$B$BHV9f(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$N2r@O(B ($B@EBg1!9)(B) ($B3X(B)$B!{DD(B $B1'?8(B$B!&(B ($B@EBgAO2J1!(B) ($B3X(B)$B?eC+(B $B9@Li(B$B!&(B ($B@EBg%0%j!<%s8&(B) ($B@5(B)$Bc7F#(B $BN4G7(B | Acoustic Cavitation Sonoluminescence Particle Flocculation
| P |
77 | 20kHz$BBSD62;GH$K$h$j7A@.$9$k5e>uN3;R6E=8BN$N2sE>1?F0$N2D;k2=7WB,(B ($B@EBg9)(B) ($B3X(B)$B!{>>1:(B $BN4@?(B$B!&(B ($B@EBg1!9)(B) ($B3X(B)$BDD(B $B1'?8(B$B!&(B ($B@EBgAO2J1!(B) ($B3X(B)$B?eC+(B $B9@Li(B$B!&(B ($B@EBg%0%j!<%s8&(B) ($B@5(B)$Bc7F#(B $BN4G7(B | Separation Ultrasound Particle Image Velocimetry
| P |
138 | $B0[$J$k(BBOD$BIi2Y2<$K$*$1$kC4BNE:2C3h@-1xE%K!$N>K2=FC@-(B ($B0&I2Bg1!M}9)(B) ($B@5(B)$B!{@n:j(B $B7rFs(B$B!&(B ($B3X(B)$B0KF#(B $BCR(B$B!&(B ($B4X@>2=9)(B) $BK-ED(B $B1Q><(B | Nitrification Activated sludge process Carrier
| O |
218 | $BD@9_J,N%$rMxMQ$7$?E4$5$SN3;RJaB*%G%P%$%9$N3+H/(B ($B;0I)EE5!(B) ($B@5(B)$B!{HSEg(B $BLP(B$B!&(B $B<99T(B $BOB9@(B$B!&(B $BLnED(B $B@6<#(B | Iron oxide Sedimentation Circulating water
| O |
929 | $B%U%m%C%/$ND@9_G[8~$HL)EY4X?t$N@:EY8~>e$K$D$$$F(B ($BC^GHBg@8L?(B) ($B@5(B)$B!{B-N)(B $BBY5W(B$B!&(B $BBW(B $By~pC(B$B!&(B (CAS) $B>S(B $BJv(B | Floc Diameter Two-sphere-model Sedimentation orientation
| O |
931 | $B<'@-N3;R$N6&B8$K$h$kHy:YAtN`J,;61U$N%/%m%9%U%m!<$m2aKl$rMQ$$$?C&?e(B ($B:42lBgM}9)(B) ($B@5(B)$B!{@n4nED(B $B1Q9'(B$B!&(B ($B:42lBg1!9)(B) ($B3X(B)$BLZC+(B $B1IH~(B$B!&(B ($B:42lBgM}9)(B) ($B@5(B)$B?9Dg(B $B??B@O:(B$B!&(B ($B@5(B)$BBgEO(B $B7<2p(B$B!&(B ($B:42lBgG@(B) $B=PB<(B $B441Q(B | microalgae dewatering cross flow
| O |
939 | $BYxYB$*$h$S?6F0$K$h$kE`7kG;=L$X$N1F6A(B ($B@EBg1!Am2J(B) ($B3X(B)$B!{1|B<(B $B0!Lm(B$B!&(B ($B@5(B)$BLZB<(B $B85I'(B$B!&(B ($B@EBg5;=QIt(B) ($B@5(B)$BBg66(B $BOB5A(B | freeze concentration vibration stirring
| P |
984 | $B?)IJ!&6]!&9ZAG$rM-8z3hMQ$9$kKlMxMQ7?GQ?e=hM}%W%m%;%9$N3+H/(B ($BL>Bg1!9)(B) ($B@5(B)$B!{JR6M(B $B@?G7(B$B!&(B ($B3X(B)$BKLH*(B $BCR;V(B$B!&(B ($B3X(B)$B?eLn(B $BM35.(B$B!&(B ($B@5(B)$BF~C+(B $B1Q;J(B | filtration membrane reactor decolorization
| O |
1020 | Influence of humic acid on the flocculation of colloidal particles by cationic flocculant (U. Tsukuba) ($B3X(B)$B!{(BLim Voon Huey$B!&(B ($B@5(B)Adachi Yasuhisa$B!&(B Yamashita Yuji | 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 ($B:eI\Bg1!9)(B) ($B3X(B)$B2<0KF&(B $BOB:H(B$B!&(B ($B@5(B)$B4d:j(B $BCR9((B$B!&(B ($BLyED;:6H(B) $BLyED(B $BOK9/(B$B!&(B ($B:eI\Bg1!9)(B) ($B@5(B)$B!{4dED(B $B@/;J(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 ($BD92,5;Bg1!9)(B) ($B3$(B)$Bld(B $B2E(B琨$B!&(B ($B@5(B)$B!{>.NS(B $B9b?C(B$B!&(B ($B9b:=G.3X9)6H(B) $B:4F#(B $BJvI'(B | suspension purification biomass fiber filtration
| P |
1266 | $BM;2rB.EY$N0c$$$,E`7kM;2rK!$K$h$k?eMO1U$NG;=L$K5Z$\$91F6A(B ($BIY;39b@l(B) ($B@5(B)$B!{CfEg(B $B1I$B!&(B $B>e;3(B $B2Z2B(B$B!&(B ($B@5(B)$BJvK\(B $B9/@5(B | freeze-thawing technique thawing rate concentration distribution
| O |
1443 | $B%J%N%R%I%m%-%7%"%Q%?%$%H=89gBN$NCf6u%^%$%/%m%9%U%#%"$N%?%s%Q%/ ($B?73cBg(B) ($B@5(B)$B!{EDCf(B $B9'L@(B$B!&(B $B9b0f(B $B7DI'(B$B!&(B $BD9@%(B $BL@;K(B$B!&(B $B;{8}(B $B0l$B!&(B $BL1It(B $BM5MN(B$B!&(B $BMn9g(B $B=)?M(B$B!&(B ($B@5(B)$BLZB<(B $BM&M:(B$B!&(B ($B@5(B)$BC+8}(B $B@5G7(B | hydroxyapatite hollow microsphere adsorption
| O |
1466 | $B6bB0%a%C%7%e%G%P%$%9$r4p$K$7$?%Q!<%F%#%/%k%+%&%s%?!<$N3+H/(B ($BJ!2,Bg9)(B) ($B@5(B)$B!{@%8M(B $B900l(B$B!&(B ($BJ!2,Bg1!9)(B) ($B3X(B)$B:4Gl(B $BFF;V(B$B!&(B ($BJ!2,Bg9)(B) $B>>2<(B $BN$B!&(B $B4d2<(B $BfF(B$B!&(B ($BB$B!&(B ($BJ!2,Bg9)(B) ($B@5(B)$BW"66(B $BM3H~;R(B$B!&(B ($B@5(B)$B?78M(B $B9@9,(B | metal mesh device size separation particle counter
| O |