$B9V1i(B $B;~9o(B | $B9V1i(B $BHV9f(B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $BJ,N`(B $BHV9f(B | $B$BHV9f(B | |
F$B2q>l(B $BBh(B1$BF|(B |
(9:00$B!A(B10:20)$B!!(B($B:BD9(B $BEgED(B $BD> |
9:00$B!A(B 9:20 | F101 | $B29EY:9$HG;EY:9$K5/0x$9$k%^%i%s%4%KBPN.$N6&B88z2L$H%R%9%F%j%7%9FC@-(B
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| 2-a | 204 |
9:20$B!A(B 9:40 | F102 | $B1UKl>e%5!<%b%-%c%T%i%j!u$N1F6A$K4X$9$k?tCM2r@O(B
($B:eBg1!4p9)(B) $B!{(B($B3X(B)$B;3K\(B $BBnLi(B $B!&(B ($B@5(B)$B9bLZ(B $BMNJ?(B $B!&(B ($B@5(B)$B2,Ln(B $BBYB'(B | Marangoni Thermocapillary Numerical Simulation
| 2-a | 1 |
9:40$B!A(B 10:00 | F103 | $B4pHD>e$K$*$1$k9bJ,;R(B/2$B@.J,MOG^7O1UE)Fb$N0\F08=>]2r@O(B
($B6eBg1!9)(B) $B!{(B($B3X(B)$B54DM(B $B7rFs(B $B!&(B ($B3X(B)$BFnN$(B $B8yH~(B $B!&(B ($B6eBg9)(B) ($B@5(B)$BCfA>(B $B9@0l(B $B!&(B ($B@5(B)$B?<0f(B $B=a(B | Droplet Internal flow Heat and mass transfer
| 2-a | 687 |
10:00$B!A(B 10:20 | F104 | $B8GBNI=LL>e$NKl>u6E=L$N?tCM2r@O(B
($B:k6LBg9)(B) $B!{(B($B@5(B)$BK\4V(B $B=S;J(B $B!&(B $B6b;R(B $B98(B $B!&(B ($B@5(B)$B8E4W(B $BFsO:(B | Film Condensation Numerical Simulation Front-Tracking
| 2-a | 286 |
(10:20$B!A(B11:40)$B!!(B($B:BD9(B $B>>7((B $BMN2p(B) |
10:20$B!A(B 10:40 | F105 | $B46291U>=(BPIV$B$rMQ$$$?Fs=E3H;66-3&LL$N9=B$2r@O(B
($BIY;3Bg9)(B) $B!{(B($B@5(B)$B;3:,(B $B3Y;V(B $B!&(B ($B@5(B)$B5HED(B $B@5F;(B $B!&(B $B0kIt(B $B@2:Z(B $B!&(B $BC+8}(B $BBsLo(B $B!&(B $B | double-diffusion interface PIV
| 2-a | 732 |
10:40$B!A(B 11:00 | F106 | $BG.HhO+I>2A$N$?$a$N9bDc29N.BN9gN.It$K$*$1$kN.BN$H9=B$$N29EYJQF0$N(BLES$B2r@O(B
($BF|4x(B) $B!{(B($B@5(B)$BA,(B $B>R>M(B $B!&(B $B6b4](B $B?-0lO:(B $B!&(B ($BElBg9)(B) $B3^86(B $BD>?M(B | Thermal Fatigue Temperature Fluctuation Large Eddy Simulation (LES)
| 2-a | 258 |
11:00$B!A(B 11:20 | F107 | $BCf@-;R@~(BCT$B$rMQ$$$?N.DL<0D6NW3&?eG.9g@.AuCVFb$G$N:.9g>uBV$N(Bin situ$B4Q;!(B
($BElKLBgB?858&(B) $B!{(B($B@5(B)$B9b8+(B $B@?0l(B $B!&(B ($BElKLBg1!9)(B) ($B3X(B)$B>._7(B $B63J<(B $B!&(B ($B@5(B)$B?y2,(B $B7r0l(B $B!&(B ($B@5(B)$BDMED(B $BN4IW(B $B!&(B ($BElKLBg(BWPI) ($B@5(B)$B0$?,(B $B2mJ8(B $B!&(B ($B?@8MBg1!9)(B) $B?yK\(B $B>!H~(B $B!&(B $BC]Cf(B $B?.9,(B $B!&(B ($B5~Bg86;RO'(B) $BsnF#(B $BBY;J(B | neutron radiography computed tomography flow-type reactor
| 2-a | 78 |
11:20$B!A(B 11:40 | F108 | $BD6NW3&?eG.9g@.H?1~4oFb$NN.F0!$?eL)EY5Z$S29EYJ,I[$N?tCM%7%_%e%l!<%7%g%s(B
($BElKLBg1!9)(B) $B!{(B($B3X(B)$B>._7(B $B63J<(B $B!&(B ($B@5(B)$B?y2,(B $B7r0l(B $B!&(B ($BElKLBgB?858&(B) ($B@5(B)$B9b8+(B $B@?0l(B $B!&(B ($BElKLBg1!9)(B) ($B@5(B)$BDMED(B $BN4IW(B $B!&(B ($BElKLBg(BWPI) ($B@5(B)$B0$?,(B $B2mJ8(B $B!&(B ($B?@8MBg1!9)(B) $B?yK\(B $B>!H~(B $B!&(B $BC]Cf(B $B?.9,(B $B!&(B ($B5~Bg86;RO'(B) $BsnF#(B $BBY;J(B | numerical simulation supercritical hydrothermal synthesis neutron radiography
| 2-a | 494 |
(11:40$B!A(B12:00)$B!!(B($B:BD9(B $BK\4V(B $B=S;J(B) |
11:40$B!A(B 12:00 | F109 | [$BN3;R!&N.BN%W%m%;%9It2q%7%s%]%8%&%`>^(B($B>)Ne>^(B)]$BB?Aj8rN.%"!<%/$N9b29>l$N@)8f$K$h$k%$%s%U%i%$%H%,%i%9MOM;$N9b8zN(2=(B
($BEl9)Bg1!AmM}9)(B) $B!{(B($B@5(B)$BEDCf(B $B3X(B $B!&(B $BN-(B $B2mhL(B $B!&(B $BCS>l(B $BM' $B!&(B $BVC(B $B=( $B!&(B ($B@5(B)$BEOJU(B $BN49T(B | Thermal plasmas Multi-phase arc In-flight melting
| 2-a | 324 |
|
(13:00$B!A(B14:00)$B!!(B($B:BD9(B $BNkLZ(B $BMN(B) |
13:00$B!A(B 13:20 | F113 | $BNdK<29EY0h$K$*$1$k3&LL3h@-:^?eMO1U$NDq93Dc8:8z2L$HEAG.FC@-(B
($B;38}Bg1!M}9)(B) $B!{(B($B@5(B)$B:4Gl(B $BN4(B $B!&(B $BEDCf(B $BD>(B $B!&(B $B>.NS(B $B<~J?(B $B!&(B $B=EB<(B $BCR;K(B | Drag reduction Heat transfer Surfactant
| 2-a | 750 |
13:20$B!A(B 13:40 | F114 | $B6I=j$9$Y$jB.EY$rM-$9$k5!G=@-EIKl>eMpN.$N?tCM%7%_%e%l!<%7%g%s(B
($B:eBg1!4p9)(B) $B!{(B($B@5(B)$B9bLZ(B $BMNJ?(B $B!&(B ($B:eBg4p9)(B) $BCfK\(B $B??5A(B $B!&(B ($B:eBg1!4p9)(B) ($B@5(B)$B2,Ln(B $BBYB'(B | Turbulent flow Functional coating film Numerical simulation
| 2-a | 211 |
13:40$B!A(B 14:00 | F115 | $B8G5$J,;6N.$K$*$1$kFsAj4VNO$HBg5,LON.BNMpN.9=B$$NAj4X(B
($BKL8+9)Bg(B) $B!{(B($B@5(B)$B;08M(B $BM[0l(B | gas-solid disperse flow inter-phase force direct numerical simulation
| 2-a | 282 |
(14:00$B!A(B15:00)$B!!(B($B:BD9(B $B0f>e(B $B5AO/(B) |
14:00$B!A(B 14:20 | F116 | $BEAG.%3%$%kIU3IYBAe$N=jMWF0NO$NAj4X(B
($BL>9)Bg(B) ($B3X(B)$B8E@n(B $BM[51(B $B!&(B ($B@5(B)$B2CF#(B $BDw?M(B $B!&(B $B!{(B($B3X(B)$B0KF#(B $B?8B@O/(B $B!&(B ($B@5(B)$BB?ED(B $BK-(B | mixing power consumption coil
| 2-b | 3 |
14:20$B!A(B 14:40 | F117 | $B3Q7?3IYBAe$N=jMWF0NO$NAj4X(B
($BL>9)Bg(B) ($B3X(B)$B8E@n(B $BM[51(B $B!&(B ($B@5(B)$B2CF#(B $BDw?M(B $B!&(B $B!{(B($B3X(B)$B? $B!&(B ($B@5(B)$BB?ED(B $BK-(B | mixing power consumption rectangular vessel
| 2-b | 7 |
14:40$B!A(B 15:00 | F118 | 2$BCJ%3%s%1!<%V%?!<%S%s$NDL5$F0NO(B
($B%@%$%;%k(B) ($B@5(B)$B550f(B $BEP(B $B!&(B ($BL>9)Bg(B) ($B@5(B)$B2CF#(B $BDw?M(B $B!&(B $B!{(B($B3X(B)$BNkLZ(B $BCRLi(B $B!&(B ($B3X(B)$B8E@n(B $BM[51(B $B!&(B ($B@5(B)$BB?ED(B $BK-(B | mixing power consumption gas-liquid
| 2-b | 8 |
(15:00$B!A(B16:00)$B!!(B($B:BD9(B $B2CF#(B $BDw?M(B) |
15:00$B!A(B 15:20 | F119 | $BA:@-N.BN$rBP>]$H$7$?DL5$3IYBAe$K$*$1$k5$K"5sF0$,:.9gB%?J$K5Z$\$91F6A$N8!F$(B
($B2#9qBg9)(B) $B!{(B($B3X(B)$BCSED(B $B??0l(B $B!&(B ($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 $B<~(B | aerated mixing cavern plastic fluid
| 2-b | 550 |
15:20$B!A(B 15:40 | F120 | $B%^%C%/%9%V%l%s%IJP?43IYBAe$K$*$1$kF0NO$*$h$S:.9g;~4V$K5Z$\$9%9%1!<%k%"%C%W$N1F6A(B
($B2#9qBg1!9)(B) $B!{(B($B3X(B)$B1`ED(B $B0l;K(B $B!&(B ($B@5(B)$B?N;V(B $BOBI'(B $B!&(B ($B@5(B)$B;03Q(B $BN4B@(B $B!&(B ($B@5(B)$B>e%N;3(B $B<~(B | eccentric mixing Maxblend impeller scale up effect
| 2-b | 664 |
15:40$B!A(B 16:00 | F121 | $B@55U8r8_2sE>Mc$N:.9gITNI0h7A@.$K5Z$\$9Mc7B$N1F6A(B
($B?@8MBg9)(B) $B!{(B($B3X(B)$B@gED(B $BAa5*(B $B!&(B ($B@5(B)$B8VED(B $B1YG7(B $B!&(B ($B%"!<%k%U%m!<(B) ($B@5(B)$BC]ED(B $B9((B $B!&(B ($B:eBg(B) ($B@5(B)$BJ?ED(B $BM:;V(B $B!&(B ($B?@8MBg9)(B) ($B@5(B)$BNkLZ(B $BMN(B $B!&(B ($B@5(B)$BF|=P4V(B $B$k$j(B | unsteady mixing impeller diameter poor mixing region
| 2-b | 312 |
(16:00$B!A(B17:00)$B!!(B($B:BD9(B $B?N;V(B $BOBI'(B) |
16:00$B!A(B 16:20 | F122 | $BBPN.:.9g$N4pK\9=B$(B
($B85:eBg(B) $B!{(B($B@5(B)$B0f>e(B $B5AO/(B | Fluid Mixing Convective Mixing Mechanism of Mixing
| 2-b | 63 |
16:20$B!A(B 16:40 | F123 | MPS$BK!$K$h$kYxYBAeFb$NN.$l$N?tCM2r@O$HZ(B
($B9=B$7W2h8&5f=j(B) $B!{(B($B@5(B)$B;3ED(B $B9d;K(B $B!&(B ($B;q@8F2(B) ($B@5(B)$BEDCf(B $B:L(B | MPS mixing CFD
| 2-b | 334 |
16:40$B!A(B 17:00 | F124 | $B%N%s%(%l%a%s%H%_%-%5!<$K$h$kHs%K%e!<%H%sN.BN$N:.9gB%?J(B
($B7DXfBgM}9)(B) $B!{(B($B3X(B)$B;\(B $BD%FR(B $B!&(B $B2#?9(B $B9d(B $B!&(B ($B@5(B)$B?"ED(B $BMx5W(B | Non-Newtonian fluid Non-element mixer chaotic mixing
| 2-b | 13 |
G$B2q>l(B $BBh(B1$BF|(B |
(9:00$B!A(B10:00)$B!!(B($B:BD9(B $B>e;3(B $B0T0l(B) |
9:00$B!A(B 9:20 | G101 | V$B;z4IFb$N%9%i%C%.%s%08=>]$K4X$9$k8&5f(B
($B@iBeED2=9)7z@_(B) $B!{F~AR(B $B4p $B!&(B $BA0@n(B $B=!B'(B $B!&(B ($B?@8MBg1!9)(B) $B:Y@n(B $BLPM:(B $B!&(B $BIZ;3(B $BL@CK(B | Slugging V-shaped elbow Flow regime
| 2-e | 41 |
9:20$B!A(B 9:40 | G102 | $B=Z(B
(IHI) $B!{(B($B@5(B)$B2+(B $B7r(B $B!&(B $B2CF#(B $B??M};R(B $B!&(B $B0k(B $BNI9T(B $B!&(B $B>>Ln(B $B?-2p(B | Gas-Liquid Film Flows CFD Packing Columns
| 2-e | 513 |
9:40$B!A(B 10:00 | G103 | Interaction between Two Moving Jets in Immiscible Liquid-Liquid Systems: An Experimental Study
(Curtin U. Tech.) Parmar Harisinh $B!&(B Pareek Vishnu $B!&(B Phan Chi M. $B!&(B (U. Hyogo) $B!{(B($B@5(B)Asakuma Yusuke $B!&(B (U. Newcastle) Evans Geoffrey | Emulsion Explosive Multiphase flow Micro fluidic
| 2-e | 573 |
(10:00$B!A(B11:00)$B!!(B($B:BD9(B $B0BED(B $B7<;J(B) |
10:00$B!A(B 10:20 | G104 | $BL5
($BFAEgBg1!(BSTS) $B!{(B($B@5(B)$BB@ED(B $B8w9@(B | Bubble and drop Dynamic motion Dimensionless number
| 2-e | 305 |
10:20$B!A(B 10:40 | G105 | $B%Q%i%\%j%C%/%U%i%$%H$K$h$k(B1/6$B=ENO4D6-Cf$G$NLO5<7n:=N3;R$N5$Aj3H;6(B
($BBg:eBgC+Bg(B) $B!{(B($B@5(B)$BKR(B $B>M(B $B!&(B (JAXA) $BK\4V(B $BA1G7(B $B!&(B $B@DLZ(B $B<"(B $B!&(B $BIp2,(B $B85(B $B!&(B $B;0LZ(B $BLT@8(B $B!&(B $BBgEg(B $BGn(B $B!&(B $B;3K\(B $B2mJ8(B $B!&(B $B8~0f(B $B@i=)(B $B!&(B ($B;:0eBg(B) $B?9K\(B $BBYIW(B $B!&(B ($B0B1R8&(B) $B>.@n(B $B9/63(B | partial gravity dust exposure regolith
| 2-e | 378 |
10:40$B!A(B 11:00 | G106 | $B%J%N%P%V%k$K$*$1$kD62;GH>H
($BJ!;3Bg9)(B) $B!{(B($B@5(B)$B7*1d(B $B=SB@O:(B $B!&(B ($B6(OB5!@_(B) $BDT(B $B=(BY(B | Nano-Bubbles Ultrasound Annihilation
| 2-e | 108 |
(11:00$B!A(B12:00)$B!!(B($B:BD9(B $BB@ED(B $B8w9@(B) |
11:00$B!A(B 11:20 | G107 | $B8w@~DI@W%7%_%e%l!<%7%g%s$K4p$E$/8w%U%!%$%P!<%W%m!<%V$rMQ$$$?5$K"N.7WB,(B
($B@EBg1!9)(B) $B!{(B($B3X(B)$B8E;T(B $BH%(B $B!&(B ($B@5(B)$B:dK\(B $BL@MN(B $B!&(B ($B3X(B)$B?eEh(B $BM44p(B $B!&(B ($B@EBgAO2J1!(B) ($B@5(B)$Bc7F#(B $BN4G7(B | Optical fiber probe Bubble measurement Ray tracing
| 2-e | 69 |
11:20$B!A(B 11:40 | G108 | MH$BHoJ$5$K"$N>e>:B.EY$J$i$S$K93NO78?t$K4X$9$k0l9M;!(B
($B;:Am8&(B) ($B@5(B)$B:4F#(B $B9/@2(B $B!&(B $B!{(B($B@5(B)$B@6Ln(B $BJ8M:(B $B!&(B $B>.3^86(B $B7<0l(B $B!&(B ($B@5(B)$B;3K\(B $B2B9'(B $B!&(B ($BEl3$Bg(B) $B@6?e(B $B2lG7(B | Hydrate Bubble Drag coefficient
| 2-e | 128 |
11:40$B!A(B 12:00 | G109 | $B05NO?6F0>l$K$*$1$kC10l5$K"6aK5N.F0>l$N(B2$B
($BL>9)Bg1!(B) $B!{(B($B3X(B)$BCf;3(B $B98?-(B $B!&(B ($B@5(B)$B4dED(B $B=$0l(B $B!&(B ($B@5(B)$B?9(B $B=( $B!&(B ($BD92,5;2JBg(B) ($B@5(B)$B9b66(B $BJY(B $B!&(B ($B1'ET5\Bg(BCORE/$B%U%)%H%m%s(B) $BBg>B(B $BH;;V(B $B!&(B ($BL>9)Bg1!(B) ($B@5(B)$BFn1@(B $BN<(B | pressure-oscillating birefringence viscoelastic fluid
| 2-a | 509 |
|
(13:00$B!A(B14:00)$B!!(B($B:BD9(B $B4dED(B $B=$0l(B) |
13:00$B!A(B 13:20 | G113 | $B5$1U:.AjN.%7%_%e%l!<%?$NFC@-$*$h$S4JJX$J7W;;%"%k%4%j%:%`(B
($B9)3X1!Bg9)(B) $B!{(B($B@5(B)$B>e;3(B $B0T0l(B | gas-liquid multiphase flow simulator pressure equation
| 2-d | 2 |
13:20$B!A(B 13:40 | G114 | $B5$1U==;zN.<0B?9&HDEc$N1UAjJ*uBV$N1F6A(B
($B;38}Bg(B) $B!{(B($B@5(B)$BCfHx(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 $B@?(B | Mass transfer coefficient Sieve plate column Bubble interactions
| 2-d | 64 |
13:40$B!A(B 14:00 | G115 | $B%^%$%/%m%P%V%k$K$h$k(BO/W$B%(%^%k%7%g%sJ,N%$K5Z$\$93&LL3h@-:^$N1F6A(B
($BL>Bg1!9)(B) $B!{(B($B3X(B)$B8eF#(B $B9,9((B $B!&(B ($B@5(B)$B0BED(B $B7<;J(B | emulsion surfactant microbubbles
| 2-d | 106 |
(14:00$B!A(B15:00)$B!!(B($B:BD9(B $B;3K\(B $BNL0l(B) |
14:00$B!A(B 14:20 | G116 | $B=[4D7?5$K"Ec$K$*$1$k5$1U%U%m!<%Q%?!<%s$N2r@O$H%*%>%s%,%9MO2rFC@-(B
($B6e9)Bg1!9)(B) $B!{(B($B3X(B)$B;3K\(B $BM35.(B $B!&(B ($B@5(B)$BGOEO(B $B2B=((B $B!&(B ($B@5(B)$B;3B<(B $BJ}?M(B $B!&(B ($B@5(B)$B | bubble column ozonation flow pattern
| 2-d | 794 |
14:20$B!A(B 14:40 | G117 | $B%^%$%/%mN.O)Fb$N5$1UCl0\F0FC@-(B
($B?@8MBg9)(B) $B!{(B($B3X(B)$B?9(B $B=_J?(B $B!&(B ($B?@8MBg1!(B) ($B3X(B)$BAj86(B $B9(I'(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 $B!&(B ($B?@8MBg1!9)(B) ($B@5(B)$B8VED(B $B1YG7(B | Gas/Liquid Interface Micro-Channel Liposome
| 2-a | 251 |
14:40$B!A(B 15:00 | G118 | $BBg5,LO(B3$BZ(B
($BElBg1!9)(B) $B!{(B($B3X(B)$B0$It(B $BM[(B $B!&(B ($BElBg9)(B) ($B@5(B)$B | Fluidized bed DEM Coarse grain model
| 2-f | 381 |
(15:00$B!A(B16:00)$B!!(B($B:BD9(B $B2CG<(B $B=cLi(B) |
15:00$B!A(B 15:20 | G119 | $BCF@-%V%l!<%I$rMQ$$$?J4BN:.9g$N?tCM%7%_%e%l!<%7%g%s(B
($BElBg9)(B) $B!{(B($B3X(B)$B?eC+(B $B?5(B $B!&(B ($B@5(B)$B | Granular analysis Elastic body analysis Powder mixing
| 2-f | 435 |
15:20$B!A(B 15:40 | G120 | $BN3;R72$NN3EYJP@O$K5Z$\$9N3;R7A>u$*$h$SN3;R7BJ,I[$N1F6A(B
($BF1;V $B!&(B ($B@5(B)$BGr@n(B $BA19,(B $B!&(B ($B@5(B)$BF|9b(B $B=E=u(B | DEM simulation segregation index percolation index
| 2-f | 203 |
15:40$B!A(B 16:00 | G121 | DEM-LES$B%O%$%V%j%C%I%7%_%e%l!<%7%g%s$K$h$kJ4BNEIAuFC@-$N2r@O(B
($BF1;V $B!&(B ($B3X(B)$BK\ED(B $B9000(B $B!&(B ($B@5(B)$B2<:d(B $B8|;R(B $B!&(B ($B@5(B)$BGr@n(B $BA19,(B $B!&(B ($B@5(B)$BF|9b(B $B=E=u(B | DEM powder coating simulation
| 2-f | 256 |
(16:00$B!A(B17:20)$B!!(B($B:BD9(B $B |
16:00$B!A(B 16:20 | G122 | $BN3;R%Y!<%99dBN%b%G%k$rMxMQ$7$?%I%i%`7?>W7b<0GK:U5!$K$*$1$kItIJC&N%5!9=$K4X$9$k4pACE*8&5f(B
($BAaBg1!(B) $B!{(B($B3X(B)$BED86(B $B0l51(B $B!&(B ($B3X(B)$B9K_7(B $BM-51(B $B!&(B ($B@5(B)$B=j(B $B@i@2(B $B!&(B $BBgOBED(B $B=(Fs(B | Discrete element method Particle-based rigid body model Drum typed agitation mill
| 2-f | 394 |
16:20$B!A(B 16:40 | G123 | $BN3;RGK2u5sF0$N%7%_%e%l!<%7%g%s(B
($BElKLBgB?858&(B) ($B3X(B)$B@P86(B $B??8c(B $B!&(B ($B@5(B)$BD%(B $BB6Ip(B $B!&(B $B!{(B($B@5(B)$B2CG<(B $B=cLi(B $B!&(B ($B3X?6(B) ($B@5(B)$BA>ED(B $BNO1{(B | DEM breakage grinding
| 2-f | 518 |
16:40$B!A(B 17:00 | G124 | $B?6F04pHD>e$NHyN3;R5sF0$N2r@O(B
($B5~Bg9)(B) $B!{(B($B3X(B)$B:dED(B $B8w1{(B $B!&(B ($B3X(B)$B>.Aa@n(B $B@NN%Ln(B $B!&(B $B0BED(B $B@5=S(B $B!&(B ($B@5(B)$B>>:d(B $B=$Fs(B | fine particle vibration adhesion force
| 2-f | 134 |
17:00$B!A(B 17:20 | G125 | Adhesion Characteristics of Charged Fine Particles
(Kyoto U.) $B!{(B($B3X(B)Wei Dan $B!&(B ($B@5(B)Matsusaka Shuji | charged particle electric field adhesion force
| 2-f | 191 |
G$B2q>l(B $BBh(B3$BF|(B |
(9:00$B!A(B10:20)$B!!(B($B:BD9(B $B;3K\(B $BE0Li(B) |
9:00$B!A(B 9:20 | G301 | $B%0%i%$%G%#%s%0%"!<%/J|EE$rF3F~$7$?%5%$%/%m%s$K$h$kN3;R$N=hM}(B
($BEl9)Bg1!M}9)(B) $B!{(B($B@5(B)$B4X8}(B $B=(=S(B $B!&(B ($B@5(B)$B>.6L(B $BAo(B $B!&(B $B5\:j(B $BOBN<(B | cyclone gliding arc discharge particle treatment
| 2-f | 499 |
9:20$B!A(B 9:40 | G302 | $B:.9gN3;R=
($BIY;3Bg1!M}9)(B) $B!{(B($B3X(B)$B]/0f(B $BBs:H(B $B!&(B ($B@5(B)$B9b@%(B $B6Q(B | electroosmotic flow rate particle packed bed Debye length
| 2-f | 226 |
9:40$B!A(B 10:00 | G303 | $B<+8JAH?%2=$rMxMQ$7$?J.L8G.J,2rK!$K$h$kGr6bC4;}%+!<%\%s%J%N9=B$BN:`NA$N9g@.(B
($B9-Bg1!9)(B) $B!{(B($B@5(B)$B2.(B $B?r(B $B!&(B Ratna Balgis $B!&(B ($B@5(B)$B1|;3(B $B4n5WIW(B $B!&(B ($B%N%j%?%1%+%s%Q%K!<%j%_%F%I(B) Anilkumar G. M. $B!&(B $B:89g(B $B@!?M(B | nanoparticle spray pyrolysis Proton exchange membrane fuel cell
| 2-f | 274 |
10:00$B!A(B 10:20 | G304 | $B%(%"%m%>%k%W%m%;%9$K$h$k%3%"%7%'%k%J%NN3;R$N9g@.(B
($B6bBtBg1!M}9)(B) $B!{(B($B3X(B)$BBgFb(B $B9/5W(B $B!&(B $BCf_7(B $BBnLi(B $B!&(B ($B6bBtBgM}9)(B) ($B@5(B)$B@%8M(B $B>OJ8(B $B!&(B ($B@5(B)$BBgC+(B $B5H@8(B | core shell nanoparticle aerosol process laser ablation
| 2-f | 527 |
(10:20$B!A(B11:40)$B!!(B($B:BD9(B $B9b@%(B $B6Q(B) |
10:20$B!A(B 10:40 | G305 | $B4%<0%5%$%/%m%s$N6I=jE*N.F0@)8f$,N3;RJ,N%@-G=$K5Z$\$91F6A(B
($B9-Bg1!9)(B) ($B3X(B)$BJ?4d(B $BM'M4(B $B!&(B $B!{(B($B@5(B)$B5HED(B $B1Q?M(B $B!&(B ($B@5(B)$B;3K\(B $BE0Li(B $B!&(B ($B@5(B)$BJ!0f(B $B9qGn(B $B!&(B ($BAn8&2=3X(B) ($B@5(B)$BG&B-(B $B51CK(B | Particle setaration Dry-cyclone separation efficiency
| 2-f | 283 |
10:40$B!A(B 11:00 | G306 | $B=P8}4I>eIt$G$NN.F0@)8f$,4%<0%5%$%/%m%sJ,5i@-G=$KM?$($k1F6A(B
($B9-Bg1!9)(B) $B!{(B($B3X(B)$BOF1`(B $BM55*(B $B!&(B ($B@5(B)$B5HED(B $B1Q?M(B $B!&(B ($B@5(B)$BJ!0f(B $B9qGn(B $B!&(B ($B@5(B)$B;3K\(B $BE0Li(B $B!&(B ($BAn8&2=3X(B) ($B@5(B)$BG&B-(B $B51CK(B | Particle Separation Dry-cyclone Separation efficiency
| 2-f | 496 |
11:00$B!A(B 11:20 | G307 | $BEE5$1KF0$rMQ$$$?O"B37??edA$NJ,5i@-G=I>2A(B
($B9-Bg1!9)(B) $B!{(B($B@5(B)$BB<>e(B $B8x0R(B $B!&(B ($B@5(B)$B5HED(B $B1Q?M(B $B!&(B ($B@5(B)$B;3K\(B $BE0Li(B $B!&(B ($B@5(B)$BJ!0f(B $B9qGn(B $B!&(B ($BF|N)2=@.(B) ($B@5(B)$B9b0f(B $B7r $B!&(B ($B@5(B)$B>>Bt(B $B8w@2(B | Classification Water sieve Electrophoresis
| 2-f | 501 |
11:20$B!A(B 11:40 | G308 | $B%^%$%/%mGH2CG.$K$h$k6bB0>K;@1v:.9g?eMO1U$NC&>KH?1~(B
($B9-Bg1!9)(B) $B!{(B($B@5(B)$BJ!0f(B $B9qGn(B $B!&(B ($B3X(B)$B0f@n(B $BM'2p(B $B!&(B ($B@5(B)$B;3K\(B $BE0Li(B $B!&(B ($B@5(B)$B5HED(B $B1Q?M(B $B!&(B ($B86;RNO5!9=(B) ($B@5(B)$B@%@n(B $BCR?C(B $B!&(B $BNkLZ(B $B@/9@(B | Metallic oxide Microwave Denitration
| 2-f | 103 |
(11:40$B!A(B12:00)$B!!(B($B;J2q(B $B8eF#(B $BK.>4(B) |
11:40$B!A(B 12:00 | G309 | [$B8&5f>)Ne>^(B]AFM$B$K$h$kN3;RJ*@-I>2A$H$=$l$rMxMQ$7$?<><0J,5i%W%m%;%9$N3+H/(B
($B9-Bg1!9)(B) $B!{(B($B@5(B)$B;3K\(B $BE0Li(B | The SCEJ Young Investigator Researcher Award
| 2-f | 804 |
|
(13:00$B!A(B14:00)$B!!(B($B:BD9(B $BLnED(B $BNh<#(B) |
13:00$B!A(B 13:20 | G313 | $BN.F0AXFb$K$*$1$kN3;R4%Ag2aDx$N(BDEM-CFD$B%b%G%k3+H/(B
($B:eBg1!9)(B) $B!{(B($B3X(B)$B@>Eh(B $B9/9T(B $B!&(B ($B@5(B)$BDT(B $BBsLi(B $B!&(B ($B@5(B)$BEDCf(B $BIR;L(B | DEM-CFD coupling simulation fluidized bed heat and mass transfer
| 2-c | 756 |
13:20$B!A(B 13:40 | G314 | $B5$K"N.F0AXCf$KB8:_$9$kAFBgJ*BN$N5sF0M=B,%b%G%k3+H/(B
($B:eBg1!9)(B) $B!{(B($B3X(B)$BElED(B $B63J?(B $B!&(B $B1|;3(B $B2BFa(B $B!&(B $BDT(B $BBsLi(B $B!&(B ($B@5(B)$BEDCf(B $BIR;L(B | Fluidized bed DEM-CFD coupling simulation
| 2-c | 65 |
13:40$B!A(B 14:00 | G315 | $B%i%$%6!<$NEy2A2sO)%b%G%k2=(B
($BElBg@88&(B) $B!{(B($B@5(B)$B@PB+(B $B??E5(B $B!&(B ($B3X(B)$B5H9>(B $BM*;K(B $B!&(B ($B@5(B)$B4Eht(B $B $B!&(B ($B@5(B)$BDi(B $BFX;J(B | Fluidized bed Equivalent circuit model Flow behavior
| 2-c | 782 |
(14:00$B!A(B15:00)$B!!(B($B:BD9(B $BDT(B $BBsLi(B) |
14:00$B!A(B 14:20 | G316 | $BN.F0AX2=3X>xCeK!$K$h$jD4@=$5$l$?C:AGA!0]HoJ$N3;R$NN.F02=5sF0(B
($B72Bg1!9)(B) $B!{(B($B3X(B)$B6=DE(B $BJ8:H(B $B!&(B ($B@5(B)$BLnED(B $BNh<#(B | carbon fiber-covered particles fluidization behavior cohesive particles
| 2-c | 399 |
14:20$B!A(B 14:40 | G317 | $BB?<
($B72Bg1!9)(B) $B!{(B($B3X(B)$BD.ED(B $BM&Lo(B $B!&(B ($B@5(B)$BLnED(B $BNh<#(B | ICFG biomass circulatinh
| 2-c | 416 |
14:40$B!A(B 15:00 | G318 | Spout-Fluid Bed$B$NN.F0FC@-(B
($BJ!2,Bg9)(B) $B!{(B($B@5(B)$B1JEg(B $BBg(B $B!&(B ($B3X(B)$B>>Hx(B $B63Je(B $B!&(B ($B@5(B)$B@Pi6(B $BMxJ8(B | spout-fluid bed maximum spoutable bed depth PIV
| 2-c | 691 |
(15:00$B!A(B16:00)$B!!(B($B:BD9(B $BF|=P4V(B $B$k$j(B) |
15:00$B!A(B 15:20 | G319 | $B5!G=@-G^BNN.F0AX$K$h$k9b4^?e@-%2%k>uJ*
($B%+%J%((B) $B!{(B($B@5(B)$BBgJ?(B $BBg0l(B $B!&(B $B@PEO(B $B?.G7(B $B!&(B ($BIY;N%7%j%7%"2=3X(B) $B9uED(B $B@6(B $B!&(B ($B@5(B)$B@uLn(B $BC#Li(B $B!&(B ($B@5(B)$B0KF#(B $BKS90(B $B!&(B ($B@EBg(B) ($B@5(B)$BN)85(B $BM:<#(B $B!&(B ($BEl9)Bg(B) ($B@5(B)$BCfLn(B $B5AIW(B | dehydration of hydrogel functional porous media fluidized bed
| 2-c | 337 |
15:20$B!A(B 15:40 | G320 | Y$B;z4IH?1~4o$G@=B$$7$?%7%j%+%>%k$N%2%k2=@)8f5;=Q(B
($B;38}Bg1!(B) $B!{(B($B3X(B)$B3-=P(B $B0<(B $B!&(B ($B@5(B)$B:4Gl(B $BN4(B | Gelling time Specific surface area Pore volume
| 2-g | 792 |
15:40$B!A(B 16:00 | G321 | $B2sJ,<0$N2C05MO2r(B-$B8:05AuCV$K$*$1$k5$K"7A@.$N4QB,(B
($BC^GHBg@84D7O(B) $B!{(B($B3X(B)$BEgED(B $BH~Jf(B $B!&(B ($BG@8&5!9=?)Am8&(B) ($B@5(B)$B>.NS(B $B8y(B $B!&(B $B?"B<(B $BK.I'(B $B!&(B ($BC^GHBg@84D7O(B) ($B@5(B)$B:4F#(B $B@?8c(B $B!&(B ($B@5(B)$B;T@n(B $BAO:n(B | bubble formation pressurized dissolution
| 2-g | 701 |
(16:00$B!A(B16:40)$B!!(B($B:BD9(B $B:4Gl(B $BN4(B) |
16:00$B!A(B 16:20 | G322 | $B%O%K%+%`Fb$NJPN.M^@)$K4X$9$k?tCME*8!F$(B
($B6eBg1!9)(B) $B!{(B($B@5(B)$B>>7((B $BMN2p(B $B!&(B ($B6eBg9)(B) ($B3X(B)$B;3Cf(B $Bb+B@O:(B $B!&(B ($B3X(B)$BB-N)(B $B9/<#(B $B!&(B ($B6eBg1!9)(B) ($B@5(B)$BJw85(B $B2m | maldistribution honeycomb CFD
| 2-a | 427 |
16:20$B!A(B 16:40 | G323 | $BJ,;6N3;R4VN.BNNO3XE*Aj8_:nMQ$NEAC#2aDx$N?tCM2r@O(B
($B5~Bg9)(B) $B!{(B($B3X(B)$BC$L&(B $BNg(B $B!&(B ($B@5(B)$B;3K\(B $BNL0l(B | Dispersion Compressible fluid Hydrodynamic interaction
| 2-a | 397 |