CN2672046Y - Slide arc discharge plasma organic waste water treating device - Google Patents
Slide arc discharge plasma organic waste water treating device Download PDFInfo
- Publication number
- CN2672046Y CN2672046Y CN 200420019724 CN200420019724U CN2672046Y CN 2672046 Y CN2672046 Y CN 2672046Y CN 200420019724 CN200420019724 CN 200420019724 CN 200420019724 U CN200420019724 U CN 200420019724U CN 2672046 Y CN2672046 Y CN 2672046Y
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- waste water
- gas
- organic waste
- arc discharge
- discharge plasma
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Abstract
The utility model discloses a slide arc discharge plasma organic waste water treating device The isolated base of a reaction cover is provided with a knife-shaped bifurcation electrode which is connected with a high-voltage power supply. A waste-liquid holding tank connected with a waste water tank is arranged in the middle part of the isolated base. The mouth of the waste-liquid holding tank is provided with an atomizing nozzle. The upper part of the reaction cover is provided with a gas-sampling mouth and a gas-exhaust pipeline whose outside is provided with a water cooling jacket. Compressed air and the waste water tank are separately connected to the atomizing nozzle through conduit pipes. Waste water and the compressed air turn into waste water vapour to be processed through the air atomizing nozzle. The mixture of gas and water pushes the sliding electric arc forming at the starting end of the arc to move downstream and generate gas-liquid mixture sliding arc to discharge electric power. Ozone, ultraviolet rays, high-energy electron, electrolytic action, OH, O and other active particles generating directly affect the waste water to be processed, therefore, the online electro-discharge treatment can be realized. The utility model is in particular used to process high concentrated organic waste water which is difficult to degradate, and no matter how high the density is, after being treated, the removing rate of COD, BOD, etc. can reach more than 99%.
Description
Affiliated technical field
The utility model relates to wastewater treatment equipment, relates in particular to a kind of Slip Arc Discharge Plasma Organic Waste Plant.
Background technology
The processing of the organic waste water especially processing of high concentrated organic wastewater is remained a stubborn problem; perplexing industries such as chemical pharmaceutical; a lot of in the prior art to method of wastewater treatment; biochemical process, electrolytic process and the flocculences etc. that conventional recommendation is used all are difficult to solution and contain complicated organic waste water handling problem, and this also is the environment protection urgent problem.Adopt research that the nonthermal plasma chemistry method handles trade effluent in the world the time not long, the method that has proposed has Pulse Discharge Treatment method in high-power electron beam method and the water.Because the density of water is far longer than the density of gas, when electronics directive water and the time, the high energy electricity in the frequent impact of water molecules in lose kinetic energy very soon, its penetration depth is very small, thereby is difficult to handle the water of big flow.The pulse arc discharge treating water is carried out in the utilization of impulsive discharge method in the water in water, discharge portion is confined to two interelectrode discharge channels with contacting of water, contact is long-pending little, main rely on the propagation of shockwave in water of discharge generation to play germicidal action, the part that being confined to of working of the molecule of objectionable impurities contacted with discharge channel.Therefore, these two kinds of methods all are difficult to realize large-scale processing.
The gliding arc discharge plasma body is an incipient in recent years new technology, and is used on the environmental protection technology, and this method can be at normal atmosphere or more produced nonequilibrium plasma under the high pressure, utilizes gliding arc discharge technology governance H abroad in recent years
2S, SO
2, N
2The research report of waste gas such as O utilizes gliding arc discharge to administer Study on wastewater or report but at home and abroad there is no.
Summary of the invention
The purpose of this utility model provides a kind of Slip Arc Discharge Plasma Organic Waste Plant, adopts the gliding arc discharge plasma body to be applicable to the processing high-concentration organic sewage difficult to degrade.
In order to achieve the above object, the technical solution adopted in the utility model is that it comprises: the bottom in reaction hood is equipped with insulator foot from bottom to up successively, be equipped with down big little on the monosymmetric insulation column of insulator foot respectively, the cutter type that links to each other with high-voltage power supply divides interdigitated electrode and forms starting the arc end, there is the waste collection groove that links to each other with wastewater trough at the insulator foot middle part, waste collection groove notch is equipped with the nozzle that is fixed on the insulator foot, the gas sampling mouth is equipped with on the top of reaction hood successively, gas exhaust duct, gas exhaust duct is equipped with the watercooling jacket that links to each other with fluid collection vials with catheter outward, and the pressurized air of air compressor and the waste water of wastewater trough insert nozzle together by conduit respectively.
The utility model is compared with background technology, the useful effect that has is: plasma body wastewater treatment of the present utility model mainly is that biochemical process is compared with present wastewater treatment industry, the plasma waste water treater has higher advantage, (1) it can Continuous Wastewater Treatment, do not need the long residence time, the organic pollutant removal non-selectivity; (2) the raw material cheapness of manufacturing electrode, system's floor space is little, and operations and maintenance is convenient, can realize automatization control with comparalive ease, with the quality that guarantees to handle; (3) do not need to add running stores such as medicament, only need electric power, conveniently be easy to get.
The utility model can adopt interval type and continous way, as makes single equipment, is used for the less factory of wastewater flow rate output etc., and continous way can be widely used in the bigger factory of wastewater flow rate output.Be mainly used in the high concentrated organic wastewater of difficult degradation, as the waste water of industries such as chemical reaction, dyestuff, printing and dyeing, fermentation, pharmacy, papermaking generation.No matter many height all can reach more than 99% by handling clearances such as back COD, BOD organic waste water concentration.
Description of drawings
Below in conjunction with drawings and Examples the utility model is further described.
Accompanying drawing is a structural representation of the present utility model.
Among the figure: 1 air compressor, 2 High-Voltage Insulation lines, 3 insulator foots, 4 insulation columns, 5 cutter types divide interdigitated electrode, 6 reaction hood, 7 wastewater troughs, 8 high-voltage power supplies, 9 waste collection grooves, 10 nozzles, 11 starting the arc ends, 12 slip electric arcs, 13 reservoirs, 14 catheters, 15 gas sampling mouths, 16 gas exhaust ducts, 17 watercooling jackets, 18 tail gas.
Embodiment
As shown in drawings, the utility model comprises: the bottom in reaction hood 6 is equipped with insulator foot 3 from bottom to up successively, be equipped with down big little on the insulator foot 3 monosymmetric insulation columns 4 respectively, the cutter type that links to each other with high-voltage power supply 8 divides interdigitated electrode 5 and forms starting the arc end 11, there is the waste collection groove 9 that links to each other with wastewater trough 7 at insulator foot 3 middle parts, waste collection groove 9 notches are equipped with the nozzle 10 that is fixed on the insulator foot 3, gas sampling mouth 15 is equipped with on the top of reaction hood 6 successively, gas exhaust duct 16, the gas exhaust duct 16 outer watercooling jackets 17 that link to each other with fluid collection vials 13 with catheter 14 that are equipped with, the waste water of the pressurized air of air compressor 1 and wastewater trough 7 inserts nozzle 10 together by conduit respectively.
Said nozzle 10, its nozzle diameter are 1~5mm, and model can adopt SUJ11, SUJ12 etc.
The minimum place of distance is 2~5mm between cutter type bifurcated two electrodes 5 at said starting the arc end 11 places.
The plasma method of wastewater treatment is to connect 10KV ac high voltage source 8, waste water solution passes through the sucking-off of gas injection from aqua storage tank 7, the waste water of the pressurized air of air compressor 1 and wastewater trough 7 sprays the speed of air-water mixtures greater than 10m/s by air atomization nozzle 10, generation is less than 15 microns waste water atomizing particle, waste water water smoke promotes the mobile downstream gliding arc discharge that produces of slip electric arc 12 that starting the arc end 11 forms, under normal pressure, obtain nonequilibrium plasma, produce ozone, ultraviolet ray, high-energy electron, electrolytic action, OH and O isoreactivity particle directly act on processed waste water, realize online discharge process, and make waste water change harmless object into.The time decision that treatment time is mainly stopped in the gliding arc discharge zone by water smoke, the water smoke flow is regulated by nozzle 10.Sample by gas sampling mouth 15, tail gas 18 is discharged by gas exhaust duct 16, and under the cooling of watercooling jacket 17, steam is condensed into liquid, flows into reservoir 13 by catheter 14.
Method of wastewater treatment described in the utility model and device can play following effect:
In the gliding arc discharge plasma body, every slip electric arc is exactly a plasma channel, will produce particles such as a large amount of high-energy electrons, ion, free radical etc. under the high temperature in plasma channel, the high pressure, as following each reaction formula:
High-energy electron and living radical (O, OH, e
Aq -, HO
2 -Deng) will bombard and the oxidation of organic compounds molecule, making its eventual degradation is CO
2And H
2Innoxious substances such as O.Simultaneously, because the generation of high temperature, high pressure plasma passage, ((3~10Gpa), make to cause following several physical-chemical reaction process in the solution of plasma channel field and external region thereof: ozone oxidation, ultraviolet photodissociation, electrohydraulic cavitation degradation and supercritical water oxidation are degraded for wavelength 75~185nm) and huge impact ripple to be accompanied by the intensive UV-light.People such as the Wei Erbai of California, USA technical institute adopt liquid electricimpulse plasma body P-Chlorophenol, and organism such as TNT carry out degradation experiment.Through 1 fen clock time, (each discharge power consumption 4~7KJ) made these several organic clearances reach 99% to about 200 times high-energy discharge.
After plasma channel forms, because it has high temperature, it just looks like a light source that outwards gives off strong UV-light, institute's radiating UV-light is absorbed by the atomizing droplet around the plasma channel at once, impel the dissolved oxygen in the water to produce excited oxygen atom and organic molecule effect, reach the purpose of oxidation of organic compounds.
Because the enormous impact pressure wave that the outwards rapid expansion of plasma channel causes by means of liquid electricity cavitation (bubble) effect, directly acts on organic molecule it is carried out the DeR of pyrolysis and free radical.
Because the atomizing droplet transmission towards periphery of the heat of plasma channel has caused the generation of many steam bubbles.In these bubbles, the supercritical water that is enough to form transient state that temperature and pressure is high.Therefore, organism in the bubble and oxygen and supercritical water dissolve each other fully, make the spontaneous beginning oxidation of organism.
In sum, the organic process of gliding arc discharge plasma degradation is quite complicated, is a mutual alternative process of multiple oxidation.
Processing example of the present utility model is as follows, the processing condition of method are: 7000~10000 volts of voltages, frequency 50Hz, the cutter type divides interdigitated electrode long 160mm, wide 35mm, thick 2.5mm, nozzle nozzle diameter 1mm, air pressure 0.3~1.5MP in the nozzle, experimental article pick up from certain pharmaceutical factory pharmacy waste water and produce the concentrating spent liquor of DSD acid.
Experimental article: pharmacy waste water
Experiment condition: voltage 10kV, waste liquid flow 42.4ml/min, gas flow 11.2l/min, carrier gas air.
Pharmacy waste water (unit: mg/l)
Test item does not adopt this skill to adopt present technique
The order art
COD
cr 1570 7
BOD
5 1340 9
NH3_N 1200 3
Experimental article: the concentrating spent liquor of producing DSD acid
Experiment condition: voltage 10kV, waste liquid flow 40.9ml/min, gas flow 10.7l/min, carrier gas air.
DSD acid concentrating spent liquor (unit: mg/l)
Test item does not adopt this skill to adopt present technique
The order art
COD
cr 1.46×10
5 97
BOD
5 4660 37
NH3_N 8040 29
Measuring method
BOD
5: dilution and inoculation method GB7488-87;
COD
Cr: potassium dichromate process GB11914-89;
NH3-N: nessler reagent colorimetry GB7479-87;
Experimental result shows that organic waste water is fine through nuisance removal effect after this art breading.
Claims (3)
1, a kind of Slip Arc Discharge Plasma Organic Waste Plant, it is characterized in that comprising: the bottom in reaction hood (6) is equipped with insulator foot (3) from bottom to up successively, be equipped with down big little on the monosymmetric insulation column of insulator foot (3) (4) respectively, the cutter type that links to each other with high-voltage power supply (8) divides interdigitated electrode (5) and forms starting the arc end (11), there is the waste collection groove (9) that links to each other with wastewater trough (7) at insulator foot (3) middle part, waste collection groove (9) notch is equipped with the nozzle (10) that is fixed on the insulator foot (3), gas sampling mouth (15) is equipped with on the top of reaction hood (6) successively, gas exhaust duct (16), the outer watercooling jacket (17) that links to each other with reservoir (13) with catheter (14) that is equipped with of gas exhaust duct (16), the waste water of the pressurized air of air compressor (1) and wastewater trough (7) inserts nozzle (10) together by conduit respectively.
2, a kind of Slip Arc Discharge Plasma Organic Waste Plant according to claim 1 is characterized in that: said nozzle (10), its nozzle diameter are 1~5mm.
3, a kind of Slip Arc Discharge Plasma Organic Waste Plant according to claim 1 is characterized in that: the minimum place of distance is 2~5mm between cutter type bifurcated two electrodes (5) that said starting the arc end (11) is located.
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CN 200420019724 CN2672046Y (en) | 2004-01-16 | 2004-01-16 | Slide arc discharge plasma organic waste water treating device |
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CN 200420019724 CN2672046Y (en) | 2004-01-16 | 2004-01-16 | Slide arc discharge plasma organic waste water treating device |
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Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2011098918A2 (en) | 2010-02-10 | 2011-08-18 | Alfredo Zolezzi-Garreton | Method and apparatus for applying plasma particles to a liquid and use for disinfecting water |
CN103210702A (en) * | 2011-01-26 | 2013-07-17 | 深圳市泓耀环境科技发展股份有限公司 | Adding method for combustion additive for combustion of liquid fuel and plasmatron device therefor |
CN103341307A (en) * | 2013-06-19 | 2013-10-09 | 浙江大学 | Method and apparatus for removing durable organic pollutants from large flow incinerator exhaust |
CN103539067A (en) * | 2013-07-26 | 2014-01-29 | 路运龙 | Combined arc discharge plasma water decomposition hydrogen production method and hydrogen production system |
CN109864646A (en) * | 2019-04-01 | 2019-06-11 | 安徽理工大学 | A kind of air plasma hand washing machine without water flow |
CN114599143A (en) * | 2020-12-04 | 2022-06-07 | 中国科学院大连化学物理研究所 | Sliding arc discharge plasma generating system |
-
2004
- 2004-01-16 CN CN 200420019724 patent/CN2672046Y/en not_active Expired - Lifetime
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2011098918A2 (en) | 2010-02-10 | 2011-08-18 | Alfredo Zolezzi-Garreton | Method and apparatus for applying plasma particles to a liquid and use for disinfecting water |
CN102870502A (en) * | 2010-02-10 | 2013-01-09 | 阿尔弗雷多·佐莱齐-加勒东 | Method and apparatus for applying plasma particles to a liquid and use for disinfecting water |
CN103210702A (en) * | 2011-01-26 | 2013-07-17 | 深圳市泓耀环境科技发展股份有限公司 | Adding method for combustion additive for combustion of liquid fuel and plasmatron device therefor |
CN103341307A (en) * | 2013-06-19 | 2013-10-09 | 浙江大学 | Method and apparatus for removing durable organic pollutants from large flow incinerator exhaust |
CN103341307B (en) * | 2013-06-19 | 2015-06-17 | 浙江大学 | Method and apparatus for removing durable organic pollutants from large flow incinerator exhaust |
CN103539067A (en) * | 2013-07-26 | 2014-01-29 | 路运龙 | Combined arc discharge plasma water decomposition hydrogen production method and hydrogen production system |
CN109864646A (en) * | 2019-04-01 | 2019-06-11 | 安徽理工大学 | A kind of air plasma hand washing machine without water flow |
CN114599143A (en) * | 2020-12-04 | 2022-06-07 | 中国科学院大连化学物理研究所 | Sliding arc discharge plasma generating system |
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Legal Events
Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
AV01 | Patent right actively abandoned |
Effective date of abandoning: 20040116 |
|
C25 | Abandonment of patent right or utility model to avoid double patenting |