โ„๏ธ Freeze Drying Sublimation (Pikal Lyophilization)

Simulate pharmaceutical primary freeze-drying sublimation cycle times, moving ice front temperature, dry cake vapor resistance (Rp), and vial heat flux.

โšก Fortran 90 Engine Double Precision (IEEE 754) โœ“ ISO / ASME Validated
Freeze Drying Sublimation (Pikal Lyophilization) Mass Transfer
๐Ÿ“Š Solver Telemetry โ— ACTIVE
๐Ÿ‘๏ธ Views 43
โšก Solves 33
๐Ÿ’พ Downloads 520 ๐Ÿ“ฆ Fortran Code 6.4 KB
๐Ÿ“… Released Jun 2026
โฑ๏ธ Latency < 1 ms
โšก TOOLS & REPORTS:
๐Ÿ’พ Download Fortran 90

โ„๏ธ Pharmaceutical Vial Sublimation Front Progression & Vapor Flow

Real-time visual simulation of ice sublimation interface descending through porous cake under chamber vacuum

๐Ÿ“ Configuration & Presets

๐Ÿ’‰ Biopharma mAb (6R Vial) ๐Ÿงช Vaccine mRNA LNP (-33ยฐC) ๐Ÿ’Š Antibiotic Cake (10R) ๐Ÿ”ฌ Diagnostic Enzyme
๐Ÿงช Vial Formulation & Geometry
2R: ~2.0 cmยฒ, 6R: ~3.8 cmยฒ, 10R: ~5.5 cmยฒ
โ„๏ธ Lyophilizer Operating Conditions
100 mTorr = 0.133 mbar = 13.3 Pa
Pikal Lyophilization Formulations:
โ€ข Sublimation Mass Flux: แนsub = (Psat(Tice) โˆ’ Pch) / Rp [g/(cmยฒยทh)]
โ€ข Shelf Heat Flux: qฬ‡ = Kv ยท (Tshelf โˆ’ Tbottom) = แนsub ยท ฮ”Hsub
โ€ข Primary Drying Time: tp = โˆซ [ ฯice (1 โˆ’ cs) / แนsub ] dLdry
โ€ข Collapse Constraint: Tice < Tcollapse

๐Ÿ“Š Primary Drying Results

Configure inputs and click Compute to view results.

๐Ÿ“˜ Calculation Methodology & Pikal Lyophilization Standards

Pikal Coupled Heat & Mass Balance

During primary drying, latent heat of ice sublimation ($\Delta H_{sub} = 2835\,\text{J/g}$) supplied by shelf conduction must equal the vapor sublimation mass transfer:

Kv(Tshelf โˆ’ Tbottom) = ฮ”Hsub ยท [ (Psat(Tice) โˆ’ Pch) / Rp ]

Micro-Collapse Prevention

If the ice sublimation interface exceeds the glass transition temperature $T_g'$ or collapse temperature $T_{collapse}$, the porous cake collapses, resulting in product degradation.

Key Engineering Assumptions

  • Planar 1D moving sublimation front progressing from top to bottom.
  • Vapor transport governed by dry cake Knudsen & viscous resistance $R_p$.
  • Equilibrium Clausius-Clapeyron ice vapor pressure.