首页> 外文会议>International Symposium on Supercritical Fluids Tome 2: SCF Properties Reactions; 20030428-20030430; Versailles; FR >Phase Equilibrium Thermodynamics for a Polycarbonate Production Process using Supercritical Carbon Dioxide
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Phase Equilibrium Thermodynamics for a Polycarbonate Production Process using Supercritical Carbon Dioxide

机译:超临界二氧化碳在聚碳酸酯生产过程中的相平衡热力学

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摘要

Thermodynamic phase equilibrium data, which are relevant to the development of a novel production process for polycarbonates from CO_2 and epoxides, are presented. In this solvent-free process, CO_2 is coupled to epoxides using various transition-metal catalyst systems. Data on the performance of these systems are discussed. Additionally, the polycarbonate solubility in CO_2 and CHO is considered, both inside and beyond the P-T ranges that have been used for synthesis of the polycarbonate. Moreover, CHO-CO_2 vapour pressure isotherms have been measured and modelled. Experimental results indicate that following the pressure decay during the polymerisation reaction offers a feasible and reliable method for on-line monitoring of monomer conversion. Results are finally discussed in terms of their implication on the development of novel production processes for polycarbonates.
机译:提出了热力学相平衡数据,该数据与开发由CO_2和环氧化物制备聚碳酸酯的新方法有关。在这种无溶剂工艺中,使用各种过渡金属催化剂系统将CO_2与环氧化物偶联。讨论了有关这些系统性能的数据。另外,考虑了聚碳酸酯在CO_2和CHO中的溶解度,在用于合成聚碳酸酯的P-T范围之内和之外。此外,已对CHO-CO_2蒸气压等温线进行了测量和建模。实验结果表明,随着聚合反应过程中压力的下降,单体监测转化提供了一种可行且可靠的方法。最后根据结果对开发聚碳酸酯新生产工艺的意义进行了讨论。

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