CN102252158A - Classified coalescence condensation nozzle - Google Patents
Classified coalescence condensation nozzle Download PDFInfo
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- CN102252158A CN102252158A CN2011102150033A CN201110215003A CN102252158A CN 102252158 A CN102252158 A CN 102252158A CN 2011102150033 A CN2011102150033 A CN 2011102150033A CN 201110215003 A CN201110215003 A CN 201110215003A CN 102252158 A CN102252158 A CN 102252158A
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- coalescence
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Abstract
The invention discloses a classified coalescence condensation nozzle and belongs to an oil fog lubrication device. The invention provides the classified coalescence condensation nozzle which can improve the effectiveness and an oil fog condensation effect of a condensation nozzle in the conventional oil fog lubrication device, improve the lubrication efficiency and reduce the removal of residual fog, and more uniform particle size distribution of oil fog can be obtained. The classified coalescence condensation nozzle comprises a primary coalescence device of which the center is provided with a primary coalescence passage and a secondary coalescence device of which the center is provided with a through hole; the primary coalescence device is arranged at the front end of the through hole of the secondary coalescence device; a first secondary coalescence passage is formed in the center of the bottom of the secondary coalescence device; and the side wall of the same side of the secondary coalescence device is provided with a second secondary coalescence passage and a third secondary coalescence passage.
Description
Technical field
The invention belongs to oil mist lubrication device, particularly relate to the condensing mouth of a kind of classification coalescence.
Background technique
Oil mist lubrication is a kind of novel centralized lubrication mode.Oil mist lubrication is the energy with pressurized air, by oil fog generator lubricant oil is atomized, produce micron-sized oil mist particles, oil mist particles is delivered to the condensing mouth of oil fog generator with compressor through pipeline, after condensing into bigger oil droplet, send into various surface of friction pair such as high-speed rolling bearing, sliding bearing, gear, worm gear, sprocket wheel and slide guide; Oil droplet after condensing forms the better oil film of lubrication effect at metal friction surface, has reduced frictional force, has reduced heating, and lubricated part temperature is obviously descended.Yet along with the application of oil mist lubrication mode in production practices, actual production status has constantly proposed new requirement to the oil mist lubrication technology, and some original technology can't satisfy user's demand.For example, the condensing mouth of existing single-stage coalescence, condensing efficient is not high, and many oil mist particles can't be condensed into oil droplet effectively.This just makes a part of lubricant oil not effectively utilized, and has caused the waste of lubricant oil, has increased lubricated cost.Simultaneously, the remaining oil mist particles dissipation of part causes certain pollution to surrounding environment in air, suck mist of oil for a long time and also will work the mischief to health.These problems have influenced the application area of oil mist lubrication to a great extent.
Summary of the invention
Deficiency at the condensing mouth of existing single-stage coalescence exists the invention provides the condensing mouth of a kind of classification coalescence.The condensing mouth of this classification coalescence can improve the validity and the condensing effect of mist of oil of condensing mouth in the present oil mist lubrication device, obtains the more mist of oil particle size distribution of uniformity, improves lubricating efficiency, reduces the eliminating of residual mist.
To achieve these goals, the present invention adopts following technological scheme, the condensing mouth of a kind of classification coalescence comprises that the center has the one-level aggregation device of one-level coalescence passage and the secondary aggregation device that the center has through hole, and the one-level aggregation device is arranged on the front end of the through hole of secondary aggregation device; Bottom centre place at described secondary aggregation device is provided with the first secondary coalescence passage, and the homonymy sidewall of described secondary aggregation device is provided with the second secondary coalescence passage and the 3rd secondary coalescence passage.
Described one-level aggregation device and secondary aggregation device are by being threaded.
The sidewall of the secondary aggregation device relative with the 3rd secondary coalescence passage with the described second secondary coalescence passage is provided with auxiliary fog inlet.
Described auxiliary fog inlet is for being horizontally disposed with.
The described second secondary coalescence passage is for being obliquely installed, and the angle of itself and substantially horizontal is-90 °~90 °.
Described the 3rd secondary coalescence passage is for being obliquely installed, and the angle of itself and substantially horizontal is-90 °~90 °.
The diameter of described one-level coalescence passage is 0.1~5mm.
The diameter of the described first secondary coalescence passage is 0.1~5mm.
The diameter of the described second secondary coalescence passage is 0.1~5mm.
The diameter of described the 3rd secondary coalescence passage is 0.1~5mm.
Beneficial effect of the present invention:
The condensing mouth of classification coalescence of the present invention utilizes varigrained oil mist particles, the quality difference, the characteristics that inertia is different, to the varigrained oil mist particles that is produced through the condensing back of one-level aggregation device, it is condensing to carry out the selectively grading coalescence once more, to obtain the mist of oil particle size distribution (as: 15 μ m, 35 μ m, 50 μ m etc.) of expectation.
The present invention can improve the condensing efficient in the condensing link of oil mist lubrication, makes the mist of oil particle size distribution of the skewness that produces through the condensing back of one-level aggregation device, more uniformity.The quality of condensing back mist of oil particle size distribution and the effect of oil mist lubrication have further been improved.The present invention installs simple and conveniently in addition, uses reliably, and non-maintaining, user cost is low, and investment cost is low, and using effect is remarkable.
Description of drawings
Fig. 1 is the structural representation of the condensing mouth of classification coalescence of the present invention;
Wherein, the 1-first secondary coalescence passage, the 2-sidewall, 3-assists fog inlet, 4-through hole, 5-one-level coalescence passage, 6-dry fog inlet, 7-one-level aggregation device, 8-secondary aggregation device, the 9-second secondary coalescence passage, 10-the 3rd secondary coalescence passage.
Embodiment
The present invention is described further below in conjunction with the drawings and specific embodiments:
The condensing mouth of a kind of classification coalescence as shown in Figure 1, comprises that the center has the one-level aggregation device 7 of one-level coalescence passage 5 and the secondary aggregation device 8 that the center has through hole 4, and one-level aggregation device 7 is arranged on the front end of the through hole 4 of secondary aggregation device 8; Bottom centre place at described secondary aggregation device 8 is provided with the first secondary coalescence passage 1, and the homonymy sidewall 2 of described secondary aggregation device 8 is provided with the second secondary coalescence passage 9 and the 3rd secondary coalescence path 10.
Described one-level aggregation device 7 and secondary aggregation device 8 are by being threaded.
The sidewall 2 of the secondary aggregation device 8 relative with the 3rd secondary coalescence path 10 with the described second secondary coalescence passage 9 is provided with auxiliary fog inlet 3.
Described auxiliary fog inlet 3 is for being horizontally disposed with.
The described second secondary coalescence passage 9 is for being obliquely installed, and the angle α of itself and substantially horizontal is-90 °~90 °.
Described the 3rd secondary coalescence path 10 is for being obliquely installed, and the angle β of itself and substantially horizontal is-90 °~90 °.
The diameter d of described one-level coalescence passage 5 is 0.1~5mm.
The diameter d 0 of the described first secondary coalescence passage 1 is 0.1~5mm.
The diameter d 1 of the described second secondary coalescence passage 9 is 0.1~5mm.
The diameter d 2 of described the 3rd secondary coalescence path 10 is 0.1~5mm.
Embodiment 1
The condensing mouth of a kind of classification coalescence as shown in Figure 1, comprises that the center has the one-level aggregation device 7 of one-level coalescence passage 5 and the secondary aggregation device 8 that the center has through hole 4, and one-level aggregation device 7 is arranged on the front end of the through hole 4 of secondary aggregation device 8; Bottom centre place at described secondary aggregation device 8 is provided with the first secondary coalescence passage 1, and the homonymy sidewall 2 of described secondary aggregation device 8 is provided with the second secondary coalescence passage 9 and the 3rd secondary coalescence path 10.Described one-level aggregation device 7 and secondary aggregation device 8 are by being threaded.The sidewall 2 of the secondary aggregation device 8 relative with the 3rd secondary coalescence path 10 with the described second secondary coalescence passage 9 is provided with auxiliary fog inlet 3.Described auxiliary fog inlet 3 is for being horizontally disposed with.
The described second secondary coalescence passage 9 is for being obliquely installed, and the angle α of itself and substantially horizontal is 60 °, and described the 3rd secondary coalescence path 10 is for being obliquely installed, and the angle β of itself and substantially horizontal is 60 °.The diameter d of described one-level coalescence passage 5 is 0.8mm; The diameter d 0 of the described first secondary coalescence passage 1 is 0.8mm; The diameter d 1 of the described second secondary coalescence passage 9 is 0.8mm; The diameter d 2 of described the 3rd secondary coalescence path 10 is 0.8mm.
The condensing mouth of a kind of classification coalescence as shown in Figure 1, comprises that the center has the one-level aggregation device 7 of one-level coalescence passage 5 and the secondary aggregation device 8 that the center has through hole 4, and one-level aggregation device 7 is arranged on the front end of the through hole 4 of secondary aggregation device 8; Bottom centre place at described secondary aggregation device 8 is provided with the first secondary coalescence passage 1, and the homonymy sidewall 2 of described secondary aggregation device 8 is provided with the second secondary coalescence passage 9 and the 3rd secondary coalescence path 10.Described one-level aggregation device 7 and secondary aggregation device 8 are by being threaded.The sidewall 2 of the secondary aggregation device 8 relative with the 3rd secondary coalescence path 10 with the described second secondary coalescence passage 9 is provided with auxiliary fog inlet 3.Described auxiliary fog inlet 3 is for being horizontally disposed with.
The described second secondary coalescence passage 9 is for being obliquely installed, and the angle α of itself and substantially horizontal is 45 °, and described the 3rd secondary coalescence path 10 is for being obliquely installed, and the angle β of itself and substantially horizontal is 45 °.The diameter d of described one-level coalescence passage 5 is 1mm; The diameter d 0 of the described first secondary coalescence passage 1 is 1mm; The diameter d 1 of the described second secondary coalescence passage 9 is 1mm; The diameter d 2 of described the 3rd secondary coalescence path 10 is 1mm.
Below in conjunction with description of drawings working procedure of the present invention:
Undressed dry fog enters from the dry fog of one-level aggregation device 7 inlet 6, through one-level coalescence passage 5 condensing after, enter secondary aggregation device 8.At this moment, dry fog is through forming the oil mist particles that granularity does not wait after once condensing in secondary aggregation device 8.Then, the oil mist particles that these granularities do not wait is because the inertia difference can enter different secondary coalescence passages, that is: the first secondary coalescence passage 1, the second secondary coalescence passage 9 and the 3rd secondary coalescence path 10 respectively under compressed-air actuated pressure.Wherein, the less oil mist particles of granularity can be waftd into the second secondary coalescence passage 9 of small particle diameter; The 3rd secondary coalescence path 10 of particle diameter during medium-grained oil mist particles can enter; The oil mist particles that granularity is bigger can enter the first secondary coalescence passage 1 of big particle diameter.The mist of oil of process secondary coalescence passage forms the more mist of oil of uniformity of particle size distribution again by condensing.Also can allow dry fog simultaneously by dry fog inlet 6 and auxiliary fog inlet 3, make mist of oil particle size distribution uniformity more, for better condition has been created in further condensing work.
Claims (10)
1. the condensing mouth of classification coalescence is characterized in that comprising that the center has the one-level aggregation device of one-level coalescence passage and the secondary aggregation device that the center has through hole, and the one-level aggregation device is arranged on the front end of the through hole of secondary aggregation device; Bottom centre place at described secondary aggregation device is provided with the first secondary coalescence passage, and the homonymy sidewall of described secondary aggregation device is provided with the second secondary coalescence passage and the 3rd secondary coalescence passage.
2. the condensing mouth of a kind of classification coalescence according to claim 1 is characterized in that described one-level aggregation device and secondary aggregation device are by being threaded.
3. the condensing mouth of a kind of classification coalescence according to claim 1 is characterized in that the sidewall of the secondary aggregation device relative with the 3rd secondary coalescence passage with the described second secondary coalescence passage is provided with auxiliary fog inlet.
4. the condensing mouth of a kind of classification coalescence according to claim 3 is characterized in that described auxiliary fog inlet is for being horizontally disposed with.
5. the condensing mouth of a kind of classification coalescence according to claim 1 is characterized in that the described second secondary coalescence passage for being obliquely installed, and the angle of itself and substantially horizontal is-90 °~90 °.
6. the condensing mouth of a kind of classification coalescence according to claim 1 is characterized in that described the 3rd secondary coalescence passage for being obliquely installed, and the angle of itself and substantially horizontal is-90 °~90 °.
7. the condensing mouth of a kind of classification coalescence according to claim 1, the diameter d that it is characterized in that described one-level coalescence passage is 0.1~5mm.
8. the condensing mouth of a kind of classification coalescence according to claim 1 is characterized in that the diameter d 0 of the described first secondary coalescence passage is 0.1~5mm.
9. the condensing mouth of a kind of classification coalescence according to claim 1 is characterized in that the diameter d 1 of the described second secondary coalescence passage is 0.1~5mm.
10. the condensing mouth of a kind of classification coalescence according to claim 1 is characterized in that the diameter d 2 of described the 3rd secondary coalescence passage is 0.1~5mm.
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CN201110215003.3A CN102252158B (en) | 2011-07-29 | 2011-07-29 | Classified coalescence condensation nozzle |
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CN201110215003.3A CN102252158B (en) | 2011-07-29 | 2011-07-29 | Classified coalescence condensation nozzle |
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CN102252158A true CN102252158A (en) | 2011-11-23 |
CN102252158B CN102252158B (en) | 2014-03-19 |
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Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3941210A (en) * | 1974-05-09 | 1976-03-02 | De Limon Fluhme & Co. | Oil mist lubricating system and condenser device |
JP2001235093A (en) * | 2000-02-23 | 2001-08-31 | Showa Corp | Fog lubricator |
CN201034154Y (en) * | 2007-05-29 | 2008-03-12 | 中国核动力研究设计院 | Oil mist condensation reclaiming type discharge valve |
CN201152451Y (en) * | 2007-12-19 | 2008-11-19 | 沈阳科鑫科技有限公司 | Sintered metal filter disc type condensation nozzle |
-
2011
- 2011-07-29 CN CN201110215003.3A patent/CN102252158B/en not_active Expired - Fee Related
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3941210A (en) * | 1974-05-09 | 1976-03-02 | De Limon Fluhme & Co. | Oil mist lubricating system and condenser device |
JP2001235093A (en) * | 2000-02-23 | 2001-08-31 | Showa Corp | Fog lubricator |
CN201034154Y (en) * | 2007-05-29 | 2008-03-12 | 中国核动力研究设计院 | Oil mist condensation reclaiming type discharge valve |
CN201152451Y (en) * | 2007-12-19 | 2008-11-19 | 沈阳科鑫科技有限公司 | Sintered metal filter disc type condensation nozzle |
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