1991
DOI: 10.1016/0009-2509(91)85036-w
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Physical absorption into non-aqueous solutions in a stirred cell reactor

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Cited by 87 publications
(98 citation statements)
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“…The observed enhancement factors appeared to decrease with decreasing driving force. This phenomenon might be related to the phenomena reported by Littel et al (1991) for gas absorption into nonaqueous solutions in a stirred cell absorber. As yet the assumption of a thin toluene layer appears to explain most of the observed phenomena for gas absorption into toluene/water emulsions.…”
Section: Discussionsupporting
confidence: 66%
“…The observed enhancement factors appeared to decrease with decreasing driving force. This phenomenon might be related to the phenomena reported by Littel et al (1991) for gas absorption into nonaqueous solutions in a stirred cell absorber. As yet the assumption of a thin toluene layer appears to explain most of the observed phenomena for gas absorption into toluene/water emulsions.…”
Section: Discussionsupporting
confidence: 66%
“…The values of b were reported to range from 0.33 for small Sc numbers to 0.5 for large Sc numbers. The exponent of power dependence of the Sh number on Re number is found to be in the range 0.6÷0.7 [16]. The mass transfer characteristics described by Eq.…”
Section: Heterogeneous Techniquesmentioning
confidence: 89%
“…Therefore, we concluded that the CO 2 absorption process was liquid-phase-controlled. To estimate the liquid-side mass transfer coefficient k L , a procedure earlier outlined by Littel et al [31] was used. For the case of physical absorption in a stirredcell reactor, a solute mass balance for both the gas and the liquid phase yields the following expression:…”
Section: Mass Transfer Considerationsmentioning
confidence: 99%