$B9V1i(J $B;~9o(J | $B9V1i(J $BHV9f(J | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(J | $BJ,N`(J $BHV9f(J | $B$BHV9f(J | |
A:$BJ,N%%W%m%;%9(J, $BD6NW3&N.BNEy(J |
(13:30$B!A(J15:00)$B!!(J($B:BD9(J $B=EK\(J $BD>Li!&@n:j!!7rFs(J) |
13:30$B!A(J 13:45 | A101 | $B0!NW3&?eCf$G$N%0%j%;%j%s$+$iF};@$X$NE>49H?1~$K4X$9$k9M;!(J
($B2,;3Bg1!4D(J) $B!{(J($B3X(J)$B>eLn(J $BfFJ?(J $B!&(J ($B2,;3Bg1!<+A3(J) ($B@5(J)$B>.Ln(J $BEX(J $B!&(J ($B2,;3Bg1!4D(J) ($B@5(J)$BLZB<(J $B9,7I(J | subcritical water glycerol lactic acid
| 8-d | 57 |
13:45$B!A(J 14:00 | A102 | $BD6NW3&Fs;@2=C:AGCf$G$N(JPMMA$B$NJ,;6=E9g(J
($B9-Bg1!9)(J) $B!{(J($B3X(J)$BF|7n(J $B2w(J $B!&(J $BQ;6L(J $BM5:H(J $B!&(J ($B@5(J)$B=ULZ(J $B>-;J(J $B!&(J ($B@5(J)$BLZ86(J $B?-0l(J $B!&(J ($B@5(J)$BBlV:(J $BHK | supercritical carbon dioxide dispersion polymerization particle
| 8-e | 39 |
14:00$B!A(J 14:15 | A103 | $BD6NW3&Fs;@2=C:AG$rMQ$$$?(JPGSS$BK!$K$h$k%]%j%^!<$NHyN3;R2=(J
($B9-Bg1!9)(J) $B!{(J($B3X(J)$BBgLn(J $BfFB@O/(J $B!&(J ($B9-Bg9)(J) $BHx:j(J $B=gDg(J $B!&(J ($B9-Bg1!9)(J) ($B@5(J)$B=ULZ(J $B>-;J(J $B!&(J ($B@5(J)$BLZ86(J $B?-0l(J $B!&(J ($B@5(J)$BBlV:(J $BHK | supercritical PGSS particle
| 8-e | 14 |
14:15$B!A(J 14:30 | A104 | NMR$B$rMQ$$$?%J%NN3;R6aK5J,;R$NF0E*5sF04Q;!$HN3;RAj4V0\F0%a%+%K%:%`$N8!F$(J
($BFAEgBg1!9)(J) $B!{(J($B3X(J)$B5WJ]ED(J $BCR;K(J $B!&(J ($B@5(J)$BKY2O(J $B=S1Q(J $B!&(J $B5HED(J $B7r(J $B!&(J ($B@5(J)$B2CF#(J $B2mM5(J $B!&(J ($B@5(J)$B30NX(J $B7r0lO:(J | nano particle phase transfer NMR
| 4-e | 3 |
14:30$B!A(J 14:45 | A105 | $B@=Kl>r7o$N0[$J$k%-%H%5%sKl$N(JCO2/N2$BF)2aJ,N%FC@-(J
($B;38}Bg1!M}9)(J) $B!{(J($B3X(J)$B2&(J $B $B!&(J ($B@5(J)$B7'@Z(J $B@t(J $B!&(J ($B@5(J)$BEDCf(J $B0l9((J $B!&(J ($B@5(J)$B4nB?(J $B1QIR(J | Chitosan CO2 separation membrane gas separation
| 4-a | 65 |
14:45$B!A(J 15:00 | A106 | Bis(triethoxysilyl)ethane (BTESE)$B$rMQ$$$?9bF)2a@-?eAGJ,N%Kl$N3+H/(J
($B9-Bg1!9)(J) $B!{(J($B3X(J)$B?78+(J $BBsLp(J $B!&(J ($B@5(J)$BD9_7(J $B425,(J $B!&(J ($B@5(J)$B6b;X(J $B@58@(J $B!&(J ($B@5(J)$B5H2,(J $BJ~5W(J $B!&(J ($B@5(J)$BETN1(J $BL-N;(J | hydrogen separation membrane reactor organic hydrides
| 4-a | 37 |
(15:00$B!A(J16:30)$B!!(J($B:BD9(J $BETN1(J $BL-N;!&EDCf(J $B0l9((J) |
15:00$B!A(J 15:15 | A107 | $BB?9&
($BFAEgBg1!@hC<650iIt(J) $B!{(J($B3X(J)$BKL86(J $BM'N<(J $B!&(J ($B3X(J)$BLZFb(J $B9@Fs(J $B!&(J ($BFAEgBg1!(JSTS$B8&5fIt(J) ($B@5(J)$B2CF#(J $B2mM5(J $B!&(J ($B@5(J)$BKY2O(J $B=S1Q(J $B!&(J ($B@5(J)$BCf@n(J $B7I;0(J $B!&(J ($B@5(J)$B?y;3(J $BLP(J | Pd-Cu alloy membrane Porous stainless steel tube Hydrogen separation
| 4-a | 28 |
15:15$B!A(J 15:30 | A108 | $BCfOBK!$rMQ$$$?%K%C%1%kGS?e$N=hM}(J
($B0&I2Bg1!M}9)(J) $B!{(J($B3X(J)$BA}ED(J $B>MB@(J $B!&(J ($B@5(J)$B@n:j(J $B7rFs(J $B!&(J ($B;0I)%l%$%h%s(J) ($B@5(J)$B6b;R(J $B??(J $B!&(J ($B@5(J)$B@n4_(J $BJ~ | nickel wastewater sedimentation
| 4-b | 24 |
15:30$B!A(J 15:45 | A109 | $BC:;@%+%k%7%&%`N3;R$r1~MQ$7$?J#9g7?_I2aJ}<0$K$h$k%U%_%s;@MO1U$N8B30_I2a(J
($B;38}Bg1!M}9)(J) $B!{(J($B3X(J)$BCSED(J $BM:Bg(J $B!&(J ($B@5(J)$BCfAR(J $B1QM:(J | humic acid calcium carbonate ultrafiltration
| 4-b | 42 |
15:45$B!A(J 16:00 | A110 | $B?6F07?%U%#%k%?!<$K$h$k6E=8%U%_%s;@%9%i%j!<$N%@%$%J%_%C%/@:L)_I2a(J
($B;38}Bg1!M}9)(J) $B!{(J($B3X(J)$B0,5H(J $B?r;K(J $B!&(J ($B@5(J)$BCfAR(J $B1QM:(J | vibratory filtration cake filtration humic acid
| 4-b | 43 |
16:00$B!A(J 16:15 | A111 | $B%X%-%5%7%"%NE4(J($B-6(J)$B;@E4(J($B-7(J)$B%+%j%&%`C4;}3h@-C:$ND4@=$H$=$N%;%7%&%`5[Ce5sF0(J
($B;M9qAm8&(J) $B!{(J($B@5(J)$B=EK\(J $BD>Li(J $B!&(J $B1v:j(J $B7J;R(J | Caesium removal activated carbon hexacyanoferrate
| 4-e | 30 |
16:15$B!A(J 16:30 | A112 | $BAj8_:nMQ4p$rF3F~$7$?4629@-%]%j%^!<$K$h$k?eCf$N9EEY@.J,$N5[C&CeFC@-(J
($B9-Bg9)(J) $B!{(J($B3X(J)$B7*;3(J $BPRM4(J $B!&(J ($B@5(J)$BGw86(J $B=$<#(J | thermosensitive polymer temperature swing adsorption
| 4-e | 35 |
(16:30$B!A(J17:45)$B!!(J($B:BD9(J $B=ULZ>-;J!&Cf@n!!7I;0(J) |
16:30$B!A(J 16:45 | A113 | $B:Y9&9=B$$N0[$J$kB?9&x5$5[Ce$N29EY0MB8@-(J
($BFAEgBg1!9)(J) $B!{(J($B3X(J)$BC]%NFb(J $B2mE5(J $B!&(J ($B@5(J)$BKY2O(J $B=S1Q(J $B!&(J $B:dHx(J $BNQ9,(J $B!&(J ($B@5(J)$B30NX(J $B7r0lO:(J $B!&(J (Queensland$BBg(J) Do D. D. | water vapor adsorption porous carbon temperature dependence
| 4-e | 2 |
16:45$B!A(J 17:00 | A114 | $B:Y9&7B$N0[$J$kB?2AK!$N8!F$(J
($B9-Bg1!9)(J) $B!{(J($B3X(J)$B9b66(J $BKcN$;R(J $B!&(J ($B@5(J)$B5H2,(J $BJ~5W(J $B!&(J ($B@5(J)$BD9_7(J $B425,(J $B!&(J ($B@5(J)$B6b;X(J $B@58@(J $B!&(J ($B@5(J)$BETN1(J $BL-N;(J | zeolite microporous adsorption
| 4-a | 29 |
17:00$B!A(J 17:15 | A115 | $B%P%$%*%(%?%N!<%k>xN1J*$K$*$1$kKlJ,N%$NE,MQ(J
($B;38}Bg1!M}9)(J) $B!{(J($B3X(J)$B6yED(J $BfF(J $B!&(J ($B@5(J)$B4nB?(J $B1QIR(J $B!&(J ($B@5(J)$BEDCf(J $B0l9((J $B!&(J ($B@5(J)$B7'@Z(J $B@t(J | bio-ethanol carbon zeolite
| 4-a | 67 |
17:15$B!A(J 17:30 | A116 | $B?;DR7?KlJ,N%3h@-1xE%K!$N1?E>A`:n$K5Z$\$9(JBOD$BMF@QIi2Y$N1F6A(J
($B0&I2Bg1!M}9)(J) $B!{(J($B3X(J)$BEZ $B!&(J ($B@5(J)$B@n:j(J $B7rFs(J | volumetric-BOD-loading activated-sludge-process submerged-membrane-filter
| 4-b | 25 |
17:30$B!A(J 17:45 | A117 | $BCf6u;e@:L)_I2aKl$NAG:`$,M>>j3h@-1xE%$N_I2aFC@-$K5Z$\$91F6A(J
($B0&I2Bg1!M}9)(J) $B!{(J($B3X(J)$BF#K\(J $BN4;V(J $B!&(J ($B@5(J)$B@n:j(J $B7rFs(J $B!&(J ($B;0I)%l%$%h%s(J) ($B@5(J)$B6b;R(J $B??(J $B!&(J ($B@5(J)$B@n4_(J $BJ~ | waste water treatment membrane activated sludge
| 4-b | 26 |