Abstract

The oxidation of methyl tert-butyl ether (MTBE) by advanced oxidation processes in conjunction with biological treatment in investigated. Firsst, the degradation of MTBE by UV/H2O2 and UV/TiO2 is studied. It is found that the optimum molar ratio or H2O2/MTBE is about 14 while the optimum concentration of TiO2 is 1.5 g/L. In addition, it is observed that a combined process of UV/H2O2 and UV/TiO2 does not have any advantage over each of these processes alone. In the second phase, biodegradability of MTBE by aerobic microorganisms is evaluated in three different approaches including BODu assessment, removal of MTBE by non-acclimated, and acclimated microorganisms. It is shown that the acclimatization of microorganisms enhances the rate of biodegradation of MTBE. Finally, it is observed that the rate of bioreaction is not improved after a photochemical pre-treatment. It is also found that using the integration of photochemical and biological treatment reduced the total residence time.

Highlights

  • Today one o f the most important global issues is water because o f its limited and valuable sources in the world

  • It was indicated that in a continuously stirred tank reactor (CSTR), the addition o f H2O2 to O3 resulted in an increase o f the rate and degree o f methyl /e/V-butyl ether (MTBE) degradation, t-butyl formate (TBF), t-butyl alcohol (TBA), methyl acetate, and acetone were determined as products o f the reactions o f O3 and O3/H 2O2 with MTBE

  • Comparison between energy wasted during bacterial growth on MTBE and that o f TB A suggested that large energy expenditure v.-ss related to the breakage o f ether bond in methyl /erZ-butyl ether (M TBE), but still losses o f energy occurred after the initial step o f M TBE degradation to TB A

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Summary

Cost Optimization for Combined Photochemical and Biological Processes for the LIST OF FIGURES

NPDOC: Non-Purgeable Dissolved Organic Carbon r: rate R: molar ratio o f H2O2 / M TBE RE; Removal Efficiency RFG: Reformulated Gasoline S : substrate concentration, mass/ volume SBR: Sequential Batch Reactor T: TiO] t: residence time, min TB A : /e/7-butyl alcohol TBF; /e/-/-butyl formate TOC: Total Organic Carbon, mg C/L TSS; Total Suspended Solid, mg/L V B : valance band. Tj : Efficiency v : frequency o f U V radiation H : specific bacterial growth rate, time''. Subsc rip ts 0 : initial B; biological reactor C: chemical reactor g: bacterial growth m: maximum S: substrate t: residence time T ; /e;7-butyl formate U: ultimate xvm ReDroduced with permission of the copyright owner.

INTRODUCTION
CHAPTER 2 LITERATURE REVIEW
Properties of MTBE
Principles of Advanced Oxidation Processes (AOPs)
UV/Hydrogen Peroxide Process
Photocatalysis
Ozone/UV Process
Fenton’s Reagent
Vacuum Ultraviolet (VUV) Process
Biological Treatment of Organics in Water
Combination of Advanced Oxidation Processes and Biological Treatment
Examples of Applications of Different AOPs for Degradation of Organic Compounds
Previous Studies on MTBE Degradation
Previous Studies on the Combination of Advanced Oxidation and Biological Processes
Photochemical Experimental Set-up
Chemical Degradation Experiments
Biodegradability of MTBE and Intermediates
Study of Biological Treatment
Biological Experimental Set-Up for Determination of Ultimate BOD
Biological Experimental Set-Up for Biodégradation o f MTBE by Mixed Culture
Biological Experimental Set-up for Biodégradation of MTBE by Acclimated Microorganisms
3.2.23.2. Biodégradation Experiments
Combination of Photocatalytic and Biological Processes for the Degradation of MTBE in Water
Reagents and Materials
Determination of MTBE Concentration
H2O2 Removal
Chemical Oxygen Demand (COD)
Dissolved Oxygen (DO)
Biological Oxygen Demand (BOD)
Mixed Liquor Volatile Suspended Solid (MLVSS)
Dark Reaction
Photoreaction
The Effect of Hydrogen Peroxide on MTBE Degradation
Combination of UV Light and H2 O2
4.14.4. The Effect of Initial Concentration of MTBE on Apparent Rate Constant
Comparison o f D iffe re nt U V-Lights in Degradation ofMTBE by TiOz Photocatalysis
Combination of UV-Light 254 nm, TiO^and
Inhibitory Effects of MTBE and its Intermediates
Ultimate BOD Determination
Biodégradation of MTBE by Mixed Culture
Biodégradation of MTBE by Acclimated Activated Sludge
Combination of Photochemical and Biological Processes for the Treatment of MTBE
Cost Optimization for Combined Photochemical and Biological Processes for the Treatment of MTBE
UE) a o
Conclusions
Recommendations
A: Determination of B O D 5
B: Determination of Removal Efficiency
C: Determination of Reaction Rate Constant
E: Determination of Ultimate BOD
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