$B9V1i(B $B;~9o(B | $B9V1i(B $BHV9f(B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $BJ,N`(B $BHV9f(B | $B$BHV9f(B | |
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10:20$B!A(B 10:40 | E105 | $B5$BN05NOJQF0$rMxMQ$7$?C10lHy:Y5$K"H/@8K!(B ($B6eBg(B) $B!{(B($B@5(B)$B??ED(B $B=SG7(B$B!&(B$B>kED(B $BG@(B$B!&(B$BEOIt(B $B@5IW(B | micro-bubble bubble generator acoustic
| S-2 | 62 |
10:40$B!A(B 11:00 | E106 | $BG4CF@-N.BN$NC&K"$K$*$1$k5$K"7A>u$N9M;!(B ($BL>9)Bg1!J*$B!&(B($B3X(B)$BFbED(B $B?.8g(B$B!&(B($BL>9)Bg1~MQ2=3X2J(B) ($B3X(B)$B@PED(B $BOB?M(B$B!&(B($BL>9)Bg1!J* | Viscoelastic removal bubble
| S-2 | 580 |
(11:00$B!A(B12:00)$B!!(B($B:BD9(B $BEZ20(B $B3hH~(B) |
11:00$B!A(B 11:20 | E107 | $BC10l5$K"$+$i$N%,%95[<}2aDx$K$*$1$kJ* ($B$B!&(B($B@5(B)$B>>K\(B $BMxC#(B$B!&(B$B5HK~(B $B;VHA(B$B!&(B$BB<>e(B $B | Gas absorption Two-color LIF PIV
| S-2 | 601 |
11:20$B!A(B 11:40 | E108 | $B@E;_1UBNCf$r>e>:$9$k(B2$B5$K"$N9gBN$*$h$SH?H/(B ($B6eBg(B) $B!{(B($B@5(B)$B??ED(B $B=SG7(B$B!&(B$BEOIt(B $B@5IW(B | bubble bouncing coalescence
| S-2 | 61 |
11:40$B!A(B 12:00 | E109 | $BG4@-N.BNCf$r>e>:$9$k5$K"!?1UE)1?F0$X$NFsAjN.BNG4EY$N1F6A(B ($B<$B!&(B$B;38}(B $B?BLi(B$B!&(B($B@5(B)$B5HED(B $BK-(B$B!&(B(Florida State U.) Sussman M. | Bubble/drop rise motion Viscosity ratio Numerical analysis
| S-2 | 667 |
|
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13:00$B!A(B 13:40 | E113 | [$BE8K>9V1i(B]$B%^%$%/%m%P%V%k8&5f$N8=>u$HE8K>(B ($B7DXfBgM}9)(B) $B!{(B($B@5(B)$BDS?"(B $B=( | microbubble water treatment bubble column
| S-2 | 118 |
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13:40$B!A(B 14:00 | E115 | $B%9%i%j! ($BIY;3Bg9)(B) $B!{(B($B@5(B)$B;3yu(B $BNLJ?(B$B!&(B($B@5(B)$B9u2,(B $BIp=S(B$B!&(B($B@5(B)$BN-(B $B5.7D(B$B!&(B$B>.?9(B $B9-Je(B$B!&(B$B?yLn(B $BD>?M(B | Slurry Bubble Liquid mixing
| S-2 | 270 |
14:00$B!A(B 14:20 | E116 | $B?eJ?6k7A%Q%$%W%i%$%s$rDL2a$9$k5$1U(B2$BAjN.$N5sF0(B ($B7DXfBgM}9)(B) $B!{(B($B3X(B)$B:45W4V(B $BBn(B$B!&(B($B@5(B)$B;{:d(B $B9(0l(B | bubble laser-scanning two-phase flow
| S-2 | 25 |
14:20$B!A(B 14:40 | E117 | $B6k7A4IFb$rN.$l$k5$1U(B2$BAj5$K"N.$NHsDj>oB.EYJQF02r@O(B ($BL>9)Bg9)(B) $B!{(B($B3X(B)$B0p3@(B $BCN9((B$B!&(B($BBgF19)Bg9)(B) ($B@5(B)$B>>1:(B $B>OM5(B$B!&(B($BL>9)Bg9)(B) ($B@5(B)$BB?ED(B $BK-(B$B!&(B($B@5(B)$B2CF#(B $BDw?M(B$B!&(B($B@5(B)$B4dED(B $B=$0l(B$B!&(B($B@5(B)$BD9DE(B $BM:0lO:(B | Numerical simulation Bubble flow Velocity fluctuation
| S-2 | 152 |
(14:40$B!A(B15:40)$B!!(B($B:BD9(B $BB@ED(B $B8w9@(B) |
14:40$B!A(B 15:00 | E118 | $B5$K"<~JUN.$l$H05NOJ,I[$N?tCM2r@O(B ($BF1;Vk(B $B=(IW(B$B!&(B($B8=Bh0l;06&(B) $B:4!9LZ(B $BFX;K(B$B!&(B($BF1;V$B!&(B($B@5(B)$BEZ20(B $B3hH~(B | bubble wake numerical simulation pressure distribution
| S-2 | 488 |
15:00$B!A(B 15:20 | E119 | $B6k7A5$K"Ec$K$*$1$kBg5,LON.F09=B$(B ($B@EBg1!(B) $B!{(B($B3X(B)$B1'ET5\(B $B@iGn(B$B!&(B($B3X(B)$B1:Ln(B $BHK9,(B$B!&(B($B;0I)2=3X%(%s%8%K%"%j%s%0(B) $BEDCf(B $B?-9((B$B!&(B($B@EBg1!(B) ($B@5(B)$Bc7F#(B $BN4G7(B | Bubble Column Two-phase Flow LDA
| S-2 | 801 |
15:20$B!A(B 15:40 | E120 | Plunging jet$B$K$h$jM65/$5$l$k5$1UFsAjN.F0$N9=B$(B ($B@EBg1!(B) $B!{(B($B3X(B)$B>>2<(B $B>05-(B$B!&(B($B3X(B)$B:g86(B $BOBLi(B$B!&(B($B@EBg9)(B) ($B@5(B)$Bc7F#(B $BN4G7(B | multi-phase flow F-TOP(Four-Tip Optical-fiber Probe) plunging jet
| S-2 | 518 |
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15:40$B!A(B 16:00 | E121 | $B5$K"Ec$GG]M\$7$?(BAgaricus blazei$B6];eBN$NBe ($BF`NI9b@l(B) ($B@5(B)$B2O1[(B $B44CK(B$B!&(B$B!{9b@%(B $BFA;R(B$B!&(B$B4]ED(B $B42;R(B$B!&(B($B4X@>2=3X(B) ($B@5(B)$BLnED(B $B=(IW(B | Bubble Column Agaricus blazei Submerged culture
| S-2 | 416 |
16:00$B!A(B 16:20 | E122 | $B8GDj2==$>~%;%k%i!<%<$K$h$kITMO@-%;%k%m!<%9$N%(%"%j%U%HE|2=H?1~A`:n(B ($B;38}Bg1!0e(B) $B!{(B($B@5(B)$B5HK\(B $B@?(B$B!&(B($B;38}Bg9)(B) $BF#86(B $B2CID(B$B!&(B($B;38}Bg1!M}9)(B) ($B@5(B)$BJ!1J(B $B8x$B!&(B($B;38}Bg(B) ($B@5(B)$BCfHx(B $B>!Ui(B | Immobilized cellulase Cellulose saccharification Airlift bioreactor
| S-2 | 100 |
16:20$B!A(B 16:40 | E123 | U$B%A%e!<%VH?1~4o$rMQ$$$?0{MQ?e%*%>%s=hM}$N%7%_%e%l!<%7%g%s(B ($B4X@>Bg9)(B) $B!{(B($B@5(B)$B<<;3(B $B>!I'(B$B!&(B$BCf@n(B $B@5$B!&(B($B3X(B)$B0KEl(B $BOBLi(B$B!&(B$B;3ED(B $BNK(B$B!&(B(JFE$B%(%s%8(B) $BDT(B $BLT;V(B | U-tube Bubble Column Ozonation Drinking water
| S-2 | 397 |
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9:00$B!A(B 9:20 | E201 | $BL8?a$-$O$J$e$2$k$N$+!!!=(B $BC+0lO:@b$NZ(B $B!=(B ($B?.=#BgA!0](B) $B!{(B($B3X(B)$B;34_(B $BATNr(B$B!&(B($B@5(B)$BI~It(B $BGn;L(B | Atomizer Bernoulli$B!G(Bs theorem Air flow pattern
| S-2 | 269 |
9:20$B!A(B 9:40 | E202 | $BJ,3d!&:F9gN.7?%^%$%/%m%_%-%5!<$K$*$1$kN.F0FC@-(B ($B%"%9%F%i%9@=Lt(B) $B!{(B($B@5(B)$BBg@n(B $BOBCK(B$B!&(B($B:eBg1!4p9)(B) ($B@5(B)$B0f>e(B $B5AO/(B$B!&(B($B@5(B)$BJ?ED(B $BM:;V(B | Micromixer Pressure drop correlation Residence time distribution
| S-2 | 95 |
9:40$B!A(B 10:00 | E203 | $B%N%s%(%l%a%s%H%_%-%5!<$N:.9gFC@-(B($BBh(B2$BJs(B) ($B7DXfBg1!(B) $B!{(B($B3X(B)$B?y@n(B $BM42p(B$B!&(B($B7DXfBgM}9)(B) ($B@5(B)$B?"ED(B $BMx5W(B | static mixer visualization mixing pattern
| S-2 | 241 |
(10:00$B!A(B11:00)$B!!(B($B:BD9(B $BK>7n(B $B2mJ8(B) |
10:00$B!A(B 10:20 | E204 | $B$i$;$s7?%^%$%/%m%A%c%s%M%k$K$*$1$kN3;R$H1UBN$NJ,N%(B ($BJ!2,Bg9)(B) $B!{8eF#(B $BM}?M(B$B!&(B($B@5(B)$B;3:j(B $B5H0l(B$B!&(B$B2>20yu(B $B4&(B$B!&(B($B@5(B)$B=t2,(B $B@.<#(B | microchannnel separation simulation
| S-2 | 114 |
10:20$B!A(B 10:40 | E205 | MRI$B$rMQ$$$?J#;(N.BN$N4IFbN.$l$K$*$1$kN.B.B,Dj(B ($B:eBg9)(B) $B!{(B($B6&(B)$BJ]ED(B $BOBB'(B$B!&(B$BO; | Magnetic resonance imaging complex fluid velocity measurement
| S-2 | 954 |
10:40$B!A(B 11:00 | E206 | $BEE5$Dq93%H%b%0%i%U%#!<uBV$N7WB,(B ($B2#9qBg9)(B) $B!{(B($B3X(B)$BED2O(B $BFX(B$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 $B<~(B | electrical resistance tomography mixing gas-liquid system
| S-2 | 505 |
(11:00$B!A(B12:00)$B!!(B($B:BD9(B $B2CF#(B $BDw?M(B) |
11:00$B!A(B 11:20 | E207 | $B%?!<%S%sMcLL>e$N05NOJ,I[$K$*$h$\$91UG4EY$N1F6A(B ($BElM}Bg9)(B) ($B@5(B)$BK>7n(B $B2mJ8(B$B!&(B$B!{(B($B3X(B)$B0BF#(B $B?r9T(B$B!&(B($B3X(B)$B9b66(B $BM':H(B$B!&(B($B3X(B)$B@5LZ(B $B9n;^(B | mixing axial flow impeller pressure distribution
| S-2 | 149 |
11:20$B!A(B 11:40 | E208 | $B1U1U7O3IYBAe$K$*$1$k1UE)J,;65sF0$K5Z$\$9J,;6AjG;EY$N1F6A(B ($B2#9qBg1!9)(B) $B!{(B($B3X(B)$BF#Eh(B $Bh=7C;R(B$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 $B<~(B | Liquid-Liquid Dispersion Steric Stabilizers Dispersed Phase Concentration
| S-2 | 507 |
11:40$B!A(B 12:00 | E209 | $BMm$_9g$$D>:?>u9bJ,;R$N9=@.J}Dx<0(B ($B:k6LBg(B) $B!{(B($B@5(B)$B8E4W(B $BFsO:(B$B!&(B$BLZB<(B $B7=(B$B!&(B($B@5(B)$BK\4V(B $B=S;J(B | Polymer dynamics Entanglement Rheology
| S-2 | 30 |
|
(14:40$B!A(B15:20)$B!!(B($B;J2q(B $B>e%N;3(B $B<~(B) |
14:40$B!A(B 15:20 | E218 | [$BE8K>9V1i(B]$B$I$3$^$G9T$1$k!)!!5$1U:.AjN.2r@O(B ($B%"!<%k%U%m!<(B) $B!{(B($B@5(B)$BC]ED(B $B9((B | CFD Two-phase flow
| S-2 | 988 |
(15:20$B!A(B16:20)$B!!(B($B:BD9(B $B9b66(B $B9,;J(B) |
15:20$B!A(B 15:40 | E220 | $BHs%K%e!<%H%sG4@-1U$K$*$1$k1}I|F05$1U3IYBMc$NF0NOFC@-(B ($B?73cBg<+A38&(B) $B!{(B($B3X(B)$B:4F#(B $BOB2B(B$B!&(B($B3X(B)$B1J0f(B $B9/G7(B$B!&(B($B?73cBg9)(B) ($B@5(B)$B5HED(B $B2mE5(B$B!&(B($B@5(B)$B;3:](B $BOBL@(B$B!&(B($B@5(B)$BBg@n(B $B51(B$B!&(B($BEg:j@=:n=j(B) ($B@5(B)$B | Non-Newtonian fluid Aerated mixing Power consumption
| S-2 | 885 |
15:40$B!A(B 16:00 | E221 | $B ($B?73cBg<+A38&(B) $B!{(B($B3X(B)$BL+85(B $B@/4x(B$B!&(B($B?73cBg9)(B) ($B@5(B)$B5HED(B $B2mE5(B$B!&(B($B@5(B)$B;3:](B $BOBL@(B$B!&(B($B@5(B)$BBg@n(B $B51(B$B!&(B($BEg:j@=:n=j(B) ($B@5(B)$B | unbaffled agitated vessel unsteadily rotating impeller gas-liquid mass transfer
| S-2 | 877 |
16:00$B!A(B 16:20 | E222 | $B1}I|?6F03IYB$K$*$1$k:.9g5!9=$HIT0BDjB?MMBN(B ($B:eBg4p9)(B) $B!{(B($B3X(B)$B:nK\(B $BOB=((B$B!&(B($B@5(B)$BJ?ED(B $BM:;V(B$B!&(B($B@5(B)$B0f>e(B $B5AO/(B | fluid mixing unstable manifolds mixing mechanism
| S-2 | 117 |
(16:20$B!A(B17:00)$B!!(B($B:BD9(B $B0f>e(B $B5AO/(B) |
16:20$B!A(B 16:40 | E223 | $B1}I|F0Mc ($B<+A32J3X8&5f2J(B) $B!{(B($B3X(B)$BLZB<(B $BL@90(B$B!&(B($B@5(B)$B$B!&(B($B?73cBg9)(B) ($B@5(B)$B5HED(B $B2mE5(B$B!&(B($B@5(B)$B;3:](B $BOBL@(B$B!&(B($B@5(B)$BBg@n(B $B51(B | unbaffled agitated vessel unsteadily rotating impeller solid-liquid mass transfer
| S-2 | 879 |
16:40$B!A(B 17:00 | E224 | $BHsDj>o3IYB$K$h$k8G1U:.9g(B ($B;37ABg(B) $B!{(B($B3X(B)$BEOn4(B $BMG2p(B$B!&(B($B@5(B)$B9b66(B $B9,;J(B | unsteady operation solid-liquid mixing dissolution-time
| S-2 | 202 |
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9:00$B!A(B 9:20 | E301 | $B3IYBAe$K7Z$$B+$M$kA!0]>u8GBN$NJ,;6(B ($B?9>>9)6H(B) $B!{(B($B3X(B)$B>S(B $B9(3$(B$B!&(B($B;37ABg9)(B) ($B@5(B)$B9b66(B $B9,;J(B | fibriform particle dispersion light particle
| S-2 | 188 |
9:20$B!A(B 9:40 | E302 | $B%I%i%U%H%A%e!<%VIU3IYBAe$K$*$1$k9bG;EY8GBNN3;R$NIbM7!&J,;6FC@-(B ($B2#9qBg9)(B) $B!{(B($B@5(B)$B;03Q(B $BN4B@(B$B!&(B$BDMED(B $B@?(B$B!&(B$BK-ED(B $BCR8<(B$B!&(B($B@5(B)$B?N;V(B $BOBI'(B$B!&(B($B@5(B)$B>e%N;3(B $B<~(B | mixing draft-tube dispersion state
| S-2 | 509 |
9:40$B!A(B 10:00 | E303 | $BHsEy29>l$K$*$1$k(BMiscible Viscous Fingering$B$N ($BL>9)Bg(B) $B!{(B($B3X(B)$BF#ED(B $B7{?M(B$B!&(B($B@5(B)$BD9DE(B $BM:0lO:(B$B!&(B($B@5(B)$B2CF#(B $BDw?M(B$B!&(B($B@5(B)$BB?ED(B $BK-(B | Viscous Fingering Hele-Shaw cell nonisothermal
| S-2 | 281 |
(10:00$B!A(B10:40)$B!!(B($B:BD9(B $B?N;V(B $BOBI'(B) |
10:00$B!A(B 10:20 | E304 | 3D-PTV$B$K$h$kYxYBAe$NN.$l>l2r@O(B ($B;37ABg9)(B) $B!{(B($B3X(B)$BCi@/(B $BL@I'(B$B!&(B($B@5(B)$B9b66(B $B9,;J(B | Mixing 3D PTV liquid flow velocity
| S-2 | 55 |
10:20$B!A(B 10:40 | E305 | $B%*%/%?%8%C%H$N=[4D;~4VJ,I[$NB,Dj(B ($BL>9)Bg(B) ($B@5(B)$B2CF#(B $BDw?M(B$B!&(B$B!{(B($B3X(B)$B86ED(B $B3H(B$B!&(B($B@5(B)$BB?ED(B $BK-(B$B!&(B($B@5(B)$BD9DE(B $BM:0lO:(B$B!&(B($BLnB<%^%$%/%m%5%$%(%s%9(B) ($B@5(B)$BCfC+(B $BE/<#(B | Mixing New type impeller Circulation time
| S-2 | 22 |