2010
DOI: 10.1002/jps.22086
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Freeze-Drying in Novel Container System: Characterization of Heat and Mass Transfer in Glass Syringes

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Cited by 23 publications
(34 citation statements)
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“…However, these results are in sharp contradiction to another report (16). In this study, glass syringes were suspended through a plexiglass holder.…”
Section: Freeze-drying In Syringescontrasting
confidence: 93%
“…However, these results are in sharp contradiction to another report (16). In this study, glass syringes were suspended through a plexiglass holder.…”
Section: Freeze-drying In Syringescontrasting
confidence: 93%
“…Contrary to the freeze‐drying in vials, the syringe heat transfer coefficient was pressure independent, and radiation was determined to be the dominant heat transfer mode for syringes suspended in the plexiglass holder. This is in sharp contradiction to the aforementioned assumption of Hottot et al29 Regarding the contributing mechanisms of heat transfer for the syringes in the aluminum block, gas conduction was prevalent, followed by direct conduction and radiation 30. Thus, the sublimation rate and the syringe heat transfer coefficient increased with increasing pressure.…”
Section: Relevant Container Systemscontrasting
confidence: 63%
“…For comparison, an approximately 15% higher sublimation rate was reported in literature for edge vials 12. With an increase of chamber pressure from 60 to 250 mTorr, the sublimation rate for syringes in the plexiglass holder decreased by about 28% as the driving force for sublimation decreased 30. Contrary to the freeze‐drying in vials, the syringe heat transfer coefficient was pressure independent, and radiation was determined to be the dominant heat transfer mode for syringes suspended in the plexiglass holder.…”
Section: Relevant Container Systemsmentioning
confidence: 73%
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“…], therefore more heat is transferred to the gelcast sample via gas conduction at a high pressure. The heat‐transfer coefficient K g via gas conduction isKnormalg=αnormalΛ0PnormalC1+lfalse(normalαΛ0false/λ0false)PnormalCwhere Λ 0 is the free molecular heat conductivity of the gas at 0°C, λ 0 the heat conductivity of the water vapor at ambient pressure, P c the chamber pressure, l the constant “effective” distance characterizing the gap between the shelf and the sample surface, and α is a term related to the energy accommodation coefficient, α c and the absolute temperature of the gas, T ,α=αC2normalαnormalC273.2T…”
Section: Resultsmentioning
confidence: 99%