IMAGE PROCESSING TO DETERMINE MASS TRANSFER COEFFICIENT FOR GAS BUBBLE
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 sin...
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Al-Nahrain Journal for Engineering Sciences
2008-03-01
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Online Access: | https://nahje.com/index.php/main/article/view/519 |
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doaj-e6ba6505e88e4e60b35124977ded91452020-11-25T01:58:10ZengAl-Nahrain Journal for Engineering Sciencesمجلة النهرين للعلوم الهندسية2521-91542521-91622008-03-01112263269519IMAGE PROCESSING TO DETERMINE MASS TRANSFER COEFFICIENT FOR GAS BUBBLENaseer A. Al-Habobia0Aalaa A. Turkib1Chemical Engineering in Al- Nahrain UniversityChemical Engineering in Al- Nahrain UniversityThis 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/shttps://nahje.com/index.php/main/article/view/519Bubble Columns, Mass Transfer,Coalescing, Flow Regime, Image Processing |
collection |
DOAJ |
language |
English |
format |
Article |
sources |
DOAJ |
author |
Naseer A. Al-Habobia Aalaa A. Turkib |
spellingShingle |
Naseer A. Al-Habobia Aalaa A. Turkib IMAGE PROCESSING TO DETERMINE MASS TRANSFER COEFFICIENT FOR GAS BUBBLE مجلة النهرين للعلوم الهندسية Bubble Columns, Mass Transfer, Coalescing, Flow Regime, Image Processing |
author_facet |
Naseer A. Al-Habobia Aalaa A. Turkib |
author_sort |
Naseer A. Al-Habobia |
title |
IMAGE PROCESSING TO DETERMINE MASS TRANSFER COEFFICIENT FOR GAS BUBBLE |
title_short |
IMAGE PROCESSING TO DETERMINE MASS TRANSFER COEFFICIENT FOR GAS BUBBLE |
title_full |
IMAGE PROCESSING TO DETERMINE MASS TRANSFER COEFFICIENT FOR GAS BUBBLE |
title_fullStr |
IMAGE PROCESSING TO DETERMINE MASS TRANSFER COEFFICIENT FOR GAS BUBBLE |
title_full_unstemmed |
IMAGE PROCESSING TO DETERMINE MASS TRANSFER COEFFICIENT FOR GAS BUBBLE |
title_sort |
image processing to determine mass transfer coefficient for gas bubble |
publisher |
Al-Nahrain Journal for Engineering Sciences |
series |
مجلة النهرين للعلوم الهندسية |
issn |
2521-9154 2521-9162 |
publishDate |
2008-03-01 |
description |
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 |
topic |
Bubble Columns, Mass Transfer, Coalescing, Flow Regime, Image Processing |
url |
https://nahje.com/index.php/main/article/view/519 |
work_keys_str_mv |
AT naseeraalhabobia imageprocessingtodeterminemasstransfercoefficientforgasbubble AT aalaaaturkib imageprocessingtodeterminemasstransfercoefficientforgasbubble |
_version_ |
1724971095193288704 |