DROP-SIZE DISTRIBUTIONS PRODUCED BY TURBULENT PIPE FLOW OF IMMISCIBLE LIQUIDS

[1] ADLER CR, 1954, CHEM ENG PROG, V50, P14

[2] CLAY PH, 1940, KON NED AKAD WET, V43, P979

[3] CLAY PH, 1940, KON NED AKAD WET, V43, P852

[4] COLLINS SB, 1967, THESIS OREGON STATE

[5] FUNDAMENTALS OF THE HYDRODYNAMIC MECHANISM OF SPLITTING IN DISPERSION PROCESSES [J]. AICHE JOURNAL, 1955, 1 (03) : 289 - 295

[6] KINTNER RC, 1961, CAN J CHEM ENG, V39, P235

[7] KOLMOGOROV AN, 1949, AKAD NAUK USSR DOKL, V66, P825

[8] DROPLET SIZE DISTRIBUTION IN SPRAYS [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1951, 43 (06): : 1317 - 1324

[9] MAXIMUM STABLE DROP SIZE IN TURBULENT FLOW - EFFECT OF PIPE DIAMETER [J]. CHEMICAL ENGINEERING SCIENCE, 1965, 20 (01) : 57 - &

[10] PARTICLE MOTIONS IN SHEARED SUSPENSIONS .12. DEFORMATION AND BURST OF FLUID DROPS IN SHEAR AND HYPERBOLIC FLOW [J]. JOURNAL OF COLLOID SCIENCE, 1961, 16 (03): : 238 - &

[1] ADLER CR, 1954, CHEM ENG PROG, V50, P14

[2] CLAY PH, 1940, KON NED AKAD WET, V43, P979

[3] CLAY PH, 1940, KON NED AKAD WET, V43, P852

[4] COLLINS SB, 1967, THESIS OREGON STATE

[5] FUNDAMENTALS OF THE HYDRODYNAMIC MECHANISM OF SPLITTING IN DISPERSION PROCESSES [J]. AICHE JOURNAL, 1955, 1 (03) : 289 - 295

[6] KINTNER RC, 1961, CAN J CHEM ENG, V39, P235

[7] KOLMOGOROV AN, 1949, AKAD NAUK USSR DOKL, V66, P825

[8] DROPLET SIZE DISTRIBUTION IN SPRAYS [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1951, 43 (06): : 1317 - 1324

[9] MAXIMUM STABLE DROP SIZE IN TURBULENT FLOW - EFFECT OF PIPE DIAMETER [J]. CHEMICAL ENGINEERING SCIENCE, 1965, 20 (01) : 57 - &

[10] PARTICLE MOTIONS IN SHEARED SUSPENSIONS .12. DEFORMATION AND BURST OF FLUID DROPS IN SHEAR AND HYPERBOLIC FLOW [J]. JOURNAL OF COLLOID SCIENCE, 1961, 16 (03): : 238 - &