posted on 2017-01-11, 00:00authored byJicong Li, Tsai-ta C. Lai, Bernhardt L. Trout, Allan S. Myerson
A continuous crystallization process
has potential advantages such
as lower cost and improved flexibility in pharmaceutical production
when compared to batch crystallization. In this work, multistage continuous
cooling crystallization processes for cyclosporine were developed.
The approach demonstrated that optimization of stage conditions can
be used to improve yield and purity. For a multi-impurity system such
as cyclosporine, the segregation of each impurity should be estimated
separately due to their different behaviors. The effective distribution
coefficients of the impurities were calculated and related to the
steady state mother liquor concentrations. A population balance and
mass balance model including distribution coefficients for impurities
was used to estimate maximum yields and purities that could be obtained
at various operating conditions. The results showed the limitation
in yield and purity improvement using a mixed-suspension, mixed-product
removal cascade. In addition, optimization along with economic analysis
can aid in determining operating conditions for a high yield with
acceptable equipment and operation cost.