CN201702042U - Gas-liquid separator - Google Patents
Gas-liquid separator Download PDFInfo
- Publication number
- CN201702042U CN201702042U CN2010201549634U CN201020154963U CN201702042U CN 201702042 U CN201702042 U CN 201702042U CN 2010201549634 U CN2010201549634 U CN 2010201549634U CN 201020154963 U CN201020154963 U CN 201020154963U CN 201702042 U CN201702042 U CN 201702042U
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- CN
- China
- Prior art keywords
- gas
- liquid
- separator
- housing
- baffling
- 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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- Separating Particles In Gases By Inertia (AREA)
- Cyclones (AREA)
Abstract
The utility model discloses a gas-liquid separator comprising a shell, wherein a tangential gas inlet is arranged on the side wall of the shell, the top of the shell is provided with a gas outlet, the bottom of the shell is provided with a liquid outlet, a gas-liquid baffling separating device is arranged in a cavity in the shell, and the gas inlet is positioned blow the gas-liquid baffling separating device. The gas-liquid separator not only is suitable for gas-liquid separation in chemical industry, but also suitable for separating dust, particle and the like in gas.
Description
Technical field
The utility model relates to the chemical industry equipment field, relates in particular to a kind of separator that free eddy flow carries out gas-liquid separation of using.
Background technology
In chemical industry, often to use gas-liquid separator, be used for the liquid in the gas is removed, with gas or liquids recovery utilization, mechanical separation method commonly used at present has: isolated by filtration, gravity inertial separation, cyclonic separation and the separation of film separate type etc.Cyclonic separating apparatus simple structure is wherein invested for a short time, and maintenance maintenance is convenient, and power consumption is low, and is not subjected to the restriction of divided gas flow temperature concentration, therefore becomes chemical industry and uses maximum gas-liquid separation devices.But the not ideal enough or complex structure of the general separating effect of Cyclonic separating apparatus commonly used is not suitable for industrial applications.
Summary of the invention
Technical problem to be solved in the utility model is: at the deficiency that gas-liquid separator in the prior art exists, provide a kind of simple in structure, easy operating, gas-liquid separator that separative efficiency is high
For solving the problems of the technologies described above, the technical solution of the utility model is:
Gas-liquid separator, comprise housing, the sidewall of described housing is provided with tangential air inlet, the top of described housing is provided with the gas outlet, the bottom of described housing is provided with liquid outlet, be provided with gas-liquid baffling separator in the internal cavities of described housing, described air inlet is positioned at the below of described gas-liquid baffling separator.
Wherein, described gas-liquid baffling separator comprises lower baffle and upper baffle, described lower baffle is the back taper of bottom opening, described upper baffle is open-topped taper, and described gas-liquid baffling separator is divided into the internal cavities of housing the cyclone separating chamber that is positioned at described lower baffle below, is positioned at the rectification chamber in the middle of lower baffle and the upper baffle and is positioned at the flash chamber of upper baffle top.
As a kind of improvement, described gas-liquid baffling separator is fixed on the described inner walls, and is provided with fixed head and is connected with housing.
As further improvement, the top of described housing is provided with vacuum interface.
Owing to adopted technique scheme, the beneficial effects of the utility model are:
1, gas-liquid baffling separator of the present utility model is divided into the internal cavities of housing the cyclone separating chamber that is positioned at the lower baffle below, is positioned at the rectification chamber in the middle of lower baffle and the upper baffle and is positioned at the flash chamber of upper baffle top, therefore enter the shell separator gas inside, at first separate at the indoor first time cyclone liquid gas of carrying out of cyclonic separation, when entering the rectification chamber then, locular wall vary in diameter because of the rectification chamber, gas-liquid can be carried out the second time and be separated, the rectification chamber less by bore enters flash chamber, can obtain dilatation flash distillation for the third time.
2, the lower baffle of the utility model gas-liquid baffling separator is a back taper, when the gas that enters shell separator rotates in the space of cyclone separating chamber, the drop in the gas because deadweight or rotary course run into lower baffle and fall.
3, the utility model is provided with vacuum interface on the top of shell separator, can operate under vacuum condition, strengthens separating effect.
Description of drawings
Below in conjunction with drawings and Examples the utility model is further specified.
Fig. 1 is the structure cutaway view of the utility model embodiment.
Fig. 2 is the cutaway view at A-A place among Fig. 1.
Among the figure, 1. housing; 11. air inlet; 12. gas outlet; 13. liquid outlet; 14. vacuum interface; 2. gas-liquid baffling separator; 21. lower baffle; 22. upper baffle; 23. fixed head; 3. cyclone separating chamber; 4. rectification chamber; 5. flash chamber.
The specific embodiment
As shown in the figure, gas-liquid separator, comprise housing 1, the sidewall of described housing 1 is provided with tangential air inlet 11, the top of described housing 1 is provided with gas outlet 12, and the bottom of described housing 1 is provided with liquid outlet 13, is provided with gas-liquid baffling separator 2 in the internal cavities of described housing 1, described air inlet 11 is positioned at the below of described gas-liquid baffling separator 2, and the top of described housing 1 is provided with vacuum interface 14.
Wherein, described gas-liquid baffling separator 2 comprises lower baffle 21 and upper baffle 22, described lower baffle 21 is the back taper of bottom opening, described upper baffle 22 is open-topped taper, and described gas-liquid baffling separator 2 is divided into the internal cavities of housing 1 cyclone separating chamber 3 that is positioned at described lower baffle 21 belows, is positioned at the rectification chamber 4 in the middle of lower baffle 21 and the upper baffle 22 and is positioned at the flash chamber 5 of upper baffle 22 tops.Described gas-liquid baffling separator 2 is fixed on described housing 1 inwall, and is provided with fixed head 23 and is connected with housing 1.
During the utility model work, the gas that enters shell separator 1 from tangential air inlet 11 at first rotates in the space of cyclone separating chamber 3, drop in the gas is finished for the first time and is separated because deadweight or rotary course are run into lower baffle 21 and fallen; Gas enters rectification chamber 4 from the back taper import of gas-liquid baffling separator 2 lower baffle 21 then, because the instantaneous expansion in 4 spaces, rectification chamber, gas can obtain flash separation for the second time, gas is in rectification chamber 4 in the uphill process, because the special construction of rectification chamber 4, not only obtained distilling effect, and the drop in the gas is run into once more on the inwall of gas-liquid baffling separator 2 and is fallen; Gas is after rectification chamber 4 enters flash chamber 5, because the instantaneous expansion in space obtains dilatation flash distillation for the third time.Gas after three separation is 12 discharges from the gas outlet, and isolated liquid is discharged from the liquid outlet 13 that is positioned at housing 1 bottom.The utility model is provided with vacuum interface 14, so gas-liquid separation also can carry out under vacuum condition, to strengthen separating effect.
The utility model is not only applicable to gas-liquid separation, and is applicable to dust in the divided gas flow, particle etc.
Claims (4)
1. gas-liquid separator, comprise housing, the sidewall of described housing is provided with tangential air inlet, the top of described housing is provided with the gas outlet, the bottom of described housing is provided with liquid outlet, it is characterized in that: be provided with gas-liquid baffling separator in the internal cavities of described housing, described air inlet is positioned at the below of described gas-liquid baffling separator.
2. gas-liquid separator as claimed in claim 1, it is characterized in that: described gas-liquid baffling separator comprises lower baffle and upper baffle, described lower baffle is the back taper of bottom opening, described upper baffle is open-topped taper, and described gas-liquid baffling separator is divided into the internal cavities of housing the cyclone separating chamber that is positioned at described lower baffle below, is positioned at the rectification chamber in the middle of lower baffle and the upper baffle and is positioned at the flash chamber of upper baffle top.
3. gas-liquid separator as claimed in claim 2 is characterized in that: described gas-liquid baffling separator is fixed on the described inner walls, and is provided with fixed head and is connected with housing.
4. gas-liquid separator as claimed in claim 2 is characterized in that: the top of described housing is provided with vacuum interface.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010201549634U CN201702042U (en) | 2010-04-06 | 2010-04-06 | Gas-liquid separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010201549634U CN201702042U (en) | 2010-04-06 | 2010-04-06 | Gas-liquid separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201702042U true CN201702042U (en) | 2011-01-12 |
Family
ID=43439189
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010201549634U Expired - Fee Related CN201702042U (en) | 2010-04-06 | 2010-04-06 | Gas-liquid separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201702042U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105344165A (en) * | 2015-12-07 | 2016-02-24 | 大连熵华节能科技有限公司 | Gas-water separation device |
| CN105964065A (en) * | 2016-07-27 | 2016-09-28 | 广西田东锦鑫化工有限公司 | Coal tar separator and coal tar separating system adopting same |
| CN106865921A (en) * | 2015-09-22 | 2017-06-20 | 丛爱国 | Purification efficiency is higher, sewage disposal device with Treatment of Sludge |
-
2010
- 2010-04-06 CN CN2010201549634U patent/CN201702042U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106865921A (en) * | 2015-09-22 | 2017-06-20 | 丛爱国 | Purification efficiency is higher, sewage disposal device with Treatment of Sludge |
| CN106915839A (en) * | 2015-09-22 | 2017-07-04 | 丛爱国 | A kind of purification efficiency is higher, sewage disposal device with Treatment of Sludge |
| CN105344165A (en) * | 2015-12-07 | 2016-02-24 | 大连熵华节能科技有限公司 | Gas-water separation device |
| CN105964065A (en) * | 2016-07-27 | 2016-09-28 | 广西田东锦鑫化工有限公司 | Coal tar separator and coal tar separating system adopting same |
| CN105964065B (en) * | 2016-07-27 | 2019-01-04 | 广西田东锦鑫化工有限公司 | Coal tar oil eliminator and the coal tar separation system for using the coal tar oil eliminator |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110112 Termination date: 20110406 |