{"title":"Efficient Production of Inhalable Micro-Nanoparticles: Mechanism, Process Optimization, and Modular Continuous Micro-Crystallizer Design","authors":"Yuan Wang, Ding-Jun Chu, Jin-Liang Li, Xiao-Qiang Xie, Guo-Bin Ren, Ming-Hui Qi","doi":"10.1021/acs.oprd.5c00011","DOIUrl":null,"url":null,"abstract":"Batch production of micro-nanoparticles suffers from high energy consumption and low efficiency, and continuous crystallization is considered a promising solution. This study reported the design of a modular continuous coaxial mixing crystallizer (CCMC) system for the production of micro-nanoparticles of the pharmaceutical compound fluticasone propionate (FP), and the performance of the system was evaluated. Guided by experimentally determined thermodynamic and kinetic data of FP crystallization, computational fluid dynamics simulations were employed to optimize the crystallizer design, resulting in enhanced mixing efficiency occurring within 40 ms. Through a three-stage experimental protocol, the continuous crystallization process was optimized: (1) key process parameters were screened using factorial design; (2) the operational design space was mapped via response surface methodology; and (3) particle size control mechanisms were elucidated through analysis of mixing processes. Quantitative analysis identified the antisolvent-to-solution ratio as the dominant factor governing particle size distribution, attributed to its critical role in nucleation kinetics. The CCMC platform demonstrated robust and efficient operation for 25 min, delivering a single-run output equivalent to 990 doses of commercial formulation. Comparative studies revealed advantages over batch processing, including comparable powder crystallinity, improved crystal morphology, and narrower size distributions within a micro-nanometer range. The coaxial mixing crystallizer system exhibits excellence in flexibility, productivity, and material recovery.","PeriodicalId":55,"journal":{"name":"Organic Process Research & Development","volume":"309 1","pages":""},"PeriodicalIF":3.1000,"publicationDate":"2025-04-23","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Organic Process Research & Development","FirstCategoryId":"92","ListUrlMain":"https://doi.org/10.1021/acs.oprd.5c00011","RegionNum":3,"RegionCategory":"化学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q2","JCRName":"CHEMISTRY, APPLIED","Score":null,"Total":0}
引用次数: 0
Abstract
Batch production of micro-nanoparticles suffers from high energy consumption and low efficiency, and continuous crystallization is considered a promising solution. This study reported the design of a modular continuous coaxial mixing crystallizer (CCMC) system for the production of micro-nanoparticles of the pharmaceutical compound fluticasone propionate (FP), and the performance of the system was evaluated. Guided by experimentally determined thermodynamic and kinetic data of FP crystallization, computational fluid dynamics simulations were employed to optimize the crystallizer design, resulting in enhanced mixing efficiency occurring within 40 ms. Through a three-stage experimental protocol, the continuous crystallization process was optimized: (1) key process parameters were screened using factorial design; (2) the operational design space was mapped via response surface methodology; and (3) particle size control mechanisms were elucidated through analysis of mixing processes. Quantitative analysis identified the antisolvent-to-solution ratio as the dominant factor governing particle size distribution, attributed to its critical role in nucleation kinetics. The CCMC platform demonstrated robust and efficient operation for 25 min, delivering a single-run output equivalent to 990 doses of commercial formulation. Comparative studies revealed advantages over batch processing, including comparable powder crystallinity, improved crystal morphology, and narrower size distributions within a micro-nanometer range. The coaxial mixing crystallizer system exhibits excellence in flexibility, productivity, and material recovery.
期刊介绍:
The journal Organic Process Research & Development serves as a communication tool between industrial chemists and chemists working in universities and research institutes. As such, it reports original work from the broad field of industrial process chemistry but also presents academic results that are relevant, or potentially relevant, to industrial applications. Process chemistry is the science that enables the safe, environmentally benign and ultimately economical manufacturing of organic compounds that are required in larger amounts to help address the needs of society. Consequently, the Journal encompasses every aspect of organic chemistry, including all aspects of catalysis, synthetic methodology development and synthetic strategy exploration, but also includes aspects from analytical and solid-state chemistry and chemical engineering, such as work-up tools,process safety, or flow-chemistry. The goal of development and optimization of chemical reactions and processes is their transfer to a larger scale; original work describing such studies and the actual implementation on scale is highly relevant to the journal. However, studies on new developments from either industry, research institutes or academia that have not yet been demonstrated on scale, but where an industrial utility can be expected and where the study has addressed important prerequisites for a scale-up and has given confidence into the reliability and practicality of the chemistry, also serve the mission of OPR&D as a communication tool between the different contributors to the field.