Water treatment nitrate adsorption treatment device

CN224858242UActive Publication Date: 2026-10-16SHANDONG SIHAI WATER TREATMENT EQUIP CO LTD
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Patent Information

Application Number
CN202522491177.2
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2025-11-25
Publication Date
2026-10-16
Estimated Expiration
2035-11-25

AI Technical Summary

Technical Problem

[0003]此种工艺存在一些弊端和缺点:1.能耗高,需高压运行,设备投资大,膜组件成本高;2.膜易受悬浮物、有机物、微生物污染,需复杂预处理,增加了成本;3.产生高浓度浓水(含 2-5 倍原水浓度的硝酸盐),浓水处理难度大,对环境污染的危害度高;4.运行成本高,适合高水质要求但规模较小的场景;5.工艺节点分散,占地面积大,制作及现场施工周期长

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Abstract

The utility model is suitable for water treatment technical field provides a kind of water treatment nitrate adsorption treatment device, including: base, the top surface of base is equipped with adsorption column, self-priming pump, regenerant circulating pump, clean water pool, dilute regeneration box, thick regeneration box and regeneration water pump, the self-priming pump is connected with the adsorption column, the adsorption column with the clean water pool is connected by first pipeline, dilute regeneration box and the thick regeneration box between being equipped with baffle, the clean water pool is located at the top of dilute regeneration box and thick regeneration box, the regeneration water pump is connected with dilute regeneration box and the adsorption column, the regenerant circulating pump is connected with dilute regeneration box and clean water pool, by this, the utility model has the advantages of low investment cost, low operating cost, low floor area, short construction period, low threshold, high adaptability.
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Description

Technical Field

[0001] This utility model relates to the field of water treatment technology, and in particular to a water treatment nitrate adsorption treatment device. Background Technology

[0002] Traditional water treatment methods for nitrate adsorption utilize the selective permeability of semi-permeable membranes to retain nitrate ions under pressure, thereby separating water from pollutants.

[0003] This process has some drawbacks and disadvantages: 1. High energy consumption, requiring high-pressure operation, large equipment investment, and high membrane module cost; 2. The membrane is susceptible to fouling by suspended solids, organic matter, and microorganisms, requiring complex pretreatment, which increases costs; 3. It produces high-concentration concentrate (containing nitrates at 2-5 times the concentration of raw water), which is difficult to treat and poses a high risk of environmental pollution; 4. High operating costs, suitable for scenarios with high water quality requirements but small scale; 5. The process nodes are dispersed, requiring a large area and a long manufacturing and on-site construction cycle.

[0004] In conclusion, the existing technology obviously has inconveniences and defects in practical use, so it is necessary to improve it. Utility Model Content

[0005] To address the aforementioned shortcomings, this invention provides a water treatment nitrate adsorption device.

[0006] To achieve the above objectives, this utility model provides a water treatment nitrate adsorption treatment device, comprising: a base, an adsorption column, a self-priming pump, a regenerant circulation pump, a clear water tank, a dilute regeneration tank, a concentrated regeneration tank, and a regenerated water pump on the top surface of the base; the self-priming pump is connected to the adsorption column; the adsorption column is connected to the clear water tank via a first pipe; the dilute regeneration tank and the concentrated regeneration tank are located behind the adsorption column, and a partition is provided between the dilute regeneration tank and the concentrated regeneration tank; the clear water tank is located on top of the dilute regeneration tank and the concentrated regeneration tank; the regenerated water pump is located between the dilute regeneration tank and the adsorption column and is connected to both the dilute regeneration tank and the adsorption column; and the regenerant circulation pump is located between the concentrated regeneration tank and the adsorption column and is connected to both the dilute regeneration tank and the clear water tank.

[0007] According to the water treatment nitrate adsorption device of this utility model, a second pipe is provided between the self-priming pump and the adsorption column.

[0008] According to the water treatment nitrate adsorption device of this utility model, a high-flow-rate filter is provided on the base, and the high-flow-rate filter is connected to the self-priming pump and the adsorption column through the second pipe.

[0009] According to the water treatment nitrate adsorption device of this utility model, the regenerated water pump is connected to the dilute regeneration tank and the adsorption column through a third pipeline.

[0010] According to the water treatment nitrate adsorption device of this utility model, the regenerant circulation pump is connected to the concentrated regeneration tank through a fourth pipe, and the regenerant circulation pump is connected to the dilute regeneration tank through a fifth pipe.

[0011] According to the water treatment nitrate adsorption device of this utility model, the clear water tank is connected to the dilute regeneration tank and the concentrated regeneration tank through connecting pipes.

[0012] According to the water treatment nitrate adsorption device of this utility model, the base is equipped with a control box for controlling and adjusting the entire treatment device.

[0013] This utility model provides a water treatment nitrate adsorption device, comprising: a base, on the top surface of which is provided an adsorption column, a self-priming pump, a regenerant circulation pump, a clear water tank, a dilute regeneration tank, a concentrated regeneration tank, and a regenerated water pump. The self-priming pump is connected to the adsorption column, and the adsorption column is connected to the clear water tank via a first pipe. The dilute and concentrated regeneration tanks are located behind the adsorption column, and a partition is provided between them. The clear water tank is located on top of the dilute and concentrated regeneration tanks. The regenerated water pump is located between and connected to the dilute and adsorption columns. The regenerant circulation pump is located between and connected to the concentrated regeneration tank and the adsorption column, and connected to both the dilute and clear water tank. In summary, this utility model, through its "modular combined nitrate adsorption integrated equipment," offers the core advantages of reverse osmosis, which are essentially "low investment cost, low operating cost, small footprint, short construction period, low barrier to entry, and high adaptability." In scenarios involving small-scale treatment, low-concentration nitrate contamination, the need for targeted denitrification, and limited operation and maintenance capabilities, its advantages in terms of energy consumption, investment, operation and maintenance far outweigh those of reverse osmosis. Attached Figure Description

[0014] Figure 1 This is a three-dimensional structural schematic diagram of the present invention; Figure 2 This is a three-dimensional structural schematic diagram of the present invention from another perspective; Figure 3 This is a three-dimensional structural schematic diagram of the present invention from another perspective; Figure 4 This is a three-dimensional structural schematic diagram of the present invention from another perspective; In the diagram, 1-Adsorption column, 2-Self-priming pump, 3-Regenerant circulation pump, 4-Clear water tank, 5-Dilute regeneration tank, 6-Concentrated regeneration tank, 7-Regenerated water pump, 8-High flow rate filter, 9-Control box, 10-Base, 11-First pipe, 12-Second pipe, 13-Third pipe, 14-Fourth pipe, 15-Fifth pipe, 16-Connecting pipe. Detailed Implementation

[0015] To make the objectives, technical solutions, and advantages of this utility model clearer, the present utility model will be further described in detail below with reference to the accompanying drawings and embodiments. It should be understood that the specific embodiments described herein are merely for explaining the present utility model and are not intended to limit the present utility model.

[0016] It should be noted that in the description of this utility model, the terms "upper", "lower", "left", "right", "inner", "outer", etc., indicating the direction or positional relationship are based on the direction or positional relationship shown in the drawings. This is only for the convenience of description and does not indicate or imply that the device or element must have a specific orientation, or be constructed and operated in a specific orientation. Therefore, it should not be construed as a limitation of this utility model.

[0017] Furthermore, it should be noted that, in the description of this utility model, unless otherwise explicitly specified and limited, the terms "installation," "connection," and "joining" should be interpreted broadly. For example, they can refer to a fixed connection, a detachable connection, or an integral connection; they can refer to a mechanical connection or an electrical connection; they can refer to a direct connection or an indirect connection through an intermediate medium; and they can refer to the internal connection of two components. Those skilled in the art can understand the specific meaning of the above terms in this utility model according to the specific circumstances.

[0018] See Figures 1-4 This utility model provides a water treatment nitrate adsorption treatment device, including: a base 10, on the top surface of the base 10 are provided an adsorption column 1, a self-priming pump 2, a regenerant circulation pump 3, a clear water tank 4, a dilute regeneration tank 5, a concentrated regeneration tank 6, and a regenerated water pump 7. The self-priming pump 2 is connected to the adsorption column 1. The adsorption column 1 and the clear water tank 4 are connected by a first pipe 11. The dilute regeneration tank 5 and the concentrated regeneration tank 6 are located behind the adsorption column 1, and a partition is provided between the dilute regeneration tank 5 and the concentrated regeneration tank 6. The clear water tank 4 is located on top of the dilute regeneration tank 5 and the concentrated regeneration tank 6. The regenerated water pump 7 is located between the dilute regeneration tank 5 and the adsorption column 1 and is connected to the dilute regeneration tank 5 and the adsorption column 1. The regenerant circulation pump 3 is located between the concentrated regeneration tank 6 and the adsorption column 1 and is connected to the dilute regeneration tank 5 and the clear water tank 4.

[0019] See Figures 1-4Preferably, the self-priming pump 2 and the adsorption column 1 of this utility model are provided with a second pipe 12, through which the raw water is conveniently transported to the adsorption column 1.

[0020] See Figures 1-4 In addition, the base 10 of this utility model is provided with a high-flow filter 8. The high-flow filter 8 is connected to the self-priming pump 2 and the adsorption column 1 through the second pipe 12. The high-flow filter 8 can filter impurities in the raw water.

[0021] See Figures 1-4 Furthermore, the regenerated water pump 7 of this invention is connected to the dilute regeneration tank 5 and the adsorption column 1 through a third pipe 13, which facilitates the delivery of the regenerator to the interior of the adsorption column 1 for regeneration treatment of the adsorbent.

[0022] See Figures 1-4 Furthermore, the regenerant circulation pump 3 of this invention is connected to the concentrated regeneration tank 6 via a fourth pipe 14, and the regenerant circulation pump 3 is connected to the dilute regeneration tank 5 via a fifth pipe 15. The connection between the regenerant circulation pump 3 and the concentrated regeneration tank 6 and the dilute regeneration tank 5 facilitates the preparation of the regenerant solution.

[0023] See Figures 1-4 Even better, the clear water tank 4 of this utility model is connected to the dilute regeneration tank 5 and the concentrated regeneration tank 6 through a connecting pipe 16, which facilitates the preparation of the regeneration solution.

[0024] See Figures 1-4 Finally, the base 10 of this utility model is provided with a control box 9 for controlling and adjusting the entire processing device.

[0025] The working principle of this utility model: Raw water is pumped by self-priming pump 2, passes through high-flow filter 8, and then enters adsorption column 1. Nitrate impurities in the water are adsorbed by a special adsorbent in adsorption column 1, while the produced water enters clear water tank 4 under the driving force of self-priming pump 2.

[0026] After the equipment has been running for a period of time, the adsorbent will reach saturation and needs to be regenerated. At this time, sodium hydroxide regenerant is dissolved and prepared in the concentrated regeneration tank 6. After it is completely dissolved, it enters the dilute regeneration tank 5 through the regenerant circulation pump 3, and then enters the clear water tank 4. After being mixed with the clear water in the clear water tank 4, a regeneration solution that meets the requirements is prepared so that the device can be used in the regeneration state. Then, the sodium hydroxide regenerant enters the adsorption column 1 from the dilute regeneration tank 5 through the regeneration water pump 7 to regenerate the adsorbent.

[0027] Of course, there may be other embodiments of this utility model. Without departing from the spirit and essence of this utility model, those skilled in the art can make various corresponding changes and modifications based on this utility model, but these corresponding changes and modifications should all fall within the protection scope of the appended claims of this utility model.

Claims

1. A water treatment nitrate adsorption device, characterized in that, include: The base (10) has an adsorption column (1), a self-priming pump (2), a regenerant circulation pump (3), a clear water tank (4), a dilute regeneration tank (5), a concentrated regeneration tank (6), and a regenerated water pump (7) on its top surface. The self-priming pump (2) is connected to the adsorption column (1). The adsorption column (1) is connected to the clear water tank (4) via a first pipe (11). The dilute regeneration tank (5) and the concentrated regeneration tank (6) are located behind the adsorption column (1). A partition is provided between the dilute regeneration tank (5) and the concentrated regeneration tank (6). The clear water tank (4) is located on top of the dilute regeneration tank (5) and the concentrated regeneration tank (6). The regenerated water pump (7) is located between the dilute regeneration tank (5) and the adsorption column (1) and is connected to the dilute regeneration tank (5) and the adsorption column (1). The regenerator circulation pump (3) is located between the concentrated regeneration tank (6) and the adsorption column (1) and is connected to the dilute regeneration tank (5) and the clear water tank (4).

2. The water treatment nitrate adsorption treatment device according to claim 1, characterized in that, A second pipe (12) is provided between the self-priming pump (2) and the adsorption column (1).

3. The water treatment nitrate adsorption treatment device according to claim 2, characterized in that, The base (10) is provided with a high-flow filter (8), which is connected to the self-priming pump (2) and the adsorption column (1) through the second pipe (12).

4. The water treatment nitrate adsorption treatment device according to claim 1, characterized in that, The regenerated water pump (7) is connected to the dilute regeneration tank (5) and the adsorption column (1) via a third pipe (13).

5. The water treatment nitrate adsorption treatment device according to claim 1, characterized in that, The regenerant circulation pump (3) is connected to the concentrated regeneration tank (6) via a fourth pipe (14), and the regenerant circulation pump (3) is connected to the dilute regeneration tank (5) via a fifth pipe (15).

6. The water treatment nitrate adsorption treatment device according to claim 1, characterized in that, The clear water tank (4) is connected to the dilute regeneration tank (5) and the concentrated regeneration tank (6) via connecting pipes (16).

7. The water treatment nitrate adsorption treatment device according to claim 1, characterized in that, The base (10) is equipped with a control box (9) for controlling and adjusting the entire processing device.