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$BJ,N%!"H?1~!":`NA!"4D6-!"%(%M%k%.!<$J$I$K$*$1$k;}B3E*$J@.D9!"%0%j!<%s!&%$%N%Y!<%7%g%se$G4pACJ*@-8&5f$OI,MWIT2D7g$G$"$k!#$=$NBP>]7O$O!"$h$jJ#;($G9-HO0O$K$J$C$F$-$F$*$j!"?.Mj@-$N9b$$B,Dj%G!<%?$NC_@Q$d9b@:EY$J?d;;!&%7%_%e%l!<%7%g%s5;=Q$X$NMW5a$,A}$7$F$$$k!#K\%7%s%]%8%&%`$G$O!"^$NI=>4$b9T$&M=Dj$G$"$k!#(B

$B:G=*99?7F|;~!'(B2013-08-09 19:09:01

$B$3$NJ,N`$G$h$/;H$o$l(B
$B$F$$$k%-!<%o!<%I(B		$B%-!<%o!<%I(B$B
CO2 solubility2$B7o(B
viscosity2$B7o(B
high pressure2$B7o(B
gas hydrate2$B7o(B
phase equilibria2$B7o(B
interfacial tension1$B7o(B

$B$BHV9f(B$B9V1iBjL\!?H/I=$B%-!<%o!<%I(B$B
28GC-Wilson$B<0$K$h$k8:052<$N(B2$B@.J,7ODj055$1UJ?9U$N?d;;(B
($B;38}Bg1!M}9)(B) $B!{(B($B@5(B)$B>.^<(B $BLP$B!&(B ($B6eBg1!9)(B) ($B@5(B)$BJF_7(B $B@a;R(B		Vapor-Liquid Equilibrium
Wilson Parameter
Reduced Pressure
4/25
14:41:16
45$B%$%*%s1UBN7O2=9)J*@-$N(BPCPCE$B!&(BASOGDB$B$K$h$kJ88%8!:w!&Aj4X!&?d;;(B
($BF|BgM}9)(B) $B!{(B($B@5(B)$BFJLZ(B $B>!8J(B$B!&(B ($B@5(B)$B>>ED(B $B909,(B$B!&(B ($B@5(B)$B7*86(B $B@6J8(B		Physicochemical Properties
Ionic Liquids
PCPCE$B!&(BASOGDB
4/30
10:52:06
65$BG;EY0MB8I=LL@Q%Q%i%a!<%?%b%G%k$K$h$k(B1-butanol+water$B7O$NAjJ?9U$NAj4X(B
($B6eBg9)(B) $B!{(B($B3X(B)$BC+8}(B $B0l@8(B$B!&(B ($B@5(B)$B4d0f(B $BK'IW(B		liquid-liquid equilibrum
concentraion dependent surface area parameter model
1-butanol+water
5/2
17:29:22
262[$B>7BT9V1i(B] $B%,%9%O%$%I%l!<%H$NJ*@-8&5f$H1~MQ$X$NE83+(B
($B:eBg1!4p9)(B) $B!{(B($B@5(B)$BBg3@(B $B0l@.(B		gas hydrate
phase equilibria
cage occupancy
5/10
13:25:26
355$B%(%?%N!<%k?eMO1U$K$*$1$kD62;GH%-%c%S%F!<%7%g%s8z2L$HJ*@-CMJQ2=(B
($BH,8M9)Bg1!(B) $B!{(B($B3X(B)$B4\2V(B $B;VJf(B$B!&(B ($B@5(B)$B|b66(B $B?8(B		acoustic cavitation
ethanol aqueous solution
liquid structure
5/10
18:47:30
368Wilhelmy$BK!$K$h$k?e(B+$BBgF&L}7O$N3&LLD%NO$NB,Dj$H(BO/W$B%(%^%k%7%g%s%5%$%:$X$N1F6A(B
($BEl9)Bg1!M}9)(B) $B!{(B($B3X(B)$B0p$B!&(B ($B@5(B)$B2<;3(B $BM52p(B		O/W emulsion
interfacial tension
Wilhelmy method
5/10
19:31:08
376$B?e!
($BEl9)Bg1!M}9)(B) $B!{(B($B3X(B)$BEl6?(B $B>;51(B$B!&(B ($B@5(B)$B2<;3(B $BM52p(B		pi-electron system
high temperature and pressure water
PC-SAFT equation of state
5/10
19:52:18
452$B@.J,%U%!%_%j!
($BK!@/Bg(B) $B!{(B($B@5(B)$B@>3$(B $B1QM:(B$B!&(B $B4X8}(B $B=($B!&(B ($B@5(B)$B8c6?(B $B7r0l(B$B!&(B $B=)Dj(B $BNJN<(B		binary interaction parameter
component family method
BWR equation of state
5/12
14:18:49
548[$B>7BT9V1i(B] $BDc(BGWP$BNdG^$N3+H/!!(B-$BB,DjAuCV$H2A(B-
($B?@8MBg1!9)(B) $B!{(B($B@5(B)$B>>Hx(B $B@.?.(B		refrigerants
thermophysical property
high pressure
5/13
11:52:32
645$B6bB0:xBN$N>:2Z05$HD6NW3&Fs;@2=C:AGCf$X$NMO2rEY(B
($B9-Bg1!9)(B) $B!{(B($B3X(B)$B?92,(B $BH~HA(B$B!&(B $BBg86(B $BL$F`H~(B$B!&(B ($B@5(B)$B=ULZ(B $B>-;J(B$B!&(B ($B@5(B)$BLZ86(B $B?-0l(B$B!&(B ($B@5(B)$BBlV:(B $BHK		Sublimation
Solubilities
Metal complexes
5/13
15:15:00
652$B%$%*%s1UBN(B-$B%0%i%$%`:.9gMO1U$NJ*M}2=3XE*FC@-(B
($BF|Bg9)(B) $B!{(B($B@5(B)$B2$B!&(B ($B@5(B)$B;y6L(B $BBgJe(B$B!&(B ($B;:Am8&(B) ($B@5(B)$BKRLn(B $B5.;j(B$B!&(B ($B@5(B)$B6b5WJ](B $B8w1{(B$B!&(B $BETC[(B $B@?Fs(B		ionic liquid
glyme
CO2 solubility
5/13
15:37:01
715$BG.NO3X7rA4@~$rMQ$$$k1U1UJ,G[78?t$N?d;;(B
($B		Thermodynamic consistency line
liqui-liquid partition coefficient
grand correlation
5/13
16:54:04
804$B%0%i%$%`(B-$B%9%k%[%s;@%j%A%&%`1vMO1U$NL)EY!&G4EY!&Fs;@2=C:AGMO2rEY(B
($BF|Bg1!9)(B) $B!{(B($B3X(B)$B1sF#(B $B9/M5(B$B!&(B ($B3X(B)$B?70f(B $B9@Li(B$B!&(B ($BF|Bg9)(B) ($B@5(B)$B2$B!&(B ($B@5(B)$B;y6L(B $BBgJe(B$B!&(B ($B;:Am8&(B) ($B@5(B)$BKRLn(B $B5.;j(B$B!&(B ($B@5(B)$B6b5WJ](B $B8w1{(B		density
viscosity
CO2 solubility
5/13
18:14:20
843[$B>7BT9V1i(B] $B%^%k%A%9%1!<%k2=3X9)3X$K$h$kJ*@-$+$i5!G=@-:`NA@_7W$X$N
($B9)3X1!Bg(B) $B!{(B($B@5(B)$B9b1)(B $BMN=<(B		Properties
Simulation
Secondary Battery
5/13
19:00:07
879$B>.7?Mn?K<0G4EY7W$rMQ$$$?G4EYB,Dj$K$*$1$kIT3N$+$5$NI>2A(B
($B4X@>Bg4DET9)(B) $B!{(B($B3X(B)$B>>1J(B $BD>G7(B$B!&(B $BNkLZ(B $B5.2m(B$B!&(B ($B@5(B)$B9SLZ(B $BDgIW(B$B!&(B ($B@5(B)$B;3K\(B $B=(		viscometer
uncertainty
viscosity
5/13
19:32:43
880$B5$1UJ?9U?d;;<0$NDj?t7hDjK!(B
($BElM}BgM}(B) $B!{(B($B@5(B)$BBg9>(B $B=$B$(B		vapor-liquid equilibria
distillation
NRTL equation
5/13
19:35:04
1002$B%O%m%2%sCV49%7%/%m%Z%s%?%sM6F3BN$r%2%9%HJ,;R$H$7$?:.9g%O%$%I%l!<%H7O$N9b05Aj5sF0(B
($B:eBg1!4p9)(B) $B!{(B($B3X(B)$B>!ED(B $BfFEM(B$B!&(B ($B3X(B)$B>>K\(B $BM5$B!&(B ($B@5(B)$B?{86(B $BIp(B$B!&(B ($B@5(B)$BBg3@(B $B0l@.(B		gas hydrate
phase equilibria
high pressure
5/13
21:56:24
$B9V1i?=$79~$_0lMw(B($B%7%s%]%8%&%`HV9f!&9V1iJ,N`HV9fJL(B)
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(C) 2013 $B8x1W
Most recent update: 2013-08-09 19:09:01
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