CN2745632Y - Cyclon oil gas separating device having liquid level automatic controller - Google Patents
Cyclon oil gas separating device having liquid level automatic controller Download PDFInfo
- Publication number
- CN2745632Y CN2745632Y CN 200420097440 CN200420097440U CN2745632Y CN 2745632 Y CN2745632 Y CN 2745632Y CN 200420097440 CN200420097440 CN 200420097440 CN 200420097440 U CN200420097440 U CN 200420097440U CN 2745632 Y CN2745632 Y CN 2745632Y
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- CN
- China
- Prior art keywords
- liquid level
- housing
- spiral
- automatic control
- flow type
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- 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 relates to a cyclone oil-gas separating device having a liquid level automatic controller, which comprises a casing body, a liquid inlet pipe arranged on the casing body, a floating barrel arranged in the casing body and a valve seat thereof, a conical barrel body arranged below the liquid inlet pipe and outside the floating barrel in the casing body, an upper flange assembly and a lower flange assembly arranged on the upper end and the lower end of the casing body. The utility model has the characteristics of favorable separating effect, automatic metering function, simple structure, easy fabrication and manufacture, low cost, etc. The utility model is widely applied to oil extraction separating and metering processes.
Description
One, technical field:
The utility model relates to a kind of oil exploitation gas and oil separating plant, particularly a kind of spiral-flow type automatic control of liquid level gas and oil separating plant.
Two, background technology:
Existing oil exploitation gas and oil separating plant is made of the separation umbrella of installing in housing and the housing, funnel and gauging glass tube device etc., and the shortcoming or the deficiency of its existence are: the liquid that (1) enters is that decanter type separates inferior separating effect.(2) gauge gas metering is for manually carrying out, and workload is big, and error in dipping is also big.
Three, summary of the invention:
The purpose of this utility model provides a kind of improved spiral-flow type automatic control of liquid level gas and oil separating plant, and it can be avoided effectively and overcome shortcoming or the deficiency that exists in the prior art, and making the liquid that enters is that spiral-flow type is separated good separating effect; Gauge gas metering is for carrying out automatically, and workload is little, and error in dipping is also little.
Spiral-flow type automatic control of liquid level gas and oil separating plant described in the utility model, comprise floating drum and valve and the valve seat installed in the feed tube installed on housing and the housing and the housing, the conical shell of it is characterized in that also comprising in the described housing, below the feed tube, floating drum being installed outward, upper flange assembly and lower flange assembly that the housing upper and lower side is installed.
Wherein, described conical shell is to install outside floating drum up big and down smallly.Described feed tube is installed from the housing tangential direction, and its inner is installed on nozzle.Described housing upper and lower side is the total accepted way of doing sth syndeton of flange.Described floating drum system is from macromolecular material, as modified MC nylon etc.
The utility model has following advantage and beneficial effect compared with prior art:
1, it is simplified to be provided with taper below the oil inlet pipe in the housing, and feed tube is installed from the housing tangential direction, and its inner is installed on nozzle, and the oil stream that makes into is directed downwards the formation swirling flow along the simplified inwall of taper, produces optimal separating efficiency.
2, simple in structure, processing and fabricating is easy, and cost is low.
Four, description of drawings
Fig. 1 is the utility model structural representation
Fig. 2 is for pressing shell structure schematic diagram shown in Figure 1
Fig. 3 is for pressing structure schematic top plan view shown in Figure 2
Five, the specific embodiment
With reference to Fig. 1-Fig. 3, a kind of spiral-flow type automatic control of liquid level gas and oil separating plant, comprise floating drum 4 and cone valve 9 and the valve seat 7,8 installed in the feed tube 10 installed on housing 1 and the housing and the housing, the conical shell of also comprise in the described housing, installing feed tube below, floating drum outward 5, upper flange assembly 2 and lower flange assembly 3 that the housing upper and lower side is installed.Guide ring 6 outside the floating drum 4 is installed in the housing 1.
When liquid when oil inlet pipe 10 enters, carrying out swirling flow along conical shell 5 separates, gas rises and discharges from the stack 11 of upper flange assembly 2, and when liquid level was high, floating drum 4 was up, cone valve 9 and valve seat 7 sealings that are installed in upper flange assembly 2 bottoms, at this moment, the housing internal gas pressure raises, and liquid level descends fast and discharges from discharging tube 12, floating drum 4 descends with liquid level, cone valve 9 and valve seat 8 sealings that are installed in lower flange assembly 3 tops.Circulation so successively makes gas-liquid carry out continuous metering on the measuring instrument of installing on stack 11 and the discharging tube 12.
Claims (5)
1, a kind of spiral-flow type automatic control of liquid level gas and oil separating plant, comprise floating drum and valve and the valve seat installed in the feed tube installed on housing and the housing and the housing, the conical shell of it is characterized in that also comprising in the described housing, below the feed tube, floating drum being installed outward, upper flange assembly and lower flange assembly that the housing upper and lower side is installed.
2, spiral-flow type automatic control of liquid level gas and oil separating plant according to claim 1 is characterized in that described conical shell is to install outside floating drum up big and down smallly.
3, spiral-flow type automatic control of liquid level gas and oil separating plant according to claim 1 and 2 is characterized in that described feed tube from the installation of housing tangential direction, and its inner is installed on nozzle.
4, spiral-flow type automatic control of liquid level gas and oil separating plant according to claim 1 and 2 is characterized in that described housing upper and lower side is the total accepted way of doing sth syndeton of flange.
5, spiral-flow type automatic control of liquid level gas and oil separating plant according to claim 1 and 2 is characterized in that described floating drum system from macromolecular material, as modified MC nylon etc.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200420097440 CN2745632Y (en) | 2004-11-05 | 2004-11-05 | Cyclon oil gas separating device having liquid level automatic controller |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200420097440 CN2745632Y (en) | 2004-11-05 | 2004-11-05 | Cyclon oil gas separating device having liquid level automatic controller |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2745632Y true CN2745632Y (en) | 2005-12-14 |
Family
ID=35582218
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200420097440 Expired - Fee Related CN2745632Y (en) | 2004-11-05 | 2004-11-05 | Cyclon oil gas separating device having liquid level automatic controller |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2745632Y (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102220923A (en) * | 2011-05-20 | 2011-10-19 | 张银科 | Diesel-air separator for diesel engine |
| CN102560524A (en) * | 2012-03-06 | 2012-07-11 | 中国船舶重工集团公司第七一八研究所 | Gas-liquid separator without leakage |
-
2004
- 2004-11-05 CN CN 200420097440 patent/CN2745632Y/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102220923A (en) * | 2011-05-20 | 2011-10-19 | 张银科 | Diesel-air separator for diesel engine |
| CN102560524A (en) * | 2012-03-06 | 2012-07-11 | 中国船舶重工集团公司第七一八研究所 | Gas-liquid separator without leakage |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |