CN102775000B - A kind of Waste Water Treatment and method - Google Patents

A kind of Waste Water Treatment and method Download PDF

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Publication number
CN102775000B
CN102775000B CN201210303138.XA CN201210303138A CN102775000B CN 102775000 B CN102775000 B CN 102775000B CN 201210303138 A CN201210303138 A CN 201210303138A CN 102775000 B CN102775000 B CN 102775000B
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waste water
pond
process pond
ozone
water
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CN201210303138.XA
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CN102775000A (en
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许以青
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  • Treatment Of Water By Oxidation Or Reduction (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
  • Physical Water Treatments (AREA)

Abstract

The present embodiments relate to a kind of use physical method to combine with chemical method to carry out the method and system of waste water process.First process pond, device and ozone flow in pipes are freeed equipped with ultrasonic wave in described first process pond;Second process pond, receives and processes the waste water after pond is processed through described first, and described second process pond applies high-voltage pulse equipped with high-frequency pulse voltage generator, the waste water in this second process pond;3rd process pond, receives and processes the waste water after pond is processed through described second, and waste water carries out precipitation in described 3rd process pond and decomposes, and the 3rd process pond dress is also equipped with pH value adjuster;Collecting pit 40, described 3rd process pond UNICOM, receive the waste water after the described 3rd processes pond process and be collected;Fourth process pond, described collecting pit UNICOM, receive the water in collecting pit, Waste Water Treatment is discharged carry out reverse osmosis (RO) process to water therein after in this fourth process pond.

Description

A kind of Waste Water Treatment and method
Technical field
The present embodiments relate to sewage treatment area, particularly a kind of employing physical method and chemical method phase are tied Close the method and system carrying out waste water process.
Background technology
With social development, the increase of population and increasingly industrialize widely, in the daily life of the mankind Produce increasing sewage and waste water.Waste water mainly has sanitary sewage, industrial wastewater, refuse leachate, medical science Medical waste water etc..Particularly refuse leachate, its comprise the organic pollution of high concentration, virus, germ, Breeding acid, ammonia and nitrogen components and all kinds of heavy metals etc., use traditional waste water treatment process to be difficult to reach discharge standard, And the medical waste water of medical science includes more germ, virus etc. and requires higher to the process purifying.Traditional waste water Processing method is the chemical method of blow-off method and the increase chemical reagent using physics mostly.Blow-off method is used to need to build If bulky process pond, and the effect of stripping is limited, and it is difficult that similar ammonia and nitrogen components has certain dissolubility With blowout, and waste gas isolated in waste water is directly entered in air by blow-off method, causes secondary pollution.And Chemical method needs substantial amounts of chemical addition agent, and cost is high, and the process that in fact most chemical addition agent manufactures In inherently can produce the pollutants such as waste water and gas, actually can be absorbed in the vicious circle of dirty pollution treatment.
Entire society is more and more urgent to the demand of environmental protection, it is therefore desirable to a kind of simple effective, it is not necessary to a large amount of Chemical addition agent, floor space is little, low cost, the good method of wastewater treatment of effect.
Content of the invention
The open a kind of Waste Water Treatment of the embodiment of the present invention, uses the side that physical method combines with chemical method Formula carries out waste water process, is that waste water produces cavitation by increasing ultrasonic wave, is injected simultaneously into ozone, fully Oxidation under remove ammonia nitrogen, filter the heavy metal etc. in waste water further with high-frequency pulse voltage.
A kind of Waste Water Treatment, comprising:
First process pond, described first process pond is equipped with supersonic generator and ozone flow in pipes, described ozone Flow in pipes injection of ozone in described waste water;Described supersonic generator is dipped in and enters the useless of this first process pond In water, produce ul-trasonic irradiation and in the waste water entering the described first process pond, the cavitation utilizing ultrasonic wave is made With accelerating the oxidation disinfection effect to waste water for the ozone, described supersonic generator is the ultrasonic generation of tabular packaged type Device, is also equipped with water circulating pump in described first process pond and the waste water in the first process pond is circulated;
Second process pond, receive through described first process pond process after waste water, described second process pond equipped with High-frequency pulse voltage generator, this high-frequency pulse voltage generator includes discharge electrode, and described discharge electrode uses iron plate Or aluminium sheet material, this discharge electrode is dipped in the waste water in the described second process pond, giving up in this second process pond Water applies high-voltage pulse;
3rd process pond, receives and processes the waste water after pond is processed through described second, and waste water is processed the described 3rd Carrying out MRB process in pond and carrying out precipitation decomposition, the 3rd process pond dress is also equipped with pH value adjuster, to PH value conditioning agent is added in 3rd process pond.
Described system can also include:
Collecting pit, described 3rd process pond UNICOM, receive the waste water after the described 3rd processes pond process and carry out Collect;
Fourth process pond, described collecting pit UNICOM, receive the water in collecting pit, this fourth process pond pair Water therein discharges Waste Water Treatment after carrying out reverse osmosis (RO) process.
The further embodiment of the present invention gives the method carrying out waste water process, comprising:
Carry out ultrasonic irradiation to waste water, removed the ammonia nitrogen in waste water to described waste water injection of ozone simultaneously and become Point;
Continue to apply high-frequency pulse voltage in order to remove the heavy metal element in waste water to waste water;
PH value conditioning agent, the at ordinary times Acidity of Aikalinity of waste water is added in waste water;
Through the above-mentioned waste water processing, importing processes pond and utilizes MRB processing system 301 to carry out at MRB Manage and carry out precipitation and decompose, then carry out reverse osmosis (RO) process, discharge after finally collecting.
In above-mentioned method and system, supersonic generator 101 produces the ultrasonic wave of 10-20kHz.
The Waste Water Treatment of the embodiment of the present invention and method, it is not necessary to increase chemical addition agent, pass through ultrasonic wave With effect while ozone, waste water is substantially oxidized, and the effect of ultrasonic wave and ozone is to the sky processing pond Between less demanding, therefore size and the floor space of processing system, high frequency suitably can be set according to treating capacity Also being readily available and act on of pulse voltage, therefore whole system and method are simply effective, it is easy to the place to waste water Reason.
Brief description
Fig. 1 is one embodiment of the invention Waste Water Treatment structural representation.
Fig. 2 is the top view of one module of embodiment of the present invention discharge electrode.
Fig. 3 is another embodiment of the present invention Waste Water Treatment structural representation.
Fig. 4 is further embodiment of this invention Waste Water Treatment structural representation.
Fig. 5 is the method flow diagram that embodiment of the present invention waste water is processed.
Detailed description of the invention
For the process demand to waste water particularly refuse leachate now, provide a kind of Waste Water Treatment.? In this system, use the mode that combines with ozone of ultrasonic wave, carry out physics and chemical treatment, sufficiently simultaneously Separate the harmful components in waste water, carry out high-frequency pulse voltage process further simultaneously, filter the huge sum of money in waste water Belong to composition.
Refering to 1, the structural representation of one embodiment of the invention Waste Water Treatment.Waste Water Treatment includes:
First process pond 10, frees device and ozone flow in pipes 103 equipped with ultrasonic wave in the first process pond 10.
By introducing pipeline, waste water introducing the first process pond 10 typically by water leg, waste water enters After first process pond 10, supersonic generator 101 is started working, and enters ultrasonic wave in water.Ultrasonic wave After entering in water, cavitation effect can occur, cavitation effect can make various composition mixed at high speed internal in waste water, There is provided good environment for the degraded of organic ammonia nitrogen composition and separation, and ultrasonic wave itself also can be in Decomposition Wastewater Some impurity.Passing through ozone flow in pipes 103 injection of ozone in waste water, ozone has Strong oxdiative and makees simultaneously With, can ammonia and nitrogen components in Decomposition Wastewater, owing to there being ultrasonic wave simultaneously so that ozone is in waste water Oxidation carry out more thoroughly and fully.Through the double action of ultrasonic wave and ozone, the ammonia in waste water The organic principles such as nitrogen are adequately broken, and have reached to promote the purpose of water quality.Process through the first process pond 10 Waste water, enters the second process pond 20.
Second process pond 20, processes the waste water after pond 10 is processed through described first, processes pond 20 second In equipped with high-frequency pulse voltage generator.
After waste water enters the second process pond 20, open high-frequency pulse voltage generator 201, height is applied to waste water Frequently pulse voltage.Under the effect of high-frequency pulse voltage, the heavy metal contaminants in waste water is removed.
3rd process pond 30, receives the waste water after the second process pond 20 is processed, and waste water processes pond the 3rd MRB processing system 301 is utilized to carry out MRB process and carry out precipitation decomposition in 30, the 3rd process pond 30 Dress is also equipped with pH value adjuster (not shown), adds pH value regulation liquid to adjust in the 3rd process pond 30 The Acidity of Aikalinity of joint waste water, increases water quality further.
From the waste water processing through the 3rd process pond 30 it is believed that complete the process of waste water, discharge.
Further, as a new more specifically embodiment, above-mentioned each processes pond and collecting pit 40 It is all single, complete transfer in each pond for the waste water by arranging waterworks, it is also possible to switch valve is set 80 grades keep UNICOM and partition between pond.Ensure that waste water does not refluxes.
Further, before waste water enters collecting pit 40 or in collecting pit 40, doughnut is carried out to waste water 3012MBR process.Also other further purified treatment can be carried out.
In the first process pond 10, realize that ozone injects and waste water is discharged with the pipeline of a threeway.Ozone is sent out The ozone that raw device 105 produces enters pipeline, extracts waste water out, enter ozone and inject bottom the first process pond 10 Pipeline 103, the ozone flow in pipes 103 producing ozone generator 105, water and ozone mix, by gas Liquid mixing pump makes gas-liquid be sufficiently mixed, and is then passed through ozone flow in pipes 103 and injects in the first process pond 10 Waste water, pipeline can be extended to the bottom in the first process pond 10.Ozone flow in pipes 103 can be with The waste outflow pipe UNICOM in one process pond 10, ozone flow in pipes 103 part in the first process pond 10 is led to Cross three ports and receive the wastewater discharge pipe in the first process pond 10, drain into the second process pond 20.
A console 107 can be set on the side in the first process pond 10, be used for controlling ozone generator 105 And ultrasonic wave voltage generator.In the second process pond 20, the electric discharge of high-frequency pulse voltage generator 201 Plate 2012 can carry out modularized processing.For example the discharge electrode 2012 processing a waste water ability is made one Module.Each module is independent, to realize carrying out block combiner flexibly for treating capacity.The control of radio-frequency generator Part can hang over outside the pond in the second process pond, it is possible to is placed in console 107.Refering to Fig. 2, discharge electrode 2012 The top view of one module, is a fixing module in figure.
In the 3rd process pond 30, MBR processing system is set.Multiple back-shaped water pipe 3014 is set in pond, On the water pipe of a reversion, connecting doughnut 3012 between the part on both sides, it is fine that waste water penetrates into hollow Dimension 3012, enters into back-shaped water pipe 3014 by doughnut 3012.Top at each back-shaped water pipe 3014 Portion is provided with opening, connects collector pipe, each collector pipe be pooled at one the 3rd process pond 30 drainpipe, To get rid of waste water.Can carry out extracting waste water to collector pipe by water pump.
It is additionally provided with gas-adding pipe in the second process pond 20 and the 3rd process pond 30, in waste water, inject air so that Waste water can fully stir in pond.
Further regard to Fig. 3, collecting pit 40, described 3rd process pond 30 UNICOM can also be increased, receive warp Cross the waste water after the described 3rd process pond 30 is processed to be collected;And
Fourth process pond (not shown), described fourth process pond and collecting pit 40 UNICOM, receive through collecting pit Water in 40, Waste Water Treatment is discharged carry out reverse osmosis (RO) process to water therein after in this fourth process pond.
Further, in the build process of specific Waste Water Treatment, ozone can use the finished product of buying smelly Oxygen, can install ozone generator 105 in present treatment system simultaneously further, and ozone generator 105 produces Ozone injection of ozone flow in pipes 103.
In order to realize more preferable effect, referring to Fig. 4, the above waste gas of can setting up in the first process pond 10 is received Ji Gai, because in the first processing procedure to waste water for the process pond 10, ammonia and nitrogen components has carried out sufficient decomposition, Can produce the gases such as nitrogen, ammonia, and other impurity also can produce under the ultrasonic effect involving ozone other from Waste water is separated, if these gases are directly discharged in air, then can air born pollution be increased useless Abandon to collect and cover and can get up isolating gas collection from waste water by the escape pipe arranging on gas sampling lid 112 collect and process.
Further, the present invention implements to give the method that waste water is processed, and i.e. processes waste water in said system application Method.
Refering to Fig. 5, the embodiment of the present invention processes the method flow diagram of waste water.
S100, carries out ultrasonic irradiation to waste water, has removed the ammonia in waste water to described waste water injection of ozone simultaneously Nitrogen component;
S102, continues to apply high-frequency pulse voltage in order to remove the heavy metal element in waste water to waste water;
S103, adds pH value conditioning agent, the at ordinary times Acidity of Aikalinity of waste water in waste water;
S104, through the above-mentioned waste water processing, importing processes pond and utilizes MRB processing system 301 to carry out MRB processes and carries out precipitation and decomposes, and then carries out reverse osmosis (RO) process, discharges after finally collecting.
In above-mentioned method and system, supersonic generator 101 produces the ultrasonic wave of 10-20kHz.
The Waste Water Treatment of the embodiment of the present invention and method, it is not necessary to increase chemical addition agent, pass through ultrasonic wave With effect while ozone, waste water is substantially oxidized, and the effect of ultrasonic wave and ozone is to the sky processing pond Between less demanding, therefore size and the floor space of processing system, high frequency suitably can be set according to treating capacity Also being readily available and act on of pulse voltage, therefore whole system and method are simply effective, it is easy to the place to waste water Reason.

Claims (8)

1. a Waste Water Treatment, it is characterised in that described system includes:
First process pond, described first process pond is equipped with supersonic generator and ozone flow in pipes, described ozone Flow in pipes injection of ozone in described waste water;Described supersonic generator is dipped in and enters the useless of this first process pond In water, produce ul-trasonic irradiation and in the waste water entering the described first process pond, the cavitation utilizing ultrasonic wave is made With accelerating the oxidation disinfection effect to waste water for the ozone, described supersonic generator is that tabular packaged type ultrasonic wave is sent out Raw device, is also equipped with water circulating pump in described first process pond and the waste water in the first process pond is circulated;
Second process pond, receive through described first process pond process after waste water, described second process pond equipped with High-frequency pulse voltage generator, this high-frequency pulse voltage generator includes discharge electrode, and described discharge electrode uses iron plate Or aluminium sheet material, this discharge electrode is dipped in the waste water in the described second process pond, giving up in this second process pond Water applies high-voltage pulse;
3rd process pond, receives and processes the waste water after pond is processed through described second, and waste water is processed the described 3rd Pond carries out MBR process and carries out precipitation decomposition, the 3rd process pond is also equipped with pH value adjuster, to PH value regulator is added in 3rd process pond;
Collecting pit, with described 3rd process pond UNICOM, receives the waste water after the described 3rd processes pond process and enters Row is collected;
Fourth process pond, with described collecting pit UNICOM, receives the water in collecting pit, this fourth process pond pair Water therein discharges Waste Water Treatment after carrying out reverse osmosis (RO) process.
2. system according to claim 1, it is characterised in that described system also includes:
Ozone generator, described ozone generator is connected with described ozone flow in pipes, and this ozone generator will produce Raw ozone enters described ozone flow in pipes.
3. system according to claim 1, it is characterised in that described system also includes:
Gas sampling lid, described gas sampling lid is placed in above the described first process pond, is used for sealing described first Processing pond, described gas sampling is covered with discharge, and this gas sampling lid processes, by first, the gas discharged in pond Collect in described discharge and discharge.
4. the system according to claim the 1st, 2 or 3 any claim, it is characterised in that described Supersonic generator produces the ultrasonic wave of 20kHz.
5. the system according to claim 1-2 any claim, it is characterised in that at described first Reason pond is separate with the second process pond, processes described first and is provided with feedwater dress between pond and the second process pond Put so that the waste water in described first process pond enters the described second process pond.
6. a method of wastewater treatment, it is characterised in that described method includes:
Carry out ultrasonic irradiation to waste water, become to remove the ammonia nitrogen in waste water to described waste water injection of ozone simultaneously Point;
Continue to apply high-frequency pulse voltage in order to remove the heavy metal element in waste water to waste water;
PH value regulator, the Acidity of Aikalinity of balance waste water is added in waste water;
Through the above-mentioned waste water processing, importing processes pond and utilizes MBR processing system to carry out MBR process simultaneously Carry out precipitation to decompose, then carry out reverse osmosis (RO) process, discharge after finally collecting.
7. method according to claim 6, it is characterised in that described method includes:
Carry out ultrasonic irradiation described to waste water, simultaneously during described waste water injection of ozone, at general The top in reason pond increases gas sampling lid, isolated waste gas will be collected from waste water.
8. the method according to claim 6-7 any claim, it is characterised in that described ultrasonic wave Generator produces the ultrasonic wave of 20kHz.
CN201210303138.XA 2012-08-24 2012-08-24 A kind of Waste Water Treatment and method Expired - Fee Related CN102775000B (en)

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CN102775000B true CN102775000B (en) 2016-11-09

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Publication number Priority date Publication date Assignee Title
CN105668881B (en) * 2016-03-16 2018-07-27 湖南京明环保科技有限公司 Wastewater treatment system containing ammonia nitrogen
WO2019084937A1 (en) * 2017-11-04 2019-05-09 张瑁珈 Wastewater treatment system

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
臭氧-膜生物反应器深度处理印染废水的研究;林德贤等;《工业用水与废水》;20081231;第39卷(第6期);第41-42、46页 *
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