CN107149802A - Horizontal efficient microporous filter - Google Patents
Horizontal efficient microporous filter Download PDFInfo
- Publication number
- CN107149802A CN107149802A CN201710421675.7A CN201710421675A CN107149802A CN 107149802 A CN107149802 A CN 107149802A CN 201710421675 A CN201710421675 A CN 201710421675A CN 107149802 A CN107149802 A CN 107149802A
- Authority
- CN
- China
- Prior art keywords
- filter
- cylinder
- collector tube
- end cover
- microporous 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
- 239000007788 liquid Substances 0.000 claims abstract description 52
- 238000007599 discharging Methods 0.000 claims abstract description 36
- 230000007246 mechanism Effects 0.000 claims description 11
- 239000007921 spray Substances 0.000 claims description 5
- 238000007789 sealing Methods 0.000 claims description 4
- 240000007594 Oryza sativa Species 0.000 claims description 2
- 235000007164 Oryza sativa Nutrition 0.000 claims description 2
- 235000021186 dishes Nutrition 0.000 claims description 2
- 238000003780 insertion Methods 0.000 claims description 2
- 230000037431 insertion Effects 0.000 claims description 2
- 235000009566 rice Nutrition 0.000 claims description 2
- 238000001914 filtration Methods 0.000 abstract description 23
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 238000012423 maintenance Methods 0.000 abstract description 2
- 239000000463 material Substances 0.000 description 10
- 239000007789 gas Substances 0.000 description 9
- 238000011069 regeneration method Methods 0.000 description 7
- 238000000034 method Methods 0.000 description 6
- 230000008929 regeneration Effects 0.000 description 6
- 230000008569 process Effects 0.000 description 5
- 239000007787 solid Substances 0.000 description 5
- 238000004140 cleaning Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000003921 oil Substances 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 239000000919 ceramic Substances 0.000 description 2
- 230000006837 decompression Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 238000005245 sintering Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 206010020852 Hypertonia Diseases 0.000 description 1
- 241000233855 Orchidaceae Species 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 230000005520 electrodynamics Effects 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000012065 filter cake Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000010720 hydraulic oil Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000010926 purge Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000009418 renovation Methods 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 238000013022 venting 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
- B01D29/39—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 hollow discs side by side on, or around, one or more tubes, e.g. of the leaf type
- B01D29/41—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 hollow discs side by side on, or around, one or more tubes, e.g. of the leaf type mounted transversely on the tube
-
- 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
-
- 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
-
- 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
- B01D29/88—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor having feed or discharge devices
- B01D29/92—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor having feed or discharge devices for discharging filtrate
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Filtering Materials (AREA)
Abstract
The invention provides a kind of horizontal efficient microporous filter, including the cylinder being placed on track and the end cover being engaged with the cylinder, a collector tube is laterally equipped with filter, some filters are arranged with collector tube, the adjacent filter be arranged in parallel, and outermost filter is compressed by friction top, one end of collector tube is extended through for the discharging opening that cleaner liquid is formed outside end cover, the entrance of collector tube and the cleaner liquid passage UNICOM in the filter.Filter uses micro-porous filtration plate as medium, because the structure of micro-porous filtration plate make it that the filter area of filter is bigger.It is easy to clear up filter or to carry out replacement operation to micro-porous filtration plate simple, installs, easy to maintenance.The cylinder of filter is sleeping to put that setting is in orbit, and it is bigger that diameter can be done, and it is longer that cylinder can be done, therefore has the advantages that filter efficiency is higher, production capacity is higher.
Description
Technical field
The invention belongs to a kind of microporous filter, and in particular to a kind of horizontal efficient microporous filter.
Background technology
With the rapid growth of China's economy, the demand to all types of industries product is also increasing, in all types of industries product
Production technology in, the separation to solid and liquid is seen everywhere.So-called separation of solid and liquid is from mixed containing solid and liquid
The process for separating solid and liquid in compound, including the material for the fluid purification and removal liquid component for removing solid constituent take off
Water etc..
Solid-liquid separating equipment common at present has centrifuge, plate and frame filter press, plate filter, bag type filtering machine, candle formula
Filter, ceramic filter, titanium rod filter, microporous filter.Filter medium used also has many kinds, such as filter cloth, filter
Paper, ceramic post sintering filter core, Ti-alloyed filter element, metal agglomeration filter core, PE sintered filter cores.
Existing microporous filter is broadly divided into vertical and horizontal two kinds, and vertical microporous filter can be divided into pattern board type and row again
Tubular type, pattern board type is to open many holes on one block of plate supporting with filter, is then vertically mounted on a plurality of PE sintered filter cores
Filtered on card；Calandria is to set many collector tubes in filtering machine drum body, then PE sintered filter cores are vertically mounted on
On collector tube.Above-mentioned microporous filter can also set PE sintered filter cores or PE sintering filter plates to be remained in cylinder in the bottom of cylinder
Remaining material filtering is clean, reaches the effect for not staying surplus material.Horizontal microporous filter, which is that cylinder is sleeping, to be positioned on track, on cylinder
Portion sets aggregate pipe, the right angle setting PE sintered filter cores on aggregate pipe.But the filter core of such a horizontal microporous filter is arranged on cylinder
Internal portion, difficulty is being brought to filter element replacing and when safeguarding to operating personnel.
The content of the invention
The invention provides a kind of production capacity is higher, installs, operate, safeguard more easy, the longer horizontal height of service life
Imitate microporous filter.
The purpose of the present invention is achieved through the following technical solutions：
Horizontal efficient microporous filter, including the cylinder being placed on track and the end cover being engaged with the cylinder, it is described
Laterally it is equipped with filter on a collector tube, the collector tube and is arranged with some filters, the adjacent filter is parallel is set
Put, and outermost filter is compressed by friction top, one end of the collector tube is extended through for forming filtering outside end cover
The discharging opening of liquid, the entrance of the collector tube and the cleaner liquid passage UNICOM in the filter.
Preferably, the cylinder is set up on the track by cylinder stent, and rolling is provided with below the cylinder stent
Mechanism is taken turns, the idler wheel mechanism drives cylinder stent to slide in orbit.
Preferably, the end cover is set up in one end of dragging track by support, and the support is high with cylinder stent
Degree is suitable, and is arranged on same straight line.
Preferably, it is provided with sealing gasket between the adjacent filter.
Preferably, it is provided with least one auxiliary discharging opening, the collector tube and is provided with not below the collector tube
With liquid collecting subregion, each liquid collecting subregion is connected with discharging opening and auxiliary discharging opening respectively.
Preferably, the collector tube is arranged in filter by support frame, and support frame as described above and the collector tube are mutual
It is vertically arranged, the cylinder, which is provided with, slides light rail, support frame as described above slides light rail cooperation, the two ends of support frame as described above with described
Slided described in embedded in light rail.
Preferably, the end cover is connected with the cylinder by clamp ring locking.
Preferably, the end cover upper end is provided with drain, mouth spray and air inlet.
Preferably, the bottom of the end cover is provided with a clout mouthful.
Preferably, the end cover side is provided with a charging aperture.
Beneficial effects of the present invention are embodied in：Filter uses micro-porous filtration plate as medium, due to micro-porous filtration plate
Structure make it that the filter area of filter is bigger.When cylinder and end cover, which are sealed, to be coordinated, filter can be consolidated to material
Liquid separating technology, when needing to clear up filter or micro-porous filtration plate being changed, can remove cylinder, operation
Simply, install, it is easy to maintenance.The cylinder of filter is sleeping to put setting in orbit, and it is bigger that diameter can be done, what cylinder can be done
It is longer, therefore have the advantages that filter efficiency is higher, production capacity is higher.
Figure of description
Fig. 1：The structural representation of the present invention.
Fig. 2：Micro-porous filtration plate subregion filtering cleaner liquid of the present invention flows to schematic diagram.
Fig. 3：Hydraulic oil cylinder driving clamp ring schematic diagram of the present invention.
Fig. 4：Fig. 1 A direction views.
Fig. 5：Fig. 1 B direction views.
Fig. 6：End cover of the present invention seals clamp ring structure sectional view when coordinating with cylinder.
Fig. 7：The enlarged diagram of voussoir in Fig. 6.
Fig. 8：Tooth flange of the present invention coordinates enlarged drawing with clamp ring band increment.
Fig. 9：The process chart of the present invention.
Embodiment
Technical scheme is specifically described with reference to embodiments, and present invention is disclosed a kind of horizontal efficient micropore mistake
Filter, with reference to shown in Fig. 1-Fig. 9, including the sleeping cylinder 1 being positioned on track 16 and the sealed end being engaged with the cylinder 1
Lid 10.Specifically, the cylinder 1 is set up on the track by cylinder stent 17, the lower section of cylinder stent 17 is provided with
Idler wheel mechanism 25, the idler wheel mechanism 25 drives cylinder stent 17 to be slided in track 16.The idler wheel mechanism 25 can be used
Manual type roller mechanism, electrodynamic type idler wheel mechanism or other coasting mechanisms.
The end cover 10 is set up in one end of dragging track 16, the support 15 and cylinder stent 17 by support 15
Height quite, and is arranged on same straight line.When cylinder 1 and end cover 10 are in closure state, as shown in Figure 2.
Certainly, cylinder described above can be provided with two, be arranged on the both sides of end cover by track respectively.This hair
In bright specific embodiment by taking a cylinder as an example.
The end cover 10 is connected with the cylinder 1 by the locking of clamp ring 3.Specifically, being provided with the cylinder
Flange 6 with teeth is set on shell flange 2, the end cover 10, the two ends of the clamp ring 3 respectively with shell flange and tooth method
Orchid coordinates.The copper coin 301 for preventing clamp ring from can not rotate is provided between the shell flange 2 and the clamp ring 3, and, institute
State clamp ring inwall and be provided with the ball 302 for being easy to it to rotate, in order to ensure outside the flexibility of ball 302, the clamp ring 3
Wall is provided with the pump nozzle 304 being connected with the ball.Voussoir 303 is provided between the tooth flange 6 and clamp ring 3.For
It is easy to be cross-linked a connecting plate 23 in the opening and closing of clamp ring, the clamp ring and the cylinder, connecting plate staggeredly
Connected between 23 by oil cylinder 22.The oil cylinder 22 is moved, and drives the clamp ring campaign.
The upper end of end cover 10 is provided with drain 7, mouth spray 8 and air inlet 9.The bottom of the end cover is set
It is equipped with a clout mouthful 14.The side of end cover 1, which is provided with one, to be used to convey the charging aperture 24 that material enters filter.
The mouth spray 8 is used to be passed through backwash liquor to filter, to filter inner chamber and filter 5 spray clearly
Wash.The air inlet 9 is used to be passed through filter gas to carry out the control of filter internal pressure, is typically passed through compressed air
Or nitrogen.Accordingly, pressure release can be carried out to filter by drain 7, in order to strengthen at security protection, the drain 7
It is additionally provided with a safety valve.
Laterally it is equipped with the filter on a collector tube 11, the collector tube 11 and is arranged with some filters 5.It is adjacent
The filter be arranged in parallel, in order to ensure to be provided with sealing between the sealing between filter, the adjacent filter 5
Pad 18, and compressed in the end of collector tube 11 by friction top 19.
The other end of the collector tube is extended through for the outer discharging opening 12 for forming cleaner liquid of end cover 10, the liquid collecting
The entrance of pipe 11 and the cleaner liquid passage UNICOM in the filter 5, during filtering, after cleaner liquid is filtered by filter 5, finally
Flowed out by the discharging opening 12 of collector tube 11.The center of filter 5 offers a centre bore, and centered on the centre bore
Scattered to surrounding in divergent shape, some cleaner liquid passages are internally formed in filter.The cleaner liquid passage is in the filter
It is interior to be set in blind hole, and the surface of the filter is capillary microcellular structure.
The lower section of the collector tube 11 is provided with least one auxiliary discharging opening 13, and the present embodiment is to be provided with an auxiliary
Illustrated exemplified by discharging opening 13.The auxiliary discharging opening 13 is arranged at the lower section of the discharging opening 12.Specifically, the liquid collecting
Two sections of liquid collecting subregions are provided with pipe 11, every section of liquid collecting subregion is connected with discharging opening 12 and auxiliary discharging opening 13 respectively.Knot
Close shown in Fig. 2, collector tube is being provided with center liquid collection section close to end cover side, and is arranged at center liquid collection section outer ring
Border liquid collection section, and the center liquid collection section separated with the border liquid collection section by dividing plate, wherein, center liquid collecting portion
Divide and the UNICOM of discharging opening 12, the border liquid collection section and auxiliary discharging opening 13 UNICOM, further, close end cover inner side
Filter 5 cleaner liquid passage and border liquid collection section UNICOM, the filter filtering passage of the other end and the center of collector tube
Liquid collection section UNICOM.Cleaner liquid is last to be flowed out by discharging opening 12 and auxiliary discharging opening 13 respectively.
The purpose of multiple discharging openings is, when carrying out blowback, can carry out blowback to the filter 5 of diverse location respectively,
While so that purge gas is a small amount of, more preferable cleaning performance can be reached.I.e. when to the one of filtering area blowback of filter
During cleaning, another filtering area can be closed, and tolerance is than Liang Ge area's blowback simultaneously cleaning foot during such blowback, and gas is wasted
It is few.
The collector tube 11 is arranged in filter by support frame, and support frame as described above 20 mutually hangs down with the collector tube 11
Straight to set, the cylinder 1, which is provided with, slides light rail 21, and support frame as described above 20 coordinates with the light rail 21 that slides, specifically, described
Slided described in the two ends insertion of support frame in light rail, when end cover 10 and 1 relative motion of cylinder, the two ends of support frame as described above
Motion in light rail 21 is slided described.
For a further understanding of the operation principle of the present invention, its filtering process is described in detail below：
S1, feed step：
After confirming that all valves are closed, charging aperture 24, discharging opening 12, auxiliary discharging opening 13, drain 7 are opened respectively, starts thing
Material conveying pump 28, under normal circumstances drain 7 have gentle breeze blowout, when feed liquid liquid level reach liquid level LT1 after close drain 7, slightly
Cleaner liquid is flowed out from discharging opening 12 and auxiliary discharging opening 13 afterwards, and the filter 5 of micropore is filtered to material.Filtering starts pressure
General control slowly transits to normal filtration state after 0.01Mpa, 10-15 minutes.
S2, filtration step：
Strict control feed pressure, generally 0.2-0.25Mpa, hypertonia is easily caused serious to the pore of filter 5
Block, cause regeneration difficult, influence service life.When filtering rate drops to certain value or treat that the material in batch can 27 is complete
After portion is transported in filter, material-handling pump 28 is closed, filtering terminates, stops charging.
S3, just blow step：
Close charging aperture 24, open air inlet 9, constantly toward be passed through in filter depressurized through decompressor 29 after 0.1-
0.25Mpa low-pressure gas, continues to filter.This step referred to as just blows step；After material liquid surface reaches liquid level LT2, due to liquid
Position declines, and short circuit occurs for gas, and discharging opening 12 and auxiliary discharging opening 13 occur a large amount of venting events, now just blowing step knot
Beam, into next step feed back step.
S4, feed back step：
Discharging opening 12 and auxiliary discharging opening 13 are closed, the clout mouthful 14 of end cover bottom is opened, by the remaining material in filter
Liquid is returned toward in head tank 27.
S5, slag dumping step：
After remaining feed liquid is all discharged in filter, air inlet 9 and clout mouthful 14 are closed, drain 7 is opened, it is ensured that filter
Interior pressure is after zero, then drives clamp ring 3 to turn an angle by the power of oil cylinder 22, makes clamp ring 3 and tooth flange 6 complete
It is complete to disengage, then by cylinder slide idler wheel mechanism 25 by cylinder 1 be axially removed to filter 5 out of cylinder 1 it is completely out.Then
Blowback valve 30 is opened, 0.4-0.6MPa gases after decompression is reversely passed through from discharging opening 12 and auxiliary discharging opening 13 respectively, makes filter
Cake is disengaged and unloaded with filter 5 and transported.
S6, regeneration step：
1）Physics regenerates（It can be carried out under filter closed state or open mode）
Backwash valve 31 is opened, first a certain amount of backwash liquor, backwash liquor is reversely passed through from discharging opening 12 and auxiliary discharging opening 13 respectively
Flowed out outward by interior from filter 5, shape of such as drenching with rain.Then blowback valve 30 is opened, equally respectively from discharging opening 12 and auxiliary
Help discharging opening 13 to be reversely passed through 0.4-0.6MPa gases after decompression, repeat blowback and backwash operation, can will be blocked in filtering
The particle dregs blowback of the top layer of plate 5 even deeper comes out, and this process claims gas and water mixed regeneration method, can carry out repeatedly（Revival
Fruit is preferably）.
2）Chemical regeneration（Only carried out in filter closed state）
Drain 7 is opened, starts material-handling pump 28, regenerated liquid is inputted in cylinder 1 from charging aperture 24, when liquid level reaches liquid level
After LT1, material-handling pump 28 and charging aperture 24 are closed, allows filter 5 to be soaked more than 24 hours in regenerated liquid, is then shut off putting
Eat dishes without rice or wine 7, open air inlet 9 and bottom clout mouthful 14, toward filter in be passed through the 0.1-0.25Mpa after decompressor 29 is depressurized
Low-pressure gas, regenerated liquid is pushed back into regeneration flow container 26 from bottom clout mouthfuls 14, then carry out physics regeneration.This renovation process only exists
Resistance reaches when physics regeneration there is not after effect or filtered uses after certain value.
The present invention still has a variety of specific embodiments.All skills formed by all use equivalent substitutions or equivalent transformation
Art scheme, all falls within the scope of protection of present invention.
Claims (10)
1. horizontal efficient microporous filter, including the cylinder being placed on track and the end cover being engaged with the cylinder, its
It is characterised by：Laterally it is equipped with the filter on a collector tube, the collector tube and is arranged with some filters, it is adjacent described
Filter is be arranged in parallel, and outermost filter is compressed by friction top, and one end of the collector tube is extended through for sealed end
The outer discharging opening for forming cleaner liquid of lid, the entrance of the collector tube and the cleaner liquid passage UNICOM in the filter.
2. horizontal efficient microporous filter as claimed in claim 1, it is characterised in that：The cylinder is set up by cylinder stent
In on the track, being provided with idler wheel mechanism below the cylinder stent, the idler wheel mechanism drives cylinder stent in orbit
Slide.
3. horizontal efficient microporous filter as claimed in claim 2, it is characterised in that：The end cover is set up by support
In one end of dragging track, the support is highly suitable with cylinder stent, and is arranged on same straight line.
4. horizontal efficient microporous filter as claimed in claim 1, it is characterised in that：Set between the adjacent filter
There is sealing gasket.
5. horizontal efficient microporous filter as claimed in claim 1, it is characterised in that：Be provided with below the collector tube to
Be provided with different liquid collecting subregions in few auxiliary discharging opening, the collector tube, each liquid collecting subregion respectively with discharging opening
With auxiliary discharging opening connection.
6. horizontal efficient microporous filter as claimed in claim 1, it is characterised in that：The collector tube is set by support frame
In in filter, support frame as described above is arranged in a mutually vertical manner with the collector tube, and the cylinder, which is provided with, slides light rail, the support
Frame coordinates with the light rail that slides, and is slided described in the two ends insertion of support frame as described above in light rail.
7. horizontal efficient microporous filter as claimed in claim 1, it is characterised in that：The end cover leads to the cylinder
Cross clamp ring locking connection.
8. horizontal efficient microporous filter as claimed in claim 1, it is characterised in that：The end cover upper end, which is provided with, puts
Eat dishes without rice or wine, mouth spray and air inlet.
9. horizontal efficient microporous filter as claimed in claim 1, it is characterised in that：The bottom of the end cover is provided with
One clout mouthful.
10. horizontal efficient microporous filter as claimed in claim 1, it is characterised in that：The end cover side is provided with
One charging aperture.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710421675.7A CN107149802A (en) | 2017-06-07 | 2017-06-07 | Horizontal efficient microporous filter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710421675.7A CN107149802A (en) | 2017-06-07 | 2017-06-07 | Horizontal efficient microporous filter |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107149802A true CN107149802A (en) | 2017-09-12 |
Family
ID=59794914
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710421675.7A Pending CN107149802A (en) | 2017-06-07 | 2017-06-07 | Horizontal efficient microporous filter |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107149802A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107684769A (en) * | 2017-09-29 | 2018-02-13 | 威孔过滤科技（苏州）有限公司 | Quickly press dry filter and its filter method |
| CN114307328A (en) * | 2021-12-14 | 2022-04-12 | 泰州科聚新材料技术研究院有限公司 | Polymer waste water filtration and purification residue drying device |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2748152Y (en) * | 2004-07-08 | 2005-12-28 | 宜兴市过滤设备厂 | Improved horizontal blade type sulfur liquid filtering machine |
| CN101229459A (en) * | 2007-10-23 | 2008-07-30 | 温州市东瓯微孔过滤有限公司 | Horizontal ultrafine powder filtering, washing and drying press integrated machine |
| CN102416392A (en) * | 2011-11-09 | 2012-04-18 | 吉林大学 | Horizontal type roller granular material washing filter |
| CN206934861U (en) * | 2017-06-07 | 2018-01-30 | 威孔过滤科技（苏州）有限公司 | Horizontal efficient microporous filter |
-
2017
- 2017-06-07 CN CN201710421675.7A patent/CN107149802A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2748152Y (en) * | 2004-07-08 | 2005-12-28 | 宜兴市过滤设备厂 | Improved horizontal blade type sulfur liquid filtering machine |
| CN101229459A (en) * | 2007-10-23 | 2008-07-30 | 温州市东瓯微孔过滤有限公司 | Horizontal ultrafine powder filtering, washing and drying press integrated machine |
| CN102416392A (en) * | 2011-11-09 | 2012-04-18 | 吉林大学 | Horizontal type roller granular material washing filter |
| CN206934861U (en) * | 2017-06-07 | 2018-01-30 | 威孔过滤科技（苏州）有限公司 | Horizontal efficient microporous filter |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107684769A (en) * | 2017-09-29 | 2018-02-13 | 威孔过滤科技（苏州）有限公司 | Quickly press dry filter and its filter method |
| CN114307328A (en) * | 2021-12-14 | 2022-04-12 | 泰州科聚新材料技术研究院有限公司 | Polymer waste water filtration and purification residue drying device |
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