Residence time distribution studies in microstructured plate reactors

Abstract Residence time distributions (RTDs) have been investigated experimentally for reactors with straight and zig-zag channels. The channels are formed by microstructured plates placed on top of each other and containing obstacles and holes to allow flow in 3 dimensions. Experimental RTD measurements were performed by monitoring the concentration of a tracer dye by means of a LED-photodiode system. The RTD was obtained for five different flowrates and four geometries containing straight and zig-zag channels. It was found that the zig-zag channel configuration gives a narrower distribution as compared to the straight channel ones. Secondary flows were thought to be present in the zig-zag channel even at small Reynolds numbers. Furthermore, as the flowrate increased, the variance of the distribution of all geometries increased. The RTD for a single rectangular cross section channel (with no 3-dimensional flow) was found to have the largest variance from all reactors investigated due to its largest hydraulic diameter. However, its variance was not far from those of microstructured reactors and this was attributed to its small aspect ratio (shallow, wide channel). The RTDs of all microstructured reactors, and in particular the zig-zag geometry, were less sensitive to flowrate increase than the RTDs of the rectangular channel, for the range of flowrates investigated.

[1]  Patrice Tochon,et al.  Intensification of heat-transfer and mixing in multifunctional heat exchangers by artificially generated streamwise vorticity , 2006 .

[2]  Debashis Dutta,et al.  Effect of channel geometry on solute dispersion in pressure-driven microfluidic systems , 2006 .

[3]  T. Henkel,et al.  Characterisation of residence time and residence time distribution in chip reactors with modular arrangements by integrated optical detection , 2004 .

[4]  Octave Levenspiel,et al.  The interpretation of residence-time experiments , 1970 .

[5]  Hassan Peerhossaini,et al.  Chaotic heat transfer for heat exchanger design and comparison with a regular regime for a large range of Reynolds numbers , 2000 .

[6]  Catherine Xuereb,et al.  Effect of microchannel aspect ratio on residence time distributions and the axial dispersion coefficient , 2009 .

[7]  Aydın Durmuş,et al.  Investigation of heat transfer and pressure drop in a concentric heat exchanger with snail entrance , 2002 .

[8]  Asterios Gavriilidis,et al.  Residence time distributions in microchannels: Comparison between channels with herringbone structures and a rectangular channel , 2010 .

[9]  Dirk Janasek,et al.  A novel method for determining residence time distribution in intricately structured microreactors. , 2008, Lab on a chip.

[10]  Saif A. Khan,et al.  Transport and reaction in microscale segmented gas-liquid flow. , 2004, Lab on a chip.

[11]  C. W. Gardiner,et al.  Handbook of stochastic methods - for physics, chemistry and the natural sciences, Second Edition , 1986, Springer series in synergetics.

[12]  Adeniyi Lawal,et al.  Mass transfer enhancement in microchannel reactors by reorientation of fluid interfaces and stretching , 2005 .

[13]  Krishna D.P. Nigam,et al.  Coiled configuration for flow inversion and its effect on residence time distribution , 1984 .

[14]  Milorad P. Dudukovic,et al.  Convolution and deconvolution of nonideal tracer response data with application to three-phase packed-beds , 1989 .

[15]  R. Aris On the dispersion of a solute in a fluid flowing through a tube , 1956, Proceedings of the Royal Society of London. Series A. Mathematical and Physical Sciences.

[16]  G. Taylor Dispersion of soluble matter in solvent flowing slowly through a tube , 1953, Proceedings of the Royal Society of London. Series A. Mathematical and Physical Sciences.

[17]  A. Vikhansky,et al.  Effect of diffusion on residence time distribution in chaotic channel flow , 2008 .

[18]  I. Mezić,et al.  Chaotic Mixer for Microchannels , 2002, Science.

[19]  J. Josserand,et al.  Mixing processes in a zigzag microchannel: finite element simulations and optical study. , 2002, Analytical chemistry.

[20]  E. B. Nauman,et al.  Mixing in continuous flow systems , 1983 .

[21]  Dusan Boskovic,et al.  Modelling of the residence time distribution in micromixers , 2008 .

[22]  O. Levenspiel,et al.  Tracer curves and the residence time distribution , 1970 .

[23]  Octave Levenspiel,et al.  Notes on the diffusion-type model for the longitudinal mixing of fluids in flow , 1995 .

[24]  T. Liliedahl,et al.  Analysis method of pyrolysis kinetics using modern signal processing techniques , 1991 .

[25]  Malcolm R. Mackley,et al.  The measurement and characterisation of residence time distributions for laminar liquid flow in plastic microcapillary arrays , 2009 .