CN202893539U - Cyclone oil-water or oil-gas separation device - Google Patents
Cyclone oil-water or oil-gas separation device Download PDFInfo
- Publication number
- CN202893539U CN202893539U CN 201220342490 CN201220342490U CN202893539U CN 202893539 U CN202893539 U CN 202893539U CN 201220342490 CN201220342490 CN 201220342490 CN 201220342490 U CN201220342490 U CN 201220342490U CN 202893539 U CN202893539 U CN 202893539U
- Authority
- CN
- China
- Prior art keywords
- oil
- eddy flow
- section
- pipe
- 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
Links
Images
Landscapes
- Cyclones (AREA)
Abstract
The utility model relates to a cyclone oil-water or oil-gas separation device. The cyclone oil-water or oil-gas separation device comprises a pollution discharge pipe, a cyclone section, a diversion and isolation pipe, a first acceleration section, a separation section, a second acceleration section, a flow stabilizing section and a middle shaft, wherein the pollution discharge pipe, the cyclone pipe, the first acceleration section, the separation section, the second acceleration and the flow stabilizing section are respectively connected in a way that the lower end is connected with the upper end; and the diversion and isolation pipe is arranged in the cyclone section, the upper end of the middle shaft arranged in the diversion and isolation pipe is higher than the upper end surface of the pollution discharge pipe, and the lower end surface of the middle shaft is higher than the lower edge of the first acceleration section. The cyclone section is of an oval structure. The cyclone oil-water or oil-gas separation device can separate oil and water, separate oil and gas and improve the separation efficiency to the greatest extent; and simultaneously, the oil and the water, as well as the oil and the gas can not be re-mixed during startup and shutdown of a cyclone separator, so that the cyclone oil-water or oil-gas separation device is more practical.
Description
Technical field
The utility model patent relates to the oil water separator in a kind of profit-oil gas centrifugal separation technology field, is particularly useful for a kind of of the industries such as oil field, petrochemical industry.
Background technology
Traditional oil water separator, its primary structure as shown in Figure 1, this traditional oil water separator comprises blow-off pipe 1, feed zone 10, accelerating sections 11, segregation section 12 and water exit end 13; And feed zone is cylindrical structure, on blow-off pipe 1 lower end and the feed zone along concordant.Generally can only be used for carrying out water-oil separating, can not carry out Oil-gas Separation, and when startup and shutdown, also can cause profit and oil gas again to mix, thereby make the efficient of water-oil separating low.
Because the defective that above-mentioned existing traditional oil water separator exists to founding a kind of a kind of eddy flow profit or gas and oil separating plant of new structure, can be improved general existing traditional oil water separator, make it have more practicality.Through constantly research, design, and after repeatedly studying sample and improvement, finally create the present invention who has practical value.
Summary of the invention
The purpose of this utility model is, overcome the defective that existing traditional oil water separator exists, and provide a kind of a kind of eddy flow profit or gas and oil separating plant of new structure, technical problem to be solved be make it can separate profit again can separation oil and gas, improve to greatest extent the efficient of separating, thereby more be suitable for practicality.
Another purpose of the present utility model is, a kind of eddy flow profit or gas and oil separating plant are provided, and technical problem to be solved is that profit and oil gas can not mix again when making its cyclone separator startup and shutdown, thereby more is suitable for practicality.
The purpose of this utility model and solve its technical problem and realize by the following technical solutions.According to a kind of eddy flow profit or the gas and oil separating plant that the utility model proposes, comprise blow-off pipe, accelerating sections, segregation section, its characteristics are: also comprise eddy flow section, water conservancy diversion isolated tube, steady flow segment and axis, wherein said accelerating sections comprises the first accelerating sections and the second accelerating sections.Wherein, what the blow-off pipe lower end joined is the upper end of eddy flow section, and this eddy flow section lower end joins is the first accelerating sections upper end, and what join with the lower end of accelerating sections is the upper end of segregation section, what the lower end of this segregation section joined is the upper end of the second accelerating sections, and what join with the lower end of accelerating sections is the steady flow segment upper end.These a plurality of charging apertures are located at the side of eddy flow section, and described water conservancy diversion isolated tube is arranged on the eddy flow intersegmental part.The purpose of this utility model and solve its technical problem and also can be applied to the following technical measures to achieve further.
Aforesaid a kind of eddy flow profit or gas and oil separating plant, wherein said eddy flow section is oval structure.
Aforesaid a kind of eddy flow profit or gas and oil separating plant, its characteristics are: described water conservancy diversion isolated tube external diameter is less than the blow-off pipe internal diameter, and between the external diameter of this water conservancy diversion isolated tube and blow-off pipe internal diameter liquid or gas are passed through, both gaps are that 2-6mm, particularly 4mm are best.
Aforesaid a kind of eddy flow profit or gas and oil separating plant, its characteristics are: the upper end that is arranged on inner axis is higher than the upper surface of blow-off pipe, this axis lower surface is higher than the lower edge of the first accelerating sections, both spacings are in the scope of 4-10cm, and the material of described axis is stainless steel, plastics or other materials.
By technique scheme, the utility model can reach suitable technological progress and practicality, and has value on the industry, and it has following advantages at least:
1, the utility model is owing to having adopted disciform eddy flow section, so that enter after the eddy flow section produces eddy flow with the mixing material of pressure, sufficient space is left in the centre, to guarantee that oil or the gas that will separate can rise faster, set up the second accelerating sections in the lower end of segregation section simultaneously, make it both can satisfy the purpose of water-oil separating, also satisfied simultaneously the purpose of carrying out Oil-gas Separation, increase the efficient of separating, compared with traditional cyclone pipe, can raise the efficiency 1-2 doubly.
2, simultaneously, the utility model is after the eddy flow intersegmental part has been set up the water conservancy diversion isolated tube, guarantee that the pending mixing material that just enters from feed zone can not be brought into fuel-displaced or gas outlet, particularly equipment just opened or device shutdown in, avoided the situation of batch mixing to occur.
3, in addition, the utility model blow-off pipe is until middle shaft structure is set up in the first accelerating sections inside, behind the beginning eddy flow, because the effect of centrifugal force, the oil that density to be separated is lighter or can be smoothly directly make progress along the axis of design, so that discharging is more smooth, thereby promote the efficient of separating, reduced the pressure of cyclone separator charging.
4, in sum: after adopting the technical solution of the utility model, designed equipment has not only been avoided the phenomenon of batch mixing when switchgear, and the efficient of separation also can be provided simultaneously, compares its efficient with traditional equipment and approximately improves 1-2 doubly.
Above-mentioned explanation only is the general introduction of technical solutions of the utility model, for can clearer understanding technological means of the present utility model, and can be implemented according to the content of specification, below with preferred embodiment of the present utility model and cooperate accompanying drawing to be described in detail as follows.
The specific embodiment of the present utility model is provided in detail by following examples and accompanying drawing thereof.
Description of drawings
Fig. 1 is the structural representation of prior art;
Fig. 2 is structural representation of the present utility model;
Fig. 3 is eddy flow section cross-sectional configuration schematic diagram of the present utility model.
1: blow-off pipe 2: the eddy flow section
3: 4: the first accelerating sections of water conservancy diversion distance piece
5: 6: the second accelerating sections of segregation section
7: steady flow segment 8: axis
9: charging aperture 10: feed zone
11: accelerating sections 12: segregation section
13: water exit end
The specific embodiment
Be to reach technological means and the effect that predetermined utility model purpose is taked for further setting forth the utility model, below in conjunction with accompanying drawing and preferred embodiment, to according to a kind of eddy flow profit or its specific embodiment of gas and oil separating plant, structure, feature and the effect thereof that the utility model proposes, be described in detail as follows.
See also Fig. 2, shown in Figure 3, a kind of eddy flow profit or the gas and oil separating plant of the utility model preferred embodiment, it mainly comprises blow-off pipe 1, eddy flow section 2, water conservancy diversion isolated tube 3, the first accelerating sections 4, segregation section 5, the second accelerating sections 6, steady flow segment 7 and axis 8: wherein: the lower end of blow-off pipe 1 is right after the upper end of eddy flow section 2, what the lower end of this eddy flow section 2 joined is the upper end of the first acceleration 4, what join with the lower end of accelerating end 4 is the upper end of segregation section 5, the join upper end of the second accelerating sections 6, the lower end of this segregation section 5, what join with the lower end of accelerating end 6 is the upper end of steady flow segment 7, a plurality of charging apertures 9 are located at the side of eddy flow section 2, and described water conservancy diversion isolated tube 3 is arranged on eddy flow section 2 inside.
Wherein, eddy flow section 2 is oval structure, the present embodiment is provided with 2 charging apertures 9 and distributes respectively and (see figure 3) is set in the two sides of eddy flow section, and the size of this charging aperture 9 designs separately according to the size of inlet amount, the size of equipment and the size of production capacity to be processed.Described water conservancy diversion isolated tube 3 external diameters are less than the internal diameter of blow-off pipe 1, and between the internal diameter of water conservancy diversion isolated tube 3 external diameters and blow-off pipe 1 liquid or gas are passed through, and this water conservancy diversion isolated tube 3 is hollow tube.The axis 8 that is arranged on blow-off pipe 1 and water conservancy diversion isolated tube 3 inside is solid construction, can adopt stainless steel or plastic material, and the top of this axis 8 is higher than blow-off pipe 1, and its axis 8 bottoms can not surpass the lower edge of the first accelerating sections 4.The diameter of this axis 8 is 15-20mm, and material is stainless steel or composite plastic, and the lower edge of axis is a little more than the upper edge of the first accelerating sections 4, apart from being preferably between the 4-10cm.
The utility model is owing to having adopted disciform eddy flow section, so that enter after the eddy flow section produces eddy flow with the mixing material of pressure, sufficient space is left in the centre, to guarantee that oil or the gas that will separate can rise faster, simultaneously set up the second accelerating sections 6 in the inside, bottom of segregation section 5, increased the efficient of separating, compare with traditional cyclone pipe, can raise the efficiency 1-2 doubly. simultaneously, the utility model is after water conservancy diversion isolated tube 3 has been set up in eddy flow section 2 inside, guarantee that the firm pending mixing material that enters from the charging aperture 9 of eddy flow section 2 can not be brought into blow-off pipe 1, particularly when the utility model has just been opened or closed, avoided the situation of batch mixing to occur.In addition, axis 8 of the present utility model, behind the beginning eddy flow, because the effect of centrifugal force, the oil that density to be separated is lighter or can be smoothly directly make progress along the axis 8 of design so that discharging is more smooth, thereby has promoted the efficient of separating.
The water conservancy diversion isolated tube 3 of the utility model application is of a size of 2-6mm with the gap of blow-off pipe 1, and is particularly effective about 4mm;
The utility model has been set up the second accelerating sections 6 below segregation section 5, can guarantee more fully the Re-isolation of pollutant, more is conducive to guarantee the purity of separating.
The above, it only is preferred embodiment of the present utility model, be not that the utility model is done any pro forma restriction, although the utility model discloses as above with preferred embodiment, yet be not to limit the utility model, any those skilled in the art, within not breaking away from the technical solutions of the utility model scope, when the technology contents that can utilize above-mentioned announcement is made a little change or is modified to the equivalent embodiment of equivalent variations, in every case be the content that does not break away from technical solutions of the utility model, any simple modification that foundation technical spirit of the present utility model is done above embodiment, equivalent variations and modification all still belong in the scope of technical solutions of the utility model.
Claims (5)
1. an eddy flow profit or gas and oil separating plant, comprise blow-off pipe (1), accelerating sections, segregation section (5), it is characterized in that: also comprise eddy flow section (2), water conservancy diversion isolated tube (3), steady flow segment (7) and axis (8), wherein said accelerating sections comprises the first accelerating sections (4) and the second accelerating sections (6), wherein, what blow-off pipe (1) lower end joined is the upper end of eddy flow section (2), what this eddy flow section (2) lower end joined is the first accelerating sections (4) upper end, what join with the lower end of accelerating sections (4) is the upper end of segregation section (5), what the lower end of this segregation section (5) joined is the upper end of the second accelerating sections (6), what join with the lower end of accelerating sections (6) is steady flow segment (7) upper end, a plurality of charging apertures (9) are located at the side of eddy flow section (2), and described water conservancy diversion isolated tube (3) is arranged on eddy flow section (2) inside.
2. a kind of eddy flow profit according to claim 1 or gas and oil separating plant is characterized in that: described eddy flow section (2) is oval structure.
3. a kind of eddy flow profit according to claim 1 or gas and oil separating plant, it is characterized in that: described water conservancy diversion isolated tube (3) external diameter is less than blow-off pipe (1) internal diameter, and between the external diameter of this water conservancy diversion isolated tube (3) and blow-off pipe (1) internal diameter liquid or gas are passed through, both gaps are 2-6mm.
4. the described a kind of eddy flow profit of any one or gas and oil separating plant according to claim 1-3, it is characterized in that: the described upper end that is arranged on blow-off pipe (1), water conservancy diversion isolated tube (3) and the first accelerating sections 4 inner axis (8) is higher than the upper surface of blow-off pipe (1), this axis (8) lower surface is higher than the lower edge of the first accelerating sections (4), both spacings are in the scope of 4-10cm, and the material of described axis (8) is stainless steel, plastics or other materials.
5. a kind of eddy flow profit according to claim 3 or gas and oil separating plant is characterized in that: the best 4mm of being in the gap between the external diameter of this water conservancy diversion isolated tube (3) and blow-off pipe (1) internal diameter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220342490 CN202893539U (en) | 2012-07-13 | 2012-07-13 | Cyclone oil-water or oil-gas separation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220342490 CN202893539U (en) | 2012-07-13 | 2012-07-13 | Cyclone oil-water or oil-gas separation device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202893539U true CN202893539U (en) | 2013-04-24 |
Family
ID=48114261
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220342490 Expired - Fee Related CN202893539U (en) | 2012-07-13 | 2012-07-13 | Cyclone oil-water or oil-gas separation device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202893539U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111298509A (en) * | 2020-02-14 | 2020-06-19 | 东北石油大学 | Multistage cylinder oil-water separator |
-
2012
- 2012-07-13 CN CN 201220342490 patent/CN202893539U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111298509A (en) * | 2020-02-14 | 2020-06-19 | 东北石油大学 | Multistage cylinder oil-water separator |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102225382B (en) | Pitting oil collecting curved cyclone of overflow pipe | |
| CN102423549B (en) | Dewatering apparatus and oil-water cyclone separator of pipe type distributor oil-water separator | |
| CN201648141U (en) | Multiphase separating system for oil-containing wastewater treatment | |
| CN202224255U (en) | Symmetrical double-rotation type swirler | |
| CN102198984A (en) | Multiphase separation method and system for processing oily waste water | |
| US11123754B2 (en) | Liquid-liquid-solid three-phase separator for waste oil | |
| CN200991662Y (en) | Cascade type cyclone separator | |
| CN205391820U (en) | Tubular profit hydrocyclone separation equipment | |
| CN201519621U (en) | Gas-liquid-solid three-phase separated water cyclone | |
| CN102251765A (en) | Axial type inlet oil-water cyclone separator | |
| CN202447206U (en) | Adjustable gas liquid separation device | |
| CN208726806U (en) | Pipe type oil-water separator | |
| CN206188452U (en) | Oil -water separator | |
| CN202893539U (en) | Cyclone oil-water or oil-gas separation device | |
| CN108328686B (en) | Multi-rotation gravity drive type oil-water coalescence-separation tank | |
| CN103537386A (en) | Rotational flow oil-water or oil-gas separation device | |
| CN203999038U (en) | Cyclone-type water-and-oil separator | |
| CN201603478U (en) | Novel gas-liquid-solid three-phase integrated separator | |
| CN105999770B (en) | A kind of profit spiral stream guidance separator | |
| CN203222698U (en) | Scummer used for purifying low-concentration paper pulp | |
| CN201962249U (en) | Electric emulsion breaker | |
| CN203155401U (en) | Feeding distributor of horizontal screw sedimentation centrifuge | |
| CN206965950U (en) | A kind of concentration-type cyclone | |
| CN102500136A (en) | Combined cylindrical oil-water cyclone separating device | |
| CN2808309Y (en) | Stratification ore concentrator |
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: 20130424 Termination date: 20140713 |
|
| EXPY | Termination of patent right or utility model |