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9:00$B!A(B 9:20 | F301 | $B5U%_%;%k$rMQ$$$?0lK\:?3K;@Cj=P$K$*$1$k(BDNA$B3&LL3h@-:^$N1F6A(B ($B?@8MBg1!9)(B) $B!{(B($B3X(B)$B@PDE(B $BD>$B!&(B($B@5(B)$B4];3(B $BC#@8(B$B!&(B($B6eBg1!9)(B) $B:YLZ(B $BBnLi(B$B!&(B($B@5(B)$B8eF#(B $B2m9((B$B!&(B($B?@8MBg1!9)(B) ($B@5(B)$BBg8~(B $B5H7J(B$B!&(B($B@5(B)$B>>;3(B $B=(?M(B | DNA micelle extract
| 4-f | 683 |
9:20$B!A(B 9:40 | F302 | $B%/%i%&%s%(!<%F%k$H$N:x7A@.$rMxMQ$7$??e@-FsAj7O$K$*$1$k%?%s%Q%/ ($B5\:jBg9)(B) $B!{(B($B@5(B)$BBgEg(B $BC#Li(B$B!&(B$BKv$B!&(B($B3X(B)$B9CHe(B $B@i2F(B$B!&(B($B@5(B)$BGO>l(B $BM3@.(B | aqueous two-phase system crown ether protein
| 4-f | 166 |
9:40$B!A(B 10:00 | F303 | W/O/W$B%(%^%k%7%g%sK!$K$h$kL55!Cf6uHyN3;R$ND4@=(B ($BBgJ,Bg9)(B) $B!{(B($B3X(B)$B;05\(B $B?5Li(B$B!&(B($B@5(B)$BT"J,(B $B=$;0(B$B!&(B($B@5(B)$BDL:e(B $B1I0l(B$B!&(B($B@5(B)$BJ?ED(B $B@?(B | microballoon emulsion interfacial reaction
| 4-f | 159 |
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10:00$B!A(B 10:20 | F304 | $B%W%m%j%s%"%k%-%kM6F3BN$N9g@.$H%l%"%a%?%kJ,N%!&2s<}$X$N1~MQ(B ($B5\:jBg9)(B) $B!{(B($B3X(B)$B6b4](B $B?5B@O:(B$B!&(B($B@5(B)$BBgEg(B $BC#Li(B$B!&(B($B@5(B)$BGO>l(B $BM3@.(B | rare metal separation extraction
| 4-f | 627 |
10:20$B!A(B 10:40 | F305 | $B8~N.@\?(%9%W%l! ($BEl9)BgM}9)(B) $B!{(B($B3X(B)$BA}ED(B $BIRLi(B$B!&(B($B@5(B)$B$O$P$-(B $B9-82(B$B!&(B($B@5(B)$B9>F,(B $BN50l(B | spray column coal tar absorption oil extraction rate
| 4-f | 450 |
10:40$B!A(B 11:00 | F306 | $B%$%*%s1UBN;Y;}1UKl$K$*$1$k%3!<%k%?!<%k5[<}L}$NF)2a(B ($BEl9)BgM}9)(B) $B!{(B($B3X(B)$BEgED(B $B5AG7(B$B!&(B($B@5(B)$B$O$P$-(B $B9-82(B$B!&(B($B@5(B)$B9>F,(B $BN50l(B | ionic liquid supported liquid membrane coal tar absorption oil
| 4-f | 446 |
(11:00$B!A(B12:00)$B!!(B($B:BD9(B $B9>F,!!N50l(B) |
11:00$B!A(B 11:20 | F307 | $B%8%"%_%I7OG[0L;R$rMQ$$$?%$%*%s1UBNCj=P7O$N9=C[(B ($B86;RNO5!9=(B) $B!{(B($B@5(B)$B2<>r(B $B98;JO:(B$B!&(B$BAR66(B $B7r2p(B$B!&(B($B@5(B)$BD9Fl(B $B90?F(B$B!&(B($B6eBg1!9)(B) ($B@5(B)$B5WJ]ED(B $BIY@8;R(B$B!&(B($B@5(B)$B8eF#(B $B2m9((B | ionic liquids solvent extraction separation
| 4-f | 119 |
11:20$B!A(B 11:40 | F308 | $B%+%k%\%s;@7O?75,Cj=P:^$K$h$k4uEZN`6bB0$N%$%*%s1UBNCj=P(B ($B6eBg1!9)(B) $B!{(B($B@5(B)$B5WJ]ED(B $BIY@8;R(B$B!&(B($B3X(B)$B>.Lx(B $BM52p(B$B!&(B($B86;RNO5!9=(B) ($B@5(B)$B2<>r(B $B98;JO:(B$B!&(B($B6eBg1!9)(B) ($B@5(B)$BCfEg(B $B0l5*(B$B!&(B($B@5(B)$B?@C+(B $BE5Jf(B$B!&(B($B@5(B)$B8eF#(B $B2m9((B | ionic liquids rare earth extraction
| 4-f | 443 |
11:40$B!A(B 12:00 | F309 | $BF};@J,N%$X$N%$%*%s1UBN4^?;Cf6u;eKl$N1~MQ(B ($BF1;V$B!&(B($B@5(B)$B>>K\(B $BF;L@(B$B!&(B($B@5(B)$B6aF#(B $BOB@8(B$B!&(B($BK-EDCf8&(B) ($B@5(B)$BEhB<(B $BN4(B$B!&(B($B@5(B)$BDT(B $B@5CK(B | Liquid membrane Lactic acid Hollow fiber
| 4-f | 178 |
12:00$B!A(B 13:00 | $BCk5Y$_(B |
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13:00$B!A(B 13:20 | F313 | $B%P%$%*%(%?%N!<%kG;=L%W%m%;%9$N(BHIDiC$B2=$N8!F$(B ($B4X@>2=3X(B) $B!{(B($B@5(B)$BJR2,(B $BK.IW(B$B!&(B($B@5(B)$BLnED(B $B=(IW(B$B!&(B($B@5(B)$B;3O)(B $B42;J(B$B!&(B($B@5(B)$BARC+(B $B?-9T(B$B!&(B($B@5(B)$B6bED(B $BK|J?(B$B!&(B($B@5(B)$B8~ED(B $BCi90(B | Energy-saving Distillation Bioethanol Production HIDiC
| 4-c | 17 |
13:20$B!A(B 13:40 | F314 | $BH/9Z1UM3Mh(BL-$BF};@$N%(%9%F%k2=!"2C?eJ,2r$K$h$k@:@=(B ($BElG@9)Bg9)(B) $B!{(B($B@5(B)$BK\B?(B $BB@$B!&(B($B@5(B)$B9q4c(B $B9'M:(B$B!&(B$B2CF#(B $BBYM5(B | lactic acid reactive distillation fermentation broth
| 4-c | 755 |
13:40$B!A(B 14:00 | F315 | Application of a Fully Thermally Coupled Distillation Column for Practical Azeotropic Separation (Dong-A U.) Sung Ick Gi$B!&(B$B!{(B($B@5(B)Kim Young Han | Energy-Efficient Distillation Thermally Coupled Distillation Azeotropic Distillation
| 4-c | 26 |
(14:00$B!A(B15:00)$B!!(B($B:BD9(B $B;3K\!!=( |
14:00$B!A(B 14:20 | F316 | $B%J%,%*%+!!%Q%C%-%s%0!V%9!<%Q!<(BH$B%Q%C%/!W(B2$BG\$N=hM}NL$rC#@.$9$k5,B'= ($B>xN1MQ5,B'= | Linear Flow High Liquid Hold High Operating Capacity
| 4-c | 39 |
14:20$B!A(B 14:40 | F317 | $BC1>xN1 ($BF|BgM}9)(B) $B!{(B($B3X(B)$BK\66(B $B8-E5(B$B!&(B($B%*%a%,%7%_%e%l!<%7%g%s(B) ($B@5(B)$B2#;3(B $B9n8J(B$B!&(B($BF|BgM}9)(B) ($B@5(B)$B>>ED(B $B909,(B$B!&(B($B@5(B)$B7*86(B $B@6J8(B$B!&(B($B@5(B)$BFJLZ(B $B>!8J(B | Simple Distillation Estimation of Components Change of Temperature
| 4-c | 217 |
14:40$B!A(B 15:00 | F318 | TAME$B9g@.H?1~>xN1%W%m%;%9$NHsDj>o%7%_%e%l!<%7%g%s(B ($B;37ABg1!M}9)(B) $B!{(B($B3X(B)$B0f9x(B $BC#O:(B$B!&(B($B@5(B)$B>>ED(B $B7=8g(B$B!&(B($B;:Am8&(B) ($B@5(B)$BCf4d(B $B>!(B$B!&(B($B@5(B)$BBg?9(B $BN4IW(B | reactive distillation dynamic simulation TAME
| 4-c | 324 |
(15:00$B!A(B16:00)$B!!(B($B:BD9(B $BFJLZ!!>!8J(B) |
15:00$B!A(B 15:20 | F319 | $B= ($BElM}BgM}(B) $B!{(B($B@5(B)$BBg9>(B $B=$B$(B | flooding packed column distillation
| 4-c | 613 |
15:20$B!A(B 15:40 | F320 | $B= ($BLZB<2=9)5!(B) $B!{@>ED(B $B<~9T(B$B!&(B($B@5(B)$BCf@>(B $B=S@.(B$B!&(B$BB-N)(B $B>0fb(B$B!&(B($B;:Am8&(B) ($B@5(B)$BCf4d(B $B>!(B | HIDiC Distillation proccess design
| 4-c | 761 |
15:40$B!A(B 16:00 | F321 | $B5$1UJ?9U$K5Z$\$91v8z2L$rMxMQ$7$?:.9gGQ;@$+$i$N;@$N>xN1J,N%(B ($B4X@>Bg4D6-ET;T9)(B) ($B@5(B)$B;3K\(B $B=($B!&(B$B!{(B($B3X(B)$BIMED(B $BM5;0(B$B!&(B($B3X(B)$BJ?Ln(B $B@5?M(B$B!&(B$BD.Ln(B $B>-9((B$B!&(B($B?9ED2=3X9)6H(B) $BI4ED(B $BK.t!(B | waste acid distillation recycle
| 4-j | 597 |