New Process Flowsheet for CO2 Compression and Purification Unit; Dynamic Investigation and Control

Document Type : Research Article

Authors

Department of Chemical Engineering, University of Sistan and Baluchestan, Zahedan, I.R. IRAN

Abstract

The present study provides a novel process flowsheet for CO2 compression and purification unit (CPU) in order to improve its product quality and control performance. Unlike the previous process flowsheet, the number of cold-boxes has been reduced to one, which in turn decreases investment costs and improves energy integration. The performance of the proposed flowsheet was compared with two recently suggested ones for a given feed. The results showed that, compared with the other process flowsheet, the new one not only can operate at lower operating pressure but also needs a significantly smaller heat-transfer area. Also, the dynamic behavior and controllability of the proposed process flowsheet are analyzed to ensure proper functioning. The control loops used in the new flowsheet were simpler than those used in the previous flowsheet, and controllability was achieved using proportional (P) and Proportional-Integral (PI) controllers, which offers a performance advantage over the other process flowsheet. Using step changes, the effects of disturbances in feed temperature, flow rate, and composition on the final product specifications were also investigated. The proposed flowsheet process proved to be robust against the disturbances, and the control structure was able to handle them appropriately. The proposed process flowsheet was also able to maintain purity and recovery rates of 96.74% and 90.08%, respectively, in the face of disturbance.

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[1] Modak A., Jana S., Advancement in Porous Adsorbents For Post-Combustion COCapture,  Microporous and Mesoporous Materials, 276: 107-132 (2019).
[2] Anwar M., Fayyaz A., Sohail N., Khokhar M., Baqar M., Khan W., Rasool K., Rehan M., Nizami A., CO2 Capture and Storage: A Way Forward for Sustainable Environment, Journal of Environmental Management, 226: 131-144, (2018).
[3] Koytsoumpa E. I., Bergins C., Kakaras E., The CO2 Economy: Review of CO2 Capture and Reuse Technologies, The Journal of Supercritical Fluids, 132: 3-16 (2018).
[4] Nie L., Mu Y., Jin J., Chen J., Mi J., Recent Developments and Consideration Issues in Solid Adsorbents for CO2 Capture from Flue Gas, Chinese Journal of Chemical Engineering, 26: 2303-2317 (2018).
[6] Oh S.-Y., Binns M., Cho H., Kim J.-K., Energy Minimization of MEA-based CO2 Capture Process, Applied Energy, 169: 353-362 (2016).
[7] Pérez-Fortes M., Schöneberger J.C., Boulamanti A., Tzimas E., Methanol Synthesis Using Captured CO2 as Raw Material: Techno-Economic and Environmental Assessment, Applied Energy, 161: 718-732 (2016).
[8] Romeo L. M., Bolea I., Escosa J. M., Integration of Power Plant and Amine Scrubbing to Reduce CO2 Capture Costs, Applied Thermal Engineering, 28: 1039-1046 (2008).
[9] Metz B., Davidson O., De Coninck H., Loos M., Meyer L., "Carbon Dioxide Capture and Storage", (2005).
[10] Xiang Y., Cai L., Guan Y., Liu W., Han Y., Liang Y., Study on the Integrated System of LNG oxy-Fuel Power Plant and the Application of Supercritical CO2, Energy Procedia, 158: 1863-1870 (2019).
[11] Romeo L. M., Bolea I., Lara Y., Escosa J. M., Optimization of Intercooling Compression in CO2 Capture Systems, Applied Thermal Engineering, 29: 1744-1751 (2009).
[12] De Lena E., Spinelli M., Romano M., CO2 Capture in Cement Plants by “Tail-End” Calcium Looping Process, Energy Procedia, 148: 186-193 (2018).
[13] Chansomwong A., Zanganeh K., Shafeen A., Douglas P., Croiset E., Ricardez-Sandoval L., Dynamic Modelling of a CO2 Capture and Purification Unit for an Oxy-Coal-Fired Power Plant, International Journal of Greenhouse Gas Control, 22: 111-122 (2014).
[15] Koohestanian E., Samimi A., Mohebbi-Kalhori D., Sadeghi J., Sensitivity Analysis and Multi-Objective Optimization of CO2-CPU Process Using Response Surface Methodology, Energy, 122: 570-578 (2017).
[18] B. Jin, H. Zhao, and C. Zheng, Dynamic Exergy Method and its Application for CO2 Compression and Purification Unit in Oxy-Combustion Power Plants, Chemical Engineering Science, 144: 336-345 (2016).
[19] Fu C., Gundersen T., Techno-Economic Analysis of CO2 Conditioning Processes in a Coal Based Oxy-Combustion Power Plant, International Journal of Greenhouse Gas Control, 9: 419-427 (2012). 
[20] API, "Recommended Practice 521,", vol. 521, API (1997).
[21] Martins F.G., Tuning PID Controllers Using the ITAE Criterion, International Journal of Engineering Education, 21: 867-   (2005).
[22] De Visser E., Hendriks C., de Koeijer G., Liljemark S., Barrio M., Austegard A.,. Brown A, “Dynamics CO2 Quality Recommendations”, DYNAMIS Project (6th Framework Programme), The Netherlands, pp. 16-35, 2007.
[23] Pipitone G., Bolland O., Power Generation with CO2 Capture: Technology for CO2 Purification, International Journal of Greenhouse Gas Control, 3: 528-534 (2009).
[24] Aspen Plus, Aspen Plus Documentation Version V7. 3, Aspen Tech, Cambridge, MA, USA,(2011).
[25] Koohestanian E., Sadeghi J., Mohebbi-Kalhori D., Shahraki F., Samimi A., A Novel Process for CO2 Capture from the Flue Gases to Produce Urea and Ammonia, Energy, 144: 279-285, (2018).
[26] Turton R., Bailie R.C., Whiting W.B., Shaeiwitz J.A., "Analysis, Synthesis and Design of Chemical Processes", Pearson Education, (2008).
[27] Luyben W. L., "Distillation Design and Control Using Aspen Simulation" John Wiley & Sons, Inc., (2013).
[30] Ludwig E.E., "Applied Process Design for Chemical and Petrochemical Plants", vol. 2, Gulf Professional Publishing, (1997).
[31] Carl R.B., "Rules of Thumb for Chemical Engineers," USA: Gulf Publishing Company, (1998).