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Liquid antisolvent crystallization of pharmaceutical compounds: current status and future perspectives. Drug Deliv Transl Res 2023; 13:400-418. [PMID: 35953765 DOI: 10.1007/s13346-022-01219-1] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [Key Words] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Accepted: 07/30/2022] [Indexed: 12/30/2022]
Abstract
The present work reviews the liquid antisolvent crystallization (LASC) to prepare the nanoparticle of pharmaceutical compounds to enhance their solubility, dissolution rate, and bioavailability. The application of ultrasound and additives is discussed to prepare the particles with narrow size distribution. The use of ionic liquid as an alternative to conventional organic solvent is presented. Herbal compounds, also known for low aqueous solubility and limited clinical application, have been crystalized by LASC and discussed here. The particle characteristics such as particle size and particle size distribution are interpreted in terms of supersaturation, nucleation, and growth phenomena. To overcome the disadvantage of batch crystallization, the scientific literature on continuous flow reactors is also reviewed. LASC in a microfluidic device is emerging as a promising technique. The different design of the microfluidic device and their application in LASC are discussed. The combination of the LASC technique with traditional techniques such as high-pressure homogenization and spray drying is presented. A comparison of product characteristics prepared by LASC and the supercritical CO2 antisolvent method is discussed to show that LASC is an attractive and inexpensive alternative for nanoparticle preparation. One of the major strengths of this paper is a discussion on less-explored applications of LASC in pharmaceutical research to attract the attention of future researchers.
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2
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Mendis NP, Wang J, Lakerveld R. A Workflow for Crystallization Process Design with Simultaneous Process Optimization and Solvent Selection based on the Perturbed‐Chain Statistical Associating Fluid Theory. CHEM-ING-TECH 2023. [DOI: 10.1002/cite.202200123] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 01/18/2023]
Affiliation(s)
- Nethrue Pramuditha Mendis
- The Hong Kong University of Science and Technology Department of Chemical and Biological Engineering Clear Water Bay Hong Kong China
| | - Jiayuan Wang
- Zhejiang University of Technology School of Chemical Engineering 310014 Hang Zhou China
| | - Richard Lakerveld
- The Hong Kong University of Science and Technology Department of Chemical and Biological Engineering Clear Water Bay Hong Kong China
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3
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Mendis NP, Wang J, Lakerveld R. Simultaneous Solvent Selection and Process Design for Continuous Reaction–Extraction–Crystallization Systems. Ind Eng Chem Res 2022. [DOI: 10.1021/acs.iecr.1c05012] [Citation(s) in RCA: 3] [Impact Index Per Article: 1.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/30/2022]
Affiliation(s)
- Nethrue Pramuditha Mendis
- Department of Chemical and Biological Engineering, The Hong Kong University of Science and Technology, Clear Water Bay, Hong Kong, China
| | - Jiayuan Wang
- School of Chemical Engineering, Zhejiang University of Technology, Hangzhou 310014, China
| | - Richard Lakerveld
- Department of Chemical and Biological Engineering, The Hong Kong University of Science and Technology, Clear Water Bay, Hong Kong, China
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4
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Yousefi Seyf J, Asgari M. Parametrization of PC-SAFT EoS for Solvents Reviewed for Use in Pharmaceutical Process Design: VLE, LLE, VLLE, and SLE Study. Ind Eng Chem Res 2022. [DOI: 10.1021/acs.iecr.2c00429] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/30/2022]
Affiliation(s)
- Jaber Yousefi Seyf
- Department of Chemical Engineering, Hamedan University of Technology, 65155-579, Hamedan, Iran
| | - Mohammad Asgari
- Department of Chemical Engineering, Sharif University of Technology, 1458889694, Tehran, Iran
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5
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Keßler T, Kunde C, Linke S, Sundmacher K, Kienle A. Integrated computer-aided molecular and process design: Green solvents for the hydroformylation of long-chain olefines. Chem Eng Sci 2022. [DOI: 10.1016/j.ces.2021.117243] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/03/2022]
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6
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Wang J, Chen D, Zhu L. Integrated Working Fluids and Process Optimization for Refrigeration Systems Using Polar PC-SAFT. Ind Eng Chem Res 2021. [DOI: 10.1021/acs.iecr.1c03624] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/29/2022]
Affiliation(s)
- Jiayuan Wang
- College of Chemical Engineering, Zhejiang University of Technology, 310014 Hangzhou, China
| | - Duoduo Chen
- College of Chemical Engineering, Zhejiang University of Technology, 310014 Hangzhou, China
| | - Lingyu Zhu
- College of Chemical Engineering, Zhejiang University of Technology, 310014 Hangzhou, China
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7
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Abstract
Recovering waste solvent for reuse presents an excellent alternative to improving the greenness of industrial processes. Implementing solvent recovery practices in the chemical industry is necessary, given the increasing focus on sustainability to promote a circular economy. However, the systematic design of recovery processes is a daunting task due to the complexities associated with waste stream composition, techno-economic analysis, and environmental assessment. Furthermore, the challenges to satisfy the desired product specifications, particularly in pharmaceuticals and specialty chemical industries, may also deter solvent recovery and reuse practices. To this end, this review presents a systems-level approach including various methodologies that can be implemented to design and evaluate efficient solvent recovery pathways.
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Affiliation(s)
- Emmanuel A Aboagye
- Department of Chemical Engineering, Henry M. Rowan College of Engineering, Rowan University, 201 Mullica Hill Road, Glassboro, NJ, 08028, USA
| | - John D Chea
- Department of Chemical Engineering, Henry M. Rowan College of Engineering, Rowan University, 201 Mullica Hill Road, Glassboro, NJ, 08028, USA
| | - Kirti M Yenkie
- Department of Chemical Engineering, Henry M. Rowan College of Engineering, Rowan University, 201 Mullica Hill Road, Glassboro, NJ, 08028, USA
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8
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Watson O, Jonuzaj S, McGinty J, Sefcik J, Galindo A, Jackson G, Adjiman CS. Computer Aided Design of Solvent Blends for Hybrid Cooling and Antisolvent Crystallization of Active Pharmaceutical Ingredients. Org Process Res Dev 2021; 25:1123-1142. [PMID: 34295139 PMCID: PMC8289336 DOI: 10.1021/acs.oprd.0c00516] [Citation(s) in RCA: 10] [Impact Index Per Article: 2.5] [Reference Citation Analysis] [Abstract] [Key Words] [Grants] [Track Full Text] [Download PDF] [Figures] [Journal Information] [Subscribe] [Scholar Register] [Received: 11/26/2020] [Indexed: 02/06/2023]
Abstract
Choosing a solvent and an antisolvent for a new crystallization process is challenging due to the sheer number of possible solvent mixtures and the impact of solvent composition and crystallization temperature on process performance. To facilitate this choice, we present a general computer aided mixture/blend design (CAMbD) formulation for the design of optimal solvent mixtures for the crystallization of pharmaceutical products. The proposed methodology enables the simultaneous identification of the optimal process temperature, solvent, antisolvent, and composition of solvent mixture. The SAFT-γ Mie group-contribution approach is used in the design of crystallization solvents; based on an equilibrium model, both the crystal yield and solvent consumption are considered. The design formulation is implemented in gPROMS and applied to the crystallization of lovastatin and ibuprofen, where a hybrid approach combining cooling and antisolvent crystallization is compared to each method alone. For lovastatin, the use of a hybrid approach leads to an increase in crystal yield compared to antisolvent crystallization or cooling crystallization. Furthermore, it is seen that using less volatile but powerful crystallization solvents at lower temperatures can lead to better performance. When considering ibuprofen, the hybrid and antisolvent crystallization techniques provide a similar performance, but the use of solvent mixtures throughout the crystallization is critical in maximizing crystal yields and minimizing solvent consumption. We show that our more general approach to rational design of solvent blends brings significant benefits for the design of crystallization processes in pharmaceutical and chemical manufacturing.
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Affiliation(s)
- Oliver
L. Watson
- Department
of Chemical Engineering, Centre for Process Systems Engineering, Institute
for Molecular Science and Engineering and EPSRC Future Manufacturing
Hub in Continuous Manufacturing and Advanced Crystallisation, Imperial College London, South Kensington Campus, London SW7 2AZ, U.K.
| | - Suela Jonuzaj
- Department
of Chemical Engineering, Centre for Process Systems Engineering, Institute
for Molecular Science and Engineering and EPSRC Future Manufacturing
Hub in Continuous Manufacturing and Advanced Crystallisation, Imperial College London, South Kensington Campus, London SW7 2AZ, U.K.
| | - John McGinty
- EPSRC
Future Manufacturing Hub in Continuous Manufacturing and Advanced
Crystallisation, Department of Chemical and Process Engineering, University of Strathclyde, 75 Montrose Street, Glasgow G1 1XJ, U.K.
| | - Jan Sefcik
- EPSRC
Future Manufacturing Hub in Continuous Manufacturing and Advanced
Crystallisation, Department of Chemical and Process Engineering, University of Strathclyde, 75 Montrose Street, Glasgow G1 1XJ, U.K.
| | - Amparo Galindo
- Department
of Chemical Engineering, Centre for Process Systems Engineering, Institute
for Molecular Science and Engineering and EPSRC Future Manufacturing
Hub in Continuous Manufacturing and Advanced Crystallisation, Imperial College London, South Kensington Campus, London SW7 2AZ, U.K.
| | - George Jackson
- Department
of Chemical Engineering, Centre for Process Systems Engineering, Institute
for Molecular Science and Engineering and EPSRC Future Manufacturing
Hub in Continuous Manufacturing and Advanced Crystallisation, Imperial College London, South Kensington Campus, London SW7 2AZ, U.K.
| | - Claire S. Adjiman
- Department
of Chemical Engineering, Centre for Process Systems Engineering, Institute
for Molecular Science and Engineering and EPSRC Future Manufacturing
Hub in Continuous Manufacturing and Advanced Crystallisation, Imperial College London, South Kensington Campus, London SW7 2AZ, U.K.
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9
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Diab S, Gerogiorgis DI. No More Than Three: Technoeconomic Mixed Integer Nonlinear Programming Optimization of Mixed Suspension, Mixed Product Removal Crystallizer Cascades for Melitracen, an Antidepressant API. Ind Eng Chem Res 2020. [DOI: 10.1021/acs.iecr.0c03535] [Citation(s) in RCA: 7] [Impact Index Per Article: 1.4] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/28/2022]
Affiliation(s)
- Samir Diab
- Institute for Materials and Processes (IMP), School of Engineering, University of Edinburgh, The Kings Buildings, Edinburgh EH9 3FB, Scotland, U.K
| | - Dimitrios I. Gerogiorgis
- Institute for Materials and Processes (IMP), School of Engineering, University of Edinburgh, The Kings Buildings, Edinburgh EH9 3FB, Scotland, U.K
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10
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Chemmangattuvalappil NG. Development of solvent design methodologies using computer-aided molecular design tools. Curr Opin Chem Eng 2020. [DOI: 10.1016/j.coche.2019.11.005] [Citation(s) in RCA: 12] [Impact Index Per Article: 2.4] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 01/22/2023]
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11
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Hu C, Testa CJ, Wu W, Shvedova K, Shen DE, Sayin R, Halkude BS, Casati F, Hermant P, Ramnath A, Born SC, Takizawa B, O'Connor TF, Yang X, Ramanujam S, Mascia S. An automated modular assembly line for drugs in a miniaturized plant. Chem Commun (Camb) 2020; 56:1026-1029. [PMID: 31854390 DOI: 10.1039/c9cc06945c] [Citation(s) in RCA: 20] [Impact Index Per Article: 4.0] [Reference Citation Analysis] [Abstract] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 12/13/2022]
Abstract
We report here a fully automated, end-to-end, integrated continuous manufacturing process for a small-molecule generic medication with built-in quality assurance. The entire process fits into a box of 30.7 m2 modular footprint and a total residence time of less than 30 h, with a throughput up to 40.3 × 106 tablets per year.
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Affiliation(s)
- Chuntian Hu
- CONTINUUS Pharmaceuticals, 25R Olympia Ave, Woburn, MA 01801, USA.
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12
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A Hybrid Framework for Simultaneous Process and Solvent Optimization of Continuous Anti-Solvent Crystallization with Distillation for Solvent Recycling. Processes (Basel) 2020. [DOI: 10.3390/pr8010063] [Citation(s) in RCA: 4] [Impact Index Per Article: 0.8] [Reference Citation Analysis] [Abstract] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/16/2022] Open
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.
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13
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Systematic Selection of Green Solvents and Process Optimization for the Hydroformylation of Long-Chain Olefines. Processes (Basel) 2019. [DOI: 10.3390/pr7120882] [Citation(s) in RCA: 5] [Impact Index Per Article: 0.8] [Reference Citation Analysis] [Abstract] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/16/2022] Open
Abstract
Including ecologic and environmental aspects in chemical engineering requires new methods for process design and optimization. In this work, a hydroformylation process of long-chain olefines is investigated. A thermomorphic multiphase system is employed that is homogeneous at reaction conditions and biphasic at lower temperatures for catalyst recycling. In an attempt to replace the toxic polar solvent N,N-dimethylformamide (DMF), ecologically benign alternatives are selected using a screening approach. Economic process optimization is conducted for DMF and two candidate solvents. It is found that one of the green candidates performs similarly well as the standard benchmark solvent DMF, without being toxic. Therefore, the candidate has the potential to replace it.
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14
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Diab S, Gerogiorgis DI. Technoeconomic Optimization of Continuous Crystallization for Three Active Pharmaceutical Ingredients: Cyclosporine, Paracetamol, and Aliskiren. Ind Eng Chem Res 2018. [DOI: 10.1021/acs.iecr.8b00679] [Citation(s) in RCA: 9] [Impact Index Per Article: 1.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 01/13/2023]
Affiliation(s)
- Samir Diab
- School of Engineering (IMP), University of Edinburgh, The King’s Buildings, Edinburgh, EH9 3FB, Scotland, United Kingdom
| | - Dimitrios I. Gerogiorgis
- School of Engineering (IMP), University of Edinburgh, The King’s Buildings, Edinburgh, EH9 3FB, Scotland, United Kingdom
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