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Solubility of Supercritical CO2 in Polystyrene during Foam Formation via

机译:泡沫形成过程中超临界CO2在聚苯乙烯中的溶解度

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The use of supercritical fluids, such as CO2, for polymer foam formation has become popular in the last decade. These physical blowing agents are environmentally responsible, and are able to provide certain processing advantages during foam formation. In order to be able to understand foam formation under relatively high pressures and temperatures, thermodynamic phase equilibrium analysis is required coupled with a good equation of state. The Statistical Associated Fluid Theory (SAFT) equation of state (EOS) is studied in detail for the carbon dioxide/polystyrene system, under supercritical CO2 conditions. The SAFT EOS is found to perform better than the Soave-Redlich-Kwong (SRK) EOS, especially when considering liquid phase compositions and densities. Experimental data from the literature is used to validate model parameters cited in the literature for polystyrene-CO2 binary systems under supercritical conditions. The analysis is done with the assumption that the vapor phase is pure CO2 and in equilibrium with the liquid CO2-polystyrene condensed phase.
机译:在过去的十年中,使用超临界流体(例如CO2)来形成聚合物泡沫已经变得很普遍。这些物理发泡剂对环境负责,并且能够在泡沫形成期间提供某些加工优势。为了能够在相对较高的压力和温度下理解泡沫的形成,需要进行热力学相平衡分析以及良好的状态方程。详细研究了在超临界CO2条件下二氧化碳/聚苯乙烯体系的统计缔合流体理论(SAFT)状态方程(EOS)。发现SAFT EOS的性能优于Soave-Redlich-Kwong(SRK)EOS,尤其是在考虑液相组成和密度时。来自文献的实验数据用于验证文献中引用的超临界条件下聚苯乙烯-CO2二元系统的模型参数。该分析是在假设气相为纯CO2且与液态CO2-聚苯乙烯冷凝相平衡的前提下进行的。

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