CN215712350U - Many first integrated devices of sewage treatment - Google Patents

Many first integrated devices of sewage treatment Download PDF

Info

Publication number
CN215712350U
CN215712350U CN202121332598.6U CN202121332598U CN215712350U CN 215712350 U CN215712350 U CN 215712350U CN 202121332598 U CN202121332598 U CN 202121332598U CN 215712350 U CN215712350 U CN 215712350U
Authority
CN
China
Prior art keywords
device body
gas
liquid
sewage treatment
filter screen
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN202121332598.6U
Other languages
Chinese (zh)
Inventor
吴偲
崔荣煜
梅若心
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Jiangsu Environmental Protection Industry Ltd By Share Ltd
Original Assignee
Jiangsu Environmental Protection Industry Ltd By Share Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Jiangsu Environmental Protection Industry Ltd By Share Ltd filed Critical Jiangsu Environmental Protection Industry Ltd By Share Ltd
Priority to CN202121332598.6U priority Critical patent/CN215712350U/en
Application granted granted Critical
Publication of CN215712350U publication Critical patent/CN215712350U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Treatment Of Water By Oxidation Or Reduction (AREA)

Abstract

The utility model discloses a sewage treatment multi-element integrated device which comprises a device body, wherein a gas-liquid mixing component, an activated carbon filter screen and a catalytic oxidation component are arranged in the device body from bottom to top, the catalytic oxidation component comprises a plurality of ultraviolet light catalytic plates, the ultraviolet light catalytic plates are arranged on the side wall of the device body at a certain angle, a channel for sewage to flow is formed between the ultraviolet light catalytic plates, a plurality of catalyst plates are arranged between the ultraviolet light catalytic plates, a spray head for introducing ozone is arranged on the side wall of the device body, the spray head is positioned between the ultraviolet light catalytic plates, and the activated carbon filter screen divides the interior of the device body into a mixing area and a reaction area. The structure layout of the utility model enables the waste liquid to be mixed with ozone and a catalyst and to be catalytically oxidized to the maximum extent, greatly improves the catalytic oxidation efficiency of the waste liquid, and has simple structure and simple and convenient operation.

Description

Many first integrated devices of sewage treatment
Technical Field
The utility model belongs to the technical field of gas-liquid reaction equipment, and particularly relates to a sewage treatment multielement integrated device.
Background
In the process of treating the industrial waste liquid, the source of the industrial waste liquid is various, so that the industrial waste liquid has the characteristics of more complex composition, high decomposition difficulty, toxicity, acidity or alkalinity and the like, and the evolution treatment difficulty is high. Currently, ozone oxidation technology, photocatalytic oxidation, Fenton oxidation and the like are commonly used, a single treatment technology has large limitation and needs to be matched with other treatment technologies for common treatment, but in the actual treatment process, the mixing degree and the reaction efficiency of ozone, a catalyst and industrial waste liquid in a reaction container are low, so that the evolution efficiency of the waste liquid is low, the waste liquid cannot be rapidly catalyzed and oxidized, and the emission standard is reached. And the existing equipment needs to realize the common treatment process by combination, so that the energy consumption rate is increased, the operation is complex, and the management difficulty is high.
SUMMERY OF THE UTILITY MODEL
In order to overcome the defects of the prior art, the utility model aims to provide a multi-element integrated device for sewage treatment, and aims to solve the problems that in the prior art, the evolution efficiency of waste liquid is low, the waste liquid cannot be subjected to rapid catalytic oxidation, and the emission standard is reached due to the low mixing degree and low reaction efficiency of ozone, a catalyst and the waste liquid in a reaction container. And the prior equipment needs to realize the common treatment process by combination, thereby increasing the energy consumption rate, having complex operation and high management difficulty.
The utility model is realized by adopting the following technical scheme:
the utility model provides a many units integrated device of sewage treatment, includes the device body, inside gas-liquid mixture component, active carbon filter screen and the catalytic oxidation component of being provided with from bottom to top of device body, the catalytic oxidation component includes a plurality of photocatalysis boards, the photocatalysis board is certain angle and installs on device body lateral wall, and forms the passageway that supplies the sewage circulation between the photocatalysis board, be provided with a plurality of catalyst boards between the photocatalysis board, the shower nozzle that is used for letting in ozone is installed to device body lateral wall, the shower nozzle is located between the photocatalysis board, the active carbon filter screen divides device body inside into mixed area and reaction zone.
In order to optimize the technical scheme, the specific measures adopted further comprise:
further, be provided with the stirring component between active carbon filter screen and the gas-liquid mixture component, the stirring component includes a plurality of puddlers, puddler fixed mounting is in the pivot, the pivot has step motor through the coupling joint, step motor fixed mounting is on device body lateral wall.
Further, the gas-liquid mixing component comprises a gas-liquid mixing cavity and a nozzle, the gas-liquid mixing cavity is provided with a gas inlet, a liquid inlet and a flow stabilizing port, the nozzle is fixed on the base of the catalytic oxidation filtering chamber through a substrate, and the nozzle is connected with the flow stabilizing port.
Further, a solid catalyst is distributed on the catalyst plate, and the pore diameter of the catalyst plate is smaller than that of the solid catalyst.
Furthermore, adjacent photocatalytic plates are respectively and fixedly installed on the symmetrical side walls of the device body, and the catalyst plates and the horizontal plane form an acute angle of 30 degrees in an inclined upward direction to form a flow channel for sewage to pass through from bottom to top.
Further, a gas-liquid separation piece is installed above the catalytic oxidation component, an air outlet hole is formed in the top end of the device body, and a water outlet hole is formed in the side wall of the device body.
Further, the gas-liquid separation spare includes the gas-liquid filter screen, the gas-liquid filter screen passes through support fixed mounting at this internally at the device, the gas-liquid filter screen outer lane is provided with out the water weir, it is located one side of device body inner wall to go out the water weir, it communicates with the apopore to go out the water weir.
Further, the lower end of the device body is provided with a rotating wheel.
The utility model has the beneficial effects that:
compared with the prior art, the sewage evolution analysis device is divided into a plurality of treatment chambers, firstly, the stirring rod is matched with ozone to preliminarily stir and mix the waste liquid, the oxygen content in the waste liquid is improved, then, the time and the area of contact reaction between the waste liquid and the catalyst plates are increased through a flow channel formed by the catalyst plates, meanwhile, in the catalytic oxidation process, the ozone is continuously supplemented, the catalyst plates are matched to keep the highest catalytic oxidation efficiency constantly, the flow direction of the waste liquid and the structural layout of each treatment chamber enable the waste liquid to be mixed with the ozone and the catalyst to the maximum degree and to be subjected to catalytic oxidation, the catalytic oxidation efficiency of the waste liquid is greatly improved, the structure is simple, and the operation is simple and convenient.
Drawings
FIG. 1 is a schematic structural view of an integrated device of the present invention.
The reference signs are: the device comprises a device body 10, an air outlet 11, a water outlet 12, a rotating wheel 20, a gas-liquid mixing component 30, a gas-liquid mixing cavity 31, an air inlet 311, a liquid inlet 312, a flow stabilizing port 313, a nozzle 32, a substrate 33, an activated carbon filter screen 40, a catalytic oxidation component 50, an ultraviolet light catalytic plate 51, a catalyst plate 52, a spray head 53, a stirring component 60, a stirring rod 61, a rotating shaft 62, a coupling 63, a stepping motor 64, a gas-liquid separating component 70, a gas-liquid filter screen 71, a support 72 and a water outlet weir 73.
Detailed Description
In order to clarify the technical solution and working principle of the present invention, the present invention is further described in detail with reference to the following embodiments in conjunction with the accompanying drawings, it should be noted that, without conflict, the embodiments or technical features described below may be combined to form a new embodiment.
The utility model provides a sewage treatment multi-element integrated device as shown in figure 1, which comprises a device body 10 and a rotating wheel 20 arranged at the lower end of the device body 10, wherein a gas-liquid mixing component 30, an activated carbon filter screen 40 and a catalytic oxidation component 50 are arranged in the device body 10 from bottom to top, and the activated carbon filter screen 40 divides the interior of the device body 10 into a mixing area a and a reaction area b from bottom to top.
The gas-liquid mixing component 30 comprises a gas-liquid mixing cavity 31 and a nozzle 32, wherein the gas-liquid mixing cavity 31 is provided with a gas inlet 311, a liquid inlet 312 and a steady flow port 313, sewage is introduced from the liquid inlet 312, a strong oxygen agent such as ozone is introduced from the gas inlet 311, then the sewage flows out of the steady flow port 313, the nozzle 32 is fixed on a base of the device body 10 through a substrate 33, the nozzle 32 is connected with the steady flow port 313, and the mixed sewage is sprayed into a mixing area a through the nozzle 32.
Be provided with stirring component 60 between active carbon filter screen 40 and the gas-liquid mixture component 30, stirring component 60 includes a plurality of puddlers 61, puddler 61 fixed mounting is on pivot 62, pivot 62 is connected with step motor 64 through shaft coupling 63, step motor 64 fixed mounting is on the device body 10 lateral wall. Stirring is constantly carried out on the sewage through the stirring rod 61, so that the ozone is further fully mixed and dissolved with the sewage, and a preliminary ozone catalytic oxidation process is realized.
Catalytic oxidation component 50 includes a plurality of parallel arrangement's ultraviolet catalysis board 51, and is adjacent ultraviolet catalysis board 51 is fixed mounting respectively on the lateral wall of device body 10 symmetry, and ultraviolet catalysis board 51 and horizontal plane become the acute angle of 30 degrees slopes, forms the current runner of confession sewage from bottom to top, be provided with a plurality of catalyst boards 52 between the ultraviolet catalysis board 51, the last distribution of catalyst board 52 has solid catalyst, catalyst board 52's aperture is less than solid catalyst's aperture, can prevent that solid catalyst from coming off from catalyst board 52, the shower nozzle 53 that is used for letting in ozone is installed to device body 10 lateral wall, shower nozzle 53 is located between the ultraviolet catalysis board 51. Utilize the passageway that ultraviolet catalysis board 51 formed, can increase sewage catalytic oxidation's degree, cooperation catalyst board 52 has improved catalytic oxidation's efficiency simultaneously greatly, through the ozone that lets in continuously, can keep the oxygen content in the sewage, keeps catalytic oxidation's efficiency.
The catalytic oxidation component 50 top is provided with gas-liquid separation spare 70, the venthole 11 has been seted up on the top of device body 10, apopore 12 has been seted up to device body 10 lateral wall, gas-liquid separation spare 70 includes gas-liquid filter screen 71, gas-liquid filter screen 71 passes through support 72 fixed mounting in device body 10, the gas-liquid filter screen 61 outer lane is provided with out weir 73, it is located one side of device body 10 inner wall to go out weir 73, it communicates with apopore 12 to go out weir 73.
The working principle of the utility model is as follows:
firstly, respectively introducing ozone and sewage from an air inlet 311 and a liquid inlet 312, then uniformly mixing in the gas-liquid mixing cavity 31, spraying the mixture into the mixing region a from a steady flow port 313 through a nozzle, and continuously stirring through a stirring rod 61 to carry out a preliminary ozone oxidation process; then the sewage goes upward, passes through a flow channel formed between the ultraviolet light catalysis plates 51, is combined with the solid catalyst on the catalyst plate 52 to carry out full reaction, and simultaneously, a spray nozzle 54 between the ultraviolet light catalysis plates 51 can be opened, ozone is introduced, the oxygen content in the water is increased, and the high efficiency of catalytic oxidation is kept constantly; finally, the gas after catalytic oxidation is discharged through the gas outlet 11, and the evolved sewage flows into the water outlet 12 through the water outlet weir 73 and is discharged.
The above is only a preferred embodiment of the present invention, and the protection scope of the present invention is not limited to the above-mentioned embodiments, and all technical solutions belonging to the idea of the present invention belong to the protection scope of the present invention. It should be noted that modifications and embellishments within the scope of the utility model may be made by those skilled in the art without departing from the principle of the utility model.

Claims (8)

1. The utility model provides a many unit integrated device of sewage treatment which characterized in that: including the device body, inside gas-liquid mixture component, activated carbon filter screen and the catalytic oxidation component of being provided with from bottom to top of device body, the catalytic oxidation component includes a plurality of ultraviolet catalysis boards, the ultraviolet catalysis board is certain angle and installs on device body lateral wall, and forms the passageway that supplies the sewage circulation between the ultraviolet catalysis board, be provided with a plurality of catalyst boards between the ultraviolet catalysis board, the shower nozzle that is used for letting in ozone is installed to device body lateral wall, the shower nozzle is located between the ultraviolet catalysis board, the activated carbon filter screen is with device body inside division mixing area and reaction zone.
2. The sewage treatment multi-unit integrated device according to claim 1, wherein: be provided with the stirring component between active carbon filter screen and the gas-liquid mixture component, the stirring component includes a plurality of puddlers, puddler fixed mounting is in the pivot, there is step motor in the pivot through the coupling joint, step motor fixed mounting is on device body lateral wall.
3. The sewage treatment multi-unit integrated device according to claim 1, wherein: the gas-liquid mixing component comprises a gas-liquid mixing cavity and a nozzle, the gas-liquid mixing cavity is provided with a gas inlet, a liquid inlet and a flow stabilizing port, the nozzle is fixed on a base of the catalytic oxidation filtering chamber through a substrate, and the nozzle is connected with the flow stabilizing port.
4. The sewage treatment multi-unit integrated device according to claim 1, wherein: the catalyst plate is distributed with solid catalyst, and the aperture of the catalyst plate is smaller than that of the solid catalyst.
5. The multi-element integrated sewage treatment device according to claim 3, wherein: and the adjacent ultraviolet light catalysis plates are respectively and fixedly arranged on the symmetrical side walls of the device body, and the catalyst plates and the horizontal plane form an acute angle of 30 degrees inclined upwards to form a flow passage for sewage to pass through from bottom to top.
6. The sewage treatment multi-unit integrated device according to claim 1, wherein: the catalytic oxidation component is provided with a gas-liquid separation part at the upper end, the top end of the device body is provided with a gas outlet, and the side wall of the device body is provided with a water outlet.
7. The sewage treatment multi-unit integrated device according to claim 6, wherein: the gas-liquid separation spare includes the gas-liquid filter screen, the gas-liquid filter screen passes through support fixed mounting and is originally internal at the device, the gas-liquid filter screen outer lane is provided with out the water weir, it is located one side of device body inner wall to go out the water weir, it communicates with the apopore to go out the water weir.
8. The multi-element integrated sewage treatment device according to claim 7, wherein: the lower end of the device body is provided with a rotating wheel.
CN202121332598.6U 2021-06-16 2021-06-16 Many first integrated devices of sewage treatment Active CN215712350U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202121332598.6U CN215712350U (en) 2021-06-16 2021-06-16 Many first integrated devices of sewage treatment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202121332598.6U CN215712350U (en) 2021-06-16 2021-06-16 Many first integrated devices of sewage treatment

Publications (1)

Publication Number Publication Date
CN215712350U true CN215712350U (en) 2022-02-01

Family

ID=80042793

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202121332598.6U Active CN215712350U (en) 2021-06-16 2021-06-16 Many first integrated devices of sewage treatment

Country Status (1)

Country Link
CN (1) CN215712350U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112551775A (en) * 2020-11-11 2021-03-26 安徽科技学院 Ultraviolet ozone catalytic oxidation sewage treatment device and method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112551775A (en) * 2020-11-11 2021-03-26 安徽科技学院 Ultraviolet ozone catalytic oxidation sewage treatment device and method

Similar Documents

Publication Publication Date Title
US7264231B2 (en) Diffused gas aeration apparatus
CN211946444U (en) Continuous flow intermittent aeration fluidized bed coupling activated sludge integrated reactor
CN215712350U (en) Many first integrated devices of sewage treatment
JP3397096B2 (en) Apparatus and method for ozone treatment of biological sludge
CN106630108B (en) Wastewater decoloring device with rotary releaser and decoloring method
CN112194287B (en) Sewage treatment device and method thereof
CN110668552B (en) Ozone synergistic micro hydrogen peroxide catalytic device and method
JP2005144425A (en) Diffuser
CN110668551B (en) Ozone catalytic device and method
CN111217441B (en) Ozone oxidation reactor and use method thereof
CN104773810A (en) Catalytic ozonation device
CN216236452U (en) Ozone advanced oxidation water treatment equipment
CN116002911A (en) Combined ozone catalytic oxidation water purification device and raw water purification method
CN206188474U (en) Wastewater decoloration device with rotary release ware
CN212127673U (en) Fountain catalytic ozonation reaction system
CN112755936B (en) Device for continuously preparing pseudo-boehmite and preparation method thereof
CN216639069U (en) Multi-working-condition adjustable biochemical sewage treatment skid-mounted device
CN2526315Y (en) Integrated membrane bioreactor
JP2009039673A (en) Apparatus and method for treating waste water
CN110734124A (en) high-efficiency ozone catalytic oxidation water treatment system and control method
CN109987695A (en) A kind of Three phase ozone catalytic vulcanization tower
CN104445511A (en) Combined device for treating ammonia nitrogen in wastewater
CN212504305U (en) Organic wastewater treatment system
CN217323483U (en) Ozone catalytic tower
CN215249804U (en) Water vapor circulation ozone reaction system

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant