Kinetic Studies and Statistical Design of CO2 Capture Process from Stream of Gas Mixture at Elevated Temperature Using Composites of Nanoparticles

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Chitosan and clay materials of 50:50 ratio, produced and characterized from periwinkle shells and clay soil, was applied to capture CO2 from gas mixture at elevated temperatures (50OC to 250OC) in a column bed, packed with the particles of dimension length 1.5 (m), and inner diameter 0.02 (m). The composition of gas mixture are 0.003, 0.002, 0.05, 0.15, 0.02, and 0.76 for CH4, C2H6, H2, CO2, H2O vapour, and N2, respectively at condition of pressure 49 (kPa), temperature 250OC, and flow rate 75 (L/min) from exhaust column into the column bed for adsorption process. The kinetic and isotherm models are adopted and simulations performed from the experimental data to determine suitable adsorption parameters for the process. Also, Aspen plus and statistical optimization tool to simulate the experimental data are utilized to determine the optimal yield and conditions of factors. The coefficient of determination of 0.992 showed that the quadratic model is best suitable for the combination of parameters and fitted well, while the optimization result gave significant difference among the bed height, temperature and time and their interactions. The result revealed that the adsorption process best followed Elovich kinetic and fitted well in the Freundlich multilayer adsorption isotherm with parameters 0.0187 (mg/g.hr), 175.932, and 1.5 for the kinetic constant, adsorption constant, and intensity respectively. The root means square errors and deviation values gave negligible values of 0.166; 0.045, and 0.0345; 0.0094 for the design/simulation; optimization models applied, when compared to the experimental data. The regression results of the factors analysis showed that the model R2 of 0.995 is more reliable and fitted well than the modified R2 of 0.985 and the estimated R2 of 0.965. The central composite design for the optimization of the process gave maximum yield of 0.9411 at suitable combine time and temperature factors effect. Aspen plus simulation result gave yield of 0.9831 CO2 removed from optimal conditions of time, temperature, and bed height of 2.8 (hrs), 155.6°C, and 3.44 (cm) respectively. It was noticed that N2, CH4, C2H6, and water vapour were removed from the gas mixture of yields 0.9972, 0.9832, 0.9831, and 0.9947 respectively.

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February 2026

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[1] H.Spliethoff. Power generation from solid fuels, Springer: Berlin/ Heidelberg, Germany (2010).

Google Scholar

[2] S. Sarkar. Fuel and combustion; University Press: New Delhi, India (2009).

Google Scholar

[3] H. Yang, Z. Xu, M. Fan, R. Gupta, R. Slimane, A.E. Bland, I. Wright. Progress in carbon dioxide separation and capture: A review. Journal of Environmental Science. 20 (2008)14 – 27.

DOI: 10.1016/s1001-0742(08)60002-9

Google Scholar

[4] L. Nord, O. Bolland. Carbon dioxide emission management in power generation. Wiley-Verlag GmbH & Co: Weinheim, Germany. (2020).

Google Scholar

[5] P. Madejski. Thermal power plants, new trends and recent developments; Intech Open Limited, London, UK (2018).

Google Scholar

[6] P. Madejski, T. Janda, N. Modlinski, D.A Nabaglo. Combustion process optimization and numerical analysis for the low emission operation of pulverized coal-fired boiler. Intech Open Limited, London, UK (2016).

DOI: 10.5772/64442

Google Scholar

[7] ETP. Special report on carbon capture utilization and storage CCUS in clean energy transition, IEA, Paris, France (2020). https://iea.blob.core.windows.net/assets/7f8aed40-89af-4348-be19c8a67df0b9ea/Energy-Technology-Perspective-2020-PDF.

DOI: 10.1787/208b66f4-en

Google Scholar

[8] C. Stewart, M.A. Hessami, H.A. Mir-Akbar. A study of methods of carbon dioxide capture and sequestration, the sustainability of a photosynthetic bioreactor approach, Energy Conversion Management, 46 (2005) 403 – 420.

DOI: 10.1016/j.enconman.2004.03.009

Google Scholar

[9] H. Shijaz, Y. Attada. V.S. Patnaikuni, R. Vooradi, S.B. Anne. Analysis of integrated gasification combined cycle power plant incorporating chemical looping combustion for environment. Friendly utilization of Indian coal, Energy Conversion Management.151 (2017) 414-425.

DOI: 10.1016/j.enconman.2017.08.075

Google Scholar

[10] S. Mukherjee, P. Kumar, A. Yang, P. Fennell. Energy and exergy analysis of chemical looping combustion technology and comparison with pre-combustion and oxy-fuel combustion technologies for CO2 capture, Journal of Environment and Chemical Engineering. 3,1 (2015) 2104 – 2114.

DOI: 10.1016/j.jece.2015.07.018

Google Scholar

[11] Y. Wanga, L. Zhaoa, A. Ottoa, M. Robiniusa, D.A. Stoltena. A review of post-combustion CO2 capture technologies from coal-fired power plants, Energy Procedia. 114 (2017)650 – 665.

DOI: 10.1016/j.egypro.2017.03.1209

Google Scholar

[12] Z. Yong, V. Mata, R. Aliro. Adsorption of carbon dioxide at high temperature. A review. Separation and Purification Technologies. 26 (2002) 195 – 203.

DOI: 10.1016/s1383-5866(01)00165-4

Google Scholar

[13] B.B. Saha, S. Koyama, I.I. El-sharkawy, K. Habib, K. Srinivasan, P. Dutta. Evaluation of adsorption parameters and heat of adsorption through desorption measurements. Journal of Chemical Engineering Data. 52 (2007) 2419 – 2424.

DOI: 10.1021/je700369j

Google Scholar

[14] M. Yates, J. Blanco, P. Avila, M. Martin. Honeycomb monoliths of activated carbons for effluent gas purification. Microporous Mesoporous Materials. 37 (2000) 201 – 208.

DOI: 10.1016/s1387-1811(99)00266-8

Google Scholar

[15] O.E. Ojong, P.D. Benibo, F.I. Abam, S.S. Silas. Enhancing CO2 Adsorption from Flue Gas Mixture at Elevated Temperature using Composite of Nanoparticles. Advances in Science and Technology, Trans Tech Publication 160 (2025) 279-289.

DOI: 10.4028/p-3cwdqg

Google Scholar

[16] W. Dadet, O.E. Ojong, C.O. Wosu. Absorption and Simulation of Carbon (IV) Oxide Recovery Plant with Monoethanolamine Solvent using Aspen HYSYS. Caritas Journal of Chemical Engineering and Industrial Biotechnology. 2,1(2025) 2025.

Google Scholar

[17] W. Dadet, O.E. Ojong, K.K. Dagde. The Design and Energy Simulation of CO2 Capture Process (CCP) for a Liquefied Natural Gas (LNG) Plant. Advances in Science and Technology.  142 (2024) 181–192

DOI: 10.4028/p-fd9c5r

Google Scholar

[18] J. Zhou, S. Yang, J. Yu, Z. Shu. Novel hollow microsphere of hierarchical Zn-Al layered double hydroxides and their enhanced adsorption capacity for phosphate in H2O. Journal of Hazard Materials. 19, 2 (2011)114 – 121.

DOI: 10.1016/j.jhazmat.2011.06.013

Google Scholar

[19] T.H. Ho, T. Howes, B.R. Bhandari. Encapsulation of gases in powder solid matrices and their applications. Powder Technology. 59 (2017)87–108.

DOI: 10.1016/j.powtec.2014.03.054

Google Scholar

[20] T. Yaun, W. Xia, J. Yin, X. Zhou, W. Yang. Kinetic and thermodynamic studies on the phosphate's removal by dolomite mineral. Journal of Chemistry, 1, 2 (2015) 1 – 8.

Google Scholar

[21] N.Y. Mezenner, A. Bensmaili. Kinetics and thermodynamic study of phosphate absorption on iron hydroxide-egg shell waste. Chemical Engineering Journal. 1, 2 (2009)147: 87-98.

DOI: 10.1016/j.cej.2008.06.024

Google Scholar

[22] X. Qui. Critical review in adsorption kinetic models. Journal of Zhejiang University. 10, 1(2009) 716 – 724.

Google Scholar

[23] S. Yakout, E. Elsherif. Batch kinetic isotherm and thermodynamic studies of absorption of strontium from aqueous solutions onto low-cost rice straw-based carbons, Carbon Science and Technology. 1 (2010)144 – 153.

Google Scholar

[24] W.J. Weber, J.C. Morris. Kinetics of adsorption on carbon from solutions. Journal of the Sanitary Engineering Division. 89 (1963) 31 – 39.

Google Scholar

[25] K. Pasavant, A. Rutter, R.K. Rowe, J.S. Poland. Biosorption of hydrocarbon contaminated soils in the Canadian Arctic by land farming. Colf Register of Science and Technology. 53(2006)102 -114.

DOI: 10.1016/j.coldregions.2007.07.006

Google Scholar

[26] A.A. Ujile. Evaluating groundwater contamination process and developing framework for qualitative management in part of Nigeria. International Journal of Innovative Research in Science, Engineering and Technology. 2 ,8 (2013) 3890 – 3900.

Google Scholar

[27] A. Balouch M. Kolachi, F.N. Talpur, H. Khan, M.T. Bhanger. Sorption kinetics, isotherm and thermodynamic modelling of defluoridation of ground water using natural absorbents. American Journal of Analytical Chemistry. 4 (2013) 221 – 228.

DOI: 10.4236/ajac.2013.45028

Google Scholar

[28] A. Dada, A. Olalekan, O. Dada. Langmuir, Freundlich, Tempkin and Dubinin-Radush Kevich isotherm s studies of equilibrium sorption of Z onto phosphoric acid modified rice husk. Journal of Applied Chemistry 3 (2012)38 – 45.

DOI: 10.9790/5736-0313845

Google Scholar

[29] N. Boujelben, F. Bouhamed, Z. Eloyear, J. Bouzid, M. Feki. Removal of phosphates ions from aqueous solutions using MO2- Coated sand and brick. Desalination Water Treatment, 52 (2013) 2282 – 2292.

DOI: 10.1080/19443994.2013.822324

Google Scholar

[30] K.Y. Foo, B. Hameed. Insights into the modelling of adsorption isotherm systems. Chemical Engineering Journal. 120,156 (2010) 2 – 10.

Google Scholar

[31] M. Tempkin, N. Pyzher. Heavy metals removal and isotherms study. Acta Physiochem., URSS 12,1 (1940) 217 – 222.

Google Scholar

[32] O.E. Ojong, C.O. Wosu, A. Emenike, P. Ubi. Design and simulation of 30 000 tons per year of cumene plant from natural gas field. Pure and Applied Chemistry (2024a)

DOI: 10.1515/pac-2023-1135

Google Scholar

[33] O.E. Ojong, V.I. Etim, G.E-E. Aquah, R.I. Uzono. Design and Simulation of the Major Units of Acetone Plant from Isopropyl Alcohol (IPA) Route. Advances in Science and Technology.142 (2024b) 171–180.

DOI: 10.4028/p-nmaxr7

Google Scholar

[34] O.E. Ojong. Design of Geothermal groundwater heating and cooling plant: A trial study in Eleme Fertilizer Company in Niger Delta Region. Gamification and Augmented Reality, 3,106 (2025) 1-10.

DOI: 10.56294/gr2025106

Google Scholar