首页> 外文期刊>The Korean journal of chemical engineering >Two component phase equilibria for the 3-methoxy-3-methyl-1-butanol and 1-methoxy-2-methyl-2-propanol in supercritical carbon dioxide
【24h】

Two component phase equilibria for the 3-methoxy-3-methyl-1-butanol and 1-methoxy-2-methyl-2-propanol in supercritical carbon dioxide

机译:用于3-甲氧基-3-甲基-1-丁醇和1-甲氧基-2-甲基-2-丙醇的两个组分相平衡,超临界二氧化碳

获取原文
获取原文并翻译 | 示例
           

摘要

Two component mixtures, 3-methoxy-3-methyl-1-butanol (MMB)+carbon dioxide and 1-methoxy-2-methyl-2-propanol (MMP)+carbon dioxide, were investigated at 313.2, 333.2, 353.2, 373.2 and 393.2 K and at 4.29 to 20.95 MPa to get phase equilibrium data. The phase separation of vapor+liquid behavior for the MMB and MMP plays a momentous function as the organic solvent in a diversity of industrial processes. The two MMB+carbon dioxide and MMP+carbon dioxide components have mixture critical curves that have maxima in the p-T plot between the T-c (critical temperatures) of MMB and carbon dioxide or MMP and carbon dioxide. The two component systems of MMB+ carbon dioxide and MMP+carbon dioxide mixture display type-I in simplest behavior. The measured results for the two component mixtures, MMB+carbon dioxide and MMP+carbon dioxide, are modelled with a general cubic equation of state, the Peng-Robinson, containing the k(ij), eta(ij) adjustable factor.
机译:在313.2,333.2,353.2,373.2中,研究了两种组分混合物,3-甲氧基-3-甲基-1-丁醇(MMB)+二氧化碳和1-甲氧基-2-甲基-2-丙醇(MMP)+二氧化碳。373.2和393.2 k和4.29至20.95 MPa以获得相平衡数据。 MMB和MMP的蒸气+液体行为的相分离在工业过程的多样性中作为有机溶剂发挥着一大一次功能。两种MMB +二氧化碳和MMP +二氧化碳组分具有混合临界曲线,其在MMB和二氧化碳或二氧化碳和二氧化碳和二氧化碳之间的T-C(临界温度)之间的P-T图中具有最大值。 MMB +二氧化碳的两个组分系统和MMP +二氧化碳混合物显示型 - I以最简单的行为。两个组分混合物,MMB +二氧化碳和MMP +二氧化碳的测量结果用一般的立方方程,彭罗宾逊,包含K(IJ),ETA(IJ)可调因子。

著录项

获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号