$BBh(B1$BF|(B | |||||
---|---|---|---|---|---|
$B9V1i(B $B;~9o(B | $B9V1i(B $BHV9f(B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $BJ,N`(B | $BHV9f(B $B | |
$B!cN.BN%W%m%;%9%7%s%]%8%&%`!d(B | |||||
(10:20$B!A(B11:00)$B!!(B($B:BD9(B $B<<;3(B $B>!I'(B) | |||||
E105 | $B5$BN05NOJQF0$rMxMQ$7$?C10lHy:Y5$K"H/@8K!(B | micro-bubble bubble generator acoustic | S-2 | 62 | |
E106 | $BG4CF@-N.BN$NC&K"$K$*$1$k5$K"7A>u$N9M;!(B | Viscoelastic removal bubble | S-2 | 580 | |
(11:00$B!A(B12:00)$B!!(B($B:BD9(B $BEZ20(B $B3hH~(B) | |||||
E107 | $BC10l5$K"$+$i$N%,%95[<}2aDx$K$*$1$kJ* | Gas absorption Two-color LIF PIV | S-2 | 601 | |
E108 | $B@E;_1UBNCf$r>e>:$9$k(B2$B5$K"$N9gBN$*$h$SH?H/(B | bubble bouncing coalescence | S-2 | 61 | |
E109 | $BG4@-N.BNCf$r>e>:$9$k5$K"!?1UE)1?F0$X$NFsAjN.BNG4EY$N1F6A(B | Bubble/drop rise motion Viscosity ratio Numerical analysis | S-2 | 667 | |
(13:00$B!A(B13:40)$B!!(B($B;J2q(B $BC]ED(B $B9((B) | |||||
E113 | [$BE8K>9V1i(B]$B%^%$%/%m%P%V%k8&5f$N8=>u$HE8K>(B | microbubble water treatment bubble column | S-2 | 118 | |
(13:40$B!A(B14:40)$B!!(B($B:BD9(B $Bc7F#(B $BN4G7(B) | |||||
E115 | $B%9%i%j! | Slurry Bubble Liquid mixing | S-2 | 270 | |
E116 | $B?eJ?6k7A%Q%$%W%i%$%s$rDL2a$9$k5$1U(B2$BAjN.$N5sF0(B | bubble laser-scanning two-phase flow | S-2 | 25 | |
E117 | $B6k7A4IFb$rN.$l$k5$1U(B2$BAj5$K"N.$NHsDj>oB.EYJQF02r@O(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) | |||||
E118 | $B5$K"<~JUN.$l$H05NOJ,I[$N?tCM2r@O(B | bubble wake numerical simulation pressure distribution | S-2 | 488 | |
E119 | $B6k7A5$K"Ec$K$*$1$kBg5,LON.F09=B$(B | Bubble Column Two-phase Flow LDA | S-2 | 801 | |
E120 | Plunging jet$B$K$h$jM65/$5$l$k5$1UFsAjN.F0$N9=B$(B | multi-phase flow F-TOP(Four-Tip Optical-fiber Probe) plunging jet | S-2 | 518 | |
(15:40$B!A(B16:40)$B!!(B($B:BD9(B $B;{:d(B $B9(0l(B) | |||||
E121 | $B5$K"Ec$GG]M\$7$?(BAgaricus blazei$B6];eBN$NBe | Bubble Column Agaricus blazei Submerged culture | S-2 | 416 | |
E122 | $B8GDj2==$>~%;%k%i!<%<$K$h$kITMO@-%;%k%m!<%9$N%(%"%j%U%HE|2=H?1~A`:n(B | Immobilized cellulase Cellulose saccharification Airlift bioreactor | S-2 | 100 | |
E123 | U$B%A%e!<%VH?1~4o$rMQ$$$?0{MQ?e%*%>%s=hM}$N%7%_%e%l!<%7%g%s(B | U-tube Bubble Column Ozonation Drinking water | S-2 | 397 | |
$BBh(B2$BF|(B | |||||
$B9V1i(B $B;~9o(B | $B9V1i(B $BHV9f(B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $BJ,N`(B | $BHV9f(B $B | |
$B!cN.BN%W%m%;%9%7%s%]%8%&%`!d(B | |||||
(9:00$B!A(B10:00)$B!!(B($B:BD9(B $B;3:j(B $B5H0l(B) | |||||
E201 | $BL8?a$-$O$J$e$2$k$N$+!!!=(B $BC+0lO:@b$N | Atomizer Bernoulli$B!G(Bs theorem Air flow pattern | S-2 | 269 | |
E202 | $BJ,3d!&:F9gN.7?%^%$%/%m%_%-%5!<$K$*$1$kN.F0FC@-(B | Micromixer Pressure drop correlation Residence time distribution | S-2 | 95 | |
E203 | $B%N%s%(%l%a%s%H%_%-%5!<$N:.9gFC@-(B($BBh(B2$BJs(B) | static mixer visualization mixing pattern | S-2 | 241 | |
(10:00$B!A(B11:00)$B!!(B($B:BD9(B $BK>7n(B $B2mJ8(B) | |||||
E204 | $B$i$;$s7?%^%$%/%m%A%c%s%M%k$K$*$1$kN3;R$H1UBN$NJ,N%(B | microchannnel separation simulation | S-2 | 114 | |
E205 | MRI$B$rMQ$$$?J#;(N.BN$N4IFbN.$l$K$*$1$kN.B.B,Dj(B | Magnetic resonance imaging complex fluid velocity measurement | S-2 | 954 | |
E206 | $BEE5$Dq93%H%b%0%i%U%#!< | 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) | |||||
E207 | $B%?!<%S%sMcLL>e$N05NOJ,I[$K$*$h$\$91UG4EY$N1F6A(B | mixing axial flow impeller pressure distribution | S-2 | 149 | |
E208 | $B1U1U7O3IYBAe$K$*$1$k1UE)J,;65sF0$K5Z$\$9J,;6AjG;EY$N1F6A(B | Liquid-Liquid Dispersion Steric Stabilizers Dispersed Phase Concentration | S-2 | 507 | |
E209 | $BMm$_9g$$D>:?>u9bJ,;R$N9=@.J}Dx<0(B | Polymer dynamics Entanglement Rheology | S-2 | 30 | |
(14:40$B!A(B15:20)$B!!(B($B;J2q(B $B>e%N;3(B $B<~(B) | |||||
E218 | [$BE8K>9V1i(B]$B$I$3$^$G9T$1$k!)!!5$1U:.AjN.2r@O(B | CFD Two-phase flow | S-2 | 988 | |
(15:20$B!A(B16:20)$B!!(B($B:BD9(B $B9b66(B $B9,;J(B) | |||||
E220 | $BHs%K%e!<%H%sG4@-1U$K$*$1$k1}I|F05$1U3IYBMc$NF0NOFC@-(B | Non-Newtonian fluid Aerated mixing Power consumption | S-2 | 885 | |
E221 | $B | unbaffled agitated vessel unsteadily rotating impeller gas-liquid mass transfer | S-2 | 877 | |
E222 | $B1}I|?6F03IYB$K$*$1$k:.9g5!9=$HIT0BDjB?MMBN(B | fluid mixing unstable manifolds mixing mechanism | S-2 | 117 | |
(16:20$B!A(B17:00)$B!!(B($B:BD9(B $B0f>e(B $B5AO/(B) | |||||
E223 | $B1}I|F0Mc | unbaffled agitated vessel unsteadily rotating impeller solid-liquid mass transfer | S-2 | 879 | |
E224 | $BHsDj>o3IYB$K$h$k8G1U:.9g(B | unsteady operation solid-liquid mixing dissolution-time | S-2 | 202 | |
$BBh(B3$BF|(B | |||||
$B9V1i(B $B;~9o(B | $B9V1i(B $BHV9f(B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $BJ,N`(B | $BHV9f(B $B | |
$B!cN.BN%W%m%;%9%7%s%]%8%&%`!d(B | |||||
(9:00$B!A(B10:00)$B!!(B($B:BD9(B $B5HED(B $B2mE5(B) | |||||
E301 | $B3IYBAe$K7Z$$B+$M$kA!0]>u8GBN$NJ,;6(B | fibriform particle dispersion light particle | S-2 | 188 | |
E302 | $B%I%i%U%H%A%e!<%VIU3IYBAe$K$*$1$k9bG;EY8GBNN3;R$NIbM7!&J,;6FC@-(B | mixing draft-tube dispersion state | S-2 | 509 | |
E303 | $BHsEy29>l$K$*$1$k(BMiscible Viscous Fingering$B$N | Viscous Fingering Hele-Shaw cell nonisothermal | S-2 | 281 | |
(10:00$B!A(B10:40)$B!!(B($B:BD9(B $B?N;V(B $BOBI'(B) | |||||
E304 | 3D-PTV$B$K$h$kYxYBAe$NN.$l>l2r@O(B | Mixing 3D PTV liquid flow velocity | S-2 | 55 | |
E305 | $B%*%/%?%8%C%H$N=[4D;~4VJ,I[$NB,Dj(B | Mixing New type impeller Circulation time | S-2 | 22 |