Transposition from a batch to a continuous process for microencapsulation by interfacial polycondensation

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• 作者：Fé ; licie Theron^a ; ^b ; ^{felicie.theron@mines-nantes.fr} ; Zoé ; Anxionnaz-Minvielle^c ; Nathalie Le Sauze^a ; ^b ; Michel Cabassud^a ; ^b
• 关键词：Microencapsulation ; Interfacial polycondensation ; Continuous process ; Static mixer ; Milli reactor ; Coiled tube reactor
• 刊名：Chemical Engineering and Processing
• 出版年：2012
• 期刊代码：15_02552701
• 类别：ce
• 出版时间：April, 2012
• 卷：54
• 期：Complete
• 页码：42-54
• 文件大小：1278 K

摘要

A novel continuous process is proposed and investigated to produce microcapsules by interfacial polycondensation. Polymeric microcapsules are obtained via a two-step process including an initial emulsification of two immiscible fluids in static mixers and a subsequent interfacial polycondensation reaction performed in two different continuous reactors, the Deanhex heat exchanger/reactor or a classical coiled-tube. This study is carried out through a step by step approach. A model system involving polyurea as the polymeric membrane and cyclohexane as the encapsulated species is chosen. A semi-batch reaction kinetic study is first performed in order to obtain kinetics data of the polycondensation reaction and to highlight hydrodynamic issues that can happen when running the encapsulation reaction in classical stirred tank. Parameters influencing droplets size obtained when carrying out emulsification in static mixers are then investigated. The hydrodynamic of the Deanhex reactor used is also characterized in terms of mixing time and residence time distribution. To validate the innovative continuous process, the emulsion droplets obtained at the static mixer outlet are encapsulated firstly in the Deanhex reactor and secondly in the coiled-tube. The apparent reaction kinetics and microcapsules characteristics corresponding to different operating conditions are discussed.