1985
DOI: 10.1002/jhrc.1240080109
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Liquid butane as a solvent for static coating of capillary columns

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1985
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Cited by 7 publications
(2 citation statements)
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“…Limitation by mass transfer will become more significant with decreasing column diameter, lower evaporation temperatures, and longer columns. Assuming the solvent vapor behaves ideally and obeys the Poiseuille law, and after converting from the mass flow of the solvent vapor to the speed of the meniscus, a formula for the mass transfer limited coating speed "u" has been derived by Xu and Vermeulen [15,16] 'Experimental data from [18]. For the calculations, a coating temperature of 22°C is used (room temperature in [ls]); SE-33 stationary phase.…”
Section: Resultsmentioning
confidence: 99%
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“…Limitation by mass transfer will become more significant with decreasing column diameter, lower evaporation temperatures, and longer columns. Assuming the solvent vapor behaves ideally and obeys the Poiseuille law, and after converting from the mass flow of the solvent vapor to the speed of the meniscus, a formula for the mass transfer limited coating speed "u" has been derived by Xu and Vermeulen [15,16] 'Experimental data from [18]. For the calculations, a coating temperature of 22°C is used (room temperature in [ls]); SE-33 stationary phase.…”
Section: Resultsmentioning
confidence: 99%
“…This independence of coating velocity on stationary phase concentration is somewhat surprising, since for normal or wide bore columns, large differences in evaporation time are observed between thin and thick film columns. Wiimman et al [18], for example, measured coating times for different thin and thick film 50 and 230 pm i.d. columns using butane and pentane as solvent and SE-33 as stationary phase.…”
Section: Resultsmentioning
confidence: 99%