Spray Drying Case Studies

Particle Size Distribution Comparison

 

Spray Drying
Equipment

Case Study #1
Compound A

Case Study #2
Kollidon 17 PF

Case Study #3
Kollidon VA64

Case Study #4
Dexolve-7TM

Buchi-290 12.6 µm 5.0 µm 5.9 µm 8.11 µm
CritiTech SD30
(cGMP Phase I & II)
9.6 µm 3.9 µm 5.0 µm 6.87 µm (Methanol)
6.89 µm (Water)

 

  • Distribution spread is calculated by subtracting the Dv10 from the Dv90.
  • In every case, the CritiTech SD30 produced similar particles to the Buchi-290 but with a narrower distribution.

 

Production Rate Increase

 

Compound A

Solvent

Feed Concentration

Feed Rate

Production Rate Increase

Buchi B-290 Dichloromethane 2 % 5 ml/min

9.5x

CritiTech SD30 47.5 ml/min

 


 

Kollidon® VA64

Solvent

Feed Concentration

Feed Rate

Production Rate Increase

Buchi B-290 Methanol 10 % 8.2 ml/min

5.5x

CritiTech SD30 45 ml/min

 


 

Dexolve– 7

Solvent

Feed Concentration

Feed Rate

Production Rate Increase

Buchi B-290 Methanol 2.7 % 14 ml/min

3.2x

CritiTech SD30 45 ml/min

 


 

Kollidon® 17 PF

Solvent

Feed Concentration

Feed Rate

Production Rate Increase

Buchi B-290 Acetone 4 % 16 ml/min

1.9x

CritiTech SD30 30 ml/min

 

Notes
1.Production runs were designed to reproduce material not to maximize the production rate.
2.Another product has been processed with the SD30 in dichloromethane at a feed rate of 135 ml/min or 10.8 kg/hr.

Spray Drying Scale-Up Case Study #1 – Compound A

 

Raw
CritiTech SD30
  • Customer’s target product profile was D50 <10 μm and as close to 5 μm as possible.
  • Feasibility testing conducted using the Buchi B-290.
  • Scale-up testing and manufacturing conducted on the CritiTech SD30.
  • D50 of 4.49 to 12.2 μm were produced.

 

Compound A – SD30 Scale-up runs

Dv10 3.32 5.15 0.759 0.848 0.821 0.645
Dv50 8.61 12.2 4.99 4.94 5.05 4.49
Dv90 23.5 24.4 36 11.1 12.3 10.2

 

 

The larger capacity SD30 (cGMP Manufacturing Unit) produced spray-dried material consistent with the material produced on the Buchi B-290, at a production rate of 9.5x.

 

Buchi B-290

(POC Unit)

CritiTech SD30

(cGMP Phase I & II Unit)

D10 (µm) 4.20 0.65
D50 (µm) 9.30 4.49
D90 (µm) 16.80 10.20

 

 

XRPD

Comparison of Buchi-290 and CritiTech SD30

 

All materials are amorphous.

 

Production Yield Comparison

Spray Drying Equipment

Number of Runs

Average Yield

Buchi-290 11 73%
CritiTech SD30 12 70%

 

70% production yield on the SD30 was observed for “Compound A.”  Yield would likely have been higher if a larger mean particle size was requested by the customer.  Nevertheless, the SD30’s yield was very similar to yields observed on the Buchi-290, but with smaller and more narrow particle size distribution.

As with any spray drying equipment, the production yield can vary substantially depending on the target product profile and processing parameters.

Spray Drying Case Study #2 – Kollidon® 17 PF

 

Raw Material
CritiTech SD30

Kollidon® 17 PF

PVP-based solubilizer for parenteral and oral formulations1

Hydrophilic crystallization inhibitor

1. “Kollidon 17 PF.” Excipients for Drug Formulation, BASF, pharmaceutical.basf.com/en/Drug-Formulation/Kollidon-17-PF.html.

 

Buchi B-290 (POC Unit)

CritiTech SD30 (cGMP Phase I & II Unit)

D10 (µm) 0.779 0.777
D50 (µm) 2.53 2.17
D90 (µm) 5.73 4.65

 

 

Spray Drying Case Study #3 – Kollidon® VA 64

 

Raw Material
CritiTech SD30

 

Kollidon® VA 64

PVP-based excipient used in granulation as a dry binder and as a film-forming agent in tablet coatings and topical sprays

 

Buchi B-290 (POC Unit)

CritiTech SD30 (cGMP Phase I & II Unit)

D10 (µm) 0.342 0.426
D50 (µm) 2.94 2.13
D90 (µm) 6.20 5.46

 

 

 

Spray Drying Case Study #4 – Dexolve™

 

Raw Material
CritiTech Spray Dried Material

Dexolve-7TM

Sulfobutyl Ether β-Cyclodextrin Sodium (SBECD) excipient for enhanced bioavailability and improved pharmaceutical formulations.

 

Buchi B-290
Methanol

CritiTech SD30
Methanol

CritiTech SD30
Water

D10 (µm) 1.43 1.77 1.21
D50 (µm) 4.57 4.28 3.49
D90 (µm) 9.54 8.64 8.10

 


 

 

System

Solvent

Concentration

Feed Rate

Production Rate

Rate Increase

Buchi B-290 Methanol 2.7 % 14 ml/min 0.378 g/min NA
CritiTech SD30 Methanol 2.7 % 45 ml/min 1.215 g/min

3.2x

CritiTech SD30 Water 15.32 % 31.5 ml/min 4.826 g/min

12.8x

 

The DexolveTM particle size distribution produced on the Buchi B-290 was was reproduced using the SD30 at a 3.2x production rate increase with the methanol system and 12.8x increase in the water system. Higher production rate increases is expected with further process optimization.