$B9V1i(B $B;~9o(B | $B9V1i(B $BHV9f(B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $BJ,N`(B | $BHV9f(B $B | |
---|---|---|---|---|---|
$B%7%s%]%8%&%`(B <$B0!NW3&!&D6NW3&N.BN$r4^$`7O$NJ*@-8&5f$N:GA0@~(B> | |||||
(10:00$B!A(B11:20) ($B:BD9(B $B;y6L(B $BBgJe!&9&(B $B>;0l(B) | |||||
R104 | Chemoselective hydrogenation of chloronitrobenzene in supercritical carbon dioxide using Pd supported on heteroatom substituted MCM-41 | supercritical carbon dioxide hydrogenation chloronitrobenzene | S-13 | 113 | |
R105 | $B%J%N6u7dFb$K$*$1$kNW3&E@9_2<(B | Critical point Nanopore Molecular dynamics | S-13 | 175 | |
R106 | $BFs@.J,:.9gN.BN$NNW3&E@6aK5$K$*$1$k2a>j%(%s%?%k%T!<$NFC0[E*5sF0$NM=B,(B II. $BNW3&50@W$H2a>j%(%s%?%k%T!<$rF@$k>uBV$N(Bp-T$BLL>e$G$N0LCV4X78(B | excess enthalpy critical locus binary mixture | S-13 | 917 | |
R107 | $BNW3&E@6aK5$G$N%Y%s%<%s(B+$B%7%/%m%X%-%5%s7O$N2a>j%(%s%?%k%T!<-6(B | Excess enthalpy Critical Point Binary fluid mixtures | S-13 | 1004 | |
(11:20$B!A(B12:00) ($B;J2q(B $BAj_7(B $B?r;K(B) | |||||
R108 | [$B>7BT9V1i(B] $BD6NW3&N.BNCf$G$NEE2Y0\F0H?1~$H%W%m%H%s0\F0H?1~(B | electron transfer proton transfer supercritical fluid | S-13 | 111 | |
(13:00$B!A(B14:40) ($B:BD9(B $BC]NS(B $BNI9@!&Aj_7(B $B?r;K(B) | |||||
R113 | $B%X%-%5%s(B+$BB?J,;6%]%j%(%A%l%s7O$N9b299b05AjJ?9U(B | polydisperse polyethylene phase equilibria Sanchez-Lacombe EOS | S-13 | 642 | |
R114 | $B%(%A%l%s(B/ $B?];@%S%K%k6&=E9gBN(B(EVA)$B@=B$$K4X$9$k(B4$B@.J,7OAjJ?9U$N%7%_%e%l!<%7%g%s(B | phase equilibria poly(ethylene-co-vinyl acetate) Sanchez-Lacombe equation of state | S-13 | 383 | |
R115 | $B;g302D;kJ,8wK!$rMQ$$$?K0OBMO2r05NOC5:wK!$K$h$kD6NW3&(BCO2$BCf$NM-5!J*$NMO2rEYB,Dj(B | spectroscopic solubility measurement supercritical carbon dioxide organic compounds | S-13 | 1007 | |
R116 | $BJ,;R>pJs$+$i$NG[0L?tM=B,$rMQ$$$?>uBVJ}Dx<0$K$h$kD6NW3&Fs;@2=C:AG$X$NMO2rEY$N?d;;(B | drug solubility coordination number supercritical carbon dioxide | S-13 | 477 | |
R117 | $BD6NW3&Fs;@2=C:AGCf$N%>%k%2%kK!$K$h$k%J%NN3;R4^M-Kl$N:n@=$K$*$1$k5$1UJ?9U$NGD0.(B | vapor-liquid equilibrium supercritical carbon dioxide silica alkoxide | S-13 | 371 | |
(14:40$B!A(B16:20) ($B:BD9(B $B:4F#(B $BA1G7!&2<;3(B $BM52p(B) | |||||
R118 | $BE7A3J*4^M-5!G=@-@.J,$ND6NW3&N.BN@:N1$N%b%G%k2=$K8~$1$?5$1UJ?9U$NB,Dj(B | supercritical fluid vapor-liquid equilibrium rectification | S-13 | 550 | |
R119 | CO2-$B%a%?%N!<%k:.9gN.BNCf$K$*$1$kM-5!2=9gJ*$NL58B4u | Taylor dispersion CO2 mixture Diffusion coefficient | S-13 | 801 | |
R120 | $BD6NW3&5Z$S1UBN>uBVCf$K$*$1$k%H%j%9(B($B%"%;%A%k%"%;%H%J%H(B)$B%"%k%_%K%&%`$N3H;678?t$NB,Dj$HAj4X(B | diffusion supercritical fluid chromatography metal complex | S-13 | 925 | |
R121 | $BFs;@2=C:AGKDD% | CO2-Expanded Liquid Polymer Solution Viscosity | S-13 | 112 | |
R122 | $BFs;@2=C:AG2C05$K$h$kM;E@9_2<$NG.NO3XE*2r@O(B | carbon dioxide equation of state phase equilibrium | S-13 | 58 | |
$B3X@8>^I=>4<0(B |