CN216336806U - Sodium hypochlorite reactor - Google Patents
Sodium hypochlorite reactor Download PDFInfo
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- CN216336806U CN216336806U CN202123131702.8U CN202123131702U CN216336806U CN 216336806 U CN216336806 U CN 216336806U CN 202123131702 U CN202123131702 U CN 202123131702U CN 216336806 U CN216336806 U CN 216336806U
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- sodium hypochlorite
- inlet pipe
- neutralization
- feed liquor
- neutralization tank
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Abstract
The utility model provides a sodium hypochlorite reactor, includes cylindric neutralization tank, is equipped with the glass steel inside lining in the cylindric neutralization tank, by supreme sodium hypochlorite feed liquor pipe, neutralization solution feed liquor pipe and the fluid-discharge tube of being equipped with in proper order down on the lateral wall of cylindric neutralization tank, the axle center of cylindric neutralization tank is deviated in the export of sodium hypochlorite feed liquor pipe, and neutralization solution feed liquor pipe and sodium hypochlorite feed liquor pipe are the glass steel pipeline. The utility model has the advantages that: sodium hypochlorite sewage and neutralization solution in the neutralization pond enter into cylindric neutralization tank together and discharge after mixing by oneself, and cylindric neutralization tank, sodium hypochlorite feed liquor pipe and neutralization solution feed liquor pipe are the glass steel material, effectively prevent to corrode, increase life, reduce the unplanned number of times of stopping.
Description
Technical Field
The utility model relates to the technical field of sewage treatment, in particular to a sodium hypochlorite reactor.
Background
At present, sewage treatment sodium hypochlorite all is the direct neutralization pond outlet conduit that gets into in the ammonium phosphate workshop production, and at this in-process, because of sodium hypochlorite corrosivity is strong, and is serious to sodium hypochlorite exit linkage neutralization pond outlet conduit corrosion, uses for a long time and causes the pipeline to break easily, and the polluted environment need shut down and weld the restoration to the pipeline, increases the unplanned parking, influences production efficiency.
SUMMERY OF THE UTILITY MODEL
The present invention aims to provide a sodium hypochlorite reactor for overcoming the above disadvantages.
The sodium hypochlorite neutralizing tank comprises a cylindrical neutralizing tank, wherein a glass fiber reinforced plastic lining is arranged in the cylindrical neutralizing tank, a sodium hypochlorite liquid inlet pipe, a neutralizing liquid inlet pipe and a liquid discharge pipe are sequentially arranged on the side wall of the cylindrical neutralizing tank from bottom to top, the outlet of the sodium hypochlorite liquid inlet pipe deviates from the axis of the cylindrical neutralizing tank, and the neutralizing liquid inlet pipe and the sodium hypochlorite liquid inlet pipe are glass fiber reinforced plastic pipelines.
The bottom of the cylindrical neutralization tank is hemispherical, and the sodium hypochlorite liquid inlet pipe is positioned on the hemispherical surface.
The hemispherical bottom of the cylindrical neutralization tank is provided with an emptying pipe, and the emptying pipe is provided with a valve.
One end of the neutralizing liquid inlet pipe extends into the cylindrical neutralizing tank, and the liquid outlet direction of the neutralizing liquid inlet pipe is downward.
The liquid outlet of the neutralization liquid inlet pipe is positioned right above the liquid outlet of the sodium hypochlorite liquid inlet pipe.
The cylindrical neutralizing tank is divided into two parts by a glass fiber reinforced plastic flow equalizing plate.
The glass fiber reinforced plastic flow equalizing plate is vertically arranged in the cylindrical neutralizing tank, the neutralizing liquid inlet pipe and the sodium hypochlorite inlet pipe are positioned on the same side of the glass fiber reinforced plastic flow equalizing plate, and the liquid discharge pipe is positioned on the other side of the glass fiber reinforced plastic flow equalizing plate.
The glass fiber reinforced plastic flow equalizing plate is transversely installed in the cylindrical neutralizing tank and is positioned between the neutralizing liquid inlet pipe and the liquid outlet pipe.
The opening direction of the sodium hypochlorite liquid inlet pipe faces to the tangential direction of the cylindrical neutralization tank.
The diameter of the sodium hypochlorite liquid inlet pipe is smaller than that of the neutralization solution liquid inlet pipe.
The utility model has the advantages that: sodium hypochlorite sewage and neutralization solution in the neutralization pond enter into cylindric neutralization tank together and discharge after mixing by oneself, and cylindric neutralization tank, sodium hypochlorite feed liquor pipe and neutralization solution feed liquor pipe are the glass steel material, effectively prevent to corrode, increase life, reduce the unplanned number of times of stopping.
Description of the drawings
FIG. 1 is a schematic diagram of the present invention.
Fig. 2 is a schematic view of the internal structure of the present invention.
FIG. 3 is a schematic structural view of a second installation mode of the flow equalizing plate made of glass fiber reinforced plastics.
Detailed Description
In order to make the objects, technical solutions and advantages of the embodiments of the present invention clearer, the technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are some, but not all, embodiments of the present invention. The components of embodiments of the present invention generally described and illustrated in the figures herein may be arranged and designed in a wide variety of different configurations.
Thus, the following detailed description of the embodiments of the present invention, presented in the figures, is not intended to limit the scope of the utility model, as claimed, but is merely representative of selected embodiments of the utility model. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention. It should be noted that: like reference numbers and letters refer to like items in the following figures, and thus, once an item is defined in one figure, it need not be further defined and explained in subsequent figures.
In the description of the embodiments of the present invention, it should be noted that, if the terms "upper", "lower", "inside", "outside", etc. are used for indicating the orientations or positional relationships based on the orientations or positional relationships shown in the drawings or the orientations or positional relationships that the products of the present invention usually place when using, the present invention is only used for convenience of description and simplification of the description, but does not indicate or imply that the devices or elements indicated must have specific orientations, be constructed in specific orientations, and operate, and thus, the present invention should not be construed as being limited. Furthermore, the appearances of the terms "first," "second," and the like in the description of the present invention are only used for distinguishing between the descriptions and are not intended to indicate or imply relative importance.
In the description of the embodiments of the present invention, it should be further noted that unless otherwise explicitly stated or limited, the terms "disposed" and "connected" should be interpreted broadly, and may be, for example, fixedly connected, detachably connected, or integrally connected; can be mechanically or electrically connected; they may be connected directly or indirectly through intervening media, or they may be interconnected between two elements. The specific meanings of the above terms in the present invention can be understood in specific cases to those skilled in the art.
As shown in the attached drawing, the sodium hypochlorite neutralizing tank comprises a cylindrical neutralizing tank 1, a glass fiber reinforced plastic lining is arranged in the cylindrical neutralizing tank 1, a sodium hypochlorite liquid inlet pipe 2, a neutralizing liquid inlet pipe 3 and a liquid discharge pipe 4 are sequentially arranged on the side wall of the cylindrical neutralizing tank 1 from bottom to top, the outlet of the sodium hypochlorite liquid inlet pipe 2 deviates from the axis of the cylindrical neutralizing tank 1, and the neutralizing liquid inlet pipe 3 and the sodium hypochlorite liquid inlet pipe 2 are glass fiber reinforced plastic pipelines.
The hemispherical bottom of the cylindrical neutralization tank 1 is provided with an emptying pipe 6, and the emptying pipe 6 is provided with a valve, so that liquid in the cylindrical neutralization tank 1 can be emptied when the machine is stopped and maintained.
One end of the neutralizing liquid inlet pipe 3 extends into the cylindrical neutralizing tank 1, and the liquid outlet direction of the neutralizing liquid inlet pipe 3 is downward; the liquid outlet of the neutralization liquid inlet pipe 3 is positioned right above the liquid outlet of the sodium hypochlorite liquid inlet pipe 2. So that the neutralization solution enters and generates downward potential energy and sodium hypochlorite enters and generates forward potential energy to collide, and the mixing efficiency is improved.
The cylindrical neutralization tank 1 is divided into two parts by the glass fiber reinforced plastic flow equalizing plate 7, and the mixed liquid is subjected to secondary dispersion mixing when passing through the glass fiber reinforced plastic flow equalizing plate 7, so that the mixing efficiency is improved.
The first installation mode of the glass fiber reinforced plastic flow equalizing plate 7 is as follows: the glass fiber reinforced plastic flow equalizing plate 7 is vertically arranged in the cylindrical neutralizing tank 1, the neutralizing liquid inlet pipe 3 and the sodium hypochlorite inlet pipe 2 are positioned on the same side of the glass fiber reinforced plastic flow equalizing plate 7, and the liquid discharge pipe 4 is positioned on the other side of the glass fiber reinforced plastic flow equalizing plate 7.
The second installation mode of the glass fiber reinforced plastic flow equalizing plate 7 is as follows: the glass fiber reinforced plastic flow equalizing plate 7 is transversely installed in the cylindrical neutralizing tank 1, and the glass fiber reinforced plastic flow equalizing plate 7 is positioned between the neutralizing liquid inlet pipe 3 and the liquid outlet pipe 4.
The opening direction of the sodium hypochlorite liquid inlet pipe 2 faces the tangential direction of the cylindrical neutralization tank 1, and the flowing speed in the cylindrical neutralization tank 1 is increased to the greatest extent when the sodium hypochlorite enters.
The diameter of sodium hypochlorite feed liquor pipe 2 is less than the diameter of neutralization solution feed liquor pipe 3, improves the impact force when sodium hypochlorite enters.
The working mode and principle are as follows: neutralization pond is connected to 3 one ends of neutralization liquid feed liquor pipe, and in discharging the neutralization liquid in the neutralization pond into cylindric neutralization jar 1, then discharge from fluid-discharge tube 4 again, when sodium hypochlorite sewage discharge, open sodium hypochlorite feed liquor pipe 2's valve, sodium hypochlorite enters into cylindric neutralization jar 1 from sodium hypochlorite feed liquor pipe 2 in, because the export of sodium hypochlorite feed liquor pipe 2 deviates from the axle center of cylindric neutralization jar 1, the kinetic energy when liquid flows in can make the interior solution of cylindric neutralization jar 1 rotate, play the mixing action by oneself, the sewage after the intensive mixing reaction is discharged from fluid-discharge tube 4 together.
Claims (10)
1. The utility model provides a sodium hypochlorite reactor, it includes cylindric neutralization tank (1) its characterized in that, is equipped with the glass steel inside lining in cylindric neutralization tank (1), is equipped with sodium hypochlorite feed liquor pipe (2), neutralization solution feed liquor pipe (3) and fluid-discharge tube (4) by supreme down on the lateral wall of cylindric neutralization tank (1) in proper order, and the axle center of cylindric neutralization tank (1) is deviated in the export of sodium hypochlorite feed liquor pipe (2), and neutralization solution feed liquor pipe (3) and sodium hypochlorite feed liquor pipe (2) are the glass steel pipeline.
2. Sodium hypochlorite reactor according to claim 1, characterized in that the bottom of the cylindrical neutralization tank (1) is hemispherical, and the sodium hypochlorite inlet pipe (2) is located on the hemispherical surface.
3. Sodium hypochlorite reactor according to claim 2, characterized in that the cylindrical neutralization tank (1) is provided with a vent (6) at its hemispherical bottom and that the valve is provided on the vent (6).
4. Sodium hypochlorite reactor according to claim 1, characterized in that one end of the neutralizing liquid inlet pipe (3) extends into the cylindrical neutralizing tank (1), and the outlet of the neutralizing liquid inlet pipe (3) is directed downwards.
5. Sodium hypochlorite reactor according to claim 4, characterized in that the outlet of the inlet pipe (3) of the neutralizing solution is located directly above the outlet of the inlet pipe (2) of sodium hypochlorite.
6. Sodium hypochlorite reactor according to claim 1, characterized in that the cylindrical neutralization tank (1) is divided into two parts by a glass fiber reinforced plastic flow equalizing plate (7).
7. Sodium hypochlorite reactor according to claim 6, characterized in that the glass fiber reinforced plastic flow equalizing plate (7) is vertically installed in the cylindrical neutralizing tank (1), the neutralizing liquid inlet pipe (3) and the sodium hypochlorite inlet pipe (2) are located on the same side of the glass fiber reinforced plastic flow equalizing plate (7), and the liquid outlet pipe (4) is located on the other side of the glass fiber reinforced plastic flow equalizing plate (7).
8. Sodium hypochlorite reactor according to claim 6, characterized in that the glass fiber reinforced plastic flow equalizing plate (7) is installed transversely inside the cylindrical neutralization tank (1), the glass fiber reinforced plastic flow equalizing plate (7) being located between the inlet pipe (3) and the outlet pipe (4) of the neutralization solution.
9. Sodium hypochlorite reactor according to claim 1, characterized in that the opening direction of the sodium hypochlorite inlet pipe (2) is directed to the tangential direction of the cylindrical neutralization tank (1).
10. Sodium hypochlorite reactor according to claim 1, characterised in that the diameter of the sodium hypochlorite inlet pipe (2) is smaller than the diameter of the neutralisation solution inlet pipe (3).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN202123131702.8U CN216336806U (en) | 2021-12-14 | 2021-12-14 | Sodium hypochlorite reactor |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202123131702.8U CN216336806U (en) | 2021-12-14 | 2021-12-14 | Sodium hypochlorite reactor |
Publications (1)
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CN216336806U true CN216336806U (en) | 2022-04-19 |
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CN202123131702.8U Active CN216336806U (en) | 2021-12-14 | 2021-12-14 | Sodium hypochlorite reactor |
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CN (1) | CN216336806U (en) |
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2021
- 2021-12-14 CN CN202123131702.8U patent/CN216336806U/en active Active
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