CN205569832U - Centrifugal gas -liquid separator - Google Patents
Centrifugal gas -liquid separator Download PDFInfo
- Publication number
- CN205569832U CN205569832U CN201620282645.3U CN201620282645U CN205569832U CN 205569832 U CN205569832 U CN 205569832U CN 201620282645 U CN201620282645 U CN 201620282645U CN 205569832 U CN205569832 U CN 205569832U
- Authority
- CN
- China
- Prior art keywords
- spiral coil
- liquid separator
- tank body
- gas
- centrifugal gas
- Prior art date
- 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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Abstract
The utility model discloses a centrifugal gas -liquid separator, including a jar body to reach the inlet pipe in the middle part of the intercommunication jar is personally experienced sth. Part of the body respectively, the blast pipe at top, the fluid -discharge tube of bottom, be provided with the spiral coil of port intercommunication inlet pipe in the jar body, the axial of spiral coil becomes vertical state, the pipe wall upper surface of spiral coil is equipped with a plurality of gas pockets. The utility model discloses a gaseous phase is spilled over from the gas pocket does not need to pass through completely the spiral coil, and the velocity of flow mitigatees gradually, and the liquid phase increases along the spiral coil velocity of flow gradually, and the current difference of gaseous phase and liquid phase is increasing, and the separation effect is better.
Description
Technical field
This utility model relates to a kind of centrifugal gas-liquid separator.
Background technology
Gas-liquid separator is a kind of equipment for being separated with liquid medium by the gas mixed, and is divided into gravitational settling, baffle separation, centrifugal force separate, silk screen separation, ultra-filtration and separation, filler separation etc. according to isolating construction;Current centrifugal force separate generally uses vertical helical pipe, mixed phase material to realize separating after passing completely through helical pipe, and the speed difference of gas phase and liquid phase is less, and separating effect is limited.
Summary of the invention
The technical problems to be solved in the utility model is to provide a kind of centrifugal gas-liquid separator, and the speed difference that can solve the gas phase of existing centrifugal gas-liquid separator and liquid phase is less, causes the problem that separating effect is limited.
This utility model is achieved through the following technical solutions:
A kind of centrifugal gas-liquid separator, including tank body, and it is respectively communicated with the feed pipe in the middle part of tank body, the exhaustor at top, the discharging tube of bottom, described tank body is provided with the spiral coil of upper port connection feed pipe, the axially vertical state of one-tenth of described spiral coil, the tube wall upper surface of described spiral coil is provided with multiple pore.
Further scheme of the present utility model is, described spiral coil diameter from the top down is gradually reduced.
Further scheme of the present utility model is, the tank body top between spiral coil and exhaustor is provided with mesh mist eliminator.
Further scheme of the present utility model is that described tank body is made up of PP material.
This utility model advantage compared with prior art is:
One, gas phase is overflowed from pore and be need not completely by spiral coil, and flow velocity gradually relaxes, and liquid phase is gradually increased along spiral coil flow velocity, and the current difference of gas phase and liquid phase is increasing, and separating effect is more preferable;
Two, spiral coil diameter from the top down is gradually reduced, and improves the flow velocity of liquid phase further, thus improves separating effect further;
Three, mesh mist eliminator can effectively remove liquid phase collision or the fog of evaporation generation, improves separating effect further.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Detailed description of the invention
A kind of centrifugal gas-liquid separator as shown in Figure 1, including the tank body 1 being made up of PP material, and it is respectively communicated with the feed pipe 2 in the middle part of tank body 1, the exhaustor 3 at top, the discharging tube 4 of bottom, described tank body 1 is provided with the spiral coil 5 of upper port connection feed pipe 2, the axially vertical state of one-tenth of described spiral coil 5, the tube wall upper surface of described spiral coil 5 is provided with multiple pore 6, described spiral coil 5 diameter from the top down is gradually reduced, and tank body 1 top between spiral coil 5 and exhaustor 3 is provided with mesh mist eliminator 7.
Mixed phase is sent into from feed pipe 2, and gas phase pore 6 from spiral coil 5 overflows, and liquid phase is accelerated dirty along spiral coil 5, and final gas phase is arranged from exhaustor 3 through mesh mist eliminator 7, and liquid phase is by the outer row of discharging tube 4.
Claims (3)
1. a centrifugal gas-liquid separator, including tank body (1), and it is respectively communicated with the feed pipe (2) at tank body (1) middle part, the exhaustor (3) at top, the discharging tube (4) of bottom, it is characterized in that: described tank body (1) is provided with the spiral coil (5) of upper port connection feed pipe (2), the axially vertical state of one-tenth of described spiral coil (5), the tube wall upper surface of described spiral coil (5) is provided with multiple pore (6);Described spiral coil (5) diameter from the top down is gradually reduced.
2. a kind of centrifugal gas-liquid separator as claimed in claim 1, it is characterised in that: tank body (1) top between spiral coil (5) and exhaustor (3) is provided with mesh mist eliminator (7).
3. a kind of centrifugal gas-liquid separator as claimed in claim 1, it is characterised in that: described tank body (1) is made up of PP material.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201620282645.3U CN205569832U (en) | 2016-04-07 | 2016-04-07 | Centrifugal gas -liquid separator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201620282645.3U CN205569832U (en) | 2016-04-07 | 2016-04-07 | Centrifugal gas -liquid separator |
Publications (1)
Publication Number | Publication Date |
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CN205569832U true CN205569832U (en) | 2016-09-14 |
Family
ID=56864333
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201620282645.3U Expired - Fee Related CN205569832U (en) | 2016-04-07 | 2016-04-07 | Centrifugal gas -liquid separator |
Country Status (1)
Country | Link |
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CN (1) | CN205569832U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106861240A (en) * | 2017-05-04 | 2017-06-20 | 哈尔滨瀚钧药业有限公司 | For separating the fat-soluble spiral separator with water-soluble mixed liquor |
CN111689543A (en) * | 2020-07-17 | 2020-09-22 | 西藏神州瑞霖环保科技股份有限公司 | Sewage treatment system and control method thereof |
-
2016
- 2016-04-07 CN CN201620282645.3U patent/CN205569832U/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106861240A (en) * | 2017-05-04 | 2017-06-20 | 哈尔滨瀚钧药业有限公司 | For separating the fat-soluble spiral separator with water-soluble mixed liquor |
CN111689543A (en) * | 2020-07-17 | 2020-09-22 | 西藏神州瑞霖环保科技股份有限公司 | Sewage treatment system and control method thereof |
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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: 20160914 Termination date: 20210407 |