Influence of reactor geometry on mixing characteristics in a down flow jet loop bioreactor: newtonian and non-newtonian fluids |
| |
Authors: | M Velan T K Ramanujam |
| |
Institution: | (1) Department of Chemical Engg., Indian Institute of Technology, 600 036 Madras, India;(2) Department of Chemical Engg., Alagappa College of Technology, Anna University, 600 025 Madras, India |
| |
Abstract: | Mixing characteristics in the downcomer and the riser of a continuous down-flow jet loop bioreactor was studied with Newtonian and non-Newtonian fluids. The mixing parameters were determined through the curve fitting of the experimental impulse response data with the solution of one dimensional axial dispersion model. It was found that circulation number and axial dispersion coefficient increased with an increase in liquid flow rate and draft tube to column diameter ratio and the axial dispersion coefficient was comparatively higher in the riser. The circulation number increased with decrease in nozzle diameter. The model predicted the experimental data well within 8% deviation for both the systems (water and CMC). Correlations were obtained to predict axial dispersion coefficients in the riser and downcomer of the reactor. |
| |
Keywords: | |
本文献已被 SpringerLink 等数据库收录! |
|