Rapid determination of vial heat transfer parameters using tunable diode laser absorption spectroscopy (TDLAS) in response to step-changes in pressure set-point during freeze-drying.

The purpose of this study was to perform a rapid determination of vial heat transfer parameters, that is, the contact parameter K(cs) and the separation distance l(v), using the sublimation rate profiles measured by tunable diode laser absorption spectroscopy (TDLAS). In this study, each size of vial was filled with pure water followed by a freeze-drying cycle using a LyoStar II dryer (FTS Systems) with step-changes of the chamber pressure set-point at to 25, 50, 100, 200, 300, and 400 mTorr. K(cs) was independently determined by nonlinear parameter estimation using the sublimation rates measured at the pressure set-point of 25 mTorr. After obtaining K(cs), the l(v) value for each vial size was determined by nonlinear parameter estimation using the pooled sublimation rate profiles obtained at 25 to 400 mTorr. The vial heat transfer coefficient K(v), as a function of the chamber pressure, was readily calculated, using the obtained K(cs) and l(v) values. It is interesting to note the significant difference in K(v) of two similar types of 10 mL Schott tubing vials, primary due to the geometry of the vial-bottom, as demonstrated by the images of the contact areas of the vial-bottom.

[1]  Lisa M Hardwick,et al.  Determination of Shelf Heat Transfer Coefficients Along the Shelf Flow Path of a Freeze Dryer Using the Shelf Fluid Temperature Perturbation Approach , 2007, Pharmaceutical development and technology.

[2]  M. Pikal,et al.  Mass and heat transfer in vial freeze-drying of pharmaceuticals: role of the vial. , 1984, Journal of pharmaceutical sciences.

[3]  H. A. Luther,et al.  Applied numerical methods , 1969 .

[4]  J. Andrieu,et al.  Determination of mass and heat transfer parameters during freeze-drying cycles of pharmaceutical products. , 2005, PDA journal of pharmaceutical science and technology.

[5]  M. Pikal,et al.  Process control in freeze drying: determination of the end point of sublimation drying by an electronic moisture sensor. , 1989, Journal of parenteral science and technology : a publication of the Parenteral Drug Association.

[6]  Y. S. Touloukian Thermophysical properties of matter , 1970 .

[7]  H. U. Akay,et al.  The Nonsteady State Modeling of Freeze Drying: In-Process Product Temperature and Moisture Content Mapping and Pharmaceutical Product Quality Applications , 2005, Pharmaceutical development and technology.

[8]  Lisa M. Hardwick,et al.  Rapid determination of dry layer mass transfer resistance for various pharmaceutical formulations during primary drying using product temperature profiles. , 2006, International journal of pharmaceutics.

[9]  M. Pikal,et al.  Physical chemistry of freeze-drying: measurement of sublimation rates for frozen aqueous solutions by a microbalance technique. , 1983, Journal of pharmaceutical sciences.

[10]  Steven J Davis,et al.  Evaluation of tunable diode laser absorption spectroscopy for in-process water vapor mass flux measurements during freeze drying. , 2007, Journal of pharmaceutical sciences.

[11]  J. Mize Optimization Techniques With Fortran , 1973 .