rationalising the freeze drying of protein formulations

1
Rationalising the freeze-drying of protein formulations: Comparison of a series of pre- and post- lyophilisation properties Debra McMahon 1,2 , Duncan Craig 1 , Vicky Kett 1 & Kevin Ward 2 1 School of Pharmacy, Queen’s University Belfast, 97 Lisburn Road, Belfast, BT9 7BL, UK 2 Biopharma Technology Ltd., Winnall Valley Road, Winchester, SO23 0LD, UK INTRODUCTION Freeze-drying (lyophilisation) is a unit operation in which a solvent, usually water, is frozen and then sublimed in a vacuum. It is commonly used in the pharmaceutical industry when there are stability issues with the active ingredient in solution, as is often true for proteins 1 . In order to prevent processing defects during freeze-drying, active ingredients are formulated with excipients, which may serve specific functions, such as providing bulk properties, thermal stability and activity preservation to the product. Many groups of molecules have been shown to perform these functions, including disaccharides, amino acids, polymers and non-ionic surfactants 2 . The aim of the present study was to evaluate the pre- and post- lyophilisation properties of a large series of protein-excipient combinations and to evaluate them on the basis of retained protein activity and other qualitative and quantitative analyses. MATERIALS AND METHODS Dextran (mw 9500kDa) glucose, mannitol, sucrose and trehalose were obtained as analytical grade from Sigma. Lactate dehydrogenase (LDH, also Sigma) was obtained as an ammonium sulphate suspension and dialyzed prior to formulation. The LDH activity assay kit was based on the spectrophotometric method of Henry, et al 3 and was obtained from ThermoTrace (Australia). Dextran and mannitol were used as excipients at 2%w/v, either alone or in combination with 1%w/v glucose, sucrose or trehalose. The solutions were analyzed using MTDSC, DTA and freeze drying microscopy (details below). Aliquots (1ml) of the solutions were dispensed into freeze-drying vials, partially stoppered and freeze dried using a VirTis Genesis 12EL freeze-dryer. The solutions were frozen to -40 o C and held for 1hr. The pressure was decreased to 200mT, and shelves heated gently to 10 o C and held for 10hrs. Pressure was reduced to 100mT, and shelves lowered to -10 o C and held for 11hrs. Pressure was further reduced to 50mT and temperature increased to 20 o C and held for 15hrs. Samples of solutions were analyzed using MTDSC (TA Instruments DSC2920). Samples were cooled at 2 o C/min from 20 o C to -60 o C and reheated at the same rate. The modulation period was ±0.4 o C over 60s. Freezing resistance annalysis and DTA were carried out using a BTL Lyotherm (Biopharma Technology Ltd) Freeze-drying behaviour of the samples was observed using a freeze-drying microscope (BTL Lyostat2, Biopharma Technology Ltd., UK). Samples of solution (1-2ul) sandwiched between cover slips 75um apart were cooled to -20 o C or below, before pressure was reduced and sample temperature adjusted in order to observe eutectic melting or collapse of the sample while drying, with annealing used to encourage solute crystallisation where necessary. Freeze dried products were analyzed using MTDSC (same modulation as previously) and TGA over the range 20- 200 o C. Reconstituted samples were analyzed for retained protein activity. RESULTS Thermal events in the frozen solutions were clearly observed using MTDSC (Figure 1). These generally correlated with collapse events observed using FDM (Figures 2a & b). Dry state transitions were also yielded by MTDSC (Figure 3). A range of pre- and post- lyophilisation properties for some of the mixtures used here are shown in the Table below. The results of the protein activity assay indicated that dextran and mannitol by themselves do not protect LDH. However, including sugars had a lyoprotective effect (Figure 4) with sucrose performing the best in both cases. Figure 1 MTDSC of 2%w/v dextran solution showing Tg’ Figure 4 Effect of Inclusion of low mw saccharides to dextran and mannitol on maintained LDH activity Figure 2a & b Dextran at -11.4 o C and -9.1 o C respectively 0 10 20 30 40 50 60 70 80 90 100 dex man glu dex-glu man-glu suc dex-suc man-suc tre dex-tre man-tre Excipients % Retained Activit y CONCLUSIONS Initial results confirm expectations that while excipients with favourable thermal or bulk properties impart certain qualities to a formulation, they do not necessarily maintain protein activity. Statistical analysis and rationalisation of these and other pre- and post- lyophilisation properties for a range of formulations is currently ongoing. REFERENCES 1: MJ Pikal. BioPharm, 3(8):18-27 (1990). 2: JF Carpenter, MJ Pikal, et al. Pharm Res. 14(8):969-975 (1997). 3: RJ Henry et al Am. J.Clin.Path. 34:381- 383 (1960) -11.65°C(I) -12.02°C -10.61°C 0.0000 Nonrev Heat Flow (W/g) -0.080 -0.075 -0.070 -0.065 -0.060 Rev Heat Flow (W/g) -0.20 -0.15 -0.10 -0.05 Heat Flow (W/g) -50 -40 -30 -20 -10 0 10 20 Temperature (°C) Exo Up Universal V3.2B TA Instruments 3.98 136.05 -14.2 to -6.2 Dextran-trehalose 3.94 102.77 -16.5 to -14.5 Dextran-sucrose 2.94 103.02 -18.9 to -12.8 Dextran-glucose 4.83 112.01 -12.4 to -10.9 Dextran 1.90 99.01 -18.5 to -15.9 Mannitol-trehalose 2.5 119.42 -20.0 to -16.7 Mannitol-sucrose 2.28 82.43 -42.0 to -26.4 Mannitol-glucose 0.46 107.39 -11.2 to -9.3 Mannitol Water content % Product Tg ( o C) Collapse range ( o C) Excipients 121.92°C(I) 121.05°C 122.16°C -0.08 -0.07 -0.06 -0.05 -0.04 -0.03 -0.02 Nonrev Heat Flow (W/g) -0.08 -0.07 -0.06 Rev Heat Flow (W/g) -0.18 -0.17 -0.16 -0.15 -0.14 -0.13 -0.12 Heat Flow (W/g) 0 50 100 150 Temperature (°C) Exo Up Universal V3.2B TA Instruments Figure 3 MTDSC of freeze-dried dextran (2%w/v) showing Tg

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Rationalising the freeze drying of protein formulations: comparison of a series of pre- and post- lyophilisation properties. Debra McMahon, Duncan Craig, Vicky Kett and Kevin Ward. Queen\'s University Belfast and BTL.

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Page 1: Rationalising the Freeze Drying of Protein Formulations

Rationalising the freeze-drying of protein formulations: Comparison of a series of pre- and post- lyophilisation properties

Debra McMahon1,2, Duncan Craig1, Vicky Kett1 & Kevin Ward2

1School of Pharmacy, Queen’s University Belfast, 97 Lisburn Road, Belfast, BT9 7BL, UK2Biopharma Technology Ltd., Winnall Valley Road, Winchester, SO23 0LD, UK

INTRODUCTIONFreeze-drying (lyophilisation) is a unit operation in which a solvent, usually water, is frozen and then sublimed in a vacuum. It is commonly used in the pharmaceutical industry when there are stability issues with the active ingredient in solution, as is often true for proteins1. In order to prevent processing defects during freeze-drying, active ingredients are formulated with excipients, which may serve specific functions, such as providing bulk properties, thermal stability and activity preservation to the product. Many groups of molecules have been shown to perform these functions, including disaccharides, amino acids, polymers and non-ionic surfactants2. The aim of the present study was to evaluate the pre- and post- lyophilisation properties of a large series of protein-excipient combinations and to evaluate them on the basis of retained protein activity and other qualitative and quantitative analyses.

MATERIALS AND METHODSDextran (mw 9500kDa) glucose, mannitol, sucrose and trehalose were obtained as analytical grade from Sigma. Lactate dehydrogenase (LDH, also Sigma) was obtained as an ammonium sulphate suspension and dialyzed prior to formulation. The LDH activity assay kit was based on the spectrophotometricmethod of Henry, et al3 and was obtained from ThermoTrace (Australia). Dextran and mannitol were used as excipients at 2%w/v, either alone or in combination with 1%w/v glucose, sucrose or trehalose. The solutions were analyzed using MTDSC, DTA and freeze drying microscopy (details below).

Aliquots (1ml) of the solutions were dispensed into freeze-drying vials, partially stoppered and freeze dried using

a VirTis Genesis 12EL freeze-dryer. The solutions were frozen to -40oC and held for 1hr. The pressure was decreased to 200mT, and shelves heated gently to 10oC and held for 10hrs. Pressure was reduced to 100mT, and shelves lowered to -10oC and held for 11hrs. Pressure was further reduced to 50mT and temperature increased to 20oC and held for 15hrs.

Samples of solutions were analyzed using MTDSC (TA Instruments DSC2920). Samples were cooled at 2oC/min from 20oC to -60oC and reheated at the same rate. The modulation period was ±0.4oC over 60s. Freezing resistance annalysisand DTA were carried out using a BTLLyotherm (Biopharma Technology Ltd)

Freeze-drying behaviour of the samples was observed using a freeze-drying microscope (BTL Lyostat2, Biopharma Technology Ltd., UK). Samples of solution (1-2ul) sandwiched between cover slips 75um apart were cooled to-20oC or below, before pressure was reduced and sample temperature adjusted in order to observe eutectic melting or collapse of the sample while drying, with annealing used to encourage solute crystallisation where necessary.

Freeze dried products were analyzed using MTDSC (same modulation as previously) and TGA over the range 20-200oC. Reconstituted samples were analyzed for retained protein activity.

RESULTSThermal events in the frozen solutions were clearly observed using MTDSC (Figure 1). These generally correlated with collapse events observed using FDM (Figures 2a & b). Dry state transitions were also yielded by MTDSC (Figure 3).

A range of pre- and post- lyophilisation properties for some of the mixtures used here are shown in the Table below.

The results of the protein activity assay indicated that dextran and mannitol by themselves do not protect LDH. However, including sugars had a lyoprotectiveeffect (Figure 4) with sucrose performing the best in both cases.

Figure 1 MTDSC of 2%w/v dextran solution showing Tg’

Figure 4 Effect of Inclusion of low mw saccharides to dextran and mannitol on maintained LDH activity

Figure 2a & b Dextran at -11.4oC and -9.1oC respectively 0

102030405060708090

100

dex

man gl

u

dex-

glu

man

-glu

suc

dex-

suc

man

-suc tre

dex-

tre

man

-tre

Excipients

% R

etai

ned

Act

ivity

CONCLUSIONSInitial results confirm expectations that while excipients with favourable thermal or bulk properties impart certain qualities to a formulation, they do not necessarily maintain protein activity. Statistical analysis and rationalisation of these and other pre-and post- lyophilisation properties for a range of formulations is currently ongoing.

REFERENCES1: MJ Pikal. BioPharm, 3(8):18-27 (1990).2: JF Carpenter, MJ Pikal, et al. Pharm Res. 14(8):969-975 (1997). 3: RJ Henry et al Am. J.Clin.Path. 34:381-383 (1960)

-11.65°C(I)

-12.02°C

-10.61°C

0.0000

Non

rev

Hea

t Flo

w (W

/g)

-0 .080

-0.075

-0.070

-0.065

-0.060

Rev

Hea

t Flo

w (W

/g)

-0 .20

-0.15

-0.10

-0.05

Hea

t Flo

w (W

/g)

-50 -40 -30 -20 -10 0 10 20

Temperature (°C)Exo Up Universal V3.2B TA Instrum ents

3.98136.05-14.2 to -6.2Dextran-trehalose

3.94102.77-16.5 to -14.5Dextran-sucrose

2.94103.02-18.9 to -12.8Dextran-glucose

4.83112.01-12.4 to -10.9Dextran

1.9099.01-18.5 to -15.9Mannitol-trehalose

2.5119.42-20.0 to -16.7Mannitol-sucrose

2.2882.43-42.0 to -26.4Mannitol-glucose

0.46107.39-11.2 to -9.3 Mannitol

Water content %Product Tg (oC)

Collapse range (oC)

Excipients

121.92°C (I)

121.05°C

122.16°C

-0.08

-0.07

-0.06

-0.05

-0.04

-0.03

-0.02

Non

rev

Hea

t Flo

w (W

/g)

-0 .08

-0.07

-0.06

Rev

Hea

t Flo

w (W

/g)

-0 .18

-0.17

-0.16

-0.15

-0.14

-0.13

-0.12

Hea

t Flo

w (W

/g)

0 50 100 150

Temperature (°C)Exo Up Universal V3.2B TA Instrum ents

Figure 3 MTDSC of freeze-dried dextran (2%w/v) showing Tg