CN213950938U - Multifunctional efficient filter - Google Patents
Multifunctional efficient filter Download PDFInfo
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- CN213950938U CN213950938U CN202022848694.8U CN202022848694U CN213950938U CN 213950938 U CN213950938 U CN 213950938U CN 202022848694 U CN202022848694 U CN 202022848694U CN 213950938 U CN213950938 U CN 213950938U
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Abstract
The utility model discloses a multifunctional high-efficiency filter, which comprises a cylindrical casing which is longitudinally arranged, wherein a filter element is longitudinally arranged in the casing, the top and the bottom of the casing are respectively provided with an upper cover and a lower cover, the top of the upper cover is provided with a driving device, a material discharge port is arranged below the lower cover, an electric control system is arranged on the side surface of the casing, the side surface of the casing is also provided with a water inlet and a water outlet, and the water inlet is higher than the water outlet; the filter core includes filter screen and a plurality of metal fixed strip, and the filter screen is formed by metal wedge strip spiral winding, all leaves the gap 15 that is used for filterable between the spiral metal wedge strip, and the metal fixed strip is along the axial welding at the filter screen surface according to equidistance interval. The utility model discloses work efficiency is high, and the filter effect is very good, increases factor of safety, has reduced advantages performance such as operation, construction cost.
Description
Technical Field
The utility model relates to a filtration processing technique, concretely relates to multi-functional high-efficient filter.
Background
At present, sludge concentration is an effective method for reducing the water content and the volume of sludge. Sludge concentration is mainly used for reducing interstitial water of sludge. The concentrated sludge is paste-like, and can retain fluidity, and can reduce water content of sludge discharged from water treatment structure, so that it is a sludge treatment method capable of reducing its volume, and is applicable to sludge with high water content, for example active sludge, and its water content is up to about 99%. When the water content of the sludge is reduced from 99% to 96%, the volume of the sludge can be reduced to 1/4. In order to further treat the sludge efficiently and economically, concentration must first be carried out. The water content of the concentrated sludge is generally 95-97%. In the process of sludge concentration, the discharged sludge water contains a large amount of organic substances, and the organic substances are generally mixed with the original sewage for treatment without direct discharge so as to avoid polluting the environment. The tradition carries out the concentrated processing to mud, often adopts the civil engineering sludge thickening pond method that has vertical current formula or radial flow formula shape, uses high-order concentrated jar, but this type of treatment all has a large amount of problems:
1. large floor area, high operation cost and high civil construction cost. In view of the complex installation and maintenance, the maintenance time is long, the failure rate is high, and the maintenance cost is high.
2. The effect is influenced by the retention time of the sewage. For example, the too short sewage retention time can cause the concentration of supernatant to be too high, the concentration of sludge to be too low, and the required concentration effect cannot be achieved; if the retention time is prolonged, anaerobic decomposition or denitrification can be carried out, sludge is directly floated, and the concentration can not be carried out smoothly.
3. The concentration effect is influenced by climate. For example, the effect of temperature on the concentration effect is reflected in two opposite aspects: when the temperature is increased, on one hand, sewage is easy to hydrolyze and acidify (putrefy), so that the concentration effect is reduced; on the other hand, the increase in temperature lowers the viscosity of the sludge, and makes it easy to separate interstitial water from the particles, thereby improving the thickening effect.
4. The sludge concentration condition can not be directly observed, and the working state is not convenient to adjust at any time.
5. The safety factor is low, the common pool/pot is deep, and people, animals and sundries are easy to fall into the pool/pot and are damaged.
On the other hand, the paper industry wastewater contains not only harmful chemical inorganic substances but also organic substances such as volatile phenols, precipitated solids, suspended substances, and cellulose, which are necessary raw materials in the paper making process, and thus cellulose needs to be recycled. At present, a flocculation precipitation tower method is generally adopted, and a sedimentation method is utilized to separate out fibers so as to achieve the purposes of recovering the fibers and clarifying white water. The settling tower is a more existing settling device, white water enters the inner cover body of the settling tower from the top of the tower, and the inner cover body and the shunt tubes are used for enabling the white water to form a rotational flow body with certain strength and form a stable centrifugal settling form to sink. When the concentration of the white water is higher, the white water can continue to precipitate in the cone part of the tower, and at the moment, the concentration of the tail pulp in the cone part of the tower forms a stable concentration gradient according to the height of the cone under the action of downward flow distribution formed by the tail pulp continuously discharged from the bottom of the cone of the tower and gradually accelerates to enter the precipitation speed of the concentrated white water in the cone part. Most of the primarily precipitated precipitation water bypasses the edge of the inner cover body, so that the tower body awakening part continues to precipitate at a slow upward movement speed until the precipitation water enters the overflow groove through the overflow ring. As mentioned above, the separation method using the precipitation column method also has a number of problems:
1. the settleable performance of the fiber in water is utilized, the fiber can be settled only by the residence time, so that the settling tower generally occupies huge area.
2. A certain amount of fibers still exist in the effluent, and the filtering and separating effect is not good.
3. The installation and maintenance are complex, the maintenance time is long, and the maintenance cost is relatively high.
4. The civil engineering construction cost is high.
5. The effect is influenced by the retention time of the white water, for example, the retention time of the white water is too short, so that the concentration of the supernatant fiber liquor is high, the concentration of the discharged fibers is too low, and the fiber recovery effect is poor; the excessive retention time causes hydrolytic acidification, and the white water contains various dissolved organic matters, inorganic matters and the like, so that the particle size of the particles such as fibers is reduced, the specific gravity is reduced, and the sinking is difficult.
6. The fiber recovery effect is affected by weather, and for example, when the temperature is increased, the white water is easily hydrolyzed and acidified (rotten), so that the fiber recovery effect is reduced.
7. The process conditions of fiber recovery cannot be directly observed.
8. The safety factor is low, the common pool/tank is deep, and people, animals and sundries are easy to fall into the pool/tank and are damaged.
Through the above description, it is necessary to design a novel multifunctional high-efficiency filtering device for both sludge concentration and liquid filtration and fiber recovery and filtration separation.
SUMMERY OF THE UTILITY MODEL
The utility model provides a multi-functional high-efficient filter can fold the clearance that the spiral shell body goes out mud mouth according to import sludge concentration change automatically regulated to make the even atress of backpressure board, thereby the change arouses the problem that mud mouth mud cake moisture content changes because of the import sludge concentration change.
The invention aims to be realized by the following technical scheme:
a multifunctional high-efficiency filter is characterized in that: the filter core is longitudinally arranged in the machine shell, an upper cover and a lower cover are respectively arranged at the top and the bottom of the machine shell, a driving device is arranged at the top of the upper cover, a material outlet is arranged below the lower cover, an electric control system is arranged on the side surface of the machine shell, a water inlet and a water outlet are also arranged on the side surface of the machine shell, and the water inlet is higher than the water outlet; the filter core includes filter screen and a plurality of metal fixed strip, and the filter screen is formed by metal wedge strip spiral winding, all leaves the gap that is used for filterable between the spiral metal wedge strip, and the metal fixed strip is along the axial welding at the filter screen surface according to equidistance interval.
The width of the gap is 5-20 microns.
The sharp-angled end of the cross section of the metal wedge-shaped strip faces outwards.
The metal fixing strip is also a wedge-shaped strip, and the sharp-angled end of the metal fixing strip is welded with the outer surface of the filter screen.
The metal fixing strip can be made of steel wires, copper wires or aluminum wires.
The filter element can be internally provided with a reinforcing frame or not.
The water inlet is close to the upper cover end, and a pressure gauge is arranged on a pipeline of the water inlet.
The water outlet is close to the end of the lower cover, and a pressure gauge is arranged on a pipeline of the water outlet.
And a pressure difference controller is arranged in the middle of the outer side of the casing.
Still be provided with belt cleaning device in the casing, further, belt cleaning device has the cleaning brush.
The material outlet is provided with an electromagnetic valve or a pneumatic valve, and the opening and closing of the material outlet are controlled through the electromagnetic valve or the pneumatic valve.
The utility model discloses a theory of operation is:
the fluid to be treated is sent into the filter element through the water inlet, the purified water is filtered from the inside of the filter element to the outside of the filter element through the gap of the filter element and then flows to the water outlet to be discharged, in the filtering process, materials (sludge/fibers and the like) larger than the gap of the filter element are blocked by the filter screen, the more the materials inside the filter element accumulate along with the accumulation of time, a filter cake is formed on the surface of the filter element in the process and blocks the filtering gap of the filter element, so that the pressure of the water inlet is gradually larger than the pressure of the water outlet, when the pressure difference value of the inlet and the outlet reaches a set value, the cleaning assembly is started to clean the surface of the filter element, the material discharge port is automatically opened, the materials are discharged, and the purpose of concentration/recovery/separation is realized.
In the operation process, the cleaning device can continuously or intermittently clean the filter element, and the cleaning can also be controlled by the pressure difference value or time of the inlet and the outlet or manually.
Through the structure, the utility model has the advantages of it is following:
1. the utility model discloses integration global design, compact structure, area is little, and the installation is simple, directly lays and to use on satisfying the level land that the bearing required, does not have civil engineering construction expense almost, and installation cost is lower.
2. Based on integrated global design structure, the utility model discloses easy maintenance, maintenance duration is short.
3. The utility model can continuously and automatically operate, and the rotary drum filter cartridge mode is adopted for filtering, so the dosage of the medicament is less, and the operating cost is low.
4. The utility model is laid on the ground, the drum filter drum is open, and the sludge concentration condition can be directly observed.
5. The utility model discloses factor of safety is high, and closed casing can avoid people/animal debris to get into equipment.
6. The utility model discloses do not receive the weather influence, also not influenced by sewage dwell time, can advance mud in succession, continuous filtration.
7. The utility model discloses can be applicable to sludge concentration technology in trades such as municipal administration, gravel yard, food, chemical industry, medicine, beer, water treatment and handle, realize arranging mud concentrated.
8. The utility model discloses can be applicable to the filtering separation among the fibre recovery technology, especially white water fibre retrieves, fibre separation is used in the leather trade.
9. The utility model discloses a filter screen of different meshes is changed to the accessible, replaces solid-liquid separation machines such as microstrainer to use.
Drawings
Fig. 1 is a schematic view of the partial cross-sectional structure of the present invention.
Fig. 2 is a schematic front view of the structure of the present invention.
Fig. 3 is a schematic top view of the present invention.
Fig. 4 is a schematic perspective view of the present invention.
Fig. 5 is a schematic perspective view of the drum filter cartridge of the present invention.
Fig. 6 is a schematic front view of the drum filter cartridge of the present invention.
Fig. 7 is a schematic top view of the drum filter cartridge of the present invention.
Wherein the reference numerals are: the device comprises a machine shell 1, a driving device 2, a cleaning assembly 3, a filter element 4, an electric control system 5, a material discharge port 6, a water outlet 7, a water inlet 8, a differential pressure controller 9, an upper cover 10, a lower cover 11, a pressure gauge 12, a metal wedge-shaped strip 13, a metal fixing strip 14 and a gap 15.
Detailed Description
The structure and operation of the present invention will be described with reference to the accompanying drawings.
Example 1
As shown in figures 1-4, the multifunctional high-efficiency filter comprises a cylindrical machine shell 1 which is longitudinally arranged, and the cylindrical machine shell 1 is placed on the ground through a support leg at the bottom. The filter core 4 is longitudinally arranged in the machine shell 1, the top and the bottom of the machine shell 1 are respectively provided with an upper cover 10 and a lower cover 11, the top of the upper cover 10 is provided with a driving device 2, a material outlet 6 is arranged below the lower cover 11, an electric control system 5 is arranged on the side surface of the machine shell 1, the side surface of the machine shell 1 is also provided with a water inlet 8 and a water outlet 7, and the water inlet 8 is higher than the water outlet 7.
As shown in fig. 5-7, the filter element 4 includes a filter screen and a plurality of metal fixing strips 14, the filter screen is formed by spirally winding metal wedge strips 13, gaps 15 for filtering are reserved between the metal wedge strips 13, and the metal fixing strips 14 are axially welded on the outer surface of the filter screen at equal intervals.
Example 2
In this embodiment, based on the basic structure of embodiment 1, the water inlet 8 is close to the end of the upper cover 10, and a pressure gauge 12 is arranged on the pipe of the water inlet 8. The water outlet 7 is close to the end of the lower cover 11, and a pressure gauge 12 is arranged on a pipeline of the water outlet 7.
And a pressure difference controller 9 is arranged in the middle of the outer side of the machine shell 1.
Example 3
Based on the basic structure of embodiment 1 or 2, a cleaning device is further arranged in the machine case 1, and further, the cleaning device is provided with a cleaning brush.
Example 4
According to any one of the structures of the embodiments 1 to 3, the material discharge port 6 is provided with an electromagnetic valve or a pneumatic valve, and the opening and the closing of the material discharge port 6 are controlled by the electromagnetic valve or the pneumatic valve.
Example 5
Based on any one of the structures of the embodiments 1 to 4, the drum filter cartridge assembly is further designed as follows:
the width of the gap 15 is 5-20 microns.
The sharp-angled end of the cross-section of the metal wedge strip 13 faces outwards.
The metal fixing strip 14 is also a wedge-shaped strip, and the sharp-angled end of the metal fixing strip is welded with the outer surface of the filter screen.
The metal fixing strip 14 can be made of steel wire, copper wire or aluminum wire.
The inside of the filter element 4 can be provided with a reinforcing frame or not.
According to embodiment 1-5 the filter, the utility model discloses a theory of operation is:
the fluid to be treated is sent into the filter element 4 through the water inlet 8, the purified water is filtered out of the filter element 4 from the filter element 4 through the gap 15 of the filter element 4 and then flows to the water outlet 7 to be discharged, in the filtering process, the materials (sludge/fibers and the like) larger than the gap 15 of the filter element 4 are blocked by the filter screen, the more the materials inside the filter element 4 accumulate along with the accumulation of time, a filter cake can be formed on the surface of the filter element 4 in the process, the filtering gap 15 of the filter element 4 is blocked, so that the pressure of the water inlet 8 is gradually larger than the pressure of the water outlet 7, when the pressure difference value of the inlet and the outlet reaches a set value, the cleaning assembly 3 is started to clean the surface of the filter element 4, the material discharge port 6 is automatically opened, the materials are discharged, and the purposes of concentration, recovery and separation are achieved.
In the operation process, the cleaning device can continuously or intermittently clean the filter element 4, and the cleaning can also be controlled by the pressure difference value or time of the inlet and the outlet or manually.
The utility model discloses not only applicable sludge concentration technology is handled and is realized arranging mud concentration in trades such as municipal administration, gravel yard, food, chemical industry, medicine, beer, water treatment, also can be arranged in the filtering separation of fibre recovery technology, and especially white water fibre retrieves, the fibre separation is used in the leather trade.
The above description is only a preferred embodiment of the present invention, and is not intended to limit the present invention, and any modifications, equivalent replacements, improvements, etc. made within the spirit and principle of the present invention should be included within the protection scope of the present invention.
Claims (9)
1. A multifunctional high-efficiency filter is characterized in that: the filter comprises a cylindrical machine shell (1) which is longitudinally arranged, wherein a filter element (4) is longitudinally arranged in the machine shell (1), the top and the bottom of the machine shell (1) are respectively provided with an upper cover (10) and a lower cover (11), the top of the upper cover (10) is provided with a driving device (2), a material discharge port (6) is arranged below the lower cover (11), the side surface of the machine shell (1) is provided with an electric control system (5), the side surface of the machine shell (1) is also provided with a water inlet (8) and a water outlet (7), and the water inlet (8) is higher than the water outlet (7); the filter core (4) include filter screen and a plurality of metal fixed strip (14), and the filter screen is formed by metal wedge strip (13) spiral winding, all leaves gap (15) that are used for filterable between spiral metal wedge strip (13), and metal fixed strip (14) are along the axial welding at the filter screen surface according to the interval of equidistance.
2. The multifunctional high-efficiency filter according to claim 1, wherein: the width of the gap (15) is 5-20 microns.
3. The multifunctional high-efficiency filter according to claim 1, wherein: the sharp-angled end of the section of the metal wedge-shaped strip (13) faces outwards.
4. The multifunctional high-efficiency filter according to claim 1 or 3, wherein: the metal fixing strip (14) is also a wedge-shaped strip, and the sharp-angled end of the metal fixing strip is welded with the outer surface of the filter screen.
5. The multifunctional high-efficiency filter according to claim 1, wherein: the metal fixing strip (14) is made of steel wires, copper wires or aluminum wires.
6. The multifunctional high-efficiency filter according to claim 1, wherein: the inside of filter screen still is equipped with the strengthening frame.
7. The multifunctional high-efficiency filter according to claim 1, wherein: the water inlet (8) is close to the end of the upper cover (10), and a pressure gauge (12) is arranged on a pipeline of the water inlet (8); the water outlet (7) is close to the end of the lower cover (11), and a pressure gauge (12) is arranged on a pipeline of the water outlet (7); and a pressure difference controller (9) is arranged in the middle of the outer side of the machine shell (1).
8. The multifunctional high-efficiency filter according to claim 1, wherein: still be provided with belt cleaning device in casing (1), belt cleaning device has the cleaning brush.
9. The multifunctional high-efficiency filter according to claim 1, wherein: the material outlet (6) is provided with an electromagnetic valve or a pneumatic valve, and the opening and closing of the material outlet (6) are controlled through the electromagnetic valve or the pneumatic valve.
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CN202022848694.8U CN213950938U (en) | 2020-12-02 | 2020-12-02 | Multifunctional efficient filter |
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CN202022848694.8U CN213950938U (en) | 2020-12-02 | 2020-12-02 | Multifunctional efficient filter |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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CN114570087A (en) * | 2021-12-30 | 2022-06-03 | 南京农业大学 | Vertical flow type micro-filter and working method thereof |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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CN114570087A (en) * | 2021-12-30 | 2022-06-03 | 南京农业大学 | Vertical flow type micro-filter and working method thereof |
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