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|---|---|---|---|
| mixing | 6$B7o(B | | |
| mixing impeller | 3$B7o(B | | |
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| gas-liquid mixing | 1$B7o(B | | |
| $B | $B9V1iBjL\!?H/I=| $B%-!<%o!<%I(B | $BH/I=7A<0(B | |
|---|---|---|---|
| 78 | $B5$(B-$B1U3IYB$K$*$1$k | gas-liquid mixing mixing impeller simulation | P |
| 79 | $B9bDL5$>r7o2<$N5$1UYxYBAe$K$*$1$kH?1~@-2~A1(B | gas-liquid agitation high gas flow rate shear-force agitating impeller | P |
| 80 | DEM$B%7%_%e%l!<%7%g%s$rMQ$$$?9bB.J4BN:.9gAuCV$N1):,7A>u$,:.9g$K5Z$\$91F6A(B | DEM simulation segregation design | P |
| 81 | $B | mixing Hi-F mixer | P |
| 82 | $BN.F0AXFbJ4BN:.9g@-$NDjNL2= | fluidized bed powder mixing quantitative method | P |
| 83 | $BN.F02r@O5;=Q$rMQ$$$?3IYBAe%9%1!<%k%"%C%W;vNc(B | mixing scale-up | P |
| 84 | $B=;M'$N3IYBMc(BLine-Up | mixing impeller high share gas absorption | P |
| 85 | $B2=3X%W%i%s%H$K$*$1$kYxYB%7%_%e%l!<%7%g%s;vNc$N>R2p(B | CFD mixing | P |
| 87 | $B?77?%&%)!<%k(B $B%&%'%C%?! | mixing heat transfer splash | P |
| 88 | $B3IYBAe7?H?1~5!$N@_7W;X?K(B($B3IYBMc!"%P%C%U%k$rCf?4$K(B) | mixing mixing impeller baffle | P |
| 90 | $BBg7?Mc$rMQ$$$?JP?43IYB(B | eccentric mixing large-type impeller mixing | P |
| 92 | $BBg7?Mc$N:.9g@-G=I>2A$H;HMQ$9$k:]$NCeL\E@(B | large paddle impeller power consumption streak line | P |
| 137 | $B3IYB%W%m%;%9$K$*$1$kN3;RK!N.BN%7%_%e%l!<%7%g%s$NE,MQ(B | CFD MPS method scaleup | P |
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(C) 2015 $B8x1WMost recent update: 2015-07-10 15:24:01
For more information contact $B2=3X9)3X2q;vL36I(B $BBh(B80$BG/2q(B $BLd$$9g$;78(B
E-mail: inquiry-80a
www3.scej.orgThis page was generated by easp 2.36; update.pl 2.37 (C)1999-2015 kawase
easp 2.36; update.pl 2.37 (C)1999-2015 kawase