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XG201-XG216, XG301-XG308

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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

$B:G=*99?7F|;~!'(B2013-08-20 14:03:53
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(9:00$B!A(B10:40) ($B:BD9(B $B9SLZ(B $BDgIW!&Bg>l(B $BLPIW(B)
9:00$B!A(B 9:20XG201$B%(%?%N!<%k?eMO1U$K$*$1$kD62;GH%-%c%S%F!<%7%g%s8z2L$HJ*@-CMJQ2=(B
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acoustic cavitation
ethanol aqueous solution
liquid structure
S-38355
9:20$B!A(B 9:40XG202($B9V1iCf;_(B)

100512
9:40$B!A(B 10:00XG203$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 $BK'IW(B
liquid-liquid equilibrum
concentraion dependent surface area parameter model
1-butanol+water
S-3865
10:00$B!A(B 10:20XG204$B>.7?Mn?K<0G4EY7W$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 $B=(
viscometer
uncertainty
viscosity
S-38879
10:20$B!A(B 10:40XG205$B%0%i%$%`(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 $B8w1{(B
density
viscosity
CO2 solubility
S-38804
(10:40$B!A(B11:20) ($B;J2q(B $B;y6L(B $BBgJe(B)
10:40$B!A(B 11:20XG206[$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 $B@.?.(B
refrigerants
thermophysical property
high pressure
S-38548
(11:20$B!A(B12:00) ($B;J2q(B $B?{86(B $BIp(B)
11:20$B!A(B 12:00XG208[$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
S-38262

(13:00$B!A(B14:20) ($B:BD9(B $B>>ED(B $B909,!&:4!9LZ(B $B@5OB(B)
13:00$B!A(B 13:20XG213$B?e!
($BEl9)Bg1!M}9)(B) $B!{(B($B3X(B)$BEl6?(B $B>;51(B$B!&(B ($B@5(B)$B2<;3(B $BM52p(B
pi-electron system
high temperature and pressure water
PC-SAFT equation of state
S-38376
13:20$B!A(B 13:40XG214Wilhelmy$BK!$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 $BM52p(B
O/W emulsion
interfacial tension
Wilhelmy method
S-38368
13:40$B!A(B 14:00XG215$B6bB0:xBN$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 $BHK
Sublimation
Solubilities
Metal complexes
S-38645
14:00$B!A(B 14:20XG216$B%O%m%2%sCV49%7%/%m%Z%s%?%sM6F3BN$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
S-381002
XG $B2q>l!&Bh(B 3 $BF|(B
(9:00$B!A(B11:00) ($B:BD9(B $B7*86(B $B@6J8!&DZ0f(B $BL@CK(B)
9:00$B!A(B 9:20XG301$B%$%*%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 $B@?Fs(B
ionic liquid
glyme
CO2 solubility
S-38652
9:20$B!A(B 9:40XG302GC-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 $B@a;R(B
Vapor-Liquid Equilibrium
Wilson Parameter
Reduced Pressure
S-3828
9:40$B!A(B 10:00XG303$BG.NO3X7rA4@~$rMQ$$$k1U1UJ,G[78?t$N?d;;(B
($B
Thermodynamic consistency line
liqui-liquid partition coefficient
grand correlation
S-38715
10:00$B!A(B 10:20XG304$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
S-3845
10:20$B!A(B 10:40XG305$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 $BNJN<(B
binary interaction parameter
component family method
BWR equation of state
S-38452
10:40$B!A(B 11:00XG306$B5$1UJ?9U?d;;<0$NDj?t7hDjK!(B
($BElM}BgM}(B) $B!{(B($B@5(B)$BBg9>(B $B=$B$(B
vapor-liquid equilibria
distillation
NRTL equation
S-38880
(11:00$B!A(B11:40) ($B;J2q(B $B2<;3(B $BM52p(B)
11:00$B!A(B 11:40XG307[$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
S-38843
$B9V1iH/I=%W%m%0%i%`(B
$B2=3X9)3X2q(B $BBh(B45$B2s=)5(Bg2q(B
(C) 2013 $B8x1W
Most recent update: 2013-08-20 14:03:53
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