[1] G.J. ten Brink, I. Arends, R.A. Sheldon, Green, catalytic oxidation of alcohols in water, Science 287(5458) (2000) 1636-1639. [2] A. Funakawa, I. Yamanaka, S. Takenaka, K. Otsuka, Selectivity control of carbonylation of methanol to dimethyl oxalate and dimethyl carbonate over gold anode by electrochemical potential, J. Am. Chem. Soc. 126(17) (2004) 5346-5347. [3] J.-i. Yoshida, K. Kataoka, R. Horcajada, A. Nagaki, Modern strategies in electroorganic synthesis, Chem. Rev. 108(7) (2008) 2265-2299. [4] Y. Yang, J. Li, H. Wang, X. Song, T. Wang, B. He, X. Liang, H.H. Ngo, An electrocatalytic membrane reactor with self-cleaning function for industrial wastewater treatment, Angew. Chem. Int. Ed. 50(9) (2011) 2148-2150. [5] Y. Yang, H. Wang, J. Li, B. He, T. Wang, S. Liao, Novel functionalized nano-TiO2 loading electrocatalytic membrane for oily wastewater treatment, Environ. Sci. Technol. 46(12) (2012) 6815-6821. [6] H. Wang, H. Wang, J. Li, D. Bin, Z. Yin, J. Kang, B. He, An electrocatalytic reactor for the high selectivity production of sodium 2,2,3,3-tetrafluoropropionate from 2,2,3,3-tetrafluoro-1-propanol, Electrochim. Acta 123(2014) 33-41. [7] D. Bin, H. Wang, J. Li, H. Wang, Z. Yin, J. Kang, B. He, Z. Li, Controllable oxidation of glucose to gluconic acid and glucaric acid using an electrocatalytic reactor, Electrochim. Acta 130(2014) 170-178. [8] Y. Zhang, K. Wei, W. Han, X. Sun, J. Li, J. Shen, L. Wang, Improved electrochemical oxidation of tricyclazole from aqueous solution by enhancing mass transfer in a tubular porous electrode electrocatalytic reactor, Electrochim. Acta 189(2016) 1-8. [9] M.H. Schnoor, C.D. Vecitis, Quantitative examination of aqueous ferrocyanide oxidation in a carbon nanotube electrochemical filter:Effects of flow rate, ionic strength, and cathode material, J. Phys. Chem. C 117(6) (2013) 2855-2867. [10] T. Carroll, N.A. Booker, Axial features in the fouling of hollow-fibre membranes, J. Membr. Sci. 168(1-2) (2000) 203-212. [11] X. Li, J. Li, J. Wang, H. Wang, B. He, H. Zhang, W. Guo, H.H. Ngo, Experimental investigation of local flux distribution and fouling behavior in double-end and dead-end submerged hollow fiber membrane modules, J. Membr. Sci. 453(2014) 18-26. [12] P. Talebizadeh, H. Rahimzadeh, M. Babaie, S. Javadi Anaghizi, H. Ghomi, G. Ahmadi, R. Brown, Evaluation of residence time on nitrogen oxides removal in non-thermal plasma reactor, PLoS One 10(10) (2015), e0140897. [13] S.F. Benjamin, Z. Liu, C.A. Roberts, Automotive catalyst design for uniform conversion efficiency, Appl. Math. Model. 28(6) (2004) 559-572. [14] M.W.D. Brannock, H. De Wever, Y. Wang, G. Leslie, Computational fluid dynamics simulations of MBRs:Inside submerged versus outside submerged membranes, Desalination 236(1-3) (2009) 244-251. [15] G. Wu, T. Song, CFD simulation of the effect of upstream flow distribution on the light-off performance of a catalytic converter, Energy Convers. Manag. 46(13-14) (2005) 2010-2031. [16] R. Abejón, C.L. Gijiu, M.P. Belleville, D. Paolucci-Jeanjean, J. Sanchez-Marcano, Simulation and analysis of the performance of tubular enzymatic membrane reactors under different configurations, kinetics and mass transport conditions, J. Membr. Sci. 473(2015) 189-200. [17] FLUENT, Fluent 6 user's guide, FLUENT, Lebanon, USA, 2005. [18] C.-C. Tseng, C.-J. Li, Numerical investigation of the inertial loss coefficient and the porous media model for the flow through the perforated sieve tray, Chem. Eng. Res. Des. 106(2016) 126-140. [19] M. Musto, N. Bianco, G. Rotondo, F. Toscano, G. Pezzella, A simplified methodology to simulate a heat exchanger in an aircraft's oil cooler by means of a porous media model, Appl. Therm. Eng. 94(2016) 836-845. [20] K.S. Kshetrimayum, I. Jung, J. Na, S. Park, Y. Lee, S. Park, C.-J. Lee, C. Han, Cfd simulation of microchannel reactor block for Fischer-Tropsch synthesis:Effect of coolant type and wall boiling condition on reactor temperature, Ind. Eng. Chem. Res. 55(3) (2016) 543-554. [21] W. Sheng, S. Wang, Distribution optimization for plate-fin catalytic combustion heat exchanger, Chem. Eng. J. 131(1) (2007) 171-179. [22] X. Wang, F. Thauvin, K.K. Mohanty, Non-Darcy flow through anisotropic porous media, Chem. Eng. Sci. 54(12) (1999) 1859-1869. [23] J.I. Yoshida, H. Kim, A. Nagaki, Green and sustainable chemical synthesis using flow microreactors, ChemSusChem 4(3) (2011) 331-340. [24] L. Hanguo, C. Zhanfeng, Optimization of operating conditions for glucose oxidation in an enzymatic membrane bioreactor, J. Membr. Sci. 302(1-2) (2007) 180-187. [25] J. Liu, Z. Cui, Optimization of operating conditions for glucose oxidation in an enzymatic membrane bioreactor, J. Membr. Sci. 302(s 1-2) (2007) 180-187. [26] E. Emmanuel, G. Keck, J.-M. Blanchard, P. Vermande, Y. Perrodin, Toxicological effects of disinfections using sodium hypochlorite on aquatic organisms and its contribution to AOX formation in hospital wastewater, Environ. Int. 30(7) (2004) 891-900. [27] F. Karimi, S.N. Ashrafizadeh, F. Mohammadi, Process parameter impacts on adiponitrile current efficiency and cell voltage of an electromembrane reactor using emulsion-type catholyte, Chem. Eng. J. 183(2012) 402-407. [28] M. Ramstedt, A.V. Shchukarev, S. Sjöberg, Characterization of hydrous manganite (γ-MnOOh) surfaces-An XPS study, Surf. Interface Anal. 34(1) (2002) 632-636. [29] H. Liu, C.D. Vecitis, Reactive transport mechanism for organic oxidation during electrochemical filtration:Mass-transfer, physical adsorption, and electrontransfer, J. Phys. Chem. C 116(1) (2012) 374-383. [30] A. Singh, L. Spiccia, Water oxidation catalysts based on abundant 1st row transition metals, Coord. Chem. Rev. 257(17-18) (2013) 2607-2622. [31] S. Chang, A.G. Fane, The effect of fibre diameter on filtration and flux distribution-Relevance to submerged hollow fibre modules, J. Membr. Sci. 184(2) (2001) 221-231. [32] X. Li, J. Li, H. Wang, X. Huang, B. He, Y. Yao, J. Wang, H. Zhang, H.H. Ngo, W. Guo, A filtration model for prediction of local flux distribution and optimization of submerged hollow fiber membrane module, AICHE J. 61(12) (2015) 4377-4386. |