CN218764743U - Chemical heat exchanger with porous tube plate - Google Patents
Chemical heat exchanger with porous tube plate Download PDFInfo
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- CN218764743U CN218764743U CN202222660189.XU CN202222660189U CN218764743U CN 218764743 U CN218764743 U CN 218764743U CN 202222660189 U CN202222660189 U CN 202222660189U CN 218764743 U CN218764743 U CN 218764743U
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- baffle
- shell
- heat exchanger
- sealed lid
- closing plate
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Abstract
The utility model belongs to the technical field of the heat exchanger technique and specifically relates to a chemical industry heat exchanger with porous tube sheet, which comprises an outer shell, the both sides at shell both ends all are provided with the connecting seat, shell one side bottom intercommunication has the feed liquor pipe, shell one side top intercommunication has the drain pipe, the shell both ends all are provided with sealed lid, two the relative outside of sealed lid all communicates there is the connecting pipe, two sealed lid with all be provided with the closing plate between the shell, two the intercommunication has a plurality of pipelines, one of them between the closing plate is provided with the baffle in the sealed lid, the outer lane of baffle with there is the space between the inner wall of sealed lid, the baffle is close to a plurality of pipeline one side all is provided with a plurality of stock, and is a plurality of all be provided with a plurality of brush posts on the stock, baffle and one of it is provided with coupling mechanism between the closing plate. The device has very high practical value, is worth promoting.
Description
Technical Field
The utility model relates to a heat exchanger technical field especially relates to a chemical industry heat exchanger with porous tube sheet.
Background
In chemical production, a lot of substances take place that chemical reaction can release a large amount of heat, makes the liquid temperature that the reaction gets very high, just needs to cool down the reation kettle that liquid was placed this moment, and the most commonly used method is exactly to use chemical heat exchanger to cool down the reation kettle that liquid was placed.
After being connected reation kettle with chemical heat exchanger, chemical heat exchanger can reduce reation kettle's heat dissipation back temperature, and chemical heat exchanger is inside to have the crystal to appear, if let these crystals continue along the pipeline operation, will have the crystal to adhere to the condition emergence inside the pipeline, and what more can block up the pipeline, influences the work of whole pipeline.
SUMMERY OF THE UTILITY MODEL
The utility model aims at solving and exist among the prior art and be connected the back with reation kettle and chemical heat exchanger, chemical heat exchanger can reduce reation kettle's heat dissipation rear temperature, and chemical heat exchanger is inside to have the crystal to appear, if let these crystals continue along the pipeline operation, will have the crystal to adhere to the condition emergence inside the pipeline, and more the person can block up the shortcoming of pipeline, and the chemical heat exchanger who is equipped with porous tube sheet who proposes.
In order to achieve the above purpose, the utility model adopts the following technical scheme:
the utility model provides a design chemical industry heat exchanger with porous tube sheet, includes the shell, the both sides at shell both ends all are provided with the connecting seat, shell one side bottom intercommunication has the feed liquor pipe, shell one side top intercommunication has the drain pipe, the shell both ends all are provided with sealed lid, two the relative outside of sealed lid all communicates there is the connecting pipe, two sealed lid with all be provided with the closing plate between the shell, two the intercommunication has a plurality of pipelines between the closing plate, one of them sealed internal baffle that is provided with of lid, the outer lane of baffle with there is the space between the inner wall of sealed lid, the baffle is close to a plurality of pipeline one side all is provided with a plurality of stock, and is a plurality of all be provided with a plurality of brush posts on the stock, baffle and one of them be provided with coupling mechanism between the closing plate.
Preferably, a plurality of the long rods are all installed on the baffle through bearings, and a plurality of the long rods penetrate through a plurality of the pipelines and are provided with the uniform rotating blades.
Preferably, the connecting mechanism comprises a fixing rod mounted on one of the sealing plates, the fixing rod penetrates through the baffle and is provided with a stopper, and a spring is arranged on the fixing rod between the stopper and the baffle.
Preferably, the fixed rod is rectangular in shape, and the fixed rod is in transition fit with the baffle.
The utility model provides a pair of chemical industry heat exchanger with porous tube sheet, beneficial effect lies in: this chemical industry heat exchanger with porous tube sheet lets interval between baffle and the closing plate can be adjusted through setting up coupling mechanism to let in liquid gets into a plurality of pipelines from the connecting pipe of shell bottom, liquid can strike the baffle, let a plurality of stocks of baffle area remove in a plurality of, thereby let a plurality of brush posts on a plurality of stocks clean a plurality of pipeline inner walls, thereby avoid a plurality of pipeline inner walls can the crystallization to generate.
Drawings
Fig. 1 is a schematic structural diagram of a chemical heat exchanger with a porous tube sheet according to the present invention.
Fig. 2 is a first schematic structural view of a cross-sectional view of a chemical heat exchanger with a porous tube sheet according to the present invention.
Fig. 3 is a structural schematic diagram ii of a cross-sectional view of a chemical heat exchanger with a porous tube sheet according to the present invention.
Fig. 4 is a partial enlarged view of fig. 3 at a.
Fig. 5 is a partial enlarged view of fig. 3 at B.
In the figure: the device comprises a shell 1, a connecting seat 2, a liquid inlet pipe 3, a liquid outlet pipe 4, a sealing cover 5, a connecting pipe 6, a sealing plate 7, a pipeline 8, a baffle plate 9, a long rod 10, a brush column 11, a rotating blade 12, a fixed rod 13, a stop block 14 and a spring 15.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the 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.
Example 1
Referring to fig. 1-5, a chemical heat exchanger with porous tube sheet, including shell 1, the both sides at shell 1 both ends all are provided with connecting seat 2, shell 1 one side bottom intercommunication has feed liquor pipe 3, shell 1 one side top intercommunication has drain pipe 4, shell 1 both ends all are provided with sealed lid 5, the relative outside of two sealed lids 5 all communicates with connecting pipe 6, all be provided with closing plate 7 between two sealed lids 5 and the shell 1, it has a plurality of pipelines 8 to communicate between two closing plate 7, be provided with baffle 9 in one of them sealed lid 5, there is the space between the outer lane of baffle 9 and the inner wall of sealed lid 5, baffle 9 is close to a plurality of pipelines 8 one side and all is provided with a plurality of stock 10, all be provided with a plurality of brush posts 11 on a plurality of stock 10, be provided with coupling mechanism between baffle 9 and one of them closing plate 7, coupling mechanism is including installing dead lever 13 on one of them closing plate 7, dead lever 13 runs through baffle 9 and installs dog 14, be provided with spring 15 on the dead lever 13 between dog 14 and the baffle 9.
Through setting up spring 15, let interval between baffle 9 and the closing plate 7 can be adjusted to in letting liquid get into a plurality of pipelines 8 from connecting pipe 6 of 1 bottom of shell, liquid can strike baffle 9, let baffle 9 take a plurality of stock 10 to remove in pipeline 8, thereby let a plurality of brush post 11 on a plurality of stock 10 clean a plurality of 8 inner walls of pipeline, thereby avoid a plurality of 8 inner walls of pipeline can the crystallization to generate.
(the first liquid of setting is connected with the reation kettle that needs the cooling, so first liquid needs some pure clean, thereby first liquid generally can set up to the distilled water, the second liquid of setting does not have the requirement, the second liquid sets up to common water can) with the first liquid that needs the cooling from feed liquor pipe 3 interior 4 flows of following drain pipe that gets into shell 1, the second liquid that will flow gets into in shell 1 from connecting pipe 6 department of shell 1 bottom, flow from connecting pipe 6 department at shell 1 top, because the second liquid can heat up, thereby lead to the inside crystal of can appearing of second liquid and adsorb on a plurality of pipelines 8, through the second liquid flow velocity change that will flow 1, thereby let spring 15 extrude baffle 9, the second liquid of cooperation different speeds strikes baffle 9, thereby let the interval can change between baffle 9 and the closing plate 7, thereby let a plurality of brush post 11 on a plurality of stock 10 can clean a plurality of pipelines 8 inner walls.
Example 2
Optimization is carried out on the basis of the embodiment 1, referring to fig. 1-5, the shape of the fixing rod 13 is set to be rectangular, and the fixing rod 13 is in transition fit with the baffle 9.
Through setting up 13 shells of dead lever for the rectangle, let dead lever 13 can avoid baffle 9 to rotate in sealed lid 5 is inside to a plurality of stock 10 of avoiding the setting of baffle 9 bottom can collide with 8 inner walls of a plurality of pipelines, thereby prolong the life of a plurality of stock 10 and a plurality of pipeline 8.
Example 3
Optimization is carried out on the basis of the embodiment 1, and referring to fig. 1-5, a plurality of long rods 10 are all arranged on a baffle 9 through bearings, and a plurality of long rods 10 all penetrate through a plurality of pipelines 8 and are all provided with rotating blades 12.
Through using bearing installation to cooperate the rotatory leaf 12 of 10 bottom fixed mounting of stock on baffle 9 with a plurality of stock 10, let the liquid that 6 connecting pipes of shell 1 bottom got into can strike rotatory leaf 12, let rotatory leaf 12 take stock 10 internal rotation in pipeline 8 to let stock 10 take a plurality of brush post 11 to the clear more thoroughly of 8 inner walls of pipeline of belt.
The above, only be the embodiment of the preferred of the present invention, but the protection scope of the present invention is not limited thereto, and any person skilled in the art is in the technical scope of the present invention, according to the technical solution of the present invention and the utility model, which are designed to be replaced or changed equally, all should be covered within the protection scope of the present invention.
Claims (4)
1. The utility model provides a chemical industry heat exchanger with porous tube sheet, includes shell (1), its characterized in that, shell (1) both ends all are provided with sealed lid (5), two sealed lid (5) with all be provided with closing plate (7) between shell (1), two intercommunication has a plurality of pipelines (8) between closing plate (7), one of them be provided with baffle (9) in sealed lid (5), the outer lane of baffle (9) with there is the space between the inner wall of sealed lid (5), baffle (9) are close to a plurality of pipeline (8) one side all is provided with a plurality of stock (10), and is a plurality of all be provided with a plurality of brush posts (11) on stock (10), baffle (9) and one of them be provided with coupling mechanism between closing plate (7).
2. The heat exchanger provided with perforated tube sheet according to claim 1, wherein a plurality of said long rods (10) are mounted on said baffle plate (9) through bearings, and a plurality of said long rods (10) extend through a plurality of said pipes (8) and are mounted with rotating vanes (12).
3. The heat exchanger with perforated tube plate according to claim 1, wherein the connecting mechanism comprises a fixing rod (13) mounted on one of the sealing plates (7), the fixing rod (13) penetrates the baffle plate (9) and is mounted with a stopper (14), and a spring (15) is arranged on the fixing rod (13) between the stopper (14) and the baffle plate (9).
4. The chemical heat exchanger with perforated tube plate as recited in claim 3, wherein the shape of the fixing rod (13) is rectangular, and the fixing rod (13) is in transition fit with the baffle (9).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202222660189.XU CN218764743U (en) | 2022-10-10 | 2022-10-10 | Chemical heat exchanger with porous tube plate |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202222660189.XU CN218764743U (en) | 2022-10-10 | 2022-10-10 | Chemical heat exchanger with porous tube plate |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN218764743U true CN218764743U (en) | 2023-03-28 |
Family
ID=85698842
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202222660189.XU Active CN218764743U (en) | 2022-10-10 | 2022-10-10 | Chemical heat exchanger with porous tube plate |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN218764743U (en) |
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2022
- 2022-10-10 CN CN202222660189.XU patent/CN218764743U/en active Active
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