IMAGE PROCESSING TO DETERMINE MASS TRANSFER COEFFICIENT FOR GAS BUBBLE

Authors

  • Naseer A. Al-Habobia Chemical Engineering in Al- Nahrain University
  • Aalaa A. Turkib Chemical Engineering in Al- Nahrain University

Keywords:

Bubble Columns, Mass Transfer,, Coalescing, Flow Regime, Image Processing

Abstract

This paper suggests a simple system to study the hydrodynamics in a bubble column reactor and measuring gas-liquid specific interfacial area a,

individual mass transfer coefficient kL, gas holdupG, flow regime, bubble size distribution, coalescence of bubbles, and bubble rising velocity for a single bubble by using image processing techniques. The images were taken by a digital camera and then analyzed with MATLAB 2008 to extract the required data of design parameters for the bubble columns. Experiments of bubble column of (0.081m diameter and 1.03 m height) were carried out with air-water. Gas velocity UG

is varied from (0.22×10-4 -0.22×10-3) m/s. This range of values of UG allows the study the homogeneous flow regimes. To study the flow regime in bubble column the gas velocity changes from (0.00967-0.131521 m/s), afford to study and select the Homogeneous, Transition and Heterogeneous regimes. Transition velocity from bubbly to churn turbulent flow for (air-water) system, was about 0.148982 m/s

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Published

05-03-2008

How to Cite

[1]
N. A. Al-Habobia and A. A. Turkib, “IMAGE PROCESSING TO DETERMINE MASS TRANSFER COEFFICIENT FOR GAS BUBBLE”, NJES, vol. 11, no. 2, pp. 263–269, Mar. 2008, Accessed: Nov. 13, 2024. [Online]. Available: https://nahje.com/index.php/main/article/view/519

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