CN102701414A - Purifying treatment method of sodium lauryl sulfate with ozone - Google Patents
Purifying treatment method of sodium lauryl sulfate with ozone Download PDFInfo
- Publication number
- CN102701414A CN102701414A CN2012100252361A CN201210025236A CN102701414A CN 102701414 A CN102701414 A CN 102701414A CN 2012100252361 A CN2012100252361 A CN 2012100252361A CN 201210025236 A CN201210025236 A CN 201210025236A CN 102701414 A CN102701414 A CN 102701414A
- Authority
- CN
- China
- Prior art keywords
- ozone
- sodium lauryl
- lauryl sulphate
- water
- treatment method
- 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
Links
Images
Landscapes
- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
The invention discloses an automobile wastewater treatment method, particularly a purifying treatment method of sodium lauryl sulfate with ozone, belonging to the technical field of traffic environment. By detecting the pollutant concentration and regulating the reaction temperature, the sodium lauryl sulfate is completely decomposed into water, Na<+>, SO4<2-> and dischargeable carbon dioxide, thereby overcoming the defects in residual pollution and other aspects in the method in the prior art; and the amount of ozone required by completely decomposing sodium lauryl sulfate is calculated, and the opening of a water outlet valve and the flow of the introduced ozone are regulated and controlled to efficiently treat pollutants.
Description
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 often be principal pollutant in the wastewater from car washer with the sodium lauryl sulphate.Therefore, essential for the processing of sodium lauryl sulphate in the wastewater from car washer.
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 sodium lauryl sulphate; Through detection of contamination concentration, the conditioned reaction temperature makes sodium lauryl sulphate be decomposed into water, Na fully
+, SO
4 2-With the carbonic acid gas that can discharge, and calculate sodium lauryl sulphate and decompose required ozone amount fully, reach efficient processing 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 sodium lauryl sulphate:
1, the ozone content in temperature 10 ~ 40
waste water reaches 3.5mg/L when above, according to reaction formula
Ozone can carry out oxygenolysis completely to sodium lauryl sulphate, generates water, Na
+, SO
4 2-With the carbonic acid gas that can discharge, eliminated the harm of sodium lauryl sulphate molecule and reaction derived products thereof to water quality;
2, through detecting Pollutant levels in the waste water; Temperature be 10 ~ 40
time; Determine the molar weight of sodium lauryl sulphate in the unit volume; According to when reaction sodium lauryl sulphate with the molar relationship ratio of ozone, determine 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 the concentration of sodium lauryl sulphate, regulates control outlet valve aperture and ozone amount.
The invention has the beneficial effects as follows: the present invention is through the processing of ozone to tensio-active agent sodium lauryl sulphate in the wastewater from car washer; Reduce even eliminate the exhaust emission of wastewater from car washer; And through detection to sodium lauryl sulphate content in the wastewater from car washer; Regulate ozone flow and outlet valve aperture, thereby reach 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 sodium lauryl sulphate, 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, the ozone content in temperature 10 ~ 40
, waste water reaches 3.5mg/L when above, according to reaction formula
Ozone can carry out oxygenolysis completely to sodium lauryl sulphate, 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 the harm of original sodium lauryl sulphate molecule and reaction derived products thereof to water quality;
2, through detecting Pollutant levels in the waste water; Controlled temperature 10 ~ 40
; The concentration of the sodium lauryl sulphate of sewage inlet is 800mg/L; The relative molecular mass of sodium lauryl sulphate is 288, can calculate the quality of sodium lauryl sulphate in one liter of waste water solution, is converted into molar weight again and is about 0.0028mol; The 1mol sodium lauryl sulphate is decomposed the ozone that needs consume 12mol fully; Thereby calculate the ozone of required 0.0336mol, when the ozone input was 4g/min, the ozone amount that calculates reaction in a minute was 0.083 mol; Can handle the sodium lauryl sulphate of 0.0069mol; The quality that is converted into sodium lauryl sulphate is 1.99g, considers solubleness and the reaction efficiency of ozone in water, need be the flow rate control of outlet valve in 2.5L/min;
3, wastewater from car washer after filtering; Detect the concentration of sodium lauryl sulphate in the waste water through proofing unit; Is that the ozone of 4g/min feed mixing vessel with the hydraulic pressure of 0.6Mpa with air input through topping-up pump, through thorough mixing, adjusts the water valve aperture flow is remained in the 2.5L/min; More than 85%, 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 sodium lauryl sulphate:
(1) ozone content in temperature 10 ~ 40
waste water reaches 3.5mg/L when above, according to reaction formula
Ozone can carry out oxygenolysis completely to sodium lauryl sulphate, generates water, Na
+, SO
4 2-With the carbonic acid gas that can discharge, eliminated the harm of sodium lauryl sulphate molecule and reaction derived products thereof to water quality;
(2) through detecting Pollutant levels in the waste water; Temperature be 10 ~ 40
time; Determine the molar weight of sodium lauryl sulphate in the unit volume; According to when reaction sodium lauryl sulphate with the molar relationship ratio of ozone, determine 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 the concentration of sodium lauryl sulphate, regulates control outlet valve aperture and ozone amount.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2012100252361A CN102701414A (en) | 2012-02-06 | 2012-02-06 | Purifying treatment method of sodium lauryl sulfate with ozone |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2012100252361A CN102701414A (en) | 2012-02-06 | 2012-02-06 | Purifying treatment method of sodium lauryl sulfate with ozone |
Publications (1)
Publication Number | Publication Date |
---|---|
CN102701414A true CN102701414A (en) | 2012-10-03 |
Family
ID=46894554
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN2012100252361A Pending CN102701414A (en) | 2012-02-06 | 2012-02-06 | Purifying treatment method of sodium lauryl sulfate with ozone |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN102701414A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111995000A (en) * | 2020-08-03 | 2020-11-27 | 河海大学 | Membrane distillation system for treating wastewater containing salt and surfactant and application of membrane distillation system |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1736887A (en) * | 2005-04-29 | 2006-02-22 | 吴学云 | Waste water resuing method of chemical method carwash |
-
2012
- 2012-02-06 CN CN2012100252361A patent/CN102701414A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1736887A (en) * | 2005-04-29 | 2006-02-22 | 吴学云 | Waste water resuing method of chemical method carwash |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111995000A (en) * | 2020-08-03 | 2020-11-27 | 河海大学 | Membrane distillation system for treating wastewater containing salt and surfactant and application of membrane distillation system |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN109879550B (en) | Photovoltaic cell production wastewater purification system | |
CN102795746B (en) | Treatment method for waste incineration power plant leachate and device thereof | |
CN103833166B (en) | A kind of methyldiethanolamine (MDEA) process for treating industrial waste water | |
CN110002639A (en) | A kind of processing unit and method of middle and advanced stage aged refuse in MSW landfill percolate | |
CN106007167B (en) | The processing method of the pickling waste waters containing incretion interferent | |
CN101948220B (en) | Method for treating printing and dyeing wastewater | |
CN102701414A (en) | Purifying treatment method of sodium lauryl sulfate with ozone | |
CN102701401A (en) | Method of using ozone for purifying carbon-12 sodium alcohol ether sulphate | |
CN102701413A (en) | Purifying treatment method of sodium hexadecylsulfonate with ozone | |
CN110482683B (en) | Sewage advanced treatment method and equipment based on activated carbon technology | |
CN204874185U (en) | High salt sewage treatment plant | |
CN102701403A (en) | Purifying treatment method of polyoxyethylene oleate with ozone | |
CN102701399A (en) | Purifying treatment method of C16 fatty alcohol ammonium sulfate with ozone | |
CN102701415A (en) | Purifying treatment method of hexadecanol lactate with ozone | |
CN102701400A (en) | Method of using ozone for purifying isopropyl myristate | |
CN102701398A (en) | Purifying treatment method of polyoxyethylene stearate with ozone | |
CN102701407A (en) | Method using ozone for purification treatment of alkyl sulfate sodium salt | |
CN102701417A (en) | Method using ozone for purification treatment of sodium butyl oleate sulfate | |
CN102701406A (en) | Method of using ozone for purifying lauric glycerol monostearate | |
CN102701410A (en) | Method using ozone for purification treatment of lauryl polyoxyethylene ether triethanolamine sulfate | |
CN102701404A (en) | Method of using ozone for purifying isopropyl palmitate | |
CN102701402A (en) | Purifying treatment method of fatty alcohol polyethenoxy ether sodium sulfate with ozone | |
CN210313897U (en) | Denitration desulfurization circulating water treatment device | |
CN102701409A (en) | Method using ozone for purification treatment of monoethanolamine dodecyl sulfate | |
CN102701412A (en) | Method using ozone for purification treatment of sodium hexadecyl diphenyl ether monosulfonate |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C12 | Rejection of a patent application after its publication | ||
RJ01 | Rejection of invention patent application after publication |
Application publication date: 20121003 |