$BC+8}(B $B5.;V!J5~ETBg3X!K!&;03Q(B $BN4B@!J2#IM9qN)Bg3X!K!&>1;J(B $B1RB@!JElKLBg3X!K!&A}ED(B $BM&?M!JBg:e;TN)Bg3X!K!&3-=P!!0 |
$B:G=*99?7F|;~!'(B2021-02-07 15:20:01
$B$3$NJ,N`$G$h$/;H$o$l(B $B$F$$$k%-!<%o!<%I(B | $B%-!<%o!<%I(B | $B | |
---|---|---|---|
numerical simulation | 5$B7o(B | ||
Surfactant | 2$B7o(B | ||
Heat Transfer | 2$B7o(B | ||
Stefan-Maxwell Equation | 1$B7o(B |
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $BH/I=7A<0(B | |
---|---|---|---|
42 | $B0lLL2CG.?eJ?6k7AN.O)$K$*$1$kJ#9gBPN.G.EAC#$K5Z$\$9N.O)@_CV>r7o$N1F6A(B | mixed convection heat transfer numerical simulation | O |
45 | $B8G1U3IYBAeFb$NJILLG.EAC#$K5Z$\$9IbM7@-N3;R:.F~$N1F6A(B | Solid-Liquid Mixing Floating Particle Heat Transfer | O |
49 | $B?75,L52A!A6I=jJ(F-$*$h$S1U1U3&LL$NI=LL2~ | Microwave dimensionless number boiling | O |
254 | $B$R$b>u%_%;%k?eMO1U7O$N%a%=%9%1!<%k%7%_%e%l!<%7%g%s(B | surfactant micelle DPD simulation | O |
259 | $B%K%e!<%H%sN.BNC1=c$;$sCGN.F02<$K$*$1$kK@>uA!0]$N%@%$%J%_%/%9(B | fiber motion shear flow numerical simulation | O |
361 | $B1UBN$H5$BN$N%/%m%9%U%m!<8=>]$K$*$1$kN.BNB.EY$K4X$9$k | ligament breakup LDV | O |
362 | $BHs%K%e!<%H%sN.BN%b%G%k$r9MN8$7$?1UBN$H5$BN$N%/%m%9%U%m!<8=>]$K4X$9$k?tCM2r@OE*8!F$(B | Volume of Fluid liquid jet crossflow | O |
389 | $BN.F0>lCf$N9bJ,;R$H$NMm$^$j$"$$$K5/0x$9$k%]%j%(%A%l%s%0%j%3!<%k$NN.F0Dq93$NJQ2=(B | drag force polymer conformation polymer entanglement | O |
431 | $BCOCfG.MxMQ%7%9%F%`$N:NG.4I$K$*$1$kDq93Dc8:8z2L(B | Drag Reduction Geothermal heat utilization system Surfactant | O |
432 | $B0BDj2=:^$rMQ$$$?(BMR$BN.BN$N%l%*%m%8!<$H0BDj@-I>2A | Stabilizer Stability Oil separation | O |
433 | $B%9%?%F%#%C%/%_%-%5!<$K$*$1$k(BMetzener-Otto$B7?J?6Q$;$sCGB.EY?d;;<0$K5Z$\$9=uAv6h4V$N1F6A(B | static mixer non-Newtonian fluid | O |
482 | $B%+!<%F%s%3!<%F%#%s%0$N?tCM%7%_%e%l!<%7%g%s(B | Coating Numerical Simulation | O |
486 | $BG4CF@-N.BNCf$NJ,;67O$K$*$1$k%7%"%7%C%/%K%s%0(B | suspension rheology viscoelastic | O |
512 | $B9g0l$rH<$&3KJ(F-5$K"$N@.D95sF0$N?tCM2r@O(B | Nucleate Boiling Bubble Growth Coalescence | O |
552 | $B2sE>1_?m4V$K$*$1$k(Bshear-thinning$BN.BNN.$l$N?tCM2r@O(B | Conical Taylor vortex flow Shear-thinning fluid Numerical simulation | O |
618 | $BN.DL7O05NO?6F0>l$K$*$1$k5$K"6aK5N.BN$NFs | continuous flow channel two-dimensional polarization measurement pressure oscillation | O |
649 | $B%"%k%+%j?eEE2r$K$*$1$k;@AG@8@.H?1~@-G=$NI>2A$H;@AG5$K"@8@.5sF0$N4X78(B | Alkaline water Electrolysis bubble growth rate hydrogen | O |
742 | VOF$B4X?t$+$i(BLevel Set $B4X?t$r9=@.$9$k7W;;K!(B | Level Set VOF surface tension | O |
802 | $B9bG4@-N.BNFCM-$N5sF0$N%b%G%k2=$H?tCM%7%_%e%l!<%7%g%s(B | high viscous fluid particle method numerical simulation | O |
851 | $B9bG4@-%"%k%+%jMO2r@-2q9g9bJ,;RMO1UCf$K$*$1$k;^J,$+$l7A>u$rM-$9$k5$K"$N>e>:1?F0(B | Bubble rise motion Viscoelastic fluid Elongated branching shape | O |
854 | $B;0@.J,7O$N3H;6$K$*$1$k(BStefan-Maxwell$B<0$H(BCorrection velocity$B$rMQ$$$?6a;w<0$NHf3S(B | Stefan-Maxwell Equation Gas Diffusion Correction Velocity | O |