1969
DOI: 10.1002/jps.2600581107
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Two-Phase Method for the Investigation of Interphase Transport II: Experimental Aspects

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1969
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Cited by 9 publications
(3 citation statements)
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“…The applicability of equation 2 was tested by linear regression and found valid as shown below:P. B. McNulQ and M . Karelno SAA: l / K w = lo4 (0.253 $-2.8S/Kp) r = 0.998 + SAA: l/Kw = lo4 (0.329 + 2.91/Kp) r = 12, we estimated the stagnant layer thicknesses, Axo and Axw, for nhexanol transfer as follows :(13) Axo = .Do/ko = 0.0473 x 10-Axw = ow/k, = 0.805 X 10-5/3.04 X lop4 = 265 pm These values are within the ranges of 83-340 pm reported byHoward et al (1969) for the aqueous film thicknesses in their stirred cell studies. Comparison of experimental and predicted K , for mass transfer of n-alcohols from Wesson oil to water at 24°C.…”
supporting
confidence: 64%
“…The applicability of equation 2 was tested by linear regression and found valid as shown below:P. B. McNulQ and M . Karelno SAA: l / K w = lo4 (0.253 $-2.8S/Kp) r = 0.998 + SAA: l/Kw = lo4 (0.329 + 2.91/Kp) r = 12, we estimated the stagnant layer thicknesses, Axo and Axw, for nhexanol transfer as follows :(13) Axo = .Do/ko = 0.0473 x 10-Axw = ow/k, = 0.805 X 10-5/3.04 X lop4 = 265 pm These values are within the ranges of 83-340 pm reported byHoward et al (1969) for the aqueous film thicknesses in their stirred cell studies. Comparison of experimental and predicted K , for mass transfer of n-alcohols from Wesson oil to water at 24°C.…”
supporting
confidence: 64%
“…The findings of this study have been correlated with the previous research in these laboratories and demonstrate when an oil-water interfacial barrier is rate determining (5-7) and when bulk matrix diffusional factors are dominant (1)(2)(3). These investigations (1-4) have considered, for example, the simultaneous multiphase interactions involving pH and the buffer decane were dispersed.…”
supporting
confidence: 81%
“…Limited work has been reported on theoretical models and experimental explorations of the interfacial transfer of the drug across a liquid-liquid (L-L) interface. [15][16][17][18][19][20][21] In order to understand the transfer kinetics occurring at the L-L interface, it is necessary to develop a mathematical description which accurately depicts the interfacial processes. The resulting model needs to be sufficiently detailed based on first principles and free of empirical parameters so that the physical properties, kinetics, and operating conditions which affect the interfacial process can be correctly identified and quantified.…”
Section: Introductionmentioning
confidence: 99%