SCEJ

$B2=3X9)3X2q(B $BBh(B44$B2s=)5(Bg2q(B

$B9V1i%W%m%0%i%`!J2q>l!&F|DxJL!K(B

K$B2q>l(B $BBh(B3$BF|(B

$B:G=*99?7F|;~!'(B2012-08-20 15:02:17
$B9V1i(B
$B;~9o(B		$B9V1i(B
$BHV9f(B		$B9V1iBjL\!?H/I=$B%-!<%o!<%I(B$BJ,N`(B
$BHV9f(B		$B$BHV9f(B
$B%7%s%]%8%&%`(B $B!c:G@hC<%W%m%;%9$rC4$&4pACJ*@-!]B,Dj$H%7%_%e%l!<%7%g%s!]!d(B
(9:00$B!A(B10:00)$B!!(B($B:BD9(B $BHf9>Eh(B $BM42p(B)
9:00$B!A(B 9:20K3012$B@.J,7O6&J(:.9gJ*$KBP$9$kG.NO3X7rA4@~$rMxMQ$7$?5$1UJ?9U=c?h?d;;$H%G%b%W%m%0%i%`$N
($B
Thermodynamic consistency line
azeotropic mixture
vapor-liquid equilibria
S-18593
9:20$B!A(B 9:40K302$BG.NO3X7rA4@~$rMQ$$$k(B3$B@.J,7ODj295$1UJ?9U$N=c?h?d;;$H
($B
Thermodynamic consistency line
ternary vapor-liquid equiliebria
UNIQUAC equation
S-18855
9:40$B!A(B 10:00K303$B@E;_%;%kCf5$AjD>@\:N
($BF|K\%j%U%!%$%s(B) $B!{(B($B@5(B)Freitag Joerg $B!&(B ($B@5(B)$BC];3(B $BM'7i(B $B!&(B ($B@5(B)$B:dEl(B $BK'9T(B $B!&(B ($B
Thermodynamic consistency line
vapor-liquid equilibria
static cell
S-18928
(10:00$B!A(B11:20)$B!!(B($B:BD9(B $B=ULZ(B $B>-;J(B)
10:00$B!A(B 10:20K304$B>x5$05IU6a$G$N3K2=$K$h$k;6Mp$NB,Dj(B
($BK!@/Bg4D6-1~2=(B) $B!{(B($B@5(B)$B@>3$(B $B1QM:(B $B!&(B ($BK!@/Bg%5%98&(B) ($B@5(B)$B8c6?(B $B7r0l(B
nucleation
vaporization
scattering
S-18143
10:20$B!A(B 10:40K305$BHs@~7A%l!<%6!
($B6bBtBg(B) $B!{(B($B@5(B)$BHf9>Eh(B $BM42p(B $B!&(B ($BK!@/Bg(B) $BLZB<(B $B2BJ8(B $B!&(B ($B6bBtBg(B) ($B@5(B)$B9b66(B $B7{;J(B
diffusion coefficient
ionic liquids
nonlinear laser spectroscopy
S-18370
10:40$B!A(B 11:00K306$B%(%?%N!<%k(B+$B?e(B+$B%(%9%F%k(B($B?];@%V%A%k!"?];@%"%_%k!"Mo;@%(%A%k(B)$B$N(B3$B@.J,7O$N1U1UJ?9U$H!"%(%?%N!<%k(B+$B?e(B+$B?];@%V%A%k(B+KCl$B$N(B4$B@.J,7O$N1U1UJ?9U$NB,Dj(B
($BK!@/Bg@8L?(B) $B!{(B($B@5(B)$BJR;3(B $B42Ip(B $B!&(B ($BK!@/Bg9)(B) $B_:@n(B $BBYJ?(B $B!&(B ($BK!@/Bg!#9)(B) ($B3X(B)$B:4F#(B $BCNLi(B
Bioethanol
Butyl acetate
Potassium chlorise
S-18703
11:00$B!A(B 11:20K307$B9-$$29EY!&05NO>r7o$K$*$1$k%$%*%s1UBN(B-CO2$B7O$N(BpVT$B$HEE5$EAF3EY(B
($B;:Am8&(B) ($B@5(B)$BKRLn(B $B5.;j(B $B!&(B ($B@5(B)$BA}ED(B $BA1M:(B $B!&(B $B!{(B($B@5(B)$B6b5WJ](B $B8w1{(B $B!&(B ($B%Q%J%=%K%C%/(B) $B8~;3(B $BMN(B
ionic liquid
carbon dioxide
pVT
S-18589
(11:20$B!A(B12:00)$B!!(B($B;J2q(B $BKRLn(B $B5.;j(B)
11:20$B!A(B 12:00K308[$BE8K>9V1i(B]$B%,%9%O%$%I%l!<%H$NG.NO3XE*0BDj@-$H%2%9%HJ,;R$NdF@jM-@-(B
($B:eBg1!4p9)(B) $B!{(B($B@5(B)$B?{86(B $BIp(B
Gas Hydrate
Phase equilibria
Cage occupancy
S-18405
(13:00$B!A(B14:00)$B!!(B($B:BD9(B $BIZED(B $BBgJe(B)
13:00$B!A(B 13:20K313$BD6NW3&Fs;@2=C:AGB8:_2<$K$*$1$k%]%j%+!<%\%M!<%H$N7k>=2=(B
($B9-Bg1!9)(B) $B!{66K\(B $B5.5A(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 $BHK
polycarbonate
carbon dioxide
crystallization
S-18761
13:20$B!A(B 13:40K314$B%0%k!<%W4sM?>uBV<0$r3hMQ$7$?(BCO2$BJ*M}5[<}:^$NA*DjK!(B
($B1~MQJ*@-(B) $B!{(B($B@5(B)$BBg>l(B $BLPIW(B
Group Contribution
Equation of State
CO2 Physical Absorption
S-18953
13:40$B!A(B 14:00K315$B=cJ*
($B;38}Bg1!(B) $B!{(B($B@5(B)$B>.^<(B $BLP $B!&(B ($B3X(B)$B|bAR(B $B7<(B $B!&(B ($B6eBg1!(B) ($B@5(B)$BJF_7(B $B@a;R(B $B!&(B ($B1'It9b@l(B) ($B@5(B)$BJ!CO(B $B8-<#(B
Vapor-Liquid Equilibrium
Wilson Parameter
Ester
S-1850
(14:00$B!A(B15:00)$B!!(B($B:BD9(B $BBg>l(B $BLPIW(B)
14:00$B!A(B 14:20K316$B%0%k!<%W4sM?K!$rE,MQ$7$?(BCOSMOSPACE$B$K$h$k%"%k%3!<%k(B+$B%"%k%+%s7O$N5$1UJ?9U$NAj4X(B
($B1'It6=;:(B) $B!{(B($B3X(B)$B<<9-(B $B!&(B ($B@5(B)$B2#ED(B $B $B!&(B ($B1'It9b@l(B) ($B@5(B)$BJ!CO(B $B8-<#(B $B!&(B ($B6eBg1!9)(B) ($B@5(B)$B4d0f(B $BK'IW(B
COSMOSPACE
activity coefficient
vapor liquid equilibrium
S-18749
14:20$B!A(B 14:40K317$BG;EY0MB8I=LL@Q%Q%i%a!<%?%b%G%k$K$h$kAjJ?9U$NAj4X(B
($B6eBg9)(B) $B!{(B($B@5(B)$B4d0f(B $BK'IW(B $B!&(B ($B3X(B)$B;3K\(B $BM*B@(B
Activity coefficient model
Quasi chemical
Concentration dependent surface area parameter
S-18266
14:40$B!A(B 15:00K318$B86;RCDJ,2r$K$h$k6~@^N($N?d;;K!(B
(KRI) $B!{C01)(B $B=_(B
refractive index
property prediction
QSPR
S-1865
(15:00$B!A(B16:20)$B!!(B($B:BD9(B $B4d0f(B $BK'IW(B)
15:00$B!A(B 15:20K319$B4J0W7?(BWilson$B<0$K$h$k(B3$B@.J,7O5$1UJ?9U$N?d;;(B
($BF|BgM}9)(B) $B!{(B($B@5(B)$BFJLZ(B $B>!8J(B $B!&(B ($B3X(B)$BN)@P(B $B2m $B!&(B ($B@5(B)$B>>ED(B $B909,(B $B!&(B ($B@5(B)$B7*86(B $B@6J8(B
Wilson equation
T-K Wilson equation
ASOG
S-18255
15:20$B!A(B 15:40K320$B5$1UJ?9U$K$*$1$k%$%*%s1UBN$N8z2L$N?d;;(B
($BElM}BgM}(B) $B!{(B($B@5(B)$BBg9>(B $B=$B$(B
vapor-liquid equilibria
ion liquid
solvation method
S-18581
15:40$B!A(B 16:00K321$BI8=`J(E@(BTb$B$rI,MW$H$7$J$$L56K@-J*
($BK!@/Bg@8L?(B) $B!{(B($B@5(B)$B8c6?(B $B7r0l(B $B!&(B ($B@5(B)$B@>3$(B $B1QM:(B
Critical temperature
Normal boiling point
Group contribution method
S-18737
16:00$B!A(B 16:20K322$B>o29>o05$+$iD6NW3&>uBV$K$*$1$k%"%k%3!<%k?eMO1U$NL)EY!&G4EY5sF0$NE}0lE*2r@O(B
($BElKLBg1!9)(B) $B!{(B($B@5(B)$B>.Ln(B $B9*(B $B!&(B ($B3X(B)$B8^==Mr(B $BNi;R(B $B!&(B ($B3X(B)$BA0ED(B $BM*4u(B $B!&(B ($B@5(B)$BBgED(B $B>; $B!&(B ($B@5(B)$B:4F#(B $BA1G7(B $B!&(B ($B@5(B)$BCv8T(B $B9((B
alcohol
density
viscosity
S-18748
$B9V1i%W%m%0%i%`(B
$B2=3X9)3X2q(B $BBh(B44$B2s=)5(Bg2q(B
(C) 2012 $B8x1W
Most recent update: 2012-08-20 15:02:17
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