CN106621508B - A kind of filter device - Google Patents
A kind of filter device Download PDFInfo
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- CN106621508B CN106621508B CN201611152978.5A CN201611152978A CN106621508B CN 106621508 B CN106621508 B CN 106621508B CN 201611152978 A CN201611152978 A CN 201611152978A CN 106621508 B CN106621508 B CN 106621508B
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- China
- Prior art keywords
- filter
- warehouse
- filter plate
- storehouse
- point
- 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.)
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- 239000000463 material Substances 0.000 claims abstract description 38
- 238000001914 filtration Methods 0.000 claims abstract description 31
- 239000011148 porous material Substances 0.000 claims description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 11
- 238000003756 stirring Methods 0.000 claims description 7
- 240000007594 Oryza sativa Species 0.000 claims 1
- 235000007164 Oryza sativa Nutrition 0.000 claims 1
- 235000009566 rice Nutrition 0.000 claims 1
- 230000000903 blocking effect Effects 0.000 abstract description 8
- 230000000694 effects Effects 0.000 abstract 1
- 230000005484 gravity Effects 0.000 abstract 1
- 239000000126 substance Substances 0.000 description 11
- 239000002245 particle Substances 0.000 description 9
- 239000000571 coke Substances 0.000 description 4
- 239000013618 particulate matter Substances 0.000 description 3
- 230000018044 dehydration Effects 0.000 description 2
- 238000006297 dehydration reaction Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000003610 charcoal Substances 0.000 description 1
- 238000004939 coking Methods 0.000 description 1
- 230000005574 cross-species transmission Effects 0.000 description 1
- 238000005235 decoking Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000003111 delayed effect Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000000750 progressive effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 239000011343 solid material Substances 0.000 description 1
- 238000003860 storage Methods 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
- B01D29/01—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 flat filtering elements
- B01D29/03—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 flat filtering elements self-supporting
-
- 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
-
- 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
- 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
- B01D29/76—Handling the filter cake in the filter for purposes other than for regenerating
- B01D29/86—Retarding cake deposition on the filter during the filtration period, e.g. using stirrers
-
- 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
- B01D29/94—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 the filter cake, e.g. chutes
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Treatment Of Sludge (AREA)
- Filtration Of Liquid (AREA)
Abstract
The invention discloses a kind of filter devices, including filtering cabin and feed pipe, the first filter plate for the filtering cabin to be successively separated into the first warehouse and the second warehouse along the vertical direction is provided in the filtering cabin, the filtering direction of first filter plate is upward, the discharge port of the feed pipe is connected to second warehouse, outlet is respectively arranged in first warehouse and second warehouse, the outlet of second warehouse is provided with switch valve.In the filter device, because the first filter plate is inverted, filter from bottom to up, moisture most in material can be effectively set to filter out, to complete filtering, again because the first filter plate is inverted, major diameter material can stay in the downside of the first filter plate, and major diameter material not will cause the blocking of the first filter plate then at this time under the effect of gravity.So the filter device can efficiently solve the problem of filter device is easy blocking.
Description
Technical field
The present invention relates to material processing technology fields, more specifically to a kind of filter device.
Background technique
The coke that delayed coking generates, after hydraulic decoking device clear, the burnt aqueous mixtures of discharge are dehydrated
Filtration treatment.The filter device general structure of existing domestic enterprise's production is complicated, and standardization interchangeability is poor, with low content of technology, solid-liquid
The defects of separation is not thorough, and is easily blocked, is difficult to meet the requirement of coke filtration.
It is that current those skilled in the art are anxious in conclusion how to efficiently solve the problem of filter device is easy blocking
Problem to be solved.
Summary of the invention
In view of this, the filter device can efficiently solve the purpose of the present invention is to provide a kind of filter device
Filter the problem of device is easy blocking.
In order to achieve the above object, the invention provides the following technical scheme:
A kind of filter device, including filtering cabin and feed pipe are provided in the filtering cabin for by the filtering cabin edge
Up and down direction is successively separated into the first filter plate of the first warehouse and the second warehouse, the filtering direction court of first filter plate
On, the discharge port of the feed pipe is connected to second warehouse, is respectively set in first warehouse and second warehouse
There is outlet, the outlet of second warehouse is provided with switch valve.
Preferably, the second mistake that pore size filter is greater than first filter plate aperture is provided in second warehouse
Filter plate, second warehouse is successively separated into first point of storehouse and second point of storehouse by second filter plate along the vertical direction, described
Upward, and the discharge port of the feed pipe is connected to the filtering direction of second filter plate with second point of storehouse.
Preferably, it is provided with filter hole on the pipeline section portion side wall being located in first point of storehouse on the feed pipe, it is described
The aperture of filter hole is greater than the pore size filter of first filter plate and is not more than the pore size filter of second filter plate.
Preferably, it is provided in second point of storehouse for by the uniform agitating device of material stirring.
Preferably, the agitating device includes impeller and the motor for driving wheel rotation.
Preferably, from top to bottom at gradual shrinkage, the bottom in second point of storehouse is provided with outlet in second point of storehouse.
Preferably, the outlet of first warehouse is connected with water pump, and the outlet in second point of storehouse is provided with slurry
Pump.
Preferably, the pore size filter of first filter plate is between 2.5 millimeters to 3.5 millimeters, second filter plate
Pore size filter between 5.5 millimeters to 6.5 millimeters.
A kind of filter device provided by the invention, the coke brushed down that is mainly used for liquidating are filtered dehydration.Specifically
The filter device includes filtering cabin and feed pipe.The first filter plate is wherein provided in filtering cabin, the first filter plate is used for mistake
Filter position is separated into the first warehouse and the second warehouse along the vertical direction.Wherein the filtering direction of the first filter plate is upward, i.e., to be filtered
Substance from the downside of the first filter plate, up flow by side.Wherein the discharge port of feed pipe is connected to the second warehouse, and material is straight
It connects and is transferred in the second warehouse.Wherein the first warehouse and the second warehouse are respectively arranged with outlet, wherein passing through the first warehouse
Outlet finely ground particle substance and water can be discharged.And the wherein outlet of the second warehouse, it can be by mistake non-in the second warehouse
The material discharge filtered out, and it is provided with switch valve.
According to above-mentioned technical solution, it is recognised that passing through feed pipe for object by Pulp pump in the application filter device
Material is delivered in the second warehouse, and switch valve is closed in the second warehouse at this time, and material can be built up, under pressure, small
Grain substance and water can be flowed up from the filter hole of the first filter plate, be entered in the first warehouse, and from the row of the first warehouse
Outlet discharge.And when being filled into certain, the switch valve of the second warehouse is opened at this time, is arranged by the outlet of the second warehouse
Out.It in the filter device, because the first filter plate is inverted, i.e., filters, can effectively make big absolutely in material from bottom to up
Partial moisture filters out, and to complete to filter, and because the first filter plate is inverted, major diameter material can stay in the first filter plate
Downside, and major diameter material not will cause the blocking of the first filter plate then at this time.So the filter device can efficiently solve filtering
Device is easy the problem of blocking.
Detailed description of the invention
In order to more clearly explain the embodiment of the invention or the technical proposal in the existing technology, to embodiment or will show below
There is attached drawing needed in technical description to be briefly described, it should be apparent that, the accompanying drawings in the following description is only this
Some embodiments of invention for those of ordinary skill in the art without creative efforts, can be with
It obtains other drawings based on these drawings.
Fig. 1 is the perspective structure schematic diagram of filter device provided in an embodiment of the present invention.
It is marked in attached drawing as follows:
Feed pipe 1, the first warehouse 2,3, first points of the first filter plate, 4, second points of storehouse storehouse 5, the second filter plate 6, stirring dress
Set 7.
Specific embodiment
The embodiment of the invention discloses a kind of filter devices, to efficiently solve the problem of filter device is easy blocking.
Following will be combined with the drawings in the embodiments of the present invention, and technical solution in the embodiment of the present invention carries out clear, complete
Site preparation description, it is clear that described embodiments are only a part of the embodiments of the present invention, instead of all the embodiments.It is based on
Embodiment in the present invention, it is obtained by those of ordinary skill in the art without making creative efforts every other
Embodiment shall fall within the protection scope of the present invention.
Referring to Fig. 1, Fig. 1 is the perspective structure schematic diagram of filter device provided in an embodiment of the present invention.
In a specific embodiment, a kind of filter device is present embodiments provided, be mainly used for liquidating the coke brushed down
Charcoal is filtered dehydration.The specific filter device includes filtering cabin and feed pipe 1.
The first filter plate 3 is wherein provided in filtering cabin, the first filter plate 3 is for filtering cabin to be separated into along the vertical direction
First warehouse 2 and the second warehouse, that is, the warehouse for being located at 3 upside of the first filter plate is the first warehouse 2, and is located at the first filter plate 3
The warehouse of downside is the second warehouse.
Wherein upward, i.e., substance to be filtered is from the downside of the first filter plate 3 up effluent for the filtering direction of the first filter plate 3
Dynamic, small particle substance passes through the filter hole of the first filter plate 3, and large particulate matter can not then pass through filter hole, stay in the first mistake
The downside of filter plate 3.Specifically, can make the pore size filter of the first filter plate 3 between 2.5 millimeters to 3.5 millimeters, and preferably exist
3 millimeters, so that filtered material is used directly for washing away furnace roof again.Wherein pore size filter refer to allowing by object
The partial size of maximum particle diameter material in material.
Wherein the discharge port of feed pipe 1 is connected to the second warehouse, and material is transferred directly in the second warehouse, i.e., will be high
Pressure material is transferred to the second warehouse, until the second warehouse spill-over, under high-pressure, small particle substance and water can pass through first
Filter plate 3, large particulate matter can rest on the downside of the first filter plate 3 at this time.
Wherein the first warehouse 2 and the second warehouse are respectively arranged with outlet, wherein pass through the outlet of the first warehouse 2, it can
Finely ground particle substance and water to be discharged.And the wherein outlet of the second warehouse, it will can not be filtered away in the second warehouse
Material discharge.It should be noted that wherein the outlet of the second warehouse should be provided with switch valve.With filtering when, by second
Switch valve at the outlet of warehouse is closed, and is discharged to avoid finely ground particle substance and water from the outlet of the second warehouse, and not
When filtering, the switch valve of the second warehouse is opened, so that the large particulate matter left can be discharged from the outlet.
In the present embodiment, in the application filter device, material is delivered to by the second storehouse by feed pipe 1 by Pulp pump
Interior, switch valve is closed in the second warehouse at this time, and material can build up, under pressure, finely ground particle substance and water meeting
It flows up, is entered in the first warehouse 2 from the filter hole of the first filter plate 3, and be discharged from the outlet of the first warehouse 2.And
When being filled into certain, the switch valve of the second warehouse is opened at this time, is discharged by the outlet of the second warehouse.In the filtering
It in device, because the first filter plate 3 is inverted, i.e., filters from bottom to up, can effectively make moisture most in material
It filters out, to complete to filter, and because the first filter plate 3 is inverted, major diameter material can stay in the downside of the first filter plate 3, and
Major diameter material not will cause the blocking of the first filter plate 3 then at this time.So the filter device can efficiently solve filter device appearance
Susceptible to plugging problem.
Further, can make to be provided with pore size filter is greater than 3 pore size filter of the first filter plate second in the second warehouse
Filter plate 6, for the second warehouse to be separated into first point of storehouse 4 and second point of storehouse 5 along the vertical direction, to be i.e. located in the second warehouse
The warehouse of second filter plate, 6 upside is first point of storehouse 4, and the warehouse positioned at 6 downside of the second filter plate is the second warehouse.And this
The filtering direction of two filter plates 6 upward, i.e., filters from the bottom to top, and the discharge port of feed pipe 1 is connected to second point of storehouse 5 at this time.It needs
It is noted that second point of storehouse 5 should be provided with outlet, the outlet of the first warehouse 2 can specifically be arranged second
Divide Cang5Chu.It by the second filter plate 6, can effectively alleviate 3 filter pressure of the first filter plate, accelerate filtering.It needs to illustrate
It is that, wherein outlet can be separately provided in first point of storehouse 4, can also be discharged by the way that the outlet of second point of Cang5Chu is arranged in.But
It is when the substance for needing separately storage in first point of storehouse 4 and second point of storehouse 5, when can produce material by on-off valve control
Between, material in first point of storehouse 4 and second point of storehouse 5 is released in batches.Wherein the pore size filter of the second filter plate 6 can be 5.5
Millimeter is between 6.5 millimeters, and preferably 6 millimeters.
Further, the pipeline section portion in first point of storehouse 4 can be located on feed pipe 1, to setting on the side wall of the tube end
It is equipped with filter hole, and so that the aperture of the filter hole is greater than the pore size filter of the first filter plate 3, and the second filter plate 6 should be not more than
Pore size filter.So that part finely ground particle substance and water, flow out in advance from the filter hole of feed pipe 1, can then substantially reduce
The filter pressure of second filter plate 6.Filter hole aperture is equal with the pore size filter of the second filter plate 6 on the specific feed pipe 1,
The filter pressure of the second filter plate 6 is reduced with maximum dynamics.
In view of that under 1 material pressure of feed pipe, big partial size material can be made gradually to tire out pressure when being filtered, can make big
Partial size material is gradually compacted, and is unfavorable for material and is discharged from outlet, be based on this, can be provided in second point of storehouse 5 for inciting somebody to action
The uniform agitating device 7 of material stirring.Specifically, stirring rod can be used, in order to guarantee to stir evenly, preferred stirring is filled herein
Setting 7 includes impeller and the motor for driving wheel rotation, and it is loose again can be conducive to solid material for impeller laminated structure.
Further, it can make second point of storehouse 5 from top to bottom in gradual shrinkage, and be provided in the bottom in second point of storehouse 5
Outlet.Herein it is tapered should be it is continuous tapered, so that material collapses to outlet, be discharged with facilitating from outlet, specifically
Space in second point of storehouse, 5 storehouse can be made triangular in shape.Further material for convenience is discharged from outlet, can be second
The outlet in point storehouse 5 is provided with Pulp pump, big partial size material remaining after filtering can be discharged, it should be noted that be
Facilitate discharge, should make to reserve certain moisture in the material of discharge.And in view of the material particular diameter in the first warehouse 2 compares
It is small, and then it can be connected with water pump in the outlet of the first warehouse 2, to facilitate water and the discharge of small particle material.
Each embodiment in this specification is described in a progressive manner, the highlights of each of the examples are with other
The difference of embodiment, the same or similar parts in each embodiment may refer to each other.
The foregoing description of the disclosed embodiments enables those skilled in the art to implement or use the present invention.
Various modifications to these embodiments will be readily apparent to those skilled in the art, as defined herein
General Principle can be realized in other embodiments without departing from the spirit or scope of the present invention.Therefore, of the invention
It is not intended to be limited to the embodiments shown herein, and is to fit to and the principles and novel features disclosed herein phase one
The widest scope of cause.
Claims (6)
1. a kind of filter device, including filtering cabin and feed pipe, be provided in the filtering cabin for by the filtering cabin along
Lower direction is successively separated into the first filter plate of the first warehouse and the second warehouse, which is characterized in that the mistake of first filter plate
Filter direction upward, the discharge port of the feed pipe is connected to second warehouse, in first warehouse and second warehouse
It is respectively arranged with outlet, the outlet of second warehouse is provided with switch valve；Filter hole is provided in second warehouse
Diameter is greater than second filter plate in first filter plate aperture, and second filter plate is vertically square by second warehouse
To being successively separated into first point of storehouse and second point of storehouse, upward, and the feed pipe goes out the filtering direction of second filter plate
Material mouth is connected to second point of storehouse；Filtering is provided on the pipeline section portion side wall being located in first point of storehouse on the feed pipe
Hole, the aperture of the filter hole are greater than the pore size filter of first filter plate and are not more than the filter hole of second filter plate
Diameter.
2. filter device according to claim 1, which is characterized in that be provided in second point of storehouse for stirring material
Mix uniform agitating device.
3. filter device according to claim 2, which is characterized in that the agitating device includes impeller and for driving leaf
Take turns the motor of rotation.
4. filter device according to claim 3, which is characterized in that second point of storehouse is from top to bottom at gradual shrinkage, institute
The bottom for stating second point of storehouse is provided with outlet.
5. filter device according to claim 4, which is characterized in that the outlet of first warehouse is connected with water pump,
The outlet in second point of storehouse is provided with Pulp pump.
6. filter device according to claim 5, which is characterized in that the pore size filter of first filter plate is in 2.5 millis
Rice is between 3.5 millimeters, and the pore size filter of second filter plate is between 5.5 millimeters to 6.5 millimeters.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611152978.5A CN106621508B (en) | 2016-12-14 | 2016-12-14 | A kind of filter device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611152978.5A CN106621508B (en) | 2016-12-14 | 2016-12-14 | A kind of filter device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN106621508A CN106621508A (en) | 2017-05-10 |
| CN106621508B true CN106621508B (en) | 2019-09-27 |
Family
ID=58822506
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201611152978.5A Active CN106621508B (en) | 2016-12-14 | 2016-12-14 | A kind of filter device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106621508B (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109107250A (en) * | 2018-10-09 | 2019-01-01 | 辽宁工程技术大学 | A kind of device and method of river load water and soil separation |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4125469A (en) * | 1977-06-15 | 1978-11-14 | Emerson Electric Co. | Bi-directional filter drier |
| CN2315116Y (en) * | 1997-12-12 | 1999-04-21 | 张汉棕 | Water purifier |
| CN2440063Y (en) * | 2000-09-04 | 2001-07-25 | 北京科大环保技术研究所 | Farm water-purifying tank |
| CN201850186U (en) * | 2010-11-05 | 2011-06-01 | 重庆创隆科技有限公司 | High-precision integrated water purifier |
| CN203458905U (en) * | 2013-08-23 | 2014-03-05 | 绿地环保科技股份有限公司 | Combined filtering pond |
| CN206381707U (en) * | 2016-12-14 | 2017-08-08 | 湖南万通科技股份有限公司 | A kind of filter |
-
2016
- 2016-12-14 CN CN201611152978.5A patent/CN106621508B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4125469A (en) * | 1977-06-15 | 1978-11-14 | Emerson Electric Co. | Bi-directional filter drier |
| CN2315116Y (en) * | 1997-12-12 | 1999-04-21 | 张汉棕 | Water purifier |
| CN2440063Y (en) * | 2000-09-04 | 2001-07-25 | 北京科大环保技术研究所 | Farm water-purifying tank |
| CN201850186U (en) * | 2010-11-05 | 2011-06-01 | 重庆创隆科技有限公司 | High-precision integrated water purifier |
| CN203458905U (en) * | 2013-08-23 | 2014-03-05 | 绿地环保科技股份有限公司 | Combined filtering pond |
| CN206381707U (en) * | 2016-12-14 | 2017-08-08 | 湖南万通科技股份有限公司 | A kind of filter |
Also Published As
| Publication number | Publication date |
|---|---|
| CN106621508A (en) | 2017-05-10 |
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Denomination of invention: A filtering device Effective date of registration: 20220524 Granted publication date: 20190927 Pledgee: Hunan Xingsha Rural Commercial Bank Co.,Ltd. quantang sub branch Pledgor: HUNAN WANTONG TECHNOLOGY Co.,Ltd. Registration number: Y2022980005184 |