CN107670364A - Continuously thickening filter and its thickening system and method for thickening - Google Patents
Continuously thickening filter and its thickening system and method for thickening Download PDFInfo
- Publication number
- CN107670364A CN107670364A CN201711011791.8A CN201711011791A CN107670364A CN 107670364 A CN107670364 A CN 107670364A CN 201711011791 A CN201711011791 A CN 201711011791A CN 107670364 A CN107670364 A CN 107670364A
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- CN
- China
- Prior art keywords
- filter
- group
- fuselage
- thickening
- filtering
- 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.)
- Granted
Links
- 230000008719 thickening Effects 0.000 title claims abstract description 38
- 238000000034 method Methods 0.000 title claims abstract description 7
- 238000001914 filtration Methods 0.000 claims abstract description 43
- 239000000463 material Substances 0.000 claims abstract description 36
- 230000000712 assembly Effects 0.000 claims abstract description 6
- 238000000429 assembly Methods 0.000 claims abstract description 6
- 239000007788 liquid Substances 0.000 claims abstract description 6
- 230000015572 biosynthetic process Effects 0.000 claims abstract description 5
- 238000007599 discharging Methods 0.000 claims description 12
- 238000012544 monitoring process Methods 0.000 claims description 3
- 238000009423 ventilation Methods 0.000 claims description 3
- 238000007664 blowing Methods 0.000 claims description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000001471 micro-filtration Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/50—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with multiple filtering elements, characterised by their mutual disposition
- B01D29/52—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with multiple filtering elements, characterised by their mutual disposition in parallel connection
- B01D29/54—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with multiple filtering elements, characterised by their mutual disposition in parallel connection arranged concentrically or coaxially
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/62—Regenerating the filter material in the filter
- B01D29/66—Regenerating the filter material in the filter by flushing, e.g. counter-current air-bumps
- B01D29/68—Regenerating the filter material in the filter by flushing, e.g. counter-current air-bumps with backwash arms, shoes or nozzles
- B01D29/688—Regenerating the filter material in the filter by flushing, e.g. counter-current air-bumps with backwash arms, shoes or nozzles with backwash arms or shoes acting on the cake side
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Filtration Of Liquid (AREA)
Abstract
The invention provides a kind of continuously thickening filter and its thickening system and method for thickening, the viscosity of material needed for reaching is thickened by the continuous filtering of thickening filter progress of the present invention, heretofore described filter includes filter fuselage, the filtering area of filter assemblies formation is provided with the fuselage, the filter fuselage center is vertically installed with a live spindle, superposition is arranged with some groups of screen pipes in the live spindle, agitating paddle is arranged at intervals between screen pipe described in every group, it is provided with the top of the filter fuselage in the drive mechanism of live spindle connection, the cleaner liquid of the screen pipe is discharged from the side of filter fuselage.The present invention uses stacked filter assemblies, and while increasing filter area, viscosity that can also be while filtering needed for control, a tractor serves several purposes, practicality is high.
Description
Technical field
The invention belongs to micro porous filtration thickening technology field, and in particular to a kind of quick continuously thickening filter and its thickening
System.
Background technology
The application scenario of Millipore filtration techniques is more and more extensive, and a card is provided with the top of existing microporous filter,
Filter core is vertically arranged with the card, material is flowed out after being filtered by filter core by the cleaner liquid passage in card.By
In the uniform vertical form of the filter core on its card, if after cartridge surface is covered by filter residue, only by washing can not well by
Its filter residue removes, and cause subsequently to press dry and filter is not thorough, and filter effect is bad.Meanwhile there is viscosity for some
Feed liquid can not be by controlling its viscosity in filtering, and efficiency is low.
The content of the invention
In order to solve the deficiencies in the prior art, quickly increase continuous thick filter and its thickening system the invention provides a kind of
System.
The purpose of the present invention is achieved through the following technical solutions：
Continuously thickening filter, including filter fuselage, the filtering area of filter assemblies formation, the mistake are provided with the fuselage
Filter body center is vertically installed with a live spindle, is superimposed in the live spindle and is arranged with some groups of filter layers, described in every group
Agitating paddle is arranged at intervals between filter layer, the driving being connected with the live spindle is provided with the top of the filter fuselage
Mechanism, the cleaner liquid of the screen pipe are discharged from the side of filter fuselage.
Preferably, the screen pipe group that filter layer described in every group is set at least provided with two layers of upper and lower superposition, the adjacent mistake
It is arranged at intervals between chimney filter group, every layer of screen pipe group is made up of the tiling of multiple screen pipes, and the filtration channel of screen pipe
Openend and the discharge pipe UNICOM outside filter fuselage.
Preferably, the upper end of the filter is provided with charging aperture, and the bottom of the filter is provided with underflow outlet, institute
The side for stating underflow outlet offers a feedback outlet.
Preferably, the filter also includes the pressure gauge for being used to detect pressure in filter for being arranged at fuselage roof.
Preferably, the filter fuselage lower end is provided with a lower cover, and the lower cover is taper, and the underflow outlet is set
In the lower cover bottom.
Preferably, the drive mechanism is reductor, and the reductor is arranged at the filter by machine frame of speed reducing machine
Surface.
Preferably, the side of the filter discharge pipe is additionally provided with blowback pipeline.
Preferably, the blowback pipeline passes through valve UNICOM with the discharge pipe.
Preferably, the fast thickening filter system described in any of the above, including a fast thickening filter and the mistake
The material kettle of filter connection, is provided with feed pump between the material kettle and the filter, the feedback outlet of the filter with
Material kettle is additionally provided with a quantifier by pipeline UNICOM, the discharging opening of the filter.
Preferably, above-described continuously thickening filter method, comprises the following steps：
S1, material enter the charging aperture of filter fuselage by material kettle；
S2, drive mechanism driving live spindle slowly rotate, and material passes through the filtering of screen pipe, and the filtering material after filtering is by going out
Pipe material is discharged；And detect the amount of discharging opening in real time by the quantifier of discharging opening, viscosity is calculated with this；
S3, by detecting the pressure in filter, if reaching the pressure of setting, feedback outlet is opened, by the material in filter
Returned in material kettle and circulated by feedback outlet；
S4, first group of blowback valve in blowback pipeline is opened, now, close the outlet valve of first group of screen pipe group of discharging opening
Door, the blowback of first group of screen pipe group of ventilation progress out of blowback pipeline；Now, the filtering of other screen pipe groups is not influenceed；
S5, after completing S4, first group of blowback valve is closed, open the discharge valve of first group of screen pipe group；It is anti-by second group
Blowing valve is opened, and is closed the discharge valve of second group of screen pipe group, is carried out corresponding blowback；The like carry out filtering layer by layer
And blowback；Until reaching required concentration；
S6, complete material thickening work after, to filter fuselage interior carry out blowback step, meanwhile, pass through the pressure of filter
Power table implements the pressure in monitoring and controlling filter；
S7, most underflow exports discharge from the underflow of filtering motor spindle at last.
Beneficial effects of the present invention are embodied in：, can also be while increasing filter area using stacked filter assemblies
Filtering controls required viscosity, a tractor serves several purposes, practicality height simultaneously.
Brief description of the drawings
Fig. 1：The structural representation of filter of the present invention.
Fig. 3：The cross-sectional view of filter layer of the present invention.
Fig. 2：Filtration system structural representation with filter of the present invention.
Embodiment
Technical scheme is specifically described with reference to embodiments, and with reference to shown in Fig. 1-Fig. 3, present invention is disclosed one
Quick continuously thickening filter, including filter fuselage 1, the upper lid of the filtering fuselage 1 are provided with charging aperture 3 and for detecting
The pressure gauge 9 of pressure in filter fuselage.The lower end of filter fuselage 1 is provided with a taper lower cover, the bottom of the lower cover
Offer underflow outlet 7.The side of the underflow outlet 7 offers a feedback outlet.
The filtering area of filter assemblies formation is provided with the fuselage 1, the filtering fuselage center is vertically installed with a rotation
Turn main shaft, be superimposed in the live spindle and be arranged with some groups of filter layers.Filter layer described in every group is upper and lower at least provided with two layers
The screen pipe group set is superimposed, every layer of screen pipe group is made up of the tiling of multiple screen pipes 4, with 3 layers of tiling in the present embodiment
Screen pipe group be set to one group of formation filtering area.The screen pipe of layered laminate can greatly increase filter area.
In order to preferably carry out the stirring of material, agitating paddle 5, the filtering are provided between screen pipe described in adjacent every group
The top of machine fuselage 1 is provided with the drive mechanism of live spindle connection, and the cleaner liquid of the screen pipe is from filter machine
The side discharge of body.The drive mechanism is reductor 11, and the reductor is arranged at the filter by machine frame of speed reducing machine
Surface.
With reference to shown in Fig. 2, the screen pipe is microfiltration tube, is internally provided with filtration channel, the screen pipe group
Centre offers the mounting hole 42 for being connected with live spindle, and the filtration channel 41 is by one lateral screen pipe of screen pipe
Extension is formed at the blind hole in the screen pipe, and the openend of the filtration channel passes through a UNICOM road 43 and filter fuselage
The outer UNICOM of discharge pipe 6.The side of the filter discharge pipe 6 is additionally provided with blowback pipeline 61.The blowback pipeline with
The discharge pipe passes through corresponding blowback valve and discharge valve UNICOM.It is arranged in parallel between every group of screen pipe group, with more preferable
Carry out continuously thickening filtering, do not interfere with each other.
Present invention further teaches a kind of thickening filtration system using above-described fast thickening filter, including one fast
Speed thickening filter, the material kettle 12 that is connected with the filter, be provided between the material kettle 12 and the filter into
Expect pump 13, feedback outlet and the material kettle of the filter are additionally provided with a meter by pipeline UNICOM, the discharging opening of the filter
Gauge.
Meanwhile the present invention also illustrates a kind of continuously thickening filter method that filter is thickened using contact described above,
Comprise the following steps：
S1, material enter the charging aperture of filter fuselage by material kettle；
S2, drive mechanism driving live spindle slowly rotate, and material passes through the filtering of screen pipe, and the filtering material after filtering is by going out
Pipe material is discharged；And detect the amount of discharging opening in real time by the quantifier of discharging opening, viscosity is calculated with this；
S3, by detecting the pressure in filter, if reaching the pressure of setting, open feedback outlet 71, by the thing in filter
Material is returned in material kettle by feedback outlet and circulated；
S4, first group of blowback valve 62 in blowback pipeline is opened, now, close the outlet valve of first group of screen pipe group of discharging opening
Door 63, the blowback of first group of screen pipe group of ventilation progress out of blowback pipeline；Now, the filtering of other screen pipe groups is not influenceed；
S5, after completing S4, first group of blowback valve 62 is closed, open the discharge valve 63 of first group of screen pipe group；By second
Group blowback valve is opened, and is closed the discharge valve of second group of screen pipe group, is carried out corresponding blowback；The like carry out layer by layer
Filtering and blowback；Until reaching required concentration；
S6, complete material thickening work after, to filter fuselage interior carry out blowback step, meanwhile, pass through the pressure of filter
Power table implements the pressure in monitoring and controlling filter；
S7, most underflow exports discharge from the underflow of filtering motor spindle at last.
Certainly the present invention still has a variety of specific embodiments, does not just enumerate herein.It is all using equivalent substitution or
Equivalent transformation and all technical schemes formed, all fall within the scope of protection of present invention.
Claims (10)
1. continuously thickening filter, including filter fuselage, the filtering area of filter assemblies formation is provided with the fuselage, it is special
Sign is：The filtering fuselage center is vertically installed with a live spindle, is superimposed in the live spindle and is arranged with some groups of mistakes
Filtering layer, agitating paddle is arranged at intervals between filter layer described in every group, is provided with the top of the filter fuselage in the rotation
The drive mechanism of main shaft connection, the cleaner liquid of the screen pipe are discharged from the side of filter fuselage.
2. continuously thickening filter as claimed in claim 1, it is characterised in that：Filter layer is at least provided with two layers described in every group
It is upper and lower to be superimposed the screen pipe group set, it is arranged at intervals between the adjacent screen pipe group, every layer of screen pipe group is by multiple mistakes
Chimney filter tiling is formed, and the openend of the filtration channel of the screen pipe in every group of filter layer and the discharge pipe outside filter fuselage
UNICOM.
3. continuously thickening filter as claimed in claim 1, it is characterised in that：The upper end of the filter is provided with charging
Mouthful, the bottom of the filter is provided with underflow outlet, and the side of the underflow outlet offers a feedback outlet.
4. continuously thickening filter as claimed in claim 3, it is characterised in that：The filter also includes being arranged at fuselage top
The pressure gauge for being used to detect pressure in filter in portion.
5. continuously thickening filter as claimed in claim 4, it is characterised in that：The filter fuselage lower end is provided with
Lid, the lower cover is taper, and the underflow outlet is arranged at the lower cover bottom.
6. continuously thickening filter as claimed in claim 5, it is characterised in that：The drive mechanism is reductor, described to subtract
Fast machine is arranged at the surface of the filter by machine frame of speed reducing machine.
7. continuously thickening filter as claimed in claim 5, it is characterised in that：The side of the filter discharge pipe is also set
It is equipped with blowback pipeline.
8. continuously thickening filter as claimed in claim 7, it is characterised in that：The blowback pipeline leads to the discharge pipe
Cross corresponding valve UNICOM.
9. the continuously thickening filter system as described in any in claim 1-8, it is characterised in that：Including a fast thickening mistake
Filter, the material kettle being connected with the filter, are provided with feed pump, the filtering between the material kettle and the filter
The feedback outlet of machine is additionally provided with a quantifier with material kettle by pipeline UNICOM, the discharging opening of the filter.
A kind of 10. continuously thickening filter method as claimed in claim 1, it is characterised in that：Comprise the following steps：
S1, material enter the charging aperture of filter fuselage by material kettle；
S2, drive mechanism driving live spindle slowly rotate, and material passes through the filtering of screen pipe, and the filtering material after filtering is by going out
Pipe material is discharged；And detect the amount of discharging opening in real time by the quantifier of discharging opening, viscosity is calculated with this；
S3, by detecting the pressure in filter, if reaching the pressure of setting, feedback outlet is opened, by the material in filter
Returned in material kettle and circulated by feedback outlet；
S4, first group of blowback valve in blowback pipeline is opened, now, close the outlet valve of first group of screen pipe group of discharging opening
Door, the blowback of first group of screen pipe group of ventilation progress out of blowback pipeline；Now, the filtering of other screen pipe groups is not influenceed；
S5, after completing S4, first group of blowback valve is closed, open the discharge valve of first group of screen pipe group；It is anti-by second group
Blowing valve is opened, and is closed the discharge valve of second group of screen pipe group, is carried out corresponding blowback；The like carry out filtering layer by layer
And blowback；Until reaching required concentration；
S6, complete material thickening work after, to filter fuselage interior carry out blowback step, meanwhile, pass through the pressure of filter
Power table implements the pressure in monitoring and controlling filter；
S7, most underflow exports discharge from the underflow of filtering motor spindle at last.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711011791.8A CN107670364B (en) | 2017-10-26 | 2017-10-26 | Continuous thickening filter and thickening system and thickening method thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711011791.8A CN107670364B (en) | 2017-10-26 | 2017-10-26 | Continuous thickening filter and thickening system and thickening method thereof |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN107670364A true CN107670364A (en) | 2018-02-09 |
| CN107670364B CN107670364B (en) | 2023-07-18 |
Family
ID=61141595
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201711011791.8A Active CN107670364B (en) | 2017-10-26 | 2017-10-26 | Continuous thickening filter and thickening system and thickening method thereof |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107670364B (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110102080A (en) * | 2018-05-28 | 2019-08-09 | 浙江东瓯过滤机制造有限公司 | The short grained filtering-condensing apparatus of ternary precursor and method for concentration with stirring |
| CN110270292A (en) * | 2019-07-15 | 2019-09-24 | 威孔过滤科技（苏州）有限公司 | Ternary precursor filtering and concentrating system and its method for concentration |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102527123A (en) * | 2010-12-07 | 2012-07-04 | 苏州恒尔机械制造有限公司 | Tube plate combined type filter |
| CN202555043U (en) * | 2012-03-29 | 2012-11-28 | 邢传宏 | Filter tube and filter assembly composed of the filter tube |
| CN104645690A (en) * | 2015-02-11 | 2015-05-27 | 合肥通用机械研究院 | Layered multi-filter disc filter |
| CN206366234U (en) * | 2016-11-16 | 2017-08-01 | 西安超滤环保科技股份有限公司 | A kind of slurry is automatically counter to clean filtering recovering system |
| CN207591389U (en) * | 2017-10-26 | 2018-07-10 | 威孔过滤科技（苏州）有限公司 | Continuously thickening filter and its thickening system |
-
2017
- 2017-10-26 CN CN201711011791.8A patent/CN107670364B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102527123A (en) * | 2010-12-07 | 2012-07-04 | 苏州恒尔机械制造有限公司 | Tube plate combined type filter |
| CN202555043U (en) * | 2012-03-29 | 2012-11-28 | 邢传宏 | Filter tube and filter assembly composed of the filter tube |
| CN104645690A (en) * | 2015-02-11 | 2015-05-27 | 合肥通用机械研究院 | Layered multi-filter disc filter |
| CN206366234U (en) * | 2016-11-16 | 2017-08-01 | 西安超滤环保科技股份有限公司 | A kind of slurry is automatically counter to clean filtering recovering system |
| CN207591389U (en) * | 2017-10-26 | 2018-07-10 | 威孔过滤科技（苏州）有限公司 | Continuously thickening filter and its thickening system |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110102080A (en) * | 2018-05-28 | 2019-08-09 | 浙江东瓯过滤机制造有限公司 | The short grained filtering-condensing apparatus of ternary precursor and method for concentration with stirring |
| CN110102081A (en) * | 2018-05-28 | 2019-08-09 | 浙江东瓯过滤机制造有限公司 | The short grained filtering-condensing apparatus of ternary precursor and filtration and concentration method |
| CN110102080B (en) * | 2018-05-28 | 2022-09-16 | 浙江东瓯过滤机制造有限公司 | Filtering and concentrating device and method for ternary precursor granules with stirring function |
| CN110102081B (en) * | 2018-05-28 | 2022-09-16 | 浙江东瓯过滤机制造有限公司 | Filtering and concentrating device and filtering and concentrating method for ternary precursor small particles |
| CN110270292A (en) * | 2019-07-15 | 2019-09-24 | 威孔过滤科技（苏州）有限公司 | Ternary precursor filtering and concentrating system and its method for concentration |
Also Published As
| Publication number | Publication date |
|---|---|
| CN107670364B (en) | 2023-07-18 |
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