CN209230079U - A kind of high-efficiency full solution type heat exchanger - Google Patents
A kind of high-efficiency full solution type heat exchanger Download PDFInfo
- Publication number
- CN209230079U CN209230079U CN201822032191.6U CN201822032191U CN209230079U CN 209230079 U CN209230079 U CN 209230079U CN 201822032191 U CN201822032191 U CN 201822032191U CN 209230079 U CN209230079 U CN 209230079U
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- heat exchanger
- shell
- exchanger tube
- isocon
- partition
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Abstract
The utility model discloses a kind of high-efficiency full solution type heat exchangers, belong to technical field of heat exchange devices, including shell, partition, heat exchanger tube and isocon, and partition is set in the housing and housing cavity is separated into multiple holding tanks;Heat exchanger tube is set in the housing and sequentially passes through multiple holding tanks;The top of shell is equipped with multiple outlet tubes, and multiple outlet tubes are connected to multiple holding tanks one-to-one correspondence;The bottom of shell is equipped with multiple inlet tubes, and multiple inlet tubes are corresponded with the bottom of multiple holding tanks and are connected to;Isocon is set in holding tank and be connected to inlet tube, isocon it is vertical with the axis of heat exchanger tube and equipped with multiple along the arrangement of isocon axis and towards the spray orifice of heat exchanger tube.Refrigerating fluid is added into one or a few holding tank by one or a few inlet tube, so that less refrigerating fluid keeps higher liquid level in one or a few holding tank, refrigerating fluid can be contacted preferably with heat exchanger tube, improve the heat exchange efficiency of heat exchanger.
Description
Technical field
The utility model belongs to technical field of heat exchange devices more particularly to a kind of high-efficiency full solution type heat exchanger.
Background technique
Requirement of the country for industrial products energy-saving and emission-reduction at present is higher and higher, including air-conditioning, the section of refrigeration industry
It can require also constantly improving.Existing full-liquid type heat exchanger, the control method of cryogenic temperature one is pass through adjustment housings
The flow of middle refrigerating fluid controls cryogenic temperature.Such control mode, when the flow of refrigerating fluid is smaller, refrigerating fluid and heat exchanger tube
Insufficient contact, cause heat exchanger heat exchange efficiency decline.
Utility model content
The technical problem to be solved by the utility model is to provide a kind of high-efficiency full solution type heat exchangers, to solve the prior art
In, when the flow of refrigerating fluid is smaller, the insufficient contact of refrigerating fluid and heat exchanger tube, the technology for causing heat exchanger heat exchange efficiency to decline
Problem.
In order to solve the above technical problems, technical solution adopted in the utility model is:
A kind of high-efficiency full solution type heat exchanger, including shell, partition, heat exchanger tube and isocon, the partition are set to the shell
In vivo and the housing cavity is separated into multiple holding tanks;The heat exchanger tube is disposed in the housing and sequentially passes through multiple institutes
State holding tank;The top of the shell is equipped with multiple outlet tubes, and multiple outlet tubes are connected to multiple holding tank one-to-one correspondence;
The bottom of the shell is equipped with multiple inlet tubes, and multiple inlet tubes are corresponded with the bottom of multiple holding tanks and are connected to;Institute
It states isocon to be connected in the holding tank and with the inlet tube, the isocon is vertical with the axis of the heat exchanger tube simultaneously
It arranges along the isocon axis and equipped with multiple towards the spray orifice of the heat exchanger tube.
Further, the heat exchanger tube is multiple with being arranged and being parallel to each other along the longitudinal direction.
Further, the preceding liquid-distributing plate being located on front side of the partition is equipped in the shell, the preceding liquid-distributing plate will be described
It closes into intake antrum the front end of housing cavity;The housing forward end is equipped with the water inlet pipe being connected to the intake antrum, the heat exchange
The front end of pipe connect with the preceding liquid-distributing plate and is connected to the intake antrum.
Further, the rear liquid-distributing plate positioned at the membrane backside is equipped in the shell, the rear liquid-distributing plate will be described
The back-end closure of housing cavity is at water chamber;The housing rear end is equipped with the outlet pipe being connected to the water chamber, the heat exchange
The rear end of pipe is connected to the rear liquid-distributing plate and is connected to the water chamber.
Further, the partition is multiple with being arranged successively along the shell axis;The partition, which is equipped with, is located at institute
State above heat exchanger tube and be connected to the intercommunicating pore of the two neighboring holding tank.
Further, the shell is in the cylinder that axis is arranged along the longitudinal direction.
Further, the isocon has multiple, and multiple isocons are set to multiple receivings correspondingly
It is connected in slot and with multiple inlet tube one-to-one correspondence.
The beneficial effects of adopting the technical scheme are that in use, by multiple inlet tubes respectively with it is multiple cold
But liquid pipe connects, and when needing stronger refrigeration effect, refrigerating fluid is added into shell simultaneously for multiple inlet tubes, so that multiple appearances
It receives and is each filled with refrigerating fluid in slot and heat exchanger tube carries out heat exchange, guarantee refrigeration effect;It, can be with when needing weaker refrigeration effect
Refrigerating fluid is added into one or a few holding tank by one or a few inlet tube, so that less refrigerating fluid
Higher liquid level is kept in one or a few holding tank, refrigerating fluid can be contacted preferably with heat exchanger tube, improve heat exchange
The heat exchange efficiency of device.
Detailed description of the invention
Utility model will be further described in detail below with reference to the attached drawings and specific embodiments.
Fig. 1 is the main view of the utility model high-efficiency full solution type heat exchanger;
Fig. 2 is the cross-sectional view in Fig. 1 at A-A.
In figure: 1- shell;2- partition;3- holding tank;4- heat exchanger tube;5- outlet tube;6- inlet tube;7- isocon;Before 8-
Liquid-distributing plate;Liquid-distributing plate after 9-;10- intercommunicating pore;11- water inlet pipe;12- intake antrum;13- outlet pipe;14- water chamber;15- spray orifice.
Specific embodiment
Below with reference to the attached drawing in the utility model embodiment, the technical scheme in the embodiment of the utility model is carried out clear
Chu is fully described by, it is clear that and described embodiment is only a part of the embodiment of the utility model, rather than whole
Embodiment.Based on the embodiments of the present invention, those of ordinary skill in the art are without making creative work
Every other embodiment obtained, fall within the protection scope of the utility model.
As depicted in figs. 1 and 2, a kind of high-efficiency full solution type heat exchanger, including shell 1, partition 2, heat exchanger tube 4 and isocon 7;
The partition 2 is set in shell 1 and 1 inner cavity of shell is separated into multiple holding tanks 3;The heat exchanger tube 4 be set to shell 1 in and according to
It is secondary to pass through multiple holding tanks 3;The top of the shell 1 is equipped with multiple outlet tubes 5, and multiple outlet tubes 5 and multiple holding tanks 3 are one by one
Corresponding connection;The bottom of the shell 1 is equipped with multiple inlet tubes 6, and the bottom one of multiple inlet tubes 6 and multiple holding tanks 3 is a pair of
It should be connected to;The isocon 7 is set in holding tank 3 and is connected to inlet tube 6, and each isocon 7 is vertical with the axis of heat exchanger tube 4
And it is equipped with multiple arrange along 7 axis of isocon and towards the spray orifice of heat exchanger tube 4 15.
In use, multiple inlet tubes 6 are connect with multiple coolant pipes respectively, it is more when needing stronger refrigeration effect
Refrigerating fluid is added into shell 1 simultaneously in a inlet tube 6, carries out heat with heat exchanger tube 4 so that being each filled with refrigerating fluid in multiple holding tanks 3
Exchange guarantees refrigeration effect;It, can be by one or a few inlet tube 6 is to one when needing weaker refrigeration effect
Or refrigerating fluid is added in a few holding tank 3, so that less refrigerating fluid is kept at one or in a few holding tank 3
Higher liquid level, refrigerating fluid can be contacted preferably with heat exchanger tube 4, improve the heat exchange efficiency of heat exchanger.
Coolant liquid is sprayed towards heat exchanger tube 4 by spray orifice 15, the coolant liquid in holding tank 3 can be stirred, go to drive and change
The bubble on 4 surface of heat pipe.Isocon 7 can be the steel pipe for being horizontally set on 3 bottom of holding tank, the middle part of isocon 7 and feed liquor
The inner end of pipe 6 is connected to, closed at both ends.The upper surface of isocon 7 is arranged in spray orifice 15, is directed at heat exchanger tube 4 upwards.More specifically,
Multiple outlet tubes 5 are connected to multiple holding tanks 3 one-to-one correspondence, so that can distinguish after the coolant liquid gasification in each holding tank 3
It is discharged from each outlet tube 5.
Further, as depicted in figs. 1 and 2, heat exchanger tube 4 is multiple with being arranged and being parallel to each other along the longitudinal direction.Shell
Body 1 can be the horizontally disposed rectangle of long axis, and multiple heat exchanger tubes 4 are mounted in shell 1, and parallel with 1 long axis of shell.Shell
Body 1 is also possible to the horizontally disposed cylinder of axis, and multiple heat exchanger tubes 4 are mounted in shell 1, and parallel with 1 axis of shell.
Further, as shown in Figure 1, being equipped with the preceding liquid-distributing plate 8 for being located at the front side of partition 2 in shell 1, preceding liquid-distributing plate 8 is by shell
It closes into intake antrum 12 front end of 1 inner cavity of body;1 front end of shell is equipped with the water inlet pipe 11 that is connected to intake antrum 12, before heat exchanger tube 4
End connect with preceding liquid-distributing plate 8 and is connected to intake antrum 12.
Specifically, shell 1 is horizontal cylinder, partition 2 is mounted on the middle part of 1 inner cavity of shell, and preceding liquid-distributing plate 8 is installed
In the front of 1 inner cavity of shell.Preceding liquid-distributing plate 8 is diameter circular steel plate identical with 1 intracavity diameter of shell, preceding 8 edge of liquid-distributing plate
With 1 inner wall sealing welding of shell, the forward end seal of 1 inner cavity of shell is formed into intake antrum 12, the front end of shell 1 is equipped with water inlet pipe
11.Multiple through holes are offered in preceding 8 plate face of liquid-distributing plate, multiple 4 front ends of heat exchanger tube are corresponding with through hole respectively to install, so that into
Water pipe 11 is connected to by intake antrum 12 and through hole with 4 front end of heat exchanger tube.
Further, as shown in Figure 1, being equipped with the rear liquid-distributing plate 9 for being located at the rear side of partition 2 in shell 1, rear liquid-distributing plate 9 is by shell
The back-end closure of 1 inner cavity of body is at water chamber 14;1 rear end of shell is equipped with the outlet pipe 13 that is connected to water chamber 14, after heat exchanger tube 4
End is connected to rear liquid-distributing plate 9 and is connected to water chamber 14.
Specifically, shell 1 is horizontal cylinder, partition 2 is mounted on the middle part of 1 inner cavity of shell, and then liquid-distributing plate 9 is installed
At the rear portion of 1 inner cavity of shell.Liquid-distributing plate 9 is diameter circular steel plate identical with 1 intracavity diameter of shell, rear 9 edge of liquid-distributing plate afterwards
With 1 inner wall sealing welding of shell, the back-end sealing of 1 inner cavity of shell is formed into water chamber 14, the rear end of shell 1 is equipped with outlet pipe
13.Multiple through holes are offered in 9 plate face of liquid-distributing plate afterwards, the installation corresponding with through hole respectively of multiple 4 rear ends of heat exchanger tube makes to obtain
Water pipe 13 is connected to by water chamber 14 and through hole with 4 rear end of heat exchanger tube.
Further, as depicted in figs. 1 and 2, partition 2 is multiple with being arranged successively along 1 axis of shell;Each partition 2
Equipped with the intercommunicating pore 10 for being located at 4 top of heat exchanger tube and the two neighboring holding tank 3 of connection.The position of intercommunicating pore 10 is higher than heat exchanger tube 4,
When so that the coolant liquid in a holding tank 3 is excessive, it can be kept away by intercommunicating pore 10 to other adjacent 3 overflows of holding tank
Exempt from coolant liquid to be directly discharged from outlet tube 5.Intercommunicating pore 10 can be a through hole on 2 top of partition, be also possible to by partition 2
Interval between 1 top of top and shell is formed.
Further, as depicted in figs. 1 and 2, shell 1 is in the cylinder that axis is arranged along the longitudinal direction.
Specifically, partition 2 can be circular steel plate a small area is cut along string be made.Multiple 2 phases of partition
Mutually parallel and be sequentially arranged in shell 1 along the longitudinal direction, the position of 2 cutaway portion of partition is located above to form intercommunicating pore
10.On direction from the front to the back, the area of each 2 cutaway portion of partition is increasing, so that the height of 10 lower edge of intercommunicating pore
Degree successively reduces, and coolant liquid is successively overflowed to from the front to the back in each holding tank 3.
Further, as depicted in figs. 1 and 2, isocon 7 has multiple, and multiple isocons 7 are set to multiple correspondingly
It is connected in holding tank 3 and with multiple inlet tubes 6 one-to-one correspondence.Be equipped with isocon 7 in each holding tank 3, each isocon 7 with
The corresponding inlet tube 6 of holding tank 3 connection where itself.
Many details are explained in the following description in order to fully understand the utility model, but this is practical new
Type can also be implemented using other than the one described here other way, and those skilled in the art can be without prejudice to this reality
With doing similar popularization in the case where novel intension, therefore the utility model is not limited by the specific embodiments disclosed below.
Claims (7)
1. a kind of high-efficiency full solution type heat exchanger, which is characterized in that including shell, partition, heat exchanger tube and isocon, the partition is set
In being separated into multiple holding tanks in the shell and by the housing cavity;The heat exchanger tube is disposed in the housing and successively wears
Cross multiple holding tanks;The top of the shell is equipped with multiple outlet tubes, and multiple outlet tubes and multiple holding tanks are one by one
Corresponding connection;The bottom of the shell is equipped with multiple inlet tubes, one a pair of bottom of multiple inlet tubes and multiple holding tanks
It should be connected to;The isocon is set in the holding tank and is connected to the inlet tube, the isocon and the heat exchanger tube
Axis is vertical and is equipped with multiple arrange along the isocon axis and towards the spray orifice of the heat exchanger tube.
2. high-efficiency full solution type heat exchanger as described in claim 1, it is characterised in that: the heat exchanger tube has to be set along the longitudinal direction
It sets and is parallel to each other multiple.
3. high-efficiency full solution type heat exchanger as described in claim 1, it is characterised in that: be equipped in the shell and be located at the partition
The preceding liquid-distributing plate of front side, the preceding liquid-distributing plate close the front end of the housing cavity at intake antrum;The housing forward end is equipped with
The water inlet pipe being connected to the intake antrum, the front end of the heat exchanger tube connect with the preceding liquid-distributing plate and connect with the intake antrum
It is logical.
4. high-efficiency full solution type heat exchanger as described in claim 1, it is characterised in that: be equipped in the shell and be located at the partition
The rear liquid-distributing plate of rear side, the rear liquid-distributing plate is by the back-end closure of the housing cavity at water chamber;The housing rear end is equipped with
The outlet pipe being connected to the water chamber, the rear end of the heat exchanger tube are connected to the rear liquid-distributing plate and connect with the water chamber
It is logical.
5. high-efficiency full solution type heat exchanger as claimed in claim 2, it is characterised in that: the partition has along the shell axis
What is be arranged successively is multiple;The partition is equipped with the connection for being located above the heat exchanger tube and being connected to the two neighboring holding tank
Hole.
6. high-efficiency full solution type heat exchanger as described in claim 1, it is characterised in that: the shell is set along the longitudinal direction in axis
The cylinder set.
7. high-efficiency full solution type heat exchanger as claimed in any one of claims 1 to 6, it is characterised in that: the isocon has more
A, multiple isocons, which are set in multiple holding tanks correspondingly and correspond with multiple inlet tubes, to be connected
It is logical.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201822032191.6U CN209230079U (en) | 2018-12-05 | 2018-12-05 | A kind of high-efficiency full solution type heat exchanger |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201822032191.6U CN209230079U (en) | 2018-12-05 | 2018-12-05 | A kind of high-efficiency full solution type heat exchanger |
Publications (1)
Publication Number | Publication Date |
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CN209230079U true CN209230079U (en) | 2019-08-09 |
Family
ID=67506229
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201822032191.6U Active CN209230079U (en) | 2018-12-05 | 2018-12-05 | A kind of high-efficiency full solution type heat exchanger |
Country Status (1)
Country | Link |
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CN (1) | CN209230079U (en) |
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2018
- 2018-12-05 CN CN201822032191.6U patent/CN209230079U/en active Active
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