A mass transfer model of absorption of carbon dioxide in a bubble column reactor by using magnesium hydroxide slurry

2013 ◽  
Vol 17 ◽  
pp. 240-249 ◽  
Author(s):  
L. Cheng ◽  
T. Li ◽  
T.C. Keener ◽  
J.Y. Lee
Keyword(s):  
Carbon Dioxide ◽  
Mass Transfer ◽  
Magnesium Hydroxide ◽  
Bubble Column ◽  
Bubble Column Reactor ◽  
Transfer Model ◽  
Mass Transfer Model ◽  
Column Reactor

scholarly journals Mass Transfer Coefficient Studies in Bubble Column Reactor

2010 ◽  
Vol 4 (7) ◽  
Author(s):  
D. Devakumar ◽  
K. Saravanan ◽  
T. Kannadasan ◽  
B. Meenakshipriya
Keyword(s):  
Mass Transfer ◽  
Transfer Coefficient ◽  
Mass Transfer Coefficient ◽  
Bubble Column ◽  
Bubble Column Reactor ◽  
Column Reactor

scholarly journals CARBON DIOXIDE BIOFIXATION BY Chlorella sp. IN A BUBBLE COLUMN REACTOR AT DIFFERENT FLOW RATES AND CO2 CONCENTRATIONS

2019 ◽  
Vol 36 (2) ◽  
pp. 639-645 ◽  
Author(s):  
Reza Pourjamshidian ◽  
Hossein Abolghasemi ◽  
Mohammad Esmaili ◽  
Hossein D. Amrei ◽  
Mehran Parsa ◽  
...  
Keyword(s):  
Carbon Dioxide ◽  
Bubble Column ◽  
Bubble Column Reactor ◽  
Flow Rates ◽  
Column Reactor ◽  
Chlorella Sp ◽  
Co2 Concentrations

scholarly journals An Experimental Investigation of Overall Mass Transfer coefficient ( K_Ga ) of 〖CO〗_2 absorption using Monoethanolamine(MEA) and Diethanolamine(DEA) in a Bubble Column Reactor (BCR)

2020 ◽  
Vol 13 (1) ◽  
pp. 67-73
Author(s):  
Elaf Thamera ◽  
Salih Abduljabbar Rushdi
Keyword(s):  
Mass Transfer ◽  
Transfer Coefficient ◽  
Mass Transfer Coefficient ◽  
Flow Rate ◽  
Gas Flow ◽  
Bubble Column ◽  
Bubble Column Reactor ◽  
Air Flow Rate ◽  
Column Reactor ◽  
Overall Mass Transfer Coefficient

In this work, an absorption technology   was used actually to investigation the  mass transfer coefficient of carbon dioxide from a gaseous mixture (air, carbon dioxide) in  blended solution Monoethanolamine (MEA) and Diethanolamine (DEA)  in a bubble column reactor (BCR) . The bubble column reactor(BCR) was made of Plexiglas with 1.5 m high and 0.1 m inside diameter. The overall mass transfer coefficient (  was evaluated at different operating conditions , gas flow rate, air Flow rate ,liquid flow rate .Where the gas flow rates were 10, 15 and 20 L /min ,  air flow rate 100,150 and 200 L/h ,and liquid flow rate 5 ,10,15 L /min . This experiment  by   using  continuous   process with helping centrifugal  pump  . High-performance gas chromatographic (GC) was performed to evaluate  loading during absorption experiment . The  experimental results have shown that the   loading in range of  0.581-1.367 (mol  /mole amine),and the maximum value of overall mass transfer coefficient ( KG) was 0.04 S-1 .

scholarly journals Gas-liquid mass transfer with instantaneous chemical reaction in a slurry bubble column containing fine reactant particles

2016 ◽  
Vol 22 (1) ◽  
pp. 85-93 ◽  
Author(s):  
Xiaolei Li ◽  
Chunying Zhu
Keyword(s):  
Mass Transfer ◽  
Transfer Coefficient ◽  
Mass Transfer Coefficient ◽  
Chemical Reaction ◽  
Bubble Column ◽  
Transfer Model ◽  
Phase System ◽  
Mass Transfer Model ◽  
Slurry Bubble Column ◽  
Irreversible Chemical Reaction

In this study, the mass transfer accompanied by an instantaneous irreversible chemical reaction in a slurry bubble column containing sparingly soluble fine reactant particles has been analyzed theoretically. Based on the penetration theory, combining the cell model, a one-dimensional mass transfer model was developed. In the model, the effects of the particle size and the particle dissolution near the gas-liquid interface on the mass transfer were taken into account. The mass transfer model was solved and an analytical expression of the time-mean mass transfer coefficient was attained. The reactive absorption of SO2from gas mixtures into Mg(OH)2/water slurry was investigated experimentally in a bubble column reactor to validate the mass transfer model. The results indicate that the present model has good predicting performance and could be used to predict mass transfer coefficient for the complicated gas-liquid-solid three-phase system with an instantaneous irreversible chemical reaction.

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