|
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K$B2q>l(B |
(9:30$B!A(B10:45) ($B:BD9(B $BLZB<(B $B9,7I!&4_K\(B $B>:(B) |
9:30$B!A(B 9:45 | K101 | $BL55!!&9bJ,;R6E=8:^J;MQ7O$N=|By@-G=$KM?$($k9bJ,;RJ*@-$N1F6A(B
($B:eI\Bg9)(B) $B!{8eF#(B $B@5B@O:(B$B!&(B ($B0B@Q_I;f(B) $BNw2,(B $BM5?M(B$B!&(B ($B:eI\Bg9)(B) $BLZA>(B $BM'9aN$(B$B!&(B ($B:eI\Bg1!9)(B) ($B@5(B)$BEDCf(B $B9'FA(B$B!&(B ($B@5(B)$B4dED(B $B@/;J(B | Flocculation Composite flocculant Water treatment
| 4-b | 45 |
9:45$B!A(B 10:00 | K102 | $B?;DR7?KlJ,N%3h@-1xE%K!$K$*$1$k(BBOD$BMF@QIi2Y$N0c$$$K$h$k1xE%G;EY$NJQ2=(B
($B0&I2Bg9)(B) $B!{BgDM(B $B7DB@O:(B$B!&(B ($B@5(B)$B@n:j(B $B7rFs(B | activated sludge treatment submerged membrane sludge concentration
| 4-b | 61 |
10:00$B!A(B 10:15 | K103 | $BH>F3BN9)Dx$K$*$1$k%7%j%3%sGS?e$NJ?HD7?(BMF$BKl$K$h$k8G1UJ,N%(B
($BBg:eEEDLBg(B) $B!{KRLn(B $BfF(B$B!&(B $BF#Ln(B $BM4?M(B$B!&(B ($B3X(B)$BCSED(B $BD>$B!&(B ($B@5(B)$B9b2,(B $BBgB$(B | colloidal silicon solid-liquid separation MF membrane
| 4-b | 62 |
10:15$B!A(B 10:30 | K104 | $BJ?HD7?(BMF$BKl$r;HMQ$7$?Gx5$$K$h$k%@%$%J%_%C%/_I2a$NN.$l2r@O(B
($BBg:eEEDLBg(B) $B!{J?@P(B $BOB4u(B$B!&(B $B;38}(B $BNC2p(B$B!&(B ($B3X(B)$BCSED(B $BD>$B!&(B ($B@5(B)$B9b2,(B $BBgB$(B | solid-liquid separation flow analysis aeration
| 4-b | 65 |
10:30$B!A(B 10:45 | K105 | $B;nNA$NJP@O$rH<$&1s?4C&?eA`:n(B
($B:eI\Bg9)(B) $B!{%.%s%F%#%s(B $B%"%k%S%s(B$B!&(B ($B:eI\Bg1!9)(B) ($B3X(B)$BJ!;3(B $BN<(B$B!&(B ($B@5(B)$BEDCf(B $B9'FA(B$B!&(B ($B@5(B)$B4dED(B $B@/;J(B | Centrifuge Segregation Sedimentation
| 4-b | 67 |
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10:45$B!A(B 11:00 | K106 | $B%^%$%/%m%P%V%k$r4^$`8G1U7O$NFC@-(B
($B:eI\Bg9)(B) $B!{@8J}(B $B51(B$B!&(B ($B:eI\Bg1!9)(B) ($B3X(B)$B5AK\(B $BL@I'(B$B!&(B ($B@5(B)$BEDCf(B $B9'FA(B$B!&(B ($B@5(B)$B4dED(B $B@/;J(B | Microbubble Aggregation Zeta potential
| 4-b | 69 |
11:00$B!A(B 11:15 | K107 | $B%+%A%*%s@-$*$h$S%"%K%*%s@-4629@-%]%j%^!<$NJ;MQ$K$h$k>e?e1xE%$NC&?e(B
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| 4-b | 73 |
11:15$B!A(B 11:30 | K108 | $BD@9_$rH<$&%9%i%j!<$N$m2aFC@-(B
($B:eI\Bg9)(B) $B!{@P0f(B $BIp;V(B$B!&(B ($B:eI\Bg1!9)(B) ($B@5(B)$BEDCf(B $B9'FA(B$B!&(B ($B@5(B)$B4dED(B $B@/;J(B | Filtration Expression Settling
| 4-b | 93 |
11:30$B!A(B 11:45 | K109 | $B%_%-%5!<%;%H%i!
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| 4-f | 15 |
11:45$B!A(B 12:00 | K110 | $BM-MQJ*r7o2<$G$NCj=P!A%9%i%0N.$NMxMQ!A(B
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| 4-f | 58 |
(13:00$B!A(B14:15) ($B:BD9(B $BJ!CO(B $B8-<#!&9b2,(B $BBgB$(B) |
13:00$B!A(B 13:15 | K111 | $B2aG.?e>x5$$rMQ$$$?%P%$%*%^%93h@-C:$ND4@=(B
($BOB2N;39b@lJ*$B!&(B ($B@5(B)$B4_K\(B $B>:(B | activated carbon superheated steam adsorption
| 4-e | 37 |
13:15$B!A(B 13:30 | K112 | $B2aG.?e>x5$$K$h$jD4@=$5$l$?3h@-C:$K$*$1$kCe?'GQ?eCf$N860xJ*
($BOB2N;39b@lJ*>Hx(B $B4n?M(B$B!&(B ($B@5(B)$B4_K\(B $B>:(B | colored wastewater activated carbon superheated steam
| 4-e | 38 |
13:30$B!A(B 13:45 | K113 | $BG_43D4L#GQ1U$K4^$^$l$kE7A3?'AG$N3h@-C:$K$*$1$k5[CeJ?9U4X78(B
($BOB2N;39b@lJ*$B!&(B ($B@5(B)$B4_K\(B $B>:(B | activated carbon adsorption mechanism natural color
| 4-e | 40 |
13:45$B!A(B 14:00 | K114 | $B%P%$%*%^%9C:2=J*$ND4<>:`$H$7$F$NMxMQ(B
($B4X@>Bg4D6-ET;T(B) $B!{1F1:(B $BD>$B!&(B $BJ!ED(B $B>M;R(B$B!&(B ($B@5(B)$BNS(B $B=g0l(B | biomass adsorption humidity
| 4-e | 27 |
14:00$B!A(B 14:15 | K115 | $B3h@-C:$rMQ$$$?G"FGAG$N5[Ce=|5n(B
($B4X@>Bg4D6-ET;T(B) $B!{9b>>(B $B2B9((B$B!&(B $B2F86(B $BM-;J(B$B!&(B ($B@5(B)$BNS(B $B=g0l(B | uremic toxin activated carbon adsorption
| 4-e | 47 |
(14:15$B!A(B15:45) ($B:BD9(B $B4_K\(B $B>:!&NS(B $B=g0l(B) |
14:15$B!A(B 14:30 | K116 | $B0l;@2=CbAG5[CeC4BN$K$h$k?75,C&>K%W%m%;%9$N3+H/(B
($B:eI\Bg9)(B) $B!{(B($B3X(B)$B1|0f(B $B85(B$B!&(B ($B3X(B)$B;3K\(B $BfFB@(B$B!&(B ($BB?EDEE5!(B) $B;3Fb(B $B;MO:(B$B!&(B ($B8x32KI;_5!4o8&(B) $B@uLn(B $B=(><(B$B!&(B ($B:eI\Bg9)(B) ($B@5(B)$B0BED(B $B>;90(B$B!&(B ($B@5(B)$B2.Ln(B $BGn9/(B | denitration process NOx Nitrogen monoxide
| 4-e | 63 |
14:30$B!A(B 14:45 | K117 | $B29EY1~Ez7?5[Ce:`$K$h$k?eCf$N6bB0%$%*%s$N5[C&CeFC@-(B
($B9-Bg9)(B) $B!{(B($B3X(B)$B;38}(B $BBsGO(B$B!&(B ($B9-Bg1!9)(B) ($B3X(B)$B7*;3(B $BPRM4(B$B!&(B ($B@5(B)$BGw86(B $B=$<#(B | thermosensitive adsorbent temperature swing metal ion
| 4-e | 76 |
14:45$B!A(B 15:00 | K118 | $B%"%k%+%j=hM}$r;\$7$?(BZSM-5$B%<%*%i%$%H$N?e>x5$5[Ce5sF0(B
($BFAEgBg9)(B) $B!{(B($B3X(B)$B:4F#(B $BJ89a(B$B!&(B ($BFAEgBg1!@hC<650iIt(B) ($B3X(B)$B?yLn(B $B??@8(B$B!&(B ($B3X(B)$BLZB<(B $B;0@iN$(B$B!&(B ($BFAEgBg1!(BSTS$B8&5fIt(B) ($B@5(B)$B2CF#(B $B2mM5(B$B!&(B ($B@5(B)$BCf@n(B $B7I;0(B$B!&(B ($B@5(B)$B?y;3(B $BLP(B | ZSM-5 zeolite Alkali treatment Water adsorption
| 4-e | 127 |
15:00$B!A(B 15:15 | K119 | $B%(%?%N!<%k?eMO1U$+$i3F
($B1'It9b@l(B) $B!{:dK\(B $BNK(B$B!&(B ($B@5(B)$B;05H(B $B9n8J(B$B!&(B ($B@5(B)$BJ!CO(B $B8-<#(B | Adsorption equilibria Ethanol Aqueous solution
| 4-e | 121 |
15:15$B!A(B 15:30 | K120 | $B%(%?%N!<%k>x5$$+$i3F
($B1'It9b@l(B) $B!{@>B<(B $BM451(B$B!&(B ($B@5(B)$B;05H(B $B9n8J(B$B!&(B ($B@5(B)$BJ!CO(B $B8-<#(B | Adsorption equilibria Ethanol Elution method
| 4-e | 123 |
15:30$B!A(B 15:45 | K121 | $B3X=,MQ?eAGG3NAEECS%-%C%H$N2~NI$H%a%s%F%J%s%9(B
($B1'It9b@l(B) $B!{2-K\(B $BBn8J(B$B!&(B ($B@5(B)$B;05H(B $B9n8J(B$B!&(B ($B@5(B)$BJ!CO(B $B8-<#(B | PEM fuel cell Hydrogen Maintenance
| 14-c | 129 |