CN106512540A - Ultrafine vacuum oil filter - Google Patents

Ultrafine vacuum oil filter Download PDF

Info

Publication number
CN106512540A
CN106512540A CN201611145425.7A CN201611145425A CN106512540A CN 106512540 A CN106512540 A CN 106512540A CN 201611145425 A CN201611145425 A CN 201611145425A CN 106512540 A CN106512540 A CN 106512540A
Authority
CN
China
Prior art keywords
vacuum
oil
pipeline
filter
vacuum separator
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
Application number
CN201611145425.7A
Other languages
Chinese (zh)
Inventor
王同和
王挥
王一挥
王嘉强
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
(dalian Kaihong Science & Technology Co Ltd
Original Assignee
(dalian Kaihong Science & Technology Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by (dalian Kaihong Science & Technology Co Ltd filed Critical (dalian Kaihong Science & Technology Co Ltd
Priority to CN201611145425.7A priority Critical patent/CN106512540A/en
Publication of CN106512540A publication Critical patent/CN106512540A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D36/00Filter circuits or combinations of filters with other separating devices
    • B01D36/003Filters 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 invention provides an ultrafine vacuum oil filter. The ultrafine vacuum oil filter is characterized by comprising a coarse filter, a heater, a vacuum separator, a condenser, an oil pump and a fine filter, wherein an oil inlet pipe is communicated with the coarse filter; an output pipe of the coarse filter enters the heater through a pipeline I; an output pipe of the heater enters the vacuum separator and is communicated with an input pipe of an atomizing-spraying device of the vacuum separator through a pipeline II; an upper exhaust pipe of the vacuum separator is communicated with the condenser, and the condenser is connected with a subsequent processing device; a bottom output pipe of the vacuum separator is communicated with the oil pump through a pipeline III, and enters the fine filter for further filtering and discharging essential oil; a part of oil is communicated with the pipeline I through a pipeline IV after passing through the oil pump, and reenters the heater for recycling. The ultrafine vacuum oil filter has reasonable structural design, is small in size, and is safe and reliable; the filtering effect can be ensured effectively, and a high-cleanliness oil product is obtained.

Description

Superfinishing vacuum type oil filter
Technical field
A kind of the present invention relates to oil filtering device, more particularly to superfinishing vacuum type oil filter.
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 to remove 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;It is mixed into impurity to wear and tear working surface, makes working surface leave wound Trace etc..
Vacuum oil-filter is to remove the solid impurity and moisture in impure absolute oil using vacuum evaporation-filter element filtering method Filter bank.Vacuum oil-filter mainly includes vacuum separator and the vacuum pump being connected with vacuum separator by pipeline, oil extraction Pump, coarse filter, fine filter etc..Oil product is cleaned in vacuum separator, and the moisture vapor in oil product is simultaneously arranged by vacuum pump Go out, realize the purification of oil product, the oil product after purification is discharged by oil pump.
At present traditional vacuum oil-filter is generally sprayed using less vaporization chamber, shower nozzle, causes moisture in fluid not Fully can evaporate, it is impossible to reduce the moisture in fluid.Filter adopts stainless (steel) wire material filter element substantially, although reduce Cost, but filtering accuracy is not high, and fine particle impurity number is the important of measurement treatment effect in extra-high voltage transmission Index.
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 superfinishing vacuum type oil filter.The present invention mainly utilizes coarse filtration With the improvement of fine straining cooperation, the structure layout design of vacuum separator and condensing units, so as to play raising evaporation efficiency, oil is made Product have the effect of higher quality.
The technological means that the present invention is adopted are as follows:
A kind of superfinishing vacuum type oil filter, it is characterised in that include:Coarse filter, heater, vacuum separator, condensation dress Put, oil pump and fine filter;
Oil inlet pipe is connected with the coarse filter, and the outlet tube of the coarse filter enters the heater, institute by pipeline I The outlet tube 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 units, and the condensing units are located with follow-up again Reason device is connected;
The bottom outlet tube 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 quintessence oil;
After the oil pump described in, a part of fluid is connected with the pipeline I by pipeline IV and re-enters into the heating Device carries out recirculation.
Further, the nozzle of the atomizing sprayer that the vacuum separator internal upper part is provided with includes uniform into column distribution First jet and second nozzle, be provided with default angle between the first jet and the second nozzle.
Further, in the vacuum separator, middle part is provided with the flash distillation plant for abundant atomization.
Further, in the vacuum separator, middle and lower part is provided with the packing area of abundant reaction.
Further, the side middle and lower part of the vacuum separator is additionally provided with liquid level controller.
Further, the condensing units include that inlet, liquid outlet, cooling medium inlet and cooling medium go out liquid Mouthful, connected by coiled pipe between the cooling medium inlet and the cooling medium liquid outlet.
Compared with the prior art, the vacuum separator that the present invention is provided has the atomizing sprayer of special construction, adopts Nozzle with angle design, is more uniformly distributed can injection;The flash distillation plant arranged by middle part, can effectively collect mist Carburetion liquid, forms oil film, steam is preferably evaporated;Bottom is provided with packing layer, can effectively go the removal of impurity fully to react, make oil Liquid is further processed;In addition, top exhaust tube coordinates condensing units to use, allow steam to be preferably condensed into subsequent treatment and do Foot prepares;Further, making the impurity in fluid fully be removed by two processes of coarse filtration and fine straining.
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 Empty 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.
Description of the drawings
In order to be illustrated more clearly that the embodiment of the present invention or technical scheme of the prior art, below will be to embodiment or existing 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 these 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 the present invention.
Fig. 2 is the nozzle schematic diagram of the atomizing sprayer of the present invention.
Fig. 3 is the structural representation of the condensing units of the present 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, liquid level controller;13rd, pipeline Ⅲ;14th, oil pump;15th, fine filter;16th, pipeline IV;17th, first jet;18th, second nozzle;19th, inlet;20th, liquid outlet; 21st, cooling medium inlet;22nd, cooling medium liquid outlet;23rd, coiled pipe.
Specific embodiment
For making purpose, technical scheme and the 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 The a part of embodiment of the present invention, rather than the embodiment of whole.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, a kind of superfinishing vacuum type oil filter, including:Coarse filter 2, heater 4, vacuum separator 8, condensation Device 7, oil pump 14 and fine filter 15;
Oil inlet pipe 1 is connected with the coarse filter 2, and the outlet tube of the coarse filter 2 enters the heating by pipeline I 3 Device 4, the outlet tube of the heater 4 enter 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 units 7, the condensing units 7 again with it is rear Continuous processing meanss are connected;
The bottom outlet tube of the vacuum separator 8 is connected with the oil pump 14 by pipeline III 13 and enters back into the essence Quintessence oil is discharged after further being filtered in filter 15;
After the oil pump 14 described in, a part of fluid be connected with the pipeline I 3 by pipeline IV 16 re-enter into it is described Recirculation is carried out in heater 4.
As shown in Fig. 2 the nozzle of atomizing sprayer 9 that 8 internal upper part of the vacuum separator is provided with include it is uniform in column The first jet 17 and second nozzle 18 of distribution, is provided with default folder between the first jet 17 and the second nozzle 18 Angle.
In the vacuum separator 8, 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.
The side middle and lower part of the vacuum separator 8 is additionally provided with liquid level controller 12.
As shown in figure 3, the condensing units 7 include that inlet 19, liquid outlet 20, cooling medium inlet 21 and condensation are situated between Matter liquid outlet 22, is connected by coiled pipe 23 between the cooling medium inlet 21 and the cooling medium liquid outlet 22.
Finally it should be noted that:Various embodiments above only to illustrate technical scheme, rather than a limitation;To the greatest extent Pipe has been described in detail to the present invention with reference to foregoing embodiments, it will be understood by those within the art that:Its according to So the technical scheme described in foregoing embodiments can be modified, or which part or all technical characteristic are entered Row equivalent;And these modifications or replacement, do not make the essence of appropriate technical solution depart from various embodiments of the present invention technology The scope of scheme.

Claims (6)

1. a kind of superfinishing vacuum type oil filter, it is characterised in that include:Coarse filter (2), heater (4), vacuum separator (8), Condensing units (7), oil pump (14) and fine filter (15);
Oil inlet pipe (1) is connected with the coarse filter (2), and the outlet tube of coarse filter (2) enters described by pipeline I (3) Heater (4), the outlet tube of heater (4) enter 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 vacuum separator (8) is connected with the condensing units (7), condensing units (7) again It is connected with aftertreatment device;
The bottom outlet tube of vacuum separator (8) be connected with the oil pump (14) by pipeline III (13) enter back into it is described Quintessence oil is discharged after further being filtered in fine filter (15);
After the oil pump (14) described in, a part of fluid is connected with the pipeline I (3) by pipeline IV (16) and re-enters into institute Recirculation is carried out in stating heater (4).
2. superfinishing vacuum type oil filter according to claim 1, it is characterised in that vacuum separator (8) internal upper part The nozzle of the atomizing sprayer (9) being provided with includes uniform first jet (17) and second nozzle (18) into column distribution, described Default angle is provided between first jet (17) and the second nozzle (18).
3. superfinishing vacuum type oil filter according to claim 1, it is characterised in that in vacuum separator (8) middle part It is provided with the flash distillation plant (10) for abundant atomization.
4. superfinishing vacuum type oil filter according to claim 1, it is characterised in that under in vacuum separator (8) Portion is provided with the packing area (11) of abundant reaction.
5. superfinishing vacuum type oil filter according to claim 1, it is characterised in that the side of vacuum separator (8) Middle and lower part is additionally provided with liquid level controller (12).
6. superfinishing vacuum type oil filter according to claim 1, it is characterised in that described condensing units (7) include feed liquor Mouth (19), liquid outlet (20), cooling medium inlet (21) and cooling medium liquid outlet (22), the cooling medium inlet (21) connected by coiled pipe (23) and the cooling medium liquid outlet (22) between.
CN201611145425.7A 2016-12-13 2016-12-13 Ultrafine vacuum oil filter Pending CN106512540A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201611145425.7A CN106512540A (en) 2016-12-13 2016-12-13 Ultrafine vacuum oil filter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201611145425.7A CN106512540A (en) 2016-12-13 2016-12-13 Ultrafine vacuum oil filter

Publications (1)

Publication Number Publication Date
CN106512540A true CN106512540A (en) 2017-03-22

Family

ID=58342150

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201611145425.7A Pending CN106512540A (en) 2016-12-13 2016-12-13 Ultrafine vacuum oil filter

Country Status (1)

Country Link
CN (1) CN106512540A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110508043A (en) * 2019-09-10 2019-11-29 青岛晨明海洋装备技术有限公司 A kind of vaccum dewatering oil filter of lube purification environmental protection and energy saving
CN112221245A (en) * 2020-10-12 2021-01-15 张伶柯 Wood squeezing sesame oil evaporating device

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN202048805U (en) * 2011-01-30 2011-11-23 重庆市昊盾科技发展有限公司 Condenser for oil filter
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

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN202048805U (en) * 2011-01-30 2011-11-23 重庆市昊盾科技发展有限公司 Condenser for oil filter
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 (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110508043A (en) * 2019-09-10 2019-11-29 青岛晨明海洋装备技术有限公司 A kind of vaccum dewatering oil filter of lube purification environmental protection and energy saving
CN110508043B (en) * 2019-09-10 2024-04-19 青岛晨明海洋装备技术有限公司 Environment-friendly energy-saving vacuum water removal oil filter for oil purification
CN112221245A (en) * 2020-10-12 2021-01-15 张伶柯 Wood squeezing sesame oil evaporating device

Similar Documents

Publication Publication Date Title
CN108568131B (en) Stripping liquid regeneration device and stripping liquid regeneration process
CN106310768B (en) A kind of waste lubricant oil regeneration utilizes device and its technique for applying
US1493579A (en) Gas washer
DE4240196A1 (en) Process for cooling and cleaning gas containing ultrafine particles, in particular top gas or generator gas, and device for carrying it out
CN106731176A (en) Vacuum type oil filter atomizing sprayer
CN106512540A (en) Ultrafine vacuum oil filter
CN208454853U (en) A kind of benzene acetonitrile continuous rectification apparatus
CN204798975U (en) Vacuum oil filter of secondary filter and high -efficient dehydration
CN115403203A (en) High-reliability seawater desalination device
CN104837965A (en) Refined-coal production method, and refined-coal production device
CN102963909B (en) Method for recovering and reutilizing waste ammonia gas in LED (light-emitting diode) manufacturing through ammonia water method
US2676670A (en) Process for the purification of gases
CN106730951A (en) Vacuum type oil filter vacuum separator
CN204767503U (en) Stills for chemical industry
CN107311856A (en) A kind of purification recovery system of acetic acid waste liquid
CN107281903A (en) Thermal-arrest gas cleaning plant
CN106422395A (en) Condensing device for vacuum oil filter
CN106566649A (en) Method and system for regenerating fuel oil and base oil from waste engine oil
CN215610590U (en) Organic solvent's edulcoration water trap
CN212450920U (en) Purification device for process water in light hydrocarbon cracking device
CN209412109U (en) A kind of device being used to prepare high-purity dimeric acid
CN201470266U (en) Washing furfural gas-residue separating unit
CN216712015U (en) Circulating system for recycling waste heat of ammonia water for potassium carbonate desulfurization regeneration heat source
CN210645164U (en) Vacuum low-temperature spray evaporation condensation system
CN103920335A (en) Vacuum oil filter

Legal Events

Date Code Title Description
C06 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
RJ01 Rejection of invention patent application after publication

Application publication date: 20170322