CN218653388U

CN218653388U - Novel synthesize filter equipment and buddha's warrior attendant line sand device

Info

Publication number: CN218653388U
Application number: CN202122685785.9U
Authority: CN
Inventors: 石龙; 叶琴; 朱玉祥; 赖显忠; 邹士林; 孟炳宇
Original assignee: Zhangjiakou Yuanshi New Material Co ltd
Current assignee: Zhangjiakou Yuanshi New Material Co ltd
Priority date: 2021-11-04
Filing date: 2021-11-04
Publication date: 2023-03-21
Anticipated expiration: 2031-11-04

Abstract

The utility model relates to a liquid filtration technology field, in particular to novel synthesize filter equipment and diamond wire sand on device. The filtering device comprises a filtering tank; the filter tank is divided into a first chamber, a second chamber, a third chamber and a fourth chamber in sequence by the four baffles in a cross or similar cross mode; the feeding hole is positioned on the side edge of the filter tank and communicated with the first chamber; a discharge port communicated with the fourth chamber; and overflowing holes are formed in the second baffle and the third baffle, and backflow holes are formed in the third baffle. The utility model discloses a method that the device utilized U type and S type to flow to deposit carries out the precipitation of multistage grade etc. with the impurity in the liquid and reduces the particle content in the liquid, can effectually slow down the change cycle, reaches the operation requirement of long-time operation, is favorable to the application scope of technology, reduces artifical extravagant.

Description

Novel synthesize filter equipment and diamond wire sand on device

Technical Field

The utility model relates to a liquid filtration technology field, in particular to novel synthesize filter equipment and diamond wire sand on device.

Background

The industrial filter consists of a shell, a multi-element filter element, a back washing mechanism, an electric cabinet, a speed reducer, an electric valve, a differential pressure controller and the like. The inner cavity of the transverse clapboard in the shell is divided into an upper cavity and a lower cavity, a plurality of filter elements are arranged in the upper cavity, so that the filtering space is fully utilized, the size of the filter is obviously reduced, and a back washing sucker is arranged in the lower cavity. When the filter works, turbid liquid enters the lower cavity of the filter through the inlet and enters the inner cavity of the filter element through the clapboard holes. Impurities larger than the gap of the filter element are intercepted, and the purified liquid passes through the gap to reach the upper cavity and is finally sent out from the outlet.

The traditional filtering process is a single mode, liquid is rapidly circulated and flows through a liquid filter in a pressure mode, and the filtering precision of a filter element meets the use requirement. The liquid filter is an indispensable device on the medium conveying pipeline, and is usually installed at the inlet end of a pressure reducing valve, a pressure relief valve, a constant water level valve or other equipment to eliminate impurities in the medium so as to protect the normal use of the valve and the equipment. When fluid enters a filter cylinder with a filter screen of a certain specification, impurities are blocked, clean filtrate is discharged from a filter outlet, when the filter cylinder needs to be cleaned, the detachable filter cylinder is taken out and is installed again after treatment, besides a mesh filter, the filter has various filters, such as a lamination filter, a sand filter, a carbon filter and the like, the main principle is to use the pore size of a filter medium to intercept substances smaller than the pore size of the filter medium, and certain filter media have special effects of adsorption and the like. Most filters are not troublesome in backwashing, and a good backwashing effect can be achieved by only introducing clean water into the medium in the reverse backwashing filter from one end of filtered water.

But the use requirements are more complicated, such as pollution waste and cost increase caused by replacing the filter element regularly. If the content of particle impurities in the liquid is higher, the replacement period of the filter element is shortened, and if a process with special requirements is adopted, the use requirement cannot be met.

The other one is traditional coagulation sedimentation and flocculation adsorption, the principle is that the separation effect is achieved through the specific gravity and physical properties of different substances, the advantage is that impurities in liquid can be separated cleanly, but one of the principles is that the time is spent longer, the storage space and the occupied site are larger, in addition, the usage amount of circulating materials is larger, and unnecessary storage and fund occupation waste are caused.

The traditional filtering method at present can not meet the requirements of the existing process, the excessive investment is easy to cause waste, the excessive investment is caused, the common filtering method is easy to cause the problems of pipeline blockage caused by uneven impurity content in liquid, wear of a pump head, influence on product performance in the flushing process and the like.

SUMMERY OF THE UTILITY MODEL

In order to solve the problem, the utility model aims at providing a novel synthesize filter equipment and diamond wire sand device.

In order to achieve the above object, the utility model discloses specifically adopt following technical scheme:

a novel integrated filtration device comprising:

a filter tank;

the filter tank is divided into a first chamber, a second chamber, a third chamber and a fourth chamber in sequence by the four baffles in a cross or similar cross mode; the first chamber, the second chamber, the third chamber, and the fourth chamber may be the same or different in size.

The feeding hole is positioned on the side edge of the filter tank and is communicated with the first chamber;

the discharge port is positioned on the side edge of the filter tank and communicated with the fourth chamber;

and overflowing holes are formed in the second baffle and the fourth baffle, and backflow holes are formed in the third baffle.

Preferably, the bottom of the filter tank is provided with a magnet.

Preferably, the magnet is a plurality of bar magnets arranged in parallel.

Preferably, the two adjacent magnets are placed in opposite directions, and the distance between the two adjacent magnets is 1 cm-1.5 cm.

Preferably, the overflowing hole and the refluxing hole are in the shape of a lower semicircle.

Preferably, the second baffle and the fourth baffle are curved surfaces and convex, and the convex direction is opposite to the flowing direction of the feed liquid.

Preferably, the height of the overflowing hole is lower than that of the backflow hole.

Preferably, the distance between the overflowing hole and the bottom of the filter tank is 3 cm-5 cm, and the height difference between the overflowing hole and the backflow hole is kept between 16 cm-20 cm.

Preferably, the feed inlet is provided with a coarse filter screen, and the discharge outlet is provided with a fine filter screen.

Preferably, the first chamber, the second chamber, the third chamber and the fourth chamber formed by the first baffle, the second baffle, the third baffle and the fourth baffle, and the liquid flow path formed by the overflowing hole and the refluxing hole are U-shaped.

A diamond wire sanding device comprising:

the subslot is a sand feeding slot;

the filtration device of any of the preceding claims;

the subslot and the filter tank circulate the liquid through a pipeline.

Advantageous effects

The utility model discloses a change cycle can effectually be slowed down to backflow filtering and multistage sediment, reaches the operation requirement of long-time operation, is favorable to the application scope of technology, reduces artifical extravagant.

The utility model discloses a problem that the absorption in magnetic field is depositd can reach quick sediment and is prevented to deposit and fluctuate and cause.

The utility model discloses can improve the not enough of sand technology on present buddha's warrior attendant line, improve particulate matter control in the liquid, stop the quality fluctuation that causes because of the inequality of granule content, influence the performance of product.

Drawings

Fig. 1 is the utility model discloses sand device structure schematic diagram on buddha's warrior attendant line.

Fig. 2 is a schematic view of the filter tank of the present invention.

Fig. 3 is a schematic diagram of a third baffle structure of the present invention.

Fig. 4 is a schematic diagram of the magnet arrangement of the present invention.

Fig. 5 is a flow chart of the device of the present invention.

1-a filter tank; 2-a first baffle; 3-a second baffle; 4-a third baffle; 5-a fourth baffle; 6-a first chamber; 7-a second chamber; 8-a third chamber; 9-a fourth chamber; 10-a feed inlet; 11-a discharge hole; 12-an overflow aperture; 13-a return orifice; 14-a magnet; 15-coarse filter screen; 16-fine filter screen; 17-a feed pipe; 18-a discharge pipe; 19-subslot.

Detailed Description

The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. The following description of at least one exemplary embodiment is merely illustrative in nature and is in no way intended to limit the invention, its application, or uses. Based on the embodiments of the present invention, all other embodiments obtained by a person skilled in the art without making creative efforts belong to the protection scope of the present invention.

It is noted that the terminology used herein is for the purpose of describing particular embodiments only and is not intended to be limiting of exemplary embodiments according to the present application. As used herein, the singular forms "a", "an" and "the" are intended to include the plural forms as well, and it should be understood that when the terms "comprises" and/or "comprising" are used in this specification, they specify the presence of stated features, steps, operations, devices, components, and/or combinations thereof, unless the context clearly indicates otherwise.

Unless specifically stated otherwise, the relative arrangement of the components and steps, the numerical expressions, and numerical values set forth in these embodiments do not limit the scope of the present invention. Techniques, methods, and apparatus known to those of ordinary skill in the relevant art may not be discussed in detail but are intended to be part of the specification where appropriate.

The present invention will be described in detail below with reference to the accompanying drawings so as to facilitate the understanding of the present invention by those skilled in the art.

As shown in fig. 1, the novel integrated filtering device and diamond wire sanding device of the present invention comprises a filtering tank 1, a magnet 14 is disposed at the bottom of the filtering tank 1, a feeding port 10 is disposed at the upper part of the filtering tank 1, and the feeding port 10 is connected to a feeding pipe 17; and a discharge port 11 is arranged at the lower part of the side edge of the filter tank 1, the discharge port 11 is communicated with a discharge pipe 18, and the feed pipe 17 and the discharge pipe 18 are both communicated with a sub-tank 19.

A discharge port (not shown) for sediment is designed at the bottom of the filter tank 1, which is convenient for clearing sediment.

As shown in fig. 4, the magnets 14 are a plurality of bar magnets arranged in parallel, and two adjacent magnets 14 are oppositely arranged at a distance of 1cm to 1.5cm. As can be seen from the figure, the bar magnets are arranged in two rows, and each row is provided with 4 magnets in parallel. The magnetic field effect through magnet can effectual absorption metal particles and precipitate, promotes the precipitation effect.

As shown in fig. 2, which is a plan view of the filter tank 1, it can be seen that the filter tank 1 is a rectangular parallelepiped, and includes a first baffle plate 2, a second baffle plate 3, a third baffle plate 4, and a fourth baffle plate 5, which divide the filter tank 1 into a first chamber 6, a second chamber 7, a third chamber 8, and a fourth chamber 9 in order in a cross-like or cross-like shape. As shown in fig. 2, the first chamber 6 and the second chamber 7 are separated by the second baffle 3, the second chamber 7 and the third chamber 8 are divided by the third baffle 4, and the third chamber 8 and the fourth chamber 9 are divided by the fourth baffle 5; the fourth chamber 9 and the first chamber 6 are divided by the first baffle 2.

As shown in fig. 2, a feed port 10, which is located at a side of the filter tank 1, communicates with the first chamber 6; the discharge opening 11 communicates with the fourth chamber 9. And overflowing holes 12 are arranged on the second baffle plate 3 and the fourth baffle plate 5, and a backflow hole 13 is arranged on the third baffle plate 4. The third baffle 4 is constructed as shown in fig. 3. As can be seen in the figure, the overflow aperture 12 is in the shape of a lower half circle. Of course, the return holes 13 are also formed in a lower semicircular shape for better settling. The lower semicircle shape refers to a similar 180-degree sector structure formed by a line segment and an arc below the line segment, and comprises a semicircle and a quasi-semicircle, such as a semi-ellipse formed by the line segment and the arc line segment.

As shown in fig. 2, the second baffle 3 and the fourth baffle 5 are curved convex shapes, and the convex direction is opposite to the liquid flowing direction. Like this second baffle 3 and fourth baffle 5 have formed the baffle of S-shaped, can reach the effect of buffering rivers, can stabilize the velocity of flow for the efficiency of natural sedimentation.

In order to ensure the effect of sedimentation, the height of the two overflow holes 12 is lower than the height of the return hole 13. In this embodiment, the distance between the overflowing hole 12 and the bottom of the filter tank 1 is 3 cm-5 cm, and the height difference between the overflowing hole 12 and the backflow hole 13 is kept at 16 cm-20 cm. So set up, can effectively prevent the secondary stirring that the backward flow impact leads to.

A coarse filter screen 15 is arranged at the feed inlet 10, and a fine filter screen 16 is arranged at the discharge outlet 11. The coarse filter screen 15 can effectively filter out some impurities with large particles, and the fine filter screen 16 can ensure that the particles cannot affect the stability of the process along with the liquid flowing into the sub-tank 19. In this embodiment, the coarse filter screen 15 is a 300-mesh filter screen, and the material of the filter screen may be stainless steel or PP-based corrosion-resistant material, such as 316L stainless steel or resin fiber. The mesh of the fine filter screen 16 is 1-10 μm.

As can be seen from fig. 1 to 2, the first chamber 6, the second chamber 7, the third chamber 8 and the fourth chamber 9 formed by the first baffle 2, the second baffle 3, the third baffle 4 and the fourth baffle 5, and the liquid flow path formed by the overflowing hole 12 and the refluxing hole 13 are U-shaped.

A diamond wire sanding device comprising:

the subslot 19 is a sand feeding trough; further comprising the filtration device of any of the preceding claims; the sub-tank 19 circulates the liquid through the filter tank 1 by a pipe. The lines are the feed pipe 17 and the discharge pipe 18 described above. As can be seen from FIG. 1, the sub tank 19 is higher than the filter tank 1, and the feed pipe 17 is higher than the discharge pipe 18, so that a pump is provided on the discharge pipe 18 to facilitate the liquid in the filter tank 1 to enter the sub tank 19.

The utility model discloses a method of use of device is shown in fig. 5, includes the following step:

step S1: when a large amount of particles are brought in by the liquid circulation, the liquid flows back to be roughly filtered, and a 300-mesh filter screen is used for filtering at the feed inlet 10. The content of particles in the filtered liquid in the step can be controlled between 0.1 and 10 microns.

Step S2: filtered liquid enters a filter tank 1, the interior of the filter tank 1 is subjected to cavity transformation to form four cavities, an S partition + U-shaped path structure is formed, a magnet is arranged at the bottom of the filter tank, and the liquid passes through each cavity and is precipitated through multistage precipitation and a magnetic field. Through the buffer convection effect of the magnetic field and the liquid flow and the adsorption effect of the magnetic field and the liquid flow on the metal precipitates, the precipitated liquid basically meets the use requirements of the process.

And step S3: the precision filtration before the discharge port 11 can well meet the requirements of the process by controlling the precision of the bracket and the filter cloth, namely, the filter cloth runs for a long time, and the replacement period of the filter cloth can be extended to more than 1 month.

If in some special application fields, some general filtering devices can be added on one side of the circulating pump to meet the requirements of process use. According to the existing product quality requirements, when the content of particles in the liquid exceeds a certain concentration, scraping and cutting effects can be formed along with liquid flow, and the surface particle and surface layer quality of the product are influenced.

In addition, the functional devices in the embodiments of the present application may be integrated together to form an integrated device, or a device may exist alone, or two or more devices may form an independent part.

The above-mentioned embodiments only represent some embodiments of the present invention, and the description thereof is specific and detailed, but not to be construed as limiting the scope of the present invention. It should be noted that, for those skilled in the art, without departing from the concept of the present invention, several variations and modifications can be made, which all fall within the scope of the present invention.

Claims

1. A novel synthesize filter equipment which characterized in that includes:

a filter tank (1);

the filter tank comprises a first baffle (2), a second baffle (3), a third baffle (4) and a fourth baffle (5), wherein the four baffles divide the filter tank (1) into a first chamber (6), a second chamber (7), a third chamber (8) and a fourth chamber (9) in a cross or similar cross mode;

the feeding hole (10) is positioned on the side edge of the filter tank (1) and is communicated with the first chamber (6);

the discharge port (11) is positioned on the side edge of the filter tank, and the discharge port (11) is communicated with the fourth chamber (9);

overflowing holes (12) are formed in the second baffle plate (3) and the fourth baffle plate (5), and backflow holes (13) are formed in the third baffle plate (4).

2. Device according to claim 1, characterized in that the bottom of the filter tank (1) is provided with magnets (14).

3. The device according to claim 2, wherein the magnets (14) are a plurality of bar magnets arranged in parallel, and two adjacent magnets (14) are oppositely arranged and spaced at a distance of 1cm to 1.5cm.

4. The device according to claim 1, characterized in that the flow-through holes (12) and the flow-back holes (13) are of lower semicircular shape.

5. Device according to claim 1, characterized in that said second baffle (3) and fourth baffle (5) are curved and convex in shape, said convex direction being opposite to the liquid flow direction.

6. Device according to claim 1, characterized in that the level of the overflow opening (12) is lower than the level of the return opening (13).

7. The device according to claim 1, characterized in that the overflowing hole (12) is 3 cm-5 cm away from the bottom of the filter tank (1), and the height difference between the overflowing hole (12) and the backflow hole (13) is kept between 16 cm-20 cm.

8. The device according to claim 1, characterized in that a coarse filter screen (15) is arranged at the inlet opening (10) and a fine filter screen (16) is arranged at the outlet opening (11).

9. The device according to claim 1, characterized in that the first chamber (6), the second chamber (7), the third chamber (8) and the fourth chamber (9) formed by the first baffle (2), the second baffle (3), the third baffle (4) and the fourth baffle (5) and the liquid flow path formed by the overflowing hole (12) and the refluxing hole (13) are U-shaped.

10. A diamond wire sanding device, comprising:

a subslot (19) which is a sanding tank;

the filter device of any one of claims 1 to 9;

the sub-tank (19) and the filter tank (1) circulate the liquid through a pipeline.