@article{oai:kanazawa-u.repo.nii.ac.jp:00011863,
 author = {Morita, Haruki and 森田, 春樹},
 issue = {1},
 journal = {金沢大学工学部紀要 = Memoirs of the Faculty of Technology Kanazawa University},
 month = {Jun},
 note = {The mass transfer coefficients were determinded by the Coluburn-Welsh technique with the apparatus shown in Fig.1. for methyl ethyl ketone-water and normal butanol-water.
Since the transfer coefficients are dependent on the Reynolds numburs and physical properties of the two phases, the effect of the Schmidt numbers were checked by the Gordon­-Sherwood method.
As a result, it was found that the mass transfer took place approximately according to the following equation.
k₁/v₁ = 5.78X10⁻⁷(Re₁+Re₂・µ₂/µ₁)²
where k₁ : individual mass transfer coefficient, v₁：kinematic viscosity of 1 phase, Re₁, Re₂, µ₁ , µ₂ : Reynolds numbers and viscosity of both phases.},
 pages = {84--90},
 title = {液液界面における相互飽和速度について},
 volume = {3},
 year = {1962}
}