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E$B2q>l(B $BBh(B2$BF|(B |
(10:00$B!A(B11:00)$B!!(B($B:BD9(B $B5WJ]ED(B $BIY@8;R(B) |
10:00$B!A(B 10:20 | E204 | 1,3-$B%W%m%Q%s%8%*!<%k$NCj=PJ,N%(B
($BF1;V $B!&(B ($B@5(B)$B>>K\(B $BF;L@(B $B!&(B ($B@5(B)$B6aF#(B $BOB@8(B | Extraction 1,3-Propanediol Fermentation
| 4-f | 234 |
10:20$B!A(B 10:40 | E205 | $B?eMO@-%]%j%^!<$G%3!<%F%#%s%0$7$?Cj=P:^4^?;
($BKL6eBg9q:]4D6-9)(B) $B!{(B($B@5(B)$B@>IM(B $B>OJ?(B $B!&(B ($B3X(B)$BLZH((B $B2BF`;R(B $B!&(B ($B3X(B)$B@n:j(B $B0+(B $B!&(B ($B@5(B)$B5HDM(B $BOB<#(B | solvent impregnated resin separation rare earth metal
| 4-f | 210 |
10:40$B!A(B 11:00 | E206 | $B%0%"%K%8%s$rG[0L4p$H$9$kCj=P;nLt$K$h$k1v;@MO1U$+$i$N5.6bB0%$%*%s$NCj=P5sF0(B
($B5\:jBg9)(B) $B!{(B($B3X(B)$BKc@8(B $BCNN$(B $B!&(B ($BET>k9)@l(B) ($B@5(B)$B4d7'(B $BH~F`;R(B $B!&(B ($B5\:jBg9)(B) ($B@5(B)$BBgEg(B $BC#Li(B $B!&(B ($B@5(B)$BGO>l(B $BM3@.(B | extraction rare metal membrane transport
| 4-f | 662 |
(11:00$B!A(B12:00)$B!!(B($B:BD9(B $B@>IM(B $B>OJ?(B) |
11:00$B!A(B 11:20 | E207 | $B%$%*%s1UBNCj=P7O$K$*$1$kE4$+$i$N4uEZN`6bB0$NA*BrE*Cj=PJ,N%(B
($B6eBg1!9)(B) $B!{(B($B3X(B)$BGO>l(B $BM:;0(B $B!&(B ($B@5(B)$B5WJ]ED(B $BIY@8;R(B $B!&(B ($B86;RNO5!9=(B) ($B@5(B)$B2<>r(B $B98;JO:(B $B!&(B ($B6eBg1!9)(B) ($B@5(B)$B?@C+(B $BE5Jf(B $B!&(B ($B@5(B)$B8eF#(B $B2m9((B | rare earth metals ionic liquid liquid membrane
| 4-f | 452 |
11:20$B!A(B 11:40 | E208 | $B%$%*%s1UBNA*BrK!$rMQ$$$k%A%*%U%'%sC&N2$N$?$a$N5$1UJ?9U?d;;%G%b%W%m%0%i%`$N
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| 4-f | 504 |
11:40$B!A(B 12:00 | E209 | Selection of Amine Absorbents for CO2 Capture
(RITE) $B!{(B($B@5(B)Chowdhury Firoz Alam $B!&(B Yamada Hidetaka $B!&(B Higashii Takayuki $B!&(B (NSC) Onoda Masami $B!&(B (RITE) ($B@5(B)Kazama Shingo | Absorption Carbon dioxide CO$2$ capture
| 4-d | 89 |
|
(13:00$B!A(B14:00)$B!!(B($B:BD9(B $BB?ED(B $B7JFsO:(B) |
13:00$B!A(B 13:20 | E213 | O/W$B%(%^%k%7%g%s$N2<8~N.%G%C%I%(%s%I_I2a$K$*$1$k_I2aB.EY$NB%?J8z2L(B
($BL>Bg1!9)(B) $B!{(B($B3X(B)$BAb(B $BC#7<(B $B!&(B ($B@5(B)$BF~C+(B $B1Q;J(B | filtration O/W emulsion cake resistance
| 4-b | 514 |
13:20$B!A(B 13:40 | E214 | $B4uGv%3%m%$%I$NA4AK;_7?DjB.5Z$SDj05@:L)%1!<%/_I2a$K$*$1$kKlJD:I$NI>2A(B
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| 4-b | 495 |
13:40$B!A(B 14:00 | E215 | $BJB9TJ?KlHD7?1s?4%;%k$K$h$k%?%s%Q%/
($B;38}Bg1!M}9)(B) $B!{(B($B3X(B)$BF#K\(B $B=S(B $B!&(B ($B1'It%U%#%k%`(B) ($B@5(B)$BLx86(B $B9(51(B $B!&(B ($B;38}Bg1!M}9)(B) ($B@5(B)$BCfAR(B $B1QM:(B | centrifugal ultrafiltration cross-flow filtration cake filtration
| 4-b | 468 |
(14:00$B!A(B15:20)$B!!(B($B:BD9(B $BJR6M(B $B@?G7(B) |
14:00$B!A(B 14:20 | E216 | $BC:;@%+%k%7%&%`%\%G%#!<%U%#!<%I_I2a!?%W%j%3!<%H_I2aJ;MQJ}<0$K$h$k%U%_%s;@MO1U$NDj058B30_I2aFC@-(B
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| 4-b | 277 |
14:20$B!A(B 14:40 | E217 | $BA!0]$m:`$r;H$C$?5^B.$m2a4o$K$*$1$kJa=88zN(1F6A0x;R$N@0M}(B
($B7*ED9)6H(B) $B!{B?ED(B $B7JFsO:(B $B!&(B $BBg_7(B $B8x?-(B $B!&(B ($BL>Bg1!9)(B) ($B@5(B)$BDX(B $B=_0lO:(B | $B$m2a(B $B%b%G%k<0(B $B9bJ,;R6E=8:^(B
| 4-b | 492 |
14:40$B!A(B 15:00 | E218 | $BN.BN!&8GBNO"@.%7%_%e%l!<%7%g%s$K$h$k_I:`Dq93$N?d;;(B
($BF1;Ve(B $BMNJ?(B $B!&(B ($BF1;V $B!&(B ($BF1;V $B!&(B ($B@5(B)$BGr@n(B $BA19,(B $B!&(B ($B@5(B)$BF|9b(B $B=E=u(B | lattice Boltzmann method fluid-structure interaction microfilteration
| 4-b | 568 |
15:00$B!A(B 15:20 | E219 | $BM6EE1KF0$K$h$k%(%?%N!<%kCfJ,;6C:AGHyN3;R$NJ,N%(B
($B5~Bg1!9)(B) $B!{(B($B3X(B)$B4d:j(B $BM[2p(B $B!&(B ($B@5(B)$B:4Ln(B $B5*>4(B $B!&(B ($B@5(B)$BEDLg(B $BH%(B | dielectrophoresis particle separation
| 4-b | 343 |
(15:20$B!A(B16:20)$B!!(B($B:BD9(B $B@n:j(B $B7rFs(B) |
15:20$B!A(B 15:40 | E220 | $BEE>l2<$N05L)D@9_2aDx(B
($B:eI\Bg1!9)(B) $B!{(B($B@5(B)$BEDCf(B $B9'FA(B $B!&(B $B2CF#(B $B90 $B!&(B $BF#86(B $B7r;J(B $B!&(B ($B@5(B)$B4dED(B $B@/;J(B | Solid-Liquid Separation Electroforced Sedimentation Current Density
| 4-b | 637 |
15:40$B!A(B 16:00 | E221 | $BG4EZ%U%m%C%/7|By1U$K$*$1$k3&LLD@9_B.EY<0$NF3=P$HE,MQ(B
($B0q>kBgG@(B) $B!{(B($B@5(B)$BBg0f(B $B@aCK(B $B!&(B $BCf@P(B $B9nLi(B $B!&(B $B@FF#(B $BBsLi(B $B!&(B $B?eLn(B $B9'B@O:(B $B!&(B $B@>B<(B $BF`DE4u(B | flocculated-suspension settlimg-velocity permeability
| 4-b | 595 |
16:00$B!A(B 16:20 | E222 | kHz$BBSD62;GH>H
($B@EBg9)(B) $B!{(B($B3X(B)$BCfB<(B $BM4B@(B $B!&(B ($B@EBgAO2J1!(B) ($B@5(B)$Bc7F#(B $BN4G7(B | Solid-liquid separation Ultrasound Acoustic cavitation bubble
| 4-b | 12 |
(16:20$B!A(B17:40)$B!!(B($B:BD9(B $B4dED(B $B@/;J(B) |
16:20$B!A(B 16:40 | E223 | $B:.9gMO1U$K$*$1$kD62;GH>H
($B0&I2Bg1!M}9)(B) $B!{(B($B@5(B)$B@n:j(B $B7rFs(B $B!&(B $BT"85(B $B>49((B $B!&(B ($B3X(B)$B0KF#(B $B5W9@(B | Freeze concentration Ultrasonic irradiation Number of solute
| 4-b | 44 |
16:40$B!A(B 17:00 | E224 | $B?6$H$&E`7kG;=L$K$h$kMO1U$NG;=LFC@-(B
($BL>Bg1!9)(B) $B!{(B($B@5(B)$BJR6M(B $B@?G7(B $B!&(B ($B3X(B)$B2,ED(B $BOBG7(B $B!&(B ($B@5(B)$BF~C+(B $B1Q;J(B $B!&(B ($B0&I2Bg1!M}9)(B) ($B@5(B)$B@n:j(B $B7rFs(B | freeze concentration shaking separation
| 4-b | 491 |
17:00$B!A(B 17:20 | E225 | $BD62;GHL82=J,N%$K$*$1$k%_%9%HNd5Q6E=L2aDx$N>h?t8z2L(B
(NAMtech) $B!{(B($B@5(B)$B>>1:(B $B0lM:(B $B!&(B ($B@5(B)$B? $B!&(B ($B@5(B)$B0BF#(B $BM34u;R(B | ultrasound atomization mist condensation
| 4-i | 591 |
17:20$B!A(B 17:40 | E226 | $B3IYB8G1UN.F0AX$K$h$k%7!<%HJR:`NAF1;N$NL)EY:9J,N%(B
($B@EBg9)(B) $B!{(B($B@5(B)$BN)85(B $BM:<#(B $B!&(B $BA0ED(B $B>MJ?(B $B!&(B ($B3X(B)$BF;1[(B $BB@5WO:(B $B!&(B ($BF|K\%j%U%!%$%s(B) ($B@5(B)$B:dEl(B $BK'9T(B $B!&(B ($B@5(B)$BA0ED(B $B@58c(B | fluidized bed density difference separation
| 4-j | 287 |
E$B2q>l(B $BBh(B3$BF|(B |
(9:40$B!A(B11:00)$B!!(B($B:BD9(B $B@n4nED(B $B1Q9'(B) |
9:40$B!A(B 10:00 | E303 | $B%O%K%+%`5[Ce%m!<%?$rMQ$$$?=|<>5!$N@-G=8~>e5Z$S>J%(%M@-$K4X$9$k8&5f(B
($B@>It5;8&(B) $B!{(B($B@5(B)$B6b(B $B0NNO(B | Honeycomb rotor Adsorption Energy saving
| 4-e | 678 |
10:00$B!A(B 10:20 | E304 | $B1v2=0!1t$rMQ$$$?LtIJIj3hK!$K$h$k3h@-C:$N@=B$(B
($B4X@>Bg4D6-ET;T9)(B) $B!{(B($B@5(B)$BNS(B $B=g0l(B $B!&(B $B5H;3(B $B7D(B | Activated carbon Chemical activation Biomass
| 4-e | 554 |
10:20$B!A(B 10:40 | E305 | $B%P%$%*%^%9C:2=J*$K$h$k%+%I%_%&%`=|5nFC@-$N8!F$(B
($BElBg@88&(B) $B!{(B($B@5(B)$BF#0f(B $BN4IW(B $B!&(B ($BL@<#BgM}9)(B) $B?7Gw(B $B>;;K(B $B!&(B ($BElBg@88&(B) $BF#ED(B $BMN?r(B $B!&(B ($B@5(B)$BGwED(B $B>O5A(B | biomass charcoal cadmium
| 4-e | 485 |
10:40$B!A(B 11:00 | E306 | $B3F~%a%=B?9&BN$N?e>x5$6&B8>r7o2<$K$*$1$kFs;@2=C:AG5[CeFC@-I>2A(B
(NAIST) $B!{(B($B3X(B)$B@>:d(B $BMNJe(B $B!&(B (RITE) $BEOIt(B $B5#(B $B!&(B ($B@5(B)$BM>8l(B $B9nB'(B | Separation Carbon-dioxide adsorption
| 4-e | 309 |
(11:00$B!A(B12:00)$B!!(B($B:BD9(B $BK>7n(B $BOBGn(B) |
11:00$B!A(B 11:20 | E307 | $B%?%s%Q%/
($B?@8MBg1!9)(B) $B!{(B($B3X(B)$B;{Eg(B $BBY $B!&(B $BIpED(B $B;VF`G5(B $B!&(B ($B6eBg1!9)(B) ($B@5(B)$B8eF#(B $B2m9((B $B!&(B ($B?@8MBg1!9)(B) ($B@5(B)$B>>;3(B $B=(?M(B $B!&(B ($B@5(B)$B4];3(B $BC#@8(B | Precious metal ion Biosorption Mechanism
| 4-e | 307 |
11:20$B!A(B 11:40 | E308 | $BN22+86;R$HCbAG86;R$rM-$9$k?75,5[Ce:^$N9g@.$H6b(B($B-7(B)$B$*$h$SGr6b(B($B-8(B)$B$N5[CeJ?9U(B
($BET>k9b@l(B) $B!{(B($B@5(B)$B4d7'(B $BH~F`;R(B $B!&(B ($B3X(B)$B1WN1(B $BOB7C(B $B!&(B ($B5\:jBg9)(B) ($B@5(B)$BGO>l(B $BM3@.(B | adsorption platinum equilibrium
| 4-e | 285 |
11:40$B!A(B 12:00 | E309 | $BG[0L;R$H
($B:42lBg1!(B) $B!{(B($B@5(B)$B@n4nED(B $B1Q9'(B $B!&(B ($B:42lBgM}9)(B) ($B3X(B)$BC]B<(B $B90L@(B $B!&(B ($B:42lBg1!(B) ($B@5(B)$BBgEO(B $B7<2p(B | germanium complexation adsorption
| 4-e | 176 |
F$B2q>l(B $BBh(B1$BF|(B |
(9:20$B!A(B10:40)$B!!(B($B:BD9(B $B@6=;(B $B2EF;(B) |
9:20$B!A(B 9:40 | F102 | $B%"%k%_%N%j%s;@1v7O%<%*%i%$%H(BAlPO4-18$B$NGvKl2=(B
($BAaBgM}9)(B) ($B@5(B)$B>>J}(B $B@5I'(B $B!&(B $B!{(B($B3X(B)$B;0IS(B $B=a(B $B!&(B ($B3X(B)$BARK\(B $B7I;K(B $B!&(B ($B@5(B)$B4X:,(B $BBY(B $B!&(B ($B@5(B)$B5FCO(B $B1Q0l(B | AlPO4-18 membrane H2O/AcOH separation
| 4-a | 395 |
9:40$B!A(B 10:00 | F103 | NaY$B7?%<%*%i%$%HKl$NKl7A@.2aDx(B
($BAaBgM}9)(B) ($B@5(B)$B>>J}(B $B@5I'(B $B!&(B $B!{(B($B3X(B)$BK-ED(B $B??6W(B $B!&(B ($B3X(B)$B8EH*(B $BBY2p(B $B!&(B ($B@5(B)$B4X:,(B $BBY(B $B!&(B ($B@5(B)$B5FCO(B $B1Q0l(B | membrane formation dehydration Y-type zeolite
| 4-a | 400 |
10:00$B!A(B 10:20 | F104 | $B@PC:3%$r86NA$H$9$k%<%*%i%$%HKl$N@=Kl$HF)2aJ*@-(B
($B;38}Bg1!M}9)(B) ($B3X(B)$B>.Eg(B $B=MJ?(B $B!&(B $BGrAR(B $BLP@8(B $B!&(B ($B@5(B)$B7'@Z(B $B@t(B $B!&(B ($B@5(B)$BEDCf(B $B0l9((B $B!&(B $B!{(B($B@5(B)$B4nB?(B $B1QIR(B | zeolite membrane coal fly ash pervaporation
| 4-a | 240 |
10:20$B!A(B 10:40 | F105 | SAPO-34$BKl$N>x5$F)2aFC@-$HF)2a5!9=(B
($B:eBg1!4p9)(B) $B!{(B($B3X(B)$BW"ED(B $BM:0lO/(B $B!&(B $BEOIt(B $BOB@8(B $B!&(B ($B@5(B)$BFbED(B $B9,L@(B $B!&(B ($B@5(B)$B9>F,(B $BLw9,(B $B!&(B ($B@5(B)$B@>;3(B $B7{OB(B | zeolite membrane SAPO-34 VP
| 4-a | 216 |
(10:40$B!A(B12:00)$B!!(B($B:BD9(B $B4nB?(B $B1QIR(B) |
10:40$B!A(B 11:00 | F106 | MOR$BKl$K$h$k?e!??];@>x5$F)2aJ,N%5sF0$N8!F$(B
($BAaBgM}9)(B) ($B@5(B)$B>>J}(B $B@5I'(B $B!&(B $B!{(B($B3X(B)$BFjEg(B $B2m=S(B $B!&(B ($B3X(B)$B:#@>(B $BM&J?(B $B!&(B ($B@5(B)$B4X:,(B $BBY(B $B!&(B ($B@5(B)$B5FCO(B $B1Q0l(B | mordenite membrane H2O/AcOH separation
| 4-a | 407 |
11:00$B!A(B 11:20 | F107 | NaMOR$B7?Kl$rMQ$$$??];@$N%(%9%F%k2=KlH?1~4o$K$*$1$k?e$NF)2a5sF0$N8!F$(B
($BAaBgM}9)(B) ($B@5(B)$B>>J}(B $B@5I'(B $B!&(B $B!{(B($B3X(B)$BJ?0f(B $BB@0lO/(B $B!&(B $BCf;3(B $B6G(B $B!&(B ($B@5(B)$B4X:,(B $BBY(B $B!&(B ($B@5(B)$B5FCO(B $B1Q0l(B | membrane reactor esterification mordenite membrane
| 4-a | 389 |
11:20$B!A(B 11:40 | F108 | $B%<%*%i%$%H@:L)_I2aKl$N:n@=$H$=$NF)2aFC@-(B
($B $B!&(B $BHSED(B $B9,Fs(B $B!&(B $BCS>e(B $B??MxF`(B | zeolite membrane microfiltration crystal morphology
| 4-a | 70 |
11:40$B!A(B 12:00 | F109 | $B?(G^Kl%3%s%?%/%?!<$rMQ$$$??e=hM}(B
($B;38}Bg9)(B) $B!{(B($B@5(B)$B7'@Z(B $B@t(B $B!&(B (ICSC) Nowak Pawel | membrane cataltic membrane reactor water treatment
| 4-a | 613 |
|
(13:00$B!A(B14:20)$B!!(B($B:BD9(B $B4X:,(B $BBY(B) |
13:00$B!A(B 13:20 | F113 | $BC:2=?eAGA*BrF)2a%7%j%+J#9gKl$N@=Kl>r7o8!F$(B
($B>;3(B $B3(H~(B $B!&(B ($B3X(B)$BFb3$(B $B7C2p(B $B!&(B $B9u>B(B $BNI2p(B $B!&(B $B2OK\(B $B9b;V(B $B!&(B ($B@5(B)$BLnB<(B $B4490(B | silica hybrid membrane counter diffusion CVD high temperature hydrocarbon separation
| 4-a | 4 |
13:20$B!A(B 13:40 | F114 | POSS (polyhedral oligomeric silsesquioxane)$B$rMQ$$$?%7%j%+Kl$N:n@=$H5$BNF)2aFC@-(B
($B9-Bg1!9)(B) $B!{(B($B@5(B)$B6b;X(B $B@58@(B $B!&(B ($BElM}Bg1!M}9)(B) $B1vED(B $BN49-(B $B!&(B $B74;J(B $BE7Gn(B $B!&(B ($B9-Bg1!9)(B) ($B@5(B)$B5H2,(B $BJ~5W(B $B!&(B ($B@5(B)$BETN1(B $BL-N;(B | Silica membrane Sol-gel Carbon dioxide
| 4-a | 286 |
13:40$B!A(B 14:00 | F115 | $B%a%=9&%7%j%+!?%]%j%$%_%IJ#9gKl$NF)2aJ*@-(B
($B;38}Bg1!M}9)(B) $B $B!&(B ($B3X(B)$BEgFb(B $BH~9,(B $B!&(B ($B@5(B)$B7'@Z(B $B@t(B $B!&(B ($B@5(B)$BEDCf(B $B0l9((B $B!&(B $B!{(B($B@5(B)$B4nB?(B $B1QIR(B | mesoporous silica polyimide gas separation
| 4-a | 241 |
14:00$B!A(B 14:20 | F116 | $B%a%A%k%7%/%m%X%-%5%sC&?eAGKlH?1~4o$rA[Dj$7$?%7%j%+Kl$NBQ5W@-$HH?1~86NA5Z$S@8@.J*$,M?$($k1F6A(B
($B9)3X1!Bg9)(B) $B!{(B($B@5(B)$B@%2<(B $B2mGn(B $B!&(B ($B@5(B)$B@V>>(B $B7{ $B!&(B (JX$BF|9[F|@P%(%M%k%.!<(B) $B@%@n(B $BFX;J(B $B!&(B ($B9)3X1!Bg9)(B) ($B@5(B)$BCfHx(B $B??0l(B | silica hydrogen permselective membrane chemical vapor deposition
| 4-a | 113 |
(14:20$B!A(B15:40)$B!!(B($B:BD9(B $BLnB<(B $B4490(B) |
14:20$B!A(B 14:40 | F117 | Layer-by-layer$BK!$rMQ$$$?%7%j%+GvKl$rJ,N%AX$H$9$kL55!(BUF$BKl$N:n@=(B
($B?@8MBg1!9)(B) $B!{(B($B3X(B)$B9bED(B $Bb+0l(B $B!&(B ($B@5(B)$BF#0f(B $B><9((B $B!&(B ($B@5(B)$B:4Gl(B $BBgJe(B $B!&(B ($B@5(B)$BBg8~(B $B5H7J(B $B!&(B ($B@5(B)$B@P?@(B $BE0(B $B!&(B ($B@5(B)$B?@Hx(B $B1Q<#(B $B!&(B ($B@5(B)$B4];3(B $BC#@8(B $B!&(B ($B@5(B)$B>>;3(B $B=(?M(B | Layer-by-layer method inorganic membrane water treatment membrane
| 4-a | 442 |
14:40$B!A(B 15:00 | F118 | $BM-5!%O%$%V%j%C%I%7%j%+Kl$K$h$kM-5!?eMO1U$N?;F)5$2=C&?e(B
($B9-Bg1!9)(B) $B $B!&(B ($B@5(B)$B6b;X(B $B@58@(B $B!&(B ($B@5(B)$B5H2,(B $BJ~5W(B $B!&(B $B!{(B($B@5(B)$BETN1(B $BL-N;(B | hybrid silica pervaporation dehydration
| 4-a | 342 |
15:00$B!A(B 15:20 | F119 | $BJ,;RF0NO3XK!$rMQ$$$?%7%j%+%J%N:Y9&$K$*$1$k1UAjF)2a5!9=$N8!F$(B
($B9-Bg9)(B) $B!{(B($B@5(B)$B5H2,(B $BJ~5W(B $B!&(B ($B3X(B)$B5W2,(B $B0j $B!&(B ($B@5(B)$B6b;X(B $B@58@(B $B!&(B ($B@5(B)$BETN1(B $BL-N;(B | molecular dynamics silica membrane liquid permeation
| 4-a | 519 |
15:20$B!A(B 15:40 | F120 | $BC:AGKl$NI=LL=hM}8z2L(B
($B;38}Bg1!M}9)(B) ($B3X(B)$B@P@n(B $BM598(B $B!&(B ($B3X(B)$BF#0f(B $B7IMN(B $B!&(B ($B3X(B)$B8E2l(B $BCR;R(B $B!&(B $BIp5o(B $BM&4u(B $B!&(B ($B@5(B)$B7'@Z(B $B@t(B $B!&(B ($B@5(B)$BEDCf(B $B0l9((B $B!&(B $B!{(B($B@5(B)$B4nB?(B $B1QIR(B | carbon membrane surface modification pervaporation
| 4-a | 239 |
(15:40$B!A(B17:20)$B!!(B($B:BD9(B $BETN1(B $BL-N;(B) |
15:40$B!A(B 16:00 | F121 | $BCf6u;e%+!<%\%sKl$NC&?e@-G=$KM?$($kA06nBN%]%j%^!<$X$N%+%A%*%sE:2C8z2L(B
($B;:Am8&(B) $B!{(B($B@5(B)$B5H=!(B $BH~5*(B $B!&(B ($B@5(B)$B86C+(B $B8-<#(B | Carbon membrane Hollow fiber Pervaporation
| 4-a | 213 |
16:00$B!A(B 16:20 | F122 | $B=
($B;:Am8&(B) $B!{(B($B@5(B)$B86(B $B?-@8(B $B!&(B ($B@5(B)Caravella Alessio $B!&(B ($B@5(B)$B5H=!(B $BH~5*(B $B!&(B ($B@5(B)$B86(B $B=E $B!&(B ($B@5(B)$B86C+(B $B8-<#(B | Carbon membrane Hollow fiber Computational Fluid Dynamics
| 4-a | 409 |
16:20$B!A(B 16:40 | F123 | $B:Y9&Fb=
(NAIST) $B!{(B($B3X(B)$BIp;3(B $BGnF;(B $B!&(B (RITE) ($B@5(B)$BM>8l(B $B9nB'(B $B!&(B ($B@5(B)$B1JED(B $B7rM4(B $B!&(B $BEOIt(B $B5#(B | Palladium Hydrogen Membrane
| 4-a | 308 |
16:40$B!A(B 17:00 | F124 | $B3HD%J?J}:,B'$K4p$E$$$?(BZr-Ni$B7O%"%b%k%U%!%99g6b$N?eAG3H;678?t$NI>2A(B
($B;:Am8&(B) $B!{(B($B@5(B)$B86(B $B=E $B!&(B ($B@5(B)Caravella Alessio $B!&(B ($B@5(B)$B?\ED(B $BMN9,(B $B!&(B ($B@5(B)$B8~ED(B $B2m0l(B $B!&(B ($B@5(B)$B86C+(B $B8-<#(B $B!&(B ($B@5(B)$B86(B $B?-@8(B | Hydrogen Permeation Diffusion
| 4-a | 532 |
17:00$B!A(B 17:20 | F125 | $BD62;GHJ.L8K!$K$h$kFs;@2=C:AGJ,N%Kl$N:n@=$HJ,N%@-G=I>2A(B
($B2#9qBg1!(B) $B!{(B($B3X(B)$BCfLp(B $B??Gn(B $B!&(B $B5]Lp(B $BIpB"(B $B!&(B $BIpED(B $BMN(B $B!&(B ($B@5(B)$BAj86(B $B2mI'(B | membrane separation ultrasonic mist CO2 separation
| 4-a | 473 |
F$B2q>l(B $BBh(B2$BF|(B |
(9:20$B!A(B10:40)$B!!(B($B:BD9(B $BCfB<(B $B0lJf(B) |
9:20$B!A(B 9:40 | F202 | Development of low-fouling PVDF membrane blending zwitterionic copolymer via TIPS method
($B?@8MBg1!9)(B) $B!{(B($B3X(B)$BD@(B $BK2(B $B!&(B ($B@5(B)$BBg8~(B $B5H7J(B $B!&(B ($B@5(B)$B@P?@(B $BE0(B $B!&(B ($B@5(B)$B?@Hx(B $B1Q<#(B $B!&(B ($B@5(B)$B4];3(B $BC#@8(B $B!&(B ($B@5(B)$B>>;3(B $B=(?M(B | PVDF membrane Zwitterionic copolymer Fouling
| 4-a | 380 |
9:40$B!A(B 10:00 | F203 | Development of antibiofouling RO membrane by layer-by-layer method
(Kobe U.) $B!{(B($B3X(B)Karkhanechi Hamed $B!&(B ($B3X(B)Razi Fachrul $B!&(B ($B@5(B)Ohmukai Yoshikage $B!&(B ($B@5(B)Maruyama Tatsuo $B!&(B ($B@5(B)Matsuyama Hideto | Layer-by-layer Antibiofouling RO membrane
| 4-a | 502 |
10:00$B!A(B 10:20 | F204 | $B%?%s%Q%/@\7V8w4Q;!(B
($B?@8MBg1!9)(B) $B!{(B($B3X(B)Hao Yan $B!&(B ($B@5(B)$B4];3(B $BC#@8(B $B!&(B ($B3X(B)$BNB(B $B%5%$(B $B!&(B ($B3X(B)$B4?M(B $B!&(B ($B@5(B)$BBg8~(B $B5H7J(B $B!&(B ($B@5(B)$B@P?@(B $BE0(B $B!&(B ($B@5(B)$B>>;3(B $B=(?M(B | Visualization Protein fouling Backwashing
| 4-a | 362 |
10:20$B!A(B 10:40 | F205 | $B3F2A(B
($B?@8MBg1!9)(B) $B!{(B($B3X(B)$BD9Eg(B $BM@E5(B $B!&(B ($B@5(B)$B:4Gl(B $BBgJe(B $B!&(B ($B@5(B)$B_7ED(B $BM&@8(B $B!&(B ($B@5(B)$BF#0f(B $B><9((B $B!&(B ($B@5(B)$B?@Hx(B $B1Q<#(B $B!&(B ($B@5(B)$B4];3(B $BC#@8(B $B!&(B ($B@5(B)$B>>;3(B $B=(?M(B | Membrane material Bacterial adhesion Biofilm
| 4-a | 467 |
(10:40$B!A(B12:00)$B!!(B($B:BD9(B $B5H2,(B $BJ~5W(B) |
10:40$B!A(B 11:00 | F206 | $B%]%j%^!
($BElKLBgL$Mh%;(B) $B!{(B($B@5(B)$BFn1@(B $BN<(B $B!&(B ($BElKLBg1!9)(B) $B0KF#(B $BC$FA(B $B!&(B ($B@5(B)$B;01:(B $BN4<#(B $B!&(B ($BElKLBgL$Mh%;(B) $BNkLZ(B $B0&(B $B!&(B ($B@5(B)$BDZ0f(B $B=(9T(B $B!&(B ($BElKLBg1!9)(B) ($B@5(B)$BH+;3(B $BK>(B $B!&(B ($B@5(B)$B9b1)(B $BMN=<(B $B!&(B ($BElKLBgL$Mh%;(B/$BElKLBg1!9)(B) ($B@5(B)$B5\K\(B $BL@(B | antifouling molecular dynamics polymer membrane
| 4-a | 222 |
11:00$B!A(B 11:20 | F207 | Modification of anion exchange membrane for antifouling improvement
(Kobe U.) $B!{(B($B3X(B)Mulyati Sri $B!&(B ($B@5(B)Takagi Ryosuke $B!&(B ($B@5(B)Fujii Akihiro $B!&(B ($B@5(B)Ohmukai Yoshikage $B!&(B ($B@5(B)Maruyama Tatsuo $B!&(B ($B@5(B)Matsuyama Hideto | antifouling potential Anion exchange membrane electrodialysis
| 4-a | 496 |
11:20$B!A(B 11:40 | F208 | $BC:2=?eAG7OEE2r
($BElKLBg1!9)(B) $B!{(B($B@5(B)$B9b1)(B $BMN=<(B $B!&(B ($BElKLBgL$Mh%;(B) ($B@5(B)$BFn1@(B $BN<(B $B!&(B ($BElKLBg1!9)(B) ($B@5(B)$B;01:(B $BN4<#(B $B!&(B ($BElKLBgL$Mh%;(B) $BNkLZ(B $B0&(B $B!&(B ($B@5(B)$BDZ0f(B $B=(9T(B $B!&(B ($BElKLBg1!9)(B) $BH+;3(B $BK>(B $B!&(B ($BElKLBgL$Mh%;(B/$BElKLBg1!9)(B) ($B@5(B)$B5\K\(B $BL@(B | Polymer electrolyte Degradation Molecular dynamics
| 4-a | 184 |
11:40$B!A(B 12:00 | F209 | $B%h%&2=?eAG;@4D6-$K$*$1$k%$%*%s8r49Kl$NF3EEN($N29EY0MB8@-(B
(JAEA) $B!{(B($B@5(B)$BEDCf(B $B?-9,(B $B!&(B $BH,4,(B $BE0Li(B $B!&(B $B@uLn(B $B2m=U(B $B!&(B $BA0@n(B $B9/@.(B $B!&(B $B>.4S(B $B70(B | Cation exchange membrane Hydriodic acid Conductivity
| 4-a | 497 |
|
(13:00$B!A(B14:20)$B!!(B($B:BD9(B $B?7C+(B $BBn;J(B) |
13:00$B!A(B 13:20 | F213 | $B3$?e$r6nF0MO1U$H$7$?%U%)%o!<%I!&%*%9%b%7%9GS?e=hM}%7%9%F%`(B(I):$B?eF)2a@-$HMO
($B;38}Bg1!M}9)(B) ($B3X(B)$B=EF#(B $BBgJe(B $B!&(B $B=BC+(B $B??;K(B $B!&(B $B!{(B($B@5(B)$B1sF#(B $B@kN4(B $B!&(B ($B@5(B)$BHf2E(B $B=<(B | Forward osmosis Hollow fiber membrane Water treatment
| 4-a | 547 |
13:20$B!A(B 13:40 | F214 | $B@5?;F)MQCf6u;eKl%b%8%e!<%k$K$*$1$k?;F)05H/EE%b!<%I$G$NKlFC@-$H1?E>>r7o$H$N4X78(B(I)
($B;38}Bg1!M}9)(B) ($B3X(B)$B=EF#(B $BBgJe(B $B!&(B $B=BC+(B $B??;K(B $B!&(B ($B@5(B)$B1sF#(B $B@kN4(B $B!&(B $B!{(B($B@5(B)$BHf2E(B $B=<(B | Pressure retarded osmosis Hollow fiber membrane Forward osmosis membrane
| 4-a | 543 |
13:40$B!A(B 14:00 | F215 | $B@5?;F)Kl%b%8%e!<%kI>2AAuCV$N:n@=$H?;F)05H/EE%b!<%I$K$*$1$kFC@-I>2A(B
($B;38}Bg1!M}9)(B) $B!{(B($B3X(B)$B=EF#(B $BBgJe(B $B!&(B $B=BC+(B $B??;K(B $B!&(B ($B@5(B)$B1sF#(B $B@kN4(B $B!&(B ($B@5(B)$BHf2E(B $B=<(B $B!&(B ($BEl9)Bg1!M}9)(B) $B@FF#(B $B7I0lO:(B $B!&(B $BC+2,(B $BL@I'(B | Pressure retarded osmosis Hollow fiber membrane Forward osmosis membrane
| 4-a | 538 |
14:00$B!A(B 14:20 | F216 | RO$BKl$K$h$k1vG;=L2aDx$K$*$1$k%9%1!<%k@8@.5sF0(B
($B2#9qBg9)(B) $B!{(B($B3X(B)$B;34_(B $BLwE5(B $B!&(B ($B@5(B)$B?7ED8+(B $B6)(B $B!&(B ($B@5(B)$BCfB<(B $B0lJf(B $B!&(B ($B@5(B)$B>>K\(B $B44<#(B | Reverse Osmosis scale concentration
| 4-a | 615 |
(14:20$B!A(B15:20)$B!!(B($B:BD9(B $B;TB<(B $B=E=S(B) |
14:20$B!A(B 14:40 | F217 | NF$BKl$rMQ$$$??)IJ5!G=@-@.J,$HM-2A6bB0$NG;=LJ,N%(B
($B?@8MBg1!9)(B) $B!{(B($B3X(B)$BD%(B $B0N(B $B!&(B ($B@5(B)$BNB(B $B%5%$(B $B!&(B ($B3X(B)Hao Yan $B!&(B ($B@5(B)$B>>;3(B $B=(?M(B $B!&(B ($B@5(B)$B4];3(B $BC#@8(B | nanfitration concentration precious metal ions
| 4-a | 410 |
14:40$B!A(B 15:00 | F218 | $BJ#9g(BPDMS$BHsB?9&
($B@iMU8);:5;8&(B) $B!{(B($B@5(B)$B5\>k(B $B=_(B $B!&(B ($BG@8&5!9=?)Am8&(B) ($B@5(B)$BFiC+(B $B9@;V(B | PDMS based membrane Solution-diffusion model Regular solution model
| 4-a | 377 |
15:00$B!A(B 15:20 | F219 | $B7l1UF)@O4o$NMO
($B;:Am8&44:YK&9)3X(BRC) $B!{(B($B@5(B)$B6b?9(B $BIR9,(B $B!&(B ($B;:Am8&44:YK&9)3X(BRC$B!&$D$/$P%5%$%(%s%9%"%+%G%_!<(B) ($B@5(B)$B9B8}(B $B7r:n(B | finite element method hemodiafiltration Kedem-Kachalsky equation
| 4-a | 673 |
(15:20$B!A(B16:40)$B!!(B($B:BD9(B $B6b?9(B $BIR9,(B) |
15:20$B!A(B 15:40 | F220 | $B%j%]%=!<%`$K$h$k%-%i%kG'<15!G=$K4X$9$k8&5f(B
($B:eBg1!4p9)(B) $B!{(B($B3X(B)$B@P>e(B $B6,98(B $B!&(B ($B@5(B)$BGO1[(B $BBg(B | liposome chiral recognition amino acid
| 4-a | 493 |
15:40$B!A(B 16:00 | F221 | $B%"%_%m%$%I@~0]7A@.$K5Z$\$9%j%]%=!<%`(B/$BF<%$%*%s$N1F6A(B
($B:eBg1!4p9)(B) $B!{(B($B@5(B)$BEgFb(B $B $B!&(B ($B3X(B)$BKL1:(B $BF`CN(B $B!&(B ($B3X(B)$BBg@>(B $BNJ(B $B!&(B ($B@5(B)$BGO1[(B $BBg(B $B!&(B ($B@5(B)$B5WJ]0f(B $BN<0l(B | Liposome Amyloid Copper ion
| 4-g | 476 |
16:00$B!A(B 16:20 | F222 | $B5[<>@-%$%*%s1UBN$N1UBNKl$K$h$k=|<>K!(B
($BEl9)Bg9)(B) $B3aLn(B $BE/J?(B $B!&(B $B!{(B($B@5(B)$B0KEl(B $B>O(B | dehumidification liquid membrane ionic liquid
| 4-a | 358 |
16:20$B!A(B 16:40 | F223 | $B%"%_%N;@%$%*%s1UBN$rH?1~M"AwG^BN$H$9$k3W?7E*(BCO2$BJ,N%Kl$NAO@=(B
($B?@8MBg1!9)(B) $B!{(B($B3X(B)$B3^86(B $B>)J?(B $B!&(B ($B@5(B)$B?@Hx(B $B1Q<#(B $B!&(B ($B@5(B)$B@P?@(B $BE0(B $B!&(B ($B@5(B)$B>>;3(B $B=(?M(B | Amino acid ionic liquid CO2 separation Facilitated transport membrane
| 4-a | 95 |
G$B2q>l(B $BBh(B1$BF|(B |
(9:40$B!A(B11:00)$B!!(B($B:BD9(B $BBg9>(B $B=$B$(B) |
9:40$B!A(B 10:00 | G103 | $BFbItG.8r495;=Q$rMQ$$$?%P%C%A>xN1%W%m%;%9$N>J%(%M%k%.!<2=(B
($B;37ABg1!M}9)(B) $B!{(B($B3X(B)$B;3LZ(B $BM:Bg(B $B!&(B ($B3X(B)$BNkLZ(B $BBYI'(B $B!&(B ($B@5(B)$B>>ED(B $B7=8g(B | Batch Distillation Heat-Integration Energy Saving
| 4-c | 267 |
10:00$B!A(B 10:20 | G104 | Design of Internally Heat-Integrated Distillation Columns Using Matrix Inversion
(Dong-A U.) $B!{(B($B@5(B)Kim Young Han | Internally Heat-Integrated Distillation Energy-Efficient Distillation Approximate Design
| 4-c | 14 |
10:20$B!A(B 10:40 | G105 | HIDiC$B$NEAG.JQF0$KBP$9$k@)8fJ}K!$K$D$$$F(B
($B4X@>2=3X(B) $B!{(B($B@5(B)$BJR2,(B $BK.IW(B $B!&(B ($B@5(B)$B8~ED(B $BCi90(B $B!&(B ($B@5(B)$BLnED(B $B=(IW(B $B!&(B ($B@5(B)$B;3O)(B $B42;J(B | HIDiC Heat Transfer Control
| 4-c | 23 |
10:40$B!A(B 11:00 | G106 | $B%P%C%A>xN1Ec$N?t<0%b%G%k$K$h$k%*%s%i%$%s:GE,1?E>(B
($BF|BgM}9)(B) $B!{(B($B@5(B)$BFJLZ(B $B>!8J(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) ($B3X(B)$BCfEg(B $B??M};R(B $B!&(B ($B@5(B)$B>>ED(B $B909,(B $B!&(B ($B@5(B)$B7*86(B $B@6J8(B | Batch Distillation Operation Online Optimization Mathematical Models
| 4-c | 132 |
(11:00$B!A(B12:00)$B!!(B($B:BD9(B $B>>ED(B $B7=8g(B) |
11:00$B!A(B 11:20 | G107 | $B=
($BElM}Bg(B) $B!{(B($B@5(B)$BBg9>(B $B=$B$(B | pressure drop packed tower correlation
| 4-c | 379 |
11:20$B!A(B 11:40 | G108 | $B05NO6nF07?>xN1%7%9%F%`$N>J%(%M%k%.!<@-G=$HZ$N$?$a$N4pAC
($BFAEgBg1!(BSTS$B8&(B) $B!{(B($B3X(B)$B30NX(B $B7r0lO:(B $B!&(B ($BFAEgBg9)(B) $BF#ED(B $BBn:H(B $B!&(B ($BFAEgBg1!@hC<650iIt(B) ($B@5(B)$B@uED(B $B9,M4(B $B!&(B ($BFAEgBg1!(BSTS$B8&(B) ($B@5(B)$B?y;3(B $BLP(B $B!&(B ($B@5(B)$BCf@n(B $B7I;0(B | pressure distribution compressor distillation
| 4-c | 680 |
11:40$B!A(B 12:00 | G109 | $BB?@.J,7O5$1UJ?9U?d;;$N$?$a$N%G%b%W%m%0%i%`
($B | $B5$1UJ?9U(B $B2a>j<+M3%(%M%k%.!<(B $BL58B4u | 4-c | 507 |