Abstract

A key challenge during the transition from laboratory/small batch to continuous manufacturing is the development of a process strategy that can easily be adopted for a larger batch/continuous process. Industrial practice is to develop the isolation strategy for a new drug/process in batch using the design of experiment (DoE) approach to determine the best isolation conditions and then transfer the isolation parameters selected to a large batch equipment/continuous isolation process. This stage requires a series of extra investigations to evaluate the effect of different equipment geometry or even the adaptation of the parameters selected to a different isolation mechanism (e.g., from dead end to cross flow filtration) with a consequent increase of R&D cost and time along with an increase in material consumption. The CFD25 is an isolation device used in the first instance to develop an isolation strategy in batch (optimization mode) using a screening DoE approach and to then verify the transferability of the strategy to a semicontinuous process (production mode). A d-optimal screening DoE was used to determine the effect of varying the input slurry. Properties such as solid loading, particle size distribution, and crystallization solvent were investigated to determine their impact on the filtration and washing performance and the characteristics of the dry isolated product. A series of crystallization (ethanol, isopropanol, and 3-methylbutan-1-ol) and wash solvents (n-heptane, isopropyl acetate and n-dodcane) were used for the process. To mimic a real isolation process, paracetamol-related impurities, acetanilide and metacetamol, were dissolved in the mother liquor. The selected batch isolation strategy was used for the semicontinuous isolation run. Throughput and filtration parameters, such as cake resistance and flow rate, cake residual liquid content and composition, cake purity, particle–particle aggregation, and extent and strength of agglomerates, were measured to evaluate the consistency of the isolated product produced during a continuous experiment and compared with the isolated product properties obtained during the batch process development. Overall, the CFD25 is a versatile tool which allows both new chemical entity process development in batch and the production of the active pharmaceutical ingredient in semicontinuous mode using the same process parameters without changing equipment. The isolated product properties gained during the semicontinuous run are overall comparable between samples. The residual solvent content and composition differs between some samples due to filter plate blockage. In general, the mean properties obtained during semicontinuous running are comparable with the product properties simulated using the DoE.

Highlights

  • A key challenge facing the pharmaceutical industry is maintaining particle properties across the entire purification and isolation process

  • The samples collected during the semicontinuous run showed comparable extent of agglomeration: the mean value measured was 56.4 ± 0.14%. The strength of these agglomerates was consistent throughout the eight samples, showing the formation of hard agglomerates. These values were compared with the values predicted by the design of experiment (DoE), and the results modeled are in good agreement with the experimental data

  • The pharmaceutical industry is in the process of embracing continuous manufacturing of Active pharmaceutical ingredient (API) in order to reduce production cost, improve manufacturing flexibility, reduce infrastructure cost to improve consistency of API quality critical attributes, and to reduce manufacturing lead time and to improve sustainability by reducing waste generation

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Summary

Introduction

A key challenge facing the pharmaceutical industry is maintaining particle properties across the entire purification and isolation process. Any residual dissolved solute is deposited and tends to promote granulation, changing the product particle size distribution (PSD).[3] A washing step is invariably employed to minimize these problems.[4] The final product attributes can be affected by different process and physicochemical parameters such as the feed suspension viscosity and density, PSD, suspended particle loading,[5−10] the chemical character of impurities,[11] the interactions between solvents during washing and drying,[12−14] the point at which filtration is halted (dry land or breakthrough), the pressure driving force for both filtration and washing, etc All of these processes and material attributes can affect the isolated crystal attributes (PSD, aspect ratio, and purity), filtration rate, efficiency of washing, and propensity for filter blockage.[15−19] Equipment design affects the filtration performance. It is crucial to Received: November 29, 2019 Published: March 26, 2020

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