Abstract

Anti-solvent crystallization is frequently applied in pharmaceutical processes for the separation and purification of intermediate compounds and active ingredients. The selection of optimal solvent types is important to improve the economic performance and sustainability of the process, but is challenged by the discrete nature and large number of possible solvent combinations and the inherent relations between solvent selection and optimal process design. A computational framework is presented for the simultaneous solvent selection and optimization for a continuous process involving crystallization and distillation for recycling of the anti-solvent. The method is based on the perturbed-chain statistical associated fluid theory (PC-SAFT) equation of state to predict relevant thermodynamic properties of mixtures within the process. Alternative process configurations were represented by a superstructure. Due to the high nonlinearity of the thermodynamic models and rigorous models for distillation, the resulting mixed-integer nonlinear programming (MINLP) problem is difficult to solve by state-of-the-art solvers. Therefore, a continuous mapping method was adopted to relax the integer variables related to solvent selection, which makes the scale of the problem formulation independent of the number of solvents under consideration. Furthermore, a genetic algorithm was used to optimize the integer variables related to the superstructure. The hybrid stochastic and deterministic optimization framework converts the original MINLP problem into a nonlinear programming (NLP) problem, which is computationally more tractable. The successful application of the proposed method was demonstrated by a case study on the continuous anti-solvent crystallization of paracetamol.

Highlights

  • Solution crystallization involves the formation of a crystalline solid state from a solution; it is frequently used as a separation and purification technology in pharmaceutical industry

  • A hybrid stochastic-deterministic optimization framework was developed for the simultaneous solvent selection and process optimization of a continuous anti-solvent crystallization process with solvent recycling through multi-stage distillation

  • The perturbed-chain statistical associated fluid theory (PC-SAFT) model was applied for the prediction of various thermodynamic and caloric properties for phase equilibria and energy balance calculations

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Summary

Introduction

Solution crystallization involves the formation of a crystalline solid state from a solution; it is frequently used as a separation and purification technology in pharmaceutical industry. Anti-solvent crystallization is an established method of pharmaceutical crystallization [1]. A miscible anti-solvent is mixed with a feed stream containing a solute dissolved in a solvent. If the anti-solvent is selected appropriately, a solvent mixture is created with low solubility for the solute, which provokes crystallization despite the dilution effect from mixing. Solvents are a main source of waste in pharmaceutical processes. Anti-solvent crystallization generally produces more solvent waste compared to other crystallization methods such as cooling or evaporative crystallization unless the anti-solvent can be separated and recycled

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