CO_2萃取分离离子液体[bmim][PF_6]与萘的高压相平衡  

High-pressure phase equilibria for separation of naphthalene from ionic liquid [bmim][PF_6]by supercritical CO_2 extraction

作　　者：赵锁奇[1] 孙学文[1] 浮东宝[1] 仇艳华[1] 

机构地区：[1]中国石油大学(北京)重质油国家重点实验室,北京102249

出　　处：《化工学报》2008年第5期1171-1178,共8页CIESC Journal

基　　金：国家自然科学基金项目(20276038;20490209)~~

摘　　要：采用紫外光谱在线检测的静态相平衡方法,在温度313～333K、压力8～20MPa、萘的液相浓度0.0169～0.378mol.kg-1的范围内,测定了CO2+[bmim][PF6]+萘三元系中萘在富含CO2相的浓度。结果表明,在所测温度和压力范围内,萘在富含CO2相的浓度随着温度的升高而减小,随着压力的升高而增大,而且随着萘在液相中的浓度的减小而减小。在一定的温度压力条件下,萘在富含CO2相的浓度与萘在液相中的浓度近似呈双对数线性关系。采用Chrastil缔合模型关联了所有溶解度数据,平均相对偏差为14.9%。此外,还探讨了CO2萃取分离离子液体与高沸点有机物的操作模式,发现釜式间歇操作较为适宜。The concentrations of naphthalene in CO2-rich phase for the ternary system CO2 ＋ [bmim] [PF6 ] ＋ naphthalene were determined by a static method with online high-pressure ultraviolet detection, under the conditions of naphthalene molality in the liquid phase ranging from 0. 0169 to 0. 378 mol · kg^-1 , and temperature 313--333 K, pressure 8--20 MPa. It was found that the naphthalene mole fraction in the CO2-rich phase decreased with increasing temperature, increased with increasing pressure, and decreased with decreasing naphthalene concentration in the liquid phase. The logarithm of naphthalene mole fraction in the CO2-rich phase was shown to be approximately linear, at the same temperature and pressure, with the logarithm of naphthalene concentration in the liquid phase. All the solubility data were correlated to the Chrastil＇s association model and the mean relative deviation was found to be 14. 9%. Moreover, operation modes of supercritical CO2 extraction were discussed base on the solubility data. It was found that batch operation was better than continuous operation for organics extraction from ionic liquids using supercritical CO2.

关 键 词：离子液体 二氧化碳 萘 溶解度 相平衡 

分 类 号：O642.4[理学—物理化学]