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| $B3a86L->0!J6e=#Bg!K!&ARDE@5J8!J=;=E5!3#%W%m%;%95!4o!K(B |
$B6aG/!$%_%-%7%s%05;=Q$N9bEY2=$NMW5a$d1~MQJ,Ln$N3HBg$KBP1~$7$F!$?7$?$J;kE@$+$i$N%_%-%7%s%0M}O@$N9=C[!$7WB,J}K!$d%7%_%e%l!<%7%g%s
$B:G=*99?7F|;~!'(B2011-07-05 14:32:01
| $B$3$NJ,N`$G$h$/;H$o$l(B $B$F$$$k%-!<%o!<%I(B | $B%-!<%o!<%I(B | $B | |
|---|---|---|---|
| Mixing | 8$B7o(B | | |
| CFD | 3$B7o(B | | |
| Twin-Screw Extruder | 3$B7o(B | | |
| Power Consumption | 2$B7o(B | | |
| Mixing Time | 2$B7o(B | | |
| Fluid Mixing | 2$B7o(B | | |
| Streakline | 2$B7o(B | | |
| Chaos Mixing | 2$B7o(B | | |
| isolated mixing region | 2$B7o(B | | |
| simulation | 2$B7o(B | | |
| Visualization | 2$B7o(B | | |
| solid-solid mixing | 1$B7o(B | | |
| $B | $B9V1iBjL\!?H/I=| $B%-!<%o!<%I(B | $B | |
|---|---|---|---|
| 51 | $BJ#9g:`NA$N:.9g>uBV$NDjNL2=(B: $BB?3,AX%9%1!<%k$NIT6Q0l@-(B | multiple scales of segregation complex mixture composite | 4/19 12:12:02 |
| 57 | $BFs<4%9%/%j%e2!=P5!$N?75,:.N}%(%l%a%s%H(B:$B79 | twin-screw extruder melt mixing numerical simuilation | 4/19 17:16:03 |
| 66 | [$BM%=(O@J8>^(B] $B3IYBAeFb$K$*$1$k8IN):.9gNN0h$NM}O@E*2r@O(B | Isolated Mixing Region Synchronization Visualization | 4/20 14:49:32 |
| 70 | $BN.BN$NN.$lJ}8~$NG;EY%`%i$r8z2LE*$K6Q0l2=$G$-$k@E;_7?%_%-%5$N8!F$(B | Static Mixer CFD Pulse of density | 4/20 16:26:30 |
| 76 | $BA/L@$JN.L.@~2D;k2= | Visualization Streakline Chaos Mixing | 4/20 19:00:51 |
| 113 | [$BM%=(O@J8>^(B] $B6~6J7?Hy>.%A%c%M%k$N:.9g@-G=Hf3S(B | Microchannel Fluid Mixing Bending Direction | 4/22 09:57:26 |
| 173 | $B@55U8r8_2sE>Mc3IYB$K$*$1$kN.BNJQ7AFC@-(B | mixing unsteady impeller | 4/23 11:16:50 |
| 179 | $B%@%&%J! | downer solid-solid mixing coal pyrolyzer | 4/23 18:38:28 |
| 223 | $B%,%i%96/2=7O | Twin-Screw Extruder Simulation Polymer Compounding | 4/25 13:34:01 |
| 245 | O$B!?(BW$B%(%^%k%7%g%s$rJ,;6Aj$KMxMQ$7$?9bG4EY!&1UE)J,NvB.EY$N7WB,K!(B | liquid-liquid dispersion measuring drop diameter drop breakage rate | 4/25 15:04:10 |
| 250 | $B5$1UJ,;6$,5Z$\$99bG4EY1U$N:.9g$X$N1F6A(B | Gas Dispersion Mixing Time Highly Viscous Liquids | 4/25 15:25:13 |
| 320 | $B2=3XH?1~$rMxMQ$7$?:.9g;~4VB,Dj$NLdBjE@(B | Fluid Mixing Mixing Time Chemical Reaction | 4/25 20:37:06 |
| 362 | $B3IYB1):,$K$h$jM65/$5$l$k@]F0$,AXN.:.9g$K5Z$\$91F6A(B | Chaos Mixing Streak Lobe Perturbation Effect | 4/26 12:01:18 |
| 390 | $B79 | Agitated vessel mass transfer Mixing | 4/26 14:10:28 |
| 393 | $BMpN.0h$K$*$1$kJ?%Q%I%kMcGXLLN.F0@)8fK!$H$=$NFC@-I>2A(B | Turbulent mixing paddle type impeller power consumption | 4/26 14:18:33 |
| 456 | MPS$BK!$rMQ$$$?HsDj>o3IYB$N%7%_%e%l!<%7%g%s(B | MPS simulation mixing | 4/26 17:14:17 |
| 464 | [$BE8K>9V1i(B] $B:.$<$k2J3X(B | Mixing Agitation Power Consumption | 4/26 17:32:18 |
| 474 | $BH?1~>=@O$K$*$1$kN3;R7A>u$K5Z$\$9N.F0$N1F6A(B | Crystallization Process Particle Shape Mixing | 4/26 17:53:11 |
| 596 | $B9-$$%l%$%N%k%:?tHO0O$rBP>]$H$7$?(BHi-F$B%_%-%5! | eccentric mixing large type impeller mixing energy | 4/27 11:01:09 |
| 601 | $BO"B33IYBAe$rMQ$$$?:.9gA`:n$K$*$1$kG;EY2t%9%1!<%k$N8!F$(B | continuous mixing tank reciprocating agitator scale of segregation | 4/27 11:06:27 |
| 618 | $B>e2 | Mixing Reciprocal motion CFD | 4/27 11:32:19 |
| 643 | $B2sE>1_E{7?1U1UCj=PAuCV$K$*$1$kN.F0>uBV$K5Z$\$9A`:n>r7o$N1F6A(B | mixing liquid-liquid extraction PIV | 4/27 12:27:42 |
| 706 | $BO"B3<0%K<4%(%/%9%H%k!<%@$N(BCFD$B$rMQ$$$?%9%1!<%k%"%C%W2r@O(B | Twin-Screw Extruder CFD Scale-up | 4/27 14:37:40 |
| 735 | $B3IYBAeFb$N8IN):.9gNN0h$K5Z$\$929EYJQ2=$N8z2L(B | isolated mixing region temperature change topological structure | 4/27 15:35:30 |
| 750 | $BN.L.@~$rMxMQ$7$?%^%C%/%9%V%l%s%IMc$K$*$1$kN.$l$N2D;k2=(B | Mixing Streakline Maxblend | 4/27 15:56:05 |
(C) 2011 $B8x1W
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easp 2.28; update.pl 2.28a (C)1999-2011 kawase