CN204508908U - A kind of ozone oxidation experimental installation - Google Patents
A kind of ozone oxidation experimental installation Download PDFInfo
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- CN204508908U CN204508908U CN201520130934.7U CN201520130934U CN204508908U CN 204508908 U CN204508908 U CN 204508908U CN 201520130934 U CN201520130934 U CN 201520130934U CN 204508908 U CN204508908 U CN 204508908U
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Abstract
The utility model discloses a kind of ozone oxidation experimental installation, be made up of ozone-oxidizing device, pipeline and aerating system, wherein ozone-oxidizing device is cylindrical seal tank body, tank body main body is synthetic glass, tank body lean to one side be provided with multiple sampling of wastewater mouth successively, each sampling of wastewater mouth is all provided with sampling valve; The top semi-circular end socket of tank body is connected with synthetic glass by flange with bottom semicircular end socket, top semi-circular end socket is provided with offgas duct, offgas duct is provided with exhaust sampling mouth, offgas duct is connected with device for absorbing tail gas, be filled with gac in device for absorbing tail gas, tank base is provided with pipeline for waste water turnover experimental installation; Aerating system is provided with bottom ozone-oxidizing device.The utility model can, in the response situation of testing desk research ozone and various wastewater oxidation, provide various technical parameter and theoretical foundation to follow-up industrial applications simultaneously.Have and plant the advantages such as simple to operate, reasonable in design, experimental result is reliable, have broad application prospects.
Description
Technical field
The utility model relates to the field such as environmental protection technology and water treating equipment exploitation, particularly a kind of ozone oxidation experimental installation of use for laboratory.
Background technology
Ozone is a kind of very strong oxygenant, because it does not produce secondary pollution, easy to operate, the advantage such as air can be utilized to produce on the spot, contain phenol in process, apply widely containing having waited until in the trade effluents such as cyanogen, oil refining, petrochemical complex, particularly using ozonation technology as the phenols, prussiate, COD etc. in the further degrading waste water of advanced treatment, achieve certain successful experience, but about ozone to the also ununified final conclusion of the oxidation reaction mechanism of target contaminant, cause there are some unaccountable problems in actual applications at Ozonation.Therefore people are in the urgent need to a kind of experimental installation about ozone oxidation study mechanism, to crack the oxidation mechanism of ozone to target contaminant, for industrial application provides theoretical foundation and technical director.After using the utility model experimental installation, effectively can study the relation of target contaminant and ozone concn and the utilization ratio of ozone oxidation in waste water, people are made to study the reaction mechanism of ozone and target contaminant better, simultaneously for follow-up industrial application provides theoretical parameter and technical director.
Summary of the invention
The utility model is complicated for the reaction mechanism of ozone in wastewater treatment and target contaminant, and industrial application difficult parameters is with the phenomenon of Theoretical Calculation, and the one of proposition is simple to operate, reasonable in design, the reliable ozone oxidation experimental installation of experimental result.
The utility model is by being be made up of ozone-oxidizing device, pipeline and aerating system, wherein ozone-oxidizing device is cylindrical seal tank body, tank body main body is synthetic glass, tank body lean to one side be provided with multiple sampling of wastewater mouth successively, each sampling of wastewater mouth is all provided with sampling valve; The top semi-circular end socket of tank body is connected with synthetic glass by flange with bottom semicircular end socket, top semi-circular end socket is provided with offgas duct, offgas duct is provided with exhaust sampling mouth, offgas duct is connected with device for absorbing tail gas, be filled with gac in device for absorbing tail gas, tank base is provided with pipeline for waste water turnover experimental installation; Be provided with aerating system bottom ozone-oxidizing device, aerating system is made up of ozonizer, air system, micro-hole aerator, and micro-hole aerator is connected with air system with ozonizer by aeration tube, and air system is made up of air compressor and gas-holder; Whole experimental installation is supported by angle bar.
Described tank body material is the synthetic glass with acidproof corrosion resistant character.
Described ozone-oxidizing device tank body pipeline, sealing, sampling slip, flange plate etc. are acidproof corrosion resistant, anti-oxidant material.
Described mixture pipe, the inlet pipe be connected with ozonizer are 316L stainless steel, and described micro porous aeration head is plate-like, column or hemispherical, and material is 316L stainless steel, titanium alloy or pottery.
The beneficial effects of the utility model:
The utility model can, in the response situation of testing desk research ozone and various wastewater oxidation, provide various technical parameter and theoretical foundation to follow-up industrial applications simultaneously.Have and plant the advantages such as simple to operate, reasonable in design, experimental result is reliable, have broad application prospects.
Accompanying drawing explanation
Fig. 1 is Structure and energy schema of the present utility model.
Embodiment
Refer to shown in Fig. 1, the utility model is made up of ozone-oxidizing device 1, pipeline 4 and aerating system, wherein ozone-oxidizing device 1 is cylindrical seal tank body, tank body main body is synthetic glass 13, tank body lean to one side be provided with multiple sampling of wastewater mouth 2 successively, each sampling of wastewater mouth 2 is all provided with sampling valve; The top semi-circular end socket 11 of tank body is connected with synthetic glass 13 by flange 12 with bottom semicircular end socket 14, top semi-circular end socket 11 is provided with offgas duct 7, offgas duct 7 is provided with exhaust sampling mouth 8, offgas duct 7 is connected with device for absorbing tail gas 9, be filled with gac 10 in device for absorbing tail gas 9, tank base is provided with pipeline 4 for waste water turnover experimental installation; Aerating system is provided with bottom ozone-oxidizing device 1, aerating system is made up of ozonizer, air system, micro-hole aerator 3, micro-hole aerator 3 is connected with air system with ozonizer by aeration tube 5, and air system is made up of air compressor and gas-holder; Whole experimental installation is supported by angle bar.
(in figure, making 4 into by 6)
Claims (4)
1. an ozone oxidation experimental installation, it is characterized in that: be made up of ozone-oxidizing device (1), pipeline (4) and aerating system, wherein ozone-oxidizing device (1) is cylindrical seal tank body, tank body main body is synthetic glass (13), tank body lean to one side be provided with multiple sampling of wastewater mouth (2) successively, each sampling of wastewater mouth (2) is all provided with sampling valve; The top semi-circular end socket (11) of tank body is connected with synthetic glass (13) by flange (12) with bottom semicircular end socket (14), top semi-circular end socket (11) is provided with offgas duct (7), offgas duct (7) is provided with exhaust sampling mouth (8), offgas duct (7) is connected with device for absorbing tail gas (9), be filled with gac (10) in device for absorbing tail gas (9), tank base is provided with pipeline (4) for waste water turnover experimental installation; Ozone-oxidizing device (1) bottom is provided with aerating system.
2. a kind of ozone oxidation experimental installation according to claim 1, it is characterized in that: described aerating system is made up of ozonizer, air system, micro-hole aerator (3), and micro-hole aerator (3) is connected with air system with ozonizer by aeration tube (5).
3. a kind of liquid transferring tube cleaner according to claim 2, is characterized in that: described air system is made up of air compressor and gas-holder.
4. a kind of ozone oxidation experimental installation according to claim 1, is characterized in that: described tank body material is the synthetic glass with acidproof corrosion resistant character.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520130934.7U CN204508908U (en) | 2015-03-07 | 2015-03-07 | A kind of ozone oxidation experimental installation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520130934.7U CN204508908U (en) | 2015-03-07 | 2015-03-07 | A kind of ozone oxidation experimental installation |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204508908U true CN204508908U (en) | 2015-07-29 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520130934.7U Active CN204508908U (en) | 2015-03-07 | 2015-03-07 | A kind of ozone oxidation experimental installation |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204508908U (en) |
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2015
- 2015-03-07 CN CN201520130934.7U patent/CN204508908U/en active Active
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| C14 | Grant of patent or utility model | ||
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