2009
DOI: 10.1021/bk-2009-1030.ch024
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Prediction of Gas Solubility using COSMOthermX

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Cited by 4 publications
(3 citation statements)
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“…Figure and Table show the comparison of ideal normalized CO 2 /CH 4 selectivity of [BMIM]­[DCA]/ZIF-8 with different IL/ZIF-8 and IL/CuBTC samples at 0.01 to 0.1 bar and temperature of 25 °C reported previously in literature. Figure shows the comparison of normalized selectivity of previously reported ILs/MOFs composites at 0.1 bar pressure. ,,, Normalized selectivity was computed by dividing CO 2 /CH 4 selectivity of composite samples by the corresponding values of pristine MOFs. The results demonstrated that [BMIM]­[DCA]/ZIF-8 showed better separation performance than the other composites reported previously, as shown in Figure and Table .…”
Section: Results and Discussionmentioning
confidence: 99%
“…Figure and Table show the comparison of ideal normalized CO 2 /CH 4 selectivity of [BMIM]­[DCA]/ZIF-8 with different IL/ZIF-8 and IL/CuBTC samples at 0.01 to 0.1 bar and temperature of 25 °C reported previously in literature. Figure shows the comparison of normalized selectivity of previously reported ILs/MOFs composites at 0.1 bar pressure. ,,, Normalized selectivity was computed by dividing CO 2 /CH 4 selectivity of composite samples by the corresponding values of pristine MOFs. The results demonstrated that [BMIM]­[DCA]/ZIF-8 showed better separation performance than the other composites reported previously, as shown in Figure and Table .…”
Section: Results and Discussionmentioning
confidence: 99%
“…The Conductor like Screening Model for Real Solvents (COSMO-RS) was used to determine the effects of temperature and pressure changes on the CO 2 absorption of DESs [29][30][31][32]. Two steps were required in order to proceed with the COSMO-RS simulation.…”
Section: Cosmo-rs Calculation Methodologymentioning
confidence: 99%
“…As the calculation of the gas solubility by using COSMOThermX software (version 2.1, release 01.06) requires the prior knowledge of pure compound vapour pressures of pure components, these data were taken from the literature for the CO 2 [40] and also for each studied solvent [41][42][43][44][45][46]. Vapour pressures were also estimated by generating 'energy values' by using Turbomole program [47], as already described into the literature [39,48].…”
Section: Predictive Methodsmentioning
confidence: 99%