Ullmann's Encyclopedia of Industrial Chemistry 2017
DOI: 10.1002/14356007.h12_h01.pub2
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Freeze-Drying

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Cited by 6 publications
(8 citation statements)
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“…More generally, in terms of formulation for freeze-drying, though guided by general principles ( Kharaghani et al, 2017 ), consideration must be given on a case-by-case basis to the influence of individual components on the thermal properties and final freeze-dried appearance of any given formulation. This again underlines the value of thermal analytical methods in predicting successful freeze-drying outcomes and other new analytical techniques are being introduced ( Thomik et al, 2022 ), and their use will help avoid expensive and time-consuming unacceptable freeze-drying runs in the development of lyophilization processes.…”
Section: Discussionmentioning
confidence: 99%
“…More generally, in terms of formulation for freeze-drying, though guided by general principles ( Kharaghani et al, 2017 ), consideration must be given on a case-by-case basis to the influence of individual components on the thermal properties and final freeze-dried appearance of any given formulation. This again underlines the value of thermal analytical methods in predicting successful freeze-drying outcomes and other new analytical techniques are being introduced ( Thomik et al, 2022 ), and their use will help avoid expensive and time-consuming unacceptable freeze-drying runs in the development of lyophilization processes.…”
Section: Discussionmentioning
confidence: 99%
“…For comparison, in [ 37 ], a value of K [m 2 /s] = 1.349 × 10 −4 (ε/τ) d (µm) was given, assuming pressure independence of the transport coefficient and solely slip flow, which yields a value of K = 1.15 × 10 −4 assuming τ = 1. This value is almost one order of magnitude larger than our values, which could be explained by the dominance of viscous flow in our model.…”
Section: Resultsmentioning
confidence: 99%
“…The drying rates of both cases are plotted together with heat- and mass-transfer-limited freeze drying from [ 37 ] in Figure 17 . As already expected from the discussions related to Figure 16 , the monomodal PN has a higher drying rate.…”
Section: Resultsmentioning
confidence: 99%
“…Finding linear decreases in saturation in all samples was surprising. In most cases, a nonlinear time dependency of the ice saturation was reported in the literature [ 4 , 40 ], clearly resulting from the receding of the sublimation front into the bulk material. Only a few studies document a linear trend similar to that observed in our experiments; however, in these examples, the temperature was continuously increased during the process [ 41 , 42 ] or heat was additionally supplied by microwaves [ 11 ].…”
Section: Resultsmentioning
confidence: 99%
“…The limitation of transport kinetics generally results in long drying times and an increase in an already high energy consumption. In addition, freeze-drying, or lyophilization, is conducted at low temperatures and pressure, which further impairs drying kinetics [ 1 , 2 , 3 , 4 ] and increases energy consumption. Increasing the temperature in the freeze-dryer accelerates the process [ 5 ]; however, it also increases the risk of structural damage to the material [ 6 , 7 ].…”
Section: Introductionmentioning
confidence: 99%