首页> 外文会议>International Symposium on Supercritical Fluids Tome 3: Materials Processing; 20030428-20030430; Versailles; FR >MODELING OF PARTICLE FORMATION IN SUPERCRITICAL ANTI-SOLVENT PROCESSES: DILUTED AND CONCENTRATED REGIME
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MODELING OF PARTICLE FORMATION IN SUPERCRITICAL ANTI-SOLVENT PROCESSES: DILUTED AND CONCENTRATED REGIME

机译:超临界抗溶剂过程中颗粒形成的模型:稀疏集中法

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In this work, a theoretical investigation on particle formation taking into account mass transfer and thermodynamic for ternary systems solvent-antisolvent-solute, and solute precipitation kinetic is presented for both diluted and concentrated polymeric solutions. A mathematical model of mass transfer between a droplet of polymeric organic solution and a compressed anti-solvent is solved for fully miscible conditions. The generalized Maxwell-Stefan diffusion equation is used. To fairly describe the thermodynamic of chain-like solutes, such as polymers, both the volumetric and equilibrium properties are represented by the perturbed-hard-sphere-chain-theory equation of state. For concentrated solution, where only one polymeric solid particle is generated from the initial organic-solution droplet, a simple solute precipitation kinetic gives radial profiles of solute and solvent composition, and precipitated solute as a function of time. Depending on the process variables, the solute precipitation can occur either at the initial droplet surface or internally leading either to a hollow sphere or to a compact particle, respectively. The simulation presented in this work provides the precipitated solute distribution as a function of radial coordinate and time. Process operative variables and mass transfer pathways could strongly affect the overall final particle morphology. Results are presented for solutes with different solubility and kinetic parameters.
机译:在这项工作中,提出了关于颗粒形成的理论研究,其中考虑了三元体系中溶剂-反溶剂-溶质的传质和热力学,以及稀释和浓缩聚合物溶液的溶质沉淀动力学。对于完全可混溶的条件,求解了聚合物有机溶液液滴与压缩反溶剂之间的传质数学模型。使用广义的Maxwell-Stefan扩散方程。为了公平地描述诸如聚合物之类的链状溶质的热力学,其体积和平衡性质均由摄动的硬球链状态理论方程式表示。对于浓溶液,从初始的有机溶液滴中仅产生一个聚合物固体颗粒,简单的溶质沉淀动力学就给出了溶质和溶剂组成的径向分布,并且沉淀的溶质随时间变化。取决于工艺变量,溶质沉淀可在初始液滴表面或内部分别产生中空球或致密颗粒。在这项工作中提出的模拟提供了沉淀的溶质分布作为径向坐标和时间的函数。工艺操作变量和传质途径可能会严重影响最终颗粒的整体形态。给出了具有不同溶解度和动力学参数的溶质的结果。

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