CN206457301U - A kind of decoloration device of livestock breeding wastewater - Google Patents
A kind of decoloration device of livestock breeding wastewater Download PDFInfo
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- CN206457301U CN206457301U CN201720069821.XU CN201720069821U CN206457301U CN 206457301 U CN206457301 U CN 206457301U CN 201720069821 U CN201720069821 U CN 201720069821U CN 206457301 U CN206457301 U CN 206457301U
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- decoloration device
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Abstract
The utility model discloses a kind of decoloration device of livestock breeding wastewater, including balancing reservoir, reactor, ozone generator and exhaust gas processing device, reactor is the two-stage ozone reactor being serially connected, respectively first order ozone reactor and second level ozone reactor；The top of every grade of ozone reactor is equipped with water inlet and gas outlet, bottom is equipped with delivery port and air inlet, air inlet is connected with ozone generator, and gas outlet is connected with exhaust gas processing device, and the water inlet of first order ozone reactor is connected with the delivery port of balancing reservoir；Multi-layer fixed-bed catalyst layer is provided with the inside of every grade of ozone reactor, the bottom of every grade of ozone reactor is provided with aerator.The utility model enhances the treatment effect of waste water by two-stage ozone reactor, and multi-layer fixed-bed catalyst layer is set inside ozone reactor, can avoid the loss of catalyst, can also improve the catalytic reaction efficiency of waste water.
Description
Technical field
The utility model is related to a kind of decoloration device of livestock breeding wastewater, belongs to field of waste water treatment.
Background technology
In recent years, with China's structure of agricultural production adjustment and agriculture industrialization propulsion, scale, intensive livestock and poultry support
Grow industry and be able to fast development, but a large amount of livestock breeding wastewaters of the thing followed cannot be handled effectively.Contain in livestock breeding wastewater
There are a large amount of organic pollutions, pathogenic microorganism and bacterium, color is deep, stink is dense, COD is up to 5000-40000mg/l, ammonia nitrogen is high
1000-3000mg/l, suspension is high, the exceeded decades of times of SS.Pollution from livestock and poultry turns into after industrial pollution, domestic pollution
The third-largest pollution sources, the sewage of high concentration is discharged into rivers and lakes, causes surface water, groundwater quality constantly to deteriorate, so as to make
Into severe environmental pollution, the healthy of people is directly endangered, the development of cultivation industry is also seriously constrained.
Existing handling process mainly uses anaerobic-aerobic group technology, although can effectively remove the COD of waste waterCr、BOD5
And NH3- N, but the chromaticity removing effect of waste water is not obvious, livestock breeding wastewater passes through after Aerobic Process for Treatment, and second pond goes out
Colority of water is still very high, reaches 500-2000 times (extension rate method), COD is generally 200-800mg/l, it is impossible to reach that depth takes off
The effect of color.Although existing discharge standard does not make requirement to colourity, effluent color dilution is too high very big shadow to water quality, perception
Ring, also influence the environmental benefit and social benefit of plant.Using bleaching agent, (Pig farm wastewater decolourizes and deodorization Wang Zhi tri- et al.
Research ecological sciences, 1993,2,113-116) decolouring research is carried out to the waste water of plant, have certain effect, but medicament
Consumption is excessive, and secondary pollution is heavier.
Ozone has extremely strong oxidation susceptibility, and being can be direct in a kind of oxidant of efficient non-secondary pollution, oxidizing process
Degrade or produce the organic matter in a large amount of strong oxidizing property free radicals, such as hydroxyl radical free radical (OH) decomposition water indirectly, reach drop
Low stain load and depth remove the purpose of chroma in waste water, and ozonation technology has that reaction speed is fast, simple to operate, run into
The advantages of this is relatively low, is gradually used widely.The application aspect of current ozone oxidation depth decolorization waste water of livestock poultry is still deposited
In some problems：
1) fluidised catalyst filling is in the inside of reactor, and catalyst is easily lost in the flowing of dampening, weakens
Reaction efficiency, and add operating cost；
2) ozone reaction structures typically use tower reactor, on the one hand relatively build cost high, in addition it is also necessary to which supporting consolidates
Determine device；Another aspect device structure low intensity, security is inadequate, easily by external interference；
3) ozone dosage is easily excessive, and cost is too high；On the other hand reacted substantial amounts of ozone tail gas exhaust emission
Environment；
4) before reactor water inlet, variation water quality is larger, when raw water quality changes, can influence follow-up catalysis
Reaction effect；Because equipment fault stops water inlet experiment may also can be caused to be carried out continuously.
Utility model content
The utility model makes in waste water in order to solve the above technical problems, provide a kind of decoloration device of livestock breeding wastewater
Organic matter fully contact and degraded with ozone.
The technical solution of the utility model is to provide a kind of decoloration device of livestock breeding wastewater, including balancing reservoir, reaction
Device, ozone generator and exhaust gas processing device, reactor are the two-stage ozone reactor being serially connected, respectively first order ozone
Reactor and second level ozone reactor；The top of every grade of ozone reactor is equipped with water inlet and gas outlet, and bottom is equipped with
Delivery port and air inlet, air inlet are connected with ozone generator, and gas outlet is connected with exhaust gas processing device, first order ozone
The water inlet of reactor is connected with the delivery port of balancing reservoir；Multi-layer fixed-bed catalyst is provided with the inside of every grade of ozone reactor
Layer, the bottom of every grade of ozone reactor is provided with aerator.
Further, in the inside of every grade of ozone reactor provided with 2-10 layers of fixed-bed catalytic oxidant layer.
Further, in the inside of every grade of ozone reactor provided with 4-8 layers of fixed-bed catalytic oxidant layer.
Further, the aerator is ozonation aerated disk.
Further, the shell of the balancing reservoir and reactor is made up of concrete.
Further, back washing device is set below every grade of ozone reactor.
Further, it is equipped with water pump on the water inlet pipe of balancing reservoir and reactor.
Further, the height of every grade of ozone reactor is more than 2m.
Urge by the way that by catalyst filling fixed bed, loaded on inside ozone reactor, livestock breeding wastewater is from ozone reactor top
Portion enters, and ozone gas enters from reactor bottom.When ozone flows through catalyst filling layer, in the catalytic action of catalyst
Under, the hydroxyl radical free radical for producing strong oxidizing property, hydroxyl radical free radical and the colour developing radical reaction in livestock breeding wastewater are decomposed, is reached
The effect that depth is decolourized, the air water reverse flow used enhances the mass transfer between gas, liquid, solid three-phase, improves ozone oxidation
Efficiency；Multi-layer catalyst packing layer in fixed bed inside multistage ozone reactor can reach expected catalytic effect,
Also it can guarantee that catalyst is not lost in the decrease in turn resulting in cost increase and experiment effect with current；Meanwhile, lead to smelly by bottom
The mode of oxygen, can preferably affect the flowing of livestock breeding wastewater, increase turbulences effect, improve the mass-transfer efficiency of water body,
The abundant haptoreaction of oxidizing species for making hardly degraded organic substance be produced with ozone oxidationization.
Reactor of the present utility model uses concrete structures, builds cost relatively low, it is not necessary to supporting fixing device,
High-strength structure ensures the security performance of structures.Reactor and connected device easily realize one by concrete structure
Bodyization is designed, and multiple devices is integrated in one, floor space is small.
The utility model is enhanced the treatment effect of waste water, set inside ozone reactor by two-stage ozone reactor
Multi-layer fixed-bed catalyst layer, can avoid the loss of catalyst, can also improve the catalytic reaction efficiency of waste water.
Brief description of the drawings
Fig. 1 represents the schematic diagram of the decoloration device in embodiment 1.
Embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the utility model embodiment is carried out
Clearly and completely describe, it is clear that described embodiment is only a part of embodiment of the utility model, rather than whole
Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are not under the premise of creative work is made
The every other embodiment obtained, belongs to the scope of the utility model protection.
Below by specific embodiment, the utility model is described in detail.
Embodiment 1：
The present embodiment provides a kind of decoloration device of fowl breeding wastewater, and the schematic diagram of the device is as shown in figure 1, including inside
There is the reactor 2 of fixed bed catalyst, it is actual to include two-stage ozone reactor, respectively first order ozone reactor 2a and second
Level ozone reactor 2b (for ease of describing and distinguishing, is related to first order ozone reactor and represented with a, be related to second level ozone anti-
Device is answered to be represented with b), balancing reservoir 1, ozone generator 3, exhaust gas processing device 4, the water inlet lifting water pump 5 of balancing reservoir, ozone reaction
The water inlet lifting water pump 6 of device, livestock breeding wastewater bio-chemical effluent comes water pipe 10, balancing reservoir outlet pipe 20, reactor outlet pipe
30, back washing device main sewer 40.The height of present apparatus balancing reservoir 1 is 2000mm, and width is 1000mm, and uses two-stage ozone
Reactor, every grade of ozone reactor is highly 2000mm, a diameter of 400mm, and inside loads 5 layers of fixed-bed catalytic oxidant layer and (do not marked
Number).Water inlet 7a, 7b are respectively equipped with wherein first order ozone reactor 2a and second level ozone reactor 2b, is respectively equipped with
Delivery port 8a, 8b, are respectively equipped with back washing device 9a, 9b, air inlet and the non-label in gas outlet.
When it is implemented, first, pending livestock breeding wastewater sends into balancing reservoir by the water inlet lifting water pump 5 of balancing reservoir
1.After balancing reservoir homogeneous, first order ozone reactor 2a is sent into by ozone reactor water inlet lifting water pump 6.Waste water is from first
Level ozone reactor water inlet 7a flows into first order ozone reactor 2a, anti-in fixed-bed catalytic oxidant layer with ozone from top to bottom
Should, flow out first order ozone reactor 2a, then the second level ozone for passing through series connection from the delivery port 8a of first order ozone reactor
Reactor water inlet 7b flows into second level ozone reactor 2b, likewise, carrying out after catalytic reaction, finally from ozone reactor
Delivery port 8b flows out, and is arranged into reactor outlet pipe 30 is outer.Ozone mixed gas is produced by ozone generator 3, is entered by pipeline
Ozone reactor bottom, then flow through fixed-bed catalytic oxidant layer after the aerator that ozone reactor bottom is set is dispersed
Reacted with livestock breeding wastewater bio-chemical effluent, reacted gas enters exhaust gas processing device 4, last outer row by pipeline.Ozone
Fixed bed catalyst in reactor, can effectively prevent the losing issue that comes off of catalyst.After device long-play, open smelly
The back washing device 9 being provided with oxygen reactor, it is possible to achieve air water backwash, backwash liquor is discharged by back washing device main sewer 40.
Livestock breeding wastewater passes through after Aerobic Process for Treatment, and secondary clarifier effluent handles 30min, ozone using above-mentioned decoloration device
Dosage about 50mg/l, Inlet and outlet water water quality index is as shown in the table：
It should be noted that herein, such as first and second or the like relational terms are used merely to a reality
Body or operation make a distinction with another entity or operation, and not necessarily require or imply these entities or deposited between operating
In any this actual relation or order.
Preferred embodiment of the present utility model is the foregoing is only, protection model of the present utility model is not intended to limit
Enclose.All any modification, equivalent substitution and improvements made within spirit of the present utility model and principle etc., are all contained in this reality
With in new protection domain.
Claims (8)
1. a kind of decoloration device of livestock breeding wastewater, it is characterised in that including balancing reservoir, reactor, ozone generator and tail
Flash Gas Compression Skid System, reactor is the two-stage ozone reactor being serially connected, and respectively first order ozone reactor and the second level is smelly
Oxygen reactor；The top of every grade of ozone reactor is equipped with water inlet and gas outlet, and bottom is equipped with delivery port and air inlet, enters
Gas port is connected with ozone generator, and gas outlet is connected with exhaust gas processing device, the water inlet of first order ozone reactor with
The delivery port of balancing reservoir is connected；Multi-layer fixed-bed catalyst layer, every grade of ozone reaction are provided with the inside of every grade of ozone reactor
The bottom of device is provided with aerator.
2. decoloration device as claimed in claim 1, it is characterised in that solid provided with 2-10 layers in the inside of every grade of ozone reactor
Bed catalyst layer.
3. decoloration device as claimed in claim 1, it is characterised in that solid provided with 4-8 layers in the inside of every grade of ozone reactor
Bed catalyst layer.
4. decoloration device as claimed in claim 1, it is characterised in that the aerator is ozonation aerated disk.
5. decoloration device as claimed in claim 1, it is characterised in that the shell of the balancing reservoir and reactor is by concrete system
Into.
6. decoloration device as claimed in claim 1, it is characterised in that set back washing device below every grade of ozone reactor.
7. decoloration device as claimed in claim 1, it is characterised in that be equipped with water on the water inlet pipe of balancing reservoir and reactor
Pump.
8. decoloration device as claimed in claim 1, it is characterised in that the height of every grade of ozone reactor is more than 2m.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720069821.XU CN206457301U (en) | 2017-01-20 | 2017-01-20 | A kind of decoloration device of livestock breeding wastewater |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720069821.XU CN206457301U (en) | 2017-01-20 | 2017-01-20 | A kind of decoloration device of livestock breeding wastewater |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206457301U true CN206457301U (en) | 2017-09-01 |
Family
ID=59698933
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720069821.XU Expired - Fee Related CN206457301U (en) | 2017-01-20 | 2017-01-20 | A kind of decoloration device of livestock breeding wastewater |
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| CN (1) | CN206457301U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110066065A (en) * | 2018-07-13 | 2019-07-30 | 深圳永清水务有限责任公司 | A kind of Pollution from livestock and poultry tail end wastewater advanced treatment process |
| CN110818062A (en) * | 2018-08-10 | 2020-02-21 | 四川中德盛达环境工程有限公司 | Efficient livestock and poultry breeding sewage deep oxidation and decoloration process |
| CN110885152A (en) * | 2018-09-07 | 2020-03-17 | 江苏三强环境工程有限公司 | Novel double-tower ozone disinfection tower |
-
2017
- 2017-01-20 CN CN201720069821.XU patent/CN206457301U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110066065A (en) * | 2018-07-13 | 2019-07-30 | 深圳永清水务有限责任公司 | A kind of Pollution from livestock and poultry tail end wastewater advanced treatment process |
| CN110818062A (en) * | 2018-08-10 | 2020-02-21 | 四川中德盛达环境工程有限公司 | Efficient livestock and poultry breeding sewage deep oxidation and decoloration process |
| CN110885152A (en) * | 2018-09-07 | 2020-03-17 | 江苏三强环境工程有限公司 | Novel double-tower ozone disinfection tower |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address | ||
| CP03 | Change of name, title or address |
Address after: 518052 Room 201, building A, 1 front Bay Road, Shenzhen Qianhai cooperation zone, Shenzhen, Guangdong Patentee after: Shenzhen Yongqing water limited liability company Address before: 410330 the 319 National Road of Liuyang National Economic Development Zone, Changsha, Hunan. Patentee before: HUNAN YONKER WATER CO., LTD. |
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| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170901 Termination date: 20210120 |