Sonophotocatalytic Degradation of Waste Water
-
Upload
tejas-deshpande -
Category
Engineering
-
view
476 -
download
9
Transcript of Sonophotocatalytic Degradation of Waste Water
TECHNICAL PAPERON
“Recent Trends in Chemical Engg.”( Sonophotocatalytic Degradation of Waste Water )
PRESENTED BY
Mr. Tejas D. Deshpande
B.E. (Chemical)
TATYASAHEB KORE INSTITUTE OF ENGG. AND TECHNOLOGY, WARANANAGAR.
Generators of Waste WaterDomestic Wastewater
Bathing Washing Clothes, Utensils, Vehicles etc. Sanitation waste Landfill leachate Effluents Commercial
Industrial Waste Water Chemical Petroleum and Refining Food Processing Pharmaceutical Pulp and paper Textile Dye processing
Current Waste Water TreatmentsUnit operations and processes that have been employed to waste water
treatments are divided into 3 types according to various levels of treatment as :
1. Physical - Primary methods- Physical or Physio-chemical unit Operations e.g. filtration, adsorption, air flotation, flocculation and sedimentation
2. Biological - Secondary - Biological Operations. e.g. aerobic, anaerobic and activated sludge
3. Chemical – Tertiary- Advanced Processes evolving Chemical Change e.g. Thermal oxidation (Combustion), Chemical oxidation, Ion exchange, Chemical Precipitation
Drawbacks
Incomplete elimination of Toxic & Non-biodegradable organic pollutants
Need disposal of secondary waste materials generated in the process
Can Reduce BODs but Can not reduce CODs at desirable extent
Adsorption and Coagulation - NOT useful to treat harmful infectants present in the waste water
Sedimentation, filtration, Membrane technology - Expensive and Generate toxic secondary pollutants
Chlorination generates Mutagenic and Carcinogenic by-products
Need to test and set up the emerging alternative technologies to overcome the inconveniences of conventional treatment methods
Advanced Oxidation Processes: ( AOPs ) Groups of technologies that lead to hydroxyl radical (.OH) generation
.OH Radicals- Extremely unstable and reactive, High oxidation potential
Attack organic molecules & make New oxidized intermediates with lower molecular weight or in case of complete mineralization CO2 and water
AOP - Powerful and efficient treatment methods for degrading recalcitrant materials or mineralizing stable, inhibitory, or toxic contaminants
Increasingly gaining popularity - Potential of converting harmful organic pollutants into innocuous compounds such as CO2 and H2O
Fig. Mechanism of the oxidation of benzene by Hydroxyl Radicals
Types of AOPs AOPs based on Ozone
AOPs based on Hydrogen Peroxide
Fenton Oxidation process Photolysis Photo catalysis Sonolysis Sonochemical Sonoelectrochemical Electrochemical Sonophotocatalysis
Sonophotocatalysis (Sono + Photo + Catalyst)
Combination of two advanced oxidation processes i.e. Sonication and photo catalysis
Basic reaction mechanism for both Ultrasound initiated degradation and Photo catalytic oxidation- Generation of free radicals and subsequent attack by these on the pollutant organic species
In Photo catalytic oxidation, efficiency reduces due to blocking of the catalyst activated sites
Turbulence induced by Cavitation phenomena under the action of turbulence generated by acoustic streaming – Elimination the drawbacks associated with photo catalytic oxidation
More number of free radicals are generated due to combination of 2 modes ; thereby increases the rates of reaction
Reaction MechanismReactions involved in Photo catalysis:
TiO2 + hv → TiO2 (e- + h+) TiO2 (h+) + H2O → TiO2 + H+ + HO-TiO2 (h+) + OH- → TiO2 + HO• TiO2 (e-) + O2 → TiO2 + •O2H2O2 + hv → 2HO*
Reaction involved in Sonolysis:H2O + ))))→ H* + HO* H2O + ))))) → ½ H2 + ½ H2O2 H2O2 + H* → H2O + HO*
Instruments for Sonophotocatalysis pH meter
COD digester
Spectrophotometer
Ultrasonic bath or probe
UV source such as Lamp
Catalyst such as Zno,TiO2
Magnetic Stirrer
Magnetic Stirrer pH meter
UV Lamp
Parameters that must be looked upon pH = Acidic (2.5 - 5.5)
UV wavelength = 200 to 400 nm
US frequency = 20 kHz <
Type and Amount of catalyst = Zno,TiO2,etc.
Size of catalyst particles
Initial Concentration of waste water
Case StudySONOPHOTOCATALYTIC TREATMENT OF PHARMACEUTICAL
WASTEWATER( Department of Bio-Technology and Environmental Sciences, Thapar
University ,Patiala )Sr.No Parameter Prevailing Range
(mg/ml)
1 pH 3.75
2 COD 32
3 BOD 12.8
4 TS 25.2
5 TDS 23.9
6 TSS 1.3
7 Sulphate 3.716
8 Chloride 7.526
WASTE WATER CHARACTERISTICS
Sample taken = 1000 ml pH = 4.0 Catalyst = TiO2 Amount of TiO2 catalyst = 1 - 7 gm. Oxidant = H2O2 (works as promoter) Amount of Oxidant H2O2 = 2.3-30 ml Residence Time = 2 Hrs. Wavelength of UV lamp = 280 nm Frequency of Ultrasound = 42 KHz Size of TiO2 Catalyst = 47.1-67.5 nm.
Methodology
Sr.No
Parameter
Prevailing Range (mg/ml)
After Sonophotocatalytic Treatment (mg/ml)
Percentage Degradation
1 pH 3.75 7.1 -
2 COD 32 0.32 99%
3 BOD 12.8 0.15 98.8%
4 TS 25.2 0.00 100%
5 TDS 23.9 0.102 99.5%
6 TSS 1.3 0.00 100%
7 Sulphate 3.716 0.232 93.7%
8 Chloride 7.526 0.092 98.7%
Final Characteristics
Results show that-
Efficient and Environmental friendly technique
Almost 95% degradation of recalcitrant organic pollutants
Wastewater compounds are degraded rather than concentrated or transferred into a different phase - No need of disposal of any materials
Increases the chances for the reuse of wastewater
So, we can say that Sonophotocatalysis has a good capability to treat the waste water of various industries
Results & Discussions
Advantages More number of free radicals will be available for the reaction thereby
increasing the rates of reaction
Rate constants of the combined process are greater than the sum of the rate constants of the individual processes
Wastewater compounds are degraded rather than concentrated or transferred into a different phase - there is no need to dispose of the treated materials
Complete degradation of organics into CO2 and H2O in a relatively short period of time, i.e.do not introduce any new hazardous substances into the water.
Superior over other conventional methods of wastewater treatments, in the presence of bio - recalcitrant compounds
It can effectively degrade phenols, all halides, inorganic chemicals, dyes, herbicides, pesticides
Current Shortcomings1. Removal rate of SPC is relatively high while the Operating cost is
relatively expensive due to the use of reagents and irradiation sources
2. Some techniques require pre-treatment of wastewater to ensure reliable performance, which could be potentially costlier
3. Given the potential costs, SPC may not individually handle a large amount of wastewater; instead, it should be deployed in the final stage after primary and secondary treatment have successfully removed a large proportion of contaminants
SPC wastewater treatments hardly feasible for the industry scale up because:
- Poor attention from most of the scientific community towards energy intensification in SPC- Early stage of development- Lack of standard strategies for the design of large and efficient reactors.
Still many research needs in the field of SPC treatment for wastewater ,to provide:
– Better understanding of the mechanisms of SPC– Measurements of the efficiency of process under controlled experimental conditions– Realistic evaluations of the relative costs of candidate processes versus other treatment processes
Greater effort is needed to fully understand the difficulties in the degradation process:
- To reduce the cost of waste treatment - To improve existing and future applications
Current Scenario
Conclusion Sonophotocatalysis has provided promising results from a technical and
environmental point of views while the economics aspects are still being optimized.
Future dimensions of domain of SPC depending on consideration of optimization following parameters:
1) Operating time 2) Operating cost
Research on AOPs will surely bridge a gap between innovation, invention & its application towards society.Water is H2O, hydrogen two parts, oxygen one but there is also a third thing, that makes it water and nobody knows what that is.
–D.H. Lawrence (1885–1930)
References-1 .Aitali M.K, “Wastewater depollution by photo catalytic and biodegradation processes”, (2002)1-7.
2. Adewuyi Y.G, Env. Sci. Technol. 39 (2005) 8557.
3. Alaton and Balcioglu, I. (2002) “The effect of pre-ozonation on the H2O2/UV treatment of raw and biological pre-treated textile
industry wastewater”, Water Sci. Technol., 45: 297-304.
4. Amarnath R.K, Ultrasonic chemistry, A survey and energy assessment, TR-109974, Final report, April 1998.
5. An T et al, “Decolourization and COD removal from reactive dye-containing wastewater using sonophotocatalytic technology”, Journal
of Chemical Technology & Biotechnology, Volume 78, Number 11, November 2003 , pp. 1142-1148.
6.Bahena C.L et al, Sonophotocatalytic degradation of alazine
7.Beltran, F. J., Encinar, J. M. and Alonso, M. A. (1998) “1.Nitroaromatic hydrocarbon ozonation in water. 2. Combined ozonation with
hydrogen peroxide or UV radiation”, Ind. Eng. Chem. Res., 37: 32-40.
8.Berberidou.C et al, “Sonolytic, photocatalytic and Sonophotocatalytic degradation of malachite green in aqueous solutions”,
Environmental 74 (2007) 63–72.
9. Chen Y.C, “Effect of Ultrasound on the Photo catalytic Degradation of Organic Compounds”, (2002) 1-59.
10. Chen Y.C, “Enhancement on Photo catalytic Degradation of Phenol by Ultrasound” (2002) 10-31.
Queries
??Any
Thank You…!