CN208161305U - A kind of small multi-channel steam condensation liquid trap - Google Patents
A kind of small multi-channel steam condensation liquid trap Download PDFInfo
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- CN208161305U CN208161305U CN201820527104.1U CN201820527104U CN208161305U CN 208161305 U CN208161305 U CN 208161305U CN 201820527104 U CN201820527104 U CN 201820527104U CN 208161305 U CN208161305 U CN 208161305U
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- blower
- shell
- exchanging chamber
- heat exchanging
- cylindrical wall
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Abstract
The utility model proposes a kind of small multi-channel steam to condense liquid trap, to solve the problems, such as that small-sized condensation liquid trap high-temperature gas condensation efficiency is low, condensation process is complicated.The utility model includes hollow shell, and the middle part of shell is equipped with heat exchanging chamber, and the middle part of heat exchanging chamber is equipped with steam inlet, and the lower part of heat exchanging chamber is pyramidal structure, and the bottom of pyramidal structure is equipped with liquid outlet, is equipped with the floating ball to match with liquid outlet in liquid outlet；The center of heat exchanging chamber is equipped with cylindrical wall, is equipped with blower in cylindrical wall, blower is fixed on the top of shell by fan supporter；Cylindrical wall is equipped with extraneous gas import, and extraneous gas import is connected by the gas flow pipe road with external communication with the outer gas outlet on shell.The utility model increases heat exchange efficiency by multichannel heat exchanger tube, is realized by blower and strengthens heat convection, increases heat exchange efficiency；And structure is simple, small in size, compact, reasonable, is suitable for high-temperature gas and condenses, is suitable for water condensation extraction process.
Description
Technical field
The utility model relates to the technical fields of heat exchanger more particularly to small multi-channel steam to condense liquid trap, realize
High-temperature gas condensation, moisture in air extraction process, reach high-efficiency condensation by multichannel form.
Background technique
In the prior art, high temperature condensation and the mode that moisture is extracted in air are more complicated, and device is more huge, simultaneously
The condenser of existing open air field water purification function is less, in order to provide a kind of small steam condensation easy to carry and energy-efficient
Liquid trap achievees the purpose that water purification and condensation, and this condensation liquid trap is exactly a kind of good device matched under this environment.
Existing small condenser high-temperature gas condensation efficiency is low, heat transfer process is complicated.
Utility model content
For the technical problem that existing small condenser high-temperature gas condensation efficiency is low, condensation process is complicated, this is practical new
Type proposes a kind of small multi-channel steam condensation liquid trap, increases heat exchange efficiency by multichannel heat exchanger tube, is reached by blower
The purpose of forced-convection heat transfer increases heat exchange efficiency, and heat exchanger only needs a heat exchange cavity to reach heat transfer effect, process letter
It is single.
In order to achieve the above object, the technical solution of the utility model is realized in：A kind of small multi-channel steam
Liquid trap is condensed, including hollow shell, the middle part of shell is equipped with heat exchanging chamber, and the middle part of the heat exchanging chamber is equipped with steam inlet
Mouthful, the lower part of heat exchanging chamber is pyramidal structure, and the bottom of pyramidal structure is equipped with liquid outlet, is equipped in liquid outlet and liquid outlet
The floating ball to match；The center of the heat exchanging chamber is equipped with cylindrical wall, is equipped with blower in cylindrical wall, blower is fixed by fan supporter
At the top of shell；The cylindrical wall be equipped with the import of at least three extraneous gas, extraneous gas import by with external communication
Gas flow pipe road is connected with the outer gas outlet on shell.
The top of the shell is equipped with several circumferentially equally distributed first fins, the first fin lower part respectively with shell
The top of body or fan supporter connection.
The outside in the gas flow pipe road is equipped with several equally distributed second fins.
Second fin can be circular rings rib, the straight rib of cylinder or cone rib.
The top of the blower is connected with the first flabellum, and the lower part of blower is connected with the second flabellum.
Second flabellum of the blower is in the top of external gas feed.
The steam inlet is located at the top of the position on the lower side of cylindrical wall, pyramidal structure, and steam inlet is located at outside
The lower section of gas vent.
The outer gas outlet is evenly distributed in the same level of the side wall of cylindrical wall.
When high-temperature steam is entered in heat exchanging chamber by steam inlet, blower makes external cold end gas enter extraneous gas stream
In threading a pipe, exchanged heat by the heat exchange of outside air passes pipeline and top wall surface so that high-temperature steam is condensed into drop, while height
Warm steam also carries out heat exchange condensation with heat exchanging chamber top, and drop is flowed to pyramidal structure lower part along the wall surface of shell by gravity
Floating ball around；Drop around floating ball is assembled so that floating ball is since buoyancy is to floating, and liquid is flowed out from liquid outlet,
Achieve the effect that gas-liquid separation；When discharge reduction to a certain extent when, floating ball fall, block liquid outlet again, remaining liquid
Still it is gathered near floating ball, floating ball forms mechanical fluid-tight in liquid outlet, makes vapor that can not leak；Pass through above-mentioned mistake
The multiple circulation of journey constantly flows out liquid from liquid outlet, until reaching required amount of liquid.
The beneficial effects of the utility model：It can be changed in different designs difference channel according to demand by the structure of multichannel
Heat pipe, while condensed liquid is discharged in the way of mechanical fluid-tight, make the simple energy-efficient, disclosure risk of heat transfer process
It is small, and can designed, designed port number according to demand.The utility model structure is simple, compact, reasonable, and it is cold to be suitable for high-temperature gas
Solidifying, with a kind of novel heat exchange structure enhanced heat exchange, and device volume is small, is suitable for water extraction and extraction process.
Detailed description of the invention
In order to illustrate the embodiment of the utility model or the technical proposal in the existing technology more clearly, below will be to embodiment
Or attached drawing needed to be used in the description of the prior art is briefly described, it should be apparent that, the accompanying drawings in the following description is only
It is some embodiments of the utility model, for those of ordinary skill in the art, in the premise not made the creative labor
Under, it is also possible to obtain other drawings based on these drawings.
Fig. 1 is the structural schematic diagram of the utility model.
Fig. 2 is the top view of the utility model.
Fig. 3 is the cross-sectional view of the utility model.
Fig. 4 is the axonometric drawing of the utility model.
In figure, 1- outer gas outlet, the first fin of 2-, 3- fan supporter, 4- blower, 5- steam inlet, 6- floating ball,
The second fin of 7-, 8- heat exchanging chamber, 9- outside air passes pipeline, 10- liquid outlet, 11- extraneous gas import, 12- first are fanned
Leaf, the second flabellum of 13-.
Specific embodiment
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment.Based on the embodiments of the present invention, those of ordinary skill in the art are under that premise of not paying creative labor
Every other embodiment obtained, fall within the protection scope of the utility model.
As shown in Figs 1-4, a kind of small multi-channel steam condensation liquid trap is set in the middle part of shell including hollow shell
There is heat exchanging chamber 8, the middle part of the heat exchanging chamber 8 is equipped with steam inlet 5, and the lower part of heat exchanging chamber 8 is pyramidal structure, pyramidal structure
Bottom is equipped with liquid outlet 10, is equipped with the floating ball 6 to match with liquid outlet 10 in liquid outlet 10, floating ball 6 can be with plugging fluid
Body outlet 10, while when liquid is more 6 floating liquid of floating ball from liquid outlet 10 outflow achieve the effect that gas-liquid separation.It is described
The top of heat exchanging chamber 8 is equipped with cylindrical wall, and blower 4 is equipped in cylindrical wall, and heat exchanging chamber 8 is separated by cylindrical wall with blower 4, cylindrical wall
It is equipped at least three extraneous gas import 11, extraneous gas import 11 passes through the outside on outside air passes pipeline 9 and shell
Gas vent 1 is connected.Outside air passes pipeline 9 is evenly distributed on the outside of cylindrical wall.Blower 4 is solid by fan supporter 3
It is scheduled on the top of shell, blower 4 drives flabellum heat exchanging chamber 8 to carry out enhanced heat exchange.Fan supporter 3 includes three supporting plates, from three
A different direction steadily supports blower 4.Cylindrical wall separates blower 4 and heat exchanging chamber 8, guarantees the steady operation of blower 4.It is floating
Ball 6 can take along conjunction with the empty perfection of the liquid outlet 10 of heat exchanging chamber bottom, reach air tight purpose.Small liquid is formed after steam condensation
Drop, is affected by gravity to whereabouts, is blocked in the bottom of heat exchanging chamber 8 by floating ball 6, with the cohesion of drop, so that floating ball 6 floats,
Liquid is flowed out from liquid outlet 10, achievees the effect that gas-liquid separation, discharge reduction to a certain extent when, floating ball 6 falls, and blocks up again
Firmly export, remaining liq stays in floating ball surrounding along device inner wall, and mechanical fluid-tight is formed at liquid outlet 10, make vapor without
Method leaks.
The top of the shell is equipped with several circumferentially equally distributed first fins 2,2 lower part of the first fin respectively with
The top of shell or fan supporter 3 connect.First fin 2 can not only accelerate the heat loss in heat exchanging chamber 8 can also be to blower
Achieve the purpose that fast cooling.
The outside in the gas flow pipe road 9 is equipped with several equally distributed second fins 7.Second fin 7 is circle
The straight rib of ring rib, cylinder and cone rib etc..The effect of second fin 7 is to reach reflux disturbance in order to change gas flow pattern and increase
Add heat exchange efficiency.
The extraneous gas import 11, gas flow pipe road 9 are in the lower section of the second flabellum 13 of blower 4, gas flow pipe
Road 9 is communicated with space locating for blower 4, facilitates blower that cold end gas is delivered to outside air passes pipeline 9.When blower 4 operates
External relatively cool gas is blown into outside air passes pipeline 9, reaches part counterflow heat exchange, is formed simultaneously forced convertion
Purpose.
The top of the blower 4 is connected with the first flabellum 12, and the lower part of blower 4 is connected with the second flabellum 13, the first flabellum
12 main functions are the heat exchange of top part with heat exchanging chamber 8, form forced-convection heat transfer, high efficient heat exchanging.
The steam inlet 5 is located at the top of the position on the lower side of cylindrical wall, pyramidal structure, and steam inlet 5 is located at outer
The lower section of portion's gas vent 1 so that hot steam moved upwards when entering heat exchanging chamber with the cold end gas in cylindrical wall formed heat it is close
It is poor to spend, and causes to form disturbance convection current inside entire heat exchanging chamber 8.
The cylindrical wall is the cylinder-shaped cylindrical wall of upper opening, and through-hole is evenly distributed on the side wall of cylindrical wall, makes cold
End gas is uniformly distributed into heat exchanging chamber 8.
When the utility model operates, enters in heat exchanging chamber 8 when high-temperature steam passes through steam inlet 5, open blower 4, wind
Machine 4 enters external cold end gas in outside air passes pipeline 9, and two flabellums of extension set upper and lower part make gas reach strong
Heat convection effect processed, by efficiently exchanging heat so that high-temperature steam is condensed into drop, drop by gravity influenced along
The wall surface of shell flows to around the floating ball 6 of pyramidal structure lower part；Drop around floating ball 6 is assembled so that floating ball 6 is due to floating
Power is acted on to floating, and liquid is flowed out from liquid outlet 10；When discharge reduction to a certain extent when, floating ball 6 fall, block liquid again
Body outlet 10, remaining liquid is still gathered near floating ball 6, and floating ball 6 forms mechanical fluid-tight at liquid outlet 10, steams water
Gas can not leak；Multiple circulation by the above process constantly flows out liquid from liquid outlet 10, until reaching required liquid
The scale of construction.
The above is only the preferred embodiment of the utility model only, is not intended to limit the utility model, all at this
Within the spirit and principle of utility model, any modification, equivalent replacement, improvement and so on should be included in the utility model
Protection scope within.
Claims (8)
1. a kind of small multi-channel steam condenses liquid trap, including hollow shell, the middle part of shell is equipped with heat exchanging chamber（8）,
It is characterized in that, the heat exchanging chamber（8）Middle part be equipped with steam inlet（5）, heat exchanging chamber（8）Lower part be pyramidal structure, taper
The bottom of structure is equipped with liquid outlet（10）, liquid outlet（10）It is inside equipped with and liquid outlet（10）The floating ball to match（6）；Institute
State heat exchanging chamber（8）Center be equipped with cylindrical wall, blower is equipped in cylindrical wall（4）, blower（4）Pass through fan supporter（3）It is fixed on
The top of shell；The cylindrical wall is equipped with the import of at least three extraneous gas（11）, extraneous gas import（11）By with outside
The gas flow pipe road of connection（9）With the outer gas outlet on shell（1）It is connected.
2. small multi-channel steam according to claim 1 condenses liquid trap, which is characterized in that set at the top of the shell
There are several circumferentially equally distributed first fins（2）, the first fin（2）Lower part respectively with the top of shell or fan supporter
（3）Connection.
3. small multi-channel steam according to claim 1 condenses liquid trap, which is characterized in that the gas flow pipe road
（9）Outside be equipped with several equally distributed second fins（7）.
4. small multi-channel steam according to claim 3 condenses liquid trap, which is characterized in that second fin（7）
It can be circular rings rib, the straight rib of cylinder or cone rib.
5. small multi-channel steam according to claim 1 condenses liquid trap, which is characterized in that the blower（4）It is upper
Portion is connected with the first flabellum（12）, blower（4）Lower part be connected with the second flabellum（13）.
6. small multi-channel steam according to claim 5 condenses liquid trap, which is characterized in that the blower（4）?
Two flabellums（13）In external gas feed（11）Top.
7. small multi-channel steam according to claim 1 condenses liquid trap, which is characterized in that the steam inlet
（5）Positioned at the position on the lower side of cylindrical wall, the top of pyramidal structure, steam inlet（5）Positioned at outer gas outlet（1）Under
Side.
8. small multi-channel steam according to claim 1 condenses liquid trap, which is characterized in that the outer gas outlet
（1）It is evenly distributed in the same level of the side wall of cylindrical wall.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820527104.1U CN208161305U (en) | 2018-04-13 | 2018-04-13 | A kind of small multi-channel steam condensation liquid trap |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820527104.1U CN208161305U (en) | 2018-04-13 | 2018-04-13 | A kind of small multi-channel steam condensation liquid trap |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208161305U true CN208161305U (en) | 2018-11-30 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201820527104.1U Active CN208161305U (en) | 2018-04-13 | 2018-04-13 | A kind of small multi-channel steam condensation liquid trap |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110013743A (en) * | 2019-04-24 | 2019-07-16 | 新能科电气有限公司 | Water-steam separation device |
-
2018
- 2018-04-13 CN CN201820527104.1U patent/CN208161305U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110013743A (en) * | 2019-04-24 | 2019-07-16 | 新能科电气有限公司 | Water-steam separation device |
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