Samenvatting
Purpose Biodegradable polymers have been widely investigated for controlled release formulations for protein delivery. However, the processing stability of proteins remains a major challenge. The aim of this research is to assess the influence of the hot melt extrusion process on the activity of a model protein by varying extrusion temperature, hydrophilicity of polymer and pre-stabilization of proteins with sugar glass technology.
Methods The thermolabile model protein alkaline phosphatase (AP) was spray dried with inulin in a 1:10 protein:inulin weight ratio. The spray dried powder and the bare protein were exposed to 55°C, 95°C and 130°C for 10, 30, 60 and 120 minutes to assess the effect of heat stress that can be expected during hot melt extrusion.
The spray dried powder and the bare protein were extruded with six different biodegradable polymers: the hydrophobic polymers poly-ε-caprolactone and low and high molecular weight poly (lactic-co-glycolic acid) at 55°C, 85°C and 130°C, respectively. Three hydrophilic polymers, based on the same polymers but with poly (ethylene glycol) incorporated, were extruded at the same temperatures. After extraction of protein from the extrudates by dissolving the polymer in an organic solvent, the activity of AP was determined using an enzymatic activity assay.
Results Exposure to heat stress showed a protective effect of inulin against activity loss for AP at 95°C and 130°C, whereas at 55°C almost no activity loss was seen for both bare AP and AP spray dried with inulin. The decrease of activity was in accordance with Arrhenius behavior.
After hot melt extrusion at 55°C, the remaining activity of AP was higher than 75% for all formulations, and showed an additional stabilizing effect of inulin on AP in the hydrophilic polymer. The stabilizing effect of inulin was more pronounced with extrusion at intermediate temperature (85°C), as in both the hydrophilic and the hydrophobic polymer the remaining activity of spray dried AP was about twice as high as the remaining activity of bare AP. The activity loss of AP after extrusion at 130°C was over 90% for all formulations. Moreover, no stabilizing effects of inulin were seen, most probably due to the extrusion temperature being close to the Tg of the spray dried AP-inulin.
Conclusions Heat stress data of proteins can not be used as a predictor for hot melt extrusion formulation development, as the protein activity loss after heat stress does not correlate with the activity loss after extrusion. This discrepancy is most likely due to the shear forces that occur during extrusion. The use of inulin as a protective agent can be beneficial at low and intermediate temperatures.
Methods The thermolabile model protein alkaline phosphatase (AP) was spray dried with inulin in a 1:10 protein:inulin weight ratio. The spray dried powder and the bare protein were exposed to 55°C, 95°C and 130°C for 10, 30, 60 and 120 minutes to assess the effect of heat stress that can be expected during hot melt extrusion.
The spray dried powder and the bare protein were extruded with six different biodegradable polymers: the hydrophobic polymers poly-ε-caprolactone and low and high molecular weight poly (lactic-co-glycolic acid) at 55°C, 85°C and 130°C, respectively. Three hydrophilic polymers, based on the same polymers but with poly (ethylene glycol) incorporated, were extruded at the same temperatures. After extraction of protein from the extrudates by dissolving the polymer in an organic solvent, the activity of AP was determined using an enzymatic activity assay.
Results Exposure to heat stress showed a protective effect of inulin against activity loss for AP at 95°C and 130°C, whereas at 55°C almost no activity loss was seen for both bare AP and AP spray dried with inulin. The decrease of activity was in accordance with Arrhenius behavior.
After hot melt extrusion at 55°C, the remaining activity of AP was higher than 75% for all formulations, and showed an additional stabilizing effect of inulin on AP in the hydrophilic polymer. The stabilizing effect of inulin was more pronounced with extrusion at intermediate temperature (85°C), as in both the hydrophilic and the hydrophobic polymer the remaining activity of spray dried AP was about twice as high as the remaining activity of bare AP. The activity loss of AP after extrusion at 130°C was over 90% for all formulations. Moreover, no stabilizing effects of inulin were seen, most probably due to the extrusion temperature being close to the Tg of the spray dried AP-inulin.
Conclusions Heat stress data of proteins can not be used as a predictor for hot melt extrusion formulation development, as the protein activity loss after heat stress does not correlate with the activity loss after extrusion. This discrepancy is most likely due to the shear forces that occur during extrusion. The use of inulin as a protective agent can be beneficial at low and intermediate temperatures.
| Originele taal-2 | English |
|---|---|
| Status | Published - 23-nov.-2015 |
| Evenement | Biopharmacy Day 2015 - Leuven, Belgium Duur: 23-nov.-2015 → 23-nov.-2015 |
Conference
| Conference | Biopharmacy Day 2015 |
|---|---|
| Land/Regio | Belgium |
| Stad | Leuven |
| Periode | 23/11/2015 → 23/11/2015 |