Hydrogen peroxide wastewater treatment device
By introducing a combination of wastewater equalization tank, coarse filter tank, fine filter tank and oil-water separator into the hydrogen peroxide production process, the problems of large footprint and unstable COD of wastewater treatment equipment are solved. This achieves miniaturization and efficient recovery of working fluid, and improves filtration quality and membrane lifespan.
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- HUNAN LONGSHENG ENVIRONMENTAL PROTECTION CO LTD
- Filing Date
- 2025-04-17
- Publication Date
- 2026-04-10
AI Technical Summary
Existing hydrogen peroxide production processes have wastewater treatment equipment that occupies a large area, lacks miniaturization capabilities, and has unstable effluent COD and inconvenient working fluid recovery capabilities.
The treatment device includes a wastewater equalization tank, a coarse filter tank, a fine filter tank, and an oil-water separator. Wastewater is sequentially guided to each tank through a guide pipe and a guide pump for coarse filtration, fine filtration, and oil-water separation. A booster pump then guides the wastewater to the membrane filter assembly for final filtration, and the wastewater is treated using a membrane separation device.
It achieves stable and miniaturized wastewater treatment, integrated operation, reduced footprint, improved working fluid recovery capacity and filtration quality, and extended membrane lifespan.
Smart Images

Figure CN224105701U_ABST
Abstract
Description
TECHNICAL FIELD
[0001] The utility model application relates to wastewater treatment technical field, concretely is hydrogen peroxide wastewater treatment device. BACKGROUND
[0002] Hydrogen peroxide is the "green" product that is widely used in papermaking, environmental protection, textile, chemical synthesis, electronics, medicine, food, metallurgy and many other industries, and is widely concerned by countries all over the world, especially developed countries with sound environmental protection regulations, and has unique social benefits. At present, most of the domestic hydrogen peroxide production processes use anthraquinone method. The principle of hydrogen peroxide production is: first, 2-ethylanthraquinone is dissolved in specific organic solvent heavy aromatic hydrocarbon and tricresyl phosphate to form a working solution. During the production and manufacturing of hydrogen peroxide, the wastewater thereof usually needs to be treated.
[0003] At present, most of the hydrogen peroxide project wastewater treatment processes use the traditional "wastewater storage tank + oil separation + air flotation + Fenton oxidation + sedimentation + biochemical + secondary sedimentation tank + sewage treatment plant treatment" technology. This traditional process has some shortcomings: a large amount of hydrogen peroxide, acid, alkali, ferrous sulfate, flocculating agent and the like are consumed; a large amount of iron sludge hazardous waste is generated; the land occupation area is large, the wastewater treatment equipment cannot be miniaturized well, and the hydrogen peroxide wastewater treatment effect is not good enough. In actual operation, the total phosphorus removal effect is not good, the effluent COD is unstable, and the working solution recovery capacity is relatively inconvenient. Therefore, we propose a hydrogen peroxide wastewater treatment device to solve the above problems. SUMMARY
[0004] In order to solve the problems of large land occupation area, insufficient miniaturization capacity, unstable effluent COD and relatively inconvenient working solution recovery capacity of the existing wastewater treatment equipment, the utility model provides a hydrogen peroxide wastewater treatment device to solve the above problems.
[0005] To achieve the above purpose, the utility model provides the following technical scheme: a hydrogen peroxide wastewater treatment device, comprising a wastewater conditioning tank, a coarse filtration tank, a fine filtration tank and an oil-water separation tank, and a flow guide pipe is connected between adjacent wastewater conditioning tanks, coarse filtration tanks, fine filtration tanks and oil-water separation tanks;
[0006] The side surfaces of the coarse filtration tank, the fine filtration tank and the oil-water separation tank are each provided with a flow guide pump and a pressure measuring table. The inner side of the coarse filtration tank is provided with a cloth bag filter assembly. The inner side of the fine filtration tank is provided with a folding filter element filter assembly. The bottom of the subsequent connection part of the oil-water separation tank is provided with a filter membrane filter assembly.
[0007] The side surface of the oil-water separation tank is provided with an oil outlet pipe. A liquid outlet pipe is arranged between the filter membrane filter assembly and the oil-water separation tank. A booster pump is arranged on the liquid outlet pipe. The bottom of the filter membrane filter assembly is provided with a wastewater discharge pipe.
[0008] Further, the three groups of the flow guide pipes are sequentially arranged between the adjacent wastewater conditioning tanks, the coarse filter tanks, the fine filter tanks and the oil-water separation tanks, and the three groups of the flow guide pipes are in overall communication with the wastewater conditioning tanks, the coarse filter tanks, the fine filter tanks and the oil-water separation tanks.
[0009] Further, the flow guide pumps and the pressure measuring tables are sequentially arranged on the sides of the coarse filter tanks, the fine filter tanks and the oil-water separation tanks, and the sides of the pressure measuring tables are provided with alarmers.
[0010] Further, the cloth bag filter assembly is a cloth bag filter, and the folded filter core filter assembly is a folded filter core filter.
[0011] Further, the outlet pipe is provided with a pressure measuring device, and the inner side of the filter membrane filter assembly is provided with a membrane separation device.
[0012] Further, the booster pump is a high-pressure pump body.
[0013] Further, the coarse filter tank and the fine filter tank are both provided with a switch cover plate on the top, and the two switch cover plates are respectively hingedly sealed to the top of the coarse filter tank and the fine filter tank.
[0014] Further, the coarse filter tank and the fine filter tank are both provided with a switch cover plate on the top, and the two switch cover plates are respectively hingedly sealed to the top of the coarse filter tank and the fine filter tank.
[0015] Further, the filtering precision of the cloth bag filter assembly is 3-6 um, and the filtering precision of the folded filter core filter assembly is 0.5-1.2 um.
[0016] Compared with the prior art, the beneficial effects of the utility model are:
[0017] 1、in the utility model, through three groups of flow guide pipes and flow guide pumps, the water source in the wastewater conditioning tank is sequentially guided to the coarse filter tank, the fine filter tank and the oil-water separation tank, in the process of guiding, the coarse filter tank is coarsely filtered by the cloth bag filter assembly, then the fine filter tank is finely filtered by the folded filter core filter assembly, finally the oil-water separation tank is used for oil-water separation, the wastewater is deposited at the bottom of the oil-water separation tank, is guided to the filter membrane filter assembly by the booster pump, is filtered by the membrane separation device, is discharged by the outlet pipe, and is subjected to subsequent treatment, the filter membrane filter assembly is provided with a wastewater discharge pipe, the filtered wastewater is treated, the device is stable in overall operation, can be miniaturized and integrated, is convenient for wastewater treatment, convenient to use, makes the device convenient, occupies small area, and is convenient to operate.
[0018] 2、The utility model discloses a through three diversion pumps can be respectively to the coarse filter filter jar, fine filter filter jar and oil -water separation jar wastewater carries out pressure boosting and flow guiding, makes wastewater filtration stable, and the filtration pressure intensity of coarse filter filter jar and fine filter filter jar can be by pressure measuring table real -time pressure measurement, convenient to replace, and the top of oil -water separation jar is equipped with the oil outlet pipe, and the oil -water separator can remove most of the working fluid component in wastewater, can reduce the load of subsequent membrane separation device, guarantees the stable operation of membrane separation device, prolongs the service life of membrane, and the oil outlet pipe can collect the working fluid and return, plays the recycling effect, reduces the waste of working fluid, and the device working fluid recovery capacity is good, convenient to use, and the filtering quality is excellent. BRIEF DESCRIPTION OF DRAWINGS
[0019] In order to more clearly illustrate the technical scheme in the embodiments of the present application or the prior art, the drawings needed to be used in the following embodiment or prior art description will be briefly introduced. Obviously, the drawings in the following description are only some embodiments of the present application, and those skilled in the art can obtain other drawings according to these drawings without creating any creative labor.
[0020] Figure 1 It is a structure front view of the utility model;
[0021] Figure 2 It is a structure front view of the utility model;
[0022] Figure 3 It is a structure front view of the utility model;
[0023] Figure 4 It is a structure front view of the utility model.
[0024] The meaning of the reference signs in the drawing: 1, wastewater conditioning tank; 2, coarse filter filter jar; 3, fine filter filter jar; 4, oil -water separation jar; 5, diversion pipe; 6, diversion pump; 7, pressure measuring table; 8, cloth bag filter assembly; 9, folding filter core filter assembly; 10, filter membrane filter assembly; 11, oil outlet pipe; 12, booster pump; 13, wastewater discharge pipe; 14, liquid outlet pipe; 15, alarm; 16, pressure measuring device; 17, switch cover plate. DETAILED DESCRIPTION
[0025] In order to make the application purposes, features and advantages of the present application more obvious and easy to understand, the technical solutions in the embodiments of the present application will be described clearly and completely in the following with reference to the drawings in the embodiments of the present application. Obviously, the following described embodiments are only some embodiments of the present application, not all embodiments. Based on the embodiments in the present application, all other embodiments obtained by those skilled in the art without creating any creative labor are within the scope of protection of the present application.
[0026] Referring to Figures 1-4 , the hydrogen peroxide wastewater treatment device comprises a wastewater conditioning tank 1, a coarse filtration tank 2, a fine filtration tank 3 and an oil-water separation tank 4, and flow guide pipes 5 are connected between adjacent wastewater conditioning tank 1, coarse filtration tank 2, fine filtration tank 3 and oil-water separation tank 4;
[0027] The side of the coarse filtration tank 2, the fine filtration tank 3 and the oil-water separation tank 4 is provided with a flow guide pump 6 and a pressure measuring table 7, the inside of the coarse filtration tank 2 is provided with a bag filter assembly 8, the inside of the fine filtration tank 3 is provided with a folded filter core filter assembly 9, and the bottom of the oil-water separation tank 4 is provided with a filter membrane filter assembly 10;
[0028] The side of the oil-water separation tank 4 is provided with an oil outlet pipe 11, the filter membrane filter assembly 10 and the oil-water separation tank 4 are provided with a liquid outlet pipe 14, the liquid outlet pipe 14 is provided with a booster pump 12, and the bottom of the filter membrane filter assembly 10 is provided with a wastewater discharge pipe 13.
[0029] Specifically, by three groups of flow guide pipes 5 and flow guide pumps 6, the water source in the wastewater conditioning tank 1 is sequentially guided to the coarse filtration tank 2, the fine filtration tank 3 and the oil-water separation tank 4, the coarse filtration tank 2 is coarsely filtered by the bag filter assembly 8, then finely filtered by the folded filter core filter assembly 9 in the fine filtration tank 3, and finally oil-water separated by the oil-water separation tank 4, the wastewater is deposited at the bottom of the oil-water separation tank 4, is pressurized and guided to the filter membrane filter assembly 10 by the booster pump 12, is filtered by the membrane separation device, and is discharged by the liquid outlet pipe 14, the whole operation is stable, and the miniaturized integrated operation can be used;
[0030] The flow guide pump 6 can be pressurized and guided, the filtration pressure strength of the coarse filtration tank 2 and the fine filtration tank 3 can be measured in real time by the pressure measuring table 7, and the oil-water separation tank 4 is provided with an oil outlet pipe 11 at the top, the oil-water separator can remove most of the working liquid components in the wastewater, can reduce the load of the subsequent membrane separation device, can ensure the stable operation of the membrane separation device, can prolong the service life of the membrane, the oil outlet pipe 11 can collect and return the working liquid, can play a recycling role, can make the device small and convenient, can occupy small area, and has good working liquid recycling capacity, is convenient to use, and has excellent filtration quality.
[0031] Membrane is a material with selective separation function. The process of separating, purifying and concentrating different components of feed liquid by using the selective separation of membrane is called membrane separation. It is different from traditional filtration in that membrane can separate in the range of molecules, and the process is a physical process without phase change and addition of additives. The basic principle of membrane separation process is relatively simple. In the filtration process, the feed liquid is pressurized by a high-pressure pump, and the feed liquid flows along the surface of the filter membrane at a certain flow rate. The molecules larger than the molecular weight of the membrane cut-off do not penetrate the membrane and flow back to the feed tank. The substances or molecules smaller than the molecular weight of the membrane cut-off penetrate the membrane to form the dialysate. Therefore, the membrane system has two outlets, one is the return liquid concentrate outlet, and the other is the dialysate outlet. The amount of dialysate flowing out per unit time (Hr) per unit membrane area (m2) is called membrane flux (LMH), that is, the filtration speed. The factors affecting the membrane flux include temperature, pressure, total dissolved solids (TDS), ion concentration, viscosity, etc. Since the membrane separation process is a pure physical process, it has the characteristics of no phase change, energy saving, small volume, and can be separated, so the membrane is widely used in fermentation, pharmaceutical, plant extraction, chemical industry, water treatment process and environmental protection industry. For different compositions of organic matter, different membranes are selected according to the molecular weight of the organic matter, and appropriate membrane process is selected, so as to achieve the best membrane flux and retention rate, thereby improving the production yield, reducing the investment scale and operation cost.
[0032] Further, three groups of flow guide pipes 5 are sequentially arranged between the adjacent wastewater conditioning tanks 1, coarse filtration tanks 2, fine filtration tanks 3 and oil-water separation tanks 4, and the three groups of flow guide pipes 5 are in communication with the wastewater conditioning tanks 1, coarse filtration tanks 2, fine filtration tanks 3 and oil-water separation tanks 4 as a whole.
[0033] By arranging the flow guide pipes 5 to be sequentially arranged between the adjacent wastewater conditioning tanks 1, coarse filtration tanks 2, fine filtration tanks 3 and oil-water separation tanks 4, the wastewater can flow into the oil-water separation tank 4 from the wastewater conditioning tank 1, coarse filtration tank 2 and fine filtration tank 3 in sequence, so that the water source is guided and the filtration is stable.
[0034] Further, the flow guide pumps 6 and the pressure measuring tables 7 are sequentially arranged on the side surfaces of the coarse filtration tanks 2, fine filtration tanks 3 and oil-water separation tanks 4, and the side surface of the pressure measuring table 7 is provided with an alarm 15.
[0035] By arranging the flow guide pumps 6 and the pressure measuring tables 7 to be sequentially arranged on the side surfaces of the coarse filtration tanks 2, fine filtration tanks 3 and oil-water separation tanks 4, the three flow guide pumps 6 can respectively pressurize and guide the wastewater in the coarse filtration tanks 2, fine filtration tanks 3 and oil-water separation tanks 4, so that the wastewater filtration is stable, the filtration pressure intensity of the coarse filtration tanks 2 and fine filtration tanks 3 can be measured in real time by the pressure measuring tables 7, which is convenient for replacement, and the alarm 15 plays an auxiliary role for the pressure measuring table 7. When the pressure of the pressure measuring table 7 is too high, the alarm 15 can alarm, so as to remind the staff to replace the filter element, which is convenient to use.
[0036] Further, the cloth bag filter assembly 8 is a cloth bag filter, and the folded filter core filter assembly 9 is a folded filter core filter;
[0037] By setting the cloth bag filter assembly 8 as a cloth bag filter, stable cloth bag rough filtration can be carried out, and replacement is convenient. The folded filter core filter assembly 9 is a folded filter core filter, and stable fine filtration can be carried out, and the filtration quality is high.
[0038] Further, the liquid outlet pipe 14 is provided with a pressure measuring device 16, and the inside of the filter membrane filter assembly 10 is provided with a membrane separation device;
[0039] By setting the inside of the filter membrane filter assembly 10 with a membrane separation device, the membrane is a material with selective separation function. The process of separating, purifying and concentrating different components of the feed liquid by using the selective separation of the membrane is called membrane separation. The membrane separation device plays a good filtering and separating role, and the wastewater treatment effect is excellent. The pressure measuring device 16 plays a pressure detection role. When the membrane separation device is blocked due to too much dirt, the pressure test can be carried out by the pressure measuring device 16, so that replacement and reminding can be facilitated.
[0040] Further, the booster pump 12 is a high-pressure pump body;
[0041] By setting the booster pump 12 as a high-pressure pump body, the booster flow guiding effect is good, and the use is convenient.
[0042] Further, the top of the coarse filter tank 2 and the fine filter tank 3 is provided with an opening and closing cover plate 17, and the two opening and closing cover plates 17 are respectively hinged and sealed to the top of the coarse filter tank 2 and the fine filter tank 3;
[0043] By setting the opening and closing cover plate 17, the coarse filter tank 2 and the fine filter tank 3 can be easily opened, and the filter device inside the tank body can be replaced, and the use is convenient.
[0044] Further, the filtering precision of the cloth bag filter assembly 8 is 3-6um, and the filtering precision of the folded filter core filter assembly 9 is 0.5-1.2um;
[0045] The filtering precision of the cloth bag filter assembly 8 is 5um. When the inlet and outlet pressure of the cloth bag filter exceeds 0.3MPa, the filter top cover needs to be opened, and the filter bag of the filter needs to be replaced. The filtering precision of the folded filter core filter assembly 9 is 1um. When the inlet and outlet pressure of the folded filter core filter exceeds 0.3MPa, the filter top cover needs to be opened, and the folded filter core of the filter needs to be replaced. The pressure strength can be measured in real time by the pressure measuring table 7, and the device filtering operation is stable.
[0046] Working principle: by setting wastewater conditioning tank 1, coarse filter filter tank 2, fine filter filter tank 3 and oil-water separation tank 4 are connected by three groups of guide pipe 5, and three groups of guide pipe 5 are provided with guide pump 6 and pressure measuring table 7, three groups of guide pipe 5 and guide pump 6 guide the water source in wastewater conditioning tank 1 to coarse filter filter tank 2, fine filter filter tank 3 and oil-water separation tank 4 in turn, in the guide process, coarse filter filter tank 2 is coarse filtered by bag filter assembly 8, then fine filter filter tank 3 is fine filtered by folding filter core filter assembly 9, and finally oil-water separation tank 4 is oil-water separated, wastewater is deposited at the bottom of oil-water separation tank 4, is pressurized and guided to filter membrane filter assembly 10 by booster pump 12 and liquid outlet pipe 14, is filtered by membrane separation device, and is discharged by wastewater discharge pipe 13 for subsequent treatment, the device is stable in operation, can be miniaturized and integrated, is convenient for wastewater treatment, and is convenient to use;
[0047] Three groups of guide pipe 5, guide pump 6 and pressure measuring table 7 are correspondingly installed, three guide pumps 6 can respectively pressurize and guide wastewater of coarse filter filter tank 2, fine filter filter tank 3 and oil-water separation tank 4, so that wastewater filtration is stable, the filtering precision of bag filter assembly 8 is 5um, when the inlet and outlet pressure of the bag filter exceeds 0.3MPa, the filter top cover needs to be opened and the filter bag needs to be replaced, the filtering precision of folding filter core filter assembly 9 is 1um, when the inlet and outlet pressure of the folding filter core filter exceeds 0.3MPa, the filter top cover needs to be opened and the folding filter core of the filter needs to be replaced, the pressure strength can be measured in real time by pressure measuring table 7, the device is stable in filtration operation and convenient to use, the top of oil-water separation tank 4 is provided with oil outlet pipe 11, the oil-water separator can remove most of the working liquid components in wastewater, can reduce the load of the subsequent membrane separation device, ensure the stable operation of the membrane separation device, prolong the service life of the membrane, the working liquid can be collected and returned by oil outlet pipe 11, play a recycling role, reduce the waste of working liquid, make the device small and convenient, small in floor area, and good in working liquid recycling capacity, convenient to use, and excellent in filtering quality.
[0048] It is obvious to those skilled in the art that the present application is not limited to the details of the above exemplary embodiments, and the present application can be implemented in other specific forms without departing from the spirit or essential characteristics of the present application. Therefore, the embodiments should be regarded as exemplary and non-limiting, the scope of the present application is defined by the appended claims rather than the above description, and therefore all changes falling within the meaning and scope of the essential elements of the claims are intended to be included in the present application. Any reference signs in the claims should not be regarded as limiting the claims involved.
[0049] The above-described embodiments are only used to illustrate the technical solutions of the present application, and not to limit them; although the present application has been described in detail with reference to the foregoing embodiments, those skilled in the art should understand that they can still modify the technical solutions recorded in the foregoing embodiments, or make equivalent replacements for part of the technical features; and these modifications or replacements do not make the essence of the corresponding technical solutions deviate from the spirit and scope of the technical solutions of the embodiments of the present application.
Claims
1. A hydrogen peroxide wastewater treatment device comprising a wastewater conditioning tank (1), a coarse filtration filter tank (2), a fine filtration filter tank (3), and an oil-water separation tank (4), characterized by: Flow guide pipes (5) are arranged between the adjacent wastewater conditioning tanks (1), coarse filtration tanks (2), fine filtration tanks (3) and oil-water separation tanks (4); The side surfaces of the coarse filtration tanks (2), fine filtration tanks (3) and oil-water separation tanks (4) are respectively provided with flow guide pumps (6) and pressure measuring tables (7), the inner side of the coarse filtration tank (2) is provided with a cloth bag filter assembly (8), the inner side of the fine filtration tank (3) is provided with a folded filter core filter assembly (9), and the bottom of the subsequent connecting part of the oil-water separation tank (4) is provided with a filter membrane filter assembly (10); The top of the oil-water separation tank (4) is provided with an oil outlet pipe (11), the filter membrane filter assembly (10) and the oil-water separation tank (4) are provided with a liquid outlet pipe (14), the liquid outlet pipe (14) is provided with a booster pump (12), and the bottom of the filter membrane filter assembly (10) is provided with a wastewater discharge pipe (13).
2. The hydrogen peroxide wastewater treatment apparatus according to claim 1, characterized by: Three groups of the flow guide pipes (5) are arranged between the adjacent wastewater conditioning tanks (1), coarse filtration tanks (2), fine filtration tanks (3) and oil-water separation tanks (4) in sequence, and the three groups of the flow guide pipes (5) are in communication with the wastewater conditioning tanks (1), coarse filtration tanks (2), fine filtration tanks (3) and oil-water separation tanks (4).
3. The hydrogen peroxide wastewater treatment apparatus according to claim 1, characterized by: The flow guide pumps (6) and pressure measuring tables (7) are arranged on the side surfaces of the coarse filtration tanks (2), fine filtration tanks (3) and oil-water separation tanks (4) in sequence, and the side surface of the pressure measuring table (7) is provided with an alarm (15).
4. The hydrogen peroxide wastewater treatment apparatus according to claim 1, characterized by: The cloth bag filter assembly (8) is a cloth bag filter, and the folded filter core filter assembly (9) is a folded filter core filter.
5. The hydrogen peroxide wastewater treatment apparatus according to claim 1, characterized by: The liquid outlet pipe (14) is provided with a pressure measuring device (16), and the inner side of the filter membrane filter assembly (10) is provided with a membrane separation device.
6. The hydrogen peroxide wastewater treatment apparatus according to claim 1, characterized by: The booster pump (12) is a high-pressure pump body.
7. The hydrogen peroxide wastewater treatment apparatus according to claim 1, characterized by: The top of the coarse filtration tank (2) and the top of the fine filtration tank (3) are respectively provided with a switch cover plate (17) which is hingedly sealed.
8. The hydrogen peroxide wastewater treatment apparatus according to claim 1, characterized by: The filtering precision of the cloth bag filter assembly (8) is 3-6um, and the filtering precision of the folded filter core filter assembly (9) is 0.5-1.2um.