$BBh(B1$BF|(B | |||||
---|---|---|---|---|---|
$B9V1i(B $B;~9o(B | $B9V1i(B $BHV9f(B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $BJ,N`(B | $BHV9f(B $B | |
$BN3;R!&N.BN%W%m%;%9(B | |||||
(9:00$B!A(B10:00)$B!!(B($B:BD9(B $B>e;3(B $B0T0l(B) | |||||
G101 | V$B;z4IFb$N%9%i%C%.%s%08=>]$K4X$9$k8&5f(B | Slugging V-shaped elbow Flow regime | 2-e | 41 | |
G102 | $B= | Gas-Liquid Film Flows CFD Packing Columns | 2-e | 513 | |
G103 | Interaction between Two Moving Jets in Immiscible Liquid-Liquid Systems: An Experimental Study | Emulsion Explosive Multiphase flow Micro fluidic | 2-e | 573 | |
(10:00$B!A(B11:00)$B!!(B($B:BD9(B $B0BED(B $B7<;J(B) | |||||
G104 | $BL5 | Bubble and drop Dynamic motion Dimensionless number | 2-e | 305 | |
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 | partial gravity dust exposure regolith | 2-e | 378 | |
G106 | $B%J%N%P%V%k$K$*$1$kD62;GH>H | Nano-Bubbles Ultrasound Annihilation | 2-e | 108 | |
(11:00$B!A(B12:00)$B!!(B($B:BD9(B $BB@ED(B $B8w9@(B) | |||||
G107 | $B8w@~DI@W%7%_%e%l!<%7%g%s$K4p$E$/8w%U%!%$%P!<%W%m!<%V$rMQ$$$?5$K"N.7WB,(B | Optical fiber probe Bubble measurement Ray tracing | 2-e | 69 | |
G108 | MH$BHoJ$5$K"$N>e>:B.EY$J$i$S$K93NO78?t$K4X$9$k0l9M;!(B | Hydrate Bubble Drag coefficient | 2-e | 128 | |
G109 | $B05NO?6F0>l$K$*$1$kC10l5$K"6aK5N.F0>l$N(B2$B | pressure-oscillating birefringence viscoelastic fluid | 2-a | 509 | |
(13:00$B!A(B14:00)$B!!(B($B:BD9(B $B4dED(B $B=$0l(B) | |||||
G113 | $B5$1U:.AjN.%7%_%e%l!<%?$NFC@-$*$h$S4JJX$J7W;;%"%k%4%j%:%`(B | gas-liquid multiphase flow simulator pressure equation | 2-d | 2 | |
G114 | $B5$1U==;zN.<0B?9&HDEc$N1UAjJ* | Mass transfer coefficient Sieve plate column Bubble interactions | 2-d | 64 | |
G115 | $B%^%$%/%m%P%V%k$K$h$k(BO/W$B%(%^%k%7%g%sJ,N%$K5Z$\$93&LL3h@-:^$N1F6A(B | emulsion surfactant microbubbles | 2-d | 106 | |
(14:00$B!A(B15:00)$B!!(B($B:BD9(B $B;3K\(B $BNL0l(B) | |||||
G116 | $B=[4D7?5$K"Ec$K$*$1$k5$1U%U%m!<%Q%?!<%s$N2r@O$H%*%>%s%,%9MO2rFC@-(B | bubble column ozonation flow pattern | 2-d | 794 | |
G117 | $B%^%$%/%mN.O)Fb$N5$1UCl0\F0FC@-(B | Gas/Liquid Interface Micro-Channel Liposome | 2-a | 251 | |
G118 | $BBg5,LO(B3$BZ(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) | |||||
G119 | $BCF@-%V%l!<%I$rMQ$$$?J4BN:.9g$N?tCM%7%_%e%l!<%7%g%s(B | Granular analysis Elastic body analysis Powder mixing | 2-f | 435 | |
G120 | $BN3;R72$NN3EYJP@O$K5Z$\$9N3;R7A>u$*$h$SN3;R7BJ,I[$N1F6A(B | DEM simulation segregation index percolation index | 2-f | 203 | |
G121 | DEM-LES$B%O%$%V%j%C%I%7%_%e%l!<%7%g%s$K$h$kJ4BNEIAuFC@-$N2r@O(B | DEM powder coating simulation | 2-f | 256 | |
(16:00$B!A(B17:20)$B!!(B($B:BD9(B $B | |||||
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 | Discrete element method Particle-based rigid body model Drum typed agitation mill | 2-f | 394 | |
G123 | $BN3;RGK2u5sF0$N%7%_%e%l!<%7%g%s(B | DEM breakage grinding | 2-f | 518 | |
G124 | $B?6F04pHD>e$NHyN3;R5sF0$N2r@O(B | fine particle vibration adhesion force | 2-f | 134 | |
G125 | Adhesion Characteristics of Charged Fine Particles | charged particle electric field adhesion force | 2-f | 191 | |
$BBh(B2$BF|(B | |||||
$B9V1i(B $B;~9o(B | $B9V1i(B $BHV9f(B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $BJ,N`(B | $BHV9f(B $B | |
$B9q:]%7%s%]%8%&%`(B $B!cN3;R!&N.BN%W%m%;%98&5f$K$*$1$k3W?7E*%9%F%C%W!d(B | |||||
(9:00$B!A(B10:00)$B!!(B($B:BD9(B $BB@ED(B $B8w9@(B) | |||||
G201 | [$B>7BT9V1i(B] Simulation of Processes containing Bubble, Drops and Particles | Computational Fluid Dynamics Dispersed Flow Simulation | K-1 | 26 | |
G202 | [$B>7BT9V1i(B] Hydrodynamic Interactions of Self-propelled Swimmers | active particles diffusion hydrodynamic | K-1 | 27 | |
G203 | [$B>7BT9V1i(B] Formation of a laminar compound jet and its breakup into compound droplets | compound jet compound drop hollow drop | K-1 | 28 | |
(10:00$B!A(B10:40)$B!!(B($B:BD9(B $B5H@n(B $B;KO:(B) | |||||
G204 | [$B>7BT9V1i(B] Transport of Passive and Non-Passive Particles in Chaotic Flow | transport passive chaotic flow | K-1 | 93 | |
G205 | [$B0MMj9V1i(B] Solid Particles Distribution on Dished Base of a Stirred Tank Using Conventional Impellers and Novel SATAKE Impellers | Mixing Solids Suspension Dished Based Tank | K-1 | 95 | |
(10:40$B!A(B11:40)$B!!(B($B:BD9(B $B8eF#(B $BK.>4(B) | |||||
G206 | [$B>7BT9V1i(B] Nanoparticle Synthesis and Their Functionalization in the Colloidal Method | Nanomaterial processing liquid-phase synthesis Spray route | K-1 | 85 | |
G207 | [$B0MMj9V1i(B] Numerical and experimental study of effect of dry powder inhaler design on the aerosolisation of the carrier-based formulation | dry powder inhalers device design computational fluid dynamics | K-1 | 215 | |
G208 | [$B0MMj9V1i(B] Development of catalytic coal gasification process to produce FT-process suitable synthesis gas | Coal gasification synthesis gas catalyst | K-1 | 330 | |
(11:40$B!A(B12:20)$B!!(B($B;J2q(B $B>e%N;3(B $B<~(B) | |||||
G209 | [$B%"%8%"9q:]>^(B]Numerical Simulation of Multiphase Stirred Reactors/Crystallizers and Industrial Applications | stirred reactor crystallizer numerical simulation | K-1 | 341 | |
$BBh(B3$BF|(B | |||||
$B9V1i(B $B;~9o(B | $B9V1i(B $BHV9f(B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $BJ,N`(B | $BHV9f(B $B | |
$BN3;R!&N.BN%W%m%;%9(B | |||||
(9:00$B!A(B10:20)$B!!(B($B:BD9(B $B;3K\(B $BE0Li(B) | |||||
G301 | $B%0%i%$%G%#%s%0%"!<%/J|EE$rF3F~$7$?%5%$%/%m%s$K$h$kN3;R$N=hM}(B | cyclone gliding arc discharge particle treatment | 2-f | 499 | |
G302 | $B:.9gN3;R= | electroosmotic flow rate particle packed bed Debye length | 2-f | 226 | |
G303 | $B<+8JAH?%2=$rMxMQ$7$?J.L8G.J,2rK!$K$h$kGr6bC4;}%+!<%\%s%J%N9=B$BN:`NA$N9g@.(B | nanoparticle spray pyrolysis Proton exchange membrane fuel cell | 2-f | 274 | |
G304 | $B%(%"%m%>%k%W%m%;%9$K$h$k%3%"%7%'%k%J%NN3;R$N9g@.(B | core shell nanoparticle aerosol process laser ablation | 2-f | 527 | |
(10:20$B!A(B11:40)$B!!(B($B:BD9(B $B9b@%(B $B6Q(B) | |||||
G305 | $B4%<0%5%$%/%m%s$N6I=jE*N.F0@)8f$,N3;RJ,N%@-G=$K5Z$\$91F6A(B | Particle setaration Dry-cyclone separation efficiency | 2-f | 283 | |
G306 | $B=P8}4I>eIt$G$NN.F0@)8f$,4%<0%5%$%/%m%sJ,5i@-G=$KM?$($k1F6A(B | Particle Separation Dry-cyclone Separation efficiency | 2-f | 496 | |
G307 | $BEE5$1KF0$rMQ$$$?O"B37??edA$NJ,5i@-G=I>2A(B | Classification Water sieve Electrophoresis | 2-f | 501 | |
G308 | $B%^%$%/%mGH2CG.$K$h$k6bB0>K;@1v:.9g?eMO1U$NC&>KH?1~(B | Metallic oxide Microwave Denitration | 2-f | 103 | |
(11:40$B!A(B12:00)$B!!(B($B;J2q(B $B8eF#(B $BK.>4(B) | |||||
G309 | [$B8&5f>)Ne>^(B]AFM$B$K$h$kN3;RJ*@-I>2A$H$=$l$rMxMQ$7$?<><0J,5i%W%m%;%9$N3+H/(B | The SCEJ Young Investigator Researcher Award | 2-f | 804 | |
(13:00$B!A(B14:00)$B!!(B($B:BD9(B $BLnED(B $BNh<#(B) | |||||
G313 | $BN.F0AXFb$K$*$1$kN3;R4%Ag2aDx$N(BDEM-CFD$B%b%G%k3+H/(B | DEM-CFD coupling simulation fluidized bed heat and mass transfer | 2-c | 756 | |
G314 | $B5$K"N.F0AXCf$KB8:_$9$kAFBgJ*BN$N5sF0M=B,%b%G%k3+H/(B | Fluidized bed DEM-CFD coupling simulation | 2-c | 65 | |
G315 | $B%i%$%6!<$NEy2A2sO)%b%G%k2=(B | Fluidized bed Equivalent circuit model Flow behavior | 2-c | 782 | |
(14:00$B!A(B15:00)$B!!(B($B:BD9(B $BDT(B $BBsLi(B) | |||||
G316 | $BN.F0AX2=3X>xCeK!$K$h$jD4@=$5$l$?C:AGA!0]HoJ$N3;R$NN.F02=5sF0(B | carbon fiber-covered particles fluidization behavior cohesive particles | 2-c | 399 | |
G317 | $BB?< | ICFG biomass circulatinh | 2-c | 416 | |
G318 | Spout-Fluid Bed$B$NN.F0FC@-(B | spout-fluid bed maximum spoutable bed depth PIV | 2-c | 691 | |
(15:00$B!A(B16:00)$B!!(B($B:BD9(B $BF|=P4V(B $B$k$j(B) | |||||
G319 | $B5!G=@-G^BNN.F0AX$K$h$k9b4^?e@-%2%k>uJ* | dehydration of hydrogel functional porous media fluidized bed | 2-c | 337 | |
G320 | Y$B;z4IH?1~4o$G@=B$$7$?%7%j%+%>%k$N%2%k2=@)8f5;=Q(B | Gelling time Specific surface area Pore volume | 2-g | 792 | |
G321 | $B2sJ,<0$N2C05MO2r(B-$B8:05AuCV$K$*$1$k5$K"7A@.$N4QB,(B | bubble formation pressurized dissolution | 2-g | 701 | |
(16:00$B!A(B16:40)$B!!(B($B:BD9(B $B:4Gl(B $BN4(B) | |||||
G322 | $B%O%K%+%`Fb$NJPN.M^@)$K4X$9$k?tCME*8!F$(B | maldistribution honeycomb CFD | 2-a | 427 | |
G323 | $BJ,;6N3;R4VN.BNNO3XE*Aj8_:nMQ$NEAC#2aDx$N?tCM2r@O(B | Dispersion Compressible fluid Hydrodynamic interaction | 2-a | 397 |