[1] De Swart j.W.A., Krishna R., Effect of Article Concentration on the Hydrodynamics of Bubble Column Slurry Reactors, Chem. Eng. Res. Design., Trans. Ind. chem. Eng., 73, p. 308 (1995).
[2] Jager B., Espinoza R., Advances in Low Temperature Ficher-Tropsch Synthesis, Catalyst Today, 23(1), p. 17 (1995).
[3] Shollenberger K.A., Torczynski J.R., Adkins D.R., O’Hem T., Jakson N.B., Gamma-Densitometery Tomography of Gas Holdup Spatial Distribution in Industrial Scale Bubble Column, Chem Eng Sci., 52, p. 2037 (1997).
[4] Eishenberg B., Ansel L.L., Fiato R.A., Bauman R.F., Advanced Gas Conversion Technology for Remote Natural Gas Utilization, GPA Convention, New Orleans, LA (1994).
[5] Davis B.H., Overview of Reactor for Liquid Phase Fischer-Topsch Synthesis, Catalyst Today, 71(3-4), p. 249 (2002).
[6] Yang G.Q., Luo X., Lao R., Heat-Transfer Characteristics in Slurry Bubble Columns at Elevated Pressures and Tempratures, Ind. Eng. Chem. Res., 39, p. 2568 (2000).
[7] Rose H.E, H.B. Lloyd, On The Measurement of the Size Characteristics of Powders by Photo-Extenction Methods 1. Theoretical Consideration, J. Soc. Chem. Ind., 65, p. 5 (1946).
[8] Boll R.H., C.M. Sliepcevich., Evaluation of Error of Optical Origin Arising in the Size Analysis of Dispersion by Light Transmission, J. Opt. Soc. Am., 46, p. 200 (1956).
[9] Dobbins R.L., Jizmagian G.S., Optical Scattering Cross Sections for Polydispersions of Dielectric Sphere, AIChE J., 20, p. 184 (1974).
[10] Calderbank P.H., Physical Rate Process in Industrial Fermentation, Part 1 : The Interfacial Area in Gas-Liquid Contacting with Mechanical Agitation, Trans. Inst. Chem. Engrs., 36, p. 443 (1958).
[11] Lee J.C., Ssali, G.W.K., Bubble Transport and Coalescence in a Vertical Pipe , Joint Meeting on Bubble and Foams, S1-6.1 , Verfahrenstechnische Gesellschaft im VDI Inst., Chem. Engrs., Nurenberd (1971).
[12] Trice V.G., Rodger W.A., Light Transmittance as a Measure of Interfacial Area in Liquid-Liquid Dispersion, AIChE J., 2, p. 205 (1956).
[13] Patel S.A., Daly J.G., Bukur D.B., Bubble Size Distribution in Fischer-Tropsch Waxes in a Bubble Column, AIChE J., 36, p. 93 (1996).
[14] Akita K., Yoshida F., Gas Holdup and Volumetric Mass Transfer Coefficient in Bubble Columns. Effect of Liquid Properties, Ind. Eng. Chem. Process. Des. Dev., 12, p.76 (1974).
[15] Luewisutthichat, Tsutsumi, Zdrojkowski, Bubble Cractristics in Multi-Phase Flow Systems: Bubble Sizes and Size Distribution, J. Chem. Eng. Jpn., 30, p. 461 (1999).
[16] Kulkarni A.A., Joshi J.B., Kumar V.R., Kulkarni B.D., Simultaneous Measurement of Holdup Profiles and Interfacial Area Using LDA in Bubble Column : Predictions by Multiresolution Analysis and Comparison with Experiments, Chem. Eng. Sci., 56, p. 6437 (2001).
[17] Kiambi S.L., Duquenne A.M., Bascoul A., Delmas H., Measurements of Local Interfacial Area: Application of Bi-Optical Fiber Technique, Chem Eng Sci., 56, p. 6447 (2001).
[18] Wu Q., Ishii M., Sensitivy Study on Double-Sensor Conductivity Probe for the Measurement of Interfacial Area Concentration in Bubbly Flow, Int. J. Multi Flow, 25, p. 155 (1994).
[19] Stegman D., Knop P.A., Wijnads A.J.G., Westertern K.R. Interfacial Area and Gas Holdup in a Bubble Column Reactor at Elevated Pressure, Ind. Eng. Chem. Res., 35, p. 3842 (1996).
[20] Vazquez G., Cancela M.A., Riverol C., Alvarez E., Navaza J.M., Determination of Interfacial Areas in
a Bubble Column by Different Chemical Methods, Ind. Eng. Chem. Res., 39, p. 2541 (2000).
[21] Mie P., Ann.Pys. Lpz., 33, p. 1275 (1910).
[22] Sinclair D., "Handbook of Aerosols", Ch. 7, Washington , D.C. :Atomic Energy Commission (1950).
[23] Chiao-Min-Chu., J. phys. Chem., 59, p. 841 (1955).
[24] Sheppard P.A., The Effect of Pollution on Radiation in the Atmosphere, Intern. J. Air pollut., 1, p. 31 (1958)
[25] McLaughlin C.M., Rushton J.H., Interfacial Area of Liquid-Liquid Dispersion from Light Transmission Measurements, AIChE J., 19, p.817 (1973).
[26] Garnier C., Lance M., Marié,J., Measurement of Local Flow Characteristics in Buoyancy-Driven Bubbly Flow at High Void Fraction, Experimental Thermal and Fluid Science, 26, p. 811 (2002).