CN106730951A - Vacuum type oil filter vacuum separator - Google Patents
Vacuum type oil filter vacuum separator Download PDFInfo
- Publication number
- CN106730951A CN106730951A CN201611146592.3A CN201611146592A CN106730951A CN 106730951 A CN106730951 A CN 106730951A CN 201611146592 A CN201611146592 A CN 201611146592A CN 106730951 A CN106730951 A CN 106730951A
- Authority
- CN
- China
- Prior art keywords
- vacuum
- vacuum separator
- nozzle
- separator
- filter
- 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.)
- Pending
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/16—Evaporating by spraying
- B01D1/20—Sprayers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/16—Evaporating by spraying
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/30—Accessories for evaporators ; Constructional details thereof
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D36/00—Filter circuits or combinations of filters with other separating devices
- B01D36/003—Filters in combination with devices for the removal of liquids
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The present invention provides a kind of vacuum type oil filter vacuum separator, it is characterised in that：The nozzle of the atomizing sprayer that the vacuum separator internal upper part is provided with includes uniform first jet and second nozzle into column distribution, and 30 ° 60 ° of angle is provided between the first jet and the second nozzle；Middle part is provided with the flash distillation plant for abundant atomization in the vacuum separator；Middle and lower part is provided with the packing area of abundant reaction in the vacuum separator, and described filler area uses ceramic raschig rings；The side middle and lower part of the vacuum separator is additionally provided with fluid level controller.Reasonable in design of the invention, causes that what fluid was more uniformly distributed is injected on flash distillation plant so that evaporation is more abundant by biserial nozzle, can effectively improve evaporation efficiency, acquisition cleannes oil product higher.
Description
Technical field
The present invention relates to oil filtering device, more particularly to a kind of vacuum type oil filter vacuum separator.
Background technology
At present, oil filter has been widely used in the industries such as petrochemical industry, oil, coal, electric power, military project machinery, is removal
The special equipment of water content in oil and gas.The machinery during transport storage and use can be effectively prevented to be mixed into water using oil
Divide the situation with mechanical admixture.It is well known that unpurified fluid has a certain impact to the performance of plant equipment and life-span, mix
Entering moisture can cause metal surface corrosion, reduce the viscosity of oil；Being mixed into impurity can wear and tear working surface, working surface is left wound
Trace etc..
Vacuum oil-filter is that the solid impurity and moisture in impure absolute oil are removed using vacuum evaporation-filter element filtering method
Filter bank.Vacuum oil-filter mainly includes vacuum separator and the vavuum pump, the oil extraction that are connected with vacuum separator by pipeline
Pump, coarse filter, fine filter etc..Oil product is cleaned in vacuum separator, and the moisture vapor in oil product is simultaneously arranged by vavuum pump
Go out, realize the purification of oil product, the oil product after purification is discharged by oil pump.
The vacuum separator of vacuum oil-filter traditional at present is generally sprayed using less vaporization chamber, shower nozzle, causes oil
Moisture in liquid can not fully evaporate, it is impossible to reduce the moisture in fluid.Filter uses stainless (steel) wire material to filter substantially
Core, although reduce cost, but filtering accuracy is not high, and fine particle impurity number is at measurement in extra-high voltage transmission
Manage the important indicator of effect.
To sum up, it is necessary to provide a kind of equipment to solve the above problems.
The content of the invention
According to technical problem set forth above, and provide a kind of vacuum type oil filter vacuum separator.It is of the invention main
Using using cooperatively for biserial nozzle and flash distillation plant and packing area, so as to play raising evaporation efficiency, there is oil product higher
The effect of quality.
The technological means that the present invention is used is as follows：
A kind of vacuum type oil filter vacuum separator, it is characterised in that：
The nozzle of the atomizing sprayer that the vacuum separator internal upper part is provided with includes uniform the first spray into column distribution
Mouth and second nozzle, are provided with 30 ° -60 ° of angle between the first jet and the second nozzle；
Middle part is provided with the flash distillation plant for abundant atomization in the vacuum separator；
Middle and lower part is provided with the packing area of abundant reaction in the vacuum separator, and described filler area uses ceramic raschig rings；
The side middle and lower part of the vacuum separator is additionally provided with fluid level controller.
Further, the vacuum type oil filter includes coarse filter, heater, the vacuum separator, condensing unit, oil
Pump and fine filter；
Oil inlet pipe is connected with the coarse filter, and the efferent duct of the coarse filter enters the heater, institute by pipeline I
The efferent duct for stating heater enters the vacuum separator and the atomizing sprayer of the vacuum separator by pipeline II
Input pipe is connected；
The top exhaust tube of the vacuum separator is connected with the condensing unit, and the condensing unit is located with follow-up again
Reason device is connected；
The bottom efferent duct of the vacuum separator is connected with the oil pump by pipeline III and enters back into the fine filter
In further filtered after discharge essential oil；
After through the oil pump, a part of fluid is connected with the pipeline I by pipeline IV and re-enters into the heating
Recycled in device.
Compared with the prior art, the vacuum separator that the present invention is provided has the atomizing sprayer of special construction, uses
Nozzle with angle design, can be more uniformly distributed injection；The flash distillation plant set by middle part, can effectively collect mist
Carburetion liquid, forms oil film, steam is preferably evaporated；Bottom is provided with the packing layer being made up of ceramic raschig rings, can effectively go
The removal of impurity is fully reacted, and fluid is further processed；In addition, top exhaust tube coordinates condensing unit to use, allow steam more
The good subsequent treatment that is condensed into is got ready；Further, making the impurity in fluid obtain fully by two processes of coarse filtration and refined filtration
Removal.
The present invention has small volume, safe and reliable, and the safety of pipeline can be effectively ensured, and good filtration effect is efficiently modified true
Sky evaporation cell structure, increases evaporating space, using brand-new spray structure, the advantages of improve evaporation efficiency, for the foregoing reasons
The present invention field such as can process in fluid and be widely popularized.
Brief description of the drawings
In order to illustrate more clearly about the embodiment of the present invention or technical scheme of the prior art, below will be to embodiment or existing
The accompanying drawing to be used needed for having technology description does simply to introduce, it should be apparent that, drawings in the following description are this hairs
Some bright embodiments, for those of ordinary skill in the art, without having to pay creative labor, can be with
Other accompanying drawings are obtained according to these accompanying drawings.
Fig. 1 is the structural representation of vacuum separator of the invention.
Fig. 2 is the nozzle schematic diagram of atomizing sprayer of the invention.
Fig. 3 is the structural representation of vacuum type oil filter of the invention.
In figure：1st, oil inlet pipe；2nd, coarse filter；3rd, pipeline I；4th, heater；5th, pipeline II；6th, top exhaust tube；7th, condense
Device；8th, vacuum separator；9th, atomizing sprayer；10th, flash distillation plant；11st, packing area；12nd, fluid level controller；13rd, pipeline
Ⅲ；14th, oil pump；15th, fine filter；16th, pipeline IV；17th, first jet；18th, second nozzle.
Specific embodiment
To make the purpose, technical scheme and advantage of the embodiment of the present invention clearer, below in conjunction with the embodiment of the present invention
In accompanying drawing, the technical scheme in the embodiment of the present invention is clearly and completely described, it is clear that described embodiment is
A part of embodiment of the present invention, rather than whole embodiments.Based on the embodiment in the present invention, those of ordinary skill in the art
The every other embodiment obtained under the premise of creative work is not made, belongs to the scope of protection of the invention.
As shown in Figure 1 and Figure 2, a kind of vacuum type oil filter vacuum separator, the internal upper part of the vacuum separator 8 is provided with
The nozzle of atomizing sprayer 9 include uniform first jet 17 and second nozzle 18 into column distribution, the first jet 17
30 ° -60 ° of angle is provided between the second nozzle 18；
Middle part is provided with the flash distillation plant 10 for abundant atomization in the vacuum separator 8；
Middle and lower part is provided with the packing area 11 of abundant reaction in the vacuum separator 8, and described filler area 11 is drawn using ceramics
Western ring；
The side middle and lower part of the vacuum separator 8 is additionally provided with fluid level controller 12.
As shown in figure 3, the vacuum type oil filter includes coarse filter 2, heater 4, the vacuum separator 8, condensation dress
Put 7, oil pump 14 and fine filter 15；
Oil inlet pipe 1 is connected with the coarse filter 2, and the efferent duct of the coarse filter 2 enters the heating by pipeline I 3
Device 4, the efferent duct of the heater 4 enters the atomization of the vacuum separator 8 and the vacuum separator 8 by pipeline II 5
The input pipe of spray equipment 9 is connected；
The top exhaust tube 6 of the vacuum separator 8 is connected with the condensing unit 7, the condensing unit 7 again with it is rear
Continuous processing unit is connected；
The bottom efferent duct of the vacuum separator 8 is connected with the oil pump 14 by pipeline III 13 and enters back into the essence
Essential oil is discharged after further being filtered in filter 15；
After through the oil pump 14, a part of fluid be connected with the pipeline I 3 by pipeline IV 16 re-enter into it is described
Recycled in heater 4.
Finally it should be noted that：Various embodiments above is merely illustrative of the technical solution of the present invention, rather than its limitations；To the greatest extent
Pipe has been described in detail with reference to foregoing embodiments to the present invention, it will be understood by those within the art that：Its according to
The technical scheme described in foregoing embodiments can so be modified, or which part or all technical characteristic are entered
Row equivalent；And these modifications or replacement, the essence of appropriate technical solution is departed from various embodiments of the present invention technology
The scope of scheme.
Claims (2)
1. a kind of vacuum type oil filter vacuum separator, it is characterised in that：
The nozzle of the atomizing sprayer (9) that vacuum separator (8) internal upper part is provided with includes uniform into the first of column distribution
Nozzle (17) and second nozzle (18), are provided with 30 ° -60 ° of folder between the first jet (17) and the second nozzle (18)
Angle；
Middle part is provided with the flash distillation plant (10) for abundant atomization in the vacuum separator (8)；
The interior middle and lower part of the vacuum separator (8) is provided with the packing area (11) of abundant reaction, and described filler area (11) are using ceramics
Raschig ring；
The side middle and lower part of the vacuum separator (8) is additionally provided with fluid level controller (12).
2. vacuum type oil filter vacuum separator according to claim 1, it is characterised in that the vacuum type oil filter
Including coarse filter (2), heater (4), the vacuum separator (8), condensing unit (7), oil pump (14) and fine filter (15)；
Oil inlet pipe (1) is connected with the coarse filter (2), and the efferent duct of the coarse filter (2) enters described by pipeline I (3)
Heater (4), the efferent duct of the heater (4) enters the vacuum separator (8) with the vacuum point by pipeline II (5)
Input pipe from the atomizing sprayer (9) of device (8) is connected；
The top exhaust tube (6) of the vacuum separator (8) is connected with the condensing unit (7), and the condensing unit (7) is again
It is connected with aftertreatment device；
The bottom efferent duct of the vacuum separator (8) be connected with the oil pump (14) by pipeline III (13) enter back into it is described
Essential oil is discharged after further being filtered in fine filter (15)；
After the oil pump (14), a part of fluid is connected with the pipeline I (3) by pipeline IV (16) and re-enters into institute
State and recycled in heater (4).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611146592.3A CN106730951A (en) | 2016-12-13 | 2016-12-13 | Vacuum type oil filter vacuum separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611146592.3A CN106730951A (en) | 2016-12-13 | 2016-12-13 | Vacuum type oil filter vacuum separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106730951A true CN106730951A (en) | 2017-05-31 |
Family
ID=58880867
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201611146592.3A Pending CN106730951A (en) | 2016-12-13 | 2016-12-13 | Vacuum type oil filter vacuum separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106730951A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108479090A (en) * | 2018-04-03 | 2018-09-04 | 青岛海湾精细化工有限公司 | Acetic acid removal of impurities evaporation equipment in ketene dimer production |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN203208789U (en) * | 2013-04-17 | 2013-09-25 | 重庆潜能实业(集团)有限公司 | Double-stage vacuum oil filter for super-high transformer oil |
| CN203678132U (en) * | 2013-12-07 | 2014-07-02 | 重庆市合川区邓健萍摩托车配件加工厂 | Oil online purifying machine |
-
2016
- 2016-12-13 CN CN201611146592.3A patent/CN106730951A/en active Pending
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN203208789U (en) * | 2013-04-17 | 2013-09-25 | 重庆潜能实业(集团)有限公司 | Double-stage vacuum oil filter for super-high transformer oil |
| CN203678132U (en) * | 2013-12-07 | 2014-07-02 | 重庆市合川区邓健萍摩托车配件加工厂 | Oil online purifying machine |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108479090A (en) * | 2018-04-03 | 2018-09-04 | 青岛海湾精细化工有限公司 | Acetic acid removal of impurities evaporation equipment in ketene dimer production |
| CN108479090B (en) * | 2018-04-03 | 2021-04-30 | 青岛海湾精细化工有限公司 | Acetic acid impurity removal evaporation equipment in diketene production |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN106731176A (en) | Vacuum type oil filter atomizing sprayer | |
| CN104163535A (en) | Desulfurization wastewater zero discharge device and treatment method | |
| CN106512540A (en) | Ultrafine vacuum oil filter | |
| CN106730951A (en) | Vacuum type oil filter vacuum separator | |
| EP2749341B1 (en) | Device and method for purification of flue gas of a metallurgical plant | |
| CN107281903A (en) | Thermal-arrest gas cleaning plant | |
| CN107469544A (en) | Pneumatic emulsifying processing unit and system | |
| CN204767503U (en) | Stills for chemical industry | |
| CN204767780U (en) | Secondary atomizing oil -water separator | |
| CN209412109U (en) | A kind of device being used to prepare high-purity dimeric acid | |
| CN106422395A (en) | Condensing device for vacuum oil filter | |
| CN106215447A (en) | A kind of electronic-stage hydrofluoric acid production rectifying column | |
| CN109248564A (en) | A kind of recycle device and technique of the ammonia liquor that petrochemical industry refinery acidity water treatment facilities generates | |
| CN109628179A (en) | A kind of spent organic solvent recycling and reusing device | |
| CN211611974U (en) | Filtering device for scrap steel smelting | |
| CN209522827U (en) | A kind of spent organic solvent recycling and reusing device | |
| CN204369745U (en) | A kind of mud flash tank | |
| CN207237610U (en) | A kind of gas filter drain cock | |
| CN208124320U (en) | A kind of safe water sealing groove burned for glance coal tail gas safe | |
| CN202777864U (en) | Energy-saving distillation device | |
| CN103920335A (en) | Vacuum oil filter | |
| CN204434448U (en) | A kind of multi-functional sewage mud-processing equipment | |
| CN109529560A (en) | Steam whitening method for filter tank of blast furnace granulated slag system | |
| CN205516859U (en) | Take vacuum oil filter of recoil system | |
| CN221310005U (en) | Steam condensation cooling defogging tower |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20170531 |
|
| RJ01 | Rejection of invention patent application after publication |