CN205773786U - A kind of processing system containing orange G organic wastewater - Google Patents
A kind of processing system containing orange G organic wastewater Download PDFInfo
- Publication number
- CN205773786U CN205773786U CN201620309967.2U CN201620309967U CN205773786U CN 205773786 U CN205773786 U CN 205773786U CN 201620309967 U CN201620309967 U CN 201620309967U CN 205773786 U CN205773786 U CN 205773786U
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- reaction device
- organic wastewater
- electrolysis
- catalytic oxidation
- processing system
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Abstract
The utility model discloses a kind of processing system containing orange G organic wastewater, it includes passing sequentially through, according to water (flow) direction, electrolysis reaction device, catalytic oxidation reaction device, sedimentation tank, filtering ponds and the ultrafiltration apparatus that pipeline connects；Control valve it is provided with on pipeline between electrolysis reaction device and catalytic oxidation reaction device and between catalytic oxidation reaction device and sedimentation tank；The inlet of electrolysis reaction device connects the conveyance conduit of the organic wastewater of conveying orange G, this conveyance conduit is provided with elevator pump and controls to enter the effusion meter of the wastewater flow in electrolysis reaction device；Described electrolysis reaction device has air-blast device with being connected bottom catalytic oxidation reaction device.Processing system containing orange G organic wastewater described in the utility model is possible not only to orange G dyestuff and other organic principles effectively removing in organic wastewater, it is also possible to purifying water body further, reduces cost, improves efficiency；Water body after treatment can enter directly in life water body.
Description
Technical field
This utility model relates to technical field of waste water processing, is specifically related to a kind of place containing orange G organic wastewater
Reason system.
Background technology
Orange G is a kind of azo-type chemical dye, and molecular formula is C16H10N2Na2O7S2, this compounds has
-N=N-chromophoric group, is one of conventional dyestuff of printing and dyeing mill, and the annual usage amount in the whole world accounts for the 50% of total dyestuff
Above, it is widely used in the industries such as weaving, process hides, papermaking, rubber.Owing to this compounds difficult degradation is led
Cause one of the industrial wastewater that dyeing waste water is at present relatively refractory reason, had that colourity is deep, COD concentration is high, alkali
The feature such as property is big, organic principle is complicated, salinity is high, biodegradability is poor.The place of waste water from dyestuff includes at present
Biological oxidation process, chemical oxidization method, active carbon adsorption, flocculence and electrochemical process.
Although wastewater processing technology has already been through the development of more than 100 year, the pollutant kind in sewage, sewage
Amount be as socio-economic development, growth in the living standard and be continuously increased, sewage disposal technology is also with section
The development that learns a skill and there occurs change with rapid changepl. never-ending changes and improvements, meanwhile, old sewage disposal technology is the most constantly removed from office
New and develop.The most present pollutant in chemical industrial organic wastewater are diversified, often by one
Technique can not by pollutant removal all of in waste water totally.By single a kind of technique by organic wastewater
Process discharge standard difficulty very big, and operating cost is higher；Organic wastewater is organic containing more difficult degradation
Thing, biodegradability is poor, and the waste water water quantity and quality of organic wastewater changes greatly, therefore directly uses at biochemical method
Reason wastewater from chemical industry effect is less desirable.
Utility model content
In order to overcome the deficiencies in the prior art, the purpose of this utility model is to provide one organic containing orange G
The processing system of waste water, by setting a processing system, in conjunction with multiple treatment technology, reduces cost, carries
High efficiency, enables the water body after this system processes to enter directly in life water body.
For solving the problems referred to above, the technical scheme that this utility model is used is as follows:
A kind of processing system containing orange G organic wastewater, it includes passing sequentially through pipeline even according to water (flow) direction
Electrolysis reaction device, catalytic oxidation reaction device, sedimentation tank, filtering ponds and the ultrafiltration apparatus connect；Electrolysis
Pipeline between reaction unit and catalytic oxidation reaction device and between catalytic oxidation reaction device and sedimentation tank
On be provided with control valve；The inlet of electrolysis reaction device connects the conveying of the organic wastewater of conveying orange G
Pipeline, this conveyance conduit is provided with elevator pump and controls to enter the stream of the wastewater flow in electrolysis reaction device
Gauge；Described electrolysis reaction device has air-blast device with being connected bottom catalytic oxidation reaction device.
Further in scheme, electrolysis reaction device described in the utility model is Multi-phase iron-carbon micro-electrolysis reaction
Device, this Multi-phase iron-carbon micro-electrolysis reactor includes reaction tower and the ferrum carbon electrolysis unit being positioned in reaction tower, institute
State ferrum carbon electrolysis unit to include at least connecting by lower from the electrolysis band being above fixed in reaction tower, each electrolysis band
Including the cavity surrounded by two-layer grid and the heterogeneous ferrum carbon filler being positioned in cavity.
Further in scheme, catalytic oxidation reaction device described in the utility model includes catalytic oxidation
Tower, the agitating device being fixed in catalytic oxidation tower, described catalytic oxidation top of tower is provided with throwing
Put the dog-house of catalyst and oxidant.
Further in scheme, catalytic oxidation tower bottom described in the utility model is additionally provided with heater.
Further in scheme, ultrafiltration apparatus described in the utility model includes several rolled film cores.
Further in scheme, the processing system containing orange G organic wastewater described in the utility model also includes
With the clear water reserviors that water end (W.E.) is connected that filter of ultrafiltration apparatus, the connection of described clear water reserviors has webmaster.
Further in scheme, the processing system containing orange G organic wastewater described in the utility model also includes
Reverse osmosis unit, the concentration water end (W.E.) of described ultrafiltration apparatus is provided with concentration pond, concentrates pond and fills with reverse osmosis
Putting and connected by water pipe, the water side of reverse osmosis unit connects webmaster.
Further in scheme, between reverse osmosis unit described in the utility model and concentration pond, it is provided with water
Pump.
Compared to existing technology, the beneficial effects of the utility model are: described in the utility model containing orange G
The processing system of organic wastewater, by setting a processing system, in conjunction with multiple treatment technology, has been possible not only to
Effect removes the orange G dyestuff in organic wastewater and other organic principles, it is also possible to purifying water body further, fall
Low cost, improves efficiency；Water body after system described in the utility model processes can enter directly into
In life water body.
With detailed description of the invention, this utility model is described in further detail below in conjunction with the accompanying drawings.
Accompanying drawing explanation
Fig. 1 is the structural representation of the processing system containing orange G organic wastewater described in the utility model；
Fig. 2 is this utility model processing system structural representation preferably containing orange G organic wastewater；
Wherein, each reference is: 10, electrolysis reaction device；11, reaction tower；12, ferrum carbon electrolysis group
Part；20, catalytic oxidation reaction device；21, catalytic oxidation tower；22, agitating device；23, heating
Device；30, sedimentation tank；40, filtering ponds；50, ultrafiltration apparatus；51 concentrate pond；60, conveyance conduit；
61, elevator pump；62, effusion meter；70, air-blast device；80, clear water reserviors；90, reverse osmosis unit.
Detailed description of the invention
As it is shown in figure 1, the processing system containing orange G organic wastewater described in the utility model, it include by
The electrolysis reaction device 10 of pipeline connection, catalytic oxidation reaction device 20, precipitation is passed sequentially through according to water (flow) direction
Pond 30, filtering ponds 40 and ultrafiltration apparatus 50；Electrolysis reaction device 10 and catalytic oxidation reaction device 20
Between and catalytic oxidation reaction device 20 and sedimentation tank 30 between pipeline on be provided with control valve；Electricity
The inlet solving reaction unit 10 connects the conveyance conduit 60 of the organic wastewater carrying orange G, this conveying pipe
It is provided with elevator pump 61 on road 60 and controls to enter the effusion meter 62 of the wastewater flow in electrolysis reaction device 10；
Described electrolysis reaction device 10 has air-blast device 70 with being connected bottom catalytic oxidation reaction device 20.
Further in scheme, electrolysis reaction device 10 described in the utility model is that Multi-phase iron-carbon micro-electrolysis is anti-
Answering device, this Multi-phase iron-carbon micro-electrolysis reactor includes reaction tower 11 and the ferrum carbon electrolysis unit being positioned in reaction tower
12, described ferrum carbon electrolysis unit includes at least connecting by lower from the electrolysis band being above fixed in reaction tower, each
Electrolysis band includes the cavity surrounded by two-layer grid and the heterogeneous ferrum carbon filler being positioned in cavity.
Further in scheme, catalytic oxidation reaction device 20 described in the utility model includes that catalysis oxidation is anti-
The agitating device 22 answer tower 21, being fixed in catalytic oxidation tower 21, described catalytic oxidation tower 21
Top is provided with input catalyst and the dog-house of oxidant.
In order to further speed up catalytic oxidation, improve efficiency, in further scheme, this utility model
It is additionally provided with heater 23 bottom described catalytic oxidation tower 21.
Further in scheme, ultrafiltration apparatus 50 described in the utility model includes several rolled film cores.
Further in scheme, the processing system containing orange G organic wastewater described in the utility model also includes
With the clear water reserviors 80 that water end (W.E.) is connected that filter of ultrafiltration apparatus 50, the connection of described clear water reserviors 80 has webmaster.
Owing to condensed water can be produced in ultra-filtration process, in order to avoid condensed water is wasted, further scheme
In, the processing system containing orange G organic wastewater described in the utility model also includes reverse osmosis unit 90, institute
The concentration water end (W.E.) stating ultrafiltration apparatus 50 is provided with concentration pond 51, concentrates pond 51 and leads to reverse osmosis unit 90
Cross water pipe to connect；The water side of reverse osmosis unit 90 connects webmaster.Preferably, the water outlet of reverse osmosis unit
It is provided with the clear water reserviors for storing clear water between end connection and webmaster.
For the ease of being delivered in reverse osmosis unit be further processed by the condensed water after ultrafiltration, condensed water
Further in scheme, it is provided with between reverse osmosis unit 90 described in the utility model and concentration pond 51
Water pump.
Above-mentioned embodiment is only preferred implementation of the present utility model, it is impossible to limit this practicality with this new
The scope of type protection, any unsubstantiality that those skilled in the art is done on the basis of this utility model
Change and replacement belong to this utility model scope required for protection.
Claims (8)
1. the processing system containing orange G organic wastewater, it is characterised in that it includes passing sequentially through, according to water (flow) direction, electrolysis reaction device, catalytic oxidation reaction device, sedimentation tank, filtering ponds and the ultrafiltration apparatus that pipeline connects；Control valve it is provided with on pipeline between electrolysis reaction device and catalytic oxidation reaction device and between catalytic oxidation reaction device and sedimentation tank；The inlet of electrolysis reaction device connects the conveyance conduit of the organic wastewater of conveying orange G, this conveyance conduit is provided with elevator pump and controls to enter the effusion meter of the wastewater flow in electrolysis reaction device；Described electrolysis reaction device has air-blast device with being connected bottom catalytic oxidation reaction device.
Processing system containing orange G organic wastewater the most according to claim 1, it is characterized in that, described electrolysis reaction device is Multi-phase iron-carbon micro-electrolysis reactor, this Multi-phase iron-carbon micro-electrolysis reactor includes reaction tower and the ferrum carbon electrolysis unit being positioned in reaction tower, described ferrum carbon electrolysis unit include at least two by lower from the electrolysis band being above fixed in reaction tower, each electrolysis band includes the cavity surrounded by two-layer grid and the heterogeneous ferrum carbon filler being positioned in cavity.
Processing system containing orange G organic wastewater the most according to claim 1, it is characterized in that, described catalytic oxidation reaction device includes that catalytic oxidation tower, the agitating device being fixed in catalytic oxidation tower, described catalytic oxidation top of tower are provided with input catalyst and the dog-house of oxidant.
Processing system containing orange G organic wastewater the most according to claim 3, it is characterised in that described catalytic oxidation tower bottom is additionally provided with heater.
Processing system containing orange G organic wastewater the most according to claim 1, it is characterised in that described ultrafiltration apparatus includes several rolled film cores.
6., according to the processing system containing orange G organic wastewater described in any one of claim 1-5, it is characterised in that it also includes the clear water reserviors that water end (W.E.) is connected that filter with ultrafiltration apparatus, the connection of described clear water reserviors has webmaster.
7. according to the processing system containing orange G organic wastewater described in any one of claim 1-5, it is characterized in that, this processing system containing orange G organic wastewater also includes reverse osmosis unit, the concentration water end (W.E.) of described ultrafiltration apparatus is provided with concentration pond, concentrating pond to be connected by water pipe with reverse osmosis unit, the water side of reverse osmosis unit connects webmaster.
Processing system containing orange G organic wastewater the most according to claim 7, is provided with water pump between described reverse osmosis unit and concentration pond.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620309967.2U CN205773786U (en) | 2016-04-13 | 2016-04-13 | A kind of processing system containing orange G organic wastewater |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620309967.2U CN205773786U (en) | 2016-04-13 | 2016-04-13 | A kind of processing system containing orange G organic wastewater |
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| Publication Number | Publication Date |
|---|---|
| CN205773786U true CN205773786U (en) | 2016-12-07 |
Family
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620309967.2U Expired - Fee Related CN205773786U (en) | 2016-04-13 | 2016-04-13 | A kind of processing system containing orange G organic wastewater |
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| CN (1) | CN205773786U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107055740A (en) * | 2017-04-13 | 2017-08-18 | 河海大学 | A kind of method that hydroquinones promotes ferriferous oxide catalyzing hydrogen peroxide degraded orange G waste water |
-
2016
- 2016-04-13 CN CN201620309967.2U patent/CN205773786U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107055740A (en) * | 2017-04-13 | 2017-08-18 | 河海大学 | A kind of method that hydroquinones promotes ferriferous oxide catalyzing hydrogen peroxide degraded orange G waste water |
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| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20161207 Termination date: 20170413 |
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| CF01 | Termination of patent right due to non-payment of annual fee |