Wet air oxidation: a review of process technologies and aspects in reactor design

Abstract Wet air oxidation is one of the available technologies for the treatment of aqueous wastewaters. In wet air oxidation aqueous waste is oxidized in the liquid phase at high temperatures (400–573 K) and pressures (0.5–20 MPa) in the presence of an oxygen-containing gas (usually air). The advantages of the process include low operating costs and minimal air pollution discharges, while the main limitations are the high capital costs and safety implications associated with a system operating at such severe operating conditions. As a consequence, significant development in wet air oxidation technology has concentrated on methods of reducing the prohibitive capital costs. In the design of the process a balance must therefore be made between the enhancement of overall reaction rates with temperature and pressure against their effect on capital cost and operational difficulties such as corrosion and scaling of equipment. In this paper the wet air oxidation process is introduced and a number of commercial and emerging technologies presented. These technologies employ a variety of methods to ameliorate the limitations of the technology whilst maintaining acceptable overall reaction rates. These include methods to improve mass transfer as well as the use of both homogeneous and heterogeneous catalysts to enhance reaction rate.

[1]  P. Wilkinson,et al.  Design parameters estimation for scale‐up of high‐pressure bubble columns , 1992 .

[2]  František Kaštánek,et al.  Chemical reactors for gas-liquid systems , 1992 .

[3]  K. Westerterp,et al.  Mass transfer phenomena and hydrodynamics in agitated gas—liquid reactors and bubble columns at elevated pressures: State of the art , 1989 .

[4]  S. G. Dixit,et al.  Destruction of phenol from wastewater by oxidation with sulfite-oxygen , 1991 .

[5]  V. V. Mahajani,et al.  Kinetics of Wet Air Oxidation of Glyoxalic Acid and Oxalic Acid , 1994 .

[6]  P. L. Silveston,et al.  Catalytic Oxidation of Phenol in Aqueous Solution over Copper Oxide , 1978 .

[7]  A. R. Wilhelmi,et al.  Wet air oxidation — A treatment means for aqueous hazardous waste streams , 1985 .

[8]  Roger Matthews,et al.  Performance update: Low pressure wet air oxidation unit at grangemouth, Scotland , 1997 .

[9]  S. Kolaczkowski,et al.  Degradation of maleic acid in a wet air oxidation environment in the presence and absence of a platinum catalyst , 1999 .

[10]  J. Foussard,et al.  Treatment of organic aqueous wastes: Wet air oxidation and Wet Peroxide Oxidation. , 1996, Environmental pollution.

[11]  E. Chornet,et al.  High shear jet‐mixers as two‐phase reactors: An application to the oxidation of phenol in aqueous media , 1987 .

[12]  S. Kolaczkowski,et al.  Wet Air Oxidation of Phenol: Factors that May Influence Global Kinetics , 1997 .

[13]  J. Baldasano,et al.  Wet Oxidation of Refractory Organic Compounds in Industrial Aqueous Wastes Via the Oxyjet Technology , 1995 .

[14]  S. Goto,et al.  Catalytic Oxidation of Formic Acid in Water. Intraparticle Diffusion in Liquid-Filled Pores , 1974 .

[15]  F. Luck A review of industrial catalytic wet air oxidation processes , 1996 .

[16]  J. Katzer,et al.  Involvement of free radicals in the aqueous-phase catalytic oxidation of phenol over copper oxide , 1974 .

[17]  K. Westerterp,et al.  Interfacial Areas and Gas Hold-ups in Bubble Columns and Packed Bubble Columns at Elevated Pressures , 1989 .

[18]  K. N. Clark The effect of high pressure and temperature on phase distributions in a bubble column , 1990 .

[19]  P. L. Silveston,et al.  A laboratory spinning catalyst basket reactor for multiphase contacting , 1978 .

[20]  J. Smith,et al.  Trickle‐bed reactor performance. Part II. Reaction studies , 1975 .

[21]  Christophe Bengoa,et al.  Catalytic removal of phenol from aqueous phase using oxygen or air as oxidant , 1995 .

[22]  J. Smith,et al.  Oxidation of acetic acid solutions in a trickle-bed reactor , 1976 .

[23]  Y. R. Mayhew,et al.  Thermodynamic and transport properties of fluids , 1967 .

[24]  Ching-Ming Ko,et al.  Catalytic wet oxidations of phenol- and p-chlorophenol-contaminated waters , 1995 .

[25]  P. Yue Oxidation reactors for water and wastewater treatment , 1997 .

[26]  GMaskill Smith,et al.  The chemical engineer , 1946 .

[27]  J. Foussard,et al.  Wet Oxidation of Carboxylic Acids with Hydrogen Peroxide. Wet Peroxide Oxidation (WPO®) Process. Optimal Ratios and Role of Fe:Cu:Mn Metals , 1995 .

[28]  J. Baldasano,et al.  Wet oxidation via two-phase flow reactors and high mass-transfer regimes , 1992 .

[29]  P. Wilkinson,et al.  Pressure and gas density effects on bubble break-up and gas hold-up in bubble columns , 1990 .

[30]  J. Heijnen,et al.  Mass transfer, mixing and heat transfer phenomena in low viscosity bubble column reactors , 1984 .

[31]  H. A. Pray,et al.  Solubility of Hydrogen, Oxygen, Nitrogen, and Helium in Water at Elevated Temperatures , 1952 .

[32]  J. Levec,et al.  Catalytic oxidation of organics in aqueous solutions. I : Kinetics of phenol oxidation , 1992 .

[33]  Yatish T. Shah,et al.  Design parameters estimations for bubble column reactors , 1982 .

[34]  B. Pruden,et al.  Wet air oxidation of soluble components in waste water , 1976 .

[35]  W. Regenass,et al.  Design of reactors for the wet air oxidation of industrial waste water by means of computer simulation , 1979 .

[36]  A. Mersmann,et al.  Chemical Reactors for Gas-Liquid Systems. Von F. Kastánek, J. Zahradnik, J. Kratochvil und C. Cermák. Ellis Horwood, New York 1993. 406 S., mit zahlr. Abb. und Tab., geb., £ 117,50. , 1994 .

[37]  S. Goto,et al.  Liquid-Phase Oxidation of Phenol in a Rotating Catalytic Basket Reactor , 1980 .

[38]  J. Smith,et al.  Trickle‐bed reactor performance. Part I. Holdup and mass transfer effects , 1975 .

[39]  Jyeshtharaj B. Joshi,et al.  Wet air oxidation , 1995 .

[40]  G. Zaikov,et al.  Oxidation of organic compounds : medium effects in radical reactions , 1984 .

[41]  O. Levenspiel Chemical Reaction Engineering , 1972 .

[42]  D. Stegeman,et al.  Interfacial Area and Gas Holdup in a Bubble Column Reactor at Elevated Pressures , 1996 .