|
[1] C. Ramshaw and R. Mallinson, "Mass transfer process," European patent, vol. 2568, 1979. [2] J.-L. Kang et al., "Experiment and modeling studies on absorption of CO2 by dilute ammonia in rotating packed bed," Energy Procedia, vol. 63, pp. 1308-1313, 2014. [3] T. Liu, D. Wang, W. Wang, Q. Liang, and L. Shao, "Study on the efficient production of ozone water by a rotating packed bed," Industrial & Engineering Chemistry Research, vol. 58, no. 17, pp. 7227-7232, 2019. [4] L. Agarwal, V. Pavani, D. Rao, and N. Kaistha, "Process intensification in HiGee absorption and distillation: design procedure and applications," Industrial & engineering chemistry research, vol. 49, no. 20, pp. 10046-10058, 2010. [5] G. Wang, O. Xu, Z. Xu, and J. Ji, "New HIGEE-rotating zigzag bed and its mass transfer performance," Industrial & engineering chemistry research, vol. 47, no. 22, pp. 8840-8846, 2008. [6] H.-H. Tung and R. S. MAH, "Modeling liquid mass transfer in HIGEE separation process," Chemical Engineering Communications, vol. 39, no. 1-6, pp. 147-153, 1985. [7] H.-S. Liu, C.-C. Lin, S.-C. Wu, and H.-W. Hsu, "Characteristics of a rotating packed bed," Industrial & engineering chemistry research, vol. 35, no. 10, pp. 3590-3596, 1996. [8] Y.-S. Chen and H.-S. Liu, "Absorption of VOCs in a rotating packed bed," Industrial & engineering chemistry research, vol. 41, no. 6, pp. 1583-1588, 2002. [9] C.-C. Lin, T.-Y. Wei, W.-T. Liu, and K.-P. Shen, "Removal of VOCs from gaseous streams in a high-voidage rotating packed bed," Journal of chemical engineering of Japan, vol. 37, no. 12, pp. 1471-1477, 2004. [10] Y.-S. Chen, "Correlations of mass transfer coefficients in a rotating packed bed," Industrial & engineering chemistry research, vol. 50, no. 3, pp. 1778-1785, 2011. [11] Y.-H. Chen et al., "Modeling ozone contacting process in a rotating packed bed," Industrial & engineering chemistry research, vol. 43, no. 1, pp. 228-236, 2004. [12] C. Von Sonntag and U. Von Gunten, Chemistry of ozone in water and wastewater treatment. IWA publishing, 2012. [13] G. Ciardelli and N. Ranieri, "The treatment and reuse of wastewater in the textile industry by means of ozonation and electroflocculation," Water research, vol. 35, no. 2, pp. 567-572, 2001. [14] K.-H. Ahn et al., "Ozonation of wastewater sludge for reduction and recycling," Water Science and Technology, vol. 46, no. 10, pp. 71-77, 2002. [15] S. N. Malik, P. C. Ghosh, A. N. Vaidya, and S. N. Mudliar, "Hybrid ozonation process for industrial wastewater treatment: Principles and applications: A review," Journal of Water Process Engineering, vol. 35, p. 101193, 2020. [16] J. Wang and H. Chen, "Catalytic ozonation for water and wastewater treatment: recent advances and perspective," Science of the Total Environment, vol. 704, p. 135249, 2020. [17] Y.-H. Chen et al., "Modeling ozonation process with pollutant in a rotating packed bed," Industrial & engineering chemistry research, vol. 44, no. 1, pp. 21-29, 2005. [18] D. Wang, T. Liu, L. Ma, F. Wang, and L. Shao, "Modeling and experimental studies on ozone absorption into phenolic solution in a rotating packed bed," Industrial & Engineering Chemistry Research, vol. 58, no. 17, pp. 7052-7062, 2019. [19] W. Jiao, L. Yu, Z. Feng, L. Guo, Y. Wang, and Y. Liu, "Optimization of nitrobenzene wastewater treatment with O3/H2O2 in a rotating packed bed using response surface methodology," Desalination and Water Treatment, vol. 57, no. 42, pp. 19996-20004, 2016. [20] J. Qiao, S. Luo, P. Yang, W. Jiao, and Y. Liu, "Degradation of nitrobenzene-containing wastewater by ozone/persulfate oxidation process in a rotating packed bed," Journal of the Taiwan Institute of Chemical Engineers, vol. 99, pp. 1-8, 2019. [21] Z. Zeng, H. Zou, X. Li, B. Sun, J. Chen, and L. Shao, "Ozonation of phenol with O3/Fe (II) in acidic environment in a rotating packed bed," Industrial & engineering chemistry research, vol. 51, no. 31, pp. 10509-10516, 2012. [22] L. Wang, J. Yun, H. Zhang, J. Si, X. Fang, and L. Shao, "Degradation of Bisphenol A by ozonation in rotating packed bed: Effects of operational parameters and co-existing chemicals," Chemosphere, vol. 274, p. 129769, 2021. [23] J.-L. Kang, K. Sun, D. S.-H. Wong, S.-S. Jang, and C.-S. Tan, "Modeling studies on absorption of CO2 by monoethanolamine in rotating packed bed," International Journal of Greenhouse Gas Control, vol. 25, pp. 141-150, 2014. [24] J. Hoigné and H. Bader, "Rate constants of reactions of ozone with organic and inorganic compounds in water—II: dissociating organic compounds," Water research, vol. 17, no. 2, pp. 185-194, 1983. [25] M. Deborde, S. Rabouan, J.-P. Duguet, and B. Legube, "Kinetics of aqueous ozone-induced oxidation of some endocrine disruptors," Environmental science & technology, vol. 39, no. 16, pp. 6086-6092, 2005. [26] K. Onda, H. Takeuchi, and Y. Okumoto, "Mass transfer coefficients between gas and liquid phases in packed columns," Journal of chemical engineering of Japan, vol. 1, no. 1, pp. 56-62, 1968. [27] S. Puranik and A. Vogelpohl, "Effective interfacial area in irrigated packed columns," Chemical Engineering Science, vol. 29, no. 2, pp. 501-507, 1974. [28] J. Burns, J. Jamil, and C. Ramshaw, "Process intensification: operating characteristics of rotating packed beds—determination of liquid hold-up for a high-voidage structured packing," Chemical Engineering Science, vol. 55, no. 13, pp. 2401-2415, 2000. [29] W. DeCoursey, "Enhancement factors for gas absorption with reversible reaction," Chemical Engineering Science, vol. 37, no. 10, pp. 1483-1489, 1982. [30] Y. Qin, S. Luo, S. Geng, W. Jiao, and Y. Liu, "Degradation and mineralization of aniline by O3/Fenton process enhanced using high-gravity technology," Chinese journal of chemical engineering, vol. 26, no. 7, pp. 1444-1450, 2018. [31] Z. Li., "Degradation of nitrobenzene by high-gravity intensified heterogeneous catalytic ozonation with Mn-Fe/ZSM-5 catalysts," Chemical Engineering and Processing-Process Intensification, vol. 169, p. 108642, 2021.
|