$B9V1i(B $B;~9o(B | $B9V1i(B $BHV9f(B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $BJ,N`(B $BHV9f(B | $B$BHV9f(B | |
E$B2q>l(B $BBh(B1$BF|(B |
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11:00$B!A(B 11:20 | E107 | SPG$BKlF}2=K!$rMQ$$$?C1J,;6%-%H%5%s%^%$%/%m%+%W%;%k$ND4@=(B ($BElBg9)(B) $B!{(B($B3X(B)$B7s;R(B $BBg:n(B$B!&(B($B@5(B)$B@V>>(B $B7{$B!&(B($B@5(B)$B?{86(B $B9'(B$B!&(B($B@5(B)$B5FCO(B $BN4;J(B$B!&(B($B@5(B)$BCfHx(B $B??0l(B | chitosan membrane emulsification microcapsule
| 4-a | 616 |
11:20$B!A(B 11:40 | E108 | $B2M66$5$l$?%W%k%i%s!>%+%i%.!<%J%sJ#9gKl$N=c?eF)2a(B ($BF|Bg1!@8J*;q8;(B) $B!{(B($B3X(B)$B8eF#(B $B@5(B$B!&(B($B@5(B)$BF+(B $B7E(B$B!&(B($B@5(B)$B:#0f(B $B@5D>(B$B!&(B($B@5(B)$BNkLZ(B $B8y(B | membrane pullulan Ultrafiltration
| 4-a | 168 |
11:40$B!A(B 12:00 | E109 | $B?eG.=hM}$r;\$7$?%"%Q%?%$%HMO ($B>.;39b@lJ*$B!&(B($B3X(B)$BEOJU(B $BM&B@(B$B!&(B($B@5(B)$B>eLn(B $B7xEP(B$B!&(B($B@5(B)$B@n1[(B $BBgJe(B$B!&(B($B@5(B)$BIp(B $B@.>M(B | apatite endotoxin
| 4-a | 58 |
12:00$B!A(B 13:00 | $BCk5Y$_(B |
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13:00$B!A(B 13:20 | E113 | $BG.M65/AjJ,N%K!$rMQ$$$?%J%$%m%sCf6u;eB?9&Kl$N3+H/$HFC@-I>2A(B ($B%f%K%A%+(B) $B!{(B($B@5(B)$B>.Ln(B $B5.Gn(B$B!&(B$B@nCf(B $BAo(B$B!&(B$BW"ED(B $B0lM:(B$B!&(B($B?@8MBg1!9)(B) ($B3X(B)Saeid R$B!&(B($B@5(B)$B>>;3(B $B=(?M(B | Nylon Hollow fiber membrane Thermally induced phase separation process
| 4-a | 116 |
13:20$B!A(B 13:40 | E114 | $BG.M65/AjJ,N%K!$rMQ$$$?(BPVDF$B7O%V%l%s%ICf6u;eKl$N:n@=$HKlFC@-I>2A(B ($B?@8MBg1!9)(B) $B!{(B($B3X(B)$BFs8.C+(B $BN<(B$B!&(B($B@5(B)$BBg8~(B $B5H7J(B$B!&(B($B@5(B)$B4];3(B $BC#@8(B$B!&(B($B@5(B)$BA>C+(B $BCN90(B$B!&(B($B@5(B)$B>>;3(B $B=(?M(B | hollow fiber membrane thermally induced phase separation PVDF blend membrane
| 4-a | 565 |
13:40$B!A(B 14:00 | E115 | $B9bG4@-G]M\1U$+$i$N%P%$%*%]%j%^!<$NKlJ,N%(B ($B4X@>Bg9)(B) $B8~0f(B $BJ8=S(B$B!&(B$B;3K\(B $B42;R(B$B!&(B($B4X@>Bg2=@89)(B) $B!{(B($B@5(B)$BLpLZ(B $B=(<#(B | microfiltration PGA alcohol precipitation
| 4-a | 128 |
(14:00$B!A(B15:00)$B!!(B($B:BD9(B $BLpLZ!!=(<#(B) |
14:00$B!A(B 14:20 | E116 | UF+RO$B$K$h$k(BIMS$B%W%m%;%9(B ($BEl%l(B) $B!{A0ED(B $BCR9((B$B!&(B$BKL=P(B $BM-(B$B!&(B($B@5(B)$BJw4_(B $B?J0l(B$B!&(B($B@5(B)$B?"B<(B $BCiW"(B | Integrated Membrane System Membrane fouling Ultra-filtration
| 4-b | 517 |
14:20$B!A(B 14:40 | E117 | $BBQ%U%!%&%j%s%0@-$rM-$9$k%]%jF};@Cf6u;eKl$N3+H/(B ($B?@8MBg1!9)(B) $B!{(B($B3X(B)$B4?M(B$B!&(B($B@5(B)$BBg8~(B $B5H7J(B$B!&(B($B@5(B)$B4];3(B $BC#@8(B$B!&(B($B@5(B)$BA>C+(B $BCN90(B$B!&(B($B@5(B)$B>>;3(B $B=(?M(B | poly lactic acid hollow fiber membrane fouling
| 4-a | 167 |
14:40$B!A(B 15:00 | E118 | $BKl$K$h$k2 ($BEl%l(B) $B!{>.4d(B $B2mOB(B$B!&(B$BJU8+(B $B>;90(B | RO Membrane Anti Fouling Waste Water Reclamation
| 4-a | 138 |
(15:00$B!A(B16:00)$B!!(B($B:BD9(B $B@V>>!!7{ |
15:00$B!A(B 15:20 | E119 | Metal-CMP$BGS?e=hM}$KE,$7$?9bBQ;@2=@-(BPVDF-UF$BKl(B ($B002=@.%1%_%+%k%:(B) $B!{;V4t(B $BCR(B$B!&(B$B8EK\(B $B8^O:(B | membrane polyvinylidenfluoride oxidative resistance
| 4-a | 344 |
15:20$B!A(B 15:40 | E120 | $BKlHy:Y9=B$$NM}O@2r@O$rL\E*$H$7$?M[EE;R>CLGK!%7%_%e%l!<%?$N3+H/(B ($BElKLBg1!9)(B) $B!{(B($B@5(B)$B9b1)(B $BMN=<(B$B!&(B($BElKLBgL$Mh%;(B) $BNkLZ(B $B0&(B$B!&(B($BElKLBg1!9)(B) Riadh Sahnoun$B!&(B($B6eBg0p@9%;(B) ($B@5(B)$B8E;3(B $BDL5W(B$B!&(B($BElKLBg1!9)(B) $BDZ0f(B $B=(9T(B$B!&(B$BH+;3(B $BK>(B$B!&(B($B@5(B)$B1sF#(B $BL@(B$B!&(BDel Carpio Carlos A.$B!&(B($B@5(B)$B5WJ](B $BI4;J(B$B!&(B($BElKLBgL$Mh%;%s%?!<(B/$BElKLBg1!9)(B) ($B@5(B)$B5\K\(B $BL@(B | Pore size distribution Positron annihilation lifetime spectroscopy large-scale quantum chemical calculation
| 4-a | 194 |
15:40$B!A(B 16:00 | E121 | $BCf6u;e7?5U?;F)%b%8%e!<%k$NJ* ($BElMNKB(B) $B!{(B($B@5(B)$B7'Ln(B $B=_IW(B$B!&(B($B@5(B)$B4XLn(B $B@/><(B$B!&(B($B?@8MBg1!9)(B) ($B@5(B)$B>>;3(B $B=(?M(B | membrane separation reverse osmosis hollow fiber
| 4-a | 205 |
(16:00$B!A(B16:40)$B!!(B($B:BD9(B $B9b1)!!MN=<(B) |
16:00$B!A(B 16:20 | E122 | $B?e=hM}MQCf6u;eKl$NKlI=LL9=B$$HKl%U%!%&%j%s%0$NAj4X$K4X$9$k8&5f(B ($B?@8MBg1!9)(B) ($B3X(B)$BJR6M(B $B7r(B$B!&(B$B!{(B($B@5(B)$BBg8~(B $B5H7J(B$B!&(B($B@5(B)$B4];3(B $BC#@8(B$B!&(B($B@5(B)$BA>C+(B $BCN90(B$B!&(B($B@5(B)$B>>;3(B $B=(?M(B | hollow fiber membrane fouling sodium alginate
| 4-a | 398 |
16:20$B!A(B 16:40 | E123 | $B05NOB;<:$r9MN8$7$?KlJ,N%%W%m%;%9$N%7%_%e%l!<%7%g%s(B ($BElMNBg9)(B) $B!{(B($B3X(B)$B2CF#(B $B9b;V(B$B!&(B($B3X(B)$BFAB<(B $B2m90(B$B!&(B($B@5(B)$B@n@%(B $B5A6k(B | Membrane separation simulation pressure drop
| 4-a | 609 |
E$B2q>l(B $BBh(B2$BF|(B |
(9:20$B!A(B10:00)$B!!(B($B:BD9(B $BHf2E(B $B=<(B) |
9:20$B!A(B 9:40 | E202 | Characterization of random and block copolymers of highly sulfonated poly(arylene ether sulfone) for proton exchange membrane ($B?@8MBg1!9)(B) $B!{(B($B3X(B)$BNB(B $B%5%$(B$B!&(B($B@5(B)$BBg8~(B $B5H7J(B$B!&(B($B@5(B)$B4];3(B $BC#@8(B$B!&(B($B@5(B)$BA>C+(B $BCN90(B$B!&(B($B@5(B)$B>>;3(B $B=(?M(B | proton exchange membrane sulfonated poly(arylene ether sulfone) copolymer
| 4-a | 188 |
9:40$B!A(B 10:00 | E203 | $B%P%$%]!<%iKl$rMQ$$$?EE5$F)@OK!$K$h$kGS?eCf$+$i$N%[%&AG=|5n%W%m(B $B%;%9$N3+H/(B ($BElBg?7NN0h(B) $B!{(B($B3X(B)$BD9_7(B $B425,(B$B!&(B($B@5(B)$BHSDM(B $B=_(B$B!&(B$B0f>e(B $BLwM:(B$B!&(B($B@.l~BgM}9)(B) ($B@5(B)$B;3:j(B $B>O90(B$B!&(B($BElBg?7NN0h(B) ($B@5(B)$BLxBt(B $B9,M:(B | Electrodialysis Bipolar membrane Boron removal
| 4-a | 163 |
(10:00$B!A(B11:00)$B!!(B($B:BD9(B $B>>;3!!=(?M(B) |
10:00$B!A(B 10:20 | E204 | $BEE5$F)@O$rMQ$$$?Fs;@2=C:AGJ,N%!&2s<}K!$N2A(B ($BElBg9)(B) $B!{(B($B3X(B)$B66K\(B $B2BF`(B$B!&(B($BElBg?7NN0h(B) ($B3X(B)$BD9_7(B $B425,(B$B!&(B($B@5(B)$BHSDM(B $B=_(B$B!&(B($B@.l~BgM}9)(B) ($B@5(B)$B;3:j(B $B>O90(B$B!&(B($BElBg?7NN0h(B) ($B@5(B)$BLxBt(B $B9,M:(B | electrodialysis CO2 capture bipolar membrane
| 4-a | 571 |
10:20$B!A(B 10:40 | E205 | $B%]%j%^!<%V%l%s%IK!$K$h$j:n@=$7$?(BPVA$B7O1"%$%*%s8r49Kl$K$*$1$k%$%*%sM"AwFC@-(B ($B;38}Bg1!M}9)(B) $B!{(B($B3X(B)$B@>B<(B $B7CH~(B$B!&(B$B@6?e(B $B7CN$;R(B$B!&(B($B@5(B)$BHf2E(B $B=<(B | Ion-exchange membrane permselectivity poly(vinyl alcohol)
| 4-a | 745 |
10:40$B!A(B 11:00 | E206 | $B1"%$%*%s8r49Kl$K$*$1$kM-5!1x@wJ* ($B;38}Bg1!M}9)(B) $B!{(B($B3X(B)$BD9@%(B $B$_$J$_(B$B!&(B($B3X(B)$B@>B<(B $B7CH~(B$B!&(B($B@5(B)$BEDCf(B $B?-9,(B$B!&(B($B@5(B)$BHf2E(B $B=<(B | Anion-exchange membrane Electro dialysis Fouling
| 4-a | 746 |
(11:00$B!A(B12:00)$B!!(B($B:BD9(B $B$O$P$-!!9-82(B) |
11:00$B!A(B 11:20 | E207 | $B@wNAGS?e$N%*%>%s;@2=J,2r$K$*$1$k%,%9N.NL$N1F6A(B ($BElMNBg9)(B) $B!{(B($B3X(B)$B2CF#(B $B9b;V(B$B!&(B$BBgH*(B $BGn5*(B$B!&(B($B3X(B)$BFAB<(B $B2m90(B$B!&(B($B@5(B)$B@n@%(B $B5A6k(B | ozone colored effluent simulation
| 4-d | 598 |
11:20$B!A(B 11:40 | E208 | Thermodynamic Properties of Potassium Serinate for Carbon Dioxide Absorption (Yonsei U.) $B!{(B($B3X(B)Lee J.$B!&(B($B3X(B)Song H. J.$B!&(B($B@5(B)Lee S.$B!&(B($B3X(B)Ahn S.$B!&(B($B@5(B)Park J. W. | potassium serinate carbon dioxide absorption
| 4-d | 642 |
11:40$B!A(B 12:00 | E209 | Characterization of Potassium Serinate for Carbon Dioxide Absorption (Yonsei U.) $B!{(B($B3X(B)Song H. J.$B!&(B($B@5(B)Lee S.$B!&(B($B3X(B)Lee J.$B!&(B($B3X(B)Ahn S.$B!&(B($B@5(B)Park J. W. | potassium serinate carbon dioxide absorption
| 4-d | 647 |
E$B2q>l(B $BBh(B3$BF|(B |
(9:00$B!A(B10:00)$B!!(B($B:BD9(B $B5H2,!!J~5W(B) |
9:00$B!A(B 9:20 | E301 | $B8w?(G^$rMQ$$$??e$N40A4J,2r$K$h$k?eAG@=B$$X$NKlJ,N%$N1~MQ(B ($B;38}Bg9)(B) $B!{HSED(B $B9b;K(B$B!&(B($B;38}Bg1!M}9)(B) ($B@5(B)$BEDCf(B $B0l9((B$B!&(B($B@5(B)$B4nB?(B $B1QIR(B$B!&(B$B | hydrogen production membrane separation photocatalyst
| 4-a | 615 |
9:20$B!A(B 9:40 | E302 | Pd$B<+N)GvKl$N?eAGJ,N%FC@-(B ($B9)3X1!Bg(B) $B!{(B($B3X(B)$B:4F#(B $B>;=S(B$B!&(B($B@5(B)$B2OB<(B $B8wN4(B$B!&(B($B;:Am8&(B) ($B@5(B)$B5W>>(B $B7I;R(B$B!&(B($B@5(B)$B@PDM(B $B$_$5$-(B$B!&(B($B@5(B)$B86(B $B=E$B!&(B($B@5(B)$B?\ED(B $BMN9,(B$B!&(B($B@5(B)$B86C+(B $B8-<#(B | Palladium Membrane Hydrogen
| 4-a | 55 |
9:40$B!A(B 10:00 | E303 | $B=c%Q%i%8%&%`$N?eAGF)2a78?t$N05NO0MB8@-(B ($B;:Am8&(B) $B!{(B($B@5(B)$B86(B $B=E$B!&(B$B@PDM(B $B$_$5$-(B$B!&(B($B@5(B)$B?\ED(B $BMN9,(B$B!&(B($B@5(B)$B8~ED(B $B2m0l(B$B!&(B($B@5(B)$B86C+(B $B8-<#(B | Hydrogen metal membranes palladium
| 4-a | 34 |
(10:00$B!A(B11:00)$B!!(B($B:BD9(B $B?\ED!!MN9,(B) |
10:00$B!A(B 10:20 | E304 | $B:Y9&Fb=2A(B ($BF`NI@hC$B!&(B(RITE) ($B@5(B)$B5\K\(B $B3X(B$B!&(B(RITE,$BF`NI@hC8l(B $B9nB'(B$B!&(B($B@5(B)$BF#2,(B $BM40l(B | membrane hydrogen palladium
| 4-a | 253 |
10:20$B!A(B 10:40 | E305 | V$B7O9g6bKl$K$h$k?eAGJ,N%(B ($BJ*!&:`5!9=(B) $B!{(B($B@5(B)$B@>B<(B $BKS(B$B!&(B$B8EKR(B $B@/M:(B$B!&(B($B@iMU9)Bg(B) $B4d:4(B $B9nI'(B$B!&(B($BB@M[9]9)(B) $B5H1J(B $B1QM:(B | hydrogen permeation vanadium
| 4-a | 747 |
10:40$B!A(B 11:00 | E306 | CO2$BJ,N%B%?JM"AwKl$N3+H/$H%a%s%V%l%s%j%"%/%?!<$X$N1~MQ(B ($B%k%M%C%5%s%9!&%(%J%8!($B@5(B)$B;{K\(B $B@5L@(B$B!&(B$B3k2<(B $B$+$*$j(B$B!&(B($B@5(B)$B?@Hx(B $B1Q<#(B$B!&(B$B2,ED(B $B<#(B$B!&(B($B?@8MBg1!9)(B) ($B3X(B)$B1)@n(B $BOB4u(B$B!&(B($B@5(B)$BA>C+(B $BCN90(B$B!&(B($B@5(B)$B4];3(B $BC#@8(B$B!&(B($B@5(B)$B>>;3(B $B=(?M(B | facilitated transport membrane membrane reactor carbon dioxide
| 4-a | 680 |
(11:00$B!A(B12:00)$B!!(B($B:BD9(B $BEDCf!!0l9((B) |
11:00$B!A(B 11:20 | E307 | Effect of membrane structure on gas separation performance of hollow fiber membrane contactor (Kobe U.) $B!{(B($B3X(B)Rajabzadeh Saeid$B!&(B($B3X(B)Yoshimoto Shin-ya$B!&(B($B@5(B)Ohmukai Yoshikage$B!&(B($B@5(B)Maruyama Tatsuo$B!&(B($B@5(B)Sotani Tomohiro$B!&(B($B@5(B)Teramoto Masa-aki$B!&(B($B@5(B)Matsuyama Hideto | Hollow fiber membrane contactor PVDF membrane membrane structure
| 4-a | 301 |
11:20$B!A(B 11:40 | E308 | ($B9V1iCf;_(B)
|
| 100 | 700 |
11:40$B!A(B 12:00 | E309 | $B9b05>r7o$K$*$1$kB?9&@-%;%i%_%C%/Kl$N(BCO2$BF)2a$*$h$S(BCO2/N2$BJ,N%FC@-(B ($B9-Bg9)(B) $B!{(B($B3X(B)$B;e8}(B $BAo(B$B!&(B($B@5(B)$B5H2,(B $BJ~5W(B$B!&(B($B@5(B)$B6b;X(B $B@58@(B$B!&(B($B@5(B)$BETN1(B $BL-N;(B | inorganic membrane CO2 high pressure
| 4-a | 109 |
12:00$B!A(B 13:00 | $BCk5Y$_(B |
(13:00$B!A(B14:00)$B!!(B($B:BD9(B $BLnB |
13:00$B!A(B 13:20 | E313 | $B%7%j%+Kl$K$h$k%a%?%N!<%k(B/$B%8%a%A%k%+!<%\%M!<%H$N(BPV$BJ,N%$H2A(B ($B9-Bg1!9)(B) $B:4!9LZ(B $BL@;K(B$B!&(B($B@5(B)$B5H2,(B $BJ~5W(B$B!&(B($B@5(B)$B6b;X(B $B@58@(B$B!&(B$B!{(B($B@5(B)$BETN1(B $BL-N;(B | silica membranes pervaporation transient response
| 4-a | 209 |
13:20$B!A(B 13:40 | E314 | $BB?9&@-%7%j%+Kl$K$*$1$k%"%s%b%K%"F)2aFC@-(B ($B9-Bg1!9)(B) $B!{(B($B@5(B)$B6b;X(B $B@58@(B$B!&(B$B;3K\(B $B>O(B$B!&(B($B@5(B)$B5H2,(B $BJ~5W(B$B!&(B($B@5(B)$BETN1(B $BL-N;(B | Silica membrane Ammonia Gas permeation
| 4-a | 293 |
13:40$B!A(B 14:00 | E315 | FAU$B7?%<%*%i%$%HKl$K$h$kM-5!1UBN:.9gJ*$NJ,N%(B ($B;38}Bg1!M}9)(B) $B!{(B($B@5(B)$B4nB?(B $B1QIR(B$B!&(B($B3X(B)$B0f>e(B $BM%;R(B$B!&(B$B>>;3(B $BIROB(B$B!&(B($B@5(B)$B?"B<(B $B0l9-(B$B!&(B($B@5(B)$BEDCf(B $B0l9((B | zeolite membrane pervaporation vaporpermeation
| 4-a | 294 |
(14:00$B!A(B15:00)$B!!(B($B:BD9(B $B0KEl!!>O(B) |
14:00$B!A(B 14:20 | E316 | $B%7%j%k4p$rM-$9$k%]%j%$%_%IKl$N:n@=$H5$BNF)2aA*Br@-(B ($B;38}Bg1!M}9)(B) $B!{;3>e(B $B9LJ?(B$B!&(B($B@5(B)$B?"B<(B $B0l9-(B$B!&(B($B@5(B)$BEDCf(B $B0l9((B$B!&(B($B@5(B)$B4nB?(B $B1QIR(B | gas separation polyimides silyl side groups
| 4-a | 636 |
14:20$B!A(B 14:40 | E317 | $B:Y9&%U%#%j%s%07?(BPDMS/PMHS$BKl$K$h$k?;F)5$2=J,N%(B ($B4X@>Bg9)(B) $B!{(B($B@5(B)$BEDCf(B $B=SJe(B$B!&(B$BjO(B $BD6(B$B!&(B(Hitz$BF|N)B$A%(B) ($B@5(B)$B9SLZ(B $BDgIW(B$B!&(B($B4X@>Bg9)(B) ($B@5(B)$B;0Bp(B $B5AOB(B | pervaporation PDMS/PMHS membranes pore-filling
| 4-a | 336 |
14:40$B!A(B 15:00 | E318 | $B%j%0%N%/%l%>!<%k$rA06nBN$H$9$kC:AGKl$NF)2aJ*@-(B-$BI=LL=hM}$N8z2L(B ($B;38}Bg1!M}9)(B) $B!{(B($B@5(B)$B4nB?(B $B1QIR(B$B!&(B($B3X(B)$BIp5o(B $BM&4u(B$B!&(B$B8E2l(B $BCR;R(B$B!&(B($B@5(B)$B?"B<(B $B0l9-(B$B!&(B($B@5(B)$BEDCf(B $B0l9((B$B!&(B($B:e;T9)8&(B) $B@n=.(B $B8yO/(B$B!&(B($B;0=EBg1!@8J*;q8;(B) ($B@5(B)$BgU2,(B $B@58w(B | lignin carbon membrane surface treatment
| 4-a | 286 |
(15:00$B!A(B16:00)$B!!(B($B:BD9(B $B6b;X!!@58@(B) |
15:00$B!A(B 15:20 | E319 | MFI$B%<%*%i%$%HKl$NN33&=hM}$H$=$NF)2a5!9=$N8!F$(B ($B$B!&(B$B?9(B $BAo;R(B$B!&(B($B@5(B)$BLnB<(B $B4490(B$B!&(B($B;38}Bg9)(B) ($B@5(B)$B4nB?(B $B1QIR(B | zeolite membrane post-treatment permeation mechanism
| 4-a | 258 |
15:20$B!A(B 15:40 | E320 | $B?75,%<%*%i%$%H(BCDS-1(CDO)$BKl$N9g@.$*$h$S%/%i%C%/H/@8860x$N9M;!(B ($BF|Bg9)(B) $B!{(B($B3X(B)$BJ?Ln(B $BD>?M(B$B!&(B$B@>=P(B $BMx0l(B$B!&(B($B;:Am8&(B) ($B@5(B)$BD9@%(B $BB?2C;R(B$B!&(B$BD9C+@n(B $BBY5W(B$B!&(B($B@5(B)$B@6=;(B $B2EF;(B | Zeolite membrane layered silicate Pervaporation
| 4-a | 396 |
15:40$B!A(B 16:00 | E321 | $B1UBNKl$K$h$k%(%?%N!<%k!??e:.9g>x5$$NF)2aJ,N%(B ($B?73cBg9)(B) $B!{(B($B3X(B)$B@>Eg(B $BBgM5(B$B!&(B($B@5(B)$B0KEl(B $B>O(B | liquid mambrane vapor permeation water vapor
| 4-a | 384 |
F$B2q>l(B $BBh(B1$BF|(B |
(9:40$B!A(B11:00)$B!!(B($B:BD9(B $B>.?{!!?M;|(B) |
9:40$B!A(B 10:00 | F103 | $BB?@.J,7O%$%*%s8r49$K$*$1$k%+%i%`$X$NL$:F@8 ($B2#9qBg9)(B) $B!{(B($B3X(B)$B;V2l(B $BM42p(B$B!&(B($B@5(B)$BCfB<(B $B0lJf(B$B!&(B($B@5(B)$B?7ED8+(B $B6)(B$B!&(B($B@5(B)$B>>K\(B $B44<#(B | ionexchange breakthrough curve model
| 4-e | 763 |
10:00$B!A(B 10:20 | F104 | $B9bI=LL@Q%^%0%M%?%$%H$ND4@=$HbgAG=|5nFC@-$NI>2A(B ($B5\:jBg9)(B) $B!{(B($B@5(B)$BBg\F(B $B70(B$B!&(B($B@5(B)$BBgEg(B $BC#Li(B$B!&(B($B@5(B)$BGO>l(B $BM3@.(B | adsorption magnetite arsenic
| 4-e | 65 |
10:20$B!A(B 10:40 | F105 | $BCj=P:^FbJq%^%$%/%m%+%W%;%k$K$h$k(BNi$B!"(BCo$B$NJ,N%(B ($BF1;V$B!&(B($B@5(B)$B>>K\(B $BF;L@(B$B!&(B($B@5(B)$B6aF#(B $BOB@8(B | metal adsorption microcapsule
| 4-e | 69 |
10:40$B!A(B 11:00 | F106 | Ft-ir$B$rMQ$$$?B?9&2A$H%$%*%s5[Ce7ABV$N8!F$(B ($B5~Bg1!9)(B) $B!{(B($B@5(B)$BKR(B $BBYJe(B$B!&(B($B3X(B)$BKY8}(B $B>4B@(B$B!&(B($B@5(B)$BA0(B $B0lW"(B | FeOOH phosphoric ion sulfate ion
| 4-e | 210 |
(11:00$B!A(B12:00)$B!!(B($B:BD9(B $BKR!!BYJe(B) |
11:00$B!A(B 11:20 | F107 | $B%/%(%s;@$r:x2==u:^$H$7$?B?9& ($B | divalent metal porous glass separation
| 4-e | 250 |
11:20$B!A(B 11:40 | F108 | Adsorption of Metal Ions by Composite Chitosan Beads ($BEl9)Bg1!M}9)(B) $B!{(B($B3X(B)Doldina Meruyert$B!&(B($B@5(B)$B>.?{(B $B?M;|(B | Adsorption Chitosann composite Metal ion
| 4-e | 593 |
11:40$B!A(B 12:00 | F109 | $B%^%0%M%?%$%H$*$h$S%^%0%M%?%$%H(B-$B%-%H%5%sHyN3;R$ND4@=$H(BAs($B-7(B)$B$H(BAs($B-9(B)$B$N5[CeJ?9U(B ($B5\:jBg9)(B) $B!{(B($B3X(B)$BF|9b(B $BM&2p(B$B!&(B($B@5(B)$BBg1I(B $B70(B$B!&(B($B@5(B)$BBgEg(B $BC#Li(B$B!&(B($B@5(B)$BGO>l(B $BM3@.(B | arsenic magnetite chitosan
| 4-e | 635 |
12:00$B!A(B 13:00 | $BCk5Y$_(B |
(13:00$B!A(B14:00)$B!!(B($B:BD9(B $B5WJ]ED(B $BIY@8;R(B) |
13:00$B!A(B 13:20 | F113 | $BA+0\6bB0C4;}%-%l!<%H ($B5\:jBg9)(B) $B!{(B($B@5(B)$BBgEg(B $BC#Li(B$B!&(B$BN);3(B $BJfDEH~(B$B!&(B($B@5(B)$BBg1I(B $B70(B$B!&(B($B@5(B)$BGO>l(B $BM3@.(B | Immobilized metal affinity adsorption carnosine
| 4-e | 162 |
13:20$B!A(B 13:40 | F114 | $B%0%i%U%H2=%-%H%5%sM6F3BN$ND4@=$H5.6bB05[CeFC@-$NI>2A(B ($B5\:jBg9)(B) $B!{(B($B3X(B)$B9uLZ(B $BM5B@(B$B!&(B($B%a%k%\%k%sBg(B) Stevens Geoff. W.$B!&(BM. Perera Jilska$B!&(BD. Kolev Spas$B!&(B($B5\:jBg9)(B) ($B@5(B)$BBg1I(B $B70(B$B!&(B($B@5(B)$BBgEg(B $BC#Li(B$B!&(B($B@5(B)$BGO>l(B $BM3@.(B | adsorption chitosan precious metal
| 4-e | 753 |
13:40$B!A(B 14:00 | F115 | 2-$B%"%_%N%a%A%k%T%j%8%s4^?/ ($BET>k9b@l(B) $B!{(B($B3X(B)$BFn(B $BBs(B$B!&(B($B@5(B)$B4d7'(B $BH~F`;R(B$B!&(B($B5\:jBg(B) ($B@5(B)$BGO>l(B $BM3@.(B | impregnated resin palladium
| 4-e | 331 |
(14:00$B!A(B15:00)$B!!(B($B:BD9(B $BBgEg!!C#Li(B) |
14:00$B!A(B 14:20 | F116 | $B??6u%]%s%WL}$K$h$k6b$NMOG^Cj=P(B ($B:42lBgM}9)(B) $B!{(B($B3X(B)$B0$It(B $BL-(B$B!&(B($B@5(B)$B@n4nED(B $B1Q9'(B$B!&(B($B@5(B)$BBgEO(B $B7<2p(B$B!&(B($B@5(B)$B0f>e(B $B>!Mx(B | Vacuum pump oil gold solvent extraction
| 4-e | 325 |
14:20$B!A(B 14:40 | F117 | $B?75,%j%0%K%s%2%k$N3+H/$*$h$S5.6bB0$N2s<}(B ($B:42lBgM}9)(B) $B!{(B($B3X(B)$B>>;^(B $BH~9,(B$B!&(B($B@5(B)$B@n4nED(B $B1Q9'(B$B!&(B($B@5(B)$BBgEO(B $B7<2p(B$B!&(B($B@5(B)$B0f>e(B $B>!Mx(B$B!&(B($B;0=EBg@8J*;q8;(B) ($B@5(B)$BgU2,(B $B@58w(B | wheat lignophenol precious metal
| 4-e | 260 |
14:40$B!A(B 15:00 | F118 | $B%J%H%j%&%`1v7?%_%+%s%8%e!<%9%+%95[Ce:^$N6bB0%$%*%s5[CeFC@-(B ($B:42lBgM}9)(B) $B!{:M86(B $B9'0l(B$B!&(B($B@5(B)$B0f>e(B $B>!Mx(B$B!&(B($B@5(B)$B@n4nED(B $B1Q9'(B$B!&(B($B@5(B)$BBgEO(B $B7<2p(B$B!&(B($B3X(B)$B0f>e(B $B=a0l(B | Adsorption Orange waste Heavy metals
| 4-e | 717 |
(15:00$B!A(B16:00)$B!!(B($B:BD9(B $BBg\F!!70(B) |
15:00$B!A(B 15:20 | F119 | $B%_%+%s%8%e!<%9%+%9$rMQ$$$?6b$N5[Ce!&2s<}(B ($B:42lBgM}9)(B) $B!{(B($B3X(B)$B0$It(B $BL-(B$B!&(B($B@5(B)$B@n4nED(B $B1Q9'(B$B!&(B($B@5(B)$BBgEO(B $B7<2p(B$B!&(B($B@5(B)$B0f>e(B $B>!Mx(B | polyphenol gold adsorption orange juice residue
| 4-e | 328 |
15:20$B!A(B 15:40 | F120 | PEG$B%O%$%I%m%2%k$X$N5.6bB0N`$N5[Ce(B ($BL>Bg9)(B) $B!{(B($B3X(B)$B0KF#(B $B>00o(B$B!&(B($B@5(B)$BFs0f(B $B?8(B$B!&(B($BL>8E20;T9)8&(B) ($B@5(B)$BLZ2<(B $BIpI'(B$B!&(B$B@P3@(B $BM';0(B$B!&(B$BCfLn(B $BK|7I(B$B!&(B$B;38}(B $B9@0l(B$B!&(B$B=)ED(B $B=E?M(B | hydrogel poly(ethylene glycol) precious metal
| 4-e | 461 |
15:40$B!A(B 16:00 | F121 | $B%"%k%+%j=hM}$r;\$7$?@=;f%9%i%C%8>F5Q3%$NFC@-$H$=$N1~MQ(B ($B=)EDBg9);q(B) $B!{(B($B@5(B)$BOBEh(B $BN4>;(B | paper sludge ash alkali activation water purification
| 4-e | 16 |
(16:00$B!A(B16:40)$B!!(B($B:BD9(B $BFs0f!!?8(B) |
16:00$B!A(B 16:20 | F122 | $B%$%*%s8r49IT?%I[%Y%k%H<0J,N%AuCV$K$h$k%j%s;@$HM-5!;@$NO"B3J,N%(B ($B:eI\Bg1!9)(B) $B!{(B($B3X(B)$B1J86(B $B=(98(B$B!&(B($B@5(B)$B5HED(B $B90G7(B$B!&(B($B@5(B)$BCfB<(B $B=(H~(B | separation ion-exchange adsorption
| 4-e | 409 |
16:20$B!A(B 16:40 | F123 | ($B7gHV(B)
|
| 100 | 230 |
F$B2q>l(B $BBh(B2$BF|(B |
(9:20$B!A(B10:20)$B!!(B($B:BD9(B $BDT!!CRLi(B) |
9:20$B!A(B 9:40 | F202 | $B%P%$%*%(%?%N!<%k$NH/9Z1U$+$i$N1UAj5[Ce$K$h$kG;=L!&2s<}(B ($BElBg@88&(B) $B!{(B($B3X(B)$B$B!&(B($B@5(B)$BF#ED(B $BMN?r(B$B!&(B($B@5(B)$BF#0f(B $BN4IW(B$B!&(B($B@5(B)$BGwED(B $B>O5A(B | bioethanol adsorption recovery
| 4-e | 139 |
9:40$B!A(B 10:00 | F203 | $B%P%$%*%(%?%N!<%kCf$NN22+7OIT=cJ*=|5n$rL\E*$H$7$?6bB0C4;}B?9& ($B;:Am8&(B) $B!{(B($B@5(B)$B;3K\(B $BBs;J(B$B!&(B($B@5(B)Chaichanawong Jintawat$B!&(B($B@5(B)$BBg?9(B $BN4IW(B | liquid phase adsorption porous carbon dimethylsulfide
| 4-e | 193 |
10:00$B!A(B 10:20 | F204 | IMAC$BK!$H8B30$m2a$rAH$_9g$o$;$?%R%9%A%8%s4^M-%Z%W%A%IJ,N%K!$N3+H/(B ($B5\:jBg9)(B) $B!{(B($B3X(B)$B6b4](B $B7s;0(B$B!&(B($B@5(B)$BBgEg(B $BC#Li(B$B!&(B($B@5(B)$BBg1I(B $B70(B$B!&(B($B@5(B)$BGO>l(B $BM3@.(B | ultrafiltration carnosine metal affinity
| 4-e | 750 |
(10:20$B!A(B11:20)$B!!(B($B:BD9(B $BM>8l!!9nB'(B) |
10:20$B!A(B 10:40 | F205 | $B5[CeG.$K$h$k29EY>e>:$NM^@)$rL\E*$H$7$?C_G.5!G=$rM-$9$k5[Ce:^$N3+H/(B ($BElBg@88&(B) $B!{(B($B@5(B)$BF#ED(B $BMN?r(B$B!&(B($B@5(B)$BF#0f(B $BN4IW(B$B!&(B($B@5(B)$BGwED(B $B>O5A(B | phase change material carbon dioxide adsorption heat
| 4-e | 365 |
10:40$B!A(B 11:00 | F206 | $BDc29:F@8%G%7%+%s%H%m!<%?$N@EE*$*$h$SF0E*5[CeFC@-8&5f(B ($B@>It5;8&(B) $B!{(B($B@5(B)$B6b(B $B0NNO(B$B!&(B($B@5(B)$B2,Ln(B $B9@;V(B$B!&(B($B@5(B)$B0f>e(B $B9(;V(B$B!&(B($B5[Ce$N8&5f | Desiccant rotor Adsorption Dehumidifier
| 4-e | 724 |
11:00$B!A(B 11:20 | F207 | $B?eAG5$N.Cf$K$*$1$k%H%k%(%s(B+$B%a%A%k%7%/%m%X%-%5%s$N3h@-C:$X$N5[CeFC@-$HG3NAEECS?eAGCyB"G^BN$X$N1~MQ(B ($BF|Bg@8;:9)(B) $B!{(B($B3X(B)$BCfN$(B $BM'B'(B$B!&(B($B@5(B)$BDT(B $BCRLi(B$B!&(B($B@5(B)$BF|=)(B $B=SI'(B$B!&(B($B1'ET5\Bg9)(B) ($B@5(B)$B0KF#(B $BD> | Fuel Cell Hydrogen Adsorption
| 4-e | 70 |
(11:20$B!A(B12:00)$B!!(B($B:BD9(B $B;3K\!!Bs;J(B) |
11:20$B!A(B 11:40 | F208 | $BAjJQ2=J* ($BElBg@88&(B) $B!{(B($B3X(B)$BB<>e(B $BM:B@(B$B!&(B($B@5(B)$BF#ED(B $BMN?r(B$B!&(B($B@5(B)$BF#0f(B $BN4IW(B$B!&(B($B@5(B)$BGwED(B $B>O5A(B | PSA PCM adsorption
| 4-e | 295 |
11:40$B!A(B 12:00 | F209 | $B>J%(%M%k%.!<7?05NO%9%$%s%05[CeK!$K$h$k?75,(BCO2$BJ,N%2s<}5;=Q$N3+H/(B (RITE) $B!{(B($B@5(B)$B5\K\(B $B3X(B$B!&(B($BF`NI@hC$B!&(B(RITE,$BF`NI@hC8l(B $B9nB'(B$B!&(B(RITE) $BF#2,(B $BM40l(B | carbon dioxide capture and separation adsorption
| 4-e | 347 |
F$B2q>l(B $BBh(B3$BF|(B |
(9:00$B!A(B10:00)$B!!(B($B:BD9(B $B2<>r!!98;JO:(B) |
9:00$B!A(B 9:20 | F301 | $B5U%_%;%k$rMQ$$$?0lK\:?3K;@Cj=P$K$*$1$k(BDNA$B3&LL3h@-:^$N1F6A(B ($B?@8MBg1!9)(B) $B!{(B($B3X(B)$B@PDE(B $BD>$B!&(B($B@5(B)$B4];3(B $BC#@8(B$B!&(B($B6eBg1!9)(B) $B:YLZ(B $BBnLi(B$B!&(B($B@5(B)$B8eF#(B $B2m9((B$B!&(B($B?@8MBg1!9)(B) ($B@5(B)$BBg8~(B $B5H7J(B$B!&(B($B@5(B)$B>>;3(B $B=(?M(B | DNA micelle extract
| 4-f | 683 |
9:20$B!A(B 9:40 | F302 | $B%/%i%&%s%(!<%F%k$H$N:x7A@.$rMxMQ$7$??e@-FsAj7O$K$*$1$k%?%s%Q%/ ($B5\:jBg9)(B) $B!{(B($B@5(B)$BBgEg(B $BC#Li(B$B!&(B$BKv$B!&(B($B3X(B)$B9CHe(B $B@i2F(B$B!&(B($B@5(B)$BGO>l(B $BM3@.(B | aqueous two-phase system crown ether protein
| 4-f | 166 |
9:40$B!A(B 10:00 | F303 | W/O/W$B%(%^%k%7%g%sK!$K$h$kL55!Cf6uHyN3;R$ND4@=(B ($BBgJ,Bg9)(B) $B!{(B($B3X(B)$B;05\(B $B?5Li(B$B!&(B($B@5(B)$BT"J,(B $B=$;0(B$B!&(B($B@5(B)$BDL:e(B $B1I0l(B$B!&(B($B@5(B)$BJ?ED(B $B@?(B | microballoon emulsion interfacial reaction
| 4-f | 159 |
(10:00$B!A(B11:00)$B!!(B($B:BD9(B $B>>K\!!F;L@(B) |
10:00$B!A(B 10:20 | F304 | $B%W%m%j%s%"%k%-%kM6F3BN$N9g@.$H%l%"%a%?%kJ,N%!&2s<}$X$N1~MQ(B ($B5\:jBg9)(B) $B!{(B($B3X(B)$B6b4](B $B?5B@O:(B$B!&(B($B@5(B)$BBgEg(B $BC#Li(B$B!&(B($B@5(B)$BGO>l(B $BM3@.(B | rare metal separation extraction
| 4-f | 627 |
10:20$B!A(B 10:40 | F305 | $B8~N.@\?(%9%W%l! ($BEl9)BgM}9)(B) $B!{(B($B3X(B)$BA}ED(B $BIRLi(B$B!&(B($B@5(B)$B$O$P$-(B $B9-82(B$B!&(B($B@5(B)$B9>F,(B $BN50l(B | spray column coal tar absorption oil extraction rate
| 4-f | 450 |
10:40$B!A(B 11:00 | F306 | $B%$%*%s1UBN;Y;}1UKl$K$*$1$k%3!<%k%?!<%k5[<}L}$NF)2a(B ($BEl9)BgM}9)(B) $B!{(B($B3X(B)$BEgED(B $B5AG7(B$B!&(B($B@5(B)$B$O$P$-(B $B9-82(B$B!&(B($B@5(B)$B9>F,(B $BN50l(B | ionic liquid supported liquid membrane coal tar absorption oil
| 4-f | 446 |
(11:00$B!A(B12:00)$B!!(B($B:BD9(B $B9>F,!!N50l(B) |
11:00$B!A(B 11:20 | F307 | $B%8%"%_%I7OG[0L;R$rMQ$$$?%$%*%s1UBNCj=P7O$N9=C[(B ($B86;RNO5!9=(B) $B!{(B($B@5(B)$B2<>r(B $B98;JO:(B$B!&(B$BAR66(B $B7r2p(B$B!&(B($B@5(B)$BD9Fl(B $B90?F(B$B!&(B($B6eBg1!9)(B) ($B@5(B)$B5WJ]ED(B $BIY@8;R(B$B!&(B($B@5(B)$B8eF#(B $B2m9((B | ionic liquids solvent extraction separation
| 4-f | 119 |
11:20$B!A(B 11:40 | F308 | $B%+%k%\%s;@7O?75,Cj=P:^$K$h$k4uEZN`6bB0$N%$%*%s1UBNCj=P(B ($B6eBg1!9)(B) $B!{(B($B@5(B)$B5WJ]ED(B $BIY@8;R(B$B!&(B($B3X(B)$B>.Lx(B $BM52p(B$B!&(B($B86;RNO5!9=(B) ($B@5(B)$B2<>r(B $B98;JO:(B$B!&(B($B6eBg1!9)(B) ($B@5(B)$BCfEg(B $B0l5*(B$B!&(B($B@5(B)$B?@C+(B $BE5Jf(B$B!&(B($B@5(B)$B8eF#(B $B2m9((B | ionic liquids rare earth extraction
| 4-f | 443 |
11:40$B!A(B 12:00 | F309 | $BF};@J,N%$X$N%$%*%s1UBN4^?;Cf6u;eKl$N1~MQ(B ($BF1;V$B!&(B($B@5(B)$B>>K\(B $BF;L@(B$B!&(B($B@5(B)$B6aF#(B $BOB@8(B$B!&(B($BK-EDCf8&(B) ($B@5(B)$BEhB<(B $BN4(B$B!&(B($B@5(B)$BDT(B $B@5CK(B | Liquid membrane Lactic acid Hollow fiber
| 4-f | 178 |
12:00$B!A(B 13:00 | $BCk5Y$_(B |
(13:00$B!A(B14:00)$B!!(B($B:BD9(B $B>>ED!!7=8g(B) |
13:00$B!A(B 13:20 | F313 | $B%P%$%*%(%?%N!<%kG;=L%W%m%;%9$N(BHIDiC$B2=$N8!F$(B ($B4X@>2=3X(B) $B!{(B($B@5(B)$BJR2,(B $BK.IW(B$B!&(B($B@5(B)$BLnED(B $B=(IW(B$B!&(B($B@5(B)$B;3O)(B $B42;J(B$B!&(B($B@5(B)$BARC+(B $B?-9T(B$B!&(B($B@5(B)$B6bED(B $BK|J?(B$B!&(B($B@5(B)$B8~ED(B $BCi90(B | Energy-saving Distillation Bioethanol Production HIDiC
| 4-c | 17 |
13:20$B!A(B 13:40 | F314 | $BH/9Z1UM3Mh(BL-$BF};@$N%(%9%F%k2=!"2C?eJ,2r$K$h$k@:@=(B ($BElG@9)Bg9)(B) $B!{(B($B@5(B)$BK\B?(B $BB@$B!&(B($B@5(B)$B9q4c(B $B9'M:(B$B!&(B$B2CF#(B $BBYM5(B | lactic acid reactive distillation fermentation broth
| 4-c | 755 |
13:40$B!A(B 14:00 | F315 | Application of a Fully Thermally Coupled Distillation Column for Practical Azeotropic Separation (Dong-A U.) Sung Ick Gi$B!&(B$B!{(B($B@5(B)Kim Young Han | Energy-Efficient Distillation Thermally Coupled Distillation Azeotropic Distillation
| 4-c | 26 |
(14:00$B!A(B15:00)$B!!(B($B:BD9(B $B;3K\!!=( |
14:00$B!A(B 14:20 | F316 | $B%J%,%*%+!!%Q%C%-%s%0!V%9!<%Q!<(BH$B%Q%C%/!W(B2$BG\$N=hM}NL$rC#@.$9$k5,B'= ($B>xN1MQ5,B'= | Linear Flow High Liquid Hold High Operating Capacity
| 4-c | 39 |
14:20$B!A(B 14:40 | F317 | $BC1>xN1 ($BF|BgM}9)(B) $B!{(B($B3X(B)$BK\66(B $B8-E5(B$B!&(B($B%*%a%,%7%_%e%l!<%7%g%s(B) ($B@5(B)$B2#;3(B $B9n8J(B$B!&(B($BF|BgM}9)(B) ($B@5(B)$B>>ED(B $B909,(B$B!&(B($B@5(B)$B7*86(B $B@6J8(B$B!&(B($B@5(B)$BFJLZ(B $B>!8J(B | Simple Distillation Estimation of Components Change of Temperature
| 4-c | 217 |
14:40$B!A(B 15:00 | F318 | TAME$B9g@.H?1~>xN1%W%m%;%9$NHsDj>o%7%_%e%l!<%7%g%s(B ($B;37ABg1!M}9)(B) $B!{(B($B3X(B)$B0f9x(B $BC#O:(B$B!&(B($B@5(B)$B>>ED(B $B7=8g(B$B!&(B($B;:Am8&(B) ($B@5(B)$BCf4d(B $B>!(B$B!&(B($B@5(B)$BBg?9(B $BN4IW(B | reactive distillation dynamic simulation TAME
| 4-c | 324 |
(15:00$B!A(B16:00)$B!!(B($B:BD9(B $BFJLZ!!>!8J(B) |
15:00$B!A(B 15:20 | F319 | $B= ($BElM}BgM}(B) $B!{(B($B@5(B)$BBg9>(B $B=$B$(B | flooding packed column distillation
| 4-c | 613 |
15:20$B!A(B 15:40 | F320 | $B= ($BLZB<2=9)5!(B) $B!{@>ED(B $B<~9T(B$B!&(B($B@5(B)$BCf@>(B $B=S@.(B$B!&(B$BB-N)(B $B>0fb(B$B!&(B($B;:Am8&(B) ($B@5(B)$BCf4d(B $B>!(B | HIDiC Distillation proccess design
| 4-c | 761 |
15:40$B!A(B 16:00 | F321 | $B5$1UJ?9U$K5Z$\$91v8z2L$rMxMQ$7$?:.9gGQ;@$+$i$N;@$N>xN1J,N%(B ($B4X@>Bg4D6-ET;T9)(B) ($B@5(B)$B;3K\(B $B=($B!&(B$B!{(B($B3X(B)$BIMED(B $BM5;0(B$B!&(B($B3X(B)$BJ?Ln(B $B@5?M(B$B!&(B$BD.Ln(B $B>-9((B$B!&(B($B?9ED2=3X9)6H(B) $BI4ED(B $BK.t!(B | waste acid distillation recycle
| 4-j | 597 |
G$B2q>l(B $BBh(B3$BF|(B |
(9:00$B!A(B10:00)$B!!(B($B:BD9(B $B4dED!!@/;J(B) |
9:00$B!A(B 9:20 | G301 | $B?6F07?%U%#%k%?!<$K$h$k(BPMMA$BN3;R$r4^$`%i!<%I(B/$B%j%s;@4K>W1U7O%(%^%k%7%g%s$N%/%m%9%U%m!<@:L)_I2aFC@-(B ($B;38}Bg1!M}9)(B) $B!{(B($B@5(B)$BCfAR(B $B1QM:(B$B!&(B($B3X(B)$B1JED(B $B9(;V(B$B!&(B($B;38}Bg1!0e3X(B) $B;{0f(B $B?rFs(B$B!&(B$B:d0fED(B $B8y(B | vibratory filtration crossflow microfiltration o/w emulsion
| 4-b | 97 |
9:20$B!A(B 9:40 | G302 | $BKlLL79 ($BL>Bg9)(B) $B!{(B($B3X(B)$BCfLn(B $BBg(B$B!&(B($B@5(B)$BJR6M(B $B@?G7(B$B!&(B($B@5(B)$BF~C+(B $B1Q;J(B | inclined ultrafiltration filter cake nanocolloid
| 4-b | 537 |
9:40$B!A(B 10:00 | G303 | $BF&Ie%2%k$NB?CJ%/%j!<%W05L)C&?eFC@-$K5Z$\$9E:2C6E8G:^$N1F6A(B ($BL>Bg1!9)(B) $B!{(B($B@5(B)$BJR6M(B $B@?G7(B$B!&(B($B3X(B)$B:4F#(B $B?r(B$B!&(B($B@5(B)$BF~C+(B $B1Q;J(B | consolidation dehydration creep effect
| 4-b | 312 |
(10:00$B!A(B11:00)$B!!(B($B:BD9(B $B@n:j!!7rFs(B) |
10:00$B!A(B 10:20 | G304 | $B%7%s%0%kDj05_I2a;n83$K$h$k_I2aFC@-$N05NO0MB8@-$N7hDj(B ($BL>Bg1!9)(B) $B!{(B($B@5(B)$BJR6M(B $B@?G7(B$B!&(B($B@5(B)$BF~C+(B $B1Q;J(B | filtration cake characteristics membrane resistance
| 4-b | 314 |
10:20$B!A(B 10:40 | G305 | $B%"%/%j%k7ON3;R7|By1U$NDj05@:L)_I2aFC@-(B ($B;38}Bg1!M}9)(B) $B!{(B($B3X(B)$B>eLn(B $B8wB@O:(B$B!&(B($B@5(B)$BCfAR(B $B1QM:(B | Microfiltration Acrylic particle Gel particle
| 4-b | 351 |
10:40$B!A(B 11:00 | G306 | $B%5%V%_%/%m%sN3;R= ($BL>Bg9)(B) $B!{(B($B3X(B)$BIp;T(B $B8-<#(B$B!&(B($B@5(B)$B8~0f(B $B9/?M(B$B!&(B($B@5(B)$BF~C+(B $B1Q;J(B | membrane filtration submicron particle protein
| 4-b | 653 |
(11:00$B!A(B12:00)$B!!(B($B:BD9(B $BB-N)!!BY5W(B) |
11:00$B!A(B 11:20 | G307 | $B%3%m%$%IJq3gK!$rMQ$$$?7|By1U$N@6@!2==hM}(B ($BNk9b@l(B) $B!{(B($B@5(B)$B4dED(B $B@/;J(B$B!&(B$B9>8}(B $BF`=o(B$B!&(B$B0KF#(B $BJb0T(B | colloid gel expression
| 4-b | 515 |
11:20$B!A(B 11:40 | G308 | $B9bHf=E:`$r4^M-$9$kJ4Kv6E=8:^$N=|By8z2L(B ($BNk9b@l(B) $B!{(B($B3X(B)$BCf@n(B $BCR5.(B$B!&(B($B@5(B)$B4dED(B $B@/;J(B | inorganic flocculant polymer flocculant clarification
| 4-b | 488 |
11:40$B!A(B 12:00 | G309 | $BGx5$NL$K$h$k3h@-1xE%%U%m%C%/7A>u$NJQ2=(B ($B0&I2Bg1!M}9)(B) $B!{(B($B@5(B)$B@n:j(B $B7rFs(B$B!&(B$B8M2l@%(B $BN50l(B$B!&(B$B@P0f(B $B>=;R(B$B!&(B$B;3Cf(B $BKcH~;R(B$B!&(B($B@5(B)$B>>ED(B $B98(B | activated sludge floc configuration aeration rate
| 4-b | 433 |
12:00$B!A(B 13:00 | $BCk5Y$_(B |
(13:00$B!A(B14:00)$B!!(B($B:BD9(B $BCfAR!!1QM:(B) |
13:00$B!A(B 13:20 | G313 | $BHyN3;R4^M-1U$r@EEEJ.L8$7$?$H$-$N1UE)@8@.FC@-(B ($B@EBg9)(B) $B!{(BSawada Tsuyoshi$B!&(B($B3X(B)Takeuchi Masaki$B!&(B($B@5(B)Tatemoto Yuuji$B!&(B($B%*!<%`EE5!(B) ($B@5(B)Okazaki Tadao | electrospray slurry particle separation
| 4-j | 296 |
13:20$B!A(B 13:40 | G314 | $BEE5$1KF0K!$K$h$k(BZnO$BHyN3;R$NJ,5i$K$D$$$F(B ($B4X@>Bg4DET9)(B) $B!{GO^<(B $BN<(B$B!&(B$B;32<(B $BBgJe(B$B!&(B($B@5(B)$BB<;3(B $B7{90(B$B!&(B($B@5(B)$B | Fine particles ZnO Mobility
| 4-i | 374 |
13:40$B!A(B 14:00 | G315 | $BD>@\4Q;!$K4p$E$/4KB.%V%i%&%s6E=8$K$*$1$k%U%m%C%/$N9=B$7A@.$H6E=8B.EY(B ($BC^GHBg1!@84D(B) $B!{(B($B3X(B)$B?<_7(B $BCRE5(B$B!&(B($B@5(B)$BB-N)(B $BBY5W(B | RLA Floc structure Rate of coagulation
| 4-b | 621 |
(14:00$B!A(B15:20)$B!!(B($B:BD9(B $B8~0f!!9/?M(B) |
14:00$B!A(B 14:20 | G316 | $B%U%m%C%/$ND@9_$HEE5$1KF0(B ($BC^GHBg1!@84D(B) $B!{(B($B@5(B)$BB-N)(B $BBY5W(B$B!&(B($BC^GHBg1!@84T(B) ($B3X(B)$BFbED(B $BM&B@(B | Electrophoresis Sedimentation Floc
| 4-b | 651 |
14:20$B!A(B 14:40 | G317 | $B3&LLD@9_$rB%?J$9$kN.O)7A@.$K$*$h$\$9D62;GH>H ($BG@9)8&(B) $B!{(B($B@5(B)$BBg0f(B $B@aCK(B$B!&(B($B0q>kBgG@(B) ($B@5(B)$BCf@P(B $B9nLi(B$B!&(B($BG@9)8&(B) ($B@5(B)$BC.20(B $B7$B!&(B($B0q>kBgG@(B) ($B@5(B)$BLpLn(B $B9nK!(B | sedimentation channeling ultra-sonic radiation
| 4-b | 722 |
14:40$B!A(B 15:00 | G318 | $B%a%A%k%;%k%m!<%9?eMO1U$N%2%k>uL$MO2r9bJ,;R=|5n$K$*$1$k%U%#%k%?! ($BF|K\%]!<%k(B) $B!{(B($B@5(B)$B3Q20(B $B@5?M(B$B!&(B($B@5(B)$B>B8}(B $BE0(B | Filtration Gel Standard-Blocking
| 4-b | 24 |
15:00$B!A(B 15:20 | G319 | $BIT?%I[%U%#%k%?!<$N$m2aFC@-$H%U%#%k%?!<9=B$$N4X78(B ($B2#9qBg9)(B) $B!{(B($B3X(B)$B0l%N@%(B $B8<9,(B$B!&(B($B%d%^%7%s%U%#%k%?(B) ($B@5(B)$BHx2<(B $BN5Bg(B$B!&(B($B2#9qBg9)(B) ($B@5(B)$B?7ED8+(B $B6)(B$B!&(B($B@5(B)$BCfB<(B $B0lJf(B$B!&(B($B@5(B)$B>>K\(B $B44<#(B | non woven fibrous filter filtration particles suspension
| 4-b | 764 |
(15:20$B!A(B16:00)$B!!(B($B:BD9(B $BCfB |
15:20$B!A(B 15:40 | G320 | $B%"%k%.%s;@%+%k%7%&%`<+N)Kl$ND4@=$HJ,;RJ,2h@-G=$NI>2A(B ($BF|Bg1!@8J*;q8;(B) $B!{(B($B3X(B)$B2CEg(B $B7IB@(B$B!&(B($B@5(B)$BF+(B $B7E(B$B!&(B($B@5(B)$B:#0f(B $B@5D>(B$B!&(B($B@5(B)$BNkLZ(B $B8y(B | alginate membrane separation
| 4-a | 189 |
15:40$B!A(B 16:00 | G321 | $B%$%L%j%s?eMO1U$N9bG;EYNN0h$K$_$i$l$kFC0[E*N.F0J*@-(B ($BF|Bg1!@8J*;q8;(B) $B!{(B($B3X(B)$B@DLZ(B $BB@M4(B$B!&(B($B@5(B)$BF+(B $B7E(B$B!&(B($B@5(B)$B:#0f(B $B@5D>(B$B!&(B($B@5(B)$BNkLZ(B $B8y(B | inulin viscosity slurry
| 7-h | 224 |