$B:G=*99?7F|;~!'(B2019-10-02 20:29:01
$B$3$NJ,N`$G$h$/;H$o$l(B $B$F$$$k%-!<%o!<%I(B | $B%-!<%o!<%I(B | $B | |
---|---|---|---|
filtration | 2$B7o(B | ||
membrane reactor | 1$B7o(B |
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $BH/I=7A<0(B | |
---|---|---|---|
76 | $B5e>uN3;R6E=8BN$N@8@.$K$*$1$kD62;GH%-%c%S%F!<%7%g%s5$K"$K:nMQ$9$kNO$N2r@O(B | Acoustic Cavitation Sonoluminescence Particle Flocculation | P |
77 | 20kHz$BBSD62;GH$K$h$j7A@.$9$k5e>uN3;R6E=8BN$N2sE>1?F0$N2D;k2=7WB,(B | Separation Ultrasound Particle Image Velocimetry | P |
138 | $B0[$J$k(BBOD$BIi2Y2<$K$*$1$kC4BNE:2C3h@-1xE%K!$N>K2=FC@-(B | Nitrification Activated sludge process Carrier | O |
218 | $BD@9_J,N%$rMxMQ$7$?E4$5$SN3;RJaB*%G%P%$%9$N3+H/(B | Iron oxide Sedimentation Circulating water | O |
929 | $B%U%m%C%/$ND@9_G[8~$HL)EY4X?t$N@:EY8~>e$K$D$$$F(B | Floc Diameter Two-sphere-model Sedimentation orientation | O |
931 | $B<'@-N3;R$N6&B8$K$h$kHy:YAtN`J,;61U$N%/%m%9%U%m!<$m2aKl$rMQ$$$?C&?e(B | microalgae dewatering cross flow | O |
939 | $BYxYB$*$h$S?6F0$K$h$kE`7kG;=L$X$N1F6A(B | freeze concentration vibration stirring | P |
984 | $B?)IJ!&6]!&9ZAG$rM-8z3hMQ$9$kKlMxMQ7?GQ?e=hM}%W%m%;%9$N3+H/(B | filtration membrane reactor decolorization | O |
1020 | Influence of humic acid on the flocculation of colloidal particles by cationic flocculant | Humic Acid Flocculation Rate Cationic Flocculant | P |
1056 | $B;@2=0!1t%9%i%j!<$N_I2a!&05:q2aDx$K$*$1$k3&LLF0EE3XE*1~Ez(B | streaming potential filtration period consolidation period | O |
1135 | $B%P%$%*%^%9A!0]$r$m:`$H$7$?%+%i%`7|By1U>t2=AuCV$K4X$9$k8&5f(B | suspension purification biomass fiber filtration | P |
1266 | $BM;2rB.EY$N0c$$$,E`7kM;2rK!$K$h$k?eMO1U$NG;=L$K5Z$\$91F6A(B | freeze-thawing technique thawing rate concentration distribution | O |
1443 | $B%J%N%R%I%m%-%7%"%Q%?%$%H=89gBN$NCf6u%^%$%/%m%9%U%#%"$N%?%s%Q%/ | hydroxyapatite hollow microsphere adsorption | O |
1466 | $B6bB0%a%C%7%e%G%P%$%9$r4p$K$7$?%Q!<%F%#%/%k%+%&%s%?!<$N3+H/(B | metal mesh device size separation particle counter | O |