$B |
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$B:G=*99?7F|;~!'(B2021-02-07 15:20:01
$B$3$NJ,N`$G$h$/;H$o$l(B $B$F$$$k%-!<%o!<%I(B | $B%-!<%o!<%I(B | $B | |
---|---|---|---|
Ultrafine Bubble | 3$B7o(B | ||
Fine Bubble | 2$B7o(B | ||
Dispersion | 2$B7o(B | ||
calcium alginate | 1$B7o(B |
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $BH/I=7A<0(B | |
---|---|---|---|
5 | $BC_5$< | fine bubble bubble size distribution bubble column | O |
6 | $B%&%k%H%i%U%!%$%s%P%V%k$N0BDj2=5!9=$K4X$9$k | ultrafine bubble stability gas content | O |
7 | $B%&%k%H%i%U%!%$%s%P%V%k$NF0E*5sF0$K4X$9$k | ultrafine bubble sheet lazer dynamic behavior | O |
8 | $B%&%k%H%i%U%!%$%s%P%V%k$,?"J*$N@.D9$KM?$($k1F6A$K4X$9$k | Ultrafine bubbles plant growth Semi-permeable membrane | O |
39 | $BJ,;6A0=hM}$N<+F02=$K$h$kHyN3;RN3;R7BJ,I[$N9b:F8=@-I>2AJ}K!(B | particle size dispersion measurement | O |
72 | DLS$B$=$N>lB,Dj$K$h$k%^%$%/%mGH>H | Microwave Emulsion De-emulsification | O |
85 | $BA!0]%U%#%k%?! | coalescence droplet numerical simulation | O |
151 | DEM-CFD$BK!$K$*$1$k(Bdensity scaling$BK!$NM-8z@-8!>Z(B | DEM-CFD method Density scaling technique gas-solid flow | O |
162 | $B | Stirred Tank Gas Dissolution Bubble Size | O |
181 | $BC:;@C&?e9ZAG(B-$B%j%]%=!<%`J#9gBN$rJq3g$5$;$?%2%kN3;R$ND4@=$HFs;@2=C:AG5[<}$X$N1~MQ(B | calcium alginate lipid vesicles catalyst reuse | O |
184 | [$BE8K>9V1i(B] $B%j%s;i~$H5$K"$N8z2L(B | liposomes gas-liquid flow PEGylated lipids | O |
195 | $B%(%"%U%#%k%?MQ%J%N%U%!%$%P$m:`$N=i4|N3;RJa=88zN($N8~>e$HN3;RIi2Y;~$ND9 | nano-fiber media collection efficiency pressure drop | O |
208 | [$BE8K>9V1i(B] $BN3;RK!$rMQ$$$?<+M3I=LLN.$l$H:.AjN.$N%7%_%e%l!<%7%g%s$N8=>u$HE8K>(B | MPS Free Surface Flow Multi-phase Flow | O |
317 | $B%0%i%U%!%$%H$X$N9bJ,;RE:2C:^5[Ce5sF0$,N3;R=89g>uBV5Z$SEE6KDq93$K$*$h$\$91F6A(B | Adsortion Dispersion Graphite | O |
401 | $BB?9&@-:`NA$rAH$_9~$s$@N.BN%G%P%$%9$K$*$1$kHyN3;RJ,N%5sF0$NI>2A(B | porous material particle separation microfluidic device | O |
513 | $BD62;GH;I7c$rIUM?$7$?%&%k%H%i%U%!%$%s%P%V%k?eN.$K$h$k%,%i%9JILLIUCeHyN3;R$N=|5n(B | Ultrafine Bubble Fine Bubble Ultrasonic cleaning | O |
595 | $B%$%s%/%8%'%C%H%N%:%k$+$i$N1UE)EG=P%7%_%e%l!<%7%g%s(B | inkjet nozzle droplet formation VOF | O |
655 | $B@\?(3Q$N%b%G%k$r9MN8$7$?1UE)$NJILL$X$N>WFM$K4X$9$k?tCM2r@OE*8!F$(B | Volume of fluid Droplet impact Contact angle | O |
710 | $B3IYBAeFbN.F0>l$K$*$1$k9bG4EYN.BNCf$G$N%]%j%9%A%l%sN3;R$N6E=85sF0(B | Aggregation Fine particles OpenFOAM | O |
800 | MR$BN.BN$N$;$sCGN.$l>lCf$K$*$1$kB?N3;R7OD>@\?tCM%7%_%e%l!<%7%g%s(B | Magnetorheological fluid Shear flow Apparent viscosity | O |
805 | $BN37BJ,I[$N$"$kHyN3;R$N6E=89gBNB.EY$K$*$h$\$9%$%s%Z%i!<$*$h$S%,%9YxYBA`:n4V$NHf3S(B | agglomeration size-distributed particles impeller stirring,gas stirring | O |
814 | PM2.5$B$N6E=89=B$$,= | PM Adhesion DEM | O |
831 | $B1U!&1U4VJ* | liquid/liquid mass transfer suspension pattern sedimentary liquid | O |
887 | $BN3;R4VLS4INO$N3J;R%\%k%D%^%s%7%_%e%l!<%7%g%s(B | Capillary force Lattice Boltzmann method wetting | O |