CN204865261U - Vapor -liquid separation device - Google Patents
Vapor -liquid separation device Download PDFInfo
- Publication number
- CN204865261U CN204865261U CN201520493112.5U CN201520493112U CN204865261U CN 204865261 U CN204865261 U CN 204865261U CN 201520493112 U CN201520493112 U CN 201520493112U CN 204865261 U CN204865261 U CN 204865261U
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- CN
- China
- Prior art keywords
- vapor
- baffle
- baffle plate
- liquid
- utility
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
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- 239000007788 liquid Substances 0.000 title claims abstract description 41
- 238000000926 separation method Methods 0.000 title abstract description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 12
- 239000000203 mixture Substances 0.000 abstract description 10
- 230000005484 gravity Effects 0.000 abstract description 8
- 238000012797 qualification Methods 0.000 abstract description 8
- 239000007791 liquid phase Substances 0.000 abstract description 4
- 239000012071 phase Substances 0.000 abstract description 4
- 230000009286 beneficial effect Effects 0.000 abstract description 2
- 239000000463 material Substances 0.000 abstract description 2
- 238000000034 method Methods 0.000 description 6
- 239000000126 substance Substances 0.000 description 4
- 239000012153 distilled water Substances 0.000 description 3
- 238000004062 sedimentation Methods 0.000 description 3
- 230000007812 deficiency Effects 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Landscapes
- Separating Particles In Gases By Inertia (AREA)
Abstract
The utility model discloses a vapor -liquid separation device, the utility model relates to the field of water treatment, the inside vortex device that is equipped with of barrel, the vortex device includes an at least baffle, the vortex device including straight baffle, oblique baffle and head baffle perhaps the vortex device is heliciform spoiler structure. The utility model discloses beneficial effect: before qualified steam got into appointed pipeline, the centrifugal force of production when destroying vapor -liquid separation was thoroughly broken up the vapour -liquid mixture, utilizes both gravity differences of vapour -liquid, and the liquid phase material is owing to the gravity relation is subsided downwards to with the thoroughly separation of vapour phase output article, thereby guarantee the qualification rate and the gas saturation of output article.
Description
Technical field
The utility model relates to water treatment field, particularly relates to a kind of vapor-liquid separating device.
Background technology
Present most of multi-effect distilled water machine equipment and pure steam generator equipment are when carrying out vapor-liquid separation, due under equipment centrifugal action, gas vapour speed is very fast, the unevaporated droplet of meeting entrainment portions when gas rises fast, droplet comprises unevaporated material water or is evaporated into the condensed water (waste water) separated, residual harmful substance in distilled water, causes the purity of distilled water not high, can affect qualified water output capacity and vapo(u)rous degree as processed not in time.
Utility model content
In order to overcome above-mentioned the deficiencies in the prior art, the utility model provides a kind of vapor-liquid separating device.
For achieving the above object, the utility model solves the technical scheme that its technical problem adopts and is:
A kind of vapor-liquid separating device, is characterized in that: inner barrel is provided with a disturbing flow device.
As preferred technical scheme, described disturbing flow device comprises at least one piece of baffle plate.
As preferred technical scheme, described disturbing flow device comprises straight baffle plate, slanting baffle and end socket baffle plate, described straight baffle plate is connected by head rod with slanting baffle, described end socket baffle plate is connected by the second connecting rod with slanting baffle, the shape of described end socket baffle plate is arc, and end socket baffle plate is connected with cylindrical shell by the 3rd connecting rod.
On the basis of technique scheme, the utility model can also make following improvement:
As preferred technical scheme, described disturbing flow device is also provided with droplet collection device, and described droplet collection device comprises hollow gutter channel and drainpipe, and described hollow gutter channel is located at slanting baffle outer wall, be provided with flowing water mouth bottom hollow gutter channel, drainpipe is connected with hollow gutter channel.
Adopt above-mentioned preferred technical scheme, can in the process of flow-disturbing, the drop separated be collected rapidly and discharge, ensure the qualification rate of output.
As preferred technical scheme, be provided with at least one fan bottom described straight baffle plate, fan is connected with straight baffle plate.
Adopt above-mentioned preferred technical scheme, the action time that vapour-liquid contacts straight baffle plate can be increased, vapour-liquid movement velocity is reduced, makes vapor-liquid separation more thorough.
As preferred technical scheme, described disturbing flow device is helical form spoiler, and helical baffle and center stand column are along spiral distribution, and helical baffle is fixedly connected with center stand column.
Adopt above-mentioned preferred technical scheme, when vapour-liquid mixture enters coil region, vapour-liquid up flows along helical baffle, and helical baffle can effectively reduce the speed that vapour-liquid mixture flows toward eminence, increase the length of helical form separating plate, vapour-liquid can be made effectively to be separated.
As preferred technical scheme, described helical baffle is provided with screw type spiral rhone.
Adopt above-mentioned preferred technical scheme, can in the process of flow-disturbing, the drop separated be collected rapidly and discharge, ensure the qualification rate of output.
Due to the utilization of technique scheme, the utility model compared with prior art has following beneficial effect: when qualified steam enters before appointment conveyance conduit, the centrifugal force produced when destroying vapor-liquid separation, liquid-vapor mixture is thoroughly broken up, utilize both vapour-liquids gravity difference, liquid phase substance due to the downward sedimentation of gravity relation, thus is thoroughly separated with vapour phase output product, thus ensures qualification rate and the gas saturation degree of output product.
Accompanying drawing explanation
In order to be illustrated more clearly in the utility model embodiment or technical scheme of the prior art, be briefly described to the accompanying drawing used required in embodiment or description of the prior art below, apparently, accompanying drawing in the following describes is only embodiments more of the present utility model, for those of ordinary skill in the art, under the prerequisite not paying creative work, other accompanying drawing can also be obtained according to these accompanying drawings.
Fig. 1 is the structural representation of the utility model baffle plate, slanting baffle and end socket baffle plate.
Fig. 2 be the utility model droplet collection device structural representation.
Fig. 3 is the structural representation of the utility model helical form spoiler.
The title of numeral and the corresponding component represented by letter in figure:
1-the 3rd connecting rod; 2-end socket baffle plate; 3-second connecting rod; 4-slanting baffle; 5-head rod; The straight baffle plate of 6-; 8-fan; 11-hollow gutter channel; 12-flowing water mouth; 13-drainpipe; 21-center stand column; 22-helical baffle; 23-spiral rhone.
Detailed description of the invention
Below in conjunction with specific embodiment, content of the present utility model is described in further detail:
In order to reach the purpose of this utility model, in certain embodiments, as shown in Figure 1, a kind of vapor-liquid separating device, it is characterized in that: inner barrel is provided with a disturbing flow device, described disturbing flow device comprises at least one piece of baffle plate, disturbing flow device comprises straight baffle plate 6, slanting baffle 4 and end socket baffle plate 2, described straight baffle plate 6 is connected by head rod 5 with slanting baffle 4, described end socket baffle plate 2 is connected by the second connecting rod 3 with slanting baffle 4, the shape of described end socket baffle plate 2 is arc, and end socket baffle plate 2 is connected with cylindrical shell by the 3rd connecting rod 1.
The centrifugal force that disturbing flow device produces when can destroy vapor-liquid separation, thoroughly broken up by liquid-vapor mixture, utilize both vapour-liquids gravity difference, liquid phase substance is due to the downward sedimentation of gravity relation, thus be thoroughly separated with vapour phase output product, thus ensure qualification rate and the gas saturation degree of output product.
In order to optimize implementation result of the present utility model further, described disturbing flow device is also provided with droplet collection device, described droplet collection device comprises hollow gutter channel and drainpipe, described hollow gutter channel is located at slanting baffle outer wall, be provided with flowing water mouth bottom hollow gutter channel, drainpipe is connected with hollow gutter channel.
Adopt above-mentioned preferred technical scheme, can in the process of flow-disturbing, the drop separated be collected rapidly and discharge, ensure the qualification rate of output.
In order to optimize implementation result of the present utility model further, be provided with at least one fan bottom described straight baffle plate, fan is connected with straight baffle plate.
Adopt above-mentioned preferred technical scheme, the action time that vapour-liquid contacts straight baffle plate can be increased, vapour-liquid movement velocity is reduced, make vapor-liquid separation more thorough, when vapour-liquid mixture touches fan, the movement velocity of vapour-liquid mixture reduces further, and the effective time contacting baffle plate is extended.
In order to optimize implementation result of the present utility model further, described disturbing flow device is helical form spoiler, and helical baffle and center stand column are along spiral distribution, and helical baffle is fixedly connected with center stand column.
Adopt above-mentioned preferred technical scheme, when vapour-liquid mixture enters coil region, vapour-liquid up flows along helical baffle, and helical baffle can effectively reduce the speed that vapour-liquid mixture flows toward eminence, increase the length of helical form separating plate, vapour-liquid can be made effectively to be separated.
In order to optimize implementation result of the present utility model further, described helical baffle is provided with screw type spiral rhone.
Adopt above-mentioned preferred technical scheme, can in the process of flow-disturbing, the drop separated be collected rapidly and discharge, ensure the qualification rate of output.
A kind of vapor-liquid separating device of the utility model, when qualified steam enters before appointment conveyance conduit, the centrifugal force produced when destroying vapor-liquid separation, liquid-vapor mixture is thoroughly broken up, utilize both vapour-liquids gravity difference, liquid phase substance due to the downward sedimentation of gravity relation, thus is thoroughly separated with vapour phase output product, thus ensures qualification rate and the gas saturation degree of output product.
Above-described embodiment is only for illustrating technical conceive of the present utility model and feature; its object is to person skilled in the art can be understood content of the present utility model and be implemented; protection domain of the present utility model can not be limited with this; all equivalences done according to the utility model Spirit Essence change or modify, and all should be encompassed in protection domain of the present utility model.
Claims (7)
1. a vapor-liquid separating device, is characterized in that: inner barrel is provided with a disturbing flow device.
2. a kind of vapor-liquid separating device according to claim 1, is characterized in that: described disturbing flow device comprises at least one piece of baffle plate.
3. a kind of vapor-liquid separating device according to claim 2, it is characterized in that: described disturbing flow device comprises straight baffle plate, slanting baffle and end socket baffle plate, described straight baffle plate is connected by head rod with slanting baffle, described end socket baffle plate is connected by the second connecting rod with slanting baffle, the shape of described end socket baffle plate is arc, and end socket baffle plate is connected with cylindrical shell by the 3rd connecting rod.
4. a kind of vapor-liquid separating device according to claim 3, it is characterized in that: described disturbing flow device is also provided with droplet collection device, described droplet collection device comprises hollow gutter channel and drainpipe, described hollow gutter channel is located at slanting baffle outer wall, be provided with flowing water mouth bottom hollow gutter channel, drainpipe is connected with hollow gutter channel.
5. a kind of vapor-liquid separating device according to claim 3, is characterized in that: be provided with at least one fan bottom described straight baffle plate, fan is connected with straight baffle plate.
6. a kind of vapor-liquid separating device according to claim 1, is characterized in that: described disturbing flow device is helical form spoiler, and helical baffle and center stand column are along spiral distribution, and helical baffle is fixedly connected with center stand column.
7. a kind of vapor-liquid separating device according to claim 1, is characterized in that: described helical baffle is provided with screw type spiral rhone.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520493112.5U CN204865261U (en) | 2015-07-09 | 2015-07-09 | Vapor -liquid separation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520493112.5U CN204865261U (en) | 2015-07-09 | 2015-07-09 | Vapor -liquid separation device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204865261U true CN204865261U (en) | 2015-12-16 |
Family
ID=54809697
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520493112.5U Expired - Fee Related CN204865261U (en) | 2015-07-09 | 2015-07-09 | Vapor -liquid separation device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204865261U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105642024A (en) * | 2016-03-18 | 2016-06-08 | 上海交通大学 | Swirling de-swirling coupled efficient dedusting and demisting assembly |
| CN106595333A (en) * | 2016-12-13 | 2017-04-26 | 大连凯泓科技有限公司 | Multi-stage fold-back water and vapor separating self-solidifying pipeline for high-temperature water vapor |
| CN111793547A (en) * | 2020-05-29 | 2020-10-20 | 湖州老恒和酒业有限公司 | Production process and distillation device of low-alcohol yellow wine |
| CN116943345A (en) * | 2023-07-21 | 2023-10-27 | 华东理工大学 | Gas-liquid separation inner member for strengthening condensation heat exchange |
-
2015
- 2015-07-09 CN CN201520493112.5U patent/CN204865261U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105642024A (en) * | 2016-03-18 | 2016-06-08 | 上海交通大学 | Swirling de-swirling coupled efficient dedusting and demisting assembly |
| CN106595333A (en) * | 2016-12-13 | 2017-04-26 | 大连凯泓科技有限公司 | Multi-stage fold-back water and vapor separating self-solidifying pipeline for high-temperature water vapor |
| CN111793547A (en) * | 2020-05-29 | 2020-10-20 | 湖州老恒和酒业有限公司 | Production process and distillation device of low-alcohol yellow wine |
| CN116943345A (en) * | 2023-07-21 | 2023-10-27 | 华东理工大学 | Gas-liquid separation inner member for strengthening condensation heat exchange |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20151216 |