CN207774891U - A kind for the treatment of technology device for the processing of high organic wastewater - Google Patents
A kind for the treatment of technology device for the processing of high organic wastewater Download PDFInfo
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- CN207774891U CN207774891U CN201721816879.2U CN201721816879U CN207774891U CN 207774891 U CN207774891 U CN 207774891U CN 201721816879 U CN201721816879 U CN 201721816879U CN 207774891 U CN207774891 U CN 207774891U
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- pipeline
- ozone
- reactive tank
- enters
- kettle body
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- 239000002351 wastewater Substances 0.000 title claims abstract description 59
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 75
- 239000003054 catalyst Substances 0.000 claims abstract description 29
- 238000006243 chemical reaction Methods 0.000 claims abstract description 24
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 8
- 238000000034 method Methods 0.000 claims description 7
- 239000003795 chemical substances by application Substances 0.000 claims description 5
- 238000007254 oxidation reaction Methods 0.000 abstract description 12
- 230000003647 oxidation Effects 0.000 abstract description 10
- 239000005416 organic matter Substances 0.000 abstract description 7
- 230000003197 catalytic effect Effects 0.000 abstract description 5
- 238000006555 catalytic reaction Methods 0.000 description 6
- 239000011949 solid catalyst Substances 0.000 description 5
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000003911 water pollution Methods 0.000 description 2
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 231100001261 hazardous Toxicity 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 230000007096 poisonous effect Effects 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
- 239000003403 water pollutant Substances 0.000 description 1
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- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
The utility model is related to technical field of waste water processing, more particularly to a kind for the treatment of technology device for the processing of high organic wastewater, including reaction kettle, supercharging device and Ozone generator, reaction kettle includes upper cover and lower kettle body, upper cover enters pipeline equipped with waste water, steam enters pipeline and catalyst enters pipeline, and steam enters pipeline and is equipped with the first control valve；Reactive tank group is equipped in lower kettle body, catalyst enters the downward kettle body internal stretch in one end of pipeline and above reactive tank group, it is equipped with pressure pipeline, the ozone being connected to lower kettle body outside lower kettle body and enters pipeline, supercharging device is equipped with pressure output pipeline, pressure output pipeline is connected to pressure pipeline, Ozone generator enters pipeline with ozone by pipeline and connect, and lower kettle body bottom is additionally provided with outlet conduit, and outlet conduit is equipped with the second control valve.The utility model catalytic oxidation efficiency is fast, and being capable of high organic matter in deep oxidation waste water.
Description
Technical field
The utility model is related to technical field of waste water processing, more particularly to a kind of depth for the processing of high organic wastewater
Catalytic oxidizing equipment.
Background technology
China is global water pollution one of the countries with the most serious ..., and river, lake and the reservoir in the whole nation up to 70% are by shadow
It rings.One national survey shows in the organic pollution for being discharged into various water bodys in 2007 that nearly 20% is originated from industry.These works
Factory causes important water resources to be polluted, studies have shown that the water pollution of China about 20%-30% is made due to manufacture exporting
At.《69 kinds of pollution discharge standards of GB8978-1996 integrated wastewaters》In define 69 kinds of water pollutants and allow to discharge
Concentration, predominantly traditional, Wastewater Pollutant known to everybody.However, as China becomes with fastest developing speed big in the whole world
Numerous chemicals of type economy, all types of industries discharge are consequently increased, some poisonous and hazardous high organic polluting waters are especially
It is troubling.In this regard, national requirements related factories must possess high organic matter waste water processing equipment to handle high organic wastewater.
Each step that the equipment handles high organic wastewater is all related to high organic wastewater and can maximize removal harmful substance.Its
Middle catalysis oxidation is one of the important step that the equipment handles high organic wastewater.The mode of traditional catalysis oxidation is all to allow height
Organic wastewater is directly entered reaction kettle, then passes to ozone and directly carries out catalysis oxidation.The mode of this catalysis oxidation exists
The shortcomings of reaction efficiency is low, and the degree of high organic matter is not ideal enough in oxidized waste water.
Invention content
The purpose of this utility model is that in view of the deficiencies of the prior art, provide a kind of for the processing of high organic wastewater
Treating technology device.
To solve the above problems, the utility model provides following technical scheme：
A kind for the treatment of technology device for the processing of high organic wastewater, including reaction kettle, supercharging device and ozone
Generating means, the reaction kettle include upper cover and lower kettle body, and the upper cover enters pipeline equipped with waste water, steam enters pipe
Road and catalyst enter pipeline, and the waste water enters pipeline and center of top in upper cover is arranged, and steam enters pipeline and catalysis
Agent enters pipeline and is located at the side that waste water enters pipeline, and steam enters pipeline and is equipped with the first control valve；It is equipped in lower kettle body anti-
Slot group is answered, the catalyst enters the downward kettle body internal stretch in one end of pipeline and above reactive tank group, outside lower kettle body
Enter pipeline equipped with pressure pipeline, the ozone being connected to lower kettle body, the supercharging device is equipped with pressure output pipeline, and pressure is defeated
Go out pipeline to be connected to pressure pipeline, the Ozone generator enters pipeline with ozone by pipeline and connect, and lower kettle body bottom is also
Equipped with outlet conduit, outlet conduit is equipped with the second control valve.
Further, the reactive tank group includes the first reactive tank and the second reactive tank, and the first reactive tank is anti-higher than second
Slot is answered, kettle body inner horizontal extends downward from lower kettle body inner wall for the first reactive tank and the second reactive tank, and the first reactive tank
Extending direction it is opposite with the extending direction of the second reactive tank.
Further, catalyst enters that pipeline enters pipeline including the first catalyst and the second catalyst enters pipeline, and
One catalyst enters the downward kettle body of pipeline and extends internal and be located above the first reactive tank, and the second catalyst enters the downward kettle of pipeline
Body internal stretch is simultaneously located above the second reactive tank.
Further, the ozone enters that pipeline including the first ozone enters pipeline and the second ozone enters pipeline, and first
Ozone enters pipeline and the second ozone enters pipeline and is located along the same line, and the first ozone enters pipeline and is higher than the second ozone
Into pipeline.
Further, first ozone enters the delivery outlet of pipeline and is located at the top of the first reactive tank, the second ozone into
Enter the delivery outlet of pipeline between the first reactive tank and the second reactive tank.
Further, filter screen is equipped in the outlet conduit.
Further, the Ozone generator is water process ozone generator.
Advantageous effect：A kind for the treatment of technology device for the processing of high organic wastewater of the utility model first will
Solid catalyst enters pipeline by the first catalyst and the second catalyst enters pipeline and respectively enters the first reactive tank and second
In reactive tank, then waste water enters pipeline by waste water and enters in the first reactive tank, the ozone that water process ozone generator generates
Enter pipeline by the first ozone and blow to the first reactive tank, the high organic matter in the waste water in the first reactive tank is with ozone in solid
The surface of catalyst carries out oxidation reaction, and the waste water in the first reactive tank is gradually increased and overflowed, and the waste water after spilling enters again
Second reactive tank, the ozone that water process ozone generator generates by the second ozone enter pipeline and blow to the second reactive tank, the
If there remains high organic matter will carry out oxygen again with ozone on the surface of solid catalyst in waste water in two reactive tanks
Change reaction, the waste water after being followed by subsequent processing can slowly escape through out of second reactive tank and into the bottom of reaction kettle, final to locate
Waste water after reason is discharged from outlet conduit；While waste water enters reaction kettle, steam enters pipeline by steam and enters
In reaction kettle, to allow inside reaction kettle the state for foring high temperature, supercharging device work allows inside reaction kettle and ultimately forms again
The state of high pressure-temperature, this state can speed up catalytic oxidation, in conclusion its catalytic oxidation efficiency is fast, and
And it being capable of high organic matter in deep oxidation waste water.
Description of the drawings
Fig. 1 is the stereoscopic schematic diagram of the utility model；
Fig. 2 is the partial top view of the utility model；
Fig. 3 is the sectional view along line A-A in Fig. 2；
Reference sign：Reaction kettle 1, upper cover 1a, waste water enter pipeline 1a1, and steam enters pipeline 1a2, and first urges
Agent enters pipeline 1a3, and the second catalyst enters pipeline 1a4, lower kettle body 1b, pressure pipeline 1b1, and outlet conduit 1b2, first is anti-
Slot 1b3, the second reactive tank 1b4, the first ozone is answered to enter pipeline 1b5, the second ozone enters pipeline 1b6, supercharging device 2, ozone
Generating means 3.
Specific implementation mode
With reference to the accompanying drawings of the specification and embodiment, specific embodiment of the utility model is described in further detail：
Referring to figs. 1 to a kind for the treatment of technology device for the processing of high organic wastewater shown in Fig. 3, including reaction
Kettle 1, supercharging device 2 and Ozone generator 3, the reaction kettle 1 include on upper cover 1a and lower kettle body 1b, the upper cover 1a
Enter pipeline 1a1 equipped with waste water, steam enters pipeline 1a2 and catalyst enters pipeline, the waste water enters pipeline 1a1 settings and exists
The center of top of upper cover 1a, steam enters pipeline 1a2 and catalyst enters pipeline and is located at the side that waste water enters pipeline 1a1,
Steam enters pipeline 1a2 and is equipped with the first control valve；Reactive tank group is equipped in lower kettle body 1b, the catalyst enters the one of pipeline
It holds downward kettle body 1b internal stretches and above reactive tank group, the pressure inlet being connected to lower kettle body 1b is equipped with outside lower kettle body 1b
Road 1b1, ozone enter pipeline, and the supercharging device 2 is equipped with pressure output pipeline, pressure output pipeline and pressure pipeline 1b1
Connection, the Ozone generator 3 enter pipeline with ozone by pipeline and connect, and the lower bottoms kettle body 1b are additionally provided with outlet conduit
1b2, outlet conduit 1b2 are equipped with the second control valve.
Operation principle：Solid catalyst is first entered pipeline by catalyst to enter in reactive tank group, then waste water passes through
Waste water enters pipeline 1a1 and also enters in reactive tank group, and the generation ozone of Ozone generator 3 enters pipeline by ozone and blows to instead
Slot group is answered, the high organic matter in the waste water in reactive tank carries out oxidation reaction with ozone on the surface of solid catalyst, then locates
Waste water after reason overflows out of reactive tank and flows into 1 bottom of reaction kettle, and the waste water after final process is from outlet conduit
1b2 flows out；While waste water enters reaction kettle 1, steam enters pipeline 1a2 by steam and enters in reaction kettle 1, anti-to allow
Answer the state that high temperature is formd inside kettle 1, the work of supercharging device 2 allows inside reaction kettle 1 shape for ultimately forming high pressure-temperature again
State, this state can speed up catalytic oxidation.
The reactive tank group includes the first reactive tank 1b3 and the second reactive tank 1b4, the first reactive tank 1b3 anti-higher than second
Answering slot 1b4, the first reactive tank 1b3 and the second reactive tank 1b4, from lower kettle body 1b inner walls, kettle body 1b inner horizontals extend downward, and
And first reactive tank 1b3 extending direction it is opposite with the extending direction of the second reactive tank 1b4；Waste water enters pipeline by waste water
In the first reactive tanks of 1a1 1b3, the waste water in the first reactive tank can be overflowed from the first reactive tank 1b3 flows into the second reactive tank
Waste water in 1b4, the second reactive tank 1b4 can be overflowed from the second reactive tank 1b4 flows into 1 bottom of reaction kettle.
Catalyst enters that pipeline enters pipeline 1a3 including the first catalyst and the second catalyst enters pipeline 1a4, and first urges
Agent enters the downward kettle body 1b of pipeline 1a3 and extends internal and be located above the first reactive tank 1b3, and the second catalyst enters pipeline
The downward kettle body 1b internal stretches of 1a4 are simultaneously located above the second reactive tank 1b4；First catalyst enters the catalysis of pipeline 1a3 and second
Agent, which enters pipeline 1a4, can allow solid catalyst to respectively enter in the first reactive tank 1b3 and the second reactive tank 1b4.
The ozone enters that pipeline enters pipeline 1b5 including the first ozone and the second ozone enters pipeline 1b6, the first ozone
Enter pipeline 1b6 into pipeline 1b5 and the second ozone to be located along the same line, and the first ozone enters pipeline 1b5 higher than the
Two ozone enter pipeline 1b6；Ozone generator 3 generates ozone, and then it is smelly from the first ozone to enter pipeline 1b5 and second for ozone
Oxygen enters pipeline 1b6 and enters 1 two regions in inside of reaction kettle, to make ozone be evenly distributed inside reaction kettle 1.
The delivery outlet that first ozone enters pipeline 1b5 is located at the top of the first reactive tank 1b3, and the second ozone enters pipe
The delivery outlet of road 1b6 is between the first reactive tank 1b3 and the second reactive tank 1b4；Ozone can enter pipe by the first ozone
The delivery outlet that road 1b5 and the second ozone enter pipeline 1b6 blows to the first reactive tank 1b3 and the second reactive tank 1b4 respectively.
Filter screen is equipped in the outlet conduit 1b2；Filter screen can filter out the impurity in waste water.
The Ozone generator 3 is water process ozone generator；Water process ozone generator have it is small, convenient for peace
The advantages that filling, be easy to operate, ozone output is big.
The above descriptions are merely preferred embodiments of the present invention, not makees to the technical scope of the utility model
Go out any restrictions, thus it is any trickle amendment made by the above technical examples according to the technical essence of the present invention, equivalent
Variation and modification, in the range of still falling within the technical solution of the utility model.
Claims (7)
1. a kind for the treatment of technology device for the processing of high organic wastewater, it is characterised in that：Including reaction kettle（1）, increase
Pressure device（2）And Ozone generator（3）, the reaction kettle（1）Including upper cover（1a）With lower kettle body（1b）, the upper cover
（1a）Enter pipeline equipped with waste water（1a1）, steam enter pipeline（1a2）Enter pipeline with catalyst, the waste water enters pipe
Road（1a1）It is arranged in upper cover（1a）Center of top, steam enters pipeline（1a2）With catalyst enter pipeline be located at waste water into
Enter pipeline（1a1）Side, steam enters pipeline（1a2）It is equipped with the first control valve；Lower kettle body（1b）It is interior to be equipped with reactive tank group,
The catalyst enters the downward kettle body in one end of pipeline（1b）Internal stretch is simultaneously located above reactive tank group, lower kettle body（1b）It is external
Equipped with lower kettle body（1b）The pressure pipeline of connection（1b1）, ozone enter pipeline, the supercharging device（2）It is defeated to be equipped with pressure
Go out pipeline, pressure output pipeline and pressure pipeline（1b1）Connection, the Ozone generator（3）Entered by pipeline and ozone
Pipeline connects, lower kettle body（1b）Bottom is additionally provided with outlet conduit（1b2）, outlet conduit（1b2）It is equipped with the second control valve.
2. a kind for the treatment of technology device for the processing of high organic wastewater according to claim 1, feature exist
In：The reactive tank group includes the first reactive tank（1b3）With the second reactive tank（1b4）, the first reactive tank（1b3）It is anti-higher than second
Answer slot（1b4）, the first reactive tank（1b3）With the second reactive tank（1b4）From lower kettle body（1b）Inner wall kettle body downward（1b）It is internal
Horizontal extension, and the first reactive tank（1b3）Extending direction and the second reactive tank（1b4）Extending direction it is opposite.
3. a kind for the treatment of technology device for the processing of high organic wastewater according to claim 2, feature exist
In：Catalyst enters pipeline and enters pipeline including the first catalyst（1a3）Enter pipeline with the second catalyst（1a4）, first urges
Agent enters pipeline（1a3）Downward kettle body（1b）Extend internal and is located at the first reactive tank（1b3）Top, the second catalyst enter
Pipeline（1a4）Downward kettle body（1b）Internal stretch is simultaneously located at the second reactive tank（1b4）Top.
4. a kind for the treatment of technology device for the processing of high organic wastewater according to claim 3, feature exist
In：The ozone enters pipeline and enters pipeline including the first ozone（1b5）Enter pipeline with the second ozone（1b6）, the first ozone
Into pipeline（1b5）Enter pipeline with the second ozone（1b6）It is located along the same line, and the first ozone enters pipeline（1b5）
Enter pipeline higher than the second ozone（1b6）.
5. a kind for the treatment of technology device for the processing of high organic wastewater according to claim 4, feature exist
In：First ozone enters pipeline（1b5）Delivery outlet be located at the first reactive tank（1b3）Top, the second ozone enters pipe
Road（1b6）Delivery outlet be located at the first reactive tank（1b3）With the second reactive tank（1b4）Between.
6. a kind for the treatment of technology device for the processing of high organic wastewater according to claim 1, feature exist
In：The outlet conduit（1b2）It is interior to be equipped with filter screen.
7. a kind for the treatment of technology device for the processing of high organic wastewater according to claim 1, feature exist
In：The Ozone generator（3）For water process ozone generator.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721816879.2U CN207774891U (en) | 2017-12-22 | 2017-12-22 | A kind for the treatment of technology device for the processing of high organic wastewater |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721816879.2U CN207774891U (en) | 2017-12-22 | 2017-12-22 | A kind for the treatment of technology device for the processing of high organic wastewater |
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| Publication Number | Publication Date |
|---|---|
| CN207774891U true CN207774891U (en) | 2018-08-28 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108059230A (en) * | 2017-12-22 | 2018-05-22 | 南京工业大学 | A kind for the treatment of technology device for the processing of high organic wastewater |
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2017
- 2017-12-22 CN CN201721816879.2U patent/CN207774891U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108059230A (en) * | 2017-12-22 | 2018-05-22 | 南京工业大学 | A kind for the treatment of technology device for the processing of high organic wastewater |
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