$B |
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$B:G=*99?7F|;~!'(B2022-01-31 16:50:01
$B$3$NJ,N`$G$h$/;H$o$l(B $B$F$$$k%-!<%o!<%I(B | $B%-!<%o!<%I(B | $B | |
---|---|---|---|
ultrafine bubble | 2$B7o(B | ||
DEM-simulation | 1$B7o(B |
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $BH/I=7A<0(B | |
---|---|---|---|
36 | [$BE8K>9V1i(B] $B$J$ | Fluidized Bed Catalyst Bed Emulsion Phase | O |
38 | [$BE8K>9V1i(B] $B5$K"%/%i%9%?!<$NN.BNNO3X(B | Tiny Bubbles Surfactant Multiscale Structures | O |
56 | Microrheology of gels with acoustic microbubbles | Rheology Gelatin gel Acoustic microbubble | O |
66 | $BD6=c?eCf$N6u5$%&%k%H%i%U%!%$%s%P%V%k$NG;=L$H4u | Ultrafine Bubble Concentration Dilution | O |
136 | $B%^%$%/%m%P%V%k$K$h$kIb>eJ,N%$rMxMQ$7$?%7%j%3%s%J%NN3;R2s<}%W%m%;%9$N3+H/(B | microbabbles levitation separation silicon nanoparticles | O |
173 | $BEE>l2<$K$*$1$k | Volume of fluid breakup electric field | O |
203 | $B%k!<%W4I7?N.DLAuCVCf$K$*$1$k(BHFC134a$B%O%$%I%l!<%H%9%i%j!<$NN.F05sF0(B | hydrate slurry flow characteristic viscosity | O |
270 | A data-driven parameterized surrogate model for the identification of DEM simulation parameters | Discrete element method Data-driven surrogate model Parameter identification | O |
274 | $B05NO?6F0>l$K$*$1$kFC0[5$K"7A>u$N7A@.$K4X$9$kG4CF@-$N1F6A$N8!F$(B | pressure oscillation Viscoelasticity fluid 2D high-speed polarization imaging | O |
286 | $B1U1U%9%i%0N.7A@.$K$*$$$FA`:n>r7o$,%9%i%0D9$5$HFbIt=[4DN.$K5Z$\$91F6A$N2r@O(B | slug flow liquid-liquid PIV | O |
401 | $BD62;GH$K$h$k%&%k%H%i%U%!%$%s%P%V%k$NG;EY@)8f(B | Ultrafine bubbles Ultrasound Frequency | O |
411 | $B?eJ??6F0$9$k%N%:%k$+$i$NHy:Y5$K"@8@.$K1UG4EY$,5Z$\$91F6A(B | microbubble nozzle oscillation | O |
512 | FIB-SEM$B$K$h$k2hA|2r@O$rO"7H$7$?@:L)$m2a%7%_%e%l!<%7%g%s(B | FIB-SEM Direct numerical simulation Microfiltration | O |
531 | $B%$%s%/%8%'%C%H0u:~$K$*$1$k1UE)EG=P$*$h$SCeCF%7%_%e%l!<%7%g%s(B | inkjet VOF droplets | O |
553 | $B%&%k%H%i%U%!%$%s%P%V%k$N0BDj2=5!9=$K4X$9$k | ultrafine bubble stability characterization | O |
563 | $B5e>uO"DL9&$rAH$_9~$s$@Hy>.N.BN%G%P%$%9$rMQ$$$kHyN3;R$NJ,N%(B | porous substrate particle separation microfluidic device | O |
654 | $BJ,@OE*1s?4J,N%$rMQ$$$?%7%j%+%J%NN3;R$ND@9_5sF0B,Dj$*$h$S0\N.3H;6%b%G%k$K$h$k?tCM2r@O(B | SiO2 nanoparticle Sedimentation advection-diffusion model | O |
682 | $BKlJ(F-$K$h$k5$K"@.D92aDx$N?tCM2r@O(B | Film boiling Bubble growth Numerical analysis | O |
684 | $BN3;RJ,;61UCf$K$*$1$k%W%m!<%V$N1?F0@-$KBP$9$kN3;R7B8z2L(B | Non-colloidal particles Hydrodynamic interaction Peclet number | O |
714 | $B%,%i%94pHD$K$*$1$k1UE)$N>xH/5sF0$K$*$h$\$9I=LLD4@0:^$N1F6A(B | Evaporation Contact angle droplet shape changes | O |
734 | $B3IYBAeFb$N$;$sCGB.EYJ,I[$,HyN3;R6E=8$KM?$($k1F6A(B | Agglomeration Shear distribution Mixing tank | O |
843 | $B1UBN%J%H%j%&%`$X$N<><0%S!<%:%_%k$NE,MQ8!F$$HHy>.%S!<%:5sF0$NGD0.(B | bead mill liquid sodium DEM-simulation | O |
869 | $B3h@-;@AG | colloidal catalysts enzyme reactions enzyme immobilization | O |