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$B2=3X9)3X2q(B $BBh(B51$B2s=)5(Bg2q(B (2020)

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$B:G=*99?7F|;~!'(B2021-02-07 15:20:01

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$B$F$$$k%-!<%o!<%I(B
$B%-!<%o!<%I(B$B
numerical simulation5$B7o(B*
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Stefan-Maxwell Equation1$B7o(B

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($B;37ABg1!M}9)(B) ($B3X(B)$B!{;01:(B $BOBLi(B$B!&(B ($B@5(B)$BLg3p(B $B=(
mixed convection
heat transfer
numerical simulation
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45$B8G1U3IYBAeFb$NJILLG.EAC#$K5Z$\$9IbM7@-N3;R:.F~$N1F6A(B
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Solid-Liquid Mixing
Floating Particle
Heat Transfer
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49$B?75,L52A!A6I=jJ(F-$*$h$S1U1U3&LL$NI=LL2~
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Microwave
dimensionless number
boiling
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254$B$R$b>u%_%;%k?eMO1U7O$N%a%=%9%1!<%k%7%_%e%l!<%7%g%s(B
($B5~Bg1!9)(B) ($B3X(B)$B!{J?>>(B $B?rJ8(B$B!&(B ($B@5(B)$BC+8}(B $B5.;V(B
surfactant
micelle
DPD simulation
O
259$B%K%e!<%H%sN.BNC1=c$;$sCGN.F02<$K$*$1$kK@>uA!0]$N%@%$%J%_%/%9(B
($B5~Bg1!9)(B) ($B3X(B)$B!{@nyu(B $B905.(B$B!&(B ($B@5(B)$BC+8}(B $B5.;V(B
fiber motion
shear flow
numerical simulation
O
361$B1UBN$H5$BN$N%/%m%9%U%m!<8=>]$K$*$1$kN.BNB.EY$K4X$9$k
($B6e9)Bg1!9)(B) ($B3X(B)$B!{5\K\(B $B??4u(B$B!&(B ($B@5(B)$Bc7F#(B $BBYMN(B$B!&(B ($B90A0BgM}9)(B) ($B@5(B)$B>kED(B $BG@(B$B!&(B ($BElKLBg1!9)(B) ($B@5(B)$B>>2<(B $BMN2p(B$B!&(B ($B@5(B)$B@DLZ(B $B=(G7(B$B!&(B ($B6e9)Bg1!9)(B) ($B@5(B)$BGOEO(B $B2B=((B$B!&(B ($B@5(B)$B;3B<(B $BJ}?M(B
ligament
breakup
LDV
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362$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$(B
($B6e9)Bg1!9)(B) ($B3X(B)$B!{8~0f(B $B7r?M(B$B!&(B ($B@5(B)$Bc7F#(B $BBYMN(B$B!&(B ($B90A0BgM}9)(B) ($B@5(B)$B>kED(B $BG@(B$B!&(B ($BElKLBg1!9)(B) ($B@5(B)$B>>2<(B $BMN2p(B$B!&(B ($B@5(B)$B@DLZ(B $B=(G7(B$B!&(B ($B6e9)Bg1!9)(B) ($B@5(B)$BGOEO(B $B2B=((B$B!&(B ($B@5(B)$B;3B<(B $BJ}?M(B
Volume of Fluid
liquid jet
crossflow
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389$BN.F0>lCf$N9bJ,;R$H$NMm$^$j$"$$$K5/0x$9$k%]%j%(%A%l%s%0%j%3!<%k$NN.F0Dq93$NJQ2=(B
($B?@8MBg1!9)(B) ($B3X(B)$B!{F#8M(B $B7rLp(B$B!&(B ($B@5(B)$BF|=P4V(B $B$k$j(B$B!&(B ($B@5(B)$BNkLZ(B $BMN(B
drag force
polymer conformation
polymer entanglement
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($B;38}Bg1!AO(B) ($B@5(B)$B!{:4Gl(B $BN4(B$B!&(B ($B@5(B)$B3-=P(B $B0<(B$B!&(B ($B?7F|K\6uD4(B) $B1J:d(B $BLPG7(B
Drag Reduction
Geothermal heat utilization system
Surfactant
O
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Stabilizer
Stability
Oil separation
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433$B%9%?%F%#%C%/%_%-%5!<$K$*$1$k(BMetzener-Otto$B7?J?6Q$;$sCGB.EY?d;;<0$K5Z$\$9=uAv6h4V$N1F6A(B
($B?@8MBg1!9)(B) ($B3X(B)$B!{>.@>(B $BM55.(B$B!&(B ($B@5(B)$BKY9>(B $B9';K(B$B!&(B ($B%+%M%+(B) ($B@5(B)$BK-ED(B $B6fF)(B$B!&(B ($B?@8MBg1!9)(B) ($B@5(B)$BBgB<(B $BD>?M(B$B!&(B ($B@5(B)$B8VED(B $B1YG7(B
static mixer
non-Newtonian fluid
O
482$B%+!<%F%s%3!<%F%#%s%0$N?tCM%7%_%e%l!<%7%g%s(B
($B:k6LBg9)(B) ($B3X(B)$B!{@iMU(B $B9/B@O:(B$B!&(B ($B:k6LBg1!M}9)(B) ($B3X(B)$B@iMU(B $B>"(B$B!&(B ($B3X(B)$BCfEg(B $BNKB@(B$B!&(B ($B@5(B)$BK\4V(B $B=S;J(B$B!&(B ($B%5%$%G%s2=3X(B) $BG_5\(B $B90OB(B$B!&(B $B>.ED(B $B=c5W(B
Coating
Numerical Simulation
O
486$BG4CF@-N.BNCf$NJ,;67O$K$*$1$k%7%"%7%C%/%K%s%0(B
($B6eBg(B) ($B@5(B)$B!{L>2E;3(B $B>MLi(B$B!&(B ($B6eBg(B/$B=;M'%Y!<%/%i%$%H(B) ($B3X(B)$B>>2,(B $BM$$B!&(B ($B6eBg(B) ($B@5(B)$B3a86(B $BL->0(B
suspension
rheology
viscoelastic
O
512$B9g0l$rH<$&3KJ(F-5$K"$N@.D95sF0$N?tCM2r@O(B
($BFAEgBg1!@hC<650iIt(B) ($B3X(B)$B!{W"2,(B $BM&?M(B$B!&(B ($BFAEgBg1!
Nucleate Boiling
Bubble Growth
Coalescence
O
552$B2sE>1_?m4V$K$*$1$k(Bshear-thinning$BN.BNN.$l$N?tCM2r@O(B
($B:e;TBg1!9)(B) ($B@5(B)$B!{A}ED(B $BM&?M(B$B!&(B ($B@5(B)$B0KgPED(B $B9@;V(B$B!&(B ($B?@8MBg1!9)(B) ($B@5(B)$BBgB<(B $BD>?M(B
Conical Taylor vortex flow
Shear-thinning fluid
Numerical simulation
O
618$BN.DL7O05NO?6F0>l$K$*$1$k5$K"6aK5N.BN$NFs
($BL>9)Bg1!9)(B) ($B3X(B)$B!{ED8}(B $B8WG72p(B$B!&(B ($B@5(B)$B4dED(B $B=$0l(B
continuous flow channel
two-dimensional polarization measurement
pressure oscillation
O
649$B%"%k%+%j?eEE2r$K$*$1$k;@AG@8@.H?1~@-G=$NI>2A$H;@AG5$K"@8@.5sF0$N4X78(B
($B2#9qBgM}9)(B) ($B3X(B)$B!{CSED(B $BH;B@(B$B!&(B $B>.Eh(B $BM4Bg(B$B!&(B $B%5%s%H%9(B $B%&%#%k%H%s(B$B!&(B ($B2#9qBg1!9)(B) ($B@5(B)$B;03Q(B $BN4B@(B$B!&(B $B8wEg(B $B=EFA(B
Alkaline water Electrolysis
bubble growth rate
hydrogen
O
742VOF$B4X?t$+$i(BLevel Set $B4X?t$r9=@.$9$k7W;;K!(B
($B=;M'2=3X(B) ($BK!(B)$B!{Fb66(B $BM42p(B$B!&(B ($BK!(B)$BH,=E3_(B $BM%B@(B$B!&(B ($B@5(B)$BEgED(B $BD>
Level Set
VOF
surface tension
O
802$B9bG4@-N.BNFCM-$N5sF0$N%b%G%k2=$H?tCM%7%_%e%l!<%7%g%s(B
($B%*%U%#%9<<1`(B) ($B@5(B)$B<<1`(B $B9@;J(B
high viscous fluid
particle method
numerical simulation
O
851$B9bG4@-%"%k%+%jMO2r@-2q9g9bJ,;RMO1UCf$K$*$1$k;^J,$+$l7A>u$rM-$9$k5$K"$N>e>:1?F0(B
($BFAEgBg1!AO@.2J3X(B) ($B3X(B)$B!{:dK\(B $BOB51(B$B!&(B ($BFAEgBg1!$B!&(B ($BL>9)Bg1!9)(B) ($B@5(B)$B4dED(B $B=$0l(B
Bubble rise motion
Viscoelastic fluid
Elongated branching shape
O
854$B;0@.J,7O$N3H;6$K$*$1$k(BStefan-Maxwell$B<0$H(BCorrection velocity$B$rMQ$$$?6a;w<0$NHf3S(B
($BElKLBg1!9)(B) ($B3X(B)$B!{>B_7(B $B7k(B$B!&(B ($B@5(B)$B>>@n(B $B2ELi(B$B!&(B ($B@5(B)$B>>2<(B $BMN2p(B$B!&(B ($B@5(B)$B@DLZ(B $B=(G7(B$B!&(B ($BElKLBgN.BN8&(B) $B>.5\(B $BFX
Stefan-Maxwell Equation
Gas Diffusion
Correction Velocity
O

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$B2=3X9)3X2q(B $BBh(B51$B2s=)5(Bg2q(B (2020)

(C) 2021 $B8x1W
Most recent update: 2021-02-07 15:20:01
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