CN101767858A - Method for alkaline waste water treatment through aeration process - Google Patents

Method for alkaline waste water treatment through aeration process Download PDF

Info

Publication number
CN101767858A
CN101767858A CN201010046509A CN201010046509A CN101767858A CN 101767858 A CN101767858 A CN 101767858A CN 201010046509 A CN201010046509 A CN 201010046509A CN 201010046509 A CN201010046509 A CN 201010046509A CN 101767858 A CN101767858 A CN 101767858A
Authority
CN
China
Prior art keywords
waste water
alkaline waste
water treatment
aeration process
aeration
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201010046509A
Other languages
Chinese (zh)
Inventor
余浩洋
余海荣
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hefei Debi Water Treatment Science & Technology Co Ltd
Original Assignee
Hefei Debi Water Treatment Science & Technology Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hefei Debi Water Treatment Science & Technology Co Ltd filed Critical Hefei Debi Water Treatment Science & Technology Co Ltd
Priority to CN201010046509A priority Critical patent/CN101767858A/en
Publication of CN101767858A publication Critical patent/CN101767858A/en
Pending legal-status Critical Current

Links

Images

Landscapes

  • Processing Of Solid Wastes (AREA)

Abstract

The invention relates to the field of waste water treatment, in particular to a method for alkaline waste water treatment through an aeration process. The method is that the aeration process is used for directly filling air into alkaline waste water to enable carbon dioxide in air to neutralize with the alkaline waste water. By using the carbon dioxide in the air to neutralize with the alkaline waste water, the method of the invention can reduce the pH value of the alkaline waste water and can ensure the alkaline waste water to be compliant with the emission standards.

Description

The method of alkaline waste water treatment through aeration process
Technical field
The present invention relates to field of waste water treatment, be specifically related to a kind of treatment process of alkaline waste water.
Background technology
Coal-fired power plant is in power generation process, and a large amount of coal that burns produces the flyash of a great deal of simultaneously.The method that electricity power enterprise generally adopts waterpower to carry, flyash and water are made certain density slip (that is to say buck), pass through slurry pump, it is pumped to storage ash field, buck at ash through natural subsidence, finished separating of flyash and water, clarifying water enters natural water by the overflow port of ash.Owing to have a certain amount of alkaline matter in the flyash,, make the overflow water of discharging be alkalescence and pollute natural water such as the calcium oxide of free state.Method of wastewater treatment at present commonly used has following two kinds: (1) acid-base neutralisation method: adopt industrial acids (sulfuric acid or hydrochloric acid) that the outer draining of ash disposal area is neutralized, the pH value that makes the pH value of outer draining reach national regulation is below 9; (2) stove cigarette ash water treating method: with under the admixture of buck, utilize boiler smoke to handle at flyash, thereby reach the effect that reduces grey water ph value.Along with international schedule is constantly put in environment protection, a large amount of industrial acids that the acid-base neutralisation method is used belong to the high-risk product, have certain application risk, drop into bigger simultaneously; The buck water quality instability that adopts stove cigarette ash water treating method to handle can not satisfy the qualified discharge standard of country fully.
Summary of the invention
The method that the purpose of this invention is to provide a kind of alkaline waste water treatment through aeration process, this method is simple and convenient, and is with low cost, environmental protection and processing effective.
The method of alkaline waste water treatment through aeration process of the present invention is to utilize aeration directly to inflate air in the alkaline waste water, makes carbon dioxide in air and alkaline waste water carry out neutralization reaction.
Adopt technique scheme, the present invention utilizes carbon dioxide in air gas and alkaline waste water to carry out neutralization reaction, thereby reduce the effect of alkaline waste water pH value, make its qualified discharge, method of the present invention can produce a certain amount of absorption to Atmospheric Carbon Dioxide simultaneously, has significant emission reduction effect.
Figure of description
Fig. 1 is the schema of treatment of Power buck of the present invention;
Fig. 2 is a partial schematic diagram among Fig. 1.
Embodiment
The method of alkaline waste water treatment through aeration process of the present invention, described aeration are to adopt aerator to inflate air to alkaline waste water.The aerator that aeration of the present invention uses is some.But utilize aerator one side alkalitropism waste water to charge into a large amount of air, can also constantly stir simultaneously the carrying out that quickens neutralization reaction, the aerator that general preferred use is suitably many can provide competent carbonic acid gas and alkaline waste water to carry out neutralization reaction like this, can also shorten the reaction times simultaneously.The method of alkaline waste water treatment through aeration process of the present invention, wherein said alkaline waste water are a fuel-burning power plant ash buck.Utilize aeration that carbon dioxide in air is charged into alkaline waste water and carry out neutralization reaction, this method is simple and convenient, and cheap and environmental protection does not have danger, can also effectively control the pH value of alkaline waste water simultaneously, and economic benefit and environmental benefit are remarkable.Be illustrated below by specific embodiment.
Embodiment
As shown in Figure 1, 2, wherein each label is as follows among the figure: the 10th, and power plant, the 20th, buck transport pipe, the 30th, ash disposal area, the 31st, aerator, the 32nd, an ash water port (overflow port), the 33rd, deposition flyash, the 34th, buck.The buck that power plant 10 discharges enters ash disposal area 30 through buck transport pipe 20, the ash of power plant is ash discharge water outside the venue, its alkali components is mainly calcium hydroxide, utilization is installed in the aerator 31 of an ash water port, in buck 34, charge into a large amount of air, make carbon dioxide in air and calcium hydroxide carry out neutralization reaction, concrete reaction formula is as follows:
CO 2+Ca(OH) 2→CaCO 3↓+Ca(HCO 3) 2????????(1)
Calcium hydroxide in carbon dioxide in air elder generation and the buck 34 reacts (1), along with constantly carrying out of reaction, the precipitation of calcium carbonate that generates forms deposition flyash 33, thereby the final Calcium hydrogen carbonate that generates reaches the purpose that reduces grey water ph value, and the pipeline of an ash water port 32 (overflow port) is arranged on the liquid level top of buck 34, begin draining from the top, guarantee reaction thoroughly, concrete testing data is as shown in the table:
Aeration time (mins) The ash water ph value
??0 ??10.05
??30 ??9.46
??60 ??8.85
??90 ??8.16

Claims (4)

1. the method for an alkaline waste water treatment through aeration process, this method is to utilize aeration directly to inflate air in the alkaline waste water, makes carbon dioxide in air and alkaline waste water carry out neutralization reaction.
2. the method for alkaline waste water treatment through aeration process according to claim 1 is characterized in that: described aeration is to adopt aerator to inflate air to alkaline waste water.
3. the method for alkaline waste water treatment through aeration process according to claim 2, it is characterized in that: described aerator is some.
4. the method for alkaline waste water treatment through aeration process according to claim 2 is characterized in that: described alkaline waste water is a fuel-burning power plant ash buck.
CN201010046509A 2010-01-05 2010-01-05 Method for alkaline waste water treatment through aeration process Pending CN101767858A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201010046509A CN101767858A (en) 2010-01-05 2010-01-05 Method for alkaline waste water treatment through aeration process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201010046509A CN101767858A (en) 2010-01-05 2010-01-05 Method for alkaline waste water treatment through aeration process

Publications (1)

Publication Number Publication Date
CN101767858A true CN101767858A (en) 2010-07-07

Family

ID=42500986

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201010046509A Pending CN101767858A (en) 2010-01-05 2010-01-05 Method for alkaline waste water treatment through aeration process

Country Status (1)

Country Link
CN (1) CN101767858A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105293669A (en) * 2015-11-12 2016-02-03 新疆天智辰业化工有限公司 Method for adjusting pH value of alkaline waste water
CN105645672A (en) * 2015-12-31 2016-06-08 安徽省绿巨人环境技术有限公司 Device and method for treating alkaline wastewater
CN110615517A (en) * 2019-09-07 2019-12-27 山东九思新材料科技有限责任公司 Alkaline silicon washing alkaline sewage treatment device and use method thereof
CN110981004A (en) * 2019-12-05 2020-04-10 云南罗平锌电股份有限公司 Treatment method of zinc smelting sewage

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105293669A (en) * 2015-11-12 2016-02-03 新疆天智辰业化工有限公司 Method for adjusting pH value of alkaline waste water
CN105645672A (en) * 2015-12-31 2016-06-08 安徽省绿巨人环境技术有限公司 Device and method for treating alkaline wastewater
CN110615517A (en) * 2019-09-07 2019-12-27 山东九思新材料科技有限责任公司 Alkaline silicon washing alkaline sewage treatment device and use method thereof
CN110981004A (en) * 2019-12-05 2020-04-10 云南罗平锌电股份有限公司 Treatment method of zinc smelting sewage
CN110981004B (en) * 2019-12-05 2022-05-03 云南罗平锌电股份有限公司 Treatment method of zinc smelting sewage

Similar Documents

Publication Publication Date Title
CN103933845A (en) System used for treating waste gas discharged by ships
CN102974209B (en) Desulfurization synergist having scale inhibition performance, and preparation method thereof
CN103990370A (en) Method for reducing emission of thermal power generation smoke CO2 and subsidiarily producing superfine nanometer CaCO3 from thermal power generation smoke CO2
CN101767858A (en) Method for alkaline waste water treatment through aeration process
CN201168557Y (en) Flue gas processing system
CN101637697B (en) Biological desulfurization method of smoke
CN203355578U (en) Flue gas desulfurizer adopting magnesium method for sintering machine
CN207227234U (en) A kind of reverse osmosis concentrated water utilization system
CN101732961A (en) Seawater desulfurizing process
CN102847430A (en) System and technology for cleaning flue gas
CN215539771U (en) System for utilize desulfurization waste residue mineralize mineralization carbon dioxide
CN104197309A (en) Method for recycling heat energy in low-temperature smoke containing SO3 and dust
Gianico et al. Innovative two‐steps thermo‐chemical pretreatment for sludge reduction and energy recovery: cost and energy assessment
CN202893177U (en) Smoke purifying system
CN210065435U (en) Low PH flue evaporation plant
CN102154045B (en) Method for processing low-concentration carbon dioxide in mashgas
CN201930710U (en) Magnesium desulfurization system
CN201648011U (en) Brine and boiler waste gas purifying device in vacuum salt production
CN201978642U (en) Bubbling spray tower
CN102252309B (en) Boiler descaling method
CN102580498B (en) Comprehensive treatment method for high-concentration ammonia nitrogen waste water and boiler flue gas
CN203291705U (en) Device for removing sulfur dioxide in fume by using brine purification slag
CN203728669U (en) Treatment system for flue gas and reverse osmosis concentrated water
CN103611401A (en) Brine purification waste-residue desulfurization process
CN202638254U (en) Continuous sewage discharge and carbon dioxide (CO2) collection system of boiler

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C02 Deemed withdrawal of patent application after publication (patent law 2001)
WD01 Invention patent application deemed withdrawn after publication

Open date: 20100707