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10:00$B!A(B 10:20 | D104 | $B%a%?%N!<%k$rMQ$$$?%*!<%H%5!<%^%k2~ ($B7DXfBgM}9)(B) $B!{(B($B3X(B)$B2CF#(B $BD>(B$B!&(B($B@5(B)$BC01)(B $B9/;K(B$B!&(B($BBgF1%a%?%k9)6H(B) ($B@5(B)$B@.@%(B $B9,IW(B$B!&(B($B@5(B)$B0p8+(B $BLP(B$B!&(B($B@5(B)$B2CF#(B $B1QFs(B$B!&(B($B7DXfBgM}9)(B) ($B@5(B)$BBgB<(B $BN<(B$B!&(B($B@5(B)$B2#?9(B $B9d(B$B!&(B($B@5(B)$B?"ED(B $BMx5W(B | auto-thermal reforming steam reforming partial oxidation
| 2-a | 318 |
10:20$B!A(B 10:40 | D105 | $B%a%?%N!<%k?e>x5$2~ ($B7DXfBgM}9)(B) $B!{(B($B3X(B)$B@V@1(B $BNIB?(B$B!&(B($BBgF1%a%?%k9)6H(B) ($B@5(B)$B@.@%(B $B9,IW(B$B!&(B($B@5(B)$B0p8+(B $BLP(B$B!&(B($B@5(B)$B2CF#(B $B1QFs(B$B!&(B($B7DXfBgM}9)(B) ($B@5(B)$BBgB<(B $BN<(B$B!&(B($B@5(B)$B2#?9(B $B9d(B$B!&(B($B@5(B)$B?"ED(B $BMx5W(B | methanol steam reforming hydrogen production
| 2-a | 105 |
10:40$B!A(B 11:00 | D106 | $B?eAGJ,N%Kl0lBN7?2~ ($B7DXfBgM}9)(B) $B!{(B($B3X(B)$B7,86(B $B2m?M(B$B!&(B($B@5(B)$BC01)(B $B9d9/(B$B!&(B($BBgF1%a%?%k9)6H(B) ($B@5(B)$B@.@%(B $B9,IW(B$B!&(B($B@5(B)$B0p8+(B $BLP(B$B!&(B($B@5(B)$B2CF#(B $B1QFs(B$B!&(B($B7DXfBgM}9)(B) ($B@5(B)Wardana Ing$B!&(B($B@5(B)$BBgB<(B $BN<(B$B!&(B($B@5(B)$B2#?9(B $B9d(B$B!&(B($B@5(B)$B?"ED(B $BMx5W(B | hydrogen production steam reforming membrane
| 2-a | 320 |
(11:00$B!A(B12:00)$B!!(B($B:BD9(B $B?"ED!!Mx5W(B) |
11:00$B!A(B 11:20 | D107 | $B1UAjH?1~MpN.>l$N(BLarge-eddy Simulation ($B5~Bg1!(B) $B2OLn(B $BD>5*(B$B!&(B($B5~Bg9)(B) $B!{(B($B@5(B)$B9u@%(B $BNI0l(B$B!&(B($B@5(B)$B>.?9(B $B8g(B$B!&(B($BEECf8&(B) ($B@5(B)$BF;2,(B $BIp?.(B$B!&(B(ESC) $BGO>l(B $BM:Li(B | Turbulent liquid reaction Large-eddy simulation Flamelet model
| 2-a | 338 |
11:20$B!A(B 11:40 | D108 | $BJ#9g1UE)$N%7%_%e%l!<%7%g%s$N$?$a$N;0N.BN%U%m%s%H%H%i%C%-%s%0K!$N3+H/(B ($B:k6LBg1!(B) $B!{(B($B@5(B)$BK\4V(B $B=S;J(B$B!&(B($B@5(B)$B2#DM(B $B=!G7(B$B!&(B($B@5(B)$B8E4W(B $BFsO:(B | Compound Droplet Front-Tracking Density Profile
| 2-a | 72 |
11:40$B!A(B 12:00 | D109 | $BEE5$N.BNNO3X8z2L$N;0 ($B@iMUBg1!<+(B) $B!{(B($B3X(B)$B?y;3(B $BGn><(B$B!&(B($B@iMUBg1!9)(B) ($B@5(B)$B>.AR(B $BM5D>(B$B!&(B($B@5(B)$B1vEg(B $BTcIW(B$B!&(B($B@5(B)$BBgDZ(B $BBYJ8(B | Electrohydrodynamics Simulation Dielectric Oil
| 2-g | 232 |
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13:00$B!A(B 13:20 | D113 | $B%A!<%:%[%(!<$N%/%m%9%U%m!<8B30_I2a$K$*$1$kBO@QAX$N%l%*%m%8!<$r9MN8$7$?%b%G%k2=(B ($BEl9)BgM}9)(B) $B!{(B($B3X(B)$BEb?\(B $B8&Je(B$B!&(B($B@5(B)$B5H@n(B $B;KO:(B | Ultrafiltration Transport phenomena Rheology
| 2-a | 148 |
13:20$B!A(B 13:40 | D114 | $B%^%$%/%mN.O)Fb$K$*$1$k%j%]%=!<%`@8@.5!9=(B ($B?@8MBg(B) $B!{(B($B3X(B)$BF#86(B $B=_(B$B!&(B($B?@8MBg1!(B) ($B3X(B)$B_@B<(B $BH;Lp(B$B!&(B($B?@8MBg1!9)(B) ($B@5(B)$BNkLZ(B $BMN(B$B!&(B($B@5(B)$B>!ED(B $BCN>0(B$B!&(B($B@5(B)$B8VED(B $B1YG7(B$B!&(B($B@5(B)$BGv0f(B $BMN4p(B | Micro-channel Liposome Shear Flow
| 2-a | 511 |
13:40$B!A(B 14:00 | D115 | $B4pHD>e$K$*$1$k9bJ,;RMO1UE)$N@\?(@~8GDj$K4X$9$k2r@O(B ($B6eBg1!(B) $B!{(B($B3X(B)$B@P66(B $B2CF`;R(B$B!&(B($B3X(B)$B5HC](B $BM4(B$B!&(B($B:eI\Bg9)(B) ($B@5(B)$B6bED(B $B>;G7(B$B!&(B($B6eBg9)(B) ($B@5(B)$BCfA>(B $B9@0l(B$B!&(B($B@5(B)$B?<0f(B $B=a(B | droplet evaporation simulation
| 2-a | 299 |
(14:00$B!A(B15:00)$B!!(B($B:BD9(B $B8VED(B $B1YG7(B) |
14:00$B!A(B 14:20 | D116 | $B@PC:%,%92=AuCVFb$NG3>F3%$N5sF02r@O(B ($B6eBg9)(B) $B!{(B($B3X(B)$BA0ED(B $BM5Fs(B$B!&(B($B6eBg1!9)(B) ($B@5(B)$B>>7((B $BMN2p(B$B!&(B($B@5(B)$B0f>e(B $B85(B$B!&(B($B@5(B)$BJw85(B $B2m | coal gasification combustion ash lattice Boltzmann method
| 2-a | 330 |
14:20$B!A(B 14:40 | D117 | $B= ($B6eBg1!9)(B) $B!{(B($B@5(B)$B>>7((B $BMN2p(B$B!&(B($B@5(B)$BCI>e(B $B5.;V(B$B!&(B($B@5(B)$B0f>e(B $B85(B$B!&(B($B@5(B)$BJw85(B $B2m | gas diffusion layer packed bed lattice Boltzmann method
| 2-a | 445 |
14:40$B!A(B 15:00 | D118 | Y$B;z4IH?1~4o$rMQ$$$FO"B3@=B$$5$l$?%7%j%+%>%k$NFC@-(B ($B;38}Bg1!(B) $B!{(B($B3X(B)$B5FCS(B $BAa?%(B$B!&(B($B@5(B)$B:4Gl(B $BN4(B$B!&(B($B%H%/%d%^(B) $BEDH*(B $B0l><(B$B!&(B$BB@ED(B $B9LB$(B | Silica sol Sol-gel transition Reactor
| 2-g | 645 |
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15:00$B!A(B 15:20 | D119 | $B%^%$%/%m%P%V%k$rJ,;6$5$;$?5$K"Ec$NJ* ($BL>Bg1!9)(B) $B!{(B($B@5(B)$B0BED(B $B7<;J(B$B!&(B($B3X(B)$B2&(B $B1'Ht(B$B!&(B($BF|K\%j%U%!%$%s(B) ($B@5(B)$B:dEl(B $BK'9T(B$B!&(B($B6&(B)$BC];3(B $BM'7i(B$B!&(B($B@5(B)$B@n@%(B $BBY?M(B | Micro Bubble Bubble Column Mass Transfer
| 2-d | 311 |
15:20$B!A(B 15:40 | D120 | $B5$K"Ec$K$*$1$k6I=j%\%$%IN(JQF0$H1UAjB.EYJ,I[$N4X78(B ($B@EBg9)(B) $B!{(B($B3X(B)$B:#@t(B $BNIB@(B$B!&(B($B@EBg1!(B) ($B3X(B)$BHu8}(B $B@5$B!&(B($B3X(B)$B?9@n(B $B9/0l(B$B!&(B($B@EBg9)(B) ($B@5(B)$B??ED(B $B=SG7(B$B!&(B($B@EBg1!(B) ($B@5(B)$Bc7F#(B $BN4G7(B | Local time-series void fraction Laser Doppler Anemometry Optical fiber probe
| 2-d | 160 |
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| 2-d | 631 |
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16:00$B!A(B 16:20 | D122 | $B5$1U(B2$BAjN.$r6nF0N.BN$H$7$?%(%<%/%?! ($B7DXfBg1!M}9)(B) $B!{(B($B3X(B)$BC]B<(B $BOBLi(B$B!&(B($B7DXfBgM}9)(B) $BCSED(B $BM-5#(B$B!&(B($B@5(B)$B;{:d(B $B9(0l(B$B!&(B($B@5(B)$B>.NS(B $BBgM4(B | ejector two-phase flow bubble
| 2-e | 197 |
16:20$B!A(B 16:40 | D123 | $B5$K"72Fb$N5$K"4VAj8_:nMQ$H5$K"1?F0$K$h$k1UAj$NFC@-JQ2=(B ($B@EBg9)(B) $B!{(B($B3X(B)$B?"ED(B $B=gBg(B$B!&(B($B@EBg1!(B) ($B3X(B)$B?9@n(B $B9/0l(B$B!&(B($B3X(B)$BA>:,(B $BBg<#(B$B!&(B($B@EBg9)(B) ($B@5(B)$B??ED(B $B=SG7(B$B!&(B($B@EBg1!(B) ($B@5(B)$Bc7F#(B $BN4G7(B | Bubble swarm PIV surrounding liquid motion
| 2-e | 157 |
16:40$B!A(B 17:00 | D124 | $B5$K"93NO!<;~4VJ?6Q$HBN@QJ?6Q$NHf3S8!F$!<(B ($B:eBg4p9)(B) $B!{(B($B@5(B)$B>e;3(B $B0T0l(B | bubble drag force Navier-Stokes equations time-average and volume-average
| 2-e | 762 |
$BBh(B2$BF|(B
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9:20$B!A(B 9:40 | D202 | $BG4@-N.BNCf$r<+M31?F0$9$kC10l1UE)$N0BDj@-(B ($B<$B!&(B($B3X(B)$B@V4V(B $BM3(B$B!&(B($B@5(B)$B5HED(B $BK-(B | Drop rise motion Instability Nonlinear dynamics
| 2-e | 57 |
9:40$B!A(B 10:00 | D203 | $B0lMM$JL.F0N.Cf$N5e7AN3;R$KF/$/93NO$NI>2A(B ($B:eI\Bg1!9)(B) $B!{(B($B@5(B)$B?y2,(B $B7r0l(B$B!&(B($B:eI\Bg9)(B) $B8+>e(B $B?.(B$B!&(B($BElKLBg1!9)(B) ($B@5(B)$BDMED(B $BN4IW(B$B!&(B($B5~Bg1!9)(B) ($B@5(B)$B>.?9(B $B8g(B | drag force direct numerical simulation oscillating flow
| 2-e | 310 |
10:00$B!A(B 10:20 | D204 | $B5<;wE*D>@\?tCM7W;;$K$*$1$k5eN3;R$NG4@-Dq93$*$h$S7A>uDq93$NDj<02=$H8!>Z(B (ANSYS Inc.) Agrawal Madhusuden$B!&(B($BEl9)Bg1!M}9)(B) $B!{(B($B@5(B)$BBg@n86(B $B??0l(B$B!&(B($B@5(B)$B>.@n(B $B9@J?(B | Macroscopic particle model Drag force Virtual mass force
| 2-e | 492 |
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10:20$B!A(B 10:40 | D205 | $BHyN3;RD@9_7O$K$*$1$kB.EYAj4X(B ($B5~Bg1!9)(B) $B!{(B($B3X(B)$B;3K\(B $B9d5*(B$B!&(B($B5~Bg1!9)(B/JST-CREST) ($B@5(B)$B;3K\(B $BNL0l(B | Direct Numerical Simulation(DNS) Correlation Function Density Fluctuation
| 2-e | 288 |
10:40$B!A(B 11:00 | D206 | $BMn2<5e$rMQ$$$?%2%k2=H?1~Cf$N%"%k%_%J%9%i%j!<$NG4EYI>2A(B ($BL>9)Bg(B) $B!{(B($B@5(B)$B4dED(B $B=$0l(B$B!&(B($B3X(B)$B;3ED(B $BM*2p(B$B!&(B($B3X(B)$BNkLZ(B $B9(E5(B$B!&(B($B@5(B)$B?9(B $B=($B!&(B($BL>9)Bg%;%i8&(B) $B2CF#(B $B>fL@(B$B!&(B$BF#(B $B@5FD(B | falling sphere viscosity alumina slurry
| 2-e | 711 |
(11:00$B!A(B12:00)$B!!(B($B:BD9(B $BB@ED!!8w9@(B) |
11:00$B!A(B 11:20 | D207 | Taylor-Couette$BN.$l$rMxMQ$7$?1U!98~N.1s?4Cj=PAuCV$N3+H/(B ($BEl9)Bg;q8;8&(B) $B!{(B($B@5(B)$BC]2<(B $B7rFs(B$B!&(B($BEl9)Bg(B) ($B3X(B)$BO;3Q(B $B?N(B | centrifuge extractor Taylor-Couette flow counter-current
| 2-e | 428 |
11:20$B!A(B 11:40 | D208 | $B%(%?%N!<%k$NG;=L$K8~$1$?D62;GHL82=!&Nd5Q2s<}%W%m%;%9$N9=C[(B ($BF1;V$B!&(B($BF1;V$B!&(B($BF1;V$B!&(B($B@5(B)$BEZ20(B $B3hH~(B$B!&(B($BD62;GH>zB$=j(B) ($B@5(B)$B>>1:(B $B0lM:(B | ultrasonic atomization ethanol separation mist recovery
| 2-e | 550 |
11:40$B!A(B 12:00 | D209 | $B%+%i!<%O%$%9%T!<%I%+%a%i$rMQ$$$?Fs?'(BLIF$BK!$K$D$$$F(B ($B$B!&(B$B!{(B($B3X(B)$B>.ED86(B $BM:8J(B$B!&(B$BJR;3(B $Bb+2p(B$B!&(B($B@5(B)$B>>K\(B $BMxC#(B | two-color LIF high-speed camera pH measurement
| 2-e | 345 |
$BBh(B3$BF|(B
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9:20$B!A(B 9:40 | D302 | $B%W%m%;%9@_7W5Z$S2=3XJ*2A$K4X$9$kCN<1$N9=B$2=(B-$B6bB0@v>t%W%m%;%9$X$NE,MQ(B ($BElBg9)(B) $B!{(B($B3X(B)$B5FCS(B $B9/5*(B$B!&(B($B@5(B)$BJ?Hx(B $B2mI'(B | Industrial cleaning Activity modeling Information modeling
| 6-f | 430 |
9:40$B!A(B 10:00 | D303 | $B@v>t:^GS=PM^@)$N$?$a$NBeBX@v>t%W%m%;%90FF3=P%7%9%F%`$N ($BElBg9)(B) $B!{(B($B3X(B)$BLZB<(B $BM}0lO:(B$B!&(B($B3X(B)$B5FCS(B $B9/5*(B$B!&(B($B@5(B)$BJ?Hx(B $B2mI'(B | Industrial Cleaning Engineering Knowledge Process Design
| 6-g | 448 |
(10:00$B!A(B11:00)$B!!(B($B:BD9(B $B2CG |
10:00$B!A(B 10:20 | D304 | Structural Framework Supporting Multi-objective Selection of Extraction Processes (The U. Tokyo) $B!{(B($B3X(B)Nguyen Thuy$B!&(B(ETH Zurich) Sugiyama Hirokazu$B!&(B(Nara Inst. Sci. and Tech.) ($B@5(B)Noda Masaru$B!&(B(The U. Tokyo) ($B@5(B)Hirao Masahiko | structural framework extraction processes multi-objective optimization
| 6-b | 270 |
10:20$B!A(B 10:40 | D305 | $B%3%W%m%@%/%7%g%s%T%s%A2r@O%D!<%k$rMQ$$$?<+8JG.:F@87?%W%m%;%9$NI>2A(B ($B;:Am8&(B) $B!{(B($B@5(B)$BC+8}(B $BCR(B$B!&(B($B@5(B)$BCf4d(B $B>!(B$B!&(B($B@5(B)$BBg?9(B $BN4IW(B$B!&(B($B%7%`%F%C%/(B) ($B@5(B)$BC'(B $B9@G7(B | CoProduction system pinch analysis energy saving
| 6-b | 14 |
10:40$B!A(B 11:00 | D306 | $BCJEc7?(BHIDiC$B$NEAG.%b%G%k(B ($BL>9)Bg(B) $B!{(B($B3X(B)$BEOIt(B $BCR4p(B$B!&(B($B@5(B)$BB9(B $B9HG_(B$B!&(B($B@5(B)$B66K\(B $BK'9((B | Distillation Energy Conservation Heat Integration
| 6-b | 303 |
(11:00$B!A(B12:00)$B!!(B($B:BD9(B $BLnED!!8-(B) |
11:00$B!A(B 11:20 | D307 | QSPR$B%b%G%k$NE,MQHO0O$rDj$a$k$?$a$NHFMQE*$J ($BElBg1!9)(B) $B!{(B($B3X(B)$B1&ED(B $B7<:H(B$B!&(B($B@5(B)$B9S@n(B $B@544(B$B!&(B($B@5(B)$BA%DE(B $B8x?M(B | QSPR AD(Applicability Domain) Chemometrics
| 6-g | 317 |
11:20$B!A(B 11:40 | D308 | $B%]%j%^!<%W%i%s%H$K$*$1$k%H%i%s%8%7%g%s=*N;H=Dj%b%G%k$N9=C[$H%=%U%H%;%s%5!<$X$N1~MQ(B ($BElBg1!9)(B) $B!{(B($B3X(B)$B6b;R(B $B90>;(B$B!&(B($B@5(B)$B9S@n(B $B@544(B$B!&(B($B@5(B)$BA%DE(B $B8x?M(B | soft sensor transition process control
| 6-d | 13 |
11:40$B!A(B 12:00 | D309 | $BA`6H%G!<%?$+$i$N%W%i%s%HF1Dj$K4X$9$k9M;!(B-$B@~7A4X?t%b%G%k$K$h$k%"%W%m!<%A(B- ($BL>9)Bg(B) $B!{(B($B3X(B)$B;38}(B $B@.H~(B$B!&(B($B@5(B)$BJFC+(B $B>$B!&(B($B%A%N!<(B) $B@P66(B $B@/;0(B | plant identification process control plant model
| 6-d | 104 |
12:00$B!A(B 13:00 | $BCk5Y$_(B |
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13:00$B!A(B 13:20 | D313 | TCM:$B%H!<%?%k%3%9%H%^%M%8%a%s%H(B-$B%W%m%8%'%/%H!&%9%3!<%W$H ($B%3%9%H9)3X8&(B) $B!{(B($B@5(B)$Bc7F#(B $B5A8J(B | Total Cost Management Project Scope Work Breakdown Structure
| 6-a | 355 |
13:20$B!A(B 13:40 | D314 | $BIT3NDj<{MW2<$G$NB?IJ ($B5~Bg9)(B) $B!{(B($B@5(B)$BD9C+It(B $B?-<#(B$B!&(B$BDT(B $BM*M$(B$B!&(B($B@5(B)$B2CG<(B $B3X(B | Demand uncertainty Production planning Inventory planning
| 6-a | 470 |
13:40$B!A(B 14:00 | D315 | $B4D6-JQ2=$r9MN8$7$?0U;W7hDj;Y1g$N$?$a$N%b%G%j%s%0(B ($BL>Bg9)(B) $B!{(B($B3X(B)$B>.L:(B $B=_J?(B$B!&(B($B3X(B)$B]/0f(B $B7=Je(B$B!&(B($B@5(B)$B66D^(B $B?J(B$B!&(B($B@5(B)$BLpV:(B $BCRG7(B$B!&(B($B@5(B)$B>.LnLZ(B $B9nL@(B | decision making support modeling environmental change
| 6-a | 432 |
(14:00$B!A(B15:00)$B!!(B($B:BD9(B $B>>K\!!=(9T(B) |
14:00$B!A(B 14:20 | D316 | $BDj@-%b%G%k$rMxMQ$7$?%P%C%A%W%m%;%9$N0[>o?GCG(B ($BL>Bg9)(B) $B!{(B($B3X(B)$B7-2<(B $BM%5.;R(B$B!&(B($B@5(B)$B66D^(B $B?J(B$B!&(B($B@5(B)$BLpV:(B $BCRG7(B$B!&(B($B@5(B)$B>.LnLZ(B $B9nL@(B | fault diagnosis qualitative model batch process
| 6-a | 431 |
14:20$B!A(B 14:40 | D317 | Cause-Effect$B%b%G%k$K4p$E$/%"%i!<%`%7%9%F%`$N@_7W(B ($B@EBg9)(B) $B!{(B($B3X(B)$BBg@>(B $BCR;N(B$B!&(B($B@5(B)$BIpED(B $BOB9((B$B!&(B($BL>9)Bg(B) ($B@5(B)$BIM8}(B $B9';J(B$B!&(B($B6eBg9)(B) ($B@5(B)$BLZB<(B $BD>$B!&(B($BF`NI@hC | Cause-Effect Model Alarm System Design
| 6-a | 91 |
14:40$B!A(B 15:00 | D318 | $B%^%$%/%m2=3X%W%m%;%9$NJD:I%A%c%M%k8!=P$HJD:IN(?dDj(B ($BF`NI@hC$B!&(B($B@5(B)$BLnED(B $B8-(B$B!&(B($B@5(B)$B@>C+(B $B9I0l(B | microreactor channel blockage fault diagnosis
| 6-a | 171 |
(15:00$B!A(B15:40)$B!!(B($B:BD9(B $B66D^!!?J(B) |
15:00$B!A(B 15:20 | D319 | Optimal Grade Transition in Continuous Polymerization Reactor ($BF`NI@hC$B!&(B($B@5(B)$BLnED(B $B8-(B$B!&(B($B@5(B)$B@>C+(B $B9I0l(B | Dynamic optimization Grade transition Polymer quality control
| 6-e | 513 |
15:20$B!A(B 15:40 | D320 | $BIT0BDj@-$rH<$&N.BN%7%9%F%`$K$*$1$k?6F0%Q%?!<%s$N%^%k%A%9%1!<%k2r@O(B ($BEl9)Bg1!M}9)(B) $B!{(B($B3X(B)$BF#2,(B $B:;ET;R(B$B!&(B($B@5(B)$B>>K\(B $B=(9T(B$B!&(B($B@5(B)$B9uED(B $B@i=)(B | exothermic reaction oscillatory phenomenon multiscale analysis
| 6-c | 62 |