CN214892799U - Composite corrugated plate type heat exchange tower - Google Patents
Composite corrugated plate type heat exchange tower Download PDFInfo
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- CN214892799U CN214892799U CN202121813657.1U CN202121813657U CN214892799U CN 214892799 U CN214892799 U CN 214892799U CN 202121813657 U CN202121813657 U CN 202121813657U CN 214892799 U CN214892799 U CN 214892799U
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Abstract
The utility model discloses a composite corrugated plate type heat exchange tower, which comprises a first connecting pipe, a heat transfer pipe, a second connecting pipe, a baffle plate, a tower body, a third connecting pipe and a fourth connecting pipe, wherein the tower body is of a barrel-shaped structure, a plurality of baffle plates are radially welded inside the tower body, a left pipe plate and a right pipe plate are respectively welded at two ends of the tower body in a sealing way, the heat transfer pipe passes through the left pipe plate and the right pipe plate, the top of the left side of the tower body is welded with the first connecting pipe, the lower part of the right side is welded with the fourth connecting pipe, the left end of the tower body is welded with a left pipe box, the right end of the tower body is welded with a right pipe box, the second connecting pipe is welded on the left pipe box, and the third connecting pipe is welded on the right pipe box; corrugated plates are distributed and welded on the circumference of the outer side of the tower body. The utility model adopts the mode of heat transfer pipe and baffle plate in the product, so that the fluid A carries out sectional type heat exchange on the fluid B; and corrugated plates are distributed and welded on the periphery of the outer side of the tower body corresponding to each section of baffle plate, so that the overall heat dissipation effect is improved.
Description
Technical Field
The utility model relates to a heat exchanger technical field, concretely relates to compound corrugated plate type heat exchange tower.
Background
The heat exchanger is a device for transferring part of heat of hot fluid to cold fluid, and is also called as a heat exchanger. The heat exchanger is an energy-saving device for transferring heat between materials between two or more fluids with different temperatures, and is used for transferring heat from the fluid with higher temperature to the fluid with lower temperature to make the temperature of the fluid reach the index specified by the process so as to meet the requirements of process conditions, and is also one of main devices for improving the utilization rate of energy.
When the existing heat exchange tower or heat exchanger cools the internal fluid, the heat transfer effect is poor, and in order to achieve a better effect, the size of equipment needs to be manufactured greatly sometimes, so that the requirement is met on a small site. After retrieval, a heat exchange tower which can be rapidly cooled and has a small structure is not available at present.
Disclosure of Invention
Technical problem to be solved
In order to solve the problem that exists among the above-mentioned background art, the utility model relates to a can satisfy more efficient cooling heat transfer tower makes the hot-fluid by the cooling can be by another kind of cryogenic fluid rapid cooling, and the low temperature fluid can be through the tower body fast with the air absorption heat on every side, through the buckled plate increase radiating effect, reduce the size of heat transfer tower and to the requirement of cryogenic fluid, can satisfy the demand in horizontal, vertical different places simultaneously.
(II) technical scheme
In order to achieve the above object, the utility model provides a following technical scheme:
the utility model provides a compound ripple board-like heat exchange tower, includes that first takeover, heat-transfer pipe, second takeover, baffling board, tower body, third takeover, fourth takeover, its characterized in that: the tower body is of a barrel-shaped structure, a plurality of baffle plates are radially welded in the tower body, a left tube plate and a right tube plate are respectively welded at two ends of the tower body in a sealing mode, a heat transfer tube penetrates through the left tube plate and the right tube plate and is welded with the left tube plate and the right tube plate in a sealing mode, the top of the left side of the tower body is communicated and welded with a first connecting tube, the lower portion of the right side of the tower body is communicated and welded with a fourth connecting tube, a left tube box is welded at the left end of the tower body, a right tube box is welded at the right end of the tower body, a second connecting tube is welded on the left tube box, and a third connecting tube is welded on the right tube box; corrugated plates are distributed and welded on the circumference of the outer side of the tower body.
As the preferable scheme of the previous step, two ends of the tower body are respectively welded with the left tube plate and the right tube plate in a sealing way to form a fluid A heat exchange space. And the fluid A enters the fluid A heat exchange space from the fourth connecting pipe, passes through a plurality of baffle plates and finally flows out from the first connecting pipe.
In a preferable embodiment of the above step, the second connecting pipe, the left tube box, the left tube plate, the heat transfer tube, the right tube plate, the right tube box, and the third connecting pipe are welded to form a fluid passage B. That is, the fluid B enters the space between the left tube box and the left tube plate from the second connecting tube, flows into the space between the right tube plate and the right tube box from the inside of the heat transfer tube, and finally flows out from the third connecting tube.
As the preferable scheme of the previous step, the corrugated plate is of a solid plate structure.
As the preferable scheme of the previous step, the corrugated plates are of a hollow structure, and the hollow structure is communicated and welded with the interior of the tower body. Compare solid plate structure, the effect that hollow structure's buckled plate played the radiating effect is better.
As a preferable scheme of the previous step, the heat exchange tower is of a horizontal structure, and at least two groups of supporting seats are welded at the bottoms of the left channel box and the right channel box.
As the preferable scheme of the previous step, the heat exchange tower is of a vertical structure, and at least three groups of supporting seats are welded at the bottom of the right tube box or the left tube box.
(III) advantageous effects
The utility model provides a compound corrugated plate type heat exchange tower possesses following beneficial effect:
1. the utility model adopts the mode of heat transfer pipe and baffle plate in the product, so that the fluid A carries out sectional type heat exchange on the fluid B; and corrugated plates are distributed and welded on the periphery of the outer side of the tower body corresponding to each section of baffle plate, so that the overall heat dissipation effect is improved.
2. The utility model discloses the product buckled plate can be solid plate-type, also can be hollow structure, and the welding of interior hollow portion and the inside intercommunication of tower body. The hollow corrugated plate can further play a role in increasing the heat dissipation effect, and can reduce the structural size of the conventional heat exchange tower and the cooling requirement on the fluid A.
3. The utility model discloses the product can be according to on-the-spot place needs, can design for vertical and horizontal two kinds, strong adaptability.
4. The product of the utility model is simple in structure, be convenient for manufacturing and promote, compound corrugated plate heat exchange structure has reduced the slow problem of traditional heat exchange, has improved the accuracy and the efficiency of heat exchange.
Drawings
Fig. 1 is a front view of an embodiment of the present invention;
fig. 2 is a left side view of the embodiment of the present invention;
fig. 3 is a right side view of an embodiment of the present invention;
fig. 4 is a half sectional view of an embodiment of the present invention;
FIG. 5 is a view of an embodiment of the present invention from a-a;
FIG. 6 is a view of the embodiment of the present invention from b to b;
FIG. 7 is a view of an embodiment of the present invention from c to c;
FIG. 8 is a second half sectional view of an embodiment of the present invention;
the heat exchange device comprises a first connecting pipe 1, a first connecting pipe 2, a heat transfer pipe 3, a left pipe box 4, a second connecting pipe 5, a left pipe plate 6, a supporting seat 7, a corrugated plate 8, a baffle plate 9, a tower body 10, a heat exchange space 11, a right pipe plate 12, a right pipe box 13, a third connecting pipe 14 and a fourth connecting pipe.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
The first embodiment is as follows:
as shown in fig. 1-7, the tower body 9 is a barrel-shaped structure, and a plurality of baffle plates 8 and a plurality of heat transfer pipes 2 are welded in the radial direction and in the axial direction inside the tower body. The heat transfer pipe 2 penetrates through the left pipe plate 5 and the right pipe plate 11 to be welded in a sealing mode, the top of the left side of the tower body 9 is welded with the first connecting pipe 1 in a communicating mode, the lower portion of the right side of the tower body 9 is welded with the fourth connecting pipe 14 in a communicating mode, two ends of the tower body 9 are welded with the left pipe plate 5 and the right pipe plate 11 in a sealing mode respectively to form a fluid A heat exchange space 10, namely, fluid A enters the fluid A heat exchange space 10 from the fourth connecting pipe 14, passes through the plurality of baffle plates 8 and finally flows out of the first connecting pipe 1.
The second connecting pipe 4, the left tube box 3, the left tube plate 5, the heat transfer tube 2, the right tube plate 11, the right tube box 12 and the third connecting pipe 13 are welded to form a fluid B channel, namely, the fluid B enters the space between the left tube box 3 and the left tube plate 5 from the second connecting pipe 4, flows into the space between the right tube plate 11 and the right tube box 12 from the inside of the heat transfer tube 2 and finally flows out from the third connecting pipe 13.
The corrugated plates 7 are distributed and welded on the outer side circumference of the tower body 9 corresponding to each section of the baffle plate 8. The corrugated plate 7 can be a solid plate type or a hollow structure, and the hollow part is communicated and welded with the inside of the tower body 9. The corrugated plate 7 plays a role of increasing a heat dissipation effect.
At least two groups of supporting seats 6 are welded at the bottoms of the left channel box 3 and the right channel box 12.
Example two:
as shown in fig. 8, the tower body 9 is a barrel-shaped structure, and a plurality of baffle plates 8 and a plurality of heat transfer pipes 2 are radially welded in the tower body and axially welded in the tower body. The heat transfer pipe 2 penetrates through the left pipe plate 5 and the right pipe plate 11 to be welded in a sealing mode, the top of the left side of the tower body 9 is welded with the first connecting pipe 1 in a communicating mode, the lower portion of the right side of the tower body 9 is welded with the fourth connecting pipe 14 in a communicating mode, two ends of the tower body 9 are welded with the left pipe plate 5 and the right pipe plate 11 in a sealing mode respectively to form a fluid A heat exchange space 10, namely, fluid A enters the fluid A heat exchange space 10 from the fourth connecting pipe 14, passes through the plurality of baffle plates 8 and finally flows out of the first connecting pipe 1.
The second connecting pipe 4, the left tube box 3, the left tube plate 5, the heat transfer tube 2, the right tube plate 11, the right tube box 12 and the third connecting pipe 13 are welded to form a fluid B channel, namely, the fluid B enters the space between the left tube box 3 and the left tube plate 5 from the second connecting pipe 4, flows into the space between the right tube plate 11 and the right tube box 12 from the inside of the heat transfer tube 2 and finally flows out from the third connecting pipe 13.
The corrugated plates 7 are distributed and welded on the outer side circumference of the tower body 9 corresponding to each section of the baffle plate 8. The corrugated plate 7 can be a solid plate type or a hollow structure, and the hollow part is communicated and welded with the inside of the tower body 9. The corrugated plate 7 plays a role of increasing a heat dissipation effect.
At least three sets of supporting seats 6 are welded on the right tube box 12.
The specific implementation process comprises the following steps:
the fluid A enters the fluid A heat exchange space 10 from the fourth connecting pipe 14, passes through a plurality of baffle plates 8 and finally flows out from the first connecting pipe 1. The fluid A baffls in sections, and more sufficient heat dissipation exchange is carried out on each section of heat transfer pipe 2.
The fluid B enters the spaces between the left tube header 3 and the left tube plate 5 from the second connection tube 4, flows into the spaces between the right tube plate 11 and the right tube header 12 from the inside of the heat transfer tube 2, and finally flows out from the third connection tube 13. The fluid B is in a heat exchange space 10 formed by a plurality of baffle plates 8 in a segmented manner, and the heat transfer pipe 2 carries out full heat exchange in a segmented manner, so that the cooling effect is better.
The corrugated plates 7 are distributed and welded on the outer side circumference of the tower body 9 corresponding to each section of the baffle plate 8, and the corrugated plates 7 play a role in increasing the heat dissipation effect. The corrugated plate 7 can be a solid plate type or a hollow structure, the inside of the hollow structure is communicated and welded with the inside of the tower body 9, and the heat dissipation effect is better.
The bottom parts of the left channel box 3 and the right channel box 12 are welded with at least two groups of supporting seats 6 by adopting a horizontal structure.
The bottom of the right tube box 12 is at least welded with three groups of supporting seats 6 by adopting a vertical structure.
The design purpose is achieved.
It is noted that, herein, relational terms such as first and second, and the like may be used solely to distinguish one entity or action from another entity or action without necessarily requiring or implying any actual such relationship or order between such entities or actions. Also, the terms "comprises," "comprising," or any other variation thereof, are intended to cover a non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements does not include only those elements but may include other elements not expressly listed or inherent to such process, method, article, or apparatus. Without further limitation, an element defined by the phrase "comprising an … …" does not exclude the presence of other identical elements in a process, method, article, or apparatus that comprises the element.
Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that changes, modifications, substitutions and alterations can be made in these embodiments without departing from the principles and spirit of the invention, the scope of which is defined in the appended claims and their equivalents. To sum up, the utility model discloses reach anticipated purpose.
Claims (7)
1. The utility model provides a compound ripple board-type heat exchange tower, includes first takeover (1), heat-transfer pipe (2), second takeover (4), baffling board (8), tower body (9), third takeover (13), fourth takeover (14), its characterized in that: the tower body (9) is of a barrel-shaped structure, a plurality of baffle plates (8) are radially welded in the tower body, a left tube plate (5) and a right tube plate (11) are respectively welded at two ends of the tower body (9) in a sealing mode, a heat transfer tube (2) penetrates through the left tube plate (5) and the right tube plate (11) and is welded with the left tube plate (5) and the right tube plate (11) in a sealing mode, a first connecting tube (1) is welded at the top of the left side of the tower body (9) in a communicating mode, a fourth connecting tube (14) is welded at the lower portion of the right side of the tower body (9) in a communicating mode, a left tube box (3) is welded at the left end of the tower body (9), a right tube box (12) is welded at the right end of the tower body (9), a second connecting tube (4) is welded on the left tube box (3), and a third connecting tube (13) is welded on the right tube box (12); corrugated plates (7) are distributed and welded on the outer circumference of the tower body (9).
2. A composite corrugated plate heat exchange column according to claim 1, wherein: two ends of the tower body (9) are respectively welded with the left tube plate (5) and the right tube plate (11) in a sealing mode to form a fluid A heat exchange space (10).
3. A composite corrugated plate heat exchange column according to claim 1, wherein: the second connecting pipe (4), the left pipe box (3), the left pipe plate (5), the heat transfer pipe (2), the right pipe plate (11), the right pipe box (12) and the third connecting pipe (13) are welded to form a fluid channel B.
4. A composite corrugated plate heat exchange column according to claim 1, wherein: the corrugated plate (7) is of a solid plate structure.
5. A composite corrugated plate heat exchange column according to claim 1 or 4, wherein: the corrugated plate (7) is of a hollow structure, and the hollow structure is communicated and welded with the interior of the tower body (9).
6. A composite corrugated plate heat exchange column according to any one of claims 1 to 4, wherein: the heat exchange tower is of a horizontal structure, and at least two groups of supporting seats (6) are welded at the bottoms of the left tube box (3) and the right tube box (12).
7. A composite corrugated plate heat exchange column according to any one of claims 1 to 4, wherein: the heat exchange tower is of a vertical structure, and at least three groups of supporting seats (6) are welded at the bottom of the right tube box (12) or the left tube box (3).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202121813657.1U CN214892799U (en) | 2021-08-05 | 2021-08-05 | Composite corrugated plate type heat exchange tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202121813657.1U CN214892799U (en) | 2021-08-05 | 2021-08-05 | Composite corrugated plate type heat exchange tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN214892799U true CN214892799U (en) | 2021-11-26 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202121813657.1U Active CN214892799U (en) | 2021-08-05 | 2021-08-05 | Composite corrugated plate type heat exchange tower |
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| Country | Link |
|---|---|
| CN (1) | CN214892799U (en) |
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2021
- 2021-08-05 CN CN202121813657.1U patent/CN214892799U/en active Active
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