3D CFD modelling of liquid dispersion in structured packed bed column for CO2 capture

2020 ◽  
Vol 225 ◽  
pp. 115800
Author(s):  
Mohammad Ashraf Hossain ◽  
Seyed Ali Nabavi ◽  
Panneerselvam Ranganathan ◽  
László Könözsy ◽  
Vasilije Manovic
Keyword(s):  
Co2 Capture ◽  
Packed Bed ◽  
Cfd Modelling ◽  
Packed Bed Column ◽  
Liquid Dispersion

Enhanced CO2 capture in packed-bed column bioreactors with immobilized carbonic anhydrase

2021 ◽  
pp. 134029
Author(s):  
Hannaneh Rasouli ◽  
Ion Iliuta ◽  
Francis Bougie ◽  
Alain Garnier ◽  
Maria C. Iliuta
Keyword(s):  
Carbonic Anhydrase ◽  
Co2 Capture ◽  
Packed Bed ◽  
Packed Bed Column

scholarly journals Modeling and Optimization of Carbon Dioxide Removal in Packed Bed Column Reactor

2020 ◽  
Vol 8 (3) ◽  
pp. 8-13
Author(s):  
K. Thirugnanasambandham
Keyword(s):  
Carbon Dioxide ◽  
Process Parameters ◽  
Flow Rate ◽  
Co2 Capture ◽  
Packed Bed ◽  
Operating Conditions ◽  
Feed Flow Rate ◽  
Statistical Design Of Experiments ◽  
Packed Bed Column ◽  
Column Reactor

Global warming due to greenhouse gases has become a serious global issue. Extensive efforts are being made to fighting this phenomenon through carbon capture as carbon dioxide (CO2) is its major contributor. This study focused on CO2 capture in packed bed column reactor using Poly-(D) glucosamine under the various process parameters such as temperature, feed flow rate and mass of the adsorbent. Statistical design of experiments was carried out in order to analysis the effect process parameters on the capacity of CO2 capture in packed bed column. The obtained results show that feed flow rate has the significant affect compared to others. The maximum of 956 mg of CO2 is captured under the following operating conditions; temperature of 40oC, feed flow rate of 30 ml/min and 0.25 g of the Poly-(D) glucosamine. The ability of Poly-(D) glucosamine to capture the CO2 in packed bed column is confirmed.

scholarly journals Modelling of heat transfer in a packed bed column

2011 ◽  
Vol 13 (4) ◽  
pp. 34-41 ◽  
Author(s):  
Paulina Pianko-Oprych
Keyword(s):  
Heat Transfer ◽  
Turbulent Flow ◽  
Mesh Size ◽  
Axial Direction ◽  
Packed Bed ◽  
Cfd Modelling ◽  
Packed Bed Column ◽  
Wall Functions ◽  
Temperature Distributions ◽  
Porous Media Model

Modelling of heat transfer in a packed bed column The CFD modelling of heat transfer in the packed bed column in the laminar and turbulent flow regimes has been presented. Three numerical grids with different densities were generated for the packed bed column. The modelling was performed with the use of the Porous Media Model for treating the flow inside a porous structure. The standard k-ε model along with the logarithmic wall functions for the turbulent flow range was used. The influence of the mesh size on the accuracy of the fluid flow was studied. Both radial and axial direction temperature distributions have been compared with the experimental data1 and the values calculated from a 2DADPF model. A good agreement between the experimental and the predicted values of the pressure drop, temperature distributions and heat transfer coefficient was obtained.

Efficient CO2 capture using NH2–MIL–101/CA composite cryogenic packed bed column

Cryogenics ◽  
2019 ◽  
Vol 101 ◽  
pp. 79-88 ◽  
Author(s):  
Muhammad Babar ◽  
Mohamad Azmi Bustam ◽  
Abulhassan Ali ◽  
Abdulhalim Shah Maulud ◽  
Umar Shafiq ◽  
...  
Keyword(s):  
Co2 Capture ◽  
Packed Bed ◽  
Packed Bed Column

scholarly journals A Comparative Study of Swarm Intelligence-Based Optimization Algorithms in WSN

2020 ◽  
Vol 8 (3) ◽  
pp. 1-7
Author(s):  
Aya Ayad Hussein ◽  
Rajaaaldeen Abd Khalid
Keyword(s):  
Process Parameters ◽  
Flow Rate ◽  
Co2 Capture ◽  
Carbon Capture ◽  
Statistical Design ◽  
Packed Bed ◽  
Operating Conditions ◽  
Feed Flow Rate ◽  
Statistical Design Of Experiments ◽  
Packed Bed Column

Global warming due to greenhouse gases has become a serious global issue. Extensive efforts are being made to fighting this phenomenon through carbon capture as carbon dioxide (CO2) is its major contributor. This study focused on CO2 capture in packed bed column reactor using Poly-(D) glucosamine under the various process parameters such as temperature, feed flow rate and mass of the adsorbent. Statistical design of experiments was carried out in order to analysis the effect process parameters on the capacity of CO2 capture in packed bed column. The obtained results show that feed flow rate has the significant affect compared to others. The maximum of 956 mg of CO2 is captured under the following operating conditions; temperature of 40oC, feed flow rate of 30 ml/min and 0.25 g of the Poly-(D) glucosamine. The ability of Poly-(D) glucosamine to capture the CO2 in packed bed column is confirmed.

Theoretical analysis of counter-current absorption of a poorly soluble gas based on the PDE-AD model

1986 ◽  
Vol 51 (6) ◽  
pp. 1222-1239 ◽  
Author(s):  
Pavel Moravec ◽  
Vladimír Staněk
Keyword(s):  
Experimental Data ◽  
Liquid Phase ◽  
Gas Phase ◽  
Transfer Functions ◽  
Packed Bed ◽  
Packed Bed Column ◽  
Interfacial Transport ◽  
Gaseous Component ◽  
Poorly Soluble ◽  
Counter Current

Expression have been derived in the paper for all four possible transfer functions between the inlet and the outlet gas and liquid steams under the counter-current absorption of a poorly soluble gas in a packed bed column. The transfer functions have been derived for the axially dispersed model with stagnant zone in the liquid phase and the axially dispersed model for the gas phase with interfacial transport of a gaseous component (PDE - AD). calculations with practical values of parameters suggest that only two of these transfer functions are applicable for experimental data evaluation.

Analysis of observability of model parameters for physical absorption of poorly soluble gases in packed beds

1982 ◽  
Vol 47 (10) ◽  
pp. 2639-2653 ◽  
Author(s):  
Pavel Moravec ◽  
Vladimír Staněk
Keyword(s):  
Transfer Functions ◽  
Plug Flow ◽  
Packed Bed ◽  
Model Parameters ◽  
Packed Bed Column ◽  
Interfacial Transport ◽  
Complex Arithmetic ◽  
Physical Absorption ◽  
Poorly Soluble ◽  
Phase Lags

Expressions have been derived for four possible transfer functions of a model of physical absorption of a poorly soluble gas in a packed bed column. The model has been based on axially dispersed flow of gas, plug flow of liquid through stagnant and dynamic regions and interfacial transport of the absorbed component. The obtained transfer functions have been transformed into the frequency domain and their amplitude ratios and phase lags have been evaluated using the complex arithmetic feature of the EC-1033 computer. Two of the derived transfer functions have been found directly applicable for processing of experimental data. Of the remaining two one is useable with the limitations to absorption on a shallow layer of packing, the other is entirely worthless for the case of poorly soluble gases.

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