CN217265026U

CN217265026U - Ozone oxidation reaction tower

Info

Publication number: CN217265026U
Application number: CN202221429850.XU
Authority: CN
Inventors: 陈泓铭; 范杰
Original assignee: Shandong Yangfan Environmental Engineering Co ltd
Current assignee: Shandong Yangfan Environmental Engineering Co ltd
Priority date: 2022-06-08
Filing date: 2022-06-08
Publication date: 2022-08-23
Anticipated expiration: 2032-06-08

Abstract

The utility model discloses an ozone oxidation reaction tower, which belongs to the field of sewage treatment equipment and comprises a reaction tower body, wherein a guide plate is arranged inside the reaction tower body, the ozone oxidation reaction tower is provided with a spiral guide plate which can guide sewage to slowly flow into the reaction tower, meanwhile, the upper end of the guide plate is provided with an ozone pipe, the ozone pipe downwards sprays air in the flowing process of the sewage to ensure that the sewage can fully react with ozone when flowing, the spiral guide plate has the functions of increasing the flowing time of the sewage and the time of the ozone oxidation reaction, simultaneously, the lower end inside the reaction tower is provided with a rotating rod and a stirring rod, the inner part of the reaction tower is also provided with a gas conveying pipe and a gas outlet pipe, the ozone discharging device can release ozone when stirring the sewage to fully react with the sewage, thereby ensuring that the sewage can be fully cleaned, and simultaneously ensuring that the ozone can be fully utilized, no waste is caused, and the utility model is used.

Description

Ozone oxidation reaction tower

Technical Field

The utility model relates to a sewage treatment device field, more specifically say, relate to ozone oxidation reaction tower.

Background

The ozone oxidation reaction tower is a reaction device which utilizes ozone and sewage to carry out chemical reaction so as to treat the sewage.

The patent application with application number 201610358649.X relates to an operation method and device of ozone oxidation water treatment system, it is when handling sewage, because sewage and ozone all are in the inside of reaction tower, sewage and ozone are all by oneself reaction, it is difficult to guarantee that sewage and ozone fully react, once only inject sewage and ozone into the reaction tower simultaneously and react, lead to reaction time shorter, both contacts are abundant inadequately, cause the sewage clearance clean up inadequately, ozone utilization ratio is lower, be unfavorable for the use.

SUMMERY OF THE UTILITY MODEL

Problem to exist among the prior art, the utility model aims to provide an ozone oxidation reaction tower, it is provided with the spiral guide plate, can carry out the water conservancy diversion to sewage, make inside sewage slowly flows into the reaction tower, the upper end of guide plate is provided with the ozone pipe simultaneously, at the in-process that the sewage flows, the ozone pipe jets out downwards, make sewage can fully react with ozone when flowing, and the spiral guide plate has the time of increasing sewage flow, and with ozone oxidation reaction time's effect, the inside lower extreme of this reaction tower is provided with dwang and puddler simultaneously, its inside gas-supply pipe and outlet duct that still are provided with, it stirs sewage to have the assurance, with ozone release, comprehensively react with sewage, thereby guarantee that sewage can be cleared up comprehensively, can guarantee simultaneously that ozone is by make full use of, do not cause the waste, utilize and use.

In order to solve the above problems, the utility model adopts the following technical proposal.

An ozone oxidation reaction tower comprises a reaction tower body, wherein a guide plate is arranged in the reaction tower body, baffle plates are fixedly connected with two sides of the guide plate, an ozone pipe is arranged in the reaction tower body, a gas outlet hole is formed in the lower end of the ozone pipe, a water inlet and a gas inlet are formed in the upper left end of the reaction tower body, the water inlet is communicated with the guide plate, the gas inlet is communicated with the ozone pipe, a motor is arranged at the left end of the inner part of the reaction tower body, a rotating rod is fixedly connected with the right end of the motor, a stirring rod is fixedly connected with the outer surface of the rotating rod, a connecting pipe is connected with the right end of the reaction tower body, a gas pipe is rotatably connected with the left end of the inner part of the connecting pipe, gas outlet pipes are connected with the upper end and the lower end of the gas pipe, circular holes are formed in the gas pipe and the stirring rod, a silica gel block is arranged in the circular holes, the left lower extreme and the right lower extreme of reaction tower body all are provided with the delivery port, this ozone oxidation reaction tower is provided with the spiral guide plate, can carry out the water conservancy diversion to sewage, make sewage slowly flow into inside the reaction tower, the upper end of guide plate is provided with the ozone pipe simultaneously, in the in-process that the sewage flows, the ozone pipe jets out downwards, make sewage can fully react with ozone when flowing, and the spiral guide plate has the time of increasing sewage flow, and with ozone oxidation reaction time's effect, the inside lower extreme of this reaction tower is provided with dwang and puddler simultaneously, its inside gas-supply pipe and outlet duct still are provided with, it is when stirring sewage to have the assurance, release ozone, comprehensively react with sewage, thereby guarantee that sewage can be cleared up comprehensively, can guarantee that ozone is by make full use of simultaneously, do not cause the waste, utilize and use.

Further, the guide plate sets up to the heliciform, the ozone pipe passes through the dead lever to be fixed in the upper end of guide plate, the ozone pipe also sets up to the heliciform.

Furthermore, the height of the baffle is set to be five times of the thickness of the guide plate, and the baffle has the function of limiting sewage on the guide plate.

Further, the gas-supply pipe sets up the inside at the dwang, the outlet duct sets up the inside at the puddler.

Further, the silica gel piece is whole to be divided into four piecemeals, and forms a gap in the middle of four detached silica gel pieces, and the silica gel piece has the effect sealed with the circular port, prevents to take place sewage and gets into the phenomenon of outlet duct from the circular port, and the gap that forms simultaneously between four silica gel pieces does not influence out the release ozone.

Compared with the prior art, the utility model has the advantages of:

(1) this scheme is provided with the spiral guide plate, can carry out the water conservancy diversion to sewage, make sewage slowly flow into inside the reaction tower, the upper end of guide plate is provided with the ozone pipe simultaneously, at the in-process that the sewage flows, the ozone pipe jets out air downwards, make sewage can fully react with ozone when flowing, and the spiral guide plate has the time of increasing sewage flow, and with the effect of ozone oxidation reaction time, the inside lower extreme of this reaction tower is provided with dwang and puddler simultaneously, its inside gas-supply pipe and outlet duct still are provided with, it is when stirring sewage to have the assurance, with ozone release, react comprehensively with sewage, thereby guarantee that sewage can be cleared up comprehensively, can guarantee simultaneously that ozone is by make full use of, it is extravagant not to cause, the utilization is used.

(2) The guide plate is arranged in a spiral shape, so that the flow time of the sewage is prolonged, and the reaction time of the sewage and the ozone is prolonged.

(3) Through the setting of baffle, have with sewage restriction on the guide plate, by the effect of guide plate drainage to prevent that sewage from overflowing the baffle, inside direct inflow reaction tower body.

(4) The ozone pipe is arranged at the upper end of the guide plate, so that the sewage and the ozone can be ensured to fully react.

(5) Through being provided with gas-supply pipe and outlet duct in dwang and puddler for the puddler can let in inside sewage with ozone when stirring sewage, fully reacts with sewage.

Drawings

Fig. 1 is a schematic view of the overall structure of the present invention;

fig. 2 is a top view of the deflector of the present invention;

FIG. 3 is a schematic view of a stirring rod of the present invention;

FIG. 4 is an enlarged view taken at A of FIG. 1;

fig. 5 is an enlarged view of fig. 1 at B.

The reference numbers in the figures illustrate:

1 reaction tower body, 2 guide plates, 3 baffles, 4 ozone pipes, 5 air outlets, 6 water inlets, 7 air inlets, 8 motors, 9 rotating rods, 10 stirring rods, 11 connecting pipes, 12 air conveying pipes, 13 air outlet pipes, 14 circular holes, 15 silica gel blocks and 16 water outlets.

Detailed Description

The technical solution in the embodiment of the present invention will be clearly and completely described below with reference to the accompanying drawings in the embodiment of the present invention; obviously, the described embodiments are only a part of the embodiments of the present invention, and not all embodiments, and all other embodiments obtained by those skilled in the art without any inventive work are within the scope of the present invention based on the embodiments of the present invention.

Referring to fig. 1-5, an ozone oxidation reaction tower comprises a reaction tower body 1, referring to fig. 1-5, a guide plate 2 is arranged inside the reaction tower body 1, the guide plate 2 has a function of guiding sewage to flow, baffle plates 3 are fixedly connected to both sides of the guide plate 2, an ozone tube 4 is arranged inside the reaction tower body 1, the ozone tube 4 has a function of transporting ozone, an air outlet 5 is arranged at the lower end of the ozone tube 4, the air outlet 5 has a function of releasing ozone, a water inlet 6 and an air inlet 7 are arranged at the left upper end of the reaction tower body 1, the water inlet 6 is communicated with the guide plate 2, the air inlet 7 is communicated with the ozone tube 4, a motor 8 is arranged at the left end inside the reaction tower body 1, the motor 8 belongs to the prior art, and has a function of driving a rotating rod 9 and a stirring rod 10 to rotate, a rotating rod 9 is fixedly connected to the right end of the motor 8, outer fixed surface of dwang 9 is connected with puddler 10, puddler 10 has the effect of stirring sewage, the right-hand member of reaction tower body 1 is connected with connecting pipe 11, the inside left end of connecting pipe 11 is rotated and is connected with gas-supply pipe 12, be connected with the rotation of connecting pipe 11 through gas-supply pipe 12, make dwang 9 when rotating, can drive gas-supply pipe 12 at 11 internal rotations of connecting pipe, and do not hinder gas-supply pipe 12 and transport ozone, the upper and lower both ends of gas-supply pipe 12 are connected with outlet duct 13, gas-supply pipe 12 and puddler 10 are provided with circular port 14, circular port 14 has the effect with the ozone release, circular port 14's inside is provided with silica gel piece 15, reaction tower body 1's left lower extreme and right lower extreme all are provided with delivery port 16, delivery port 16 has the effect of the sewage discharge of accomplishing the clearance.

Please refer to fig. 1 and fig. 2, the guide plate 2 sets up to the heliciform, ozone pipe 4 is fixed in the upper end of guide plate 2 through the dead lever, ozone pipe 4 also sets up to the heliciform, through setting up guide plate 2 to the heliciform, the effect that has the time of increasing the sewage flow, because ozone pipe 4 sets up the upper end at guide plate 2, so when sewage flows, ozone pipe 4 releases ozone, carry out oxidation reaction with sewage, the height of baffle 3 sets up to the quintuple of guide plate 2 thickness, baffle 3 has with sewage restriction on guide plate 2, prevent that sewage from taking place and cross baffle 3, the effect of the inside phenomenon of direct inflow reaction tower body 1.

Please refer to fig. 3 and 5, gas-supply pipe 12 sets up the inside at dwang 9, outlet duct 13 sets up the inside at puddler 10, through setting up gas-supply pipe 12 and outlet duct 13 respectively in the inside of dwang 9 and puddler 10, make puddler 10 when stirring sewage, can release ozone, thereby guarantee sewage and ozone fully react, silica gel piece 15 wholly divide into four piecemeals, and form a gap in the middle of four detached silica gel pieces 15, silica gel piece 15 has the effect sealed with circular port 14, prevent to take place sewage and get into the inside phenomenon of outlet duct 13 from circular port 14, the gap that forms between four silica gel pieces 15 simultaneously, when letting in ozone, because the effect of air current, can strut the gap, release ozone.

When the ozone oxidation reaction tower is used, ozone is simultaneously introduced into an ozone pipe 4 and a gas conveying pipe 12, sewage is introduced into a guide plate 2, a motor 8 is started, at the moment, the sewage flows into the guide plate 2 through a water inlet 6, the guide plate 2 guides the sewage, the sewage flows downwards to the bottom of a reaction tower body 1 in a rotating manner, meanwhile, the ozone flows into the ozone pipe 4 through a gas inlet 7, a gas outlet 5 arranged at the lower end of the ozone pipe 4 releases the ozone, the sewage can react with the ozone when flowing on the surface of the guide plate 2, the spiral guide plate 2 has the functions of increasing the sewage flowing time and increasing the sewage and ozone reaction time, so that the sewage and the ozone have sufficient time to react, after the sewage is guided to flow to the bottom of the reaction tower body 1 by the guide plate 2, the motor 8 drives a rotating rod 9 and a stirring rod 10 to rotate, and the stirring rod 10 stirs the sewage, simultaneously let in ozone in the inside outlet duct 13 of puddler 10, ozone flows and strikes silica gel piece 15, make the gap between the silica gel piece 15 strutted, ozone flows, mix into inside the sewage, fully react with sewage, after the reaction is accomplished, sewage flows from delivery port 16, if there is the ozone that has not used up in reaction tower body 1 inside, then can use the trachea of air pump through reaction tower body 1 upper end, take ozone out and store, wait for next use, and the operation is simple, and can guarantee sewage and ozone fully reaction, utilize and use.

The above description is only the preferred embodiment of the present invention; the scope of the present invention is not limited thereto. Any person skilled in the art should also be able to cover the technical scope of the present invention by replacing or changing the technical solution and the improvement concept of the present invention with equivalents and modifications within the technical scope of the present invention.

Claims

1. Ozone oxidation reaction tower, including reaction tower body (1), its characterized in that: the reaction tower comprises a reaction tower body (1), wherein a guide plate (2) is arranged in the reaction tower body (1), baffle plates (3) are fixedly connected to two sides of the guide plate (2), an ozone pipe (4) is arranged in the reaction tower body (1), an air outlet hole (5) is formed in the lower end of the ozone pipe (4), a water inlet (6) and an air inlet (7) are arranged at the upper left end of the reaction tower body (1), the water inlet (6) is communicated with the guide plate (2), the air inlet (7) is communicated with the ozone pipe (4), a motor (8) is arranged at the left inner end of the reaction tower body (1), a rotating rod (9) is fixedly connected to the right end of the motor (8), a stirring rod (10) is fixedly connected to the outer surface of the rotating rod (9), a connecting pipe (11) is connected to the right end of the reaction tower body (1), and a gas conveying pipe (12) is rotatably connected to the left end of the connecting pipe (11), the upper end and the lower end of the gas pipe (12) are connected with gas outlet pipes (13), the gas pipe (12) and the stirring rod (10) are provided with circular holes (14), a silica gel block (15) is arranged inside the circular holes (14), and the left lower end and the right lower end of the reaction tower body (1) are provided with water outlets (16).

2. The ozonation reaction tower of claim 1, wherein: the utility model discloses an ozone generator, including guide plate (2), ozone pipe (4), fixed pole, ozone pipe (4) are fixed in the upper end of guide plate (2), the guide plate (2) sets up to the heliciform, ozone pipe (4) also set up to the heliciform.

3. The ozonation reaction tower of claim 1, wherein: the height of the baffle (3) is set to be five times of the thickness of the guide plate (2).

4. The ozonation reaction tower of claim 1, wherein: the gas transmission pipe (12) is arranged in the rotating rod (9), and the gas outlet pipe (13) is arranged in the stirring rod (10).

5. The ozonation reaction tower of claim 1, wherein: the silicon rubber block (15) is integrally divided into four sub-blocks, and a gap is formed between the four sub-blocks (15).