Mathematical model involving chemical reaction and mass transfer for the ozonation of dimethyl phthalate in water in a bubble column reactor
Abstract
This research investigated the establishment of a mathematical model for the ozonation of dimethyl phthalate (DMP) through the analysis of the mass transfer and reactions in a semi-batch bubble column reactor. Negative step tracer experiments were conducted with ozone as a tracer, which indicated that the gas phase is perfectly well mixed at the gas flow rate of 400 mL/min. Based on the results from ozone absorption experiments the mass transfer coefficient of ozone was determined to be 0.0054 s−1. The measured stoichiometry ratio of the direct reaction between ozone and DMP was about 5. The calculated rate constant was 0.87 L/(mol·s) for the direct reaction between ozone and DMP. A mathematical model was established based on the component mass balance in the reaction system involving the direct and indirect reactions and mass transfer between gas and liquid phases enhanced by the chemical reactions. The model can predict the removal of DMP for the early stage of the ozonation process well. At the latter stage, the predicated removals deviated from the measured results mainly due to the consumption of ozone by side reactions.
Acknowledgements
Thanks are given to the National Natural Science Foundation of China (Project No. 20907072) for the financial support of this work.
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Nomenclature
Concentration of DMP in liquid phase | |
Initial concentration of DMP in liquid phase | |
Concentration of HO· in liquid phase | |
Interfacial concentration of ozone in the gas-liquid film (mol/L) | |
Concentration of ozone in gas phase (mol/L) | |
Gas-phase concentration of ozone at the reactor inlet (mol/L) | |
Concentration of ozone in aqueous phase | |
Concentration of tracer (ozone) at time t | |
Concentration of tracer (ozone) at initial time | |
Concentrations of the products in liquid phase | |
Concentrations of the scavengers in liquid phase | |
Diameter of the bubble column (m) | |
Diffusion coefficient of DMP in water (cm2/s) | |
Diffusion coefficient of ozone in water(cm2/s) | |
E | Enhancement factor |
E(t) | Residence time distribution function, |
F(t) | Evolution of dimensionless tracer (ozone) concentration, |
Height of liquid in the bubble column with aeration (m) | |
Height of liquid in the bubble column without aeration (m) | |
N | Number of tanks in series |
Molar flux of ozone diffusing from the outer edge of a liquid element (film) to the main liquid (M/(m2·s)) | |
Molar flux of ozone diffusing from the gas into the interface (M/(m2·s)) | |
Q | Gas flow rate ( |
Ozone solubility rate | |
T | Temperature of the solution (K) |
Molar volume of DMP in the solution, 214.6 cm3/mol | |
a | Specific interfacial area between gas and liquid phases (m2/m3) |
Rate constant for the reaction between DMP and hydroxyl radical | |
Chemical mass transfer coefficient of ozone (m/s) | |
Volumetric mass transfer coefficient of ozone in water (s−1) | |
Physical mass transfer coefficient of ozone (m/s) | |
Second-order rate constant for the reaction between ozone and DMP (L/(mol·s)) | |
Rate constant for the reaction between the products and hydroxyl radical | |
Rate constant for the reaction between the scavengers and hydroxyl radical | |
First-order rate constant for the self-decomposition of ozone (s−1) | |
Rate constant for the reaction between O3 and OH−, 70 M−1S−1 | |
r | Stoichiometry of the reaction between ozone and DMP |
t | Time (s) |
Mean residence time of the actual distribution function (s), | |
Superficial gas velocity (m/s), | |
β | Gas holdup, |
η | Ratio of molar fluxes of ozone |
μ | Viscosity of water (Pa·s) |
σ | Variance of distribution, |
τi | Hydraulic residence time of the ith tank (s) |
© 2017 by Walter De Gruyter GmbH
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Articles in the same Issue
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- An overview on heterogeneous Fenton and photoFenton reactions using zerovalent iron materials
- Photooxidative Degradation of Pesticides in Water; Response Surface Modeling Approach
- The treatment of aniline in aqueous solutions by gamma irradiation
- Microwave regeneration of biological activated carbon
- Molecular iodine/aqueous NH4OAc: a green reaction system for direct oxidative synthesis of nitriles from amines
- Catalytic Degradation of Safranin T in Aqueous Medium Using Non-conventional Processes
- Oxidation of 1, 2-dichlorobenzene on a commercial V2O5-WO3/nano-TiO2 catalyst: Effect of HCl addition
- Current conduction mechanisms in thermal nitride and dry gate oxide grown on 4H-silicon carbide (SiC)
- Effect of light and oxygen on repetitive bacterial inactivation on uniform, adhesive, robust and stable Cu-polyester surfaces
- Wet oxidation of an industrial high concentration pharmaceutical wastewater using hydrogen peroxide as an oxidant
- Oxidation characteristics of heavy crude oil in ignition process
- Comparative studies on the performance of porous Ti/Sno2-Sb2O3/Pbo2 enhanced by CNT and Bi Co-doped electrodes for methyl orange oxidation
- Application of photocatalytic paint for destruction of benzo[a]pyrene. Impact of air humidity
- Spray-drying synthesis and characterization of Li4Ti5O12 anode material for lithium ion batteries
- Kinetics analysis of photocatalytic degradation of Acid Orange 7 by Co/N/Er3+: Y3Al5O12/TiO2 films
- Reaction characteristics of oxygen generation from plate-like potassium superoxide within a confined space
- Electrochemical reduction of CO2 on a Cu2O/polyaniline /stainless steel based electrode
- Role of oxygen-containing functional surface groups of activated carbons on the elimination of 2-hydroxybenzothiazole from waters in A hybrid heterogeneous ozonation system
- The degradation efficiency and mechanism of meclofenamic acid in aqueous solution by UV irradiation
- Effect of electrode oxide film in micro arc oxidation on water treatment
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