turbulence generation device is composed of turbulence plates A, turbulence plates B, turbulence plates C and turbulence plates D. The turbulence plates A are welded to the inner wall of the heat flow pipes. The turbulence plates B are welded to the inner wall of the heat flow pipes and the outer wall of the cold flow pipes. The turbulence plates C and the turbulence plates D are respectively welded to the support rods A. The turbulence plates A and the turbulence plates B are respectively provided with round holes. The three-cold mixing and uniforming device is composed of mixing pipes, turbulence plates F, baffles B and guide plates. The mixing pipes are welded to the outer side of the cold flow pipes. The turbulence plates F and the baffles B are welded inside the mixing pipes. The guide plates are welded inside the cold flow pipes. The vibration damping and support device is composed of brackets, support plates A, support plates B, bases, rubber blocks A and rubber blocks B. The support plates A are welded to the lower end face of the heat flow pipes. The brackets are welded to the lower ends of the support plates A. The support plates B are welded to the inner sides of the brackets. The rubber blocks A are filled between the support plates A and the brackets. The rubber blocks B are filled between the brackets and the support plates B. The bottom ends of the brackets are welded with bases.

[0006] The heat flow pipes are square pipes, the longitudinal sections of the heat flow pipes are rectangular, and the heat flow pipes are welded by steel plates. The heat flow inlet A, the heat flow inlet B, the heat flow outlet A and the heat flow outlet B are respectively welded to the end covers. The cold flow pipes divide the inner space of the heat flow pipes into two independent front and rear regions, and the front and rear regions of the heat flow pipes respectively transport in-phase heat flows or two-phase heat flows.

[0007] The number of the shunt pipes is 2, and they are respectively located on the left and right sides of the heat flow pipe. The shunt pipes are in the shape of round cakes. A cold flow inlet is welded at the center of the outside of the right shunt pipe, a diversion pipe is welded at the center of the inside of the right shunt pipe, and connecting pipes are symmetrically welded to the edges. A cold flow outlet is welded at the center of the outside of the left shunt pipe, a diversion pipe is welded at the center of the inside of the right shunt pipe, and connecting pipes are symmetrically welded to the edges. The diversion pipe and the connecting pipes are respectively welded to the end cover; the structural dimensions of the cold flow inlet and the cold flow outlet are the same, the inner diameters of the connecting pipes and the diversion pipe are equal, and the diameter value of the cold flow inlet is 2 times the diameter value of the connecting pipe.

[0008] The cold flow pipe is formed by two steel plates welded inside the heat flow pipe. The longitudinal section of the cold flow pipe is rectangular, and there are 2 rows and 3 columns of round holes on the steel plates forming the cold flow pipe; the number of baffle plates A is 1 and it is welded in the middle of the cold flow pipe. The number of flow disturbing plates E is 5, 3 flow disturbing plates E are located on the left side of baffle plate A, and 2 flow disturbing plates E are located on the right side of baffle plate A. The round holes on the flow disturbing plates E are distributed in an equally spaced zigzag pattern.

[0009] The spiral pipe is in a rectangular spiral structure. The number of spiral pipes is 16, and 8 spiral pipes are arranged on each side of the cold flow pipe. Every 2 spiral pipes form a group and are connected by a connecting pipe; Support rod A and support rod B are respectively installed on the inner wall of the heat exchange pipe through bolts. There is a buckle A on support rod A and a buckle B on support rod B. Each spiral pipe is respectively provided with 2 horizontally arranged support rods A and 4 vertically arranged support rods B. The buckle A and the buckle B are stuck on the spiral pipe, and the inner diameter value of the spiral pipe is equal to the inner diameter value of the connecting pipe.

[0010] The flow disturbing plates A and B are arranged alternately. The flow disturbing plates A and B are respectively located at the center of adjacent spiral pipes. The flow disturbing plate A faces the connecting pipe connecting the outer ports of the two spiral pipes, and the flow disturbing plate B faces the connecting pipe connecting the inner ports of the two spiral pipes. The length value of the flow disturbing plate A is 2 times the length value of the flow disturbing plate B. There are 3 rows and 3 columns of equally spaced round holes on the flow disturbing plate A, and there is 1 column of equally spaced round holes on the flow disturbing plate B; The flow disturbing plate C is welded to the upper and lower ends of the support column A below the spiral pipe, and the flow disturbing plate D is welded to the lower end of the support column A above the spiral pipe. The flow disturbing plate C is a horizontally long plate, and the flow disturbing plate D is a vertical strip plate.

[0011] The mixing pipe is disk-shaped. The outer end face of the mixing pipe is provided with a chamfered surface. Connecting pipes are respectively welded to the left and right end faces of the mixing pipe; The bottom end of the flow disturbing plate F is welded to the outer wall of the cold flow pipe, and there is a gap between the top end and the mixing pipe. The two ends of the baffle plate B are respectively welded to the outer wall of the cold flow pipe and the inner wall of the mixing pipe. There are round holes of the cold flow pipe on both sides of the flow disturbing plate F and the baffle plate B; The guide plate is located between the baffle plate A and the flow disturbing plate E inside the cold flow pipe. The included angle between the guide plate and the cold flow pipe is 45 degrees. There are round holes of the cold flow pipe on both sides of the guide plate.

[0012] The bracket is of a circular arch structure. The number of support plates A at the upper end of the bracket is 2 and they are symmetrically arranged. The rubber blocks A and B are made of rubber.

[0013] The present invention realizes the efficient heat exchange and transportation of two heat flows through two heat transportation devices, that is, through the heat flow pipes in the two heat transportation devices The front and rear two independent regions respectively transport in-phase heat flows, such as simultaneously transporting liquid heat flows or gaseous heat flows, or simultaneously transporting two-phase heat flows, such as the front region transporting liquid heat flows and the rear region transporting gaseous heat flows. This two-heat-flow synchronous heat exchange device can not only realize the simultaneous heat exchange of two heat flows, but also reduce costs without the need to set up another set of heat exchange equipment.

[0014] The present invention sets the heat flow pipe as a square pipe. Through this design, it is not only convenient for the welding and assembly of the heat flow pipe, but also enables the fluid to form vortices at the square inner corner surfaces, prompting the fluid to flow in a turbulent manner and improving the heat exchange efficiency.

[0015] The present invention realizes the branched transportation of the cold flow through a three-way cold flow distribution device, that is, the cold flow input from the cold flow inlet is transported to the intermediate cold heat exchange device through the diversion pipe in the three-way cold flow distribution device and then transported to the two heat transportation devices through the connecting pipe, so as to realize the three-branch transportation of the cold flow, and heat exchange is carried out through these three branches at the middle part of the entire heat exchange device and at the front and rear two heat flow transportation locations respectively.

[0016] The present invention sets the diameter value of the cold flow inlet as 2 times the diameter value of the connecting pipe. Through this design, it can not only meet the requirement of inputting a large amount of cold flow into the heat exchange device, but also enable the cold flow to be pressurized and output by the diversion pipe through the reduction of the pipe diameter to ensure the stable input of the cold flow into the heat exchange device.

[0017] The present invention realizes the simultaneous heat exchange of two heat flows in the heat exchanger through the intermediate cold heat exchange device, that is, the cold flow pipes in the intermediate cold heat exchange device simultaneously exchange heat with the heat flows in the front and rear two regions of the heat exchange device.

[0018] The present invention is provided with 2 rows and 3 columns of round holes on the steel plate of the cold flow pipe. Through this design, the mixed flow of the cold flow in the cold flow pipe and the mixed flow pipe is realized.

[0019] The present invention is provided with a baffle A in the intermediate cold heat exchange device. Through this design, the interception of the cold flow in the cold flow pipe is realized, prompting the cold flow to flow towards the mixed flow pipe.

[0020] The present invention is provided with round holes distributed in an equal-spacing zigzag pattern on the spoiler E. Through this design, the turbulence of the cold flow is realized, that is, through the round holes distributed in a zigzag pattern, the cold flow is prompted to form turbulence in different directions so that the cold flow can better participate in the heat exchange.

[0021] The present invention realizes efficient heat exchange between cold and hot fluids through a spiral heat exchange device, that is, by extending the residence time of the cold fluid in the heat exchange device through the spiral tube in the spiral heat exchange device, so that the cold fluid can fully participate in heat exchange and improve the heat exchange efficiency.

[0022] The present invention sets the spiral tube as a rectangular spiral winding structure. Through this design, it can not only increase the flow path of the cold fluid to extend the residence time of the cold fluid in the heat exchange device, and the cold fluid moves in a turbulent form in the spiral tube for full heat exchange, but also cover a large area of the longitudinal section of the heat exchange device through this rectangular spiral, so that the heat flows in each area of the heat exchange device can be fully heat exchanged to eliminate the heat exchange blind area; in addition, the heat flow will generate turbulence when passing through the rectangular spiral tube, enabling the heat flows in each small area to all participate in heat exchange to improve the overall heat exchange efficiency.

[0023] The present invention is provided with support rod A and support rod B on the spiral tube. Through this design, it can not only play a role in stably supporting the spiral tube, but also generate turbulence for the passing heat flow through support rod A and support rod B.

[0024] The present invention realizes the turbulent flow of the heat flow through a turbulence generating device, that is, the heat flow in the spoiler tube is disturbed by spoiler plate A, spoiler plate B, spoiler plate C and spoiler plate D in the turbulence generating device to promote the heat flow to form a turbulent flow.

[0025] The present invention sets the length value of spoiler plate A to be twice the length value of spoiler plate B. Through this design, it is not only convenient for the arrangement of spoiler plate A and spoiler plate B between adjacent spiral tubes, but also can realize fluid disturbance in a large area.

[0026] The present invention is provided with round holes on spoiler plate A and spoiler plate B. Through this design, part of the heat flow flows out through the round holes and impacts the heat flow behind spoiler plate A and spoiler plate B, changing the flow state of the subsequent fluid, increasing the turbulent flow, and promoting the full heat exchange between the heat flow and the cold fluid in the spiral tube.

[0027] The present invention is provided with spoiler plate C and spoiler plate D on support pillar A. Through this design, the heat flow passing through the spiral tube is disturbed to promote its turbulent motion.

[0028] The present invention realizes the mixing and equalizing of three cold fluid streams through a three - cold - mixing and equalizing device, that is, the cold fluid streams in the front and rear regions of the heat flow tube and the cold fluid in the cold fluid tube, these three cold fluid streams are mixed through the mixing tube in the three - cold - mixing and equalizing device, and the three cold fluid streams exchange heat with each other during mixing, and flow out of the mixing tube in a uniform isothermal state, and perform isothermal heat exchange with the heat flows in the front and rear regions of the subsequent heat flow tube, ensuring synchronous and isothermal heat exchange of the heat flows in the two regions.

[0029] The present invention is provided with a chamfered surface on the outer end face of the mixing tube. Through this design, the cold The flowing hot stream and the cold stream flowing out of the mixing pipe through the connecting pipe play a role in guiding the flow.

[0030] In the present invention, a gap is provided between the spoiler plate F and the mixing pipe. Through this design, the cold stream flowing in from the connecting pipe and the cold stream flowing in through the round holes of the cold stream pipe are mixed, and flow through the gap between the spoiler plate F and the mixing pipe to the area between the spoiler plate F and the baffle plate B, so that the cold streams can be fully mixed and heat-exchanged. In the present invention, the angle between the deflector plate and the cold stream pipe is set to 45 degrees. Through this design, it can not only guide the mixed cold stream between the baffle plate A and the spoiler plate E, but also play a role in disturbing the mixed cold stream, causing the cold stream to form a vortex flow, promoting full heat exchange between the cold streams, and flowing out in an isothermal form. In the present invention, the vibration damping support of the heat exchange device is realized through the vibration damping support device, that is, the heat exchange device is supported by the bracket, the support plate A, the support plate B and the base in the vibration damping support device, and the impact vibration is absorbed by the rubber block A and the rubber block B to prevent the heat exchange device from being damaged by vibration.

[0031] In the present invention, the bracket is designed as a circular arch structure. Through this design, the force on the bracket is dispersed and directed towards the center of the arch-shaped bracket, improving the load-bearing capacity of the bracket.

[0032] In the present invention, the support plate B is welded to the inner side of the bracket. Through this design, the compressive strength of the bracket is improved.

[0033] In the present invention, the rubber block A and the rubber block B are respectively filled at the upper and lower ends of the bracket. Through this design, not only can the vibration energy of the heat exchange device be absorbed and consumed, but also the vibration of the bottom surface can be prevented from being transmitted to the heat exchange device; in addition, the rubber block A and the rubber block B also support the bracket to prevent the bracket from being deformed by force.

[0034] The beneficial effects of the present invention are as follows: the efficient heat exchange and transportation of two hot streams are realized through two heat transportation devices, the branched transportation of cold streams is realized through three cold sub-transportation devices, the simultaneous heat exchange of two hot streams of the heat exchanger is realized through the intermediate cold heat exchange device, the efficient heat exchange between hot and cold streams is realized through the spiral heat exchange device, the turbulent flow of the hot stream is realized through the turbulent flow generating device, the mixing and equalizing of three cold streams are realized through the three cold mixing and equalizing device, and the vibration damping support of the heat exchange device is realized through the vibration damping support device.

[0035] BRIEF DESCRIPTION OF THE DRAWINGS BRIEF DESCRIPTION OF THE DRAWINGS

[0036] Figure 1 It is a schematic top view of the overall structure of the present invention.

[0037] Figure 2 It is a schematic partial structure view of the three cold sub-transportation device of the present invention.

[0038] Figure 3It is a schematic diagram of the local fluid motion of the intercooling heat exchange device of the present invention.

[0039] Figure 4 It is a schematic diagram of the local fluid motion of the spiral heat exchange device and the turbulence generating device of the present invention.

[0040] Figure 5 It is a schematic diagram of the local structure of the spiral heat exchange device of the present invention.

[0041] Figure 6 It is a schematic diagram of the structure of the spiral tube and the connecting tube of the present invention.

[0042] Figure 7 It is a schematic diagram of the structure of the support rod A of the present invention.

[0043] Figure 8 It is a schematic diagram of the structure of the support rod B of the present invention.

[0044] Figure 9 It is a schematic diagram of the structure of the spoiler A of the present invention.

[0045] Figure 10 It is a schematic diagram of the structure of the spoiler B of the present invention.

[0046] Figure 11 It is a schematic diagram of the local fluid motion of the triple-cooling mixing device of the present invention.

[0047] Figure 12 It is a schematic diagram of the local structure of the cold flow tube and the hot flow tube of the present invention.

[0048] Figure 13 It is a schematic diagram of the structure of the vibration damping support device of the present invention.

[0049] Wherein: 1. Hot flow outlet B, 2. Support, 3. Hot flow tube, 4. Mixing tube, 5. Spoiler A, 6. Spoiler B, 7. Spiral tube, 8. Hot flow inlet B, 9. Shunt tube, 10. Cold flow outlet, 11. Hot flow inlet A, 12. End cover, 13. Hot flow outlet A, 14. Cold flow tube, 15. Cold flow inlet, 16. Connecting tube, 17. Support rod A, 18. Support rod B, 19. Spoiler C, 20. Spoiler D, 21. Round hole, 22. Spoiler E, 23. Diversion tube, 24. Baffle A, 25. Deflector, 26. Spoiler F, 27. Baffle B, 28. Snap A, 29. Snap B, 30. Base, 31. Support plate B, 32. Rubber block B, 33. Support plate A, 34. Rubber block A. Detailed implementation manners

[0050] As Figure 1As shown in the figure, a low-vibration, spiral flow disturbance and two-heat-flow synchronous uniform cooling type heat exchange device of the present invention includes two heat delivery devices, three cold distribution devices, a middle cold heat exchange device, a spiral heat exchange device, a turbulence generation device, a three-cold mixing and averaging device, and a vibration damping support device. The middle cold heat exchange device is located in the middle of the two heat delivery devices. The spiral heat exchange device, the turbulence generation device, and the three-cold mixing and averaging device are installed in the two heat delivery devices. The three cold distribution devices are located at both ends of the two heat delivery devices. The vibration damping support device is located below the two heat delivery devices.

[0051] The two heat delivery devices are composed of a heat flow pipe 3, end caps 12, a heat flow inlet A11, a heat flow inlet B8, a heat flow outlet A13, and a heat flow outlet B1. The end caps 12 are welded to both ends of the heat flow pipe 3. The heat flow inlet A11 and the heat flow inlet B8 are located on the left end cap 12 of the heat flow pipe 3. The heat flow outlet A13 and the heat flow outlet B1 are located on the right end cap 12 of the heat flow pipe 3.

[0052] The heat flow pipe 3 is a square pipe. The longitudinal section of the heat flow pipe 3 is rectangular. The heat flow pipe 3 is welded by steel plates. The heat flow inlet A11, the heat flow inlet B8, the heat flow outlet A13, and the heat flow outlet B1 are respectively welded to the end cap 12. The cold flow pipe 14 divides the space inside the heat flow pipe 3 into two independent front and rear regions. The front and rear regions of the heat flow pipe 3 respectively transport in-phase heat flows or two-phase heat flows.

[0053] The present invention realizes the efficient heat exchange and transportation of two heat flows through the two heat delivery devices, that is, through the two heat delivery devices The two independent front and rear regions of the heat flow pipe 3 in the two heat delivery devices respectively transport in-phase heat flows, such as transporting liquid heat flows or gaseous heat flows at the same time, or transporting two-phase heat flows at the same time, such as transporting liquid heat flows in the front region and gaseous heat flows in the rear region. This two-heat-flow synchronous heat exchange device can not only realize the simultaneous heat exchange of two heat flows, but also reduce costs without the need to set up another set of heat exchange equipment.

[0054] The present invention sets the heat flow pipe 3 as a square pipe. Through this design, it is not only convenient for the welding and assembly of the heat flow pipe 3, but also can make the fluid form vortices at the square inner corner surfaces, prompting the fluid to flow in a turbulent manner and improving the heat exchange efficiency.

[0055] Combined Figure 2 As shown in the figure, the three cold distribution devices are composed of a cold flow inlet 15, a shunt pipe 9, a diversion pipe 23, a connecting pipe 16, and a cold flow outlet 10. The diversion pipe 23 and the connecting pipe 16 are welded to the inner side of the shunt pipe 9. The cold flow inlet 15 and the cold flow outlet 10 are respectively welded to the outer side of the shunt pipe 9.

[0056] There are two flow dividers 9, which are respectively located on the left and right sides of the hot flow pipe 3. The flow divider 9 has a disc-shaped structure. In the middle of the outside of the right flow divider 9, a cold flow inlet 15 is welded. In the middle of the inside of the right flow divider 9, a guide pipe 23 is welded, and connecting pipes 16 are symmetrically welded to the edge. In the middle of the outside of the left flow divider 9, a cold flow outlet 10 is welded. In the middle of the inside of the right flow divider 9, a guide pipe 23 is welded, and connecting pipes 16 are symmetrically welded to the edge. The guide pipe 23 and the connecting pipes 16 are respectively welded to the end cover 12; the structural dimensions of the cold flow inlet 15 and the cold flow outlet 10 are the same, the inner diameters of the connecting pipes 16 and the guide pipe 23 are equal, and the diameter value of the cold flow inlet 15 is twice the diameter value of the connecting pipes 16.

[0057] The present invention realizes the branched transportation of cold flow through the three-cold subtransmission device, that is, the cold flow input from the cold flow inlet 15 is transported to the intermediate cold heat exchange device through the guide pipe 23 by the flow divider 9 in the three-cold subtransmission device, and is transported to the two hot transportation devices through the connecting pipes 16, so as to realize the transportation of three branches of cold flow, and heat exchange is carried out through these three branches at the middle part and the front and rear hot flow transportation parts of the whole heat exchange device respectively.

[0058] The present invention sets the diameter value of the cold flow inlet 15 to be twice the diameter value of the connecting pipes 16. Through this design, it can not only meet the input of a large amount of cold flow into the heat exchange device, but also increase the pressure of the cold flow output by the flow divider 9 by reducing the pipe diameter, so as to ensure the stable input of cold flow into the heat exchange device.

[0059] Combined Figure 3 As shown, the intermediate cold heat exchange device is composed of a cold flow pipe 14, a spoiler E22 and a baffle A24. The spoiler E22 and the baffle A24 are welded inside the cold flow pipe 14, and round holes 21 are provided on the spoiler E22.

[0060] The cold flow pipe 14 is formed by two steel plates welded inside the hot flow pipe 3. The longitudinal section of the cold flow pipe 14 is rectangular, and 2 rows and 3 columns of round holes 21 are provided on the steel plates forming the cold flow pipe 14; the number of baffles A24 is 1 and it is welded in the middle of the cold flow pipe 14. The number of spoilers E22 is 5. 3 spoilers E22 are located on the left side of the baffle A24, and 2 spoilers E22 are located on the right side of the baffle A24. The round holes 21 on the spoiler E22 are distributed in an equidistant zigzag pattern.

[0061] The present invention realizes the simultaneous heat exchange of the two hot flows of the heat exchanger through the intermediate cold heat exchange device, that is, the cold flow pipe 14 in the intermediate cold heat exchange device simultaneously exchanges heat with the hot flows in the front and rear regions of the heat exchange device.

[0062] The present invention provides 2 rows and 3 columns of round holes 21 on the steel plates of the cold flow pipe 14. Through this design, the mixed flow of the cold flow in the cold flow pipe 14 and the mixed flow pipe 4 is realized.

[0063] The present invention is provided with a baffle A24 in the intercooling heat exchange device. Through this design, the interception of the cold flow in the cold flow pipe 14 is realized, and the cold flow is promoted to flow towards the mixing pipe 4.

[0064] The present invention is provided with circular holes 21 distributed in a zigzag pattern at equal intervals on the spoiler E22. Through this design, the turbulence of the cold flow is realized, that is, through the circular holes 21 distributed in a zigzag pattern, the cold flow is promoted to form turbulence in different directions, so that the cold flow can better participate in heat exchange.

[0065] Combined Figure 4 、 Figure 5 、 Figure 6 、 Figure 7 and Figure 8 As shown in

[0066] 、

[0067] The present invention realizes the efficient heat exchange between the hot and cold flows through the spiral heat exchange device, that is, the residence time of the cold flow in the heat exchange device is extended through the spiral pipe 7 in the spiral heat exchange device, so that the cold flow can fully participate in heat exchange and improve the heat exchange efficiency.

[0068] The present invention sets the spiral pipe 7 to be in a rectangular spiral winding structure. Through this design, not only can the flow path of the cold flow be increased, so that the residence time of the cold flow in the heat exchange device is extended, and the cold flow moves in a turbulent form in the spiral pipe 7 for full heat exchange, but also a large area of the longitudinal section of the heat exchange device can be covered by this rectangular spiral, so that the heat flows in each area of the heat exchange device can be fully heat exchanged to eliminate the heat exchange blind area; in addition, the hot flow will generate turbulence when passing through the rectangular spiral pipe 7, so that the heat flows in each small area can all participate in heat exchange to improve the overall heat exchange efficiency.

[0069] The present invention is provided with a support rod A17 and a support rod B18 on the spiral pipe 7. Through this design, not only can the spiral pipe 7 be stably supported, but also the turbulence of the hot flow passing through can be generated by the support rod A17 and the support rod B18.

[0070] Combined Figure 9 andFigure 10 As shown, the turbulence generating device is composed of spoiler A5, spoiler B6, spoiler C19 and spoiler D20. Spoiler A5 is welded to the inner wall of the heat flow tube 3, spoiler B6 is welded to the inner wall of the heat flow tube 3 and the outer wall of the cold flow tube 14, spoiler C19 and spoiler D20 are respectively welded to the support rod A17, and round holes 21 are respectively provided on spoiler A5 and spoiler B6; Spoiler A5 and spoiler B6 are arranged alternately. Spoiler A5 and spoiler B6 are respectively located at the center of adjacent spiral tubes 7. Spoiler A5 faces the connecting tube 16 connecting the outer ports of the two spiral tubes 7, and spoiler B6 faces the connecting tube 16 connecting the inner ports of the two spiral tubes 7. The length value of spoiler A5 is twice the length value of spoiler B6. There are 3 rows and 3 columns of equally spaced round holes 21 on spoiler A5, and 1 column of equally spaced round holes 21 on spoiler B6; Spoiler C19 is welded to the upper and lower ends of the support A below the spiral tube 7, and spoiler D20 is welded to the lower end of the support A above the spiral tube 7. Spoiler C19 is a horizontally long plate, and spoiler D20 is a vertical strip plate.

[0071] The present invention realizes the turbulent flow of the heat flow through the turbulence generating device, that is, the heat flow in the spoiler tube is disturbed by spoiler A5, spoiler B6, spoiler C19 and spoiler D20 in the turbulence generating device, so as to promote the heat flow to form a turbulent flow.

[0072] The present invention sets the length value of spoiler A5 to be twice the length value of spoiler B6. Through this design, it is not only convenient for the arrangement of spoiler A5 and spoiler B6 between adjacent spiral tubes 7, but also can realize the fluid disturbance in a larger area.

[0073] The present invention is provided with round holes 21 on spoiler A5 and spoiler B6. Through this design, part of the heat flow flows out through the round holes 21, impacts the heat flow behind spoiler A5 and spoiler B6, changes the flow state of the fluid behind, increases the turbulent flow, and promotes the full heat exchange between the heat flow and the cold flow in the spiral tube 7.

[0074] The present invention is provided with spoiler C19 and spoiler D20 on the support A. Through this design, the heat flow flowing through the spiral tube 7 is disturbed to promote its turbulent motion.

[0075] Combined Figure 11 and Figure 12 As shown, the three-cooling mixing and homogenizing device is composed of a mixing tube 4, a spoiler F26, a baffle B27 and a deflector 25. The mixing tube 4 is welded to the outer side of the cold flow tube 14, the spoiler F26 and the baffle B27 are welded inside the mixing tube 4, and the deflector 25 is welded inside the cold flow tube 14.

[0076] The mixing flow tube 4 is disc-shaped, and a chamfered surface is provided on the outer end surface of the mixing flow tube 4. Connecting tubes 16 are respectively welded to the left and right end surfaces of the mixing flow tube 4; the bottom end of the spoiler F26 is welded to the outer wall of the cold flow tube 14 and there is a gap between the top end and the mixing flow tube 4. The two ends of the baffle B27 are respectively welded to the outer wall of the cold flow tube 14 and the inner wall of the mixing flow tube 4. There are round holes 21 of the cold flow tube 14 on both sides of the spoiler F26 and the baffle B27; the guide vane 25 is located between the baffle A24 and the spoiler E22 inside the cold flow tube 14. The included angle between the guide vane 25 and the cold flow tube 14 is 45 degrees. There are round holes 21 of the cold flow tube 14 on both sides of the guide vane 25.

[0077] In the present invention, the three-way cold flow mixing and temperature equalizing device realizes the mixing and temperature equalizing of three cold flows, that is, the cold flows in the front and rear regions of the hot flow tube 3 and the cold flow inside the cold flow tube 14 are mixed through the mixing flow tube 4 in the three-way cold flow mixing and temperature equalizing device. These three cold flows exchange heat with each other during the mixing process, and then flow out of the mixing flow tube 4 in a uniform and isothermal state, and perform isothermal heat exchange with the hot flows in the front and rear regions of the subsequent hot flow tube 3, ensuring synchronous and isothermal heat exchange of the hot flows in the two regions.

[0078] In the present invention, a chamfered surface is provided on the outer end surface of the mixing flow tube 4. Through this design, it plays a guiding role for the cold flow flowing into the mixing flow tube through the connecting tube 16 and the cold flow flowing out of the mixing flow tube 4 through the connecting tube 16.

[0079] In the present invention, a gap is provided between the spoiler F26 and the mixing flow tube 4. Through this design, the cold flow flowing in through the connecting tube 16 and the cold flow flowing in through the round hole 21 of the cold flow tube 14 are mixed, and flow through the gap between the spoiler F26 and the mixing flow tube 4 to the region between the spoiler F26 and the baffle B27, so that the cold flows can be fully mixed and heat exchanged.

[0080] In the present invention, the included angle between the guide vane 25 and the cold flow tube 14 is set to 45 degrees. Through this design, it can not only guide the mixed cold flow between the baffle A24 and the spoiler E22, but also play a role in disturbing the mixed cold flow, making the cold flow form a vortex flow, promoting full heat exchange between the cold flows, and flowing out in an isothermal form. Figure 13 Combined

[0081] As shown in the figure, the vibration damping support device is composed of a bracket 2, a support plate A33, a support plate B31, a base 30, a rubber block A34 and a rubber block B32. The support plate A33 is welded to the lower end surface of the hot flow tube 3. The bracket 2 is welded to the lower end of the support plate A33. The support plate B31 is welded to the inner side of the bracket 2. The rubber block A34 is filled between the support plate A33 and the bracket 2. The rubber block B32 is filled between the bracket 2 and the support plate B31. The bottom end of the bracket 2 is welded with the base 30.

[0081] The support 2 is of a circular arch structure. The number of support plates A33 at the upper end of the support 2 is 2 and they are symmetrically arranged. The rubber block A34 and the rubber block B32 are made of rubber.

[0082] The present invention realizes the vibration damping support of the heat exchange device through the vibration damping support device, that is, the support 2, the support plate A33, the support plate B31 and the base 30 in the vibration damping support device play a supporting role on the heat exchange device, and the rubber block A34 and the rubber block B32 absorb the impact vibration to prevent the heat exchange device from vibrating and being damaged.

[0083] The present invention sets the support 2 as a circular arch structure. Through this design, the force on the support 2 is dispersed and directed towards the center of the arch-shaped support 2, improving the bearing capacity of the support 2.

[0084] The present invention welds the support plate B31 on the inner side of the support 2. Through this design, the compressive strength of the support 2 is improved.

[0085] The present invention fills the rubber block A34 and the rubber block B32 at the upper and lower ends of the support 2 respectively. Through this design, not only can the vibration energy of the heat exchange device be absorbed and consumed, but also the vibration of the bottom surface can be prevented from being transmitted to the heat exchange device; in addition, the rubber block A34 and the rubber block B32 also play a supporting role on the support 2 to prevent the support 2 from deforming under force.

Claims

1. A low-vibration, spiral-flow-disturbing and two-heat-flow-synchronized and evenly-cooled heat exchange device, comprising two heat delivery devices, three cold distribution devices, a middle cold heat exchange device, a spiral heat exchange device, a turbulence generation device, a three-cold mixing and equalizing device, and a vibration damping and support device. The middle cold heat exchange device is located in the middle of the two heat delivery devices. The spiral heat exchange device, the turbulence generation device and the three-cold mixing and equalizing device are installed in the two heat delivery devices. The three cold distribution devices are located at both ends of the two heat delivery devices. The vibration damping and support device is located below the two heat delivery devices. It is characterized in that: The two heat transfer devices are composed of heat flow pipes, end caps, heat flow inlet A, heat flow inlet B, heat flow outlet A and heat flow outlet B. The end caps are welded to both ends of the heat flow pipes. Heat flow inlet A, heat flow inlet B are located on the left end cap of the heat flow pipe, and heat flow outlet A and heat flow outlet B are located on the right end cap of the heat flow pipe. The three cold distribution devices are composed of a cold flow inlet, a flow dividing pipe, a guiding pipe, a connecting pipe and a cold flow outlet. The guiding pipe and the connecting pipe are welded inside the flow dividing pipe. The cold flow inlet and the cold flow outlet are respectively welded outside the flow dividing pipe. The intermediate cold heat exchange device is composed of a cold flow pipe, a turbulence plate E and a baffle A. The turbulence plate E and the baffle A are welded inside the cold flow pipe, and the turbulence plate E is provided with round holes. The spiral heat exchange device is composed of a spiral pipe and the connecting pipes thereon. The spiral pipe is fixed on the inner wall of the heat flow pipe through support rod A and support rod B. Connecting pipes are respectively welded at the inlet and outlet of the spiral pipe. The turbulence generating device is composed of a turbulence plate A, a turbulence plate B, a turbulence plate C and a turbulence plate D. The turbulence plate A is welded on the inner wall of the heat flow pipe. The turbulence plate B is welded on the inner wall of the heat flow pipe and the outer wall of the cold flow pipe. The turbulence plate C and the turbulence plate D are respectively welded on the support rod A. Round holes are respectively provided on the turbulence plate A and the turbulence plate B. The three cold mixing and equalizing devices are composed of a mixing pipe, a turbulence plate F, a baffle B and a guiding plate. The mixing pipe is welded on the outer side surface of the cold flow pipe. The turbulence plate F and the baffle B are welded inside the mixing pipe. The guiding plate is welded inside the cold flow pipe. The vibration damping and support device is composed of a bracket, a support plate A, a support plate B, a base, a rubber block A and a rubber block B. The support plate A is welded on the lower end surface of the heat flow pipe. The bracket is welded at the lower end of the support plate A. The support plate B is welded inside the bracket. The rubber block A is filled between the support plate A and the bracket. The rubber block B is filled between the bracket and the support plate B. The bottom end of the bracket is welded with a base.

2. A low-vibration, spiral flow disturbance and two heat flow synchronous uniform cooling type heat exchange device according to claim 1, characterized in that: The heat flow pipe is a square pipe. The longitudinal section of the heat flow pipe is rectangular. The heat flow pipe is welded by steel plates. Heat flow inlet A, heat flow inlet B, heat flow outlet A and heat flow outlet B are respectively welded on the end caps. The cold flow pipe divides the inner space of the heat flow pipe into two independent front and rear regions. The front and rear regions of the heat flow pipe respectively transport in-phase heat flow or two-phase heat flow.

3. The low-vibration, spiral flow disturbance and two heat flow synchronous uniform cooling type heat exchange device according to claim 1, characterized in that: The number of the flow dividing pipes is 2 and they are respectively located on the left and right sides of the heat flow pipe. The flow dividing pipes are of a round cake-shaped structure. The cold flow inlet is welded in the middle of the outer side of the right flow dividing pipe. The guiding pipe is welded in the middle of the inner side of the right flow dividing pipe and connecting pipes are symmetrically welded at the edge. The cold flow outlet is welded in the middle of the outer side of the left flow dividing pipe. The guiding pipe is welded in the middle of the inner side of the right flow dividing pipe and connecting pipes are symmetrically welded at the edge. The guiding pipe and the connecting pipes are respectively welded on the end caps. The structural dimensions of the cold flow inlet and the cold flow outlet are the same. The inner diameters of the connecting pipe and the guiding pipe are equal. The diameter value of the cold flow inlet is 2 times the diameter value of the connecting pipe.

4. A low-vibration, spiral flow disturbance, and two heat flow synchronous uniform cooling type heat exchange device according to claim 1, characterized in that: The cold flow pipe is formed by two steel plates welded inside the heat flow pipe. The longitudinal section of the cold flow pipe is rectangular. The steel plates forming the cold flow pipe are provided with round holes in 2 rows and 3 columns. The number of the baffle A is 1 and it is welded in the middle of the cold flow pipe. The number of the turbulence plates E is 5. 3 turbulence plates E are located on the left side of the baffle A and 2 turbulence plates E are located on the right side of the baffle A. The round holes on the turbulence plate E are distributed in an equally spaced zigzag manner.

5. A low-vibration, spiral flow disturbance and two heat flows synchronous and uniform cooling type heat exchange device according to claim 1, characterized in that: The spiral tube has a rectangular spiral structure, and the number of spiral tubes is 16. Eight spiral tubes are arranged on each side of the cold flow tube, and every two spiral tubes form a group and are connected by a connecting tube; The support rod A and the support rod B are respectively installed on the inner wall of the heat exchange tube by bolts. There is a buckle A on the support rod A and a buckle B on the support rod B. Each spiral tube is respectively provided with two horizontally arranged support rods A and four vertically arranged support rods B. The buckle A and the buckle B are clamped on the spiral tube, and the inner diameter value of the spiral tube is equal to the inner diameter value of the connecting tube.

6. The low-vibration, spiral flow disturbance and two heat flow synchronous and uniform cooling type heat exchange device according to claim 1, characterized in that: The spoiler A and the spoiler B are arranged alternately. The spoiler A and the spoiler B are respectively located at the center of adjacent spiral tubes. The spoiler A faces the connecting tube connecting the outer ports of the two spiral tubes, and the spoiler B faces the connecting tube connecting the inner ports of the two spiral tubes. The length value of the spoiler A is twice the length value of the spoiler B. The spoiler A is provided with 3 rows and 3 columns of equally spaced round holes, and the spoiler B is provided with 1 column of equally spaced round holes; The spoiler C is welded to the upper and lower ends of the support column A below the spiral tube, and the spoiler D is welded to the lower end of the support column A above the spiral tube. The spoiler C is a horizontally long plate, and the spoiler D is a vertical strip plate.

7. A low-vibration, spiral flow disturbance and two heat flow synchronous uniform cooling type heat exchange device according to claim 1, characterized in that: The mixing tube is disc-shaped, and the outer end face of the mixing tube is provided with a chamfered surface. Connecting tubes are respectively welded to the left and right end faces of the mixing tube; The bottom end of the spoiler F is welded to the outer wall of the cold flow tube and there is a gap between the top end and the mixing tube. Both ends of the baffle B are respectively welded to the outer wall of the cold flow tube and the inner wall of the mixing tube. There are round holes of the cold flow tube on both sides of the spoiler F and the baffle B; The flow guide plate is located between the baffle A and the spoiler E in the cold flow tube. The included angle between the flow guide plate and the cold flow tube is 45 degrees, and there are round holes of the cold flow tube on both sides of the flow guide plate.

8. A low-vibration, spiral flow disturbance and two heat flow synchronous uniform cooling type heat exchange device according to claim 1, characterized in that: The bracket has a circular arch structure. The number of the support plates A at the upper end of the bracket is 2 and they are symmetrically arranged. The rubber block A and the rubber block B are made of rubber.