TY - JOUR
T1 - Surfactant flow between a Plateau border and a film during foam fractionation
AU - Grassia, P
AU - Ubal, S
AU - Giavedoni, M D
AU - Vitasari, D
AU - Martin, P J
N1 - Export Date: 8 March 2016 CODEN: CESCA Correspondence Address: Grassia, P.; Department of Chemical and Process Engineering, University of Strathclyde, James Weir Building, 75 Montrose St, United Kingdom; email: [email protected] References: Bretherton, F.P., The motion of long bubbles in tubes (1961) J. Fluid Mech., 10, pp. 166-188; Brown, A.K., Kaul, A., Varley, J., Continuous foaming for protein recovery. Part II. Selective recovery of proteins from binary mixtures (1999) Biotechnol. Bioeng., 62, pp. 291-300; Brown, L., Narsimhan, G., Wankat, P.C., Foam fractionation of globular proteins (1990) Biotechnol. Bioeng., 36, pp. 947-959; Brunner, C.A., Lemlich, R., Foam fractionation. standard separator and refluxing columns (1963) Ind. Eng. Chem. Fundam., 2, pp. 297-300; Chang, C.-H., Franses, E.I., Adsorption dynamics of surfactants at the air/water interface: A critical review of mathematical models, data and mechanisms (1995) Colloids Surf. A, Physicochem. Eng. Asp., pp. 1-45; Durand, M., Stone, H.A., Relaxation time of the topological T1 process in a two-dimensional foam (2006) Phys. Rev. Lett., 97, p. 226101; Frankel, S.P., Mysels, K.J., On the dimpling during the approach of two interfaces (1962) J. Phys. Chem., 66 (1), pp. 190-191; Grassia, P., Cilliers, J.J., Neethling, S.J., Ventura-Medina, E., Quasi-one-dimensional foam drainage (2001) Eur. Phys. J. E, 6, pp. 325-348; Grassia, P., Homsy, G.M., Thermocapillary and buoyant flows with low frequency jitter. I. Jitter confined to the plane (1998) Phys. Fluids, 10, pp. 1273-1290; Grassia, P., Homsy, G.M., Thermocapillary and buoyant flows with low frequency jitter. II. Spanwise jitter (1998) Phys. Fluids, 10, pp. 1291-1314; Joye, J.L., Hirasaki, G.J., Miller, C.A., Dimple formation and behavior during axisymmetrical foam film drainage (1992) Langmuir, 8, pp. 3083-3092; Joye, J.L., Hirasaki, G.J., Miller, C.A., Asymmetric drainage in foam films (1994) Langmuir, 10, pp. 3174-3179; Joye, J.L., Hirasaki, G.J., Miller, C.A., Numerical simulation of instability causing asymmetric drainage in foam films (1996) J. Colloid Interface Sci., 177, pp. 542-552; Lemlich, R., Adsorptive bubble separation methods. foam fractionation and allied techniques (1968) Ind. Eng. Chem., 60, pp. 16-29; Lemlich, R., Principles of foam fractionation (1968) Progress in Separation and Purification, pp. 1-56. , Interscience, New York, E.S. Perry (Ed.); Lemlich, R., Lavi, E., Foam fractionation with reflux (1961) Science, 134 (3473), p. 191; Leonard, R.A., Lemlich, R., A study of interstitial liquid flow in foam. Part I. Theoretical model and application to foam fractionation (1965) AIChE J., 11, pp. 18-25; Martin, P.J., Dutton, H.M., Winterburn, J.B., Baker, S., Russell, A.B., Foam fractionation with reflux (2010) Chem. Eng. Sci., 65, pp. 3825-3835; Ramanan, N., Homsy, G.M., Linear-stability of a lid-driven cavity flow (1994) Phys. Fluids, 6, pp. 2690-2701; Reinelt, D.A., Kraynik, A.M., Viscous effects in the rheology of foams and concentrated emulsions (1989) J. Colloid Interface Sci., 132, pp. 491-503; Reinelt, D.A., Kraynik, A.M., On the shearing flow of foams and concentrated emulsions (1990) J. Fluid Mech., 215, pp. 431-455; Richardson, S., A stick-slip problem related to the motion of a free jet at low Reynolds number (1970) Math. Proc. Camb. Philos. Soc., 67, pp. 477-489; Schwartz, L.W., Princen, H.M., A theory of extensional viscosity for flowing foams and concentrated emulsions (1987) J. Colloid Interface Sci., 118, pp. 201-211; Scriven, L.E., Dynamics of a fluid interface. Equation of motion for Newtonian surface fluids (1960) Chem. Eng. Sci., 12, pp. 98-108; Smith, M.K., Davis, S.H., Instabilities of dynamic thermocapillary liquid layers. Part 1. Convective instabilities (1983) J. Fluid Mech., 132, pp. 119-144; Stevenson, P., Remarks on the shear viscosity of surfaces stabilised with soluble surfactants (2005) J. Colloid Interface Sci., 290, pp. 603-606; Stevenson, P., Jameson, G.J., Modelling continuous foam fractionation with reflux (2007) Chem. Eng. Process., 46, pp. 1286-1291; Vitasari, D., Adsorption and Transport of Surfactant/Protein Onto a Foam Lamella Within a Foam Fractionation Column With Reflux (Ph.D. thesis) (2014), University of ManchesterVitasari, D., Grassia, P., Martin, P., Simulation of dynamics of adsorption of mixed protein-surfactant on a bubble surface (2013) Colloids Surf. A: Physicochem. Eng. Asp., 438, pp. 63-73. , (Emilia Rosa, M., Fátima Vaz, M., Teixeira, P. (Eds.), Special Issue: A Collection of Papers Presented at the 9th EUFOAM Conference, Lisbon, Portugal, 8-11 July 2012); Vitasari, D., Grassia, P., Martin, P., Surfactant transport onto a foam lamella in the presence of surface viscous stress (2016) Appl. Math. Model., 40, pp. 1941-1958; Vitasari, D., Grassia, P., Martin, P.J., Surfactant transport onto a foam lamella (2013) Chem. Eng. Sci., 102, pp. 405-423; Weaire, D., Hutzler, S., (1999) The Physics of Foams, , Clarendon Press, Oxford
PY - 2016
Y1 - 2016
N2 - A fluid mechanics problem relevant to foam fractionation processes is analysed. Specifically the fluid flow field transporting surfactant from foam Plateau borders (fed with surfactant-rich material) towards comparatively surfactant-lean foam films is considered. The extent to which this surfactant mass transfer is limited by surface viscous effects is studied. Previous work (Vitasari et al., 2016) made assumptions about the likely flow field along the Plateau border surface. These assumptions suggested that 'high' surface viscosity (measured by a suitable dimensionless parameter) led to strong suppression of the rate of surfactant mass transfer from Plateau border to film, whereas 'low' surface viscosity did not suppress this mass transfer rate in any significant way. More detailed fluid mechanical calculations which are carried out here corroborate the aforementioned assumptions in the 'high' surface viscosity regime. However the calculations suggest that in the 'low' surface viscosity regime, in contrast to the findings from the previous assumptions, moderate reductions in the rate of surfactant mass transfer are also possible. Counterintuitively these moderate reductions in mass transfer rate potentially have more negative impact on fractionation processes than the aforementioned strong suppression. This is because they tend to arise under conditions for which the efficiency of the fractionation system is particularly sensitive to any reduction whatsoever in the surfactant mass transfer rate. © 2015 Elsevier Ltd.
AB - A fluid mechanics problem relevant to foam fractionation processes is analysed. Specifically the fluid flow field transporting surfactant from foam Plateau borders (fed with surfactant-rich material) towards comparatively surfactant-lean foam films is considered. The extent to which this surfactant mass transfer is limited by surface viscous effects is studied. Previous work (Vitasari et al., 2016) made assumptions about the likely flow field along the Plateau border surface. These assumptions suggested that 'high' surface viscosity (measured by a suitable dimensionless parameter) led to strong suppression of the rate of surfactant mass transfer from Plateau border to film, whereas 'low' surface viscosity did not suppress this mass transfer rate in any significant way. More detailed fluid mechanical calculations which are carried out here corroborate the aforementioned assumptions in the 'high' surface viscosity regime. However the calculations suggest that in the 'low' surface viscosity regime, in contrast to the findings from the previous assumptions, moderate reductions in the rate of surfactant mass transfer are also possible. Counterintuitively these moderate reductions in mass transfer rate potentially have more negative impact on fractionation processes than the aforementioned strong suppression. This is because they tend to arise under conditions for which the efficiency of the fractionation system is particularly sensitive to any reduction whatsoever in the surfactant mass transfer rate. © 2015 Elsevier Ltd.
KW - Bubble
KW - Computational fluid dynamics
KW - Films
KW - Interfacial rheology
KW - Mathematical modelling
KW - Surfactant
U2 - 10.1016/j.ces.2015.12.011
DO - 10.1016/j.ces.2015.12.011
M3 - Article
SN - 1873-4405
VL - 143
SP - 139
EP - 165
JO - Chemical Engineering Science
JF - Chemical Engineering Science
ER -