CN2907905Y - Cyclone type gas water separator - Google Patents
Cyclone type gas water separator Download PDFInfo
- Publication number
- CN2907905Y CN2907905Y CN 200620116032 CN200620116032U CN2907905Y CN 2907905 Y CN2907905 Y CN 2907905Y CN 200620116032 CN200620116032 CN 200620116032 CN 200620116032 U CN200620116032 U CN 200620116032U CN 2907905 Y CN2907905 Y CN 2907905Y
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- eddy flow
- flow generating
- generating mechanism
- rotational flow
- generating device
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Abstract
The utility model relates to a rotational flow-type air and water separating device comprising a separator frame, a first rotational flow generating device, and a secondary rotational generating device; wherein, the separator frame is a cone and the side wall is provided with a first air inlet mouth, a secondary air inlet mouth and the upper and lower bottoms respectively is provided with an overfall mouth and an underset mouth; the first rotational flow generating device is composed of an air separating canister,a rotational slow petal and a fission of the air separating canister and each part is provided with a space; the rotational flow petal is welded on the side edge of the space and is connected with the inner side of the separator through a rib board; the secondary rotational flow generating device is composed of a secondary rotational flow generating device frame and a nozzle; the side wall of the secondary rotational flow generating device frame is arranged with an air outlet orifice at which a nozzle is arranged; the nozzle is inclined downward; the bottom of the secondary rotational flow generating device frame is arranged with a hole in which the air separating canister and the rotational flow pedal of the first rotational flow generating device extends; the secondary rotational flow generating device is welded with the inner side of the separator frame; and the purposes of high separating efficiency, simple device structure, and small size are achieved.
Description
Technical field
The utility model relates to a kind of separator, particularly be a kind of separator that adopts the spiral-flow type operation principle to carry out gas and fluid separation applications, especially be applied to the gas-water separation in the gas well.
Background technology
The continuous increase of gas well aquifer yield constitutes serious threat to natural gas production, more and more be subjected to people's attention and attention, adopt the downhole gas water separating system, have many advantages that general separator does not have, can use according to different occasions, its operation principle of existing seperator mainly contains centrifugal and spiral-flow type, described centrifugal be to borrow centrifugal force, sedimentation coefficient according to material, quality, the difference of density etc., use powerful centrifugal force and make separating substances, a kind of separation method that concentrates and purify, the principle of spiral-flow type is to produce eddy flow by cyclone, makes mist because secret degree separately, the difference of quality and collide separation.In order to isolate the drop in the natural gas flow in the down-hole, rely on conventional fixed gravitational settling to be difficult to realize.On the one hand, because the pressure of down-hole air-flow is big, flow velocity is fast, temperature is high, can not be with the precipitate and separate device so that the effective time of staying to be provided; Because the downhole gas flow is big, separative efficiency requires high on the other hand, and the size of separator should be very big, and the restriction that is subjected to the space, down-hole can't realize.So must adopt special separator to carry out the gas-water separation of down-hole.
Summary of the invention
The purpose of this utility model is, a kind of spiral-flow type moisture separator is provided, and adopts the spiral-flow type separation mechanism, can be used for separating of gas well natural gas and water, reduce disposal cost, increase and produce the life-span and also improve recovery ratio, minimizing is simplified surface separation to the pollution of environment, increases investment returns.
For achieving the above object, the technical solution adopted in the utility model is, a kind of spiral-flow type moisture trap is provided, and it comprises: separator body, eddy flow generating mechanism, secondary eddy flow generating mechanism; Wherein
Described separator body is a cone, sidewall have air inlet, secondary air inlet mouth and on go to the bottom and have overfall and underflow opening;
A described eddy flow generating mechanism comprises atmolysis cylinder and eddy flow lobe, and atmolysis cylinder is made up of split, and each several part has the space, and described eddy flow lobe is welded on the space lateral margin; Link together by gusset and separator body inboard;
Described secondary eddy flow generating mechanism, comprise secondary eddy flow generating mechanism body, nozzle, the sidewall of described secondary eddy flow generating mechanism body has venthole, the place is provided with nozzle at venthole, described nozzle is downward-sloping, bottom at secondary eddy flow generating mechanism body has a hole, and the atmolysis cylinder of a described eddy flow generating mechanism and eddy flow lobe stretch into wherein, and described secondary eddy flow generating mechanism and separator body inboard weld together; Sidewall at described separator body has a connector, links to each other in order to the air inlet with other spiral-flow type moisture traps, forms series connection, if when working independently, is then sealed by elastic sealing cover; The split of described composition air induction mast be 4 with 90 ° of arrangements, perhaps 3 with 120 ° of arrangements.
Advantage of the present utility model is, handles by twice rotational flow separation, and the separative efficiency height, and device structure is simple, volume is little, maintenance is easier to, and easy to use flexible, and can the series connection of many playscripts with stage directions utility model use.
Below in conjunction with accompanying drawing, to this novel above-mentionedly is described in more detail with other technical characterictic and advantage.
Description of drawings
Fig. 1 is the utility model structural representation;
Fig. 2 is that eddy flow of the utility model produces the structure top cross-sectional view;
Fig. 3 is that the utility model secondary eddy flow produces the structure vertical view.
Description of reference numerals: 1-separator body; 11-separator lower body; 12-separator loam cake; 13-separator overfall; 14-secondary air inlet mouth; The 15-underflow opening; The 16-elastic sealing cover; The 17-bolt; The 18-connector; 2-secondary eddy flow generating mechanism; 21-secondary eddy flow generating mechanism body; The 22-nozzle; 23-secondary eddy flow generating mechanism underflow opening; The 24-venthole; The 3-gusset; Eddy flow generating mechanism of 4-; Air inlet of 41-; 42-eddy flow lobe; The 43-atmolysis cylinder.
The specific embodiment
See also shown in Figure 1, it is a structural representation of the present utility model, comprise separator body 1, an eddy flow generating mechanism 4, secondary eddy flow generating mechanism 2, wherein said separator body 1 is welded by lower body 11 and separator loam cake 12, described separator lower body 11 comprises: an air inlet 41, secondary air inlet mouth 14, separator overfall 13, underflow opening 15, connector 18, a described air inlet 41 and an eddy flow generating mechanism 4 link, secondary air inlet mouth 14 is used for and will sends in the body upper strata with air-flow to be separated, carries out the secondary spiral-flow type and separates; The separator overflow is used for for 13 mouthfuls gas separated is discharged to outside the body, and underflow opening 15 is that isolated water is discharged body.Connector 18 is to be used for being in series with another separator, if unit work then is closed whole connector 18 by screw 17 with elastic sealing cover 16;
See also Fig. 1, shown in Figure 2, a described eddy flow generating mechanism 4, form by atmolysis cylinder 43 and eddy flow lobe 42, atmolysis cylinder 43 is that three parts divide body structure to rearrange for 120 °, also can divide body structure to form (not shown) for 90 ° by four parts, after entering, gas to be separated can flow out at a high speed from the gap of atmolysis cylinder 43, be that gas produces eddy flow by three eddy flow lobes 42 then, described eddy flow lobe 42 is according to 120 ° of void edges that are arranged in atmolysis cylinder 43, mode by welding links together, and have three gussets 3 that split tube 43 is inboard welded together with separator lower body 11, played the supporting fixation;
See also Fig. 1, shown in Figure 2, described secondary eddy flow generating mechanism 2, comprise plurality of nozzles 22, secondary eddy flow generating mechanism body 21, the bottom lateral margin and separator body 1 inboard of described secondary eddy flow generating mechanism body 21 weld together, have some underflow openings 23 in secondary eddy flow generating mechanism body 21 bottoms, the water that is used for secondary rotational flow separation process is produced is discharged, have a hole in bottom centre, the atmolysis cylinder 43 and the eddy flow lobe 42 of a described eddy flow generating mechanism 4 stretch in the secondary eddy flow generating mechanism body 21; Sidewall and upper wall at secondary eddy flow generating mechanism body 21 are arranged with venthole 24 with 90 °, after a gas part to be separated enters into secondary eddy flow generating mechanism body 21 inside, to discharge from venthole 24,24 places are provided with nozzle 22 at venthole, it is directed downwards inclination described nozzle 22, with the gas collisions to be separated that enters by secondary air inlet mouth 14 and produce eddy flow, help gas-water separation.
More than explanation is novel just illustrative for this; and it is nonrestrictive; those of ordinary skills understand; under the situation of the spirit and scope that do not break away from following claims and limited; can make many modifications; change, or equivalence, but all will fall in the protection domain of the present utility model.
Claims (3)
1. spiral-flow type moisture trap is characterized in that it comprises: separator body, eddy flow generating mechanism, secondary eddy flow generating mechanism; Wherein
Described separator body is a cone, sidewall have air inlet, secondary air inlet mouth and on go to the bottom and have overfall and underflow opening;
A described eddy flow generating mechanism comprises atmolysis cylinder and eddy flow lobe, and atmolysis cylinder is made up of split, between each split the space is arranged, and described eddy flow lobe is welded on the space lateral margin; Link together by gusset and separator body inboard;
Described secondary eddy flow generating mechanism, comprise secondary eddy flow generating mechanism body, nozzle, the sidewall of described secondary eddy flow generating mechanism body has venthole, the place is provided with nozzle at venthole, described nozzle is downward-sloping, bottom at secondary eddy flow generating mechanism body has a hole, and the atmolysis cylinder of a described eddy flow generating mechanism and eddy flow lobe stretch into wherein, and described secondary eddy flow generating mechanism and separator body inboard weld together.
2. spiral-flow type moisture trap according to claim 1 is characterized in that, has a connector at the sidewall of described separator body, link to each other in order to air inlet with other spiral-flow type moisture traps, form series connection,, then seal by elastic sealing cover if when working independently.
3. spiral-flow type moisture trap according to claim 1 is characterized in that, the split of described composition air induction mast be 4 with 90 ° of arrangements, perhaps 3 with 120 ° of arrangements.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620116032 CN2907905Y (en) | 2006-05-25 | 2006-05-25 | Cyclone type gas water separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620116032 CN2907905Y (en) | 2006-05-25 | 2006-05-25 | Cyclone type gas water separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2907905Y true CN2907905Y (en) | 2007-06-06 |
Family
ID=38127115
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200620116032 Expired - Fee Related CN2907905Y (en) | 2006-05-25 | 2006-05-25 | Cyclone type gas water separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2907905Y (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103128009A (en) * | 2013-03-01 | 2013-06-05 | 常熟市华能环保工程有限公司 | Cyclone separator |
-
2006
- 2006-05-25 CN CN 200620116032 patent/CN2907905Y/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103128009A (en) * | 2013-03-01 | 2013-06-05 | 常熟市华能环保工程有限公司 | Cyclone separator |
| CN103128009B (en) * | 2013-03-01 | 2015-04-29 | 常熟市华能环保工程有限公司 | Cyclone separator |
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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: 20070606 Termination date: 20110525 |