TY - JOUR
T1 - Characterization of a Multistage Continuous MSMPR Crystallization Process Assisted by Image Analysis of Elongated Crystals
AU - Capellades, Gerard
AU - Joshi, Parth U.
AU - Dam-Johansen, Kim
AU - Mealy, Michael J.
AU - Christensen, Troels V.
AU - Kiil, Søren
N1 - Funding Information:
This work was financially supported by H. Lundbeck A/S and the Technical Univ. of Denmark. The authors would like to thank B. Wenzell and L. Berring for their assistance with the SEM and XRPD analysis.
Publisher Copyright:
© 2018 American Chemical Society.
PY - 2018/11/7
Y1 - 2018/11/7
N2 - This work demonstrates how quantitative image analysis can assist in the characterization of continuous crystallization processes and in the proper selection of mathematical models for the early assessment of crystal quality. An active pharmaceutical ingredient presenting an elongated crystal habit was crystallized using two stirred tank crystallizers in series. With image analysis of the crystallization magma, the sources of crystal breakage in the crystallization cascade were identified, and the impact on crystal habit was evaluated quantitatively. As it is expected for particles presenting high aspect ratios, crystal breakage preferentially occurs in the smallest plane, perpendicular to the largest dimension. This phenomenon is hardly avoidable in downstream production, but it can be accounted for with a design approach based on the real crystal dimensions. The kinetic rate equations for nucleation and crystal growth were determined based on crystal width, from which a model for the accurate prediction of this dimension was applied. The predicted crystal size distribution is consistent through a moderate degree of crystal breakage during downstream processing.
AB - This work demonstrates how quantitative image analysis can assist in the characterization of continuous crystallization processes and in the proper selection of mathematical models for the early assessment of crystal quality. An active pharmaceutical ingredient presenting an elongated crystal habit was crystallized using two stirred tank crystallizers in series. With image analysis of the crystallization magma, the sources of crystal breakage in the crystallization cascade were identified, and the impact on crystal habit was evaluated quantitatively. As it is expected for particles presenting high aspect ratios, crystal breakage preferentially occurs in the smallest plane, perpendicular to the largest dimension. This phenomenon is hardly avoidable in downstream production, but it can be accounted for with a design approach based on the real crystal dimensions. The kinetic rate equations for nucleation and crystal growth were determined based on crystal width, from which a model for the accurate prediction of this dimension was applied. The predicted crystal size distribution is consistent through a moderate degree of crystal breakage during downstream processing.
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U2 - 10.1021/acs.cgd.8b00446
DO - 10.1021/acs.cgd.8b00446
M3 - Article
AN - SCOPUS:85055495469
SN - 1528-7483
VL - 18
SP - 6455
EP - 6469
JO - Crystal Growth and Design
JF - Crystal Growth and Design
IS - 11
ER -