CN106621547A - Cutting fluid precipitation filtration and recovery system - Google Patents
Cutting fluid precipitation filtration and recovery system Download PDFInfo
- Publication number
- CN106621547A CN106621547A CN201510726783.6A CN201510726783A CN106621547A CN 106621547 A CN106621547 A CN 106621547A CN 201510726783 A CN201510726783 A CN 201510726783A CN 106621547 A CN106621547 A CN 106621547A
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- Prior art keywords
- bin
- filtration
- layer
- connecting tube
- recovering system
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- 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
- B01D36/04—Combinations of filters with settling tanks
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Filtration Of Liquid (AREA)
Abstract
The present invention discloses a cutting fluid precipitation filtration and recovery system, which comprises a buffer bin, a filtration bin, a recovery bin, a residue collection bin, a first connection pipe, a second connection pipe, a third connection pipe, a detection meter and a control module, wherein a waste liquid is subjected to primary precipitation in the buffer bin, waste residue is deposited on the bottom portion of the buffer bin, the waste liquid enters the filtration bin in an overflow manner through the first connection pipe and is filtered by filtration sieve layers, the waste residue is trapped on the filtration sieve layers and enters the residue collection bin, the filtrate is collected on the bottom portion of the filtration bin, the filtrate collected on the bottom portion of the filtration bin enters the recovery bin through the second connection pipe, sequentially passes through filtration layers in an overflow manner in the recovery bin, and is further filtered by the filtration layers, such that the purity of the recovered liquid overflowed to the upper portion of the filtration layer is ensured. According to the present invention, through the detection result of the detection meter, the output or reflux of the recovered liquid is automatically controlled, such that the real-time performance is strong, and the reliability is high.
Description
Technical field
The present invention relates to stock-removing machine technical field, more particularly to a kind of cutting liquid precipitate filtering recovering system.
Background technology
Cutting fluid is a kind of being used in metal cutting, the mill course of processing, for cooling down and lubricating cutter and processing
The industrial type fluid of part, cutting fluid from various super strong functional auxiliary agent Jing science it is compound with form, directly discharge
Environmental pollution can be caused.
Cutting fluid is reclaimed, cutting fluid discharge can have both been reduced, cutting fluid cost can be reduced again.Machine
It is various that bed apparatus have in the course of the work a large amount of rail oils, main shaft oil, hydraulic oil and iron filings, dust etc.
Debris are mixed into cutting fluid.So, the core procedure in the recycling of cutting fluid is to be separated by filtration.
Currently, mesh filtration is adopted the filtration of cutting fluid more, but, the cutting for occurring in the market
Liquid reclaims filtration poor filtration effect in defecator, and mesh Jing often occurs blocking phenomenon, and employee needs Jing
Often maintaining is carried out to equipment, reduce production efficiency, it is impossible to meet current machine industry efficient green system
The demand made.
The content of the invention
Based on the technical problem that background technology is present, the present invention proposes a kind of cutting liquid precipitate and is recovered by filtration and is
System.
A kind of cutting liquid precipitate filtering recovering system proposed by the present invention, including：Surge bunker, filtering cabin, return
Receive storehouse, Ji Zhacang, the first connecting tube, the second connecting tube, the 3rd connecting tube, detection meter and control module；
Filtering cabin inner inclination is provided with the screen layer no less than a layer, the low side insertion Ji Zhacang of screen layer；
Level is provided with the filter layer no less than a layer in recovery bin, and recovery bin is provided with delivery valve and is located on filter layer
Side；
The first end of the first connecting tube is connected with surge bunker, and its second end connects and positioned at screen layer with filtering cabin
Top；The first end of the second connecting tube is connected and positioned at screen layer lower section, its second end and recovery with filtering cabin
Storehouse connects and positioned at filter layer lower section；The first end of the 3rd connecting tube is connected and under filter layer with recovery bin
Side, its second end connects with surge bunker；3rd connecting tube is provided with suction pump；
Detection meter is arranged in recovery bin and is located at filter layer top, and it is used to detect recovered liquid purity；Control
Module is connected respectively with detection meter, delivery valve and suction pump, and according to detection meter testing result controlled output valve
With suction pump work.
Waste liquid carries out preliminary sedimentation in surge bunker, and, in surge bunker bottom deposit, waste liquid is with the side of overflow for waste residue
Formula enters filtering cabin and is filtered by screen layer by the first connecting tube, and waste residue is trapped within screen layer and enters
Ji Zhacang, filtrate collects in the bottom of filtering cabin.The filtrate that filtering cabin bottom is collected is by the second connection
Pipe enters recovery bin, and filter layer is sequentially passed through in the way of overflow in recovery bin, and filter layer is further
Filter, so as to spill over the purity of the recovered liquid above filter layer on ensureing.
Preferably, also including booster pump, swash is provided with recovery bin, swash is located at filter layer top,
The outfan of booster pump is connected with swash.Booster pump scouring media can be input into into recovery bin to filter layer and
Screen layer carries out regressive erosion, prevents blocking.
Preferably, on-off valve, general control the first connecting tube break-make are installed in the first connecting tube.
Preferably, control module is connected respectively with booster pump and on-off valve；Purity threshold is preset with control module
Value, control module by detect meter testing result compare with purity threshold value, and according to comparative result controlled output valve,
The work of suction pump, booster pump and on-off valve.
Preferably, also including air diffuser, air diffuser is arranged at swash.Be conducive to increase to recovery bin
Wash away area.
Preferably, the quantity of screen layer is no less than two, and from the bottom to top, the filter opening aperture of screen layer is successively
Increase.To carry out layered filtration to the waste residue of different-diameter, the filter pressure of screen layer is reduced.
Preferably, the angle of inclination of screen layer is 15 °～60 °.
Preferably, the angle of inclination of screen layer is 30 °.
Being obliquely installed for screen layer, is conducive to rolling into Ji Zhacang along screen layer under Gravitative Loads in waste residue.
Preferably, the quantity of filter layer is no less than two, and from the bottom to top, the filter opening aperture of filter layer is successively
Reduce.Filter layer is filtered to ensure filter effect in progressive mode to filtrate.
Preferably, the first end of the first connecting tube is connected with the top of surge bunker.So that waste liquid is in surge bunker
Preliminary sedimentation is carried out, then filtering cabin is entered by the first connecting tube in the way of overflow, waste residue is in surge bunker
Bottom deposit,.
In the present invention, detection meter real-time detection recovered liquid purity, and can be by the way that recovered liquid is back to into surge bunker
It is circulated and processes the recovered liquid purity for ensureing final output.In the present invention, by the testing result of detection meter
The output or backflow of recovered liquid are automatically controlled, real-time, reliability is high.
The invention provides a kind of floor space is little, low cost, filtering accuracy are high, and simple structure efficiently,
The cutting fluid filtering recovering system of environmental protection.
Description of the drawings
Fig. 1 is a kind of cutting liquid precipitate filtering recovering system structural representation proposed by the present invention.
Specific embodiment
With reference to Fig. 1, a kind of cutting liquid precipitate filtering recovering system proposed by the present invention, including：Surge bunker 1,
Filtering cabin 2, recovery bin 3, collection slag storehouse 4, the first connecting tube 5, the second connecting tube 6, the 3rd connecting tube 7,
Booster pump 13, detection meter 8 and control module.
The inner inclination of filtering cabin 2 is provided with the screen layer 9 no less than a layer, the low side insertion collection slag of screen layer 9
Storehouse 4.Screen layer 9 can be filtered to waste liquid, and waste residue is retained, and waste residue is rolled under Gravitative Loads
Collection slag storehouse 4.Level is provided with the filter layer 10 no less than a layer in recovery bin 3, and recovery bin 3 is provided with output
Valve 11 is simultaneously located at the top of filter layer 10.
The first end of the first connecting tube 5 is connected with the top of surge bunker 1, and its second end connects with filtering cabin 2
And positioned at the top of screen layer 9.Waste liquid carries out preliminary sedimentation in surge bunker 1, and waste residue is in the bottom of surge bunker 1
Deposition, waste liquid is entered filtering cabin 2 and is filtered by screen layer 9 in the way of overflow by the first connecting tube 5,
Waste residue is trapped within screen layer 9 and enters collection slag storehouse 4, and filtrate collects in the bottom of filtering cabin 2.First
Be provided with connecting tube 5 on-off valve 14 for control the first connecting tube 5 break-make.
In present embodiment, in order to reduce the filter pressure of screen layer 9, blocking, the number of screen layer 9 are prevented
Amount is no less than two, and from the bottom to top, the filter opening aperture of screen layer 9 increases successively, so as to different-diameter
Waste residue carry out layered filtration.Being obliquely installed for screen layer 9, is in Gravitative Loads lower edge for the ease of waste residue
Screen layer 9 and roll into collection slag storehouse 4, the angle of inclination of screen layer 9 can be 15 °～60 °, concretely 30 °.
The first end of the second connecting tube 6 is connected and positioned at the lower section of screen layer 9 with filtering cabin 2, its second end with
Recovery bin 3 is connected and positioned at the lower section of filter layer 10.The filtrate that the bottom of filtering cabin 2 is collected is by the second connection
Pipe 6 enters recovery bin 3, and filter layer 10 is sequentially passed through in the way of overflow in recovery bin 3, and filters
Layer 10 is further filtered, so as to spill over the purity of the recovered liquid of the top of filter layer 10 on ensureing.This embodiment party
In formula, the quantity of filter layer 10 no less than two to ensure filter effect, and from the bottom to top, filter layer 10
Filter opening aperture be sequentially reduced, i.e., filter layer 10 is filtered in progressive mode to filtrate.
The first end of the 3rd connecting tube 7 is connected and positioned at the lower section of filter layer 10 with recovery bin 3, its second end with
Surge bunker 1 is connected.3rd connecting tube 7 is provided with suction pump 12.After opening suction pump 12, in recovery bin 3
Filtrate be back to surge bunker 1, be circulated filtration, it is pure so as to the recovered liquid that can ensure finally to collect
Degree.
Swash is provided with recovery bin 3, swash is located at the top of filter layer 10, the output of booster pump 13
End connects with swash.Booster pump 13 is opened to delivery air or clear water in recovery bin 3, can be to filter layer 10
Regressive erosion is carried out with screen layer 9, waste residue blocking filter layer 10 and screen layer 9 is prevented.Specifically, reclaim
The bottom of storehouse 3 or filtering cabin 2 can arrange drain valve 16, so as to alluvial in recovery bin 3 and filtering cabin 2
Cleanout fluid or purge gas are discharged.
In present embodiment, air diffuser 15 is provided with swash, to expand the output medium pair of booster pump 13
The flushing area of recovery bin 3.
Detection meter 8 is arranged in recovery bin 3 and is located at the top of filter layer 10, and it is used to detect recovered liquid purity.
Control module is connected respectively with detection meter 8, delivery valve 11, suction pump 12, booster pump 13 and on-off valve 14,
And according to detection 8 testing result controlled output valves 11, suction pump 12 of meter, booster pump 13 and the work of on-off valve 14
Make.
Purity threshold value is preset with control module, control module will detect 8 testing results of meter and purity threshold value ratio
Compared with when testing result is more than or equal to purity threshold value, delivery valve 11 and on-off valve 14 are opened, suction pump 12
Close with booster pump 13, the recovered liquid in recovery bin 3 is directly exported；When testing result is less than purity threshold value,
Delivery valve 11 and on-off valve 14 are closed, and suction pump 12 is opened, by the filtration in recovery bin 3 and filtering cabin 2
Liquid is transmitted back to surge bunker 1 and waits circular treatment, is then turned on booster pump 13 to filter layer 10 and screen layer 9
Regressive erosion is carried out, prevents filter opening from blocking.
In present embodiment, detection 8 real-time detection recovered liquid purity of meter, and can be by the way that recovered liquid is back to
Surge bunker 1 is circulated and processes the recovered liquid purity for ensureing final output.In present embodiment, by detection
The testing result of meter automatically controls the output or backflow of recovered liquid, real-time, and reliability is high.
The above, the only present invention preferably specific embodiment, but protection scope of the present invention not office
Be limited to this, any those familiar with the art the invention discloses technical scope in, according to this
The technical scheme of invention and its inventive concept in addition equivalent or change, should all cover the protection in the present invention
Within the scope of.
Claims (10)
1. it is a kind of to cut liquid precipitate filtering recovering system, it is characterised in that to include：Surge bunker (1), filtration
Storehouse (2), recovery bin (3), Ji Zhacang (4), the first connecting tube (5), the second connecting tube (6), the 3rd
Connecting tube (7), detection meter (8) and control module；
Filtering cabin (2) inner inclination is provided with the screen layer (9) no less than a layer, screen layer (9) it is low
End insertion Ji Zhacang (4)；The interior level of recovery bin (3) is provided with the filter layer (10) no less than a layer, reclaims
Storehouse (3) is provided with delivery valve (11) and positioned at filter layer (10) top；
The first end of the first connecting tube (5) is connected with surge bunker (1), and its second end is with filtering cabin (2) even
Lead to and positioned at screen layer (9) top；The first end of the second connecting tube (6) is connected and position with filtering cabin (2)
In screen layer (9) lower section, its second end connects and positioned at filter layer (10) lower section with recovery bin (3)；
The first end of the 3rd connecting tube (7) is connected with recovery bin (3) and positioned at filter layer (10) lower section, it the
Two ends connect with surge bunker (1)；3rd connecting tube (7) is provided with suction pump (12)；
Detection meter (8) is in recovery bin (3) and is located at filter layer (10) top, and it is used to detect
Recovered liquid purity；Control module is connected respectively with detection meter (8), delivery valve (11) and suction pump (12),
And according to detection meter (8) testing result controlled output valve (11) and suction pump (12) work.
2. it is as claimed in claim 1 to cut liquid precipitate filtering recovering system, it is characterised in that also including increasing
Press pump (13), is provided with swash on recovery bin (3), swash is located at filter layer (10) top, increases
The outfan of press pump (13) is connected with swash.
3. it is as claimed in claim 2 to cut liquid precipitate filtering recovering system, it is characterised in that the first connection
On-off valve (14) is installed on pipe (5).
4. it is as claimed in claim 3 to cut liquid precipitate filtering recovering system, it is characterised in that control module
It is connected with booster pump (13) and on-off valve (14) respectively；Purity threshold value is preset with control module, is controlled
Module by detect meter (8) testing result compare with purity threshold value, and according to comparative result controlled output valve (11),
The work of suction pump (12), booster pump (13) and on-off valve (14).
5. it is as claimed in claim 2 to cut liquid precipitate filtering recovering system, it is characterised in that also including scattered
Stream device (15), air diffuser (15) is at swash.
6. it is as claimed in claim 1 to cut liquid precipitate filtering recovering system, it is characterised in that screen layer (9)
Quantity be no less than two, and from the bottom to top, the filter opening aperture of screen layer (9) increases successively.
7. it is as claimed in claim 1 to cut liquid precipitate filtering recovering system, it is characterised in that screen layer (9)
Angle of inclination be 15 °～60 °.
8. it is as claimed in claim 7 to cut liquid precipitate filtering recovering system, it is characterised in that screen layer (9)
Angle of inclination be 30 °.
9. it is as claimed in claim 1 to cut liquid precipitate filtering recovering system, it is characterised in that filter layer (10)
Quantity be no less than two, and from the bottom to top, the filter opening aperture of filter layer (10) is sequentially reduced.
10. it is as claimed in claim 1 to cut liquid precipitate filtering recovering system, it is characterised in that first connects
The first end of adapter (5) is connected with the top of surge bunker (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510726783.6A CN106621547A (en) | 2015-10-28 | 2015-10-28 | Cutting fluid precipitation filtration and recovery system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510726783.6A CN106621547A (en) | 2015-10-28 | 2015-10-28 | Cutting fluid precipitation filtration and recovery system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106621547A true CN106621547A (en) | 2017-05-10 |
Family
ID=58809194
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510726783.6A Pending CN106621547A (en) | 2015-10-28 | 2015-10-28 | Cutting fluid precipitation filtration and recovery system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106621547A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108609770A (en) * | 2018-04-09 | 2018-10-02 | 芜湖立普德机械科技有限公司 | A kind of waste material recovery device based on mobile phone glass substrate |
| CN108943457A (en) * | 2017-05-24 | 2018-12-07 | 上海新昇半导体科技有限公司 | Mortar feeding mechanism |
| CN114225555A (en) * | 2021-12-16 | 2022-03-25 | 浙江壳邦力特油脂有限公司 | Filtering cyclone separation device for removing impurities in waste lubricating oil |
-
2015
- 2015-10-28 CN CN201510726783.6A patent/CN106621547A/en active Pending
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108943457A (en) * | 2017-05-24 | 2018-12-07 | 上海新昇半导体科技有限公司 | Mortar feeding mechanism |
| CN108609770A (en) * | 2018-04-09 | 2018-10-02 | 芜湖立普德机械科技有限公司 | A kind of waste material recovery device based on mobile phone glass substrate |
| CN114225555A (en) * | 2021-12-16 | 2022-03-25 | 浙江壳邦力特油脂有限公司 | Filtering cyclone separation device for removing impurities in waste lubricating oil |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| WD01 | Invention patent application deemed withdrawn after publication | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20170510 |