Intensification of CO₂ Capture by Monoethanolamine Solution in a Rotating Packed Bed Reactor Equipped with High Frequency Ultrasonic Transducers

Hefzi Lotfabadi, Mahdi; Shirzadi Ahoudashti, Masoud; Abolhasani, Mahdieh

doi:10.22075/jhmtr.2023.27119.1379

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	Intensification of CO₂ Capture by Monoethanolamine Solution in a Rotating Packed Bed Reactor Equipped with High Frequency Ultrasonic Transducers
Journal of Heat and Mass Transfer Research
مقاله 3، دوره 9، شماره 2 - شماره پیاپی 18، بهمن 2022، صفحه 121-128 اصل مقاله (502.28 K)
نوع مقاله: Full Length Research Article
شناسه دیجیتال (DOI): 10.22075/jhmtr.2023.27119.1379
نویسندگان
Mahdi Hefzi Lotfabadi؛ Masoud Shirzadi Ahoudashti؛ Mahdieh Abolhasani^*
Faculty of Chemical, Petroleum and Gas Engineering, Semnan University, Semnan, Iran
تاریخ دریافت: 18 اردیبهشت 1401، تاریخ بازنگری: 18 دی 1401، تاریخ پذیرش: 19 دی 1401
چکیده
In this study, a carbon dioxide (CO₂) absorption process in a typical rotating packed bed (RPB) reactor equipped with blade packing and under a high frequency ultrasonic field has been studied. The utilized ultrasonic transducers were ultrasonic atomizer humidifiers with a frequency of 1.7 MHz. This reactor takes advantage of both controllable high gravitational force and induced effects of high frequency ultrasound, simultaneously, in a small volume. The overall volumetric gas side mass transfer coefficient (K_Ga) with and without ultrasound was investigated. The effects of different parameters such as rotational speed (400-1600 rpm), liquid flow rate (20- 120 L/h), monoethanolamine (MEA) concentration (1- 4 mol/L), gas flow rate (2500- 4000 L/h), and CO₂ concentration (1- 4 vol%) were investigated in the absence and presence of ultrasound. The obtained results showed that the removal efficiency increased with increasing gas and liquid flow rates, and rotational speed, as well as MEA concentration. With increasing CO₂ concentration, absorption efficiency decreased. The average arithmetic value of the relative volumetric gas-side mass transfer coefficient was enhanced 11.4% under the ultrasonic field. Moreover, the average CO₂ removal efficiency was enhanced from 27.4 % in the absence of ultrasound to 29.8% in the presence of ultrasound. Therefore, high frequency ultrasound can enhance CO₂ absorption, even in high efficiency equipment like RPBs.
کلیدواژه‌ها
RPB reactor؛ Blade packings؛ High frequency ultrasonic waves؛ CO2 absorption؛ Gas-side mass transfer coefficient
عنوان مقاله [English]
تشدید جذب CO2 توسط محلول مونو اتانول آمین در یک راکتور بستر پر شده چرخان مجهز به مبدل های فراصوت فرکانس بالا
چکیده [English]
در این مطالعه، فرآیند جذب دی‌اکسید کربن (CO2) در یک راکتور بستر پر شده چرخان (RPB) مجهز به پکینگ تیغه‌ای و تحت میدان فرا صوت فرکانس بالا مورد بررسی قرار گرفته است. مبدل‌های فرا صوت مورد استفاده، از نوع مرطوب کننده فراصوت با فرکانس 1/7 مگاهرتز بودند. این نوع راکتور از نیروی گرانشی بالای قابل کنترل و اثرات القایی امواج فراصوت با فرکانس بالا به طور همزمان در حجم کم بهره می برد. ضریب انتقال جرم حجمی کلی سمت گاز (KGa) با و بدون فرا صوت مورد بررسی قرار گرفت. اثر متغیرهای مختلف مانند سرعت چرخش ( rpm1600-400)، سرعت جریان مایع (L/h 20-120)، غلظت مونواتانول امین (MEA) (1-4 mol/L)، سرعت جریان گاز (L/h 2500-4000) و غلظت CO2 (4-1 درصد حجمی) در غیاب و در حضور امواج فرا صوت بررسی شد. نتایج به‌دست‌آمده نشان داد که با افزایش دبی گاز و مایع، سرعت چرخش و همچنین غلظت MEA، بازده حذف افزایش می‌یابد. با افزایش غلظت CO2، بازده جذب کاهش یافت. میانگین حسابی ضریب انتقال جرم نسبی حجمی سمت گاز در میدان فرا صوت 11/4 درصد افزایش یافت. علاوه بر این، متوسط بازده حذف CO2 از 27/4٪ در غیاب فراصوت به 29/8٪ در حضور فراصوت افزایش یافت. بنابراین، فرا صوت با فرکانس بالا می‌تواند جذب CO2 را حتی در تجهیزات با بازده بالا مانند RPB ها افزایش دهد.
کلیدواژه‌ها [English]
راکتور RPB, پکینگ تیغه‌ای, امواج فرا صوت فرکانس بالا, جذب CO2, ضریب انتقال جرم سمت گاز

مراجع
[1] Stankiewicz, A.I. and Moulijn, J.A., 2000. Process intensification: Transforming chemical engineering, Chemical Engineering Progress, 96, pp.22-34 [2] Luo, Y., Luo, J.Z., Yue, X.J., Song, Y.J., Chu, G.W., Liu, Y., Le, Y. and Chen, J.-F., 2018. Feasibility studies of micromixing and mass-transfer in an ultrasonic assisted rotating packed bed reactor. Chemical Engineering Journal, 331, pp.510–516. [3] Ramshaw, C. and Mallinson, R.H., US 4,283,255, Mass transfer process, United States Pat 1981:12. [4] Zhang, L.L., Wang, J.X., Xiang, Y., Zeng, X.F. and Chen, J.F., 2011. Absorption of carbon dioxide with ionic liquid in a rotating packed bed contactor: Mass transfer study. Industrial & Engineering Chemistry Research, 50, pp.6957–6964. [5] Liu, H.S., Lin, C.C., Wu, S.C. and Hsu, H.W., 1996. Characteristics of a rotating packed bed. Industrial & Engineering Chemistry Research, 35(10), pp.3590–3596. [6] Kelleher, T. and Fair, J.R., 1996. Distillation Studies in a High-Gravity Contactor. Industrial & Engineering Chemistry Research, 35(12), pp.4646–4655. [7] Chen, J.F., Gao, H., Zou, H.K., Chu, G.W., Zhang, L., Shao, L., Xiang, Y. and Wu, Y.-X., 2010. Cationic polymerization in rotating packed bed reactor: Experimental and modeling. AIChE Journal, 56(4), pp.1053-1062. [8] Lin, C.C. and Liu, W.T., 2003. Ozone oxidation in a rotating packed bed, Journal of Chemical Technology & Biotechnology, 78, pp.138–141. [9] Kang, F., Wang, D., Pu, Y., Zeng, X.F., Wang, J.X. and Chen, J.F., 2018. Efficient preparation of monodisperse CaCO₃ nanoparticles as overbased nanodetergents in a high-gravity rotating packed bed reactor. Powder Technology, 325, pp.405–411. [10] Neumann, K., Gladyszewski, K., Groß, K., Qammar, H., Wenzel, D., Górak, A. and Skiborowski, M., 2018. A guide on the industrial application of rotating packed beds. Chemical Engineering Research and Design, 134, pp.443–462. [11] Thiels, M., Wong, D.S.H., Yu, C.H., Kang, J.L., Jang, S.S. and Tan, C.S., 2016. Modelling and Design of Carbon Dioxide Absorption in Rotating Packed Bed and Packed Column. IFAC-PapersOnLine, 49, pp.895–900. [12] Sheng, M., Xie, C., Zeng, X., Sun, B., Zhang, L., Chu, G., Luo, Y., Chen, J.-F. and Zou, H., 2018. Intensification of CO₂ capture using aqueous diethylenetriamine (DETA) solution from simulated flue gas in a rotating packed bed. Fuel, 234, pp.1518-1527. [13] Liu, Z., Esmaeili, A., Zhang, H., Xiao, H., Yun, J. and Shao, L., 2021. Carbon dioxide absorption with aqueous amine solutions promoted by piperazine and 1-methylpiperazine in a rotating zigzag bed, Fuel, 302, 121165. [14] Borhani, T.N., Oko, E. and Wang, M., 2018. Process modelling and analysis of intensified CO₂ capture using monoethanolamine (MEA) in rotating packed bed absorber. Journal of Cleaner Production, 204, pp.1124–1142. [15] Lukin, I., Pietzka, L., Groß, K., Górak, A. and Schembecker, G., 2020. Economic evaluation of rotating packed bed use for aroma absorption from bioreactor off-gas. Chemical Engineering and Processing- Process Intensification, 154, 108011. [16] Neumann, K., Gladyszewski, K., Groß, K., Qammar, H., Wenzel, D., Górak and A., Skiborowski, M., 2018. A guide on the industrial application of rotatingpacked beds. Chemical Engineering Research and Design, 134, pp.443-462. [17] Groß, K., de Beer, M., Dohrn, S. and Skiborowski, M., 2020. Scale-Up of the Radial Packing Length in Rotating Packed Beds for Deaeration Processes. Industrial & Engineering Chemistry Research, 59(23), pp. 11042-11053. [18] Zhao, R.-H., Li, C.-P., Guo, F. and Chen, J.-F., 2007. Scale-up Preparation of Organized Mesoporous Alumina in a Rotating Packed Bed. Industrial & Engineering Chemistry Research, 46(10), pp.3317-3320. [19] Abolhasani, M., Karami, A. and Rahimi, M., 2015. Numerical Modeling and Optimization of the Enhancement of the Cooling Rate in Concentric Tubes under Ultrasound Field. Numerical Heat Transfer, Part A: Applications, 67, pp.1282–1309. [20] Dehbani, M., Rahimi, M., Abolhasani, M., Maghsoodi, A., Afshar, P.G., Dodmantipi, A.R. and Alsairafi, A.A., 2014. CFD modeling of convection heat transfer using 1.7 MHz and 24 kHz ultrasonic waves: A comparative study. Heat and Mass Transfer, 50, pp.1319–1333. [21] Abolhasani, M., Rahimi, M., Dehbani, M. and Shabanian, S.R., 2012. CFD Modeling of Low, Medium and High Frequency Ultrasound Waves Propagation Inside a Liquid Medium. The 4rd National Conference on CFD Applications in Chemical & Petroleum Industries. [22] Aghapour Aktij, S., Taghipour, A., Rahimpour, A., Mollahosseini, A. and Tiraferri, A., 2020. A critical review on ultrasonic-assisted fouling control and cleaning of fouled membranes. Ultrasonics, 108, 106228. [23] Zheng, J., Guo, Y., Zhu, L., Deng, H. and Shang, Y., 2021. Cavitation effect in two-dimensional ultrasonic rolling process. Ultrasonics, 115, 106456. [24] Viriyananon, K., Mingbunjerdsuk, J., Thungthong, T. and Chaiworapuek, W., 2021. Characterization of heat transfer and friction loss of water turbulent flow in a narrow rectangular duct under 25–40 kHz ultrasonic waves, Ultrasonics, 114, 106366. [25] Parvizian, F., Rahimi, M., Hosseini, S.M., Madaeni, S.S. and Alsairafi, A.A., 2012. The Effect of High Frequency Ultrasound on Diffusion Boundary Layer Resistance in Ion-Exchange Membrane Transport, Desalination, 286, pp.155-165. [26] Abolhasani, M., Rahimi, M., Dehbani, M. and Alsairafi, A.A., 2012. CFD Modeling of Heat Transfer by 1.7 MHz Ultrasound Waves, Numerical. Heat Transfer. part A-Application. 62, pp. 822-841. [27] Legay, M., Gondrexon, N., Le Person, S., Boldo, P. and Bontemps, A., 2011. Enhancement of heat transfer by ultrasound: Review and recent advances. International Journal of Chemical Engineering, 2011. [28] Rahimi, M., Abolhasani, M. and Azimi, N., 2015. High frequency ultrasound penetration through concentric tubes: Illustrating cooling effects and cavitation intensity. Heat and Mass Transfer, 51, pp.587-599. [29] Abolhasani, M., Rahimi, M., Dehbani, M. and Alsairafi, A.A., 2012. CFD modeling of heat transfer by 1.7 MHz ultrasound waves, Numerical Heat Transfer, Part A: Applications, 62, pp.822–841. [30] Tay, W.H., Lau, K.K. and Shariff, A.M., 2017. High performance promoter-free CO₂ absorption using potassium carbonate solution in an ultrasonic irradiation system. Journal of CO₂ Utilization, 21, pp.383–394. [31] Bahoosh, R., Sedeh Ghahfarokhi, M. and Saffarian, M.R., 2018. Energy and Exergy Analyses of a Diesel Engine Running on Biodiesel Fuel. Journal of Heat and Mass Transfer Research, 5, pp. 95-104. [32] Lee, S.Y. and Park, S.J., 2015. A review on solid adsorbents for carbon dioxide capture, Journal of Industrial and Engineering Chemistry, 23, pp.1 –11. [33] Hu, G., Smith, K.H., Wu, Y., Mumford, K.A., Kentish, S.E., and Stevens, G.W., 2018. Carbon dioxide capture by solvent absorption using amino acids: A review, Chinese Journal of Chemical Engineering, 26(11), pp. 2229–2237. [34] Cheng, H.H. and Tan, C.S., 2011. Removal of CO₂ from indoor air by alkanolamine in a rotating packed bed. Separation and Purification Technology, 82, pp.156–166. [35] Kang, J.L., Luo, Z.J., Liu, J.L., Sun, K., Wong, D.S.H., Jang, S.S., Tan, C.-S. and Shen, J.-F., 2014. Experiment and modeling studies on absorption of CO₂ by dilute ammonia in rotating packed bed. Energy Procedia, 63, pp.1308–1313. [36] Wu, T.W., Hung, Y.T., Chen, M.T. and Tan, C.S., 2017. CO₂ capture from natural gas power plants by aqueous PZ/DETA in rotating packed bed. Separation and Purification Technology, 186, pp.309–317. [37] Jassim, M.S., Rochelle, G., Eimer, D. and Ramshaw, C., 2007. Carbon dioxide absorption and desorption in aqueous monoethanolamine solutions in a rotating packed bed, Industrial & Engineering Chemistry Research, 46, pp. 2823–2833. [38] Lin, C.C. and Chu, C.R., 2015. Feasibility of carbon dioxide absorption by NaOH solution in a rotating packed bed with blade packings. International Journal of Greenhouse Gas Control, 42, pp.117–123. [39] Yu, C.H., Wu, T.W. and Tan, C.S., 2013. CO₂ capture by piperazine mixed with non-aqueous solvent diethylene glycol in a rotating packed bed, International Journal of Greenhouse Gas Control, 19, pp.503–509. [40] Lin, C.C. and Chen, Y.W., 2011. Performance of a cross-flow rotating packed bed in removing carbon dioxide from gaseous streams by chemical absorption. International Journal of Greenhouse Gas Control, 5, pp.668–675. [41] Tay, W.H., Lau, K.K. and Shariff, A.M., 2017. High frequency ultrasonic-assisted chemical absorption of CO₂ using monoethanolamine (MEA). Separation and Purification Technology, 183, pp.136–144. [42] Shirzadi Ahou Dashti, M. and Abolhasani, M., 2020. Intensification of CO₂ capture by monoethanolamine solution containing TiO₂ nanoparticles in a rotating packed bed, International Journal of Greenhouse Gas Control, 94, 102933. [43] Jassim, M.S., 2002. Process Intensification: Absorption and Desorption of Carbon Dioxide from Monoethanolamine Solutions Using Higee Technology, (PhD Thesis, Newcastle University). [44] Lin, C.C. and Chu, C.R., 2015. Mass transfer performance of rotating packed beds with blade packings in carbon dioxide absorption into sodium hydroxide solution. Separation and Purification Technology, 150, pp.196-203. [45] Mohammadi Nouroddinvand, V. and Heidari, A., 2021. Experimental study of absorption with MEA solution in a novel Arc-RPB. Chemical Engineering and Processing- Process Intensification, 165, 108450. [46] Aroonwilas, A. and Veawab, A., 2004. Characterization and comparison of the CO₂ absorption performance into single and blended alkanolamines in a packed column. Industrial & Engineering Chemistry Research, 43, 9, pp.2228–2237. [47] Lin, C.C., Liu, W.T., and Tan, C.S., 2003. Removal of carbon dioxide by absorption in a rotating packed bed. Industrial & Engineering Chemistry Research, 42, pp.2381-2386. [48] Lin, C.C. and Kuo, Y.W., 2016. Mass transfer performance of rotating packed beds with blade packings in absorption of CO₂ into MEA solution. International Journal of Heat and Mass Transfer, 97, pp.712-718.
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Intensification of CO₂ Capture by Monoethanolamine Solution in a Rotating Packed Bed Reactor Equipped with High Frequency Ultrasonic Transducers