CN207708747U - A kind of prime orientation vortex gas-liquid separator - Google Patents
A kind of prime orientation vortex gas-liquid separator Download PDFInfo
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- CN207708747U CN207708747U CN201721627237.8U CN201721627237U CN207708747U CN 207708747 U CN207708747 U CN 207708747U CN 201721627237 U CN201721627237 U CN 201721627237U CN 207708747 U CN207708747 U CN 207708747U
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- vortex gas
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Abstract
The utility model is related to a kind of primes to orient vortex gas-liquid separator, including cylindrical shell, filter, discharge port, boss, exhaust outlet, air entry and orientation vortex gas-liquid separator；The cylindrical shell includes that upper surface and lower face, the upper surface and lower face are respectively arranged at the top and bottom of the cylindrical shell, and the filter and boss may be contained in cylindrical shell, and the boss supports the filter；The orientation vortex gas-liquid separator is arranged at filter periphery；The gas-liquid separation effect of the utility model is substantially better than existing type, Maintenance free and loss is not generated to original absorption throughput, solves the technical issues of too fast saturation of prime filter in existing apparatus blocks, overcome ratios fluid in mixed gas existing in the prior art, the direct impact filter of glutinous shape object or after the baffle for lacking orientation guiding function blocks the unordered impact filter once again of flashing of fluid defect, wide market.
Description
Technical field
Mist of oil of the present invention separation, mist of oil collection technique field, more particular to will be mixed in gas
The device that liquid phase spray, solid phase powder are detached.
Background technology
With manufacturing continuous upgrading, more and more high-precision numerical control intermetallic composite coating equipments are widely used in each
Required industry, these are by cutting fluid lubrication, the high-precision equipment of cooling, a large amount of mist of oils, the breast that will produce in high-speed cruising
Changing liquid mist can dissipate to device external space, and workshop generates serious air pollution therewith；Mist of oil separation, collection device its effect
It is to be administered to this pollution, it is ensured that clean air quality is physically and mentally healthy with safeguard work personnel, environmental protection while again energy
Cutting fluid is recovered in process equipment and is recycled, energy-conservation of consumption reduction.
When a large amount of mist of oils in process equipment, its internal starting stage is rapidly entered i.e. by oil mist collecting device suction inlet
When the first processing links, at this point, in absorbed mixed gas, liquid phase spray (including more bulky grain oil droplet, oil droplet) institute
Accounting value highest (when compared with collecting separator other subsequent processing links), difference of the part process equipment due to workpiece
It is different, cutting fluid condition difference used, while another phenomenon i.e. process equipment also occurred generate in process it is subtle
Break flour in liquid phase mixing after be formed by ratio shared by thick object similarly be in highest state (with collect separator its
When his subsequent processing link compares), both ratios objects are mixed simultaneously gives oil mist collecting device the first processing links
Great challenge is brought, a series of problems has also been derived.
Existing oil mist collecting device has following several reply forms when coping with this problem after summary：One is uses
The deckle board formula of metal perforated plate clamping woven wire and fiber-like material and it will be similar to that C-shaped profile piece by permutation and combination at frame
Filter type is intercepted；One is directly hit cylinder-shaped filter surface or local surfaces；It is that will carry mesh separately to have
Taper cap body structure setting (this type Japan similar product has more appearance) or is being inhaled between suction inlet and rear class filter cotton
The baffle of approximate slab form is arranged in closing in rear.
Based on more passive in industry practice summary for many years, the above several ways reply processing, there are multifactor places
Inefficient real, ratios liquid phase spray, subtle the break flour institute after liquid phase mixing in mixed gas caused by managing technological deficiency
The thick object formed is constantly filled into deckle board formula type filter or cylinder-shaped filter, if filter hole is more thin
Close, filling is saturated to blocking quickly, and thick object is easier to paste surface pore that hole is caused to shut.
The frame type of big gap such as profile piece permutation and combination, although being not easy to block up since the gap between profile piece is larger
Plug, but the ratios liquid phase spray (being formed by thick object after liquid phase mixing containing subtle break flour) walked and crossed is many
Next processing links are directly impinging, very big burden are caused to the efficiency persistence of overall separation device, because in the backward
The processing links of propulsion, undertake processing effect and the function of more fine oil mist particle, and bulky grain saturation fluid can lead to it
It is rapidly saturated its original effect that terminates, in reality, vertically and horizontally section, that is, air-flow is inside housings for the shell of oil mist collecting device
By section can all be much larger than air inlet open area, when air-flow enters next processing links by suction inlet high speed, in gas
Contained fluid can be directly mapped in by restricting close to suction inlet cross-sectional sizes on the windward side of the deckle board formula processing links, because of inertia
Power percussion, processing links and suction inlet distance are shorter, and the range being mapped on the windward side is also smaller, in the mapping
The outer portion body of range wishes processing intent when could not really play design, this phenomenon is very universal, therefore a variety of similar dresses
It sets from suction inlet sideline to shell and makees extension extension, purpose, which is desirable to deckle board formula processing links, relatively evenly to be undertaken
Centrifugation is handled, but this form will undoubtedly increase shell overall dimensions, while also destroyed in appearance original compact
Sense, aesthetics reduce, and another occupied space becomes larger, and there are apparent defects.
It is set between suction inlet and rear stage processing links or absorbing mouth rear with mesh taper cap body structure setting
The baffle of approximate slab form is set, taper cap structure more act as gas uniform flow, itself is almost without gas-liquid separation
Effect, the fluid spread to periphery are directly impinging next processing links together with air-flow；And the baffle of approximate slab form
It stops and falls after part fluid can be allowed to hit, but can disperse to sputter around in the central point of shock, gas-liquid is mixed again
And entering next processing links, gas-liquid cannot carry out explicitly combing to be oriented to lumping together, and separating capacity is not strong, while this
Type baffle resistance conference generates compared with lossy throughput, and separator entirety efficiency declines, it is difficult to realize energy saving purpose.
Invention content
It is an object of the invention to places in view of the above-mentioned deficiencies, and then provide a kind of prime orientation vortex gas-liquid separation
Device solves the technical issues of too fast saturation of prime filter in existing apparatus blocks, has marked improvement.
For this purpose, the present invention uses following technical scheme：
A kind of prime orientation vortex gas-liquid separator, including cylindrical shell, filter, discharge port, boss, exhaust outlet, suction
Gas port and orientation vortex gas-liquid separator；
The cylindrical shell includes that upper surface and lower face, the upper surface and lower face are respectively arranged at the cylindrical shell
The top and bottom of body, the filter and boss may be contained in cylindrical shell, and the boss is in back taper, the boss branch
The filter is supportted, the boss lower part is contacted with the lower face, and boss upper end disc is more than the outer circle of filter
Face；
The exhaust outlet is set to cylindrical shell upper surface center position, and the exhaust outlet is no more than in filter
The lower face side in hole, the cylindrical shell is provided with discharge port, and the discharge port and air entry are respectively arranged at the filtering
The both sides of device；
The orientation vortex gas-liquid separator is arranged at filter periphery, the lower part of the orientation vortex gas-liquid separator
The circle that camber line and boss upper end disc are formed be bonded, the top edge of the orientation vortex gas-liquid separator be placed on boss
The upper surface of filter is fitted in the central point and air entry that vortex gas-liquid separator is oriented described in the inner face of upper surface together
Central point horizontal inline or tend to horizontal inline.
Further, the boss and filter are in concentric circles relationship on placement location.
Further, to be thrown from the isometrical size in suction inlet circle sideline is parallel to the barrel-shaped direction of axis line of filter
Shadow, all smooth arcwall bodies of drop shadow spread being projected on orientation vortex gas-liquid separator are limited to left and right and turn over
Within volume structure.
Further, the filter is in upright tubbiness.
The technical solution adopted in the present invention is：By to initially enter the mixed airflow in oil mist collecting device shell into
Row streamlined point to, make structural constraint, compression, guiding of the air-flow by two turnups in top or so, by by air entry continue into
The high-speed flow inertia force entered promotes, and (contains to mix bulky grain fluid, oil droplet oil droplet and part fine grained fluid in gas
Subtle break flour is formed by thick object after liquid phase mixing) it is cut from the upstanding wall body camber line of orientation vortex gas-liquid separator
The lower section discharge port band of position is separated at point, fluid is discharged by discharge port, and gas circles round to rise upwards and be filtered by filter
It is discharged from exhaust outlet to next link after removing.
Beneficial effects of the present invention：1. prime orientation vortex gas-liquid separator of the present invention overcomes existing in the prior art mixed
Close ratios fluid in gas, the direct impact filter of glutinous shape object or the fluid after the baffle for lacking orientation guiding function blocks
The defect of the unordered impact filter once again of flashing, through practical more wheel tests, separating effect is substantially better than existing type, Maintenance free
And loss is not generated to original absorption throughput, do not increase original gas-liquid separation device shell space size and prior art phase
Than the present invention borrows the inertia force effect of air-flow, by guided constraint and directional separation, solves prime in existing apparatus and filters
The technical issues of too fast saturation of device blocks, wide market.
Description of the drawings
Present invention will be further explained below with reference to the attached drawings and examples.
Fig. 1 is：Orient the relationship side view of vortex gas-liquid separator and filter, shell and other structures；
Fig. 2 is：It is a piece of smooth rectangle thin plate schematic diagram at the beginning of orienting the forming of vortex gas-liquid separator；
Fig. 3 is：Orient vortex gas-liquid separator downward central point direction turnup schematic diagram in forming process；
Fig. 4 is：Orient one of vortex gas-liquid separator and filter, boss relational view；
Fig. 5 is：Orient the two of vortex gas-liquid separator and filter, boss relational view；
Fig. 6 is：Orient the relationship front view of vortex gas-liquid separator and filter, shell and other structures；
Fig. 7 is：Mixed airflow runs each stage schematic diagram.
Wherein：Cylindrical shell 1, filter 2, discharge port 4, boss 6, exhaust outlet 7, air entry 8, orientation vortex gas-liquid separation
Device 9.
Specific implementation mode
Technical solution to further illustrate the present invention below with reference to the accompanying drawings and specific embodiments.
A kind of prime orients vortex gas-liquid separator, as shown in figs. 1-7, including cylindrical shell 1, filter 2, discharge port 4,
Boss 6, exhaust outlet 7, air entry 8 and orientation vortex gas-liquid separator 9；
The cylindrical shell 1 is respectively arranged at described including upper surface 3 and lower face 5, the upper surface 3 and lower face 5
The top and bottom of cylindrical shell 1, the filter 2 and boss 6 may be contained in cylindrical shell 1, and the boss 6 is in back taper
Shape, the boss 6 support the filter 2, and 6 lower part of the boss is contacted with the lower face 5,6 upper end of boss circle
Face is more than the periphery of filter 2；
The exhaust outlet 7 is set to 1 upper surface of the cylindrical shell, 3 center position, and the exhaust outlet 7 was not more than
5 side of lower face of 2 endoporus of filter, the cylindrical shell 1 is provided with discharge port 4, and the discharge port 4 and air entry 8 are set respectively
It is placed in the both sides of the filter 2；
The orientation vortex gas-liquid separator 9 is arranged at 2 periphery of filter, the orientation vortex gas-liquid separator 9
The circle that lower part camber line and 6 upper end disc of boss are formed be bonded, the top edge for orienting vortex gas-liquid separator 9 be placed on
The upper surface of filter 2 on boss 6 is fitted in described in the inner face of upper surface 3 and orients in vortex gas-liquid separator 9 together
The central point horizontal inline of heart point and air entry 8 tends to horizontal inline.
Further, the boss 6 and filter 2 are in concentric circles relationship on placement location.
Further, to be thrown from the round isometrical size in sideline of suction inlet 8 is parallel to 2 barrel-shaped direction of axis line of filter
Shadow, all smooth arcwall bodies of drop shadow spread being projected on orientation vortex gas-liquid separator 9 are limited to left and right and turn over
Within volume structure.
Further, the filter 2 is in upright tubbiness.
Mist of oil mixed gas is by 8 quick washing of suction inlet orientation vortex gas-liquid separator 9, because orienting vortex gas-liquid separator
9 top interludes are sealed with 1 upper surface of cylindrical shell, and air-flow is directed 9 arcuate stream line shape wall body water conservancy diversion of vortex gas-liquid separator
To the right and left, while again because of orientation 9 the right and left turnup structure of vortex gas-liquid separator guiding, mist of oil mixed gas is in orientation
Filter back lower place position is disengaged to by slewing at 9 arc point of contact of vortex gas-liquid separator, high ratio in mist of oil mixed gas
Heavy oil pearl, oil droplet, liquid mix thick object and part bulky grain fog particles in inertia force impact, orientation vortex gas-liquid separation admittedly
Under the up big and down small turnup structure guiding of 9 the right and left of device and compression, 4 region of mouth, the area (are let out) in separation to the total drain in bottom
Domain is in mist of oil suction inlet lower position simultaneously by filter lower boss (back taper) structure 6, avoids and reduces and is lasting
The air-flow of entrance mixes the fluid in separated so far region and liquid the influence again of sticky matter admittedly, and gas-liquid is detached, after separation
Gas it is upwards and soaring around the convolution of 2 barrel-shaped outer wall of filter, by after the trapping again of filter by 3 row of shell upper surface
Gas port 7 is discharged to next link, and the fluid and liquid assembled mix sticky matter and continues segregated so far cumulant admittedly
It promotes, (letting out) mouth 4 by total drain is discharged.
Based on the orientation vortex gas-liquid separator 9 of prime processing, compare in existing similar technique when the first link is handled,
It is easy to cause its saturation blocking or a large amount of fluid mixtures is caused to be mingled with gas shock and lacked to the technology of next processing links
It falls into and using high specific gravity oil droplet, oil droplet, liquid in mist of oil mixed gas in the case of drawback, can be allowed to mix thick object and portion admittedly
Divide bulky grain fog particles to be efficiently separated and solve the difficulty that the first processing links are easily saturated blocking to specified region, substantially
Degree alleviates the operation burden of subsequent processing link, similarly also significantly extends the Use Limitation of subsequent processing link, makes oil
Mist separates and collects device overall operation and more stablizes.Vortex gas-liquid separator 9 is oriented in existing cartridge filter periphery to be arranged,
Do not increase additionally and occupied space, and be arranged simple, separating effect is apparent, is conducive to be widely used to promote.
Mixed gas containing mist of oil and part solid impurity, is rapidly entered by collection device air entry, mixed airflow quilt
Orient vortex gas-liquid separator arcwall body or so shunting, to the turnup structural constraint of vortex gas-liquid separator both sides, compress, draw
It leads down, ratios fluid, glutinous shape object impurity in mixed airflow etc. are quickly pushed to front lower place region, are persistently arranged by discharge port
Go out, the soaring convolution of the air-flow after separation is on prime filter periphery and enters its filter layer, and the air-flow being filtered again enters height
In the impeller of speed rotation, discharge is squeezed upwards or to follow-up link from impeller periphery, passes through the exhaust outlet on motor fixed plate periphery
It is advanced to rear class filter wall body periphery and is again introduced into filter layer and carry out rear class filtration treatment, treated pure air is by receiving
The exhaust outlet of acquisition means is discharged.
The technical principle of the present invention is described above in association with specific embodiment.These descriptions are intended merely to explain the present invention's
Principle, and it cannot be construed to limiting the scope of the invention in any way.Based on the explanation herein, the technology of this field
Personnel would not require any inventive effort the other specific implementation modes that can associate the present invention, these modes are fallen within
Within protection scope of the present invention.
Claims (4)
1. a kind of prime orients vortex gas-liquid separator, it is characterised in that：Including cylindrical shell, filter, discharge port, boss,
Exhaust outlet, air entry and orientation vortex gas-liquid separator；
The cylindrical shell includes that upper surface and lower face, the upper surface and lower face are respectively arranged at the cylindrical shell
Top and bottom, the filter and boss may be contained in cylindrical shell, and the boss is in back taper, and the boss supports
The filter, the boss lower part are contacted with the lower face, and boss upper end disc is more than the periphery of filter；
The exhaust outlet is set to cylindrical shell upper surface center position, and the exhaust outlet is not more than filter endoporus,
The lower face side of the cylindrical shell is provided with discharge port, and the discharge port and air entry are respectively arranged at the filter
Both sides；
The orientation vortex gas-liquid separator is arranged at filter periphery, the lower part camber line of the orientation vortex gas-liquid separator
It is bonded with the circle that boss upper end disc is formed, the top edge of the orientation vortex gas-liquid separator and the filtering being placed on boss
The upper surface of device is fitted in together in the central point and air entry for orienting vortex gas-liquid separator described in the inner face of upper surface
Heart point horizontal inline tends to horizontal inline.
2. prime according to claim 1 orients vortex gas-liquid separator, it is characterised in that：The boss exists with filter
It is in concentric circles relationship on placement location.
3. prime according to claim 1 orients vortex gas-liquid separator, it is characterised in that：With from suction inlet circle sideline
Isometrical size is parallel to be projected to the barrel-shaped direction of axis line of filter, the projection model being projected on orientation vortex gas-liquid separator
All smooth arcwall bodies are enclosed, are limited within the turnup structure of left and right.
4. prime according to claim 1 orients vortex gas-liquid separator, it is characterised in that：The filter is in upright
Tubbiness.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721627237.8U CN207708747U (en) | 2017-11-29 | 2017-11-29 | A kind of prime orientation vortex gas-liquid separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721627237.8U CN207708747U (en) | 2017-11-29 | 2017-11-29 | A kind of prime orientation vortex gas-liquid separator |
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| Publication Number | Publication Date |
|---|---|
| CN207708747U true CN207708747U (en) | 2018-08-10 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201721627237.8U Active CN207708747U (en) | 2017-11-29 | 2017-11-29 | A kind of prime orientation vortex gas-liquid separator |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107789937A (en) * | 2017-11-29 | 2018-03-13 | 佛山市东山瑞泽环保机器有限公司 | A kind of prime orients vortex gas-liquid separator |
| CN110090517A (en) * | 2019-05-08 | 2019-08-06 | 俞春华 | A kind of staged gas-liquid separator |
-
2017
- 2017-11-29 CN CN201721627237.8U patent/CN207708747U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107789937A (en) * | 2017-11-29 | 2018-03-13 | 佛山市东山瑞泽环保机器有限公司 | A kind of prime orients vortex gas-liquid separator |
| CN110090517A (en) * | 2019-05-08 | 2019-08-06 | 俞春华 | A kind of staged gas-liquid separator |
| CN110090517B (en) * | 2019-05-08 | 2023-09-08 | 俞春华 | Stepped gas-liquid separator |
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