CN208161293U - A kind of three-level gas-liquid separator - Google Patents
A kind of three-level gas-liquid separator Download PDFInfo
- Publication number
- CN208161293U CN208161293U CN201820467998.XU CN201820467998U CN208161293U CN 208161293 U CN208161293 U CN 208161293U CN 201820467998 U CN201820467998 U CN 201820467998U CN 208161293 U CN208161293 U CN 208161293U
- Authority
- CN
- China
- Prior art keywords
- shell
- plate
- stream guiding
- guiding barrel
- baffle plate
- 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 kind of three-level gas-liquid separators, feature be include shell, cyclone plate, wire mesh demister and stream guiding barrel, overhead gage is fixedly installed in shell, stream guiding barrel is located in shell and upper end is fixedly connected with overhead gage, air inlet is provided on shell, air inlet is located at the lower section of overhead gage, whirlwind sleeve-board is on stream guiding barrel and is fixedly connected with the casing, cyclone plate is located at the lower section of air inlet, multiple deflectors for being distributed uniformly and circumferentially and tilting down are provided on cyclone plate, the lower half portion of stream guiding barrel is located at the lower section of cyclone plate, wire mesh demister is fixed on the interior upper end of stream guiding barrel, the upper end of shell is provided with gas outlet, lower baffle plate is fixedly installed in shell, lower baffle plate is located at below stream guiding barrel, the lower end of shell is provided with liquid outlet port；Advantage is rationally to have appropriately set the structure of cyclone plate and lower baffle plate, and device structure is ingenious, good separating effect, and practicability is high.
Description
Technical field
The utility model relates to gas-liquid separator more particularly to a kind of three-level gas-liquid separators.
Background technique
Natural gas is more cleaned relative to traditional energies such as coal, petroleum, then more relative to new energy such as wind-powered electricity generation, photovoltaics
Economy, the good economy and the feature of environmental protection that natural gas has make the energy ratio shared by it increasing, it is contemplated that future
Natural gas the traditional energies such as coal will be replaced to become the first big main body energy, but the natural gas after exploitation of oil-gas field contains
A large amount of dust and liquid pollutant, it is necessary to purification separation is carried out using special equipment, but purification separation dress at present on the market
Mostly level-one or two poles are set, separating effect is bad, and separative efficiency is relatively low, and operating process is also comparatively laborious.
Summary of the invention
The technical problem to be solved by the utility model is to provide a kind of three-level gas-liquid separator, the device can obtain compared with
The natural gas of high-purity, separating effect is relatively good, and practicability is stronger.
The utility model solves technical solution used by above-mentioned technical problem：A kind of three-level gas-liquid separator, including
Shell, cyclone plate, wire mesh demister and stream guiding barrel are fixedly installed overhead gage, the stream guiding barrel in the shell
In the shell and upper end is fixedly connected with the overhead gage, and air inlet is provided on the shell, described
The inner peripheral surface of air inlet and the shell is tangent and is located at the lower section of the overhead gage, and the whirlwind sleeve-board is described
Stream guiding barrel on and be fixedly connected with the shell, the cyclone plate is located at the lower section of the air inlet, described
Multiple deflectors for being distributed uniformly and circumferentially and tilting down, the lower half of the stream guiding barrel are provided on cyclone plate
For quartile in the lower section of the cyclone plate, the wire mesh demister is fixed on the interior upper end of the stream guiding barrel, described
The upper end of shell is provided with gas outlet, and lower baffle plate is fixedly installed in the shell, and the lower baffle plate is located at described lead
Below flow cartridge body, the lower end of the shell is provided with liquid outlet port.
Further, the efficient silk screen of DP type that the wire mesh demister uses with a thickness of 300 millimeters.
Further, the lower baffle plate is at least two pieces, and between the upper and lower every setting.
Further, the lower baffle plate is made of muti-piece lower baffle plate piecemeal, and the lower baffle plate piecemeal leads between any two
It crosses lower baffle plate link block to be fixedly connected, facilitates the integral installation and maintenance of lower baffle plate.
Further, the cyclone plate is by muti-piece whirlwind group board group at the whirlwind group plate passes through rotation between any two
Wind link block is fixedly connected, and facilitates the integral installation and maintenance of whirlwind group plate.
Compared with prior art, the utility model has the advantages that：The equipment passes through cyclonic separation, gravity settling separation, silk
Net foam removal separation realizes three-level gas-liquid separation, and separating effect is better, and obtained natural gas purity is more increased, due to cyclone plate
On be provided with multiple deflectors for being distributed uniformly and circumferentially and tilting down, the gas-liquid of cyclone plate can be further improved
Separating effect has rationally appropriately set the structure of cyclone plate and lower baffle plate, and cyclone plate and lower baffle plate has been pacified with bulk form
Dress, device structure is compact ingenious, has better separative efficiency and practicability, especially suitable for the natural gas after exploitation of oil-gas field
Purification separation occasion.
Detailed description of the invention
Fig. 1 is the schematic diagram of internal structure of the utility model；
Fig. 2 is the structural schematic diagram of the cyclone plate of the utility model；
Fig. 3 is the structural schematic diagram of the lower baffle plate of the utility model.
Specific embodiment
The utility model is described in further detail below in conjunction with figure embodiment.
As shown, a kind of three-level gas-liquid separator, including shell 1, cyclone plate 2, wire mesh demister 3 and stream guiding barrel 4,
Overhead gage 5 is fixedly installed in shell 1, stream guiding barrel 4 is located in shell 1 and upper end is fixedly connected with overhead gage 5, on shell 1
It is provided with air inlet 11, the inner peripheral surface of air inlet 11 and shell 1 is tangent and is located at the lower section of overhead gage 5, and 2 sets of cyclone plate are being led
It is fixedly connected on flow cartridge body 4 and with shell 1, cyclone plate 2 is located at the lower section of air inlet 11, is provided on cyclone plate 2 multiple along circle
The deflector 21 that circumferential direction is uniformly distributed and tilts down, the lower half portion of stream guiding barrel 4 are located at the lower section of cyclone plate 2, silk screen
Demister 3 is fixed on the interior upper end of stream guiding barrel 4, and the upper end of shell 1 is provided with gas outlet 12, is fixedly installed down in shell 1
Baffle 6, lower baffle plate 6 are located at 4 lower section of stream guiding barrel, and the lower end of shell 1 is provided with liquid outlet port 13.
Wire mesh demister 3 is using the efficient silk screen of DP type with a thickness of 300 millimeters.
Lower baffle plate 6 is at least two pieces, and between the upper and lower every setting.Lower baffle plate 6 is made of muti-piece lower baffle plate piecemeal 61, lower baffle plate
Piecemeal 61 is fixedly connected by lower baffle plate link block 62 between any two.
Cyclone plate 2 is made of muti-piece whirlwind group plate 22, and whirlwind group plate 22 connects by the way that whirlwind link block 23 is fixed between any two
It connects.
The working principle of the three-level gas-liquid separator：First order cyclonic separation stage, air-flow pass through air inlet 11 tangentially
It is rotated into shell 1, and in the space of 1 inside of 4 outside of stream guiding barrel and shell, cyclone plate 2 is arranged in air inlet
Mouth 11 slightly below, can generate shunting effect to gas, strengthen solution-air, gas-solid separative efficiency, pass through the gas of cyclone plate 2
Stream continues rotary eccentric movement, and the solid of larger particles and drop can be removed from gas and be separated by centrifugal inertial force；Gas
Stream enters the second level gravity settling separation stage, and due to the difference of specific gravity of gas, liquid, solid, gas is along 4 inside of stream guiding barrel
It moves upwards, and carries a small amount of liquid and solid particle secretly, during air-flow moves upwards, influenced by gravity, therein
The upward speed of grain slightly larger drop and solid can be smaller and smaller and finally generates downward speed, and gas then continues up stream
It is dynamic to enter third separation phase, the liquid and solid that the first separation phase is isolated then carry secretly a small amount of gas along equipment continue to
Lower movement, pass through lower baffle plate 6 when, a small amount of gas can be stopped by lower baffle plate 6 and with solid particle and drop separation, then to
Upper movement, solid particle and drop continue to move downward by the gap of lower baffle plate 6；Third level silk screen foam removal separation phase, is adopted
Be enlarged to 300mm with the efficient silk screen of DP type, and by screen thickness, increase gas-liquid separation effect, 3 top of wire mesh demister there are compared with
Big space works as a buffer the gas after isolation of purified.
Claims (5)
1. a kind of three-level gas-liquid separator, it is characterised in that including shell（1）, cyclone plate（2）, wire mesh demister（3）And water conservancy diversion
Cylinder（4）, the shell（1）Inside it is fixedly installed overhead gage（5）, the stream guiding barrel（4）Positioned at the shell（1）
Interior and upper end and the overhead gage（5）It is fixedly connected, the shell（1）On be provided with air inlet（11）, the air inlet
Mouthful（11）With the shell（1）Inner peripheral surface it is tangent and be located at the overhead gage（5）Lower section, the cyclone plate
（2）It covers in the stream guiding barrel（4）It is upper and with the shell（1）It is fixedly connected, the cyclone plate（2）Positioned at described
Air inlet（11）Lower section, the cyclone plate（2）On be provided with multiple be distributed uniformly and circumferentially and what is tilted down leads
Flowing plate（21）, the stream guiding barrel（4）Lower half portion be located at the cyclone plate（2）Lower section, the silk screen foam removal
Device（3）It is fixed on the stream guiding barrel（4）Interior upper end, the shell（1）Upper end be provided with gas outlet（12）, described
Shell（1）Inside it is fixedly installed lower baffle plate（6）, the lower baffle plate（6）Positioned at the stream guiding barrel（4）Lower section, it is described
Shell（1）Lower end be provided with liquid outlet port（13）.
2. a kind of three-level gas-liquid separator as described in claim 1, it is characterised in that：The wire mesh demister（3）Using
With a thickness of 300 millimeters of the efficient silk screen of DP type.
3. a kind of three-level gas-liquid separator as described in claim 1, it is characterised in that：The lower baffle plate（6）It is at least two
Block, and between the upper and lower every setting.
4. a kind of three-level gas-liquid separator as described in claim 1, it is characterised in that：The lower baffle plate（6）By under muti-piece
Baffle piecemeal（61）Composition, the lower baffle plate piecemeal（61）Pass through lower baffle plate link block between any two（62）It is fixedly connected.
5. a kind of three-level gas-liquid separator as described in claim 1, it is characterised in that：The cyclone plate（2）It is revolved by muti-piece
Wind group plate（22）Composition, the whirlwind group plate（22）Pass through whirlwind link block between any two（23）It is fixedly connected.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820467998.XU CN208161293U (en) | 2018-04-04 | 2018-04-04 | A kind of three-level gas-liquid separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820467998.XU CN208161293U (en) | 2018-04-04 | 2018-04-04 | A kind of three-level gas-liquid separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208161293U true CN208161293U (en) | 2018-11-30 |
Family
ID=64371700
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820467998.XU Expired - Fee Related CN208161293U (en) | 2018-04-04 | 2018-04-04 | A kind of three-level gas-liquid separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208161293U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110835557A (en) * | 2019-12-06 | 2020-02-25 | 中冶焦耐(大连)工程技术有限公司 | Gas oil removing device and process |
-
2018
- 2018-04-04 CN CN201820467998.XU patent/CN208161293U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110835557A (en) * | 2019-12-06 | 2020-02-25 | 中冶焦耐(大连)工程技术有限公司 | Gas oil removing device and process |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20181130 Termination date: 20200404 |
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| CF01 | Termination of patent right due to non-payment of annual fee |