Mixing time in an agitated multi-lamp cylindrical photoreactor using electrical resistance tomography

BACKGROUND: There is scarce information on the application of electrical resistance tomography (ERT) in UV photoreactors, in which mixing and mass transfer are important. Therefore, the feasibility of an ERT system in an agitated multi-lamp UV photoreactor was investigated to monitor the mixing process. RESULTS: The locations of the UV tubes had a significant impact on the mixing time, particularly at the lower impeller speeds (45 and 150 rpm). Also, at the higher impeller speeds (250, 350, and 500 rpm) and the same radial position (r), changing the angle θ from 15 to 45°, resulted in only a slight variation of the mixing time. Finally, the maximum mixing time occurred when UV tubes were positioned at r = 13 cm (r/R = 0.68) and θ = 0°, while minimum mixing time occurred at location r = 16 cm (r/R = 0.83) and θ = 45°. CONCLUSION: The experimental results demonstrated the feasibility of the ERT system to monitor the mixing process in the UV photoreactor. The ERT results also indicated that the locations of the UV tubes had a significant effect on the mixing performance of the photoreactor. Furthermore, the mixing time varied inversely with the rotational speed, and this effect was more pronounced at lower speeds. Copyright © 2008 Society of Chemical Industry

[1]  F. Ein-Mozaffari,et al.  Using dynamic tests to study the continuous mixing of xanthan gum solutions , 2008 .

[2]  T.A. York,et al.  Towards process tomography for monitoring pressure filtration , 2005, IEEE Sensors Journal.

[3]  R. Britter,et al.  Mixing times for passive tracers in stirred tanks , 1985 .

[4]  J. Joshi,et al.  Liquid-phase mixing in stirred vessels: turbulent flow regime , 2003 .

[5]  Lin Li,et al.  Three-dimensional image analysis of mixing in stirred vessels , 1999 .

[6]  Robert West,et al.  Parametric modelling in industrial process tomography , 2000 .

[7]  M. Kaminoyama,et al.  Monitoring stability of reaction and dispersion states in a suspension polymerization reactor using electrical resistance tomography measurements , 2005 .

[8]  Jyeshtharaj B. Joshi,et al.  LIQUID PHASE MIXING IN MECHANICALLY AGITATED VESSELS , 1988 .

[9]  Gary Lucas,et al.  A six-electrode local probe for measuring solids velocity and volume fraction profiles in solids-water flows , 2000 .

[10]  René David,et al.  Effects of the Stirred Tank's Design on Power Consumption and Mixing Time in Liquid Phase , 2000 .

[11]  Farhad Ein-Mozaffari,et al.  Using CFD and Ultrasonic velocimetry to Study the Mixing of Pseudoplastic Fluids with a Helical Ribbon Impeller , 2007 .

[12]  Wuliang Yin,et al.  Measurements of the Concentration and Velocity Distribution in Miscible Liquid Mixing Using Electrical Resistance Tomography , 2001 .

[13]  C. J. Kotre,et al.  A sensitivity coefficient method for the reconstruction of electrical impedance tomograms. , 1989, Clinical physics and physiological measurement : an official journal of the Hospital Physicists' Association, Deutsche Gesellschaft fur Medizinische Physik and the European Federation of Organisations for Medical Physics.

[14]  M. Mehrvar,et al.  Pilot-plant study for the photochemical treatment of aqueous linear alkylbenzene sulfonate , 2006 .

[15]  S. Nagata,et al.  Power Characteristics of Mixing Impellers , 1956 .

[16]  D. Geselowitz An application of electrocardiographic lead theory to impedance plethysmography. , 1971, IEEE transactions on bio-medical engineering.

[17]  J. Landau,et al.  Studies on mixing. XII. Homogenation of miscible liquids in the turbulent region , 1961 .

[18]  Jyeshtharaj B. Joshi,et al.  EFFECT OF IMPELLER DESIGN ON LIQUID PHASE MIXING IN MECHANICALLY AGITATED REACTORS , 1991 .

[19]  J. Villermaux,et al.  A method for the study of turbulent mixing using fluorescence spectroscopy , 1990 .

[20]  R. Biggs,et al.  Mixing rates in stirred tanks , 1963 .

[21]  M. Moo‐Young,et al.  The blending efficiencies of some impellers in batch mixing , 1972 .

[22]  Vivek V. Ranade,et al.  Fluid mechanics and blending in agitated tanks , 1991 .

[23]  Residence time distribution of fluids in stirred annular photoreactor , 2003 .

[24]  A. V. Shepelin,et al.  Experimental Study of the Distribution Function of Water Residence Time in Disinfection Plants , 2001 .

[25]  Tomasz Dyakowski,et al.  Application of electrical resistance tomography to interrogate mixing processes at plant scale , 1997 .

[26]  R. Mann,et al.  Flow distribution and velocity measurement in a radial flow fixed bed reactor using electrical resistance tomography , 2004 .

[27]  Tom Dyakowski,et al.  Imaging nylon polymerisation processes by applying electrical tomography , 2000 .

[28]  A. B. Metzner,et al.  Flow patterns in agitated vessels , 1960 .

[29]  P. Savoye,et al.  Impact of water quality and reactor hydrodynamics on wastewater disinfection by UV, use of CFD modeling for performance optimization , 1998 .

[30]  C. Wong,et al.  Studies on homogenization efficiency of various agitators in liquid blending , 1984 .

[31]  Dominique Toye,et al.  Possibilities and Limits of Application of Electrical Resistance Tomography in Hydrodynamics of Bubble Columns , 2008 .

[32]  J. Leclerc,et al.  Influence of inlet positions on the flow behavior inside a photoreactor using radiotracers and colored tracer investigations. , 2007, Applied radiation and isotopes : including data, instrumentation and methods for use in agriculture, industry and medicine.

[33]  Ward Rw,et al.  Residual toxicity of several disinfectants in domestic wastewater. , 1978 .

[34]  O. Karl Scheible,et al.  The History of UV and Wastewater , 2004 .