CN201082373Y - Fluid filtration system - Google Patents
Fluid filtration system Download PDFInfo
- Publication number
- CN201082373Y CN201082373Y CNU2007201461104U CN200720146110U CN201082373Y CN 201082373 Y CN201082373 Y CN 201082373Y CN U2007201461104 U CNU2007201461104 U CN U2007201461104U CN 200720146110 U CN200720146110 U CN 200720146110U CN 201082373 Y CN201082373 Y CN 201082373Y
- Authority
- CN
- China
- Prior art keywords
- filter
- fluid
- fluid filter
- slurry
- outlet
- 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.)
- Expired - Lifetime
Links
- 238000001914 filtration Methods 0.000 title claims abstract description 25
- 239000012530 fluid Substances 0.000 title claims abstract description 20
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims abstract description 15
- 239000007788 liquid Substances 0.000 claims abstract description 12
- 229910052742 iron Inorganic materials 0.000 claims abstract description 8
- 238000010926 purge Methods 0.000 claims description 13
- 239000002184 metal Substances 0.000 claims description 7
- 229910052751 metal Inorganic materials 0.000 claims description 7
- 238000007599 discharging Methods 0.000 claims description 6
- 239000000463 material Substances 0.000 claims description 6
- 239000000835 fiber Substances 0.000 claims description 5
- 238000011084 recovery Methods 0.000 claims description 4
- 239000002904 solvent Substances 0.000 claims description 2
- 239000002245 particle Substances 0.000 abstract description 7
- 238000005516 engineering process Methods 0.000 abstract description 3
- 239000012535 impurity Substances 0.000 abstract description 2
- 238000011001 backwashing Methods 0.000 abstract 3
- 239000002002 slurry Substances 0.000 description 28
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical group CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 5
- 238000000576 coating method Methods 0.000 description 4
- 239000011248 coating agent Substances 0.000 description 3
- 238000011010 flushing procedure Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000000356 contaminant Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Images
Abstract
The utility model relates to a fluid filtering system, which comprises an iron removal device, a filtering device, a back washing device, a reclaiming device, and a driving device, wherein the iron removal device is provided with an iron removal groove, and a feed inlet and a discharge outlet are arranged at the two ends of the side walls of the iron removal groove; the filtering device is provided with an inlet and an outlet at the both ends, and the inlet end of the filtering device is connected with the discharge outlet of the iron removal device; the back washing device is provided with a liquid outlet at one end, and the liquid outlet is connected with the outlet of filtering device; the reclaiming device is provided with a reclamation opening at one end, and the reclamation opening is connected with the inlet of the filtering device; and the driving device is respectively connected with the filtering device and the back washing device. The utility model not only can effectively remove the impurity small particles in the fluid but also is convenient for rinsing by adopting the technology proposal.
Description
Technical field
The utility model relates to the mechanical device field, relates in particular to a kind of fluid filter system that contaminant particles in the fluid is removed.
Background technology
At present, in the battery production process, normally the liquid slurry of the both positive and negative polarity of battery is formed by coating, the filtration system of coating plant all is the manually-operated lift, the slurry after stirring is passed through metallic sieve, and then finish filter process.
Slurry is in layoutprocedure, might sneak into some metal impurities, and use the metal mesh filter slurry because the slurry viscosity is bigger, in filter process, by the slurry compressive strain, some particles just are difficult to be filtered easily, cause in the coating process particle bad more, influence electric core quality, increase the hidden danger of electric core blast.
Present stage has been produced various fluid filter systems, still, we see the defective of its existence be removal of contamination not thoroughly and be difficult to clean.
The utility model content
For solving the problems of the technologies described above, the utility model provides a kind of fluid filter system of not only effectively having removed contaminant particles in the fluid but also being convenient to clean.
The utility model is achieved through the following technical solutions: a kind of fluid filter system, comprise deironing apparatus, and have iron removal trough, its two ends are provided with charging aperture and discharging opening; Filter, its two ends have entrance and exit, and the arrival end of described filter connects described deironing apparatus discharging opening; Back purge system, the one end has a liquid outlet, and described liquid outlet connects described filter outlet; Retracting device, one end have the mouth of recovery, the described filter inlet of described recovery mouthful connection; Drive unit connects described filter and back purge system.
Described deironing apparatus inside is provided with iron-absorbing mass.
Described iron-absorbing mass is a plurality of magnet.
Described filter comprises the filter core of crossing of the shell and the portion that sets within it.
The described filter core of crossing comprises that the bracing or strutting arrangement and the portion of setting within it be equipped with the filter bag of filtering material.
Described filtering material is a metal fiber felt.
The machine solvent is equipped with in described back purge system inside.
Described organic solvent is an acetone.
Described power set are pneumatic diaphragm pumps.
Connect by pipeline between described each device, control valve is set on it.
The beneficial effects of the utility model are: owing to realize the automation of filtration system, slurry after the homogenate directly enters the slurry bucket, reduced the open-assembly time of slurry, thereby reduced, improved the uniformity of slurry viscosity because of contact the possibility that changes with air; Owing to use back purge system, saved great deal of labor; Again owing to adopt high performance metal fiber felt filter material, the ratio of precision that makes filtration filter screen in the past increases and has reusable advantage, therefore can effectively reduce the particle in the slurry, improve the uniformity of slurry viscosity, improve coating quality, and eliminate the potential safety hazard of electric core to a large extent; And then, therefore in the environment of sealing, can prevent effectively that slurry from absorbing water in air owing to deironing, filtration, backwash are all carried out in pipeline, avoid anodal some slurry hardening.
Description of drawings
Fig. 1 is an overall structure schematic diagram of the present utility model.
The specific embodiment
The utility model is described in further detail below in conjunction with the drawings and specific embodiments.
As shown in Figure 1, a kind of fluid filter system of the present utility model comprises deironing apparatus 9, filter 12, back purge system 11, retracting device 13, drive unit 10; Described deironing apparatus 9 has the de-iron groove, and its inside is provided with a plurality of magnet, and its sidewall two ends are provided with charging aperture and discharging opening; Described filter 12 comprises shell body and crosses filter core two parts, crossing filter core is made up of bracing or strutting arrangement and metal fiber felt filter bag, this filter material of metal fiber felt has good strainability, its three-dimensional structure can be carried out multiple filtration to slurry, bigger toughness and intensity can prevent to produce distortion when slurry from passing through, and it is repeatedly used the very big cost of performance saving; Organic solvent-acetone is equipped with in described back purge system 11 inside, and the one end has liquid outlet; Described retracting device 13 is one can be in order to receive the container of flushing back waste liquid, one end opening; Described drive unit 10 is a pneumatic diaphragm pump.
The feeding mouth of described deironing apparatus 9 connects slurry storing barrel 8 by pipeline, and be arranged on the below of slurry storing barrel, it is the first road filter of filtration system, its discharging opening connects the arrival end of filter 12 by pipeline, and open and close between the two by valve 1,4 control, in order to help flushing, allow slurry pass through the external pressure process filter 12 that pneumatic diaphragm pump 10 is given, finish filtration; The liquid outlet of described back purge system 11 connects the outlet of described filter 12 by pipeline, and by the switching that valve 2,3,7 is controlled between the two, can in time carry out backwash to crossing filter core, increases work efficiency; The outlet of described filter 12 connects dispense tip 14 by pipeline, and the slurry after filtering is delivered directly to dispense tip 14, and passes through the switching that valve 6 is controlled between the two; The recovery mouth of described retracting device 13 connects described overanxious device 12 inlets by pipeline, and passes through the switching that valve 5 is controlled between the two; Described pneumatic diaphragm pump 10 connects described filter 12 and back purge system 11 by pipeline, because the viscosity ratio of slurry is bigger, in order to guarantee production efficiency, provide power with pneumatic diaphragm pump 10 for filter 12 and back purge system 11, make liquid pass through filtration system fast.
This fluid filter system course of work is:
Deironing, filtration
Slurry is opened 1,4,6 valves after stirring, and closes 2,3,5,7 valves.The slurry that is contained in the slurry storing barrel 8 at first passes through deironing apparatus 9 under the effect of gravity, after the deironing, pass through filter 12 under the pressure of pneumatic diaphragm pump 10, slurry is filtered, remove larger particles, finish filtration after, slurry directly is forced on the dispense tip and is coated with.
Backwash
After the slurries filtration,, must carry out backwash in time in order to guarantee to cross in the filter 12 repeat performance of filter core.At this time want valve-off 1,4,6, open valve 2,3,5,7, be contained in cleaning fluid acetone in the back purge system 11 under the pressure of pneumatic diaphragm pump 10 against the slurries filtration direction, promptly enter again to come out from inlet from filter 12 outlets, carry out backwash to crossing filter core, the waste liquid spot after the flushing directly is discharged in the container of retracting device 13.
Yet the above is a preferred embodiment of the present utility model only, is not so limits to scope of the present utility model, so the equivalent structure that utilization the utility model specification and accompanying drawing content are carried out changes, all in like manner is included in the scope of the present utility model.
Claims (7)
1. a fluid filter system is characterized in that, comprises
Deironing apparatus has iron removal trough, and its sidewall two ends are provided with charging aperture and discharging opening;
Filter, its two ends have entrance and exit, and the arrival end of described filter connects described deironing apparatus discharging opening;
Back purge system, the one end has a liquid outlet, and described liquid outlet connects described filter outlet;
Retracting device, one end have the mouth of recovery, and described retracting device reclaims the described filter inlet of mouthful connection; And
Drive unit connects described filter and back purge system.
2. fluid filter system according to claim 1 is characterized in that, described deironing apparatus inside is provided with iron-absorbing mass.
3. fluid filter system according to claim 2 is characterized in that, described iron-absorbing mass is that a plurality of magnet are formed.
4. fluid filter system according to claim 1 is characterized in that, described filter comprises the filter core of crossing of the shell and the portion that sets within it.
5. fluid filter system according to claim 4 is characterized in that, the described filter core of crossing comprises that the bracing or strutting arrangement and the portion of setting within it be equipped with the filter bag of filtering material.
6. fluid filter system according to claim 5 is characterized in that described filtering material is a metal fiber felt.
7. fluid filter system according to claim 1 is characterized in that, the machine solvent is equipped with in described back purge system inside.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007201461104U CN201082373Y (en) | 2007-04-10 | 2007-04-10 | Fluid filtration system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007201461104U CN201082373Y (en) | 2007-04-10 | 2007-04-10 | Fluid filtration system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201082373Y true CN201082373Y (en) | 2008-07-09 |
Family
ID=39624835
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2007201461104U Expired - Lifetime CN201082373Y (en) | 2007-04-10 | 2007-04-10 | Fluid filtration system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201082373Y (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102239595A (en) * | 2008-12-08 | 2011-11-09 | 株式会社日立制作所 | Process for producing lithium secondary battery |
| CN103314472A (en) * | 2011-01-13 | 2013-09-18 | 丰田自动车株式会社 | Electrode material applying apparatus, and filtering apparatus |
| CN104291392A (en) * | 2014-09-27 | 2015-01-21 | 姚健军 | Resource-saving water treatment facility |
| CN108107946A (en) * | 2018-01-23 | 2018-06-01 | 深圳市曼恩斯特科技有限公司 | Constant temperature feeding system |
-
2007
- 2007-04-10 CN CNU2007201461104U patent/CN201082373Y/en not_active Expired - Lifetime
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102239595A (en) * | 2008-12-08 | 2011-11-09 | 株式会社日立制作所 | Process for producing lithium secondary battery |
| CN102239595B (en) * | 2008-12-08 | 2014-11-05 | 株式会社日立制作所 | Process for producing lithium secondary battery |
| CN103314472A (en) * | 2011-01-13 | 2013-09-18 | 丰田自动车株式会社 | Electrode material applying apparatus, and filtering apparatus |
| CN103314472B (en) * | 2011-01-13 | 2016-08-31 | 丰田自动车株式会社 | Electrode material applying device and defecator |
| CN104291392A (en) * | 2014-09-27 | 2015-01-21 | 姚健军 | Resource-saving water treatment facility |
| CN104291392B (en) * | 2014-09-27 | 2016-10-05 | 吴玲玲 | The water treatment facilities economized on resources |
| CN108107946A (en) * | 2018-01-23 | 2018-06-01 | 深圳市曼恩斯特科技有限公司 | Constant temperature feeding system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20080709 |