$B9V1i(B $B;~9o(B | $B9V1i(B $BHV9f(B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $BJ,N`(B | $BHV9f(B $B | |
---|---|---|---|---|---|
$B%7%s%]%8%&%`(B <$B | |||||
(9:00$B!A(B10:40) ($B:BD9(B $B9SLZ(B $BDgIW!&Bg>l(B $BLPIW(B) | |||||
XG201 | $B%(%?%N!<%k?eMO1U$K$*$1$kD62;GH%-%c%S%F!<%7%g%s8z2L$HJ*@-CMJQ2=(B | acoustic cavitation ethanol aqueous solution liquid structure | S-38 | 355 | |
XG202 | ($B9V1iCf;_(B) | 100 | 512 | ||
XG203 | $BG;EY0MB8I=LL@Q%Q%i%a!<%?%b%G%k$K$h$k(B1-butanol+water$B7O$NAjJ?9U$NAj4X(B | liquid-liquid equilibrum concentraion dependent surface area parameter model 1-butanol+water | S-38 | 65 | |
XG204 | $B>.7?Mn?K<0G4EY7W$rMQ$$$?G4EYB,Dj$K$*$1$kIT3N$+$5$NI>2A(B | viscometer uncertainty viscosity | S-38 | 879 | |
XG205 | $B%0%i%$%`(B-$B%9%k%[%s;@%j%A%&%`1vMO1U$NL)EY!&G4EY!&Fs;@2=C:AGMO2rEY(B | density viscosity CO2 solubility | S-38 | 804 | |
(10:40$B!A(B11:20) ($B;J2q(B $B;y6L(B $BBgJe(B) | |||||
XG206 | [$B>7BT9V1i(B] $BDc(BGWP$BNdG^$N3+H/!!(B-$BB,DjAuCV$H | refrigerants thermophysical property high pressure | S-38 | 548 | |
(11:20$B!A(B12:00) ($B;J2q(B $B?{86(B $BIp(B) | |||||
XG208 | [$B>7BT9V1i(B] $B%,%9%O%$%I%l!<%H$NJ*@-8&5f$H1~MQ$X$NE83+(B | gas hydrate phase equilibria cage occupancy | S-38 | 262 | |
(13:00$B!A(B14:20) ($B:BD9(B $B>>ED(B $B909,!&:4!9LZ(B $B@5OB(B) | |||||
XG213 | $B?e! | pi-electron system high temperature and pressure water PC-SAFT equation of state | S-38 | 376 | |
XG214 | Wilhelmy$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 | O/W emulsion interfacial tension Wilhelmy method | S-38 | 368 | |
XG215 | $B6bB0:xBN$N>:2Z05$HD6NW3&Fs;@2=C:AGCf$X$NMO2rEY(B | Sublimation Solubilities Metal complexes | S-38 | 645 | |
XG216 | $B%O%m%2%sCV49%7%/%m%Z%s%?%sM6F3BN$r%2%9%HJ,;R$H$7$?:.9g%O%$%I%l!<%H7O$N9b05Aj5sF0(B | gas hydrate phase equilibria high pressure | S-38 | 1002 |