$B9V1i(B $B;~9o(B | $B9V1i(B $BHV9f(B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $BJ,N`(B $BHV9f(B | $B$BHV9f(B | |
B $B2q>l!&Bh(B 3 $BF|(B |
(10:40$B!A(B12:00) ($B:BD9(B $BF#2,(B $B:;ET;R!&EgED(B $BD> |
10:40$B!A(B 11:00 | B306 | $BN3;RK!$rMQ$$$?(B3$B
($BL@<#(B) ($B@5(B)$B!{?@C+(B $BE/(B$B!&(B ($B@5(B)$B1)@8(B $B7=8c(B | Swallowing Simulation Particle method
| 2-g | 899 |
11:00$B!A(B 11:20 | B307 | $BN3;RK!$rMQ$$$?(B3$B
($BL@<#(B) ($B@5(B)$B!{?@C+(B $BE/(B$B!&(B ($B@5(B)$B1)@8(B $B7=8c(B | Swallowing Simulation Aspiration
| 2-g | 900 |
11:20$B!A(B 11:40 | B308 | $B%l!<%6%[%m%0%i%U%#!<$K$h$kG.3H;6$N2D;k2=$H(BSoret$B78?t$N7WB,(B
($BIY;3Bg9)(B) ($B@5(B)$B!{;3:,(B $B3Y;V(B$B!&(B $BBgDM(B $B7r8c(B$B!&(B ($B@5(B)$B5HED(B $B@5F;(B$B!&(B $B | thermal diffusion laser holography Soret coefficient
| 2-g | 891 |
11:40$B!A(B 12:00 | B309 | $B:.$8$j9g$o$J$$(B2$BN.BN3&LL$N1?F0(B
($B:k6LBg1!M}9)(B) ($B@5(B)$B!{8E4W(B $BFsO:(B$B!&(B $B8E4W(B $B=c0l(B$B!&(B ($B@5(B)$BK\4V(B $B=S;J(B | Rayleigh-Taylor instability Saffman-Taylor instability Front tracking method
| 2-e | 36 |
|
(13:00$B!A(B15:00) ($B:BD9(B $B |
13:00$B!A(B 13:20 | B313 | $B$;$sCGN.$lCf$r>e>:!&D@9_$9$kN.BNE)<~0O$NB.EYJ,I[$*$h$S(Bvirtual force term
($B9)3X1!Bg(B) ($B@5(B)$B>e;3(B $B0T0l(B | virtual force term bubble liquid drop
| 2-e | 27 |
13:20$B!A(B 13:40 | B314 | $B%+%C%H%;%k7?Kd$a9~$_6-3&K!$rE,MQ$7$?(BDES$B$K$h$kMpN.2r@O(B
($B=;M'2=3X(B) ($B@5(B)$B!{EDCf(B $B:;M3Mx(B$B!&(B ($B@5(B)$BEgED(B $BD>$B!&(B $BE*>l(B $B9%1Q(B$B!&(B ($B?@8MBg(B) ($B@5(B)$BIZ;3(B $BL@CK(B | Detached Eddy Simulation Cut cell Immersed Boundary Method
| 2-e | 61 |
13:40$B!A(B 14:00 | B315 | CFD$B$K$h$k%(%"%l!<%7%g%s%?%s%/Fb%,%9%[!<%k%I%"%C%W$N?d;;(B
($B7DXfBg1!M}9)(B/$B;05!9)6H(B) ($B@5(B)$B!{$B!&(B ($B7DXfBgM}9)(B) ($B@5(B)$B;{:d(B $B9(0l(B$B!&(B ($B@5(B)$BF#2,(B $B:;ET;R(B | Bubble Column Gas Holdup CFD
| 2-e | 413 |
14:00$B!A(B 14:20 | B316 | $BG4@-N.BNCf$K$*$1$k5$K"$NQrCGJQ7A!&J,Nv5sF0$N?tCM2r@O(B
($BFAEgBg1!(BSTS$B8&(B) ($B@5(B)$B!{B@ED(B $B8w9@(B$B!&(B ($BFAEgBg9)(B) $BKYED(B $BN?J?(B$B!&(B ($B@Q?e2=3X9)6H(B) ($BK!(B)$B6M\F(B $BMN;0(B | Shear flow Bubble breakup Critical Re number
| 2-e | 581 |
14:20$B!A(B 14:40 | B317 | $BAFBgN3;R$rJ,N%$9$k%5%$%/%m%s7?J,5iAuCV$N3+H/$HI>2A(B
($B9-Bg1!9)(B/$BAn8&%F%/%K%C%/%9(B) ($BK!(B)$B!{G&B-(B $B51CK(B$B!&(B ($B9-Bg1!9)(B) ($B@5(B)$BLZB<(B $B>-5.(B$B!&(B ($BAn8&2=3X(B) ($BK!(B)$B;3K\(B $B0l8J(B$B!&(B ($B9-Bg1!9)(B) ($B@5(B)$BJ!0f(B $B9qGn(B$B!&(B ($B@5(B)$B5HED(B $B1Q?M(B | Gas-cyclone Particle separetion Cut size
| 2-f | 52 |
14:40$B!A(B 15:00 | B318 | $BBSEE%J%N1UE)$N>xH/!&J,Nv2aDx$NJ,;RF0NO3XE*2r@O(B
($B6bBtBg1!<+A38&(B) $BFAH~(B $BBsLi(B$B!&(B ($B%Q%J%=%K%C%/(B) ($B@5(B)$BA0@n(B $BE/Li(B$B!&(B ($B6bBtBgM}9)(B) ($B@5(B)$B!{El(B $B=(7{(B$B!&(B ($B@5(B)$B5bED(B $B44IW(B$B!&(B ($B@5(B)$B@%8M(B $B>OJ8(B$B!&(B ($B@5(B)$BBgC+(B $B5H@8(B | Charged Nanodroplet Evaporation Molecular Dynamics
| 2-f | 794 |
15:00$B!A(B 15:20 | $B5Y7F(B |
(15:20$B!A(B17:20) ($B:BD9(B $BG&B-(B $B51CK(B) |
15:20$B!A(B 15:40 | B320 | [$B8&5f>^(B] ($B8&5fBjL\(B)$B6I=jE*N.F0@)8f5Z$S@EEE>l$rMxMQ$7$?9b@:EYHyN3;RJ,5i$K4X$9$k8&5f(B
($B9-Bg(B) ($B@5(B)$B5HED(B $B1Q?M(B |
| 2-f | 621 |
15:40$B!A(B 16:00 | B321 | Spray pyrolysis synthesis of porous V2O5 cathode material of rechargeable lithium battery
($BEl9)Bg1!M}9)(B) ($B3X(B)$B!{(BKong Long$B!&(B ($B@5(B)$BC+8}(B $B@t(B | Spray pyrolysis porous V2O5 Cathode
| 2-f | 331 |
16:00$B!A(B 16:20 | B322 | $BIT5,B'7A>uN3;RGK:U$N(BADEM$B%7%_%e%l!<%7%g%s(B
($BElKLBg1!4D6-(B) ($B3X(B)$B!{@P86(B $B??8c(B$B!&(B ($BElKLBgB?858&(B) ($B@5(B)$BD%(B $BB6Ip(B$B!&(B ($B@5(B)$B2CG<(B $B=cLi(B | DEM breakage irregural shaped
| 2-f | 499 |
16:20$B!A(B 16:40 | B323 | $B6E=8NO:9$rMxMQ$7$?N3;R>uJ*
($B9-Bg1!9)(B) ($B@5(B)$B!{J!0f(B $B9qGn(B$B!&(B ($B3X(B)$BEOED(B $B42G7(B$B!&(B ($B@5(B)$B5HED(B $B1Q?M(B | Fluidized bed Agglomeration Component separation
| 2-f | 511 |
16:40$B!A(B 17:00 | B324 | $B%m!<%kB.EY$,0[$J$kQrCG7?%m!<%k@.7A5!$N@.7AJ*6/EY(B
($B%[%=%+%o%_%/%m%s(B) ($BK!(B)$B!{4dED(B $BIR><(B$B!&(B ($BK!(B)$B>.@>(B $B9'?.(B$B!&(B ($BK!(B)$BH+Cf(B $B?-(B$B!&(B ($BK!(B)$BLZFn(B $B85(B$B!&(B ($B%[%=%+%o%_%/%m%s(B/SCE$B!&(BNet) ($B@5(B)$B9B8}(B $BCi0l(B | Roller Press Roll speed Hard Coal/Biomass
| 2-f | 550 |
17:00$B!A(B 17:20 | B325 | $BN3;RI=LL=$>~>r7o$K$h$kJ,;6@-$HN3;R4VAj8_:nMQ$N:90[(B
($B%j%s%F%C%/(B/$BG@9)Bg(B) ($B@5(B)$B!{?9(B $B9d;V(B$B!&(B ($BG@9)Bg(B) ($B@5(B)$B?@C+(B $B=(Gn(B | Colloidal probe AFM Surface modification Interaction force
| 2-f | 219 |
C $B2q>l!&Bh(B 3 $BF|(B |
(9:00$B!A(B10:20) ($B:BD9(B $BKY9>(B $B9';K(B) |
9:00$B!A(B 9:20 | C301 | $BHyN3;RN.F0AXFb5$K"$N2#J}8~J,I[B'(B
($B85IY;3Bg(B) ($B@5(B)$B;3yu(B $BNLJ?(B | Fluidized Bed Fine Particles Lateral Bubble Distribution
| 2-c | 319 |
9:20$B!A(B 9:40 | C302 | $B5$K"EcFb%^%$%/%m%P%V%k$N1UAjJ*
($B;38}Bg(B) ($B@5(B)$B!{CfHx(B $B>!Ui(B$B!&(B ($BBgEg>&A%9b@l(B) ($B@5(B)$B8EK\(B $B7$B!&(B ($B;38}Bg1!0e(B) ($B@5(B)$B5HK\(B $B@?(B | Mass transfer coefficient Micro bubble Bubble interaction
| 2-d | 183 |
9:40$B!A(B 10:00 | C303 | $B%2%kFbN.F0$r9MN8$7$?%A%c%M%kN.$N?tCM2r@O(B
($B:eBg1!4p9)(B) ($B@5(B)$B!{9bLZ(B $BMNJ?(B$B!&(B ($B3X(B)$BCfK\(B $B??5A(B$B!&(B ($B@5(B)$B2,Ln(B $BBYB'(B | Hydrogel Drag reduction Numerical simulation
| 2-a | 537 |
10:00$B!A(B 10:20 | C304 | $BG.BPN.%Q%?!<%s$NAjE>0\8=>]$K$*$1$k%(%s%H%m%T!<@8@.B.EY:GBg86M}$NE,MQK!(B
($B:eBg1!4p9)(B) ($B@5(B)$B!{H<(B $B5.I'(B$B!&(B $B=EED(B $B7=8c(B$B!&(B ($B@5(B)$B2,Ln(B $BBYB'(B | Maximum Entropy Production Principle Thermal Marangoni Convection Pattern Formation
| F-1 | 700 |
10:20$B!A(B 10:40 | $B5Y7F(B |
(10:40$B!A(B12:00) ($B:BD9(B $B;03Q(B $BN4B@!&9bLZ(B $BMNJ?(B) |
10:40$B!A(B 11:00 | C306 | $B%U%i%C%H%R!<%H%Q%$%W7?%R!<%H%9%W%l%C%@$NG.EAF3N(?dDj(B
($B$B!&(B ($B5~Bg%((B) $BsnF#(B $BBY;J(B$B!&(B ($B$B!&(B ($B@5(B)$B8^Eg(B $B?r(B | thermal conductivity evaluation thermography
| 2-a | 634 |
11:00$B!A(B 11:20 | C307 | $B9bG4@-%l%$%j!
($B:k6LBg1!(B) ($B@5(B)$B!{K\4V(B $B=S;J(B$B!&(B ($B:k6LBg9)(B) $B9b8+_7(B $B?r(B$B!&(B ($B:k6LBg1!(B) ($B@5(B)$B8E4W(B $BFsO:(B$B!&(B (IHI) $BFb;3(B $B?i(B$B!&(B $BF#86(B $B42L@(B$B!&(B ($BElBg1!(B) ($B@5(B)$B | Rayleigh-Taylor Instability Viscous Fluids Front-Tracking
| 2-a | 353 |
11:20$B!A(B 11:40 | C308 | shear-thinning$BN.BN$K$*$1$k%F%$%i!
($B?@8MBg1!9)(B) ($B3X(B)$B!{A}ED(B $BM&?M(B$B!&(B ($B@5(B)$BKY9>(B $B9';K(B$B!&(B ($B%o%k%7%c%o9)Bg(B) Hubacz R.$B!&(B ($B?@8MBg1!9)(B) ($B@5(B)$BBgB<(B $BD>?M(B | Taylor-Couette flow shear-thinning fluid numerical analysis
| 2-a | 721 |
11:40$B!A(B 12:00 | C309 | [$B8&5f>)Ne>^(B] ($B8&5fBjL\(B)$BGvKl43>DN.F02hA|K!$rMQ$$$?9bJ,;R?-D9$,MpN.M^@)$KM?$($k1F6A$N2rL@(B
($B?@8MBg(B) ($B@5(B)$BF|=P4V(B $B$k$j(B |
| 2-a | 623 |
|
(13:00$B!A(B14:20) ($B:BD9(B $B:4Gl(B $BN4(B) |
13:00$B!A(B 13:20 | C313 | $B?6F03IYB$GH/@8$9$kGHF0$K$h$kG4EZ%U%m%C%/$NIbM7$K$D$$$F(B
($B0q>kBgG@(B) ($B@5(B)$B!{Bg0f(B $B@aCK(B$B!&(B $BCf@P(B $B9nLi(B$B!&(B $B?yK\(B $BKcH~(B | Clay-floc Vertical-transport Standing-waves
| 2-b | 740 |
13:20$B!A(B 13:40 | C314 | ($B9V1iCf;_(B)
|
| 100 | 467 |
13:40$B!A(B 14:00 | C315 | $B3IYB%7%_%e%l!<%7%g%s$K$h$k%[%b%_%-%5!
($B2V2&(B) ($B@5(B)$B!{@.Eg(B $B5#(B$B!&(B ($BK!(B)$B5\Ip(B $BNIOB(B$B!&(B ($B@5(B)$B>>K\(B $BBY@5(B | mixing simulation high-shear mixer pass number distribution
| 2-b | 50 |
14:00$B!A(B 14:20 | C316 | $B%^%$%/%mGH2CG.$r
($B7WB,%(%s%8%K%"%j%s%0(B) ($BK!(B)$B668}(B $B??59(B | maicrowave heating sttiring finite-element analysis
| 2-b | 902 |
14:20$B!A(B 14:40 | $B5Y7F(B |
(14:40$B!A(B16:00) ($B:BD9(B $B668}(B $B??59!&@.Eg(B $B5#(B) |
14:40$B!A(B 15:00 | C318 | CFD$B1gMQ$K$h$k%m!<%?!2A(B
($BL@<#(B) ($B@5(B)$B!{?@C+(B $BE/(B$B!&(B ($B@5(B)$B1)@8(B $B7=8c(B$B!&(B ($B2#9qBg(B) ($B@5(B)$B;03Q(B $BN4B@(B$B!&(B ($B@5(B)$B?N;V(B $BOBI'(B$B!&(B ($B@5(B)$B>e%N;3(B $B<~(B | rotor stator emulsification CFD
| 2-b | 887 |
15:00$B!A(B 15:20 | C319 | CFD$B1gMQ$K$h$k%m!<%?!
($BL@<#(B) ($B@5(B)$B!{?@C+(B $BE/(B$B!&(B ($B@5(B)$B1)@8(B $B7=8c(B$B!&(B ($B2#9qBg(B) ($B@5(B)$B;03Q(B $BN4B@(B$B!&(B ($B@5(B)$B?N;V(B $BOBI'(B$B!&(B ($B@5(B)$B>e%N;3(B $B<~(B | Scale up Emulsification CFD
| 2-b | 901 |
15:20$B!A(B 15:40 | C320 | $B@55U8r8_2sE>Mc3IYB$NN.F0!&F0NOFC@-(B
($B?@8MBg1!9)(B) ($B@5(B)$B!{8VED(B $B1YG7(B$B!&(B ($B3X(B)$B@gED(B $BAa5*(B$B!&(B ($B3X(B)$B;3>e(B $BE5G7(B$B!&(B ($B:eBg(B) ($B@5(B)$BJ?ED(B $BM:;V(B$B!&(B ($B?@8MBg1!9)(B) ($B@5(B)$BNkLZ(B $BMN(B$B!&(B ($B?@8MBg<+(B) ($B@5(B)$BF|=P4V(B $B$k$j(B | Power requirement PIV Vortex
| 2-b | 725 |
15:40$B!A(B 16:00 | C321 | $B3IYBMc$N5/F0%H%k%/$HMc7A>u$N4X78(B
($B2#9qBg1!9)(B) ($B@5(B)$B!{?N;V(B $BOBI'(B$B!&(B ($B3X(B)$B:dEl(B $BM4??(B$B!&(B ($B@5(B)$B;03Q(B $BN4B@(B$B!&(B ($B@5(B)$B>e%N;3(B $B<~(B | start-up torque paddle impeller large type impeller
| 2-b | 159 |
(16:00$B!A(B17:00) ($B:BD9(B $B8VED(B $B1YG7!&?@C+(B $BE/(B) |
16:00$B!A(B 16:20 | C322 | $B3IYB1):,$X$N8GBNN3;R$N>WFM8=>]$KBP$9$kN3;RFC@-$N1F6A(B
($B2#9qBg9)(B) ($B@5(B)$B!{;03Q(B $BN4B@(B$B!&(B ($B3X(B)$BHSEg(B $B9-@.(B$B!&(B ($B3X(B)$B8MB<(B $B=S(B$B!&(B ($B@5(B)$B?N;V(B $BOBI'(B$B!&(B ($B@5(B)$B>e%N;3(B $B<~(B | solid-liquid mixing crystallization CFD
| 2-b | 863 |
16:20$B!A(B 16:40 | C323 | $B%(%l%a%s%H@QAX7?%9%?%F%#%C%/%_%-%5!<$N3+H/$H:.9g@-G=$NDjNLE*I>2A(B
($B%"%$%;%k(B) ($B@5(B)$B!{K>7n(B $B>:(B$B!&(B ($B;38}Bg1!M}9)(B) ($B@5(B)$B:4Gl(B $BN4(B$B!&(B ($B3X(B)$BMh@4(B $B9'L@(B | Mixing Static mixer Stacked element
| 2-b | 321 |
16:40$B!A(B 17:00 | C324 | $B:.N}2aDx$NN.F0MM<0(B:$B6I=jE*$JDjNL2=$HBg0hE*$J:.9g$X$NF6;!(B
($B6eBg9)(B) ($B@5(B)$B!{L>2E;3(B $B>MLi(B$B!&(B ($B%f%K%A%+(B) $B@5LZ(B $BC$E5(B$B!&(B ($B6eBg9)(B) ($B@5(B)$B3a86(B $BL->0(B | mixing strain-rate rheology
| 2-b | 9 |