CN205391959U - Spiral gaseous phase separator - Google Patents
Spiral gaseous phase separator Download PDFInfo
- Publication number
- CN205391959U CN205391959U CN201620148381.2U CN201620148381U CN205391959U CN 205391959 U CN205391959 U CN 205391959U CN 201620148381 U CN201620148381 U CN 201620148381U CN 205391959 U CN205391959 U CN 205391959U
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- cavity
- urceolus
- vane
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Abstract
The utility model discloses a spiral gaseous phase separator, including inner tube, urceolus, vane, admission line and leakage fluid dram, the cavity that has the cylinder between inner tube and the urceolus, the vane sets up and makes it form the passageway that spiral shell screwing in rose in the cavity, the clearance has between the inner wall of vane and urceolus, the admission line is connected with the bottom of passageway, the leakage fluid dram is located the bottom of cavity. The utility model discloses a produced centrifugal force when spiral gaseous phase separator can utilize and mix the fluid and get into the passageway that spiral shell screwing in rose gets rid of liquid phase material and solid phase material on the inner wall of cavity and subsides from the clearance to the bottom, and the gaseous phase material is then isolate alone and follow the top and remove. The utility model discloses can be used to the ceramic manufacture trade.
Description
Technical field
This utility model relates to separation technology field, particularly a kind of spiral gas phase separation device.
Background technology
The design of existing gas phase separation device is complex, and separation efficiency is relatively low, it is difficult to meet the separation demand of large-scale production.Particularly on ceramic building material production line, a large amount of dust are discharged along with cooling water and air-flow, it is necessary to first carry out preliminary gas phase separation and could implement follow-up blowdown process step.Therefore, the gas phase separation device of a kind of simple in construction, good separating effect it is badly in need of in the industry.
Utility model content
This utility model provides a kind of spiral gas phase separation device, and the centrifugal force that eddy flow produces can be utilized gas phase to be separated from fluid-mixing, easy to use, and production efficiency is come high.
A kind of spiral gas phase separation device, including inner core, urceolus, vane, admission line and leakage fluid dram, there is between described inner core and urceolus columnar cavity, described vane is arranged in cavity and forms it into spiralling passage, between described vane and the inwall of urceolus, there is gap, described admission line is connected with the bottom of passage, and described leakage fluid dram is positioned at the bottom of cavity.
Vane described in the utility model includes upper, middle and lower section, and the gap between described vane and the inwall of urceolus is positioned at middle section.
This utility model also includes upper cover, and described upper cover is positioned at the upper end of cavity.
A kind of spiral gas phase separation device disclosed in this utility model can utilize fluid-mixing to enter produced centrifugal force during spiralling passage, being thrown on the inwall of cavity by liquid phase substance and solid matter and be settled down to bottom from gap location, gaseous substance then is separately separated out drains from above.This utility model can be used for ceramic production industry.
Accompanying drawing explanation
In order to be illustrated more clearly that the technical scheme in this utility model embodiment, below the accompanying drawing used required during embodiment is described is briefly described.Obviously, described accompanying drawing is a part of embodiment of the present utility model, rather than whole embodiment, and those skilled in the art is under the premise not paying creative work, it is also possible to obtain other designs and accompanying drawing according to these accompanying drawings.
Fig. 1 is structural representation of the present utility model.
Detailed description of the invention
Below with reference to embodiment and accompanying drawing, the technique effect of design of the present utility model, concrete structure and generation is clearly and completely described, to be completely understood by the purpose of this utility model, feature and effect.Obviously; described embodiment is a part of embodiment of the present utility model, rather than whole embodiment, based on embodiment of the present utility model; other embodiments that those skilled in the art obtains under the premise not paying creative work, belong to the scope of this utility model protection.It addition, all connection/annexations being previously mentioned in literary composition, not singly refer to that component directly connects, and refer to and according to being embodied as situation, by adding or reduce connection auxiliary, more excellent draw bail can be formed.Each technical characteristic in the invention, can combination of interactions under the premise of not conflicting conflict.
As shown in Figure 1, a kind of spiral gas phase separation device, including inner core 1, urceolus 2, vane 3, admission line 4 and leakage fluid dram 5, between described inner core 1 and urceolus 2, there is columnar cavity, described vane 3 is arranged in cavity and forms it into spiralling passage, having gap 6 between described vane 3 and the inwall of urceolus 2, described admission line 4 is connected with the bottom of passage, and described leakage fluid dram 5 is positioned at the bottom of cavity.Fluid-mixing enters segregation apparatus from admission line 4, then spiralling passage is entered along vane 3, liquid phase substance and solid matter that wherein quality is higher can be thrown on cavity inner wall when fluid rotary rises, being settled down to cavity bottom from gap 6 subsequently, gaseous substance is then drained from cavity top.
Being further used as preferred embodiment, described vane 3 includes upper, middle and lower section, and the gap 6 between described vane 3 and the inwall of urceolus 2 is positioned at middle section.Epimere and hypomere seal and can ensure that fluid-mixing enters passage smoothly.
Being further used as preferred embodiment, also include upper cover 7, described upper cover 7 is positioned at the upper end of cavity.Leave the gap drained for gaseous substance between upper cover 7 and cavity, and upper cover 7 can block separator and make it exempt from foreign body intrusion.
Above better embodiment of the present utility model is illustrated, but the invention is not limited to described embodiment, those of ordinary skill in the art also can make all equivalent modifications or replacement under the premise without prejudice to this utility model spirit, and these equivalent modification or replacement are all contained in the application claim limited range.
Claims (3)
1. a spiral gas phase separation device, it is characterized in that: include inner core (1), urceolus (2), vane (3), admission line (4) and leakage fluid dram (5), between described inner core (1) and urceolus (2), there is columnar cavity, described vane (3) is arranged in cavity and forms it into spiralling passage, there is between the inwall of described vane (3) and urceolus (2) gap (6), described admission line (4) is connected with the bottom of passage, and described leakage fluid dram (5) is positioned at the bottom of cavity.
2. spiral gas phase separation device according to claim 1, it is characterised in that: described vane (3) includes upper, middle and lower section, and the gap (6) between the inwall of described vane (3) and urceolus (2) is positioned at middle section.
3. spiral gas phase separation device according to claim 1, it is characterised in that: also including upper cover (7), described upper cover (7) is positioned at the upper end of cavity.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620148381.2U CN205391959U (en) | 2016-02-26 | 2016-02-26 | Spiral gaseous phase separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620148381.2U CN205391959U (en) | 2016-02-26 | 2016-02-26 | Spiral gaseous phase separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205391959U true CN205391959U (en) | 2016-07-27 |
Family
ID=56425239
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620148381.2U Expired - Fee Related CN205391959U (en) | 2016-02-26 | 2016-02-26 | Spiral gaseous phase separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205391959U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107899307A (en) * | 2017-12-05 | 2018-04-13 | 西安石油大学 | A kind of screw type gas-liquid separator |
| CN111558257A (en) * | 2020-05-20 | 2020-08-21 | 重庆大学 | Dispersion flow liquid drop separation device |
-
2016
- 2016-02-26 CN CN201620148381.2U patent/CN205391959U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107899307A (en) * | 2017-12-05 | 2018-04-13 | 西安石油大学 | A kind of screw type gas-liquid separator |
| CN111558257A (en) * | 2020-05-20 | 2020-08-21 | 重庆大学 | Dispersion flow liquid drop separation device |
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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 |
Granted publication date: 20160727 Termination date: 20200226 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |