$BJ!0f!!9qGn!J9-EgBg3X!K!&2CG |
$B:G=*99?7F|;~!'(B2016-01-20 13:09:01
$B$3$NJ,N`$G$h$/;H$o$l(B $B$F$$$k%-!<%o!<%I(B | $B%-!<%o!<%I(B | $B | |
---|---|---|---|
Grinding | 4$B7o(B | ||
defluidization | 2$B7o(B | ||
fluidized bed | 2$B7o(B | ||
Particle Size distribution | 2$B7o(B | ||
bag filter | 2$B7o(B | ||
DEM simulation | 2$B7o(B | ||
Breakage | 1$B7o(B |
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $BH/I=7A<0(B | |
---|---|---|---|
7 | [$BM%=(O@J8>^(B] $BN.F02=%,%9@Z$j49$($K$h$C$F0z$-5/$3$5$l$kHsN.F02=8=>]$N%a%+%K%:%`(B | fluidized bed defluidization non-equimolar diffusion | O |
28 | [$BM%=(O@J8>^(B] $BFqN.F0@-N3;R$NN.F0@-I>2A$K8~$1$??75,AuCV$N3+H/(B | poor powder flowability new Apparatus drained angle | O |
64 | [$BM%=(O@J8>^(B] $B@EEEJ.L8$K$h$k1UE)J,Nv$H%$%*%sJ|=P2aDx$K5Z$\$9MO1UG;EY$N1F6A(B | Electrospray Ion Generation Nano Particle | O |
98 | DEM$B%7%_%e%l!<%7%g%s$HB?JQNL2r@O$rMQ$$$?%\!<%k%_%kFb$NN3EYJ,I[M=B,(B | DEM simulation grinding particle size distribution | O |
99 | $BBN@Q8:>/$rH<$&H?1~$rN.F0?(G^AX$G9T$&>l9g$NN.F0@-@)8f(B | fluidized bed defluidization feedforward control | O |
110 | DEM$B$rMQ$$$?2sE>%I%i%`$K$*$1$kN3;R7BJ,I[$,:.9g5sF0$K5Z$\$91F6AI>2A(B | DEM simulation Particle Size distribution Segregation | O |
122 | $B6bB0?e;@2=J*$NMO2rEY@Q$r9MN8$7$?E47OAX>uJ#?e;@2=J*$N%a%+%N%1%_%+%k9g@.(B | layered double hydroxide mechanochemical synthesis ball-milling | O |
123 | $B?eG.=hM}$K$h$k@PC:3%$H%P%$%*%^%9G3>F3%$N%<%*%i%$%H$X$N:F;q8;2=(B | Coal fly ash Biomass incineration ash Zeolite | O |
125 | $BLZF3%$N@.J,J,N%$K4X$9$k8&5f(B | Woody biomass incineration ash Size classification Component separation | O |
139 | $BN3;RJ#9g:`NA$NJ4:U2aDx$G$NHyN3;RH/?P5sF0$N8!F$(B | Dust generation Composite material Nanoparticle | O |
249 | ADEM$B$K$h$kCFA:@-2r@O$N%b%G%j%s%0(B | Advanced DEM Breakage elastic-plastic | O |
321 | $B%P%0%U%#%k%?!<$N05NOB;<:$HJ4?PF)2aN($r?d;;$9$kL5 | bag filter pressure drop particle penetration | O |
323 | $B%P%0%U%#%k%?!<$N%9%1!<%k%"%C%W$K$*$1$k:GE,@_7W>r7o$K4X$9$k9M;!(B | bag filter scale-up optimum design condition | O |
435 | $B2~NI7?$N1UBN%5%$%/%m%s$K$h$kN3;RJ,N%FC@-(B | Hydro-cyclone Separation performance Particle size | O |
529 | $BM7@17?%\!<%k%_%k$rMQ$$$?;@2=J*J#9g2=%W%m%;%9$H%<%*%i%$%H9g@.$X$N1~MQ(B | Mechanochemical processing Composite formation Zeolite crystallization | O |
633 | $B0l<405=L@.7A$K$h$kJ4BN@.7ABN6/EY$N05=LB.EY0MB8@-$KBP$9$kJ4BNFC@-$N1F6A(B | tablet strength powder characteristics nano and micro particles | O |
658 | $BJ4BN= | packing structure packed bed electrical conductivity | O |
753 | $B9bG;EY@P3%@P%9%i%j!<$N%S!<%:%_%kJ4:U$K$h$k9bJ,;RJ,;6:^$N8z2L(B | Limestone Grinding Polymer dispersant | O |
776 | $B%P!<%JFbHyJ4C:G;=L5!9=$rLO5<$7$?N.O)$K$*$1$kN3;R5sF0$N?tCM2r@O(B | Pulverized coal burner Particle concentrator Numerical analysis | O |
794 | $BI=LL2~ | Scallop shell Plywood adhesive Grinding | O |
800 | $BJ4:U$K$h$k | Metal recovery Circuit board Grinding | O |
817 | $BJ.L8G.J,2rK!$K$h$kNU;@%3%P%k%H%j%A%&%`$N9g@.$H$=$N7ABV@)8f(B | LiCoPO4 Cathode Lithium battery | O |
923 | $B8G5$N.F0AX$K$*$1$k5$K"N.F02=$X$N>uBVA+0\$K5Z$\$95!3#E*?6F0IU2C$N1F6A(B | $BN.F0AX(B $B?6F0(B $B5$K"(B | O |
958 | $B5$CfHyN3;R$N0[AG:`I=LL$X$ND@CeNL7WB,%7%9%F%`$N9=C[(B | aerosol deposition measurement | O |