2011
DOI: 10.1016/j.compchemeng.2010.10.009
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Simulation of freezing step in vial lyophilization using finite element method

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Cited by 12 publications
(5 citation statements)
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“…This is attributed to these cells' exposure to both the upper plate's radiation and air convective effects, unlike the interior and base cells, which are solely subjected to conductive heat. Consequently, the surface temperature of the carrot is consistently higher than its core and underside, aligning with Muzzio and Dini's study [36]. When sublimation drying is performed for up to 60 min (Figure 3c), the upper and lateral cells are the first to transition into the dried state.…”
Section: Simulation Resultssupporting
confidence: 87%
“…This is attributed to these cells' exposure to both the upper plate's radiation and air convective effects, unlike the interior and base cells, which are solely subjected to conductive heat. Consequently, the surface temperature of the carrot is consistently higher than its core and underside, aligning with Muzzio and Dini's study [36]. When sublimation drying is performed for up to 60 min (Figure 3c), the upper and lateral cells are the first to transition into the dried state.…”
Section: Simulation Resultssupporting
confidence: 87%
“…Mathematically, the two-phase moving boundary problem consisting of a frozen porous matrix undergoing sublimation and the low pressure binary gas mixture was reduced to a model consisting of just a second-order differential equation with two initial conditions for the location of sublimation front. Muzzio et al [76] have successfully used the dynamic axisymmetric finite element model to simulate temperature of each point in the vial and position of liquid-solid interface, without the necessity of fitting parameters or questionable assumptions. They used the model to study final product morphology as well as the crystal size in the product format and by enhancing process understanding across scales from "miniaturized lab-scale" through pilot scale and ultimately to manufacturing scale.…”
Section: Resultsmentioning
confidence: 99%
“…In addition, primary drying duration, end point of primary drying at specific temperature, and chamber pressure are also important to determine the process characteristics. Different modeling approaches have been taken to tackle each of these problems [63,69,[71][72][73][74][75][76]. Optimizing and/or troubleshooting the drying portion of a freeze-drying process can be simplified to an exercise in coupled heat and mass transfer, since a majority of the primary drying stage can be approximated to a "pseudo steady state," the heat input from the shelves to the product exactly balances the heat removed by sublimation (i.e., the heat needed to change the temperature of the product is negligible).…”
Section: Finite Element Modeling Of Lyophilization Processmentioning
confidence: 99%
“…Other objects can also be added to the slurry to introduce a customised heat flow [40]. Furthermore, instead of designing the freezing system based on trial and error, heat transfer simulations can be used to predict the thermal gradient, hence the final orientation of the aligned pores [18,[40][41][42][43]. This accelerates the mould design for ice templating and helps to unleash its potential with more complicated thermal gradients.…”
Section: Introductionmentioning
confidence: 99%