$B9V1i(B $B;~9o(B | $B9V1i(B $BHV9f(B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $BJ,N`(B $BHV9f(B | $B$BHV9f(B | |
$BN3;R!&N.BN%W%m%;%9(B |
(10:00$B!A(B11:00)$B!!(B($B:BD9(B $B5H@n!!;KO:(B) |
10:00$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 $BBYJ8(B | Electrohydrodynamics Simulation Dielectric Oil
| 2-g | 232 |
12:00$B!A(B 13:00 | $BCk5Y$_(B |
(13:00$B!A(B14:00)$B!!(B($B:BD9(B $B>>7(!!MN2p(B) |
13:00$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 |
(15:00$B!A(B16:00)$B!!(B($B:BD9(B $B>.NS!!BgM4(B) |
15:00$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 $BN4G7(B | Local time-series void fraction Laser Doppler Anemometry Optical fiber probe
| 2-d | 160 |
15:40$B!A(B 16:00 | D121 | $B%(%"%j%U%H7?5$K"EcFb5B;@C&?eAG9ZAG$N0BDj@-$K5Z$\$9%j%]%=!<%`FbIuF~$HJd9ZAG$N1F6A(B ($B;38}Bg1!0e(B) $B!{(B($B@5(B)$B5HK\(B $B@?(B$B!&(B$B;32<(B $B9'9,(B$B!&(B($B3X(B)$B;3yu(B $BN<(B$B!&(B($B;38}Bg(B) ($B@5(B)$BCfHx(B $B>!Ui(B | Airlift bubble column liposomal formate dehydrogenase cofactor
| 2-d | 631 |
(16:00$B!A(B17:00)$B!!(B($B:BD9(B $B0BED!!7<<((B) |
16:00$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 |