| [1] TERASAKA K, HIRABAYASHI A, NISHINO T, et al. Development of microbubble aerator for waste water treatment using aerobic activated sludge[J]. Chemical Engineering Science, 2011, 66(14):3172-3179.
[2] DEVATINE A, CHICIUC I, POUPOT C, et al. Micro-oxygenation of wine in presence of dissolved carbon dioxide[J]. Chemical Engineering Science, 2007,62(17):4579-4588.
[3] AGO K, NAGASAWA K, TAKITA J, et al. Development of an aerobic cultivation system by using a microbubble aeration technology[J]. Journal of Chemical Engineering of Japan, 2005, 38(9):757-762.
[4] PARMAR R, MAJUMDER S K. Microbubble generation and microbubble-aided transport process intensification:a state-of-the-art report[J]. Chemical Engineering and Processing:Process Intensification, 2013, 64(2):79-97.
[5] TELMADARREIR A, DODA A, TRIVEDI J J, et al. CO2 microbubbles:a potential fluid for enhanced oil recovery:bulk and porous media studies[J]. Journal of Petroleum Science and Engineering, 2016, 138:160-173.
[6] ROVERS T A M, SALA G, VAN-DER-LINDEN E, et al. Temperature is key to yield and stability of BSA stabilized microbubbles[J]. Food Hydrocolloids, 2016, 52:106-115.
[7] ONARI H, WATANABE K, MAEDE K, et al. High functional characteristics of micro-bubbles and water purification[J]. Resources Processing, 1999, 46(4):238-244.
[8] TERASAKA K, SHINPO Y. Recovery of fine carbon particles from water using microbubble flotation[C]//6th International Conference on Multiphase Flow. Leipzig, Germany:ICMF, 2007:2-7.
[9] SADATOMI M, KAWAHARA A, KANO K, et al. Performance of a new micro-bubble generator with a spherical body in a flowing water tube[J]. Experimental Thermal and Fluid Science, 2005, 29(5):615-623.
[10] SADATOMI M, KAWAHARA A, MATSUURA H, et al. Micro-bubble generation rate and bubble dissolution rate into water by a simple multi-fluid mixer with orifice and porous tube[J]. Experimental Thermal and Fluid Science, 2012, 41(41):23-30.
[11] GABBARD C H. Development of a Venturi type bubble generator for use in the molten-salt reactor xenon removal system[R]. Danbury:U.S. Union Carbide Corporation, 1972.
[12] GORDIYCHUK A, SVANERA M, BENINI S, et al. Size distribution and Sauter mean diameter of micro bubbles for a Venturi type bubble generator[J]. Experimental Thermal and Fluid Science, 2016, 70:51-60.
[13] AKITA K, YOSHIDA F. Bubble size, interfacial area, and liquid-phase mass transfer coefficient in bubble columns[J]. Industrial and Engineering Chemistry Process Design and Development, 1974, 13(1):84-91.
[14] BORDAS M L, CARTELLIER A, SECHET P, et al. Bubbly flow through fixed beds:microscale experiments in the dilute regime and modeling[J]. AIChE Journal, 2006, 52(11):3722-3743.
[15] LI G, YANG X, DAI G. CFD simulation of effects of the configuration of gas distributors on gas-liquid flow and mixing in a bubble column[J]. Chemical Engineering Science, 2009, 64(24):5104-5116.
[16] CHYANG C S, LIEU K, HONG S S. The effect of distributor design on gas dispersion in a bubbling fluidized bed[J]. Journal of the Chinese Institute of Chemical Engineers, 2008, 39(6):685-692.
[17] BHATIA B, NIGAM K D P, AUBAN D, et al. Effect of a new high porosity packing on hydrodynamics and mass transfer in bubble columns[J]. Chemical Engineering and Processing:Process Intensification, 2004, 43(11):1371-1380.
[18] MALDONADO J G G, BASTOUL D, BAIG S, et al. Effect of solid characteristics on hydrodynamic and mass transfer in a fixed bed reactor operating in co-current gas-liquid up flow[J]. Chemical Engineering and Processing:Process Intensification, 2008, 47(8):1190-1200.
[19] JO D, REVANKAR S T. Effect of coalescence and breakup on bubble size distributions in a two-dimensional packed bed[J]. Chemical Engineering Science, 2010, 65(14):4231-4238.
[20] WANG Y C, CHEN E. Effects of phase relative motion on critical bubbly flows through a converging-diverging nozzle[J]. Physics of Fluids, 2002, 14(9):3215-3223. |
