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$BJ,N%!"H?1~!":`NA!"4D6-!"%(%M%k%.!<$r$a$0$k?75;=Q$NDs0F$H3+H/$O$=$N;~Be$rH?1G$9$k6@$G$b$"$k!#$7$+$7!"$=$l$i$N%W%m%;%9$r9=C[$9$k$?$a$N4pAC$H$J$kJ*@-$NBg@Z$5$O$$$D$N;~Be$bJQ$o$k$3$H$J$/!"?.Mj@-$N9b$$%G!<%?$NC_@Q$H$=$l$K4p$E$$$??d;;!&%7%_%e%l!<%7%g%s$N3+H/$,$*$3$J$o$l$F$$$k!#%7%s%]%8%&%`$G$O:G?7$N5;=Q$KI,MW$JJ*@-$O2?$+$rL@$i$+$K$7$F!":G?7$NB,Dj%G!<%?$H?d;;!&%7%_%e%l!<%7%g%s$,$I$N$h$&$K3hMQ$5$l$F$$$k$N$+$rF$O@$7$F$_$?$$!#$J$*!"M%=(3X@8>^$NI=>4$b9T$&M=Dj$G$"$k(B
$B:G=*99?7F|;~!'(B2012-09-29 21:47:01
$B$3$NJ,N`$G$h$/;H$o$l(B $B$F$$$k%-!<%o!<%I(B | $B%-!<%o!<%I(B | $B | |
---|---|---|---|
Ionic liquid | 6$B7o(B | ||
viscosity | 6$B7o(B | ||
density | 4$B7o(B | ||
carbon dioxide | 3$B7o(B | ||
vapor-liquid equilibria | 3$B7o(B | ||
solubility | 3$B7o(B | ||
Thermodynamic consistency line | 3$B7o(B | ||
Cage occupancy | 2$B7o(B | ||
Supercritical carbon dioxide | 2$B7o(B | ||
glyme | 2$B7o(B | ||
Gas Hydrate | 2$B7o(B | ||
liquid liquid equilibria | 1$B7o(B |
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $B | |
---|---|---|---|
50 | $B=cJ* | Vapor-Liquid Equilibrium Wilson Parameter Ester | 4/18 10:20:03 |
55 | $B%]%j(B(n-$B%V%A%k%a%?%/%j%l!<%H(B)+$B?];@%(%9%F%k7O$NAj8_Aj8_;678?t$NB,Dj$HAj4X(B | mutual diffusion coefficient acetate ester poly(n-butyl methacrylate) | 4/18 15:16:40 |
65 | $B86;RCDJ,2r$K$h$k6~@^N($N?d;;K!(B | refractive index property prediction QSPR | 4/19 10:51:28 |
143 | $B>x5$05IU6a$G$N3K2=$K$h$k;6Mp$NB,Dj(B | nucleation vaporization scattering | 4/23 15:05:19 |
207 | $B&B(B-$B%8%1%H%J!<%H$r%"%K%*%s$H$9$k%$%*%s1UBN$NL)EY!"G4EY!"EE5$EAF3EY(B | ionic liquid density viscosity | 4/24 18:54:02 |
235 | $BG4@-4KOBK!$K$h$k=a3jL}$NG4CF@-$K4X$9$k8&5f(B | lubricant viscosity viscoelasticity | 4/25 10:44:17 |
255 | $B4J0W7?(BWilson$B<0$K$h$k(B3$B@.J,7O5$1UJ?9U$N?d;;(B | Wilson equation T-K Wilson equation ASOG | 4/25 13:31:39 |
266 | $BG;EY0MB8I=LL@Q%Q%i%a!<%?%b%G%k$K$h$kAjJ?9U$NAj4X(B | Activity coefficient model Quasi chemical Concentration dependent surface area parameter | 4/25 15:14:49 |
285 | $BD6NW3&Fs;@2=C:AG$KBP$9$kLt:^$NMO2rEYB,Dj(B | supercritical carbon dioxide uv vis spectroscopy solubility | 4/25 17:00:52 |
299 | $B:.9g%O%$%I%l!<%H$K$*$1$k?eAG$HJd=u:^$N6%AhE*dF@jM-(B | Gas hydrate Hydrogen storage Cage occupancy | 4/25 18:07:06 |
361 | $BHsJ?9U(BMD$B7W;;$K$h$k9b299b05%a%?%N!<%k?eMO1U$NG4EY5sF0$N2r@O(B | supercritical MD viscosity | 4/26 11:53:40 |
370 | $BHs@~7A%l!<%6! | diffusion coefficient ionic liquids nonlinear laser spectroscopy | 4/26 13:06:31 |
405 | [$BE8K>9V1i(B]$B%,%9%O%$%I%l!<%H$NG.NO3XE*0BDj@-$H%2%9%HJ,;R$NdF@jM-@-(B | Gas Hydrate Phase equilibria Cage occupancy | 4/26 15:39:22 |
494 | $BJ,8w3XE* | Spectroscopic measurements Supercritical carbon dioxide Anthracene solubility | 4/26 21:28:07 |
540 | [$BE8K>9V1i(B]$BJ*@-?d;;$N$J$+$NJ,;R%7%_%e%l!<%7%g%s(B-$BElKLBg3X$G$N8&5f$r?6$jJV$C$F(B | Computational Chemistry Simulation Estimation | 4/27 09:27:09 |
576 | $B%H%i%C%W%0%j!<%9%b%G%kJ*AE$B7?:.9gB'$rMQ$$$?(B3$BuBVJ}Dx<0$K$h$kAj4X(B | Triolein Hydrogen Solubility Cubic Equation of State | 4/27 10:44:55 |
579 | $B%[%9%[%K%&%`7O%$%*%s1UBNEE5$EAF3EY$N05NO!&29EY0MB8@-(B | ionic liquid electrical conductivity high pressure | 4/27 10:50:27 |
581 | $B5$1UJ?9U$K$*$1$k%$%*%s1UBN$N8z2L$N?d;;(B | vapor-liquid equilibria ion liquid solvation method | 4/27 11:01:13 |
589 | $B9-$$29EY!&05NO>r7o$K$*$1$k%$%*%s1UBN(B-CO2$B7O$N(BpVT$B$HEE5$EAF3EY(B | ionic liquid carbon dioxide pVT | 4/27 11:13:06 |
590 | $BDc4D6-Ii2YMOG^$r$a$0$k(B2$B@.J,7O:.9gJ*$NAj8_MO2rEYB,Dj$HAj4X(B | liquid liquid equilibria environment benign solvent ionic liquid | 4/27 11:15:19 |
593 | 2$B@.J,7O6&J(:.9gJ*$KBP$9$kG.NO3X7rA4@~$rMxMQ$7$?5$1UJ?9U=c?h?d;;$H%G%b%W%m%0%i%`$N | Thermodynamic consistency line azeotropic mixture vapor-liquid equilibria | 4/27 11:19:05 |
600 | $B%0%i%$%`(B-$B%j%A%&%`1vMO1U$NFs;@2=C:AG5[<}FC@-(B | glyme carbon dioxide solubility | 4/27 11:33:11 |
607 | $B%0%i%$%`(B-$B%j%A%&%`1vMO1UL)EY!&G4EY$NG;EY!&29EY0MB8@-(B | glyme density viscosity | 4/27 11:39:56 |
703 | $B%(%?%N!<%k(B+$B?e(B+$B%(%9%F%k(B($B?];@%V%A%k!"?];@%"%_%k!"Mo;@%(%A%k(B)$B$N(B3$B@.J,7O$N1U1UJ?9U$H!"%(%?%N!<%k(B+$B?e(B+$B?];@%V%A%k(B+KCl$B$N(B4$B@.J,7O$N1U1UJ?9U$NB,Dj(B | Bioethanol Butyl acetate Potassium chlorise | 4/27 14:58:33 |
708 | $B%$%_%@%>%j%&%`7O%$%*%s1UBN$KBP$9$kL)EY$*$h$SI=LLD%NO$NB,Dj(B | Surface tension Ionic liquid Density | 4/27 15:05:13 |
732 | $B>.7?Mn?K<0G4EY7W$rMQ$$$?(BTFSI$B%$%*%s1UBN$KBP$9$kG4EYB,Dj(B | Viscosity Ionic liquid Viscometer | 4/27 15:46:54 |
737 | $BI8=`J(E@(BTb$B$rI,MW$H$7$J$$L56K@-J* | Critical temperature Normal boiling point Group contribution method | 4/27 15:49:05 |
748 | $B>o29>o05$+$iD6NW3&>uBV$K$*$1$k%"%k%3!<%k?eMO1U$NL)EY!&G4EY5sF0$NE}0lE*2r@O(B | alcohol density viscosity | 4/27 16:05:55 |
749 | $B%0%k!<%W4sM?K!$rE,MQ$7$?(BCOSMOSPACE$B$K$h$k%"%k%3!<%k(B+$B%"%k%+%s7O$N5$1UJ?9U$NAj4X(B | COSMOSPACE activity coefficient vapor liquid equilibrium | 4/27 16:06:01 |
761 | $BD6NW3&Fs;@2=C:AGB8:_2<$K$*$1$k%]%j%+!<%\%M!<%H$N7k>=2=(B | polycarbonate carbon dioxide crystallization | 4/27 16:27:51 |
855 | $BG.NO3X7rA4@~$rMQ$$$k(B3$B@.J,7ODj295$1UJ?9U$N=c?h?d;;$H | Thermodynamic consistency line ternary vapor-liquid equiliebria UNIQUAC equation | 4/27 18:27:59 |
923 | $B%j%A%&%`(B-$B6u5$EECS$K$*$1$k%$%*%s1UBN4^?;Kl$rMxMQ$7$?;@AG!?CbAG$NF)2aJ,N%(B | ionic liquid membrane COSMO-SAC oxygen | 4/27 19:47:53 |
926 | $B8w%;%s%5!<$rMxMQ$7$?%3%s%Q%/%H7?MO2rEYB,DjAuCV$N3+H/(B | solubility optical sensor compact appratus | 4/27 19:50:29 |
928 | $B@E;_%;%kCf5$AjD>@\:N | Thermodynamic consistency line vapor-liquid equilibria static cell | 4/27 19:52:03 |
953 | $B%0%k!<%W4sM?>uBV<0$r3hMQ$7$?(BCO2$BJ*M}5[<}:^$NA*DjK!(B | Group Contribution Equation of State CO2 Physical Absorption | 4/27 20:49:26 |