CN203591652U - Gas-liquid separator - Google Patents
Gas-liquid separator Download PDFInfo
- Publication number
- CN203591652U CN203591652U CN201320778658.6U CN201320778658U CN203591652U CN 203591652 U CN203591652 U CN 203591652U CN 201320778658 U CN201320778658 U CN 201320778658U CN 203591652 U CN203591652 U CN 203591652U
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- CN
- China
- Prior art keywords
- cylinder
- gas
- bucket
- liquid
- liquid separator
- 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
Links
- 239000007788 liquid Substances 0.000 title claims abstract description 37
- 235000013305 food Nutrition 0.000 abstract description 2
- 238000007789 sealing Methods 0.000 abstract 3
- 238000000926 separation method Methods 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 230000004048 modification Effects 0.000 description 3
- 238000006011 modification reaction Methods 0.000 description 3
- 238000005119 centrifugation Methods 0.000 description 2
- 238000004458 analytical method Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 235000015203 fruit juice Nutrition 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
Abstract
The utility model relates to food processing equipment and particularly discloses a gas-liquid separator. The gas-liquid separator comprises a cylinder body (1), a sealing head (4) arranged at the upper end of the cylinder body (1), a gas outlet pipe connector (2) arranged on the sealing head (4), a cylinder bottom (6) arranged at the lower end of the cylinder body (1), and a support column (8) supported in the center of the cylinder bottom (6), wherein the a gas-liquid inlet pipe (5) is arranged below the cylinder body (1); a liquid outlet (7) is formed in the edge of the cylinder bottom (6); the gas-liquid separator is characterized in that the gas outlet pipe connector (2) is connected with a tapered pipe (3); the expansion end of the tapered pipe (3) extends into the sealing head (4); the gas-liquid inlet pipe (5) is introduced into the cylinder body (1) in the tangential direction.
Description
Technical field
The utility model belongs to food processing field, is specifically related to a kind of gas-liquid separator.
Background technology
In food-processing industry, particularly, in the concentrated processing of fruit juice or medicament, usually use vapo(u)rization system, in vapo(u)rization system, must there is gas-liquid separator to carry out a small amount of solution stoste that Separation of Water steam is taken away.But vapo(u)rization system is bulky, pipeline is various, controls complicated, for simplify vapo(u)rization system as far as possible, gas-liquid separator in vapo(u)rization system does not preferably need power source, can not slow down because of complex structure the flow velocity of steam, also will guarantee good gas-liquid separation effect simultaneously.Because have many huge tank bodies and various pipeline in vapo(u)rization system, need to save the floor space of gas-liquid separator again as far as possible, also need to keep the stable of tank body simultaneously.
Utility model content
For overcoming the above problems, the utility model provides a kind of gas-liquid separator, and it does not need power source, simple in structure, and floor space is little, also has good gas-liquid separation effect.
For reaching above object, the utility model is achieved by the following technical solutions.
A kind of gas-liquid separator, comprises cylinder, is arranged on the end socket of cylinder upper end, is arranged on the escape pipe interface on end socket, is arranged on the bucket end of cylinder lower end, the pillar of central authorities at the bottom of being supported on barrel; Described cylinder below is provided with gas-liquid inlet tube, and described bucket base is along being provided with liquid outlet; It is characterized in that, described escape pipe interface connects conical pipe, and the bellend of conical pipe stretches into end socket inside; Described gas-liquid inlet tube tangentially passes in cylinder.
The feature of technique scheme and further improvement:
Middle part, the described bucket end is to cylinder internal protrusion, and pillar upper end is welded and fixed with the middle part at the bucket end.
On the sidewall of described escape pipe interface, be also provided with the pipe blow-through that passes into cylinder inside.
The beneficial effects of the utility model are, tangentially pass into cylinder by gas-liquid entrance, allow the water vapour entering fast rotate in cylinder, produce centrifugal force and carry out the solution that Separation of Water steam is carried secretly, simultaneously, because the bellend of conical pipe stretches into end socket inside, the bellend limit of conical pipe and end socket inwall form less angle, while causing water vapour to flow to end socket and flow to again escape pipe interface along cylinder inwall, produce strong whirlpool, the solution that steam is carried secretly carries out centrifugation again, increase gas-liquid separation effect, middle part at the bottom of pillar upper end is welded on barrel, and bucket end middle part inwardly protruding, make pillar and the bucket end form beveled structure, be conducive to the stable of separator, saved separator floor space simultaneously.
Accompanying drawing explanation
With the specific embodiment, structure of the present utility model and function are further described with reference to the accompanying drawings below:
Fig. 1 is the structural representation of a kind of gas-liquid separator of the present utility model.
In the drawings: 1, cylinder; 2, escape pipe interface; 3, conical pipe; 4, end socket; 5, gas-liquid inlet tube; 6, the bucket end; 7, liquid outlet; 8, pillar; 9, pipe blow-through.
The specific embodiment
With reference to figure 1, a kind of gas-liquid separator of the present utility model, comprise cylinder (1), be provided with end socket (4) in cylinder (1) upper end, on end socket (4), be provided with escape pipe interface (2), at the bottom of cylinder (1) lower end is provided with barrel (6), (6) central authorities at the bottom of pillar (8) is supported on barrel.The bucket end (6) middle part is to cylinder (1) internal protrusion, and pillar (8) upper end is welded and fixed with the middle part of bucket end (6).Cylinder (1) below is provided with gas-liquid inlet tube (5), and bucket (6) edge, the end is provided with liquid outlet (7).Escape pipe interface (2) connects conical pipe (3), and the bellend of conical pipe (3) stretches into end socket (4) inside.Gas-liquid inlet tube (5) tangentially passes in cylinder (1).
In the time passing into steam fast to gas-liquid inlet tube (5), steam is forced to along rotating upwelling to escape pipe interface (2) along cylinder (1) inwall, in rotation, be separated because of the solution in centrifugal force steam, simultaneously, because the bellend of conical pipe (3) stretches into end socket (4) inside, the bellend limit of conical pipe (3) and end socket (4) form less angle, while causing water vapour to flow to end socket (4) and flow to again escape pipe interface (2) along cylinder (1) inwall, produce strong whirlpool in angle, the solution that steam is carried secretly carries out centrifugation again, increase gas-liquid separation effect.
Simultaneously, because (6) middle part at the bottom of bucket is to cylinder (1) internal protrusion, pillar (8) upper end is welded and fixed with the middle part of bucket end (6), makes pillar (8) and the bucket end (6) form beveled structure, be conducive to the Stability Analysis of Structures of separator, saved separator floor space simultaneously.Liquid outlet (7) is positioned at bucket (6) edge, the end of cylinder (1), and due to (6) middle part projection at the bottom of bucket, at the bottom of making barrel, (6) border area forms low-lyingly, is conducive to the recovery of solution.The sidewall of escape pipe interface (2) is also provided with and passes into the inner pipe blow-through (9) of cylinder (1), can pass into if desired cleaning fluid cylinder (1) inside is rinsed.
Obviously, those skilled in the art can carry out various changes and modification and not depart from spirit and scope of the present utility model the utility model.Like this, if within of the present utility model these are revised and modification belongs to the scope of the utility model claim and equivalent technologies thereof, the utility model also comprises these changes and modification interior.
Claims (3)
1. a gas-liquid separator, comprise cylinder (1), be arranged on the end socket (4) of cylinder (1) upper end, be arranged on the escape pipe interface (2) on end socket (4), be arranged on the bucket end (6) of cylinder (1) lower end, pillar (8) of (6) central authorities at the bottom of being supported on barrel; Described cylinder (1) below is provided with gas-liquid inlet tube (5), and described bucket (6) edge, the end is provided with liquid outlet (7); It is characterized in that, described escape pipe interface (2) connects conical pipe (3), and the bellend of conical pipe (3) stretches into end socket (4) inside; Described gas-liquid inlet tube (5) tangentially passes in cylinder (1).
2. a kind of gas-liquid separator according to claim 1, is characterized in that, the described bucket end (6) middle part is to cylinder (1) internal protrusion, and pillar (8) upper end is welded and fixed with the middle part of bucket end (6).
3. a kind of gas-liquid separator according to claim 1, is characterized in that, is also provided with and passes into the inner pipe blow-through (9) of cylinder (1) on the sidewall of described escape pipe interface (2).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320778658.6U CN203591652U (en) | 2013-11-28 | 2013-11-28 | Gas-liquid separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320778658.6U CN203591652U (en) | 2013-11-28 | 2013-11-28 | Gas-liquid separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203591652U true CN203591652U (en) | 2014-05-14 |
Family
ID=50672602
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320778658.6U Expired - Fee Related CN203591652U (en) | 2013-11-28 | 2013-11-28 | Gas-liquid separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203591652U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105854324A (en) * | 2016-04-25 | 2016-08-17 | 钮德明 | Jet type gas-liquid contact evaporator |
| CN106039774A (en) * | 2016-07-12 | 2016-10-26 | 西南石油大学 | Experimental device for separating gas-liquid mixture and measuring gas volume and liquid volume |
-
2013
- 2013-11-28 CN CN201320778658.6U patent/CN203591652U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105854324A (en) * | 2016-04-25 | 2016-08-17 | 钮德明 | Jet type gas-liquid contact evaporator |
| CN106039774A (en) * | 2016-07-12 | 2016-10-26 | 西南石油大学 | Experimental device for separating gas-liquid mixture and measuring gas volume and liquid volume |
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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: 20140514 Termination date: 20151128 |