CN102309876A - Improvement for dynamic filtration squeezing dewatering machine - Google Patents
Improvement for dynamic filtration squeezing dewatering machine Download PDFInfo
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- CN102309876A CN102309876A CN201110250075A CN201110250075A CN102309876A CN 102309876 A CN102309876 A CN 102309876A CN 201110250075 A CN201110250075 A CN 201110250075A CN 201110250075 A CN201110250075 A CN 201110250075A CN 102309876 A CN102309876 A CN 102309876A
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Abstract
The invention discloses an improvement for dynamic filtration squeezing dewatering machine, which comprises a filtration unit, each filtration unit comprises two parallel filter plates, an elastic press box composed of elasticity and a filter frame is provided between the two filter plates and is adjacent to the out edges part of filter plates, the elasticity and the filter plates are fixed, a sealing ring is provided between an inner side of the filter frame and the filter plates, the filter frame, the sealing ring and two filter plates forms a filtration chamber. According to the invention, the elasticity is clamped between the prominence and the filter plates, the sealing ring is provided between the inner side of the filter frame and the filter plates, the filter frame, the sealing ring and two filter plates forms a filtration chamber, so that a dynamic filtration squeezing dewatering machine structure can be simplified, and the production cost can be relatively reduced, the service life is longer and the efficiency is higher.
Description
Technical field
The present invention relates to filter press.
Background technology
Existing sludge dewatering; American-European and Japan country mostly adopts vacuum belt press filtering machine, horizontal screw centrifuge and diaphragm pressing filter press mostly with China, and will carry out flocculation agent to mud according to sludge nature and handle and add filter aid and mud is carried out the reunion and the modification of fine particle.The reduction of the filter residue water capacity after the filtration mainly relies on flocculation agent in the effect of filtering the period, and the ratio of interpolation filter aid relies on.Through the vacuum belt press filtering machine; The mud that horizontal screw centrifuge is handled, water capacity is general many about 80%, and the mud water capacity of handling through the diaphragm pressing filter press is many about 60～75%; The addition of filter aid increases; The rate of filtration is accelerated, and the water capacity of filter residue descends, and the pressure of diaphragm pressing is mostly at 1.5～1.6Mpa/CM
2Use actual conditions from the technology and the equipment of existing sludge dewatering, the vacuum belt press filtering machine, the horizontal screw centrifuge automaticity is high, but the filter residue water capacity is high, can not reach the requirement of national environmental protection department regulation.The diaphragm pressing filter press is because the structure of filter plate and the restriction of material, and the obstacle that existence can't be gone beyond aspect heat resisting and pressure resisting etc. is analyzed from filtration theory; The diaphragm pressing filter press is the cake layer work principle of filter; Along with the prolongation of filtration time, filter cake thickens, and the filter cake resistivity increases; Filtering velocity descends, and filtration time is long.And membrane filter plate is made complicated, complex operation, and service life is not long, and it is high to change price, also needs water, the gas energy, and pipeline increases supporting, increases operation and expends.
Summary of the invention
Technical problem to be solved by this invention just provides a kind of dynamic filtration squeezing dewatering machine, and is simple in structure, long service life, and efficient is high.
For solving the problems of the technologies described above, the present invention adopts following technical scheme: the dynamic filtration squeezing dewatering machine improves, and comprises at least one filter element; Each filter element comprises two parallel filter plates; Be provided with the elasticity squeeze frame of being made up of elastomer and filter frame in abutting connection with filter plate outward flange position between two filter plates, it is characterized in that: said filter frame evenly is provided with at least two protuberances on the outer ring, and elastomer is corresponding with the protuberance position; Said elastomer cramping is between said protuberance and said filter plate; And elastomer and said filter plate are fixed, and are provided with sealing ring between said filter frame inboard and said filter plate, and filter frame, sealing ring and two filters surround filter chamber.
As preferably, said filter frame is the thin structure of protuberance for framework is thick, and a circle thin wing is established at said filter plate edge, and filter plate edge thin wing thickness is less than interior thickness, and filter frame is located between the filter plate thin wing.
As preferably, said sealing ring is fixed on the filter plate, and wherein the sealing ring outside is provided with the sealing lip that extends to filter frame, and said sealing lip is fastened on the corner, said filter frame bottom.Sealing effectiveness is better.
As preferably, said sealing ring inboard is provided with convexity, and the binding face of said filter plate and said sealing ring is provided with draw-in groove, said convexity be connected in realize in the said draw-in groove fixing.It is more firm to install.
As preferably, said filter plate is square, and filter frame is circular, and said protuberance is provided with four, and said protuberance stretches to four angles of said filter plate.Both had better elastic, stability of structure when guaranteeing squeezing again.
As preferably, said elastomer is a cylinder, and said elastomer center is provided with a centre bore, and said filter plate is provided with reference column, and said elastomer is plugged on the said reference column through centre bore.Make the elastomer fixed-site.
As preferably, said filter plate is provided with inflatable mouth, the liquid outlet that leads to filter chamber, and said inflatable mouth is located at middle side part on the said filter plate, and said liquid outlet is positioned at middle side part under the said filter plate.
As preferably; Said filter chamber is provided with two charging apertures; Wherein first charging aperture is located at the protuberance downside of filter frame left side top, and second charging aperture is located at the protuberance upside of below, filter frame right side, and said charging aperture and said inflatable mouth are vertical with line between liquid outlet.The shearing force that slurry high flow velocities is into produced.
The present invention with the elastomer cramping between said protuberance and said filter plate; And between filter frame inboard and said filter plate, be provided with sealing ring; Filter frame, sealing ring and two filters surround filter chamber, have simplified the structure of dynamic filtration squeezing dewatering machine like this, the corresponding cost of manufacture that reduced; And longer service life, efficient is higher.
Description of drawings
Below in conjunction with the accompanying drawing and the specific embodiment the present invention is further described:
Fig. 1 is a structural representation of the present invention;
Fig. 2 is an A-A cutaway view among Fig. 1.
The specific embodiment
The improved embodiment 1 of explanation dynamic filtration squeezing dewatering machine of the present invention sees figures.1.and.2; Comprise at least one filter element, each filter element comprises between 1, two filter plate of two parallel filter plates the elasticity squeeze frame of being made up of elastomer 2 and filter frame 3 being provided with in abutting connection with filter plate outward flange position; Said filter frame evenly is provided with at least two protuberances 31 on the outer ring; Elastomer is corresponding with the protuberance position, and said elastomer cramping is between said protuberance and said filter plate, and elastomer and said filter plate are fixed; Be provided with sealing ring 4 between said filter frame inboard and said filter plate, filter frame, sealing ring and two filters surround filter chamber.Said filter frame is the thin structure of protuberance for framework is thick, and a circle thin wing 11 is established at said filter plate edge, and filter plate edge thin wing thickness is less than interior thickness, and filter frame is located between the filter plate thin wing.Said sealing ring is fixed on the filter plate, and wherein the sealing ring outside is provided with the sealing lip 41 that extends to filter frame, and said sealing lip is fastened on the corner, said filter frame bottom.Said sealing ring 4 inboards are provided with convexity 42, and the binding face of said filter plate and said sealing ring is provided with draw-in groove, and said convexity is connected in and realizes in the said draw-in groove fixing.Said filter plate is square, and filter frame is circular, and said protuberance is provided with four, and said protuberance stretches to four angles of said filter plate.Said elastomer is a cylinder, and said elastomer center is provided with a centre bore, and said filter plate is provided with reference column, and said elastomer is plugged on the said reference column through centre bore.Said filter plate is provided with inflatable mouth 7, the liquid outlet 8 that leads to filter chamber, and said inflatable mouth is located at middle side part on the said filter plate, and said liquid outlet is positioned at middle side part under the said filter plate.Said filter chamber is provided with two charging apertures 6, and wherein first charging aperture is located at the protuberance downside of filter frame left side top, and second charging aperture is located at the protuberance upside of below, filter frame right side, and said charging aperture and said inflatable mouth are vertical with line between liquid outlet.
Thickening of filter cake is the principal element that hinders filtering rate; Prevent that by the injection of liquid the initial stage of filter residue on filter medium from depositing in a large number, utilize the thickening of principle restriction filter cake of cross flow dynamic filtration, changed traditional cake filtration mechanism; Filter pulp is flowed perpendicular to the surface of filter medium; Solid is held back by medium, forms filter cake gradually and thickens the defective that the rate of filtration obviously slows down.The dynamic filtration theory application becomes a reality at the filter plant of plate frame structure.
1, two filter plates form two pistons that can advance; A middle filter frame forms a cylinder body, utilizes elastomer to do the middle boxes location between two blocks of plates, obtains a fixedly filter chamber thickness; And accomplish the conversion that the dynamic filtration by the diagonal angle of frame or inferior horn tangential admission filters to last cake layer; After the completion filter chamber is full of filter cake under the feed pressure effect, it is imposed super high pressure hydraulic power, make two filter plates make the cylinder piston secondary and advance; Be directly passed to filter cake through filter plate and implement the squeezing to filter residue, the bridge formation intensity that makes filter residue produces the scholar moisture content that becomes, compresses, squeezes out under greater than its critical action of hydraulic force.
Locate with elastomer at edge by two filter plates, forms a filter chamber, and under the pressure progradation; Make the filter chamber thickness variable; Obtain the filter chamber of fixed thickness during filtration, and accomplish the conversion that the dynamic filtration by the diagonal angle of frame or inferior horn tangential admission filters to last cake layer, and under the effect of hydraulic pressure high pressure; Elastomer distortion compression; Pressure passes to filter cake through filter plate, and filter cake is imposed the filter residue squeezing of hyperpressure, and the bridge formation intensity that makes filter residue produces the scholar moisture content that becomes, compresses, squeezes out under greater than its critical action of hydraulic force.
Advantage of the present invention (beneficial effect):
1, utilization advances to starch the shearing force that high flow velocities produces; Thereby suppressing cake layer thickens; The thin filter cake of generation is moved, and moving of the fine particle of easy blocking filter medium reduced that in the filtration period flocculation agent is agglomerated into oarse-grained dependence as fine particle; Reduced the secondary pollution of chemicals, and accelerated the rate of filtration mud.
2, adopt the dynamic filtration technology, the filtration period only forms thin filter cake, and the hydraulics resistance is lower, thereby flow is bigger, has accelerated filtering rate greatly, and has improved the strainability of filter cake, reduces the input of equipment, practices thrift and invests.
3, can be to Cake Wash and air blowing, the precision of purification material with get profit.
4, after filtration finishes; The hydraulic jack that utilizes machine itself to be put; Be directly passed to mud cake through filter plate; Impose the superelevation critical pressure, make that filter cake produces that scholar becomes, distortion, dehydration, changed protocnemes squeezing filter press fully and utilize plastics or the inflation of rubber-like diaphragm reverse side or produce hydraulic coupling and outwards bloat and make the squeezing pressure restriction state.Novel device does not almost have the generation of consumable accessory.Sludge filter cake thickness after the squeezing is even, volatilizees favourable greatly naturally to road, back filter cake moisture content.The critical pressure that filter cake is exerted pressure can reach the several times of traditional diaphragm pressing filter press.
5, simple to operate, energy consumption is low, whole filtration and overcritical hydraulic coupling have only the motor of two pumps, the one, advance the stock pump power consumption, the 2nd, the power consumption of hydraulic pump need not other types power.Whole machine using PLC is program control, carries out Automatic Control.
Dewatered sludge after this machine filters squeezing; The dewatered sludge that conforms to fully or surpass general office of current national Chinese Ministry of Environmental Protection notice defined moisture content＜50% that dispatches from the factory, and (CJ/T249) regulation of standard: the mud before the landfill need carry out stabilization processes: lateral shear intensity should be greater than 25KN/M
2, moisture content＜60%, the smelly degree after the sludge dewatering is less than 3 grades.
Claims (8)
1. the dynamic filtration squeezing dewatering machine improves; Comprise at least one filter element, each filter element comprises two parallel filter plates (1), is being provided with the elasticity squeeze frame of being made up of elastomer (2) and filter frame (3) in abutting connection with filter plate outward flange position between two filter plates; It is characterized in that: evenly be provided with at least two protuberances (31) on the said filter frame outer ring; Elastomer is corresponding with the protuberance position, and said elastomer cramping is between said protuberance and said filter plate, and elastomer and said filter plate are fixed; Be provided with sealing ring (4) between said filter frame inboard and said filter plate, filter frame, sealing ring and two filters surround filter chamber.
2. dynamic filtration squeezing dewatering machine according to claim 1 improves; It is characterized in that: said filter frame is the thin structure of protuberance for framework is thick; A circle thin wing (11) is established at said filter plate edge, and filter plate edge thin wing thickness is less than interior thickness, and filter frame is located between the filter plate thin wing.
3. dynamic filtration squeezing dewatering machine according to claim 2 improves, and it is characterized in that: said sealing ring is fixed on the filter plate, and wherein the sealing ring outside is provided with the sealing lip (41) that extends to filter frame, and said sealing lip is fastened on the corner, said filter frame bottom.
4. dynamic filtration squeezing dewatering machine according to claim 3 improves, and it is characterized in that: said sealing ring (4) inboard is provided with convexity (42), and the binding face of said filter plate and said sealing ring is provided with draw-in groove, and said convexity is connected in and realizes in the said draw-in groove fixing.
5. improve according to each described dynamic filtration squeezing dewatering machine of claim 1 to 4, it is characterized in that: said filter plate (1) is for square, and filter frame (3) is circular, and said protuberance (31) is provided with four, and said protuberance stretches to four angles of said filter plate.
6. dynamic filtration squeezing dewatering machine according to claim 5 improves; It is characterized in that: said elastomer (2) is a cylinder; Said elastomer center is provided with a centre bore, and said filter plate is provided with reference column, and said elastomer is plugged on the said reference column through centre bore.
7. dynamic filtration squeezing dewatering machine according to claim 6 improves; It is characterized in that: said filter plate is provided with inflatable mouth (7), the liquid outlet (8) that leads to filter chamber; Said inflatable mouth is located at middle side part on the said filter plate, and said liquid outlet is positioned at middle side part under the said filter plate.
8. dynamic filtration squeezing dewatering machine according to claim 7 improves; It is characterized in that: said filter chamber is provided with two charging apertures (6); Wherein first charging aperture is located at the protuberance downside of top, filter frame left side; Second charging aperture is located at the protuberance upside of below, filter frame right side, and said charging aperture and said inflatable mouth are vertical with line between liquid outlet.
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| Application Number | Priority Date | Filing Date | Title |
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| CN 201110250075 CN102309876B (en) | 2011-08-29 | 2011-08-29 | Improvement for dynamic filtration squeezing dewatering machine |
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| CN 201110250075 CN102309876B (en) | 2011-08-29 | 2011-08-29 | Improvement for dynamic filtration squeezing dewatering machine |
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| CN102309876B CN102309876B (en) | 2013-08-28 |
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Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104275007A (en) * | 2014-09-04 | 2015-01-14 | 浙江金鸟压滤机有限公司 | Feeding structure of dynamic filter pressure filter |
| CN104275006A (en) * | 2014-09-04 | 2015-01-14 | 浙江金鸟压滤机有限公司 | Filter press adopting dynamic filtration |
| CN104324537A (en) * | 2014-09-15 | 2015-02-04 | 浙江金鸟压滤机有限公司 | Filter-press technology of filter press |
| CN104324536A (en) * | 2014-09-15 | 2015-02-04 | 浙江金鸟压滤机有限公司 | Dynamic filter-press technology of filter press |
| CN104740908A (en) * | 2015-04-12 | 2015-07-01 | 韩洪波 | Plate-frame filter press with elastic filtering frame |
| CN105026010A (en) * | 2013-02-19 | 2015-11-04 | 奥图泰(芬兰)公司 | Method for air drying a filter cake and filter plate |
| CN111054106A (en) * | 2018-10-17 | 2020-04-24 | 张晓春 | Radial sealing method and device for filter pressing device |
| CN113952768A (en) * | 2021-09-18 | 2022-01-21 | 安徽和邦纺织科技有限公司 | High-efficient biological fiber filter disc |
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| CN2507538Y (en) * | 2001-08-08 | 2002-08-28 | 深圳市金达莱环保有限公司 | Plate press filter with adjustable filter chamber space |
| CN102068840A (en) * | 2010-12-08 | 2011-05-25 | 浙江金鸟压滤机有限公司 | Filter plate structure of non-membrane-type pressure filter |
| CN202170288U (en) * | 2011-08-29 | 2012-03-21 | 浙江金鸟压滤机有限公司 | Improved dynamic filtering and squeezing dehydrator |
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| CN2507538Y (en) * | 2001-08-08 | 2002-08-28 | 深圳市金达莱环保有限公司 | Plate press filter with adjustable filter chamber space |
| CN102068840A (en) * | 2010-12-08 | 2011-05-25 | 浙江金鸟压滤机有限公司 | Filter plate structure of non-membrane-type pressure filter |
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Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105026010A (en) * | 2013-02-19 | 2015-11-04 | 奥图泰(芬兰)公司 | Method for air drying a filter cake and filter plate |
| CN105026010B (en) * | 2013-02-19 | 2017-03-08 | 奥图泰(芬兰)公司 | For air-drying method and the filter plate of filter cake |
| US10252191B2 (en) | 2013-02-19 | 2019-04-09 | Outotec (Finland) Oy | Method for air drying a filter cake and filter plate |
| CN104275007A (en) * | 2014-09-04 | 2015-01-14 | 浙江金鸟压滤机有限公司 | Feeding structure of dynamic filter pressure filter |
| CN104275006A (en) * | 2014-09-04 | 2015-01-14 | 浙江金鸟压滤机有限公司 | Filter press adopting dynamic filtration |
| CN104275006B (en) * | 2014-09-04 | 2016-02-10 | 浙江金鸟压滤机有限公司 | A kind of dynamic filtration filter press |
| CN104324537A (en) * | 2014-09-15 | 2015-02-04 | 浙江金鸟压滤机有限公司 | Filter-press technology of filter press |
| CN104324536A (en) * | 2014-09-15 | 2015-02-04 | 浙江金鸟压滤机有限公司 | Dynamic filter-press technology of filter press |
| CN104324536B (en) * | 2014-09-15 | 2016-02-10 | 浙江金鸟压滤机有限公司 | The dynamic filter-pressing process of a kind of filter press |
| CN104740908A (en) * | 2015-04-12 | 2015-07-01 | 韩洪波 | Plate-frame filter press with elastic filtering frame |
| CN111054106A (en) * | 2018-10-17 | 2020-04-24 | 张晓春 | Radial sealing method and device for filter pressing device |
| CN113952768A (en) * | 2021-09-18 | 2022-01-21 | 安徽和邦纺织科技有限公司 | High-efficient biological fiber filter disc |
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Effective date of registration: 20181018 Address after: 510640 2414-2416 of the main building 371, five mountain road, Tianhe District, Guangzhou, Guangdong. Patentee after: Guangdong Gaohang Intellectual Property Operation Co., Ltd. Address before: 313113 No. 268, Green Avenue, industrial zone, Si an town, Changxing County, Huzhou, Zhejiang. Patentee before: Zhejiang Goldenbird Filter Press Co., Ltd. |
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Effective date of registration: 20181025 Address after: 233000 6 Chuang Yuan Road, Guzhen Economic Development Zone, Bengbu, Anhui Patentee after: Anhui smooth biological Co., Ltd. Address before: 510640 2414-2416 of the main building 371, five mountain road, Tianhe District, Guangzhou, Guangdong. Patentee before: Guangdong Gaohang Intellectual Property Operation Co., Ltd. |