## 18.5. References 81-100

> 81

> Sutherland, W.,

> “The Viscosity of Gases and Molecular Force”,

> Phil. Mag. 5:507-531, 1893.

> 82

> Hirschfelder, J.O., Taylor, and M.H., Bird, R.B.,

> “Molecular Theory of Gases and Liquids”,

> Wiley, New York, 1954.

> 83

> Chung, T.H., Lee, L.L., and Starling, K.E.,

> “Applications of Kinetic Gas Theories and Multiparameter Correlation for Prediction of Dilute Gas Viscosity and Thermal Conductivity”,

> Ind. Eng. Chem. Fundam.

> 23:8, 1984.

> 84

> Poling, B.E., Prausnitz, J.M., and O’Connell, J.P.,

> “The Properties of Gases and Liquids”,

> McGraw-Hill, New York, 2001.

> 85

> Redlich, O., and Kwong, J.N.S.,

> "On the Thermodynamics of Solutions. V. An Equation of State. Fugacities of Gaseous Solutions.",

> Chem Rev 44:233, 1949.

> 86

> Saffman, P. G.,

> “The lift on a small sphere in a slow shear flow”,

> J. Fluid Mech., 22, p. 385, 1965.

> 87

> Mei, R. and Klausner, J. F.,

> “Shear lift force on spherical bubbles”,

> Int. J. Heat and Fluid Flow, 15, p. 62, 1994.

> 88

> Antal, S. P., Lahey, R. T., and Flaherty, J. E.,

> “Analysis of phase distribution in fully developed laminar bubbly two-phase flow”,

> Int. J. Multiphase Flow, 7, pp. 635-652, 1991.

> 89

> Krepper, E., and Prasser, H-M.,

> “Measurements and CFX Simulations of a bubbly flow in a vertical pipe”,

> in AMIFESF Workshop, Computing Methods in Two-Phase Flow, 2000.

> 90

> Burns, A.D.B., Frank, Th., Hamill, I., and Shi, J-M.,

> “The Favre Averaged Drag Model for Turbulent Dispersion in Eulerian Multi-Phase Flows”,

> 5th International Conference on Multiphase Flow, ICMF-2004, Yokohama, Japan.

> 91

> Moraga, J.F., Larreteguy, A.E., Drew, D.A., and Lahey, R.T.,

> “Assessment of turbulent dispersion models for bubbly flows in the low Stokes number limit”,

> Int. J. Multiphase Flow, 29, p. 655, 2003.

> 92

> CIBSE Guide A: Environmental Design

> CIBSE, U.K., 1999.

> 93

> ISO 7730-1984(E), Moderate thermal environments - Determination of the PMV and PPD indices and specification of the conditions for thermal comfort

> 1984.

> 94

> Yamada, T. and R.D. Gunn,

> J. Chem Eng. Data, 18, p. 234, 1973.

> 95

> Pitzer, K.S., D.Z. Lippmann, R.F. Curl, C.M. Huggins, and D.E. Petersen,

> J. Am. Chem. Soc., 77: 3433 (1955).

> 96

> Aungier, R.H.,

> “A Fast, Accurate Real Gas Equation of State for Fluid Dynamic Analysis Applications”,

> Journal of Fluids Engineering, Vol. 117, pp. 277-281, 1995.

> 97

> H. Enwald, E. Peirano and A. E. Almstedt,

> “Eulerian Two-Phase Flow Theory Applied to Fluidisation”,

> Int. J. Multiphase Flow, 22 Suppl., pp. 21-66,1996.

> 98

> J. Ding and D. Gidaspow,

> “A Bubbling Fluidisation Model using Theory of Granular Flow”,

> AIChEJ. 36, pp. 523-538, 1990.

> 99

> C.K.K. Lun, S.B. Savage, D.J. Jeffery, and N. Chepurniy,

> “Kinetic Theories for Granular Flow: Inelastic Particles in Couette Flow and Slightly Inelastic Particles in a General Flow Field”,

> J. Fluid Mech., 140, pp. 223-256, 1984.

> 100

> C.K.K. Lun, and S.B. Savage,

> “The Effects of an Impact Velocity Dependent Coefficient of Restitution on Stresses Developed by Sheared Granular Materials”,

> Acta Mechanica., 63, pp. 15-44, 1986.

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