Advances in drug potency and tailored therapeutics are promoting pharmaceutical manufacturing to transition from a traditional batch paradigm to more flexible continuous processing. Here we report the development of a multistep continuous-flow CGMP (current good manufacturing practices) process that produced 24 kilograms of prexasertib monolactate monohydrate suitable for use in human clinical trials. Eight continuous unit operations were conducted to produce the target at roughly 3 kilograms per day using small continuous reactors, extractors, evaporators, crystallizers, and filters in laboratory fume hoods. Success was enabled by advances in chemistry, engineering, analytical science, process modeling, and equipment design. Substantial technical and business drivers were identified, which merited the continuous process. The continuous process afforded improved performance and safety relative to batch processes and also improved containment of a highly potent compound.
Continuous crystallization has gained interest in the pharmaceutical sector as part of the drive toward the transition from exclusive batch manufacturing to integrated continuous manufacturing in this industry. As a result, the design and operation of continuous crystallization processes for the preparation of pharmaceutical materials has been featured strongly in recent scientific literature. This review is an effort to gather together all of the published understanding on continuous crystallization with a pharmaceutical focus and to benchmark progress to date in realizing the potential benefits of transitioning this stalwart pharmaceutical unit operation from batch to continuous configurations.
Development of a
small volume continuous process that used a combination
of batch and flow unit operations to manufacture the small molecule
oncolytic candidate merestinib is described. Continuous processing
was enabled following the identification and development of suitable
chemical transformations and unit operations. Aspects of the nascent
process control strategy were evaluated in the context of a 20 kg
laboratory demonstration campaign, executed in walk-in fume hoods
at a throughput of 5–10 kg of active pharmaceutical ingredient
per day. The process comprised an automated Suzuki–Miyaura
cross-coupling reaction, a nitro-group hydrogenolysis, a continuous
amide bond formation, and a continuous deprotection. Three of the
four steps were purified using mixed-suspension, mixed-product removal
crystallizations. Process analytical technology enabled real-time
or nearly real-time process diagnostics. Findings from the demonstration
campaign informed a second process development cycle as well as decision
making for what steps to implement using continuous processing in
a proximate manufacturing campaign, which will be described in part
2 of this series.
Lilly Compound X (LCX) is an oncology drug that was tested in a phase I clinical study using starch blend capsules. The drug was given to a small patient population (4 patients) and showed large inter- and intra-patient variability. In order to evaluate the possible effect of stomach pH on exposure and ways to mitigate the variability issue, artificial stomach-duodenum (ASD) experiments were conducted to investigate the hypothesis that carefully selected dosing fluids would have an impact in minimizing exposure variability caused by the formulation, which could lead to more consistent evaluation of drug absorption in patients. The ASD data corroborates the observed variability, and was a good tool to investigate the effect of stomach pH and potential dosing solutions on duodenal concentrations. Administering capsules co-formulated with Captisol (10% drug load) along with Sprite was shown by the ASD to be an effective way to increase duodenal concentrations as well as to reduce the difference between duodenal concentrations for different gastric pH. The reduction in variability of duodenum AUC (in ASD) is expected to correlate well with a reduction of variability in patient exposure. The dosing regimen of Sprite/Captisol is therefore suggested for future clinical trials involving LCX. Furthermore, for design of early phase clinical trials, ASD technology can be used to assist in choosing the proper dosing solution to mitigate absorption and exposure variability issues.
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