The flow sheet must represent the complete process in detail taking care of all process equipment. ASPEN HYSYS simulation software was used to simulate the process, the models of the process was simulated using MATLAB. The concentration of the atmospheric CO 2 was found to having been increasing steadily and has risen up to 35% since the Industrial Revolution. This rate, at which the concentration of CO 2 is increasing, it is unlikely to slow down if no steps are taken in this regard. This research focuses on the design of CO 2 absorption design, which covers the distillation design of a washer (to remove more acidic acid) (such as SO 2 and CO 2 ). This design focus on the unit component required in the CO 2 capture and storage, this equipment includes absorption of CO 2 into MEA and a stripper for the distillation process in order to separate the CO 2 from other component, whereas the mini component design is heating exchanger, coolers, heaters, compressor and cromps. The design concepts as well as the model of the different components is well described in the article of conceptual design and model approach of an amine based on CO 2 capture. If the concept projected in this research is adopted their tendency that the rate of CO 2 emission will be under control and the environment will be saved for mankind and the vegetation.

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1. Ukpaka, C. P., Ikenyiri, P. N., & Adebayo, T. A. (2007). Mathematical modeling of cooling rate of dehydrate lime from four areas in Niger Delta. Journal of Research in Engineering, 4(3), 76-80.

2. Ukpaka, C. P. (2007). Pyrolysis kinetics of polyethylene waste in batch reactors. Journal of Modeling, Simulation and Control (AMSE, 68(1), 18-20.

3. Amadi, S. A., Ukpaka, C. P., & Fakrogha, J. J. (2007). Investigating the kinetics of heterogeneous polymerization of 2,6-dimethylphenol. Journal of Modeling, Simulation and Control (AMSE, 68(4), 34-50.

4. Ukpaka, C. P., Eno, Okon, & Farrow, T. S. (2010). Modeling the effect of physical parameters: Euler and Stanton number on the temperature fields and velocity of gas distribution on a steam heater tube. A Multidisciplinary Environmental, Agricultural Science & Technology, 1(1), 1-18.

5. Ukpaka, C. P., Ogbonnaya, E. A., & Suberu, O. Y. (2010). Studying the cooling water system in Nigeria liquefied natural gas. The Nigerian Academic Forum: A Multidisciplinary Journal, 19(4), 22-34.

6. Crooks, J. E., & Donnellan, J. P. (1989). Kinetics and mechanism of the reaction between carbon dioxide and amines in aqueous solution. Journal of the Chemical Society-Perkin Transactions, 2(4), 331-333.

7. Davison, J., Bressan, L., & Domenichini, R. (2004). Carbon dioxide capture in coal-based IGCC power plants. Seventh International Conference on Greenhouse Gas Control Technologies, Vancouver, Canada, 84.

8. Diao, Y. F., Zheng, X. Y., He, B. S., Chen, C. H., & Xu, X. C. (2004). Experimental study on capturing CO₂ greenhouse gas by ammonia scrubbing. Energy Conversion and Management, 45, 2283-2296.

9. Geankoplis, C. J. (2003). Transport Processes and Separation Process Principles (4th ed.). Upper Saddle River, NJ: Prentice Hall, 686.

10. Kanniche, M., Gros-Bonnivard, R., Jaud, P., Valle-Marcos, J., Amann, J. M., & Bouallou, C. (2010). Pre-combustion, post-combustion, and oxy-combustion in thermal power plants for CO₂ capture. Applied Thermal Engineering, 30, 53–62.

11. Khaisri, S., DeMontigny, D., Tontiwachwuthikul, P., & Jiraratananon, R. (2011). CO₂ stripping from monoethanolamine using a membrane contactor. Journal of Membrane Science, 376, 110–118.

12. Reddy, S., Scherffius, J., Freguia, S., & Fluor, R. C. (2003). Econamine™ FG PlusSM technology: An enhanced amine-based CO₂ capture process. Second National Conference on Carbon Sequestration, Alexandria, VA, 118.

13. Richardson, J. F., & Harker, J. H. (2002). Coulson and Richardson’s Chemical Engineering: Particle Technology and Separation Processes (5th ed.). Oxford, U.K.: Butterworth-Heinemann, 371.

14. Singh, D., Croiset, E., Douglas, P. L., & Douglas, M. A. (2003). Techno-economic study of CO₂ capture from an existing coal-fired power plant: MEA scrubbing vs. O₂/CO₂ recycle combustion. Energy Conversion and Management, 44, 3073-3091.

The flow sheet must represent the complete process in detail taking care of all process equipment. ASPEN HYSYS simulation software was used to simulate the process, the models of the process was simulated using MATLAB. The concentration of the atmospheric CO 2 was found to having been increasing steadily and has risen up to 35% since the Industrial Revolution. This rate, at which the concentration of CO 2 is increasing, it is unlikely to slow down if no steps are taken in this regard. This research focuses on the design of CO 2 absorption design, which covers the distillation design of a washer (to remove more acidic acid) (such as SO 2 and CO 2 ). This design focus on the unit component required in the CO 2 capture and storage, this equipment includes absorption of CO 2 into MEA and a stripper for the distillation process in order to separate the CO 2 from other component, whereas the mini component design is heating exchanger, coolers, heaters, compressor and cromps. The design concepts as well as the model of the different components is well described in the article of conceptual design and model approach of an amine based on CO 2 capture. If the concept projected in this research is adopted their tendency that the rate of CO 2 emission will be under control and the environment will be saved for mankind and the vegetation.

🔒 This is a subscription article

Full text is available to subscribers and institutional members. Please choose an option below to access it.

1. Ukpaka, C. P., Ikenyiri, P. N., & Adebayo, T. A. (2007). Mathematical modeling of cooling rate of dehydrate lime from four areas in Niger Delta. Journal of Research in Engineering, 4(3), 76-80.

2. Ukpaka, C. P. (2007). Pyrolysis kinetics of polyethylene waste in batch reactors. Journal of Modeling, Simulation and Control (AMSE, 68(1), 18-20.

3. Amadi, S. A., Ukpaka, C. P., & Fakrogha, J. J. (2007). Investigating the kinetics of heterogeneous polymerization of 2,6-dimethylphenol. Journal of Modeling, Simulation and Control (AMSE, 68(4), 34-50.

4. Ukpaka, C. P., Eno, Okon, & Farrow, T. S. (2010). Modeling the effect of physical parameters: Euler and Stanton number on the temperature fields and velocity of gas distribution on a steam heater tube. A Multidisciplinary Environmental, Agricultural Science & Technology, 1(1), 1-18.

5. Ukpaka, C. P., Ogbonnaya, E. A., & Suberu, O. Y. (2010). Studying the cooling water system in Nigeria liquefied natural gas. The Nigerian Academic Forum: A Multidisciplinary Journal, 19(4), 22-34.

6. Crooks, J. E., & Donnellan, J. P. (1989). Kinetics and mechanism of the reaction between carbon dioxide and amines in aqueous solution. Journal of the Chemical Society-Perkin Transactions, 2(4), 331-333.

7. Davison, J., Bressan, L., & Domenichini, R. (2004). Carbon dioxide capture in coal-based IGCC power plants. Seventh International Conference on Greenhouse Gas Control Technologies, Vancouver, Canada, 84.

8. Diao, Y. F., Zheng, X. Y., He, B. S., Chen, C. H., & Xu, X. C. (2004). Experimental study on capturing CO₂ greenhouse gas by ammonia scrubbing. Energy Conversion and Management, 45, 2283-2296.

9. Geankoplis, C. J. (2003). Transport Processes and Separation Process Principles (4th ed.). Upper Saddle River, NJ: Prentice Hall, 686.

10. Kanniche, M., Gros-Bonnivard, R., Jaud, P., Valle-Marcos, J., Amann, J. M., & Bouallou, C. (2010). Pre-combustion, post-combustion, and oxy-combustion in thermal power plants for CO₂ capture. Applied Thermal Engineering, 30, 53–62.

11. Khaisri, S., DeMontigny, D., Tontiwachwuthikul, P., & Jiraratananon, R. (2011). CO₂ stripping from monoethanolamine using a membrane contactor. Journal of Membrane Science, 376, 110–118.

12. Reddy, S., Scherffius, J., Freguia, S., & Fluor, R. C. (2003). Econamine™ FG PlusSM technology: An enhanced amine-based CO₂ capture process. Second National Conference on Carbon Sequestration, Alexandria, VA, 118.

13. Richardson, J. F., & Harker, J. H. (2002). Coulson and Richardson’s Chemical Engineering: Particle Technology and Separation Processes (5th ed.). Oxford, U.K.: Butterworth-Heinemann, 371.

14. Singh, D., Croiset, E., Douglas, P. L., & Douglas, M. A. (2003). Techno-economic study of CO₂ capture from an existing coal-fired power plant: MEA scrubbing vs. O₂/CO₂ recycle combustion. Energy Conversion and Management, 44, 3073-3091.