CN102701401A - Method of using ozone for purifying carbon-12 sodium alcohol ether sulphate - Google Patents

Method of using ozone for purifying carbon-12 sodium alcohol ether sulphate Download PDF

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Publication number
CN102701401A
CN102701401A CN2012100252234A CN201210025223A CN102701401A CN 102701401 A CN102701401 A CN 102701401A CN 2012100252234 A CN2012100252234 A CN 2012100252234A CN 201210025223 A CN201210025223 A CN 201210025223A CN 102701401 A CN102701401 A CN 102701401A
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Prior art keywords
ozone
sodium sulfate
alcohol sodium
polyoxyethylenated alcohol
water
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CN2012100252234A
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史忠科
梁晨
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Xian Feisida Automation Engineering Co Ltd
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Xian Feisida Automation Engineering Co Ltd
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Priority to CN2012100252234A priority Critical patent/CN102701401A/en
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Abstract

The invention discloses an automobile wastewater treatment method, belongs to the technical field of traffic environment, and particularly relates to a method of using ozone for purifying carbon-12 sodium alcohol ether sulphate. The method includes that reaction temperature and pH (potential of hydrogen) values are adjusted by detecting pollutant concentration to enable carbon-12 sodium alcohol ether sulphate to be completely decomposed into water, sodium ions, sulfate ions and dischargeable carbon dioxide. The defects of residue pollution and the like in the prior art are overcome, ozone quantity required by complete decomposition of carbon-12 sodium alcohol ether sulphate can be worked out, and high efficiency in treatment of pollutants can be achieved by regulating openness of a water outlet valve and flow of fed ozone.

Description

A kind of ozone is to the purifying treatment method of carbon 12 polyoxyethylenated alcohol sodium sulfate
Technical field
The present invention relates to a kind of automobile method of wastewater treatment, particularly free of contamination high-efficient treatment method belongs to the traffic environment technical field.
Background technology
In recent years; Along with fast development of Chinese economy; The appearance of a series of stimulation automobile consumption policies of country, the quantity of motor vehicle is how much formulas growths, the also fast development of carwash industry of arising at the historic moment in the street; By consequent automobile Cleaning Wastewater often enters sewer line, street without any processing, pollute in the flowers and plants, and in the wastewater from car washer often with carbon 12 (C 12) polyoxyethylenated alcohol sodium sulfate is principal pollutant.Therefore, for C in the wastewater from car washer 12The processing of polyoxyethylenated alcohol sodium sulfate is essential.
Existing process for treating waste water for car wash commonly used has: materialization treatment process, electrolytic process, membrane bioreactor, magnetic kind magnetic separation method etc.Wherein electrolytic process need not to add pharmaceutical chemicalss such as oxygenant, flocculation agent, convenient and flexible operation; Document " Li Bin; Li Yanglin. electrochemical process is handled the development [J] of carwash waste water recycling equipment. industrial safety and environmental protection; 2010; 5 (36): 9-10 " literary composition, confirmed that electrochemical method purifies the technical process and the basic parameter of wastewater from car washer equipment for reclaiming, water outlet has reached country and has reused water quality standard.But its equipment is huge, and power consumption is high, and reckons without the pollution that tensio-active agent brought in the automobile waste water; Membrane bioreactor is the efficient water treatment device that development in recent years is got up, and degradation efficiency is high, device compactness, succinct; Document " Han Fei, intact face is magnificent, and Chi Yichao; Tian Binghui is high rich. NACF carrier organism embrane method Treatment of Washing car waste water research [J]. environmental engineering journal, 2010; 4 (4): 751-755 " literary composition, point out at normal temperatures PH=6.5 ~ 7; Flooding quantity is when 30mL/min, and reactor drum reaches optimal operating parameter, and its effluent quality reaches the specified standard of the main water quality of car wash water in " miscellaneous domestic water quality standard " fully.But equipment needs under specific environment, to move, and is subject to the extraneous factor influence, and biomembrane activity has saturated phenomenon, can not work long hours.
Summary of the invention
In order to overcome the deficiency that there are aspects such as residual contamination in art methods, the present invention proposes the purifying treatment method of a kind of ozone to carbon 12 polyoxyethylenated alcohol sodium sulfate, through detection of contamination concentration, conditioned reaction temperature, pH value make C 12Polyoxyethylenated alcohol sodium sulfate is decomposed into water, Na fully +, SO 4 2-With the carbonic acid gas that can discharge, and calculate C 12Polyoxyethylenated alcohol sodium sulfate decomposes required ozone amount fully, reaches the efficient processing to pollutent through the ozone flow of regulating control outlet valve aperture and feeding.
The technical solution adopted for the present invention to solve the technical problems: a kind of ozone is characterized in may further comprise the steps to the purifying treatment method of carbon 12 polyoxyethylenated alcohol sodium sulfate:
1, reaches 3.5mg/L when above at temperature 10 ~ 40
Figure 843055DEST_PATH_IMAGE001
, the ozone content of pH value below 7, in the waste water, according to reaction formula
Figure 856010DEST_PATH_IMAGE002
Ozone can be to C 12Polyoxyethylenated alcohol sodium sulfate carries out oxygenolysis completely, generates water, Na +, SO 4 2-With the carbonic acid gas that can discharge, eliminated C 12Reaction such as polyoxyethylenated alcohol sodium sulfate molecule and ethers thereof, alcohols, ketone derived products is to the harm of water quality;
2, through detecting Pollutant levels in the waste water, allotment waste water solution to pH value is below 7, and temperature is 10 ~ 40
Figure 551565DEST_PATH_IMAGE001
, determine C in the unit volume 12The molar weight of polyoxyethylenated alcohol sodium sulfate, C during according to reaction 12The molar relationship ratio of polyoxyethylenated alcohol sodium sulfate and ozone is determined the content of the required ozone of reaction;
3, wastewater from car washer filters and is convenient to gas, water blended container after supercharging feeds with ozone, through detecting C 12The concentration of polyoxyethylenated alcohol sodium sulfate is regulated control outlet valve aperture and ozone amount.
The invention has the beneficial effects as follows: the present invention passes through ozone to tensio-active agent C in the wastewater from car washer 12The processing of polyoxyethylenated alcohol sodium sulfate reduces even eliminates the exhaust emission of wastewater from car washer, and passes through C in the wastewater from car washer 12The detection of polyoxyethylenated alcohol sodium sulfate content is regulated ozone flow and outlet valve aperture, thereby is reached energy-efficient.
Below in conjunction with accompanying drawing and embodiment the present invention is elaborated.
Description of drawings
Accompanying drawing 1 is the purifying treatment method principle assumption diagram of a kind of ozone of the present invention to carbon 12 polyoxyethylenated alcohol sodium sulfate, among the figure: 1. water-in; 2. strainer; 3. concentration detection apparatus; 4. topping-up pump; 5. ozone inlet mouth; 6. mixing vessel; 7. outlet valve.
Embodiment
With reference to accompanying drawing 1, concrete steps are following:
1, reaches 3.5mg/L when above at temperature 10 ~ 40, the ozone content of pH value below 7, in the waste water, according to reaction formula
Figure 908914DEST_PATH_IMAGE002
Ozone can be to C 12Polyoxyethylenated alcohol sodium sulfate carries out oxygenolysis completely, the oxidation scission of two keys takes place and further break hydrogen bond, generates water, Na +, SO 4 2-With the carbonic acid gas that can discharge, eliminated original C 12Reaction such as polyoxyethylenated alcohol sodium sulfate molecule and ethers thereof, alcohols, ketone derived products is to the harm of water quality;
2, through detecting Pollutant levels in the waste water, allotment waste water solution to pH value is below 7, and temperature is 10 ~ 40, the C of sewage inlet 12The concentration of polyoxyethylenated alcohol sodium sulfate is 600mg/L, C 12The relative molecular mass of polyoxyethylenated alcohol sodium sulfate is 420, can calculate C in one liter of waste water solution 12The quality of polyoxyethylenated alcohol sodium sulfate is converted into molar weight again and is about 0.0014mol, 1molC 12Polyoxyethylenated alcohol sodium sulfate decomposes the ozone that needs consume 18mol fully, thereby calculates the ozone of required 0.0252mol, and when the ozone input was 4g/min, the ozone amount that calculates reaction in a minute was 0.083 mol, can handle the C of 0.0046mol 12Polyoxyethylenated alcohol sodium sulfate is converted into C 12The quality of polyoxyethylenated alcohol sodium sulfate is 1.9g, considers solubleness and the reaction efficiency of ozone in water, need be the flow rate control of outlet valve in 3.2L/min;
3, wastewater from car washer detects C in the waste water through proofing unit after filtering 12The concentration of polyoxyethylenated alcohol sodium sulfate; Is that the ozone of 4g/min feed mixing vessel with the hydraulic pressure of 0.4Mpa with air input through topping-up pump; Through thorough mixing; Adjust the water valve aperture flow is remained in the 3.2L/min, more than 87%, ionic activity thing clearance is more than 90% at the monitoring of the water outlet after processing COD (COD) clearance.

Claims (1)

1. an ozone is characterized in that may further comprise the steps to the purifying treatment method of carbon 12 polyoxyethylenated alcohol sodium sulfate:
(1) reaches 3.5mg/L when above at temperature 10 ~ 40
Figure 2012100252234100001DEST_PATH_IMAGE001
, the ozone content of pH value below 7, in the waste water, according to reaction formula
Figure 2012100252234100001DEST_PATH_IMAGE002
Ozone can be to C 12Polyoxyethylenated alcohol sodium sulfate carries out oxygenolysis completely, generates water, Na +, SO 4 2-With the carbonic acid gas that can discharge, eliminated C 12Reaction such as polyoxyethylenated alcohol sodium sulfate molecule and ethers thereof, alcohols, ketone derived products is to the harm of water quality;
(2) through detecting Pollutant levels in the waste water, allotment waste water solution to pH value is below 7, and temperature is 10 ~ 40
Figure 788862DEST_PATH_IMAGE001
, determine C in the unit volume 12The molar weight of polyoxyethylenated alcohol sodium sulfate, C during according to reaction 12The molar relationship ratio of polyoxyethylenated alcohol sodium sulfate and ozone is determined the content of the required ozone of reaction;
(3) wastewater from car washer filters and is convenient to gas, water blended container after supercharging feeds with ozone, through detecting C 12The concentration of polyoxyethylenated alcohol sodium sulfate is regulated control outlet valve aperture and ozone amount.
CN2012100252234A 2012-02-06 2012-02-06 Method of using ozone for purifying carbon-12 sodium alcohol ether sulphate Pending CN102701401A (en)

Priority Applications (1)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112707522A (en) * 2020-12-21 2021-04-27 江苏赞宇科技有限公司 Wastewater treatment process of fatty alcohol-polyoxyethylene ether sodium sulfate

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06153921A (en) * 1992-11-25 1994-06-03 Shikoku Chem Corp Microbe capable of degrading polyoxyethylene lauryl ether sulfate and usage thereof
CN1736887A (en) * 2005-04-29 2006-02-22 吴学云 Waste water resuing method of chemical method carwash
CN1974431A (en) * 2005-12-01 2007-06-06 栗田工业株式会社 Water processing method containing surface active agent and processing device
CN201128706Y (en) * 2007-11-01 2008-10-08 蔡云华 Water cyclic regeneration device for carwash

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06153921A (en) * 1992-11-25 1994-06-03 Shikoku Chem Corp Microbe capable of degrading polyoxyethylene lauryl ether sulfate and usage thereof
CN1736887A (en) * 2005-04-29 2006-02-22 吴学云 Waste water resuing method of chemical method carwash
CN1974431A (en) * 2005-12-01 2007-06-06 栗田工业株式会社 Water processing method containing surface active agent and processing device
CN201128706Y (en) * 2007-11-01 2008-10-08 蔡云华 Water cyclic regeneration device for carwash

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112707522A (en) * 2020-12-21 2021-04-27 江苏赞宇科技有限公司 Wastewater treatment process of fatty alcohol-polyoxyethylene ether sodium sulfate

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Application publication date: 20121003