A molecular design method based on the COSMO-SAC model for solvent selection in ionic liquid extractive distillation

AIChE Journal ◽  
2016 ◽  
Vol 62 (8) ◽  
pp. 2853-2869 ◽  
Author(s):  
Jing Fang ◽  
Rui Zhao ◽  
Weiyi Su ◽  
Chunli Li ◽  
Jing Liu ◽  
...  
2008 ◽  
Vol 120 (10) ◽  
pp. 1949-1953 ◽  
Author(s):  
Daibin Kuang ◽  
Satoshi Uchida ◽  
Robin Humphry-Baker ◽  
Shaik M. Zakeeruddin ◽  
Michael Grätzel

2013 ◽  
Vol 791-793 ◽  
pp. 141-144
Author(s):  
Xiu Min Shi ◽  
Min Wang

In order to research the possibility of separating the azeotrope of ethyl acetate + acetonitrile with ionic liquid as the extractant. Isobaric vapor-liquid equilibria for the ternary system ethyl acetate + acetonitrile + 1-octyl-3-methylimidazolium tetrafluoroborate ([OMIBF4) were measured at 101.32 kPa using a recirculation still. The results showed that the VLE of the ternary system was different from that of the binary system. The ionic liquid (IL) studied showed a slight crossover salt effect, which changed the relative volatility of ethyl acetate to acetonitrile and eliminated the azeotropic point when the mole fraction of IL in the liquid phase was greater than 0.05. Therefore, [OMIBF4 can be used as the extractant of extractive distillation for ethyl acetate + acetonitrile system, the suitable mole fraction of [OMIBF4 is about 10%.


2008 ◽  
Vol 47 (10) ◽  
pp. 1923-1927 ◽  
Author(s):  
Daibin Kuang ◽  
Satoshi Uchida ◽  
Robin Humphry-Baker ◽  
Shaik M. Zakeeruddin ◽  
Michael Grätzel

2018 ◽  
Vol 201 ◽  
pp. 268-275 ◽  
Author(s):  
Pablo Navarro ◽  
Marcos Larriba ◽  
Noemí Delgado-Mellado ◽  
Miguel Ayuso ◽  
Marta Romero ◽  
...  

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