1937
DOI: 10.1021/ie50331a023
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Liquid film in Gas Absorption

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Cited by 28 publications
(22 citation statements)
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“…These values of S are comparable to those reported previously for cross-flow ultrafiltration and microfiltration (Koltuniewicz and Noworyta, 1994;Chatterjee, 2010;Hasan et al, 2013). Hutchinson and Sherwood (1937) studied the absorption of eight different pure gases at 25 ºC in a stirred flask containing water with the gas exposed above the stirred surface. Table 5 shows values of the mass-transfer coefficient k L , which they calculated from dissolved-gas concentration measurements, for hydrogen and oxygen at two different stirrer speeds.…”
Section: Brazilian Journal Of Chemical Engineeringsupporting
confidence: 88%
See 1 more Smart Citation
“…These values of S are comparable to those reported previously for cross-flow ultrafiltration and microfiltration (Koltuniewicz and Noworyta, 1994;Chatterjee, 2010;Hasan et al, 2013). Hutchinson and Sherwood (1937) studied the absorption of eight different pure gases at 25 ºC in a stirred flask containing water with the gas exposed above the stirred surface. Table 5 shows values of the mass-transfer coefficient k L , which they calculated from dissolved-gas concentration measurements, for hydrogen and oxygen at two different stirrer speeds.…”
Section: Brazilian Journal Of Chemical Engineeringsupporting
confidence: 88%
“…Using the theoretical equa- Danckwerts, 1970) where D i is the diffusion coefficient of the dissolved gas in the liquid, we calculated values of S that are also reported in Table 5, along with values of D i that were estimated from values of the diffusion coefficient of the dissolved gas (in water) at 20 ºC given in Table 3 in the paper of Hutchinson and Sherwood (1937) and using the Wilke-Chang correlation (Perry et al, 1984) , respectively, which indicates an increase of 659% for a change in RPM of 500%, and which also indicates that S varies with the RPM raised to a power of 1.13. The values of S derived from the absorption data of Hutchinson and Sherwood (1937) are about one to two orders of magnitude greater than those for crossflow microfiltration, as found in this work. It can be conjectured that high values of S can be obtained in a rotating-disk membrane module such as the one used by Sarkar et al (2011), which will dramatically enhance the permeate flux.…”
Section: Brazilian Journal Of Chemical Engineeringmentioning
confidence: 99%
“…Assuming for O 2 gas a transfer constant of the order of 10 À6 m/s [42], values of k w for other gases are deduced from Eq. (49).…”
Section: Where [H 2 ] Is the True Concentration In Solution (Mol/dm 3mentioning
confidence: 99%
“…Convection currents are difficult to assess quantitatively, but their significance is certainly not to be overlooked. Hutchinson and Sherwood (14) found that the absorption coefficients for oxygen in their system were 0.41 cm./hour when there was no stirring of the liquid and increased to 7.64 cm./hour when the stirring speed was increased to 1025 it. 1,.…”
Section: Absorption Of Oxygen In Liquidmentioning
confidence: 96%