CN205045844U - Processing apparatus of strong oxidation drinking water of ultraviolet ray catalysis - Google Patents
Processing apparatus of strong oxidation drinking water of ultraviolet ray catalysis Download PDFInfo
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- CN205045844U CN205045844U CN201520303360.9U CN201520303360U CN205045844U CN 205045844 U CN205045844 U CN 205045844U CN 201520303360 U CN201520303360 U CN 201520303360U CN 205045844 U CN205045844 U CN 205045844U
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Abstract
The utility model discloses a processing apparatus of strong oxidation drinking water of ultraviolet ray catalysis, including security personnel's formula filter and ultraviolet ray catalysis combination treater, ultraviolet ray catalysis combination treater includes the casing, is equipped with the strong oxidation reactor of ultraviolet lamp and photocatalysis in the casing, and the strong oxidation reactor of photocatalysis includes a plurality of photocatalysis's of containing photocatalysis carrier, the casing inboard is equipped with evenly distributed's rivers guide structure. The utility model discloses use multipurposely the synergism that the strong oxidation of ultraviolet sterilization and photocatalysis disinfected and handled the drinking water.
Description
Technical field
The utility model belongs to drinking water safety safeguards technique field, particularly a kind for the treatment of unit of ultraviolet light catalyzing and strong oxidizing tap water.
Background technology
In the systems such as all kinds of potable water supply system, urban wastewater treatment, sterilization is all one of indispensable technique ensureing water quality safety.In the sterilization and disinfection technique generally used at present, there are the methods such as ultraviolet, ozone, chlorination, silver ions.Wherein, ultraviolet exist algae kill difficulty, sterilization not thoroughly, the problem such as poor processing effect; The problems such as the existence of ozone, chlorination causes secondary pollution to tap water, and harm humans is healthy; There is the problems such as life cycle is short, end-use performance is low in silver ions.Therefore, all can not meet the drinking water safety requirements of support with upper type, cannot ensure: safe, reliable and effective, environment allows and the rational basic demand of expense.
Utility model content
Problem to be solved in the utility model is: provide a kind of can in fluid water can instantaneous sterilization, can the water technology that ensures of the drinking water safety of algae and living body biological.
In order to solve the problem, the utility model provides a kind for the treatment of unit of ultraviolet light catalyzing and strong oxidizing tap water, it is characterized in that, comprise security personnel's formula strainer and ultraviolet catalytic combining processor, described ultraviolet catalytic combining processor comprises housing, be provided with ultraviolet lamp and photochemical catalysis Strong oxdiative reactor in housing, photochemical catalysis Strong oxdiative reactor comprises multiple carrier of photocatalyst comprising photocatalyst; Case inside is provided with equally distributed current deflecting structure.
Current deflecting structure contacts the frequency for increasing crossing water with photocatalyst material.
Preferably, the load state of described photocatalyst is spherical, sheet, the threadiness of load on glass, silica gel, pottery, metal, stainless steel, nickel, titanium, netted, spongy photocatalyst.
Preferably, described photochemical catalysis Strong oxdiative reactor comprises an annular tubular carrier of photocatalyst, ultraviolet lamp is located at the central axis of this annular tubular photocatalyst, be provided with the 2-100 sheet tabular carrier of photocatalyst around ultraviolet lamp outer quartz sleeve pipe Spiral distribution radially between ultraviolet lamp and annular tubular carrier of photocatalyst, the thickness of every blade tabular carrier of photocatalyst is 0.1mm-5mm.
Preferably, the spiral element number of described tabular carrier of photocatalyst is 2-100 sheet, and the angle between itself and ultraviolet lamp outer quartz sleeve pipe is 5 ° ~ 85 °.
Preferably, the external diameter of described ultraviolet catalytic combining processor is 25mm-2000mm.
The utility model provides a kind for the treatment of unit of ultraviolet light catalyzing and strong oxidizing water, and the synergy that this device has fully utilized ultra-violet sterilization and the sterilization of photochemical catalysis Strong oxdiative carrys out processing drinking water.
The advantage of the utility model technology is:
1, the utility model combines the effect of ultraviolet light irradiation and photochemical catalysis, i.e. existing ultraviolet photolysis effect in reaction process, has again photochemical catalysis strong oxidation, utilizes photocatalysis technology thoroughly to kill microorganism etc. in current water;
2, the utility model method has very high speed of response, effectively can kill the protozoon, algae, bacterium, spore etc. that are less than 5 μm, sterilizing time is less than 5 seconds, namely in design bottle and water flow, only needs to control its water outlet peak flow and it's the water time pasts bottle;
3, substantially do not use any pharmaceutical chemicals, be conducive to Resources for construction saving type and environmentally friendly amphitypy society;
4, equipment volume according to the customization of demand occasion difference, energy consumption is extremely low, processing efficiency is high, applied widely, ultraviolet lamp tube also can according to the keying controlling ultraviolet lamp tube power supply with the keying of current during water;
5, the organic pollutant can be able to degraded in former water again while killing microorganisms.
Accompanying drawing explanation
The process flow sheet of the treatment unit of a kind of ultraviolet light catalyzing and strong oxidizing tap water that Fig. 1 provides for employing the utility model;
Fig. 2 is the internal structure schematic diagram of the treatment unit of ultraviolet light catalyzing and strong oxidizing tap water;
Fig. 3 is the schematic diagram of current deflecting structure.
Embodiment
For making the utility model become apparent, hereby with preferred embodiment, and accompanying drawing is coordinated to be described in detail below.
Embodiment 1
As Figure 2-3, for the structural representation of the treatment unit of a kind of ultraviolet light catalyzing and strong oxidizing tap water provided by the invention, comprise security personnel's formula strainer 1 and ultraviolet catalytic combining processor 2, described ultraviolet catalytic combining processor 2 comprises housing 2-3, be provided with ultraviolet lamp 2-1 and photochemical catalysis Strong oxdiative reactor 2-2 in housing 2-3, photochemical catalysis Strong oxdiative reactor 2-2 comprises multiple carrier of photocatalyst comprising photocatalyst; Equally distributed current deflecting structure 2-4 is provided with inside housing 2-3.Photochemical catalysis Strong oxdiative reactor 2-2 comprises an annular tubular carrier of photocatalyst, ultraviolet lamp 2-1 is located at the central axis of this annular tubular photocatalyst, be provided with 8 tabular carrier of photocatalyst around ultraviolet lamp 2-1 outer quartz sleeve pipe Spiral distribution radially between ultraviolet lamp 2-1 and annular tubular carrier of photocatalyst, the thickness of every blade tabular carrier of photocatalyst is 2mm.Photocatalyst adopts titanium dioxide, and load state is the light sheets catalyzer of load on pottery.The spiral element number of sheet tabular carrier of photocatalyst is 60, and the angle between itself and ultraviolet lamp 2-1 outer quartz sleeve pipe is 45 °.The external diameter of ultraviolet catalytic combining processor 2 is 100mm.The shell cavity material of ultraviolet catalytic combining processor 2 adopts glass reinforced plastic.
A kind for the treatment of process of ultraviolet light catalyzing and strong oxidizing tap water as shown in Figure 1, adopt the treatment unit of above-mentioned ultraviolet light catalyzing and strong oxidizing tap water, first, former water is delivered to through vacuum primingpump security personnel's formula filtration unit 1 that filter diameter is less than 5 μm and filters out macrobead foreign material and comprise silt, planktonic organism etc.; Then, water enters ultraviolet catalytic combining processor 2, and the biology being less than 5 μm is thoroughly killed by during ultraviolet catalytic combining processor at former water; Finally, the product water handled well is by pipeline feeding grid 3.The present invention may be used for the hydrobiont such as algae, pathogenic micro-organism killed in former water, and can place to go be had to act on to the various organic pollutants in former water simultaneously.
Normal surface well water is extracted out by vacuum primingpump and is directly introduced apparatus of the present invention, first via hole diameter is after security personnel's formula filtration unit 1 of 5 μm, and wherein diameter is less than the algae of 5 μm and bacterium through to launch ultraviolet lamp 2-1 that predominant wavelength is 254nm wavelength and to be spray-coated film type TiO prepared by the substrate of load with stainless steel
2the photochemical catalysis Strong oxdiative reactor 2-2 of photocatalyst, normal water inlet is to the flowing time of water outlet after 10 seconds, obtain product water, algae counts method and UV, visible light spectrophotometer method is used to detect the quantity of algea and bacteria, the algea and bacteria that wherein diameter is less than 5 μm does not all detect, and killing rate is 100%, cultivates the product water after process through 3 days bacterial cultivations, the bacterium being less than 5 μm detects not yet, proves that the inventive method can kill spore completely.
In use Fig. 2, a kind of water that increased contacts in the current deflecting structure 2-4 of the frequency with photocatalyst material simultaneously, the TiO of use
2area is less, and use cost is low, simultaneously its guide frame make former water repeatedly with photochemical catalysis carrier contact, thus ensure that it plays maximum efficiency.
As shown in Figure 3, current deflecting structure 2-4 makes former water with volution water flow mode through photocatalyst, to obtain frequent catalytic chance with it.
Embodiment 2
The treatment unit of a kind of ultraviolet light catalyzing and strong oxidizing tap water provided by the invention comprises security personnel's formula strainer 1 and ultraviolet catalytic combining processor 2, described ultraviolet catalytic combining processor 2 comprises housing 2-3, be provided with ultraviolet lamp 2-1 and photochemical catalysis Strong oxdiative reactor 2-2 in housing 2-3, photochemical catalysis Strong oxdiative reactor 2-2 comprises multiple carrier of photocatalyst comprising photocatalyst; Equally distributed current deflecting structure 2-4 is provided with inside housing 2-3.Photochemical catalysis Strong oxdiative reactor 2-2 comprises an annular tubular carrier of photocatalyst, ultraviolet lamp 2-1 is located at the central axis of this annular tubular photocatalyst, be provided with 100 tabular carrier of photocatalyst around ultraviolet lamp 2-1 outer quartz sleeve pipe Spiral distribution radially between ultraviolet lamp 2-1 and annular tubular carrier of photocatalyst, the thickness of every blade tabular carrier of photocatalyst is 2mm.Photocatalyst adopts titanium dioxide, and load state is the spherical photocatalyst of load on glass.The spiral element number of sheet tabular carrier of photocatalyst is 100, and the angle between itself and ultraviolet lamp 2-1 outer quartz sleeve pipe is 5 °.The external diameter of ultraviolet catalytic combining processor 2 is 1500mm.The shell cavity material of ultraviolet catalytic combining processor 2 adopts PVC.
A kind for the treatment of process of ultraviolet light catalyzing and strong oxidizing tap water, adopt the treatment unit of above-mentioned ultraviolet light catalyzing and strong oxidizing tap water, first, former water is delivered to through vacuum primingpump security personnel's formula filtration unit 1 that filter diameter is less than 5 μm and filters out macrobead foreign material and comprise silt, planktonic organism etc.; Then, water enters ultraviolet catalytic combining processor 2, and the biology being less than 5 μm is thoroughly killed by during ultraviolet catalytic combining processor at former water; Finally, the product water handled well is by pipeline feeding grid 3.The present invention may be used for the hydrobiont such as algae, pathogenic micro-organism killed in former water, and can place to go be had to act on to the various organic pollutants in former water simultaneously.
Normal surface well water is extracted out by vacuum primingpump and is directly introduced apparatus of the present invention, first via hole diameter is after security personnel's formula filtration unit 1 of 5 μm, wherein diameter is less than the algae of 5 μm and bacterium through to launch ultraviolet lamp 2-1 that predominant wavelength is 254nm wavelength and to take stainless steel as the photochemical catalysis Strong oxdiative reactor 2-2 of spray-coated film type photocatalyst of zinc oxide prepared by the substrate of load, normal water inlet is to the flowing time of water outlet after 10 seconds, obtain product water, algae counts method and UV, visible light spectrophotometer method is used to detect the quantity of algea and bacteria, the algea and bacteria that wherein diameter is less than 5 μm does not all detect, killing rate is 100%, the product water after process is cultivated through 3 days bacterial cultivations, the bacterium being less than 5 μm detects not yet, prove that the inventive method can kill spore completely.
Simultaneously increasing water in use contact in the current deflecting structure 2-4 of the frequency with photocatalyst material, and the zinc oxide area of use is less, and use cost is low, while its guide frame make former water repeatedly with photochemical catalysis carrier contact, thus ensure its performance maximum efficiency.
Current deflecting structure 2-4 makes former water with volution water flow mode through photocatalyst, to obtain frequent catalytic chance with it.
Embodiment 3
The treatment unit of a kind of ultraviolet light catalyzing and strong oxidizing tap water provided by the invention, comprise security personnel's formula strainer 1 and ultraviolet catalytic combining processor 2, described ultraviolet catalytic combining processor 2 comprises housing 2-3, be provided with ultraviolet lamp 2-1 and photochemical catalysis Strong oxdiative reactor 2-2 in housing 2-3, photochemical catalysis Strong oxdiative reactor 2-2 comprises multiple carrier of photocatalyst comprising photocatalyst; Equally distributed current deflecting structure 2-4 is provided with inside housing 2-3.Photochemical catalysis Strong oxdiative reactor 2-2 comprises an annular tubular carrier of photocatalyst, ultraviolet lamp 2-1 is located at the central axis of this annular tubular photocatalyst, be provided with 6 tabular carrier of photocatalyst around ultraviolet lamp 2-1 outer quartz sleeve pipe Spiral distribution radially between ultraviolet lamp 2-1 and annular tubular carrier of photocatalyst, the thickness of every blade tabular carrier of photocatalyst is 2mm.Photocatalyst adopts titanium dioxide, and load state is the light sheets catalyzer of load on pottery.The spiral element number of sheet tabular carrier of photocatalyst is 6, and the angle between itself and ultraviolet lamp 2-1 outer quartz sleeve pipe is 85 °.The external diameter of ultraviolet catalytic combining processor 2 is 25mm.The shell cavity material of ultraviolet catalytic combining processor 2 adopts stainless steel.
A kind for the treatment of process of ultraviolet light catalyzing and strong oxidizing tap water, adopt the treatment unit of above-mentioned ultraviolet light catalyzing and strong oxidizing tap water, first, former water is delivered to through vacuum primingpump security personnel's formula filtration unit 1 that filter diameter is less than 5 μm and filters out macrobead foreign material and comprise silt, planktonic organism etc.; Then, water enters ultraviolet catalytic combining processor 2, and the biology being less than 5 μm is thoroughly killed by during ultraviolet catalytic combining processor at former water; Finally, the product water handled well is by pipeline feeding grid 3.The present invention may be used for the hydrobiont such as algae, pathogenic micro-organism killed in former water, and can place to go be had to act on to the various organic pollutants in former water simultaneously.
Normal surface well water is extracted out by vacuum primingpump and is directly introduced apparatus of the present invention, first via hole diameter is after security personnel's formula filtration unit 1 of 5 μm, wherein diameter is less than the algae of 5 μm and bacterium through to launch ultraviolet lamp 2-1 that predominant wavelength is 254nm wavelength and to take stainless steel as the photochemical catalysis Strong oxdiative reactor 2-2 of spray-coated film type tungsten trioxide photocatalyst prepared by the substrate of load, normal water inlet is to the flowing time of water outlet after 10 seconds, obtain product water, algae counts method and UV, visible light spectrophotometer method is used to detect the quantity of algea and bacteria, the algea and bacteria that wherein diameter is less than 5 μm does not all detect, killing rate is 100%, the product water after process is cultivated through 3 days bacterial cultivations, the bacterium being less than 5 μm detects not yet, prove that the inventive method can kill spore completely.
Simultaneously increasing water in use contact in the current deflecting structure 2-4 of the frequency with photocatalyst material, and the tungstic oxide area of use is less, and use cost is low, while its guide frame make former water repeatedly with photochemical catalysis carrier contact, thus ensure its performance maximum efficiency.
Current deflecting structure 2-4 makes former water with volution water flow mode through photocatalyst, to obtain frequent catalytic chance with it.
Claims (5)
1. the treatment unit of a ultraviolet light catalyzing and strong oxidizing tap water, it is characterized in that, comprise security personnel's formula strainer (1) and ultraviolet catalytic combining processor (2), described ultraviolet catalytic combining processor (2) comprises housing (2-3), be provided with ultraviolet lamp (2-1) and photochemical catalysis Strong oxdiative reactor (2-2) in housing (2-3), photochemical catalysis Strong oxdiative reactor (2-2) comprises multiple carrier of photocatalyst comprising photocatalyst; Housing (2-3) inner side is provided with equally distributed current deflecting structure (2-4).
2. the treatment unit of ultraviolet light catalyzing and strong oxidizing tap water as claimed in claim 1, it is characterized in that, the load state of described photocatalyst is spherical, sheet, the threadiness of load on glass, silica gel, pottery, metal, stainless steel, nickel, titanium, netted, spongy photocatalyst.
3. the treatment unit of ultraviolet light catalyzing and strong oxidizing tap water as claimed in claim 1, it is characterized in that, described photochemical catalysis Strong oxdiative reactor (2-2) comprises an annular tubular carrier of photocatalyst, ultraviolet lamp (2-1) is located at the central axis of this annular tubular photocatalyst, be provided with the 2-100 sheet tabular carrier of photocatalyst around ultraviolet lamp (2-1) outer quartz sleeve pipe Spiral distribution radially between ultraviolet lamp (2-1) and annular tubular carrier of photocatalyst, the thickness of every blade tabular carrier of photocatalyst is 0.1mm-5mm.
4. the treatment unit of ultraviolet light catalyzing and strong oxidizing tap water as claimed in claim 3, it is characterized in that, the spiral element number of described tabular carrier of photocatalyst is 2-100 sheet, and the angle between itself and ultraviolet lamp (2-1) outer quartz sleeve pipe is 5 ° ~ 85 °.
5. the treatment unit of ultraviolet light catalyzing and strong oxidizing tap water as claimed in claim 1, it is characterized in that, the external diameter of described ultraviolet catalytic combining processor (2) is 25mm-2000mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520303360.9U CN205045844U (en) | 2015-05-12 | 2015-05-12 | Processing apparatus of strong oxidation drinking water of ultraviolet ray catalysis |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520303360.9U CN205045844U (en) | 2015-05-12 | 2015-05-12 | Processing apparatus of strong oxidation drinking water of ultraviolet ray catalysis |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104843825A (en) * | 2015-05-12 | 2015-08-19 | 上海伊美特实业有限公司 | Treatment device and treatment process for drinking water through ultraviolet photo-catalyzed strong oxidization |
| CN106830270A (en) * | 2017-01-18 | 2017-06-13 | 江苏泽宇环境工程有限公司 | A kind of combined type catalytic oxidizing equipment |
| CN107188266A (en) * | 2017-06-26 | 2017-09-22 | 河南泽衡环保科技股份有限公司 | Photocatalysis sewage handles Aerobic Pond |
| CN108238695A (en) * | 2016-12-23 | 2018-07-03 | 北京有色金属研究总院 | A kind of ultraviolet catalytic water treatment facilities using float type photochemical catalyst |
-
2015
- 2015-05-12 CN CN201520303360.9U patent/CN205045844U/en active Active
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104843825A (en) * | 2015-05-12 | 2015-08-19 | 上海伊美特实业有限公司 | Treatment device and treatment process for drinking water through ultraviolet photo-catalyzed strong oxidization |
| CN108238695A (en) * | 2016-12-23 | 2018-07-03 | 北京有色金属研究总院 | A kind of ultraviolet catalytic water treatment facilities using float type photochemical catalyst |
| CN108238695B (en) * | 2016-12-23 | 2020-09-15 | 有研工程技术研究院有限公司 | Ultraviolet light catalysis water treatment device applying floating type photocatalyst |
| CN106830270A (en) * | 2017-01-18 | 2017-06-13 | 江苏泽宇环境工程有限公司 | A kind of combined type catalytic oxidizing equipment |
| CN107188266A (en) * | 2017-06-26 | 2017-09-22 | 河南泽衡环保科技股份有限公司 | Photocatalysis sewage handles Aerobic Pond |
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