[1] J. D. Van Hamme, A. Singh, O.P. Ward, Physiological aspects Part 1 In a series of papers devoted to surfactants in microbiology and biotechnology, Biotechnol. Adv. 24 (6) (2006) 604-620. [2] D. Gómez-Díaz, N. Gomes, J.A. Teixeira, I. Belo, Oxygen mass transfer to emulsions in a bubble column contactor, Chem. Eng. J. 152 (2009) 354-360. [3] K. Kozo, S. Yamazoe, S. Harada, Effect of surface-active substances on gas holdup and gas-liquid mass transfer in bubble column, J. Chem. Eng. Jpn 18 (4) (1985) 287-292. [4] Z. Zhao, G. Lv, Y. Zhang, S. Lian, N. Tian, Performance of EDAB-HCl acid blended system as fracturing fluids in oil fields, Chin. J. Chem. Eng. 22 (2) (2014) 202-207. [5] B. Fu, X. Yuan, B. Liu, S. Chen, H. Zhang, A. Zeng, G. Yu, Characterization of Rayleigh convection in interfacial mass transfer by Lattice Boltzmann simulation and experimental verification, Chin. J. Chem. Eng. 19 (5) (2011) 845-854. [6] E. D. Goddard, Polymer/surfactant interaction-its relevance to detergent systems, J. Am. Oil Chem. Soc. 71 (1) (1994) 1-16. [7] S. C. Lee, Continuous extraction of penicillin G by emulsion liquid membranes with optimal surfactant composition, Chem. Eng. J. 79 (1) (2000) 61-67. [8] A.A. Sonin, T. Palermo, A. Lubek, Effect of a dispersive surfactant additive on wetting and crystallisation in a system: Water-oil-metal substrate. Application to gas hydrates, Chem. Eng. J. 69 (2) (1998) 93-98. [9] J. Chern, S. Chou, C. Shang, Effects of impurities on oxygen transfer rates in diffused aeration systems, Water Res. 35 (13) (2001) 3041-3048. [10] L.R. Rodrigues, J.A. Teixeira, R. Oliveira, Low-cost fermentative medium for biosurfactant production by probiotic bacteria, Biochem. Eng. J. 32 (3) (2006) 135-142. [11] M.K. Moraveji, E.Mohsenzadeh, M.E. Fakhari, R. Davarnejad, Effects of surface active agents on hydrodynamics and mass transfer characteristics in a split-cylinder airlift bioreactor with packed bed, Chem. Eng. Res. Des. 90 (7) (2012) 899-905. [12] M.K. Moraveji,M.M. Pasand, R. Davarnejad, Y. Chisti, Effects of surfactants on hydrodynamics andmass transfer in a split-cylinder airlift reactor, Can. J. Chem. Eng. 90 (1) (2012) 93-99. [13] P. Painmanakul, K. Loubière, G. Hébrard, M. Mietton-Peuchot, M. Roustan, Effect of surfactants on liquid-side mass transfer coefficients, Chem. Eng. Sci. 60 (22) (2005) 6480-6491. [14] R. Sardeing, P. Painmanakul, G. Hebrard, Effect of surfactants on liquid-side mass transfer coefficients in gas-liquid systems: A first step to modeling, Chem. Eng. Sci. 61 (19) (2006) 6249-6260. [15] D. Gómez-Díaz, J.M. Navaza, B. Sanjurjo, Mass-transfer enhancement or reduction by surfactant presence at a gas-liquid interface, Ind. Eng. Chem. Res. 48 (2009) 2671-2677. [16] E. Álvarez, D. Gómez-Díaz, J.M. Navaza, B. Sanjurjo, Continuous removal of carbon dioxide by absorption employing a bubble column, Chem. Eng. J. 137 (2) (2008) 251-256. [17] V. Linek, M. Korda, M. Fujasova, T. Moucha, Gas-liquid mass transfer coefficient in stirred tanks interpreted through models of idealized eddy structure of turbulence in the bubble vicinity, Chem. Eng. Process. 43 (12) (2004) 1511-1517. [18] M. Asgharpour,M.R.Mehrnia, N.Mostoufi, Effect of surface contaminants on oxygen transfer in bubble column reactors, Biochem. Eng. J. 49 (3) (2010) 351-360. [19] R. Maceiras, S.S. Alves, M.Á. Cancela, E. Álvarez, Effect of bubble contamination on gas-liquid mass transfer coefficient on CO2 absorption in amine solutions, Chem. Eng. J. 137 (2) (2008) 422-427. [20] A. García-Abuín, D. Gómez-Díaz, J.M. Navaza, B. Sanjurjo, Effect of surfactant nature upon absorption in a bubble column, Chem. Eng. Sci. 65 (15) (2010) 4484-4490. [21] J. J. Jeng, J.R.Maa, Y.M. Yang, Surface effects and mass transfer in bubble column, Ind. Eng. Chem. Process. Des. Dev. 25 (1986) 974-978. [22] I. Belo, A. García-Abuín, D. Gómez-Díaz, J.M. Navaza, I. Vidal-Tato, Effect of Tween 80 on bubble size and mass transfer in a bubble contactor, Chem. Eng. Technol. 34 (11) (2011) 1790-1796. [23] M. Jamnongwong, K. Loubiere, N. Dietrich, G. Hébrard, Experimental study of oxygen diffusion coefficients in clean water containing salt, glucose or surfactant: Consequences on the liquid-side mass transfer coefficients, Chem. Eng. J. 165 (3) (2010) 758-768. [24] D. Gómez-Díaz, J.M. Navaza, B. Sanjurjo, Density, kinematic viscosity, speed of sound, and surface tension of hexyl, octyl, and decyl trimethyl ammonium bromide aqueous solutions, J. Chem. Eng. Data 52 (3) (2007) 889-891. [25] Z. Xiao, Bubble Formation and Bubble-Wall Interaction at a Submerged Orifice Ph.D. Dissertation National University of Singapore, Singapore, 2004. [26] K. Van't Riet, J. Tramper, Basic Bioreactor Design, CRC Press, 1991. [27] L.S. Fan, O. Hemminger, Z. Yu, F.Wang, Bubbles in nanofluids, Ind. Eng. Chem. Res. 46 (12) (2007) 4341-4346. [28] D. Gómez-Díaz, J.M. Navaza, B. Sanjurjo, Interfacial area evaluation in a bubble column in the presence of a surface-active substance: comparison of method, Chem. Eng. J. 144 (3) (2008) 379-385. [29] A.H.G. Cents, D.J.W. Jansen, D.W.F. Brilman, G.F. Versteeg, Influence of small amounts of additives on gas hold-up, bubble size and interfacial area, Ind. Eng. Chem. Res. 44 (2005) 4863-4870. [30] M.D.L. Rubia, A. García-Abuín, D. Gómez-Díaz, J.M. Navaza, Interfacial area andmass transfer in carbon dioxide absorption in TEA aqueous solutions in a bubble column reactor, Chem. Eng. Process. 49 (8) (2010) 852-858. [31] K. Loubiere, G. Hebrard, Influence of liquid surface tension (surfactants) on bubble formation at rigid and flexible orifices, Chem. Eng. Process. 43 (11) (2004) 1361-1369. [32] J. Vasconcelos, Effect of contaminants onmass transfer coefficients in bubble column and airlift contactors, Chem. Eng. Sci. 58 (8) (2003) 1431-1440. [33] R. Higbie, The rate of absorption of a pure gas into still liquid during short periods of exposure, Trans. Am. Inst. Chem. Eng. 31 (1935) 365-389. [34] N. Frössling, Über die Verdünstung fallender Tropfen, Gerlands Beitr. Geophys., 52, (1938) 170-216. |