CN107160731B - A kind of pressafiner - Google Patents
A kind of pressafiner Download PDFInfo
- Publication number
- CN107160731B CN107160731B CN201710569207.4A CN201710569207A CN107160731B CN 107160731 B CN107160731 B CN 107160731B CN 201710569207 A CN201710569207 A CN 201710569207A CN 107160731 B CN107160731 B CN 107160731B
- Authority
- CN
- China
- Prior art keywords
- grid slag
- helical element
- filtering device
- grid
- header tank
- 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.)
- Active
Links
- 239000002893 slag Substances 0.000 claims abstract description 51
- 238000001914 filtration Methods 0.000 claims abstract description 28
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 20
- 239000000463 material Substances 0.000 abstract description 9
- 230000018044 dehydration Effects 0.000 abstract description 6
- 238000006297 dehydration reaction Methods 0.000 abstract description 6
- 238000001125 extrusion Methods 0.000 abstract description 6
- 239000010865 sewage Substances 0.000 abstract description 3
- 238000009434 installation Methods 0.000 description 4
- 238000000926 separation method Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005192 partition Methods 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000011038 discontinuous diafiltration by volume reduction Methods 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B30—PRESSES
- B30B—PRESSES IN GENERAL
- B30B9/00—Presses specially adapted for particular purposes
- B30B9/02—Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material
- B30B9/12—Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material using pressing worms or screws co-operating with a permeable casing
- B30B9/14—Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material using pressing worms or screws co-operating with a permeable casing operating with only one screw or worm
-
- 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
- B01D29/56—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 series connection
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B30—PRESSES
- B30B—PRESSES IN GENERAL
- B30B9/00—Presses specially adapted for particular purposes
- B30B9/02—Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material
- B30B9/26—Permeable casings or strainers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B30—PRESSES
- B30B—PRESSES IN GENERAL
- B30B9/00—Presses specially adapted for particular purposes
- B30B9/02—Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material
- B30B9/26—Permeable casings or strainers
- B30B9/262—Permeable casings or strainers means disposed in the casing facilitating the squeezing-out of liquid
Abstract
The invention discloses a kind of pressafiners, including driving device, helical element, header tank and squeezing pipe, the driving device drives the helical element rotation, the squeezing pipe is connected to the stream outlet of the helical element, the header tank is located at the helical element lower end, a feeding and filtering device is connected in the feed inlet of the helical element, the useful discharge filtering device for collecting draining is set in the feeding and filtering device and collects the grid slag filter of deslagging, the drain outlet of the discharge filtering device is connect through a drainpipe with the header tank；The deslagging outlet of the deslagging filter device is connected to the tail end of the helical element through a grid slag pipe.Feed inlet uses feeding and filtering device, the larger material of sewage and part or grid slag can effectively be shunted, delivery pipe bottom screen is avoided because dirt is excessive or excessively cause to block, is conducive to drain, enhances squeezer to the extrusion dehydration ability of material or grid slag.
Description
Technical field
The invention belongs to sewage treatment fields, and in particular to the improvement of height draining pressafiner.
Background technique
Height draining pressafiner is to realize conveying in waste water processes and squeeze integration apparatus, grid sewage-removing machine fishing
The volume reduction after conveying and compacting of grid slag out is conducive to outward transport processing, and cleaning is kept during outward transport.Existing skill
In art, the course of work of height draining pressafiner is to be sent into aqueous more tiny grid interceptor from squeezing machine inlet
Into the delivery pipe equipped with helical blade, it is transported to tail portion, is transported outward after extrusion dehydration from squeezing pipe discharge.
In real work, common high draining pressafiner, which has the following disadvantages, causes practical performance poor, due to grid
It pulls the grid interceptor come out, falls directly into squeezer material receiving port, some grid interceptor volumes are excessive excessive, mutual into strips
Winding etc., be easy to cause the delivery pipe bottom screen eyelet in squeezer to block, and causes draining difficult, influences conveying squeezing effect
Fruit.
Summary of the invention
The present invention is in view of the above problems, provide a kind of screw press that can effectively drain and extrusion dehydration effect is good
Machine.
To solve the above problems, the technical solution adopted by the present invention is that:
A kind of pressafiner, including driving device, helical element, header tank and squeezing pipe, the driving device are driven
The helical element rotation is moved, the squeezing pipe is connected to the stream outlet of the helical element, and the header tank is located at described
Helical element lower end a, it is characterised in that: feeding and filtering device is connected in the feed inlet of the helical element, in the charging
It filters the useful discharge filtering device for collecting draining of setting in device and collects the grid slag filter of deslagging, the trap drainage dress
The drain outlet set is connect through a drainpipe with the header tank；The deslagging of the deslagging filter device is exported through a grid slag Guan Lian
Connect the tail end in the helical element.
The discharge filtering device includes trap drainage net and the water fender positioned at trap drainage side off the net, the drainpipe
It is connected to the water fender outlet.
The trap drainage net is in tilted layout, and inclined angle is 45 °~70 °；The water fender is also in tilted layout, water blocking
The inclined direction of the inclined direction of plate and the trap drainage net is on the contrary, the tilt angle of the water fender is 10 °~20 °.
The deslagging filter device is grid slag filter screen, and the inclined direction of the grid slag filter screen inclines with the trap drainage net
Tilted direction is identical, and the tilt angle of the grid slag filter screen is 45 °~60.
The helical element includes shell and the shaft that shell is arranged in, and helical blade, institute are provided in the shaft
Driving device is stated to connect with the shaft.
A kind of filtering type height of the present invention drains pressafiner, and the helical blade inside delivery pipe is to have axis spiral, outer rim
Spiral bristle is installed, one section of tail portion helical blade does not have bristle, this section is press section, and the helical blade outer diameter of press section is wanted
Helical blade slightly larger than front end with bristle；Feeding and filtering device is installed in feed end, feeding and filtering device upper end is to drain
Strainer is connect by pipeline with header tank；Lower end is grid slag filter screen, is connected by pipeline with delivery pipe tail end press section；
When the grid interceptor containing large quantity of moisture enters filter device, in trap drainage wet end position, part water and material or grid
Slag separation, the water after separation flow directly into header tank by pipeline；Remaining grid interceptor falls into grid slag filter screen, partially compared with
Big material or grid slag separates herein, is directly entered press section by pipeline and carries out extrusion dehydration, using squeezing pipe row
Out；The lesser material in part or grid slag fall into delivery pipe, and driving device drives the helical blade rotation in delivery pipe, by material
Or grid slag is delivered to press section extrusion dehydration, through squeezing pipe discharge.
The utility model has the advantages that compared with prior art, the present invention has the following obvious advantages:
1, feed inlet uses feeding and filtering device, can effectively shunt sewage, reduce the discharge pressure of delivery pipe strainer,
Conveying grid slag ability is enhanced, squeezer extrusion dehydration is conducive to；
2, using feeding and filtering device, the larger material in part or grid slag can be efficiently separated, conveying bottom of the tube is avoided
Strainer is excessive because of dirt or excessively causes to block, and is conducive to drain, enhances extruding of the squeezer to material or grid slag
Water separation capability.
Detailed description of the invention
Fig. 1 is the structural schematic diagram that a kind of filtering type height of the invention drains pressafiner；
Fig. 2 is the structural schematic diagram of feeding and filtering device of the invention；
Wherein:
1, driving device；2, delivery pipe；3, helical element；4, feeding and filtering device；5, squeezing pipe；6, header tank；41, grid
Slag filter screen；42, trap drainage net；43, water fender；44, drainpipe；45, grid slag pipe.
Specific embodiment
With reference to the accompanying drawing, technical solution of the present invention is described in detail:
A kind of filtering type height draining pressafiner of the present invention is mainly driven in delivery pipe 2 by driving device 1
Helical element 3 carries out prepressing to grid interceptor.Delivery pipe 2 is mounted on 6 top of header tank.2 lower half circular portion of delivery pipe is
Aperture is less than the filter opening plate of grid interceptor；Delivery pipe 2 installs feeding and filtering device 4 above；On inside the feeding and filtering device 4
Angled (45 ° to 70 °) installations trap drainage net 42 is held, 42 aperture of trap drainage net accounts for the 2/3 of entire cross section, according to
Practical adjustment；The aperture of trap drainage net is less than grid slag, as the filter opening size in delivery pipe.Below trap drainage net 42
For the water fender 43 of inclination installation (10 ° to 20 °), in the lowest part aperture that water fender 43 is contacted with 4 wooden partition of feeding and filtering device,
Run in water pipe 44, is passed directly into header tank 6；Grid slag filter screen 41 is installed every a distance (50 ~ 200mm) in 43 lower end of water fender,
Angled (45 ° ~ 60 °) installations, the aperture of grid slag filter screen is greater than part grid slag outer diameter, according to the grid slag that actually will appear
Size considers, it can by most of grid slag, and big grid slag will not pass through.In grid slag filter screen 41 and feeding and filtering device 4
The lowest part aperture of wooden partition contact, connects grid slag pipe 45, connect with 2 tail end of delivery pipe；Squeezing pipe 5 is connect with delivery pipe 2.
A kind of filtering type height draining pressafiner of the present invention is in various, the corollary equipment of fine fack, mainly
Grid interceptor is washed, squeezed, is dehydrated, realizes the minimizing of grid slag, is convenient for subsequent transportation and processing.Such as Fig. 1 and Fig. 2 institute
Show, grid interceptor initially enters feeding and filtering device 4, and partial grid interceptor isolates grid slag and water in trap drainage net 42
Point, the moisture after separation is blocked by water fender 43 into drainpipe 44, flows into header tank 6；Another part grid interceptor and
The grid slag isolated, continues to fall, and falls into grid slag filter screen 41, and since grid slag filter screen 41 is inclination installation, grid slag is downward
When movement, the grid slag of partial volume hyperfiltration mesh diameter does not pass through strainer, and enters grid slag pipe 45, reaches 2 tail of delivery pipe
End carries out prepressing.And partial volume be less than 41 aperture of filter screen of grid slag filter screen grid slag then with moisture together, fall into delivery pipe 2
It is interior, driving device 1 drive helical element 3 act under, in delivery pipe 2 carry out prepressing remove large quantity of moisture, moisture by
The filter opening of 2 lower half circle of delivery pipe discharges into header tank 6.Grid slag after prepressing enters squeezing pipe 5, in uphill process, through gravity
Under the double action of tube wall frictional force, it is dehydrated and is discharged by twice pressing, and filter opening of the moisture through 2 lower half circle of delivery pipe of abjection
Header tank 6 is discharged into, then is discharged by the drainage hole of 6 bottom of header tank.
Claims (5)
1. a kind of pressafiner, including driving device, helical element, header tank and squeezing pipe, the driving device driving
The helical element rotation, the squeezing pipe are connected to the stream outlet of the helical element, and the header tank is located at the spiral shell
Revolve lower, it is characterised in that: a feeding and filtering device is connected in the feed inlet of the helical element, in the fed filtration
It is provided with the discharge filtering device for collecting draining in device and collects the grid slag filter of deslagging, the trap drainage dress
The drain outlet set is connect through a drainpipe with the header tank；The deslagging of the grid slag filter is exported through a grid slag Guan Lian
Connect the tail end in the helical element；The aperture of discharge filtering device is less than grid slag, and the aperture of grid slag filter is greater than part
Grid slag outer diameter.
2. pressafiner according to claim 1, it is characterised in that: the discharge filtering device includes trap drainage net
And the water fender positioned at trap drainage side off the net, the drainpipe are connected to the water fender outlet.
3. pressafiner according to claim 2, it is characterised in that: the trap drainage net is in tilted layout, inclined
Angle is 45 °~70 °；The water fender is also in tilted layout, the inclination side of the inclined direction of water fender and the trap drainage net
To on the contrary, the tilt angle of the water fender is 10 °~20 °.
4. pressafiner according to claim 3, it is characterised in that: the grid slag filter is grid slag filter screen,
The inclined direction of the grid slag filter screen is identical as the trap drainage net inclined direction, and the tilt angle of the grid slag filter screen is
45 °~60 °.
5. pressafiner according to claim 1 to 4, it is characterised in that: the helical element includes shell and sets
The shaft in shell is set, helical blade is provided in the shaft, the driving device is connect with the shaft.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710569207.4A CN107160731B (en) | 2017-07-12 | 2017-07-12 | A kind of pressafiner |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710569207.4A CN107160731B (en) | 2017-07-12 | 2017-07-12 | A kind of pressafiner |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN107160731A CN107160731A (en) | 2017-09-15 |
| CN107160731B true CN107160731B (en) | 2019-05-31 |
Family
ID=59818401
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710569207.4A Active CN107160731B (en) | 2017-07-12 | 2017-07-12 | A kind of pressafiner |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107160731B (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110368725A (en) * | 2019-08-13 | 2019-10-25 | 彭素荣 | A kind of sewage treatment preamble solid filter device |
| CN110526541A (en) * | 2019-08-26 | 2019-12-03 | 南京爱斯利尔环保设备工程有限公司 | A kind of pressafiner |
| CN113103646B (en) * | 2021-04-30 | 2022-12-13 | 河南应用技术职业学院 | Chinese herbal medicine active ingredient extraction element |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH06292997A (en) * | 1993-04-09 | 1994-10-21 | Hitachi Zosen Corp | Screw type dehydrater |
| CN102358057A (en) * | 2011-11-04 | 2012-02-22 | 天津百利阳光环保设备有限公司 | Pressofiner |
| CN203922961U (en) * | 2014-05-14 | 2014-11-05 | 北京泰昌科睿环保科技有限公司 | A kind of expeller |
| CN106014307A (en) * | 2016-07-28 | 2016-10-12 | 成都高普石油工程技术有限公司 | Method for removing solid-phase particles in drilling fluid |
| CN106273620A (en) * | 2015-05-15 | 2017-01-04 | 苏州欧复能新材料科技有限公司 | Plastic sheeting particle dehydration squeezer |
| CN206124280U (en) * | 2016-08-31 | 2017-04-26 | 北京科林之星环保技术有限公司 | Screw press |
| CN206122120U (en) * | 2016-08-30 | 2017-04-26 | 浙江三联环保科技股份有限公司 | Large granule impurity subsides filter |
-
2017
- 2017-07-12 CN CN201710569207.4A patent/CN107160731B/en active Active
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH06292997A (en) * | 1993-04-09 | 1994-10-21 | Hitachi Zosen Corp | Screw type dehydrater |
| CN102358057A (en) * | 2011-11-04 | 2012-02-22 | 天津百利阳光环保设备有限公司 | Pressofiner |
| CN203922961U (en) * | 2014-05-14 | 2014-11-05 | 北京泰昌科睿环保科技有限公司 | A kind of expeller |
| CN106273620A (en) * | 2015-05-15 | 2017-01-04 | 苏州欧复能新材料科技有限公司 | Plastic sheeting particle dehydration squeezer |
| CN106014307A (en) * | 2016-07-28 | 2016-10-12 | 成都高普石油工程技术有限公司 | Method for removing solid-phase particles in drilling fluid |
| CN206122120U (en) * | 2016-08-30 | 2017-04-26 | 浙江三联环保科技股份有限公司 | Large granule impurity subsides filter |
| CN206124280U (en) * | 2016-08-31 | 2017-04-26 | 北京科林之星环保技术有限公司 | Screw press |
Also Published As
| Publication number | Publication date |
|---|---|
| CN107160731A (en) | 2017-09-15 |
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| Date | Code | Title | Description |
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| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| CB03 | Change of inventor or designer information | ||
| CB03 | Change of inventor or designer information |
Inventor after: Li Zongfeng Inventor after: Yu Bihui Inventor before: Li Zongfeng Inventor before: Chen Bin Inventor before: Zhang Hua Inventor before: Yang Rongqun Inventor before: Weng Chunxian Inventor before: Liu Xiaojuan Inventor before: Sun Kai Inventor before: Pan Jun Inventor before: Shen Dengwu |
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| CB03 | Change of inventor or designer information | ||
| CB03 | Change of inventor or designer information |
Inventor after: Li Zongfeng Inventor after: Chen Bin Inventor after: Yu Bihui Inventor before: Li Zongfeng Inventor before: Yu Bihui |
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| GR01 | Patent grant | ||
| GR01 | Patent grant |