Cellular iron and manganese removal filtering equipment

By designing a multi-stage iron and manganese removal filtration device, and utilizing the conveying pipe to form a vortex and stepped filter blocks, the problem of long mixing and reaction time between the source water and the treatment agent is solved, achieving a highly efficient filtration effect.

CN223683169UActive Publication Date: 2025-12-19JILIN XIELI ENVIRONMENTAL PROTECTION TECHNOLOGY CO LTD
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Patent Information

Application Number
CN202423028647.3
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2024-12-09
Publication Date
2025-12-19
Estimated Expiration
2034-12-09

AI Technical Summary

Technical Problem

In existing technologies, when the source water and the treatment agent come into direct contact, the mixing and reaction time is long, resulting in low filtration efficiency.

Method used

The system employs a segmented iron and manganese removal filtration device. The source water is divided and pressurized through a delivery pipe to form a vortex, which increases the contact area and reaction rate between the source water and the solid treatment agent. The system also utilizes stepped filter blocks to improve the filtration effect.

Benefits of technology

It improves the flushing efficiency and reaction rate of the source water and solid treatment agent, thus enhancing the filtration effect.

✦ Generated by Eureka AI based on patent content.

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    Figure CN223683169U_ABST
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Abstract

The utility model relates to the technical field of iron and manganese removal filtering, and discloses cellular iron and manganese removal filtering equipment which comprises a tank body, a first pipe opening is formed in the upper end of one side of the tank body, a second pipe opening is formed in the lower end of the other side of the tank body, and the first pipe opening and the second pipe opening are both fixedly connected with the tank body; the flushing assembly is arranged in the tank body, the flushing assembly is used for fully mixing source water and a treatment agent, the flushing assembly comprises a plurality of conveying pipes, the conveying pipes are arranged in the tank body in an array mode, the conveying pipes are fixedly connected with the tank body, the source water is divided by means of the conveying pipes and sprayed out in a pressurized mode, and power is provided for the source water; source water and a solid treating agent are in full contact and react, the source water in the tank body forms a vortex due to the arrangement of the multiple groups of conveying pipes, the scouring efficiency of the source water and the solid treating agent is improved, the reaction rate is increased, the vortex is formed while power is provided for the source water through pressurization, and therefore a power source is fully utilized.
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Description

TECHNICAL FIELD

[0001] The utility model belongs to the technical field of iron and manganese removal filter, concretely relates to a format iron and manganese removal filter equipment. BACKGROUND

[0002] Iron and manganese removal filter is mainly suitable for the iron and manganese removal of groundwater in high iron and manganese area, the pretreatment of industrial softened water and desalted water equipment. The equipment adopts the iron and manganese removal principle of aeration oxidation, manganese sand catalysis, adsorption and filtration, utilizes the aeration device to dissolve oxygen in air in water, and then oxidizes Fe2+ and Mn2+ in water into Fe3+ and MnO2 insoluble in water, and combines the catalysis, adsorption and filtration of natural manganese sand to remove iron and manganese ions in water.

[0003] The file with the search number (CN211799041U) discloses a format iron and manganese removal filter tank, which comprises a tank body, the inside of the tank body is evenly divided into three filter tank bodies by a partition plate, each filter tank body is provided with a water inlet pipe and a water outlet pipe, the water inlet pipe is connected with a source water pipeline through a valve, the valve is provided with a plurality of valves, the filter tank body is provided with a backwashing drainage pipeline, the backwashing drainage pipeline is connected with the water outlet pipe through a valve, the side of the tank body is provided with an air inlet pipe, the top of the tank body is provided with an air outlet pipe, the water inlet pipe is connected with a water distribution disc, the water outlet pipe is connected with a water distribution device, the top of the tank body is provided with a lifting ring, the middle of the tank body is provided with an inspection hole, the bottom of the tank body is provided with a supporting leg, and the connecting part of the supporting leg and the tank body is provided with a reinforcing plate.

[0004] The inside of the tank body is evenly divided into three filter tank bodies by a partition plate, each filter tank body is provided with a water inlet pipe and a water outlet pipe, the water inlet pipe is connected with a source water pipeline through a valve, the valve is provided with a plurality of valves, the filter tank body is provided with a backwashing drainage pipeline, the backwashing drainage pipeline is connected with the water outlet pipe through a valve, the side of the tank body is provided with an air inlet pipe, the top of the tank body is provided with an air outlet pipe, the water inlet pipe is connected with a water distribution disc, the water outlet pipe is connected with a water distribution device, the top of the tank body is provided with a lifting ring, the middle of the tank body is provided with an inspection hole, the bottom of the tank body is provided with a supporting leg, and the connecting part of the supporting leg and the tank body is provided with a reinforcing plate.

[0005] The difference between the above-mentioned device and the prior art is that one tank body is divided into three tank bodies for synchronous filtration operation, large flow is divided into small flow for processing, and source water is directly poured into the tank body for flushing in a traditional way. After the source water enters the tank body, it directly contacts the treatment agent in the tank body, and a long time is needed for the source water to mix with the treatment agent for reaction. The efficiency of filtration is not obviously improved.

[0006] Therefore, the utility model is provided. UTILITY MODEL CONTENTS

[0007] To solve the technical problem of direct contact of source water and treatment agent, the basic concept of the technical scheme of the utility model is:

[0008] A kind of iron and manganese removal filter equipment of format, including tank body, tank body is wholly by same component, component is formed by flange plate between, the upper end of one side of tank body is provided with first pipe orifice, the lower end of the other side of tank body is provided with second pipe orifice, first pipe orifice and second pipe orifice are fixedly connected with tank body, and filter is placed in the bottom end of tank body;Scouring component, scouring component is set in tank body, and scouring component is used for source water and treatment agent to be mixed fully, and scouring component includes delivery pipe, and multiple delivery pipes are arrayed in tank body, and delivery pipe is fixedly connected with tank body.

[0009] As a preferred embodiment of the utility model, the upper end of the tank body is provided with a pressurizing port, the pressurizing port is fixedly connected with the tank body, and the bottom end of the tank body is provided with a discharge port, the discharge port is fixedly connected with the tank body.

[0010] As a preferred embodiment of the utility model, the scouring component further includes a pressurizing pipe and a shunt pipe, the pressurizing pipe is arranged at the upper end of the delivery pipe, the pressurizing pipe is connected with the pressurizing port, the shunt pipe is arranged at the lower end of the delivery pipe, and the shunt pipe is connected with the liquid inlet pipe.

[0011] As a preferred embodiment of the utility model, the scouring component further includes a first layering plate and a second layering plate, the first layering plate is arranged at the lower end of the delivery pipe, the first layering plate is fixedly connected with the delivery pipe, the first layering plate is fixedly connected with the shunt pipe, the second layering plate is arranged at the upper end of the delivery pipe, the second layering plate is fixedly connected with the delivery pipe, and the pressurizing pipe is fixedly connected with the second layering plate.

[0012] As a preferred embodiment of the utility model, the first layering plate is annular as a whole, and the middle part of the first layering plate is provided with a filter block, and the filter block is fixedly connected with the first layering plate.

[0013] As a preferred embodiment of the utility model, the filter block is columnar as a whole, and the filter block is composed of multiple groups of columns, and the columns are arranged in a stepped manner.

[0014] As a preferred embodiment of the utility model, the delivery pipe is composed of multiple groups of injection rings, the middle part of the injection ring is fixedly connected with a pipeline, and the shunt pipe is a double-way pipe.

[0015] Compared with the prior art, the utility model has the following beneficial effects:

[0016] 1. The device comprises a tank body, a first layered plate, a first pipe, a second layered plate, a second pipe, a pressure pipe and a shunt pipe.

[0017] 2. The device comprises a tank body, a first layered plate, a first pipe, a second layered plate, a second pipe, a pressure pipe and a shunt pipe.

[0018] The specific embodiments of the present application will be further described in detail below with reference to the accompanying drawings. BRIEF DESCRIPTION OF DRAWINGS

[0019] In the drawings:

[0020] Figure 1 is a three-dimensional schematic view of the present application;

[0021] Figure 2 is a sectional view of the present application;

[0022] Figure 3 is a structure schematic view of the flushing assembly of the present application;

[0023] Figure 4 is a sectional view of the tank body of the present application;

[0024] Figure 5 is a structure schematic view of the first layered plate of the present application.

[0025] In the drawings: 1, tank body; 2, liquid inlet pipe; 3, first pipe opening; 31, second pipe opening; 32, pressure opening; 33, discharge opening; 4, first layered plate; 41, conveying pipe; 42, second layered plate; 43, pressure pipe; 44, shunt pipe; 45, filter block. DETAILED DESCRIPTION

[0026] In order to make the purpose, technical scheme and advantages of the embodiments of the present application more clear, the technical scheme in the embodiments will be described clearly and completely below with reference to the drawings of the embodiments of the present application, and the following embodiments are used to illustrate the present application.

[0027] Please refer to Figures 1-5The utility model provides a kind of format iron and manganese removal filter equipment, including tank body 1, tank body 1 is wholly made of same component, and it is formed between component by flange, and the upper end of one side of tank body 1 is provided with first pipe orifice 3, and the lower end of the other side of tank body 1 is provided with second pipe orifice 31, and first pipe orifice 3 is fixedly connected with tank body 1, and the bottom end of tank body 1 is placed with the mixture of filter material activated carbon, manganese sand etc.;Scouring assembly, scouring assembly is arranged in tank body 1, and scouring assembly is used for source water and processing agent to mix fully, and scouring assembly includes conveying pipe 41, and multiple conveying pipes 41 are arrayed in tank body 1, and conveying pipe 41 is fixedly connected with tank body 1, and the upper end of tank body 1 is provided with pressurizing port 32, and pressurizing port 32 is fixedly connected with tank body 1, and the bottom end of tank body 1 is provided with discharge port 33, and discharge port 33 is fixedly connected with tank body 1, and source water is differentiated and pressurized and sprayed out by conveying pipe 41, and a power is provided to source water, so that source water and solid-state processing agent are fully contacted and react, and source water in tank body 1 is arranged to form an eddy current between multiple groups of conveying pipes 41, so that the scouring efficiency of source water and solid-state contact agent is increased, and the reaction rate is improved, and the eddy current is formed while providing power to source water by pressurization, so that a power source is fully utilized.

[0028] Wherein, scouring assembly further includes pressurizing pipe 43 and shunt pipe 44, pressurizing pipe 43 is arranged at the upper end of conveying pipe 41, and pressurizing pipe 43 is clamped with pressurizing port 32, and shunt pipe 44 is arranged at the lower end of conveying pipe 41, and shunt pipe 44 is clamped with liquid inlet pipe 2, and scouring assembly further includes first layering plate 4 and second layering plate 42, first layering plate 4 is arranged at the lower end of conveying pipe 41, and first layering plate 4 is fixedly connected with conveying pipe 41, and first layering plate 4 is fixedly connected with shunt pipe 44, and second layering plate 42 is arranged at the upper end of conveying pipe 41, and second layering plate 42 is fixedly connected with conveying pipe 41, and pressurizing pipe 43 is fixedly connected with second layering plate 42, and conveying pipe 41 has multiple groups of jet rings, and pipe is fixedly connected in the middle of jet ring, and shunt pipe 44 is double-way pipe, and solid-state processing agent enters tank body 1 by first pipe orifice 3, and source water flows to shunt pipe 44 by liquid inlet pipe 2 at this time, and source water enters first layering plate 4 by shunt pipe 44 and directly enters conveying pipe 41, and pressurizing is added to pressurizing port 32 by air compressor at this time, and pressurized gas enters second layering plate 42 by pressurizing pipe 43, and pressurized gas enters conveying pipe 41 from second layering plate 42 to pressurize source water, and source water is pressurized and sprayed out by pressurized gas by the upper jet ring of conveying pipe 41, and the operating pressure is 0.3Mpa, and source water is differentiated and pressurized and sprayed out by conveying pipe 41, and a power is provided to source water, so that source water and solid-state processing agent are fully contacted and react, and source water in tank body 1 is arranged to form an eddy current between multiple groups of conveying pipes 41, so that the scouring efficiency of source water and solid-state contact agent is increased, and the reaction rate is improved, and the eddy current is formed while providing power to source water by pressurization, so that a power source is fully utilized.

[0029] The first layered plate 4 is annular as a whole, the middle part of the first layered plate 4 is provided with a filter block 45, the filter block 45 is fixedly connected with the first layered plate 4, the filter block 45 is columnar as a whole, the filter block 45 is composed of a plurality of column bodies, the column bodies are arranged in a stepped manner, the source water after flushing flows to the bottom end of the tank body 1 through the filter block 45 in the middle part of the first layered plate 4 to contact with filter materials for filtration and is discharged through the discharge port 33, the stepped design of the filter block 45 increases the contact area of the source water and the filter block 45, and the filtration effect is improved.

[0030] Working principle: the solid treatment agent (the solid treatment agent is an existing iron and manganese removal agent, which is a prior art and will not be described here) enters the tank body 1 through the first pipe opening 3, at this time, the source water flows into the shunt pipe 44 through the liquid inlet pipe 2, the source water enters the first layered plate 4 through the shunt pipe 44 and directly enters the conveying pipe 41, at this time, the pressure in the pressurizing port 32 is increased by means of the air compressor, the pressurizing gas enters the second layered plate 42 through the pressurizing pipe 43, the pressurizing gas enters the conveying pipe 41 from the second layered plate 42 to pressurize the source water, the source water is pressurized and sprayed out by the pressurizing gas through the spraying ring on the conveying pipe 41, the operating pressure is 0.3Mpa, the source water is differentiated and pressurized and sprayed out by means of the conveying pipe 41, a power is provided for the source water, so that the source water is in full contact with the solid treatment agent and reacts, the source water in the tank body 1 forms an eddy current due to the arrangement of the plurality of conveying pipes 41, the flushing efficiency of the source water and the solid contact agent is increased, the reaction rate is improved, the eddy current is formed at the same time when the power is provided for the source water by pressurizing, so that the power source is fully utilized, the source water after flushing flows to the bottom end of the tank body 1 through the filter block 45 in the middle part of the first layered plate 4 to contact with filter materials for filtration and is discharged through the discharge port 33, the stepped design of the filter block 45 increases the contact area of the source water and the filter block 45, and the filtration effect is improved, when cleaning is needed, the upper end of the tank body 1 is opened, the flushing assembly is taken out, the filter material residues and the solid treatment agent accumulated at the bottom end of the tank body 1 are discharged from the second pipe opening 31 by means of tools.

[0031] It can be understood that the utility model is described through some embodiments, and those skilled in the art know that various changes or equivalent replacements can be made to these features and embodiments without departing from the spirit and scope of the utility model. In addition, under the guidance of the utility model, these features and embodiments can be modified to adapt to specific conditions and materials without departing from the spirit and scope of the utility model. Therefore, the utility model is not limited by the specific embodiments disclosed here, and all embodiments falling within the scope of the claims of the present application belong to the scope protected by the utility model.

Claims

1. A format iron and manganese removal filter apparatus, characterized by, Include: The tank body (1) is composed of the same parts, and the parts are connected by flanges. The first pipe (3) is arranged at the upper end of one side of the tank body (1), and the second pipe (31) is arranged at the lower end of the other side of the tank body (1). The first pipe (3) and the second pipe (31) are fixedly connected with the tank body (1), and the filter is placed at the bottom end of the tank body (1); The flushing assembly is arranged in the tank body (1), and the flushing assembly is used for mixing source water and treatment agent. The flushing assembly includes a plurality of delivery pipes (41) arranged in the tank body (1), and the delivery pipe (41) is fixedly connected with the tank body (1).

2. The filter apparatus according to claim 1, wherein The upper end of the tank body (1) is provided with a pressurizing port (32), and the pressurizing port (32) is fixedly connected with the tank body (1). The bottom end of the tank body (1) is provided with a discharge port (33), and the discharge port (33) is fixedly connected with the tank body (1).

3. The filter apparatus of claim 1, wherein, The flushing assembly further includes a pressurizing pipe (43) and a shunt pipe (44). The pressurizing pipe (43) is arranged at the upper end of the delivery pipe (41), and the pressurizing pipe (43) is connected with the pressurizing port (32). The shunt pipe (44) is arranged at the lower end of the delivery pipe (41), and the shunt pipe (44) is connected with the liquid inlet pipe (2).

4. The filter apparatus of claim 3, wherein, The flushing assembly further includes a first layering plate (4) and a second layering plate (42). The first layering plate (4) is arranged at the lower end of the delivery pipe (41), and the first layering plate (4) is fixedly connected with the delivery pipe (41). The first layering plate (4) is fixedly connected with the shunt pipe (44). The second layering plate (42) is arranged at the upper end of the delivery pipe (41), and the second layering plate (42) is fixedly connected with the delivery pipe (41). The pressurizing pipe (43) is fixedly connected with the second layering plate (42).

5. The filter apparatus of claim 4, wherein, The first layering plate (4) is annular as a whole, and the middle part of the first layering plate (4) is provided with a filter block (45), and the filter block (45) is fixedly connected with the first layering plate (4).

6. The filter apparatus of claim 5, wherein, The filter block (45) is columnar as a whole, and the filter block (45) is composed of a plurality of column bodies arranged in a stepped manner.

7. The filter apparatus of claim 3, wherein, The delivery pipe (41) is composed of a plurality of injection rings, and the middle part of the injection ring is fixedly connected with a pipeline. The shunt pipe (44) is a double-way pipe.

Citation Information

Patent Citations

  • Cellular iron and manganese removal filtering tank

    CN211799041U