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9:20$B!A(B 11:20 | ZAA301 | $B;I7c1~Ez@-%9%i%j!<$rMQ$$$?:FMxMQ2DG=$J%I%m!
($BK!@/Bg(B) ($B3X(B·$B5;4p(B)$B!{KLB<(B $B8&B@(B$B!&(B ($B@5(B)$B?9(B $BN4>;(B | desalination forward osmosis Stimuli-responsive polymer
| 4-a | 379 |
9:20$B!A(B 11:20 | ZAA302 | $B%7%j%+%i%$%H$H%"%k%_%J$NJ#AX$rCf4VAX$H$7$FF3F~$7$?B?9&
($BFAEgBg1!@hC<650iIt(B) ($B3X(B)$B!{|bC+(B $B??90(B$B!&(B ($B3X(B)$BE7??(B $B=_;V(B$B!&(B ($BFAEgBg1!(BSTS$B8&(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 $BLP(B | Palladium thin membrane Porous SUS tube support Double intermediate layers
| 4-a | 150 |
9:20$B!A(B 11:20 | ZAA303 | Clear solution$B$+$i9g@.$7$?%<%*%i%$%HKl$NF)2aJ,N%@-G=$KM?$($k=$N1F6A(B
($B;38}Bg9)(B) ($B3X(B)$B!{:41RED(B $BBsLi(B$B!&(B ($B;38}Bg1!M}9)(B) ($B3X(B)$B66K\(B $B9/;J(B$B!&(B ($B@5(B)$B7'@Z(B $B@t(B$B!&(B ($B@5(B)$BEDCf(B $B0l9((B$B!&(B ($B@5(B)$B4nB?(B $B1QIR(B | zeolite membrane pervaporation
| 4-a | 277 |
9:20$B!A(B 11:20 | ZAA304 | $B0[$J$k:Y9&7B$N;Y;}BN$K9g@.$7$?(BMFI$B7?%<%*%i%$%HKl$N9=B$$HF)2aJ*@-(B
($B;38}Bg1!M}9)(B) ($B3X(B)$B!{;32<(B $BM5B@(B$B!&(B ($B@5(B)$B7'@Z(B $B@t(B$B!&(B ($B@5(B)$BEDCf(B $B0l9((B$B!&(B ($B@5(B)$B4nB?(B $B1QIR(B | Zeolite membrane gas separation
| 4-a | 259 |
9:20$B!A(B 11:20 | ZAA305 | FAU$B7?%<%*%i%$%H$NC&?e@-G=8~>e$N8!F$(B
($BAaBg@h?JM}9)(B/$BAaBgM}9)Am8&(B/JST-CREST) ($B@5(B)$B>>J}(B $B@5I'!&(B ($BAaBg@h?JM}9)(B) ($B@5(B)$B@%2<(B $B2mGn(B$B!&(B ($B3X(B)$B!{LnB<(B $BN6%N2p(B | FAU-type zeolite Membrane Dehydration
| 4-a | 377 |
9:20$B!A(B 11:20 | ZAA306 | $B05NO>l$G$N(BCO2$BJ,N%$r;X8~$7$?DcG4@-H?1~@-%$%*%s1UBN4^M-%2%kKl$NAO@=(B
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| 4-a | 454 |
9:20$B!A(B 11:20 | ZAA307 | $BHyN3;RJ,;61U$N%/%m%9%U%m!<$m2a$K4X$9$k?tCM2r@O(B
($B?@8MBg1!9)(B/$B@hCC+(B $BkNB@(B$B!&(B ($B@5(B)$B;0Ln(B $BBY;V(B$B!&(B ($BJ!2,Bg9)(B) ($B@5(B)$B?78M(B $B9@9,(B$B!&(B ($B?@8MBg1!9)(B/$B@hC>;3(B $B=(?M(B | lattice Boltzmann method microfiltration cross-flow
| 4-a | 724 |
9:20$B!A(B 11:20 | ZAA308 | $B%<%*%i%$%HKl$NC&?e@-G=$K$*$1$kA`:n>r7o$N1F6A(B
($B%5%i%4%5Bg(B) ($B3$(B)$B!{(BTovar Miriam$B!&(B ($B;38}Bg9)(B) ($B3X(B)$B:41RED(B $BBsLi(B$B!&(B ($B3X(B)$B3aB<(B $B7D90(B$B!&(B ($B;38}Bg1!M}9)(B) ($B@5(B)$B7'@Z(B $B@t(B$B!&(B ($B@5(B)$BEDCf(B $B0l9((B$B!&(B ($B@5(B)$B4nB?(B $B1QIR(B | Zeolite membranes Pervaporation Dehydration
| 4-a | 287 |
9:20$B!A(B 11:20 | ZAA309 | $B%<%*%i%$%H4^M-(BMixed Matrix Membrane$B$NF)2aJ*@-(B
($B;38}Bg1!M}9)(B) ($B3X(B)$B!{8b(B 婷$B!&(B ($B3X(B)$BA}ED(B $BCNLi(B$B!&(B $BAjED(B $B>M0l(B$B!&(B ($B@5(B)$B7'@Z(B $B@t(B$B!&(B ($B@5(B)$BEDCf(B $B0l9((B$B!&(B ($B@5(B)$B4nB?(B $B1QIR(B | Mixed Matrix Membrane Gas permeation Zeolite
| 4-a | 499 |
9:20$B!A(B 11:20 | ZAA310 | $B>xN1BeBXKlC5:w$rL\E*$H$7$?C:2=?eAGJ,N%Kl$NF)2a%7%_%e%l!<%7%g%s(B
($B9)3X1!Bg9)(B) ($B3X(B)$B!{9bEh(B $BM44p(B$B!&(B ($B@5(B)$B9b1)(B $BMN=<(B | polyimide membranes 1,3-butaziene Frist principles molecular dynamics
| 4-a | 601 |
9:20$B!A(B 11:20 | ZAA311 | $BD62;GHJ.L8>F7kK!$K$h$k%;%i%_%C%/(B-$B6bB0J#9g9=B$$r$b$DJ,N%Kl$N%,%9F)2aFC@-(B
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| 4-a | 829 |
9:20$B!A(B 11:20 | ZAA312 | $B%/%j!<%WJQ7A$r9MN8$7$?$Y$->hB'N.BN(B-$B8GBN7O:.9gJ*$NDj0505:q2aDx$N2r@O(B
($B:eI\Bg1!9)(B) ($B3X(B)$B!{2<(B $BN4G7(B$B!&(B ($B@5(B)$BEDCf(B $B9'FA(B$B!&(B ($B@5(B)$B4dED(B $B@/;J(B | non-Newtonian fluids expression analytical solution
| 4-b | 47 |
9:20$B!A(B 11:20 | ZAA313 | $B?75,6bB0:xBN7O%$%*%s1UBN$NAO@=$H$=$N%,%95[<}@-$K4X$9$k4pACE*8!F$(B
($B?@8MBg9)(B) ($B3X(B)$B!{>>2,(B $B=_(B$B!&(B ($B?@8MBg1!9)(B/$B@hC$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B | ionic liquid gas absorption metal complex
| 4-a | 733 |
9:20$B!A(B 11:20 | ZAA314 | $B?;F)05H/EE$r;X8~$7$?0[$J$kCf6u;eKl%b%8%e!<%k$rMQ$$$?F)?e$N2r@O(B
($B?@8MBg1!9)(B/$B@hC$B!&(B ($B@5(B)$B0B@n(B $B@/9((B$B!&(B ($BElMNKB(B) $B9gED(B $B>;J?(B$B!&(B ($B?@8MBg1!9)(B/$B@hC$B!&(B ($B3X(B)$B;0Eh(B $BfF;J(B$B!&(B ($B@5(B)$B9b66(B $BCR51(B$B!&(B ($B@5(B)$BHf2E(B $B=<(B$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B | Osmotic power generation Hollow fiber module Pressure retarded osmosis
| 4-a | 506 |
9:20$B!A(B 11:20 | ZAA315 | $B%7%/%m%G%-%9%H%j%s4^M-(BMixed Matrix Membrane$B$NF)2aJ*@-(B
($B;38}Bg1!M}9)(B) ($B3X(B)$B!{A}ED(B $BCNLi(B$B!&(B ($B3X(B)$B8b(B 婷$B!&(B ($B;38}Bg9)(B) $BAjED(B $B>M0l(B$B!&(B ($B1'It9b@l(B) $B;3yu(B $BGn?M(B$B!&(B ($B;38}Bg1!M}9)(B) ($B@5(B)$B7'@Z(B $B@t(B$B!&(B ($B@5(B)$BEDCf(B $B0l9((B$B!&(B ($B@5(B)$B4nB?(B $B1QIR(B | Cyclodextrin Mixed Matrix Membrane Gas separation
| 4-a | 517 |
9:20$B!A(B 11:20 | ZAA316 | $BD62;GH>H
($B0&I2Bg1!M}9)(B) ($B3X(B)$B!{Fa?\(B $BM&BA(B$B!&(B ($B@5(B)$B@n:j(B $B7rFs(B$B!&(B ($B;38}Bg1!M}9)(B) ($B@5(B)$BCfAR(B $B1QM:(B | Ultrasonic irradiation Freeze concentration characteristics Dissolved oxygen concentration
| 4-b | 514 |
9:20$B!A(B 11:20 | ZAA317 | $BDjNL_I;f$rMQ$$$?4uGv%3%m%$%I7|By1U$NDjB._I2a5sF0(B
($B:eI\Bg1!9)(B) ($B3X(B)$B!{??It(B $BAT@8(B$B!&(B ($B:eI\Bg9)(B) $B1v8+(B $B??J?(B$B!&(B ($B:eI\Bg1!9)(B) ($B@5(B)$BEDCf(B $B9'FA(B$B!&(B ($B@5(B)$B4dED(B $B@/;J(B | Internal filtration Quantitative filter paper Constant-rate filtration
| 4-b | 735 |
9:20$B!A(B 11:20 | ZAA318 | $B%K%C%1%kGS?e$NCfOB=hM}$K5Z$\$9
($B0&I2Bg1!M}9)(B) ($B3X(B)$B!{;3K\(B $BN5Li(B$B!&(B ($B@5(B)$B@n:j(B $B7rFs(B | Nickel Ion Concentration Neutralization Treatment Solid Liquid Separation Characteristic
| 4-b | 282 |
9:20$B!A(B 11:20 | ZAA319 | $BD>N.EE>l$rMxMQ$7$?N3;R6E=85;=Q$N3+H/!AN3;R$N
($BK!@/Bg1!M}9)(B) ($B3X(B)$B!{9>NI(B $BM&N<(B$B!&(B ($BK!@/Bg@8L?(B) ($B3X(B)$B1JEg(B $B906F(B$B!&(B ($B@5(B)$B?9(B $BN4>;(B | D.C. electric field slurry floccuration
| 4-b | 731 |
9:20$B!A(B 11:20 | ZAA320 | $BC:;@%+%k%7%&%`N3;R$+$i%$%*%s2rN%$7$?%+%k%7%&%`%$%*%s$r1~MQ$7$?%U%_%s;@MO1U$N%;%i%_%C%/%9Kl_I2a(B
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| 4-b | 694 |
9:20$B!A(B 11:20 | ZAA321 | $B@5?;F)6nF0MO1U$r;X8~$7$?Fs;@2=C:AG1~Ez@-AjE>0\:`NA$K4X$9$k4pACE*8&5f(B
($B?@8MBg9)(B/$B@hC?9(B $B1vJfH~(B$B!&(B ($B?@8MBg1!9)(B/$B@hC$B!&(B ($B@5(B)$B9b66(B $BCR51(B$B!&(B ($B%@%$%;%k(B) ($BK!(B)$BIMED(B $BK-;0(B$B!&(B ($B?@8MBg1!9)(B/$B@hC>;3(B $B=(?M(B | forward osmosis draw solute carbon dioxide
| 4-a | 804 |
9:20$B!A(B 11:20 | ZAA322 | $BEE5$NO$rMxMQ$7$?8G1UJ,N%$N?d?JNO$K4X$9$k4pACE*8&5f(B
($B:eI\Bg1!9)(B) ($B3X(B)$B!{0KF#(B $B8-0l(B$B!&(B ($B:eI\Bg9)(B) $BDj0f(B $B@2F`(B$B!&(B ($B:eI\Bg1!9)(B) ($B@5(B)$BEDCf(B $B9'FA(B$B!&(B ($B@5(B)$B4dED(B $B@/;J(B | solid-liquid separation electroforced sedimentation electroosmotic dewatering
| 4-b | 736 |
9:20$B!A(B 11:20 | ZAA323 | PMMA$B%3%m%$%IJ,;67O$KJ,3dE:2C$7$?%+%A%*%s@-9bJ,;R6E=8:^$N5[Ce5sF0(B
($B:eI\Bg1!9)(B) ($B3X(B)$B!{5\Eg(B $B>"(B$B!&(B ($B:eI\Bg9)(B) $BF#86(B $BNg;R(B$B!&(B ($B:eI\Bg1!9)(B) ($B@5(B)$BEDCf(B $B9'FA(B$B!&(B ($B@5(B)$B4dED(B $B@/;J(B | Flocculation Adsorption Polyelectrolyte
| 4-b | 821 |
9:20$B!A(B 11:20 | ZAA324 | $BC:;@%+%k%7%&%`N3;R$r1~MQ$7$?%U%_%s;@MO1U$N%/%m%9%U%m!<%;%i%_%C%/%9Kl_I2aFC@-(B
($B;38}Bg1!M}9)(B) ($B3X(B)$B!{;~G$(B $BC#O/(B$B!&(B ($B;38}Bg9)(B) ($B5;4p(B)$BEOJU(B $BCRN<(B$B!&(B $BLx(B $BN;2p(B$B!&(B ($B;38}Bg1!M}9)(B) ($B@5(B)$BCfAR(B $B1QM:(B | humic acid crssflow filtration calcium ion
| 4-b | 709 |
9:20$B!A(B 11:20 | ZAA325 | $BM6EE1KF0$K$h$kN.DL<0HyN3;RJ,N%AuCV$N3+H/(B
($B5~Bg1!9)(B) ($B3X(B·$B5;4p(B)$B!{D[Fb(B $B7r2p(B$B!&(B ($B@5(B)$B:4Ln(B $B5*>4(B$B!&(B ($B@5(B)$BEDLg(B $BH%(B | particle separation dielectrophoresis silica particle
| 4-b | 665 |
9:20$B!A(B 11:20 | ZAA326 | $B%,%i%9A!0]%U%#%k%?!<<0%,%95[<}AuCVFb$N=hM}%,%9$H5[<}1U$NBZN1;~4V$,(BNOx$B5[<}8zN($K$*$h$\$91F6A(B
($B:eI\Bg9)(B) ($B3X(B)$B!{Bg0B(B $B98(B$B!&(B ($B8x32KI;_5!4o8&(B) $B@uLn(B $B=(><(B$B!&(B ($BB?EDEE5!(B) $B;3Fb(B $B;MO:(B$B!&(B ($B:eI\Bg9)(B) ($B@5(B)$B0BED(B $B>;90(B$B!&(B ($B@5(B)$B2.Ln(B $BGn9/(B | Residence time distribution of aqueous and gas phases NOx absorption equipment NOx removing efficiency
| 4-d | 320 |
9:20$B!A(B 11:20 | ZAA327 | $B%/%m%9%U%m!<7?Cf6u;eKl%3%s%?%/%?!<$N(BCO2$B5[<}@-G=$H%7%'%kB&BPN.J*
($B?.=#Bg1!M}9)(B) ($B3X(B)$B!{C]Fb(B $B0l?W(B$B!&(B ($B?.=#BgA!0](B) ($B@5(B)$BEhED(B $B8^I4N$(B$B!&(B ($B@5(B)$BD9ED(B $B8w@5(B$B!&(B ($B@5(B)$BJ!D9(B $BGn(B$B!&(B ($B@5(B)$B9b66(B $B?-1Q(B | chemical absorption porous membrane mass transfer coefficient
| 4-d | 871 |
9:20$B!A(B 11:20 | ZAA328 | $B%"%_%s4^M-%2%kN3;R%U%#%k%`$N(BCO2$B2D5U5[<}5sF0$KM?$($k(BCO2$BJ,05$N1F6A(B
($B6eBg1!9)(B) ($B3X(B)$B!{IM:j(B $B1{(B$B!&(B Yue Mengchen$B!&(B ($B@5(B)$B@1Ln(B $BM'(B$B!&(B ($B@5(B)$B;01:(B $B2B;R(B | CO2 absorption pKa gel particle
| 4-d | 765 |
9:20$B!A(B 11:20 | ZAA329 | $B%<%*%i%$%H7?:xBN7k>=(BZIF-8$B$N%a%+%N%1%_%+%k9g@.$HB$N32=(B
($B4X@>Bg9)(B) ($B3X(B)$B!{C+8}(B $B9d;V(B$B!&(B $B$B!&(B $B@>;3(B $BC#0lO:(B$B!&(B ($B@5(B)$B;0Bp(B $B5AOB(B$B!&(B ($B@5(B)$BEDCf(B $B=SJe(B | ZIF-8 mechanochemical synthesis granulation
| 4-e | 706 |
9:20$B!A(B 11:20 | ZAA330 | Merlinoite$B$rMQ$$$?(BCs$B%$%*%s$N%$%*%s8r49(B
($B4X@>Bg(B) ($B3X(B)$B!{3QC+(B $BM4$B!&(B ($B@5(B)$B:4Ln(B $B@?(B$B!&(B $BNkLZ(B $B=S8w(B$B!&(B ($B@5(B)$B;0Bp(B $B9'E5(B | Cs removal Merlinoite Ion exchange
| 4-e | 745 |
9:20$B!A(B 11:20 | ZAA331 | $B%]%j%U%'%N!<%k5[CeG=$rM-$9$kA!0]$N:n@=$H$=$N@-G=I>2A(B
($B@iMUBg(B) ($B3X(B)$B!{8eF#(B $B@;B@(B$B!&(B $B@nB<(B $BN5G72p(B$B!&(B $B2O9g(B($BLn4V(B) $BHK;R(B$B!&(B $BG_Ln(B $BB@Je(B$B!&(B ($B@5(B)$B:XF#(B $B630l(B$B!&(B ($B4D6->t2=8&(B) ($B@5(B)$BF#86(B $BK.IW(B$B!&(B $B?\6?(B $B9b?.(B$B!&(B ($B%-%j%s(B) $B9)F#(B $B$"$:$5(B$B!&(B $BF|CV(B $B=_J?(B$B!&(B $B | adsorptive fiber polyphenol
| 4-e | 750 |
9:20$B!A(B 11:20 | ZAA332 | $B%Q%i%8%&%`?(G^C4;}%j%"%/%?!<$rL\;X$7$?B?9&2A(B
($B6eBg9)(B) ($B3X(B)$B!{>>K\(B $B8w(B$B!&(B ($B6eBg1!9)(B) ($B@5(B)$B@%8M(B $B900l(B$B!&(B ($B@5(B)$B@1Ln(B $BM'(B$B!&(B ($B@5(B)$B;01:(B $B2B;R(B | porous monolith NIPAm gel palladium
| 4-e | 472 |
9:20$B!A(B 11:20 | ZAA333 | $B%^%$%/%m%O%K%+%`9=B$$rM-$9$k%+!<%\%s%/%i%$%*%2%k$K$h$k%U%'%N!<%k$H?'AG$NO"B3J,N%(B
($BKLBg1!9)(B) ($B3X(B)$B!{5HED(B $B@?0lO:(B$B!&(B ($B@5(B)$B4dB<(B $B?60lO:(B$B!&(B ($B@5(B)$B2.Ln(B $B7.(B$B!&(B ($B@5(B)$B8~0f(B $B?B(B | ice templating method phenol separation dye separation
| 4-e | 431 |
9:20$B!A(B 11:20 | ZAA334 | $B%$%*%s8r49A!0]$rMQ$$$?8&Ka%9%i%C%8$+$i$N(BNi$B5Z$S(BSn$B$NJ,N%2s<}(B
($BF`NI9b@l2=9)@l96(B) ($B3X(B)$B!{0;ED(B $B>0Li(B$B!&(B ($BF`NI9b@lJ*$B!&(B ($B@5(B)$BCfB<(B $B=(H~(B | adsorption ion exchange metal recovery
| 4-e | 721 |
9:20$B!A(B 11:20 | ZAA335 | CO2$B5[CeMQ%"%_%s=$>~%a%=B?9&BN$N%"%_%N4p9bL)EY2=$K4X$9$k8&5f(B
(NAIST) ($B3X(B)$B!{El[j(B $B:L2;(B$B!&(B (RITE) ($B@5(B)$B>B8}(B $BNKJ?(B$B!&(B ($B@5(B)$B;3ED(B $B=(>0(B$B!&(B ($B@5(B)$BM>8l(B $B9nB'(B | CO2 capture amine adsorption
| 4-e | 748 |
9:20$B!A(B 11:20 | ZAA336 | $B2aG.?e>x5$%o%s%9%F%C%WC:2=!&Ij3hK!$K$h$k3h@-C:$ND4@=(B : Cs$B5[Ce:^$X$N1~MQ(B
($BOB2N;39b@l@l962J(B) ($B3X(B)$B!{0fC+(B $B??(B$B!&(B ($BOB2N;39b@lJ*:(B | superheated steam activated carbon cesium adsorption
| 4-e | 298 |
9:20$B!A(B 11:20 | ZAA337 | $B%2%kGvKlEII[K!$rMQ$$$?%U%'%m%7%"%s2=E4B$N3BN$N(BCs$B5[Ce(B
($BEl9)Bg86;RO'8&(B) ($B3X(B)$B!{:d0f(B $BM*2p(B$B!&(B $B6b_7(B $B7CB@(B$B!&(B ($B@5(B)$B0pMU(B $BM%2p(B$B!&(B $B=oL@(B $BGn(B$B!&(B ($B@5(B)$BC]2<(B $B7rFs(B | Iron ferrocyanide Cs adsorption Thin-film gel coating method
| 4-e | 316 |
9:20$B!A(B 11:20 | ZAA338 | $B%2%k1UCj=P$rMQ$$$?%/%m%^%HK!$K$h$k%=%U%H@-6bB0$NJ,N%!&2s<}(B
($BEl9)Bg86;RO'8&(B) ($B3X(B)$B!{2OB<(B $BBn:H(B$B!&(B ($B@5(B)$BC]2<(B $B7rFs(B | Extraction Chromatography Polymer gel Adsorption
| 4-e | 867 |
9:20$B!A(B 11:20 | ZAA339 | $B3$?e$+$iJ|
($B@iMUBg(B) ($B3X(B)$B!{8eF#(B $B=Y0l(B$B!&(B $BJR6M(B $B?p4p(B$B!&(B $B@.LS(B $BfF;R(B$B!&(B ($B4D6->t2=8&(B) ($B@5(B)$BF#86(B $BK.IW(B$B!&(B $B?\6?(B $B9b?.(B$B!&(B ($B@iMUBg(B) $B2O9g(B($BLn4V(B) $BHK;R(B$B!&(B $BG_Ln(B $BB@Je(B$B!&(B ($B@5(B)$B:XF#(B $B630l(B | radioactive strontium removal sodium titanate adsorptive fiber
| 4-e | 561 |
9:20$B!A(B 11:20 | ZAA340 | $Bx5$5[C&Ce@-G=$N8~>e(B
($BFAEgBg1!@hC<650iIt(B) ($B3X(B·$B5;4p(B)$B!{:4F#(B $BJ89a(B$B!&(B ($BFAEgBg1!(BSTS$B8&(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 $BLP(B | AlPO-5 Water adsorption-desorption performance Substitution with several metals
| 4-e | 149 |
9:20$B!A(B 11:20 | ZAA341 | $B?M9)F)@OKl$rMQ$$$?JQ@-%?%s%Q%/
($BF`NI9b@lJ*$B!&(B ($B3X(B)$B6a;3(B $BM'M|(B$B!&(B ($BEl%l@hC<:`NA8&(B) $B>eLn(B $BNIG7(B$B!&(B $B9b66(B $BGn(B$B!&(B $B;3ED(B $B@?G7(B$B!&(B $BF#;^(B $BMN6G(B$B!&(B ($BF`NI9b@lJ*$B!&(B ($B@5(B)$BCfB<(B $B=(H~(B | Dialysis membrane Protein Denaturation
| 4-e | 719 |
9:20$B!A(B 11:20 | ZAA342 | $B5U%_%;%k$K$h$k%"%_%N;@J,N%$NJ,;RF0NO3X%7%_%e%l!<%7%g%s(B:$B%_%/%m9=B$$H<+M3%(%M%k%.!<(B
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| 4-f | 286 |
9:20$B!A(B 11:20 | ZAA343 | $B;il$K$*$1$k%/%m%m%U%#%k(Ba$B$N2q9g5sF0$NI>2A$J$i$S$K$=$N1~MQ(B
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| 4-f | 959 |
9:20$B!A(B 11:20 | ZAA344 | Poloxamer$B$K$h$k?eAjFsAj7O$N7A@.(B
($BL>Bg9)(B) ($B3X(B)$B!{J?;3(B $BOB$B!&(B ($BL>BgL$Mh8&(B) ($B@5(B)$B_7ED(B $B2BBe(B$B!&(B ($BL>Bg9)(B) $B1]ED(B $BMN0l(B | Poloxamer biphasic system rhenium extraction
| 4-f | 184 |
9:20$B!A(B 11:20 | ZAA345 | Modeling of solvent extraction equilibria of ammonia and nickel(II) with LIX84I
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| 4-f | 945 |
9:20$B!A(B 11:20 | ZAA346 | $B%j%>%A%&%`7k>=2=$K5Z$\$9;i
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| 4-g | 958 |
9:20$B!A(B 11:20 | ZAA347 | $BD6NW3&4%Ag$rMxMQ$7$?%+!<%\%s%J%NN3;R%(%"%m%2%k$N:n@=$HEE5$FC@-(B
($BEl9)Bg1!M}9)(B) ($B3X(B)$B!{(BKunanusont Nattanai$B!&(B ($B@5(B)$B2<;3(B $BM52p(B | supercritical carbon dioxide drying carbon nanoparticle aerogel electrical resistance
| 4-h | 640 |
9:20$B!A(B 11:20 | ZAA348 | $B9bJ,;R?eMO1U$G<>$C$?B?9&BN$N4%Ag$K$*$1$k4^9bJ,;RN(J,I[$H4%AgB.EY(B
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| 4-h | 120 |
9:20$B!A(B 11:20 | ZAA349 | $BDcN3;RG;EY%9%i%j!
($B?@8MBg1!9)(B) ($B3X(B)$B!{AD3+(B $BH~F`;R(B$B!&(B ($B3X(B)$BBm(B $B9I(B$B!&(B ($B@5(B)$B:#6p(B $BGn?.(B$B!&(B ($B@5(B)$BKY9>(B $B9';K(B | Drying model Slurry coating Particle segregation
| 4-h | 121 |
9:20$B!A(B 11:20 | ZAA350 | $BE`7k$7$?%K%s%8%s$N8:05G^BNN3;RN.F0AXFb$K$*$1$k4%AgFC@-(B
($B@EBg1!9)(B) ($B3X(B)$B!{GkK\(B $BL@MN(B$B!&(B ($B@5(B)$BN)85(B $BM:<#(B | Drying Fluidized bed Carrot
| 4-h | 239 |
9:20$B!A(B 11:20 | ZAA351 | $B5[<>@-N3;RN.F0AXFb$KA^F~$7$?<>$j8GBN$N4%Ag5sF02r@O(B
($B@EBg1!9)(B) ($B3X(B)$B!{>.0fEZ(B $BKS(B$B!&(B ($B@5(B)$BN)85(B $BM:<#(B | Drying Fluidized bed DEM-CFD
| 4-h | 241 |
9:20$B!A(B 11:20 | ZAA352 | $BE`7k4%Ag$K$h$k6&7k>=$N:n@=$K8~$1$?G.B,Dj$N3hMQ(B
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| 4-h | 758 |
9:20$B!A(B 11:20 | ZAA353 | $B%K!<%I%k;I7c$K$h$k??6u4%Ag;~$N(Bfoaming$B$*$h$S4%AgMzNr$N@)8f(B
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| 4-h | 401 |
9:20$B!A(B 11:20 | ZAA354 | $B8:054%Ag4o$rMxMQ$7$?A!0]$N4%AgFC@-$N8!F$(B
($BFAEgBg1!9)(B) ($B3X(B)$B!{:dK\(B $B9(?N(B$B!&(B ($B3$(B)$B%"%k%+%s%?%i(B $B%"%S%i(B $B%X%9!<%9(B $B%i%U%!%(%k(B$B!&(B ($B@5(B)$B30NX(B $B7r0lO:(B$B!&(B ($B@5(B)$BKY2O(B $B=S1Q(B$B!&(B ($B0$Fn9b@l(B) ($B@5(B)$B0l?9(B $BM&?M(B | Vacuum drying technology Fiber drying Drying rate
| 4-h | 855 |
ZB $B2q>l!&Bh(B 3 $BF|(B |
9:20$B!A(B 11:20 | ZBA301 | $B%$%*%s8r49%<%*%i%$%HKl$NKlF)2aFC@-(B
($B$B!&(B $BKc@8(B $BBs:H(B$B!&(B ($B3X(B)$BBg1:(B $B6W2;(B$B!&(B ($B3X(B)$BCSED(B $BJb(B$B!&(B ($B@5(B)$BLnB<(B $B4490(B | MOR zeolite membrane ion exchange water permeation
| 4-a | 713 |
9:20$B!A(B 11:20 | ZBA302 | $B%<%*%i%$%H7?:xBN7k>=(BZIF-8$B$N=%U%j!<@=Kl$H%,%9F)2aFC@-(B
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| 4-a | 740 |
9:20$B!A(B 11:20 | ZBA303 | $B%]%j%$%_%IM3MhC:AGJ#9gKl$N:n@=$H%,%9F)2aFC@-(B
($B;38}Bg1!M}9)(B) ($B3X(B)$B:dK\(B $B7rB@O:(B$B!&(B ($B@5(B)$B7'@Z(B $B@t(B$B!&(B ($B@5(B)$B!{EDCf(B $B0l9((B$B!&(B ($B@5(B)$B4nB?(B $B1QIR(B | arbon molecular sieve membranes polyimides gas permeation
| 4-a | 896 |
9:20$B!A(B 11:20 | ZBA304 | $BBg7?5UEE5$F)@O%7%9%F%`$K$*$1$kH/EEFC@-I>2A$H$=$N2r@O(B
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| 4-a | 899 |
9:20$B!A(B 11:20 | ZBA305 | $B?eG.K!$K$h$k%+!<%\%sKl$N:n@=(B
($BEl9)Bg(B) ($B3X(B)$B!{:4Ln(B $BfF:H(B$B!&(B ($B@5(B)$B0kIt(B $BIR9((B$B!&(B $B>>2<(B $B>M;R(B$B!&(B $BCfEg(B $B>O(B | activated carbon water/ethanol separation glucose
| 4-a | 913 |
9:20$B!A(B 11:20 | ZBA306 | 2$B2/CH4$BJ,N%(B
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| 4-a | 946 |
9:20$B!A(B 11:20 | ZBA307 | Na-ZSM-5$BKl$rMQ$$$?%a%?%N!<%k9g@.%a%s%V%l%s%j%"%/%?!<$N2DG=@-(B
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| 4-a | 359 |
9:20$B!A(B 11:20 | ZBA308 | $B%-%7%l%sM3Mh$NG.J,2rC:AG$rMQ$$$?(Bsilicalite-1$BKl$N%_%/%m:Y9&7B@)8f(B
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| 4-a | 365 |
9:20$B!A(B 11:20 | ZBA309 | CFD$B$rMxMQ$7$?%<%*%i%$%HKl$K$h$k(BCO2/CH4$B:.9g7OJ,N%$K$*$1$k%Q!<%_%"%s%9$NG;EY0MB8@-$N?dDj(B
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| 4-a | 949 |
9:20$B!A(B 11:20 | ZBA310 | Preparation and characterization of antifouling PVC hollow fiber membrane by blending an amphiphilic copolymer
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| 4-a | 972 |
9:20$B!A(B 11:20 | ZBA311 | $B%*!<%k%7%j%+(BSTT$B7?%<%*%i%$%HKl$N9g@.(B
($B4X@>Bg4DET9)(B) ($B3X(B)$B!{Cf0f(B $B6F;V(B$B!&(B ($B@5(B)$B9SLZ(B $BDgIW(B$B!&(B ($BF|N)B$A%(B) ($BK!(B)$B:#:d(B $BNg;K(B$B!&(B ($B;:Am8&(B) $BD9C+@n(B $BBY5W(B$B!&(B $B:4F#(B $B9d0l(B$B!&(B ($B4X@>Bg4DET9)(B) ($B@5(B)$B;3K\(B $B=( | all silica zeolite zeolite membrane pervaporation
| 4-a | 202 |
9:20$B!A(B 11:20 | ZBA312 | $BHy:YAtN`$r@:L)$m2a$9$k:]$NKl4V:905$,Kl$N%U%!%&%j%s%08=>]$K5Z$\$91F6A(B
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| 4-a | 267 |
9:20$B!A(B 11:20 | ZBA313 | $BEE5$F)@OK!$rMQ$$$?(BCO2$BJ,N%2s<}%7%9%F%`$K$*$1$kJ|;62aDx$N?e>x5$$N1F6A(B
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| 4-a | 510 |
9:20$B!A(B 11:20 | ZBA314 | CO2$B1~Ez@-%]%j%^!<$N?eOB5sF0$HB&:?4VAj8_:nMQ$K4X$9$kJ,;R%7%_%e%l!<%7%g%s(B
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| 4-a | 174 |
9:20$B!A(B 11:20 | ZBA315 | ZSM-5$BKl$K$*$1$kF)2a@-G=$HKl9=B$$N4XO"@-$N8!F$(B
($BAaBg@h?JM}9)(B/$BAaBgM}9)Am8&(B/JST-CREST) ($B@5(B)$B>>J}(B $B@5I'!&(B ($BAaBg@h?JM}9)(B) ($B3X(B)$B!{>>K\(B $BOKJ?(B$B!&(B ($B@5(B)$B@%2<(B $B2mGn(B | zeolite membrane permeability membrane structure
| 4-a | 367 |
9:20$B!A(B 11:20 | ZBA316 | OSDA$B$rMQ$$$J$$(B*BEA$B7?%<%*%i%$%HKl$N9g@.K!$HC:2=?eAGF)2aFC@-$N8!F$(B
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| 4-a | 369 |
9:20$B!A(B 11:20 | ZBA317 | $B5U?;F)Kl$X$N?F?e@-%]%j%^!<$N=$>~$,Hy@8J*IUCe$K5Z$\$91F6A(B
($B?@8MBg1!9)(B/$B@hC$B!&(B ($B@5(B)$B:4Gl(B $BBgJe(B$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B | Reverse osmosis membrane Hydrophilic polymer Bacterial adhesion
| 4-a | 398 |
9:20$B!A(B 11:20 | ZBA318 | $BM-5!MOG^$r%I%m!
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| 4-a | 36 |
9:20$B!A(B 11:20 | ZBA319 | $B9bF)?e@-$H9bBQ05@-$rM-$9$k(BTFC$B7?(BFO$BKl$N3+H/(B
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| 4-a | 717 |
ZC $B2q>l!&Bh(B 3 $BF|(B |
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| 3-a | 819 |
9:20$B!A(B 11:20 | ZCA302 | $BC:2=?eAG$NG.J,2r$K$*$1$k%H%k%(%s$*$h$S%Y%s%<%s$N@8@.$K4X$9$k>\:Y2=3XH?1~5!9=$N=$@5(B
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| 3-b | 212 |
9:20$B!A(B 11:20 | ZCA303 | $B>:29B.EY$K$h$jJQ2=$9$kHyJ4C:%A%c!<$NH?1~@-$r9MN8$7$?%V%m!<%Q%$%WFb$K$*$1$kHyJ4C:G3>F>l$N?tCM2r@O(B
($BElKLBg1!9)(B) ($B3X(B)$B!{C+K\(B $BFW0l(B$B!&(B ($B3X(B)$B@VHxDE(B $BfFBg(B$B!&(B ($B3X(B)$BAjGO(B $BC#:H(B$B!&(B ($B@5(B)$Bc7F#(B $BBYMN(B$B!&(B ($B@5(B)$B>>2<(B $BMN2p(B$B!&(B ($B@5(B)$B@DLZ(B $B=(G7(B$B!&(B ($B6eBgC:%;(B) $BLn_7(B $BAOJ?(B$B!&(B (JFE$B%9%A!<%k(B) $BB | Coal combustion Numerical simulation Reactivity
| 3-b | 175 |
9:20$B!A(B 11:20 | ZCA304 | $BCfDc29G.8;MxMQ>.7?%P%$%J%j!<%5%$%/%k$NH/EE%7%_%e%l!<%7%g%s(B
($B;37ABg1!M}9)(B) ($B3X(B)$B!{F2$B!&(B ($B%"%M%9%H4dED(B) $BOB@t(B $B9'L@(B$B!&(B $B0KF#(B $BMN(B$B!&(B $BF#2,(B $B40(B$B!&(B ($B;:Am8&(B) $BA0ED(B $BE/I'(B$B!&(B ($B;37ABg1!M}9)(B) ($B@5(B)$B>>ED(B $B7=8g(B | power generation heat engine simulation
| 3-d | 693 |
9:20$B!A(B 11:20 | ZCA305 | Time-Temperature-Transformation$B2r@O$K$h$k%I!<%W7?F3EE@-6bB0;@2=J*J4BN$N2CG.%W%m%;%9$N8zN(2=(B
(Bandung$B9)Bg(B/$BG@9)Bg(B) Widiatmoko Pramujo$B!&(B ($BG@9)Bg(B) ($B@5(B)$B!{(BLenggoro Wuled | heat treatment doping particles
| 3-e | 931 |
9:20$B!A(B 11:20 | ZCA306 | $BL55!%J%N$m2aKl$N%"%k%+%jN3;RJ,N%(B
($B$B!&(B $B4XK\(B $B6F(B$B!&(B $BW"@%(B $BCR5W(B$B!&(B $BC]Fb(B $B=_EP(B$B!&(B $BKLHx(B $BM5$B!&(B ($B@5(B)$BLnB<(B $B4490(B | counter diffusion CVD method silica hybrid membranes alkaline particles
| 4-a | 117 |
9:20$B!A(B 11:20 | ZCA307 | $BM-5!%O%$%I%i%$%IJ,N%MQ9bB.?eAGF)2a%<%*%i%$%HKl$N3+H/(B
($B$B!&(B $BGr0f(B $BKcN$Fa(B$B!&(B ($B3X(B)$BKLEh(B $B85$B!&(B ($B3X(B)$BCSED(B $BJb(B$B!&(B ($B=;M'EE9)(B) $B:XF#(B $B?r9-(B$B!&(B $BI6;3(B $BGn6)(B$B!&(B $B@P@n(B $B??Fs(B$B!&(B $B7,86(B $B0lLi(B$B!&(B ($B | MFI zeolite membrane porous silica substrate organic hydrides
| 4-a | 118 |
9:20$B!A(B 11:20 | ZCA308 | $B%=%k%\%5!<%^%kK!$K$h$k(BIRMOF-3$BKl$N:n@=$H%,%9F)2aFC@-$NI>2A(B
($BEl9)Bg1!(B) ($B3X(B)$B!{9S0f(B $BM'9a(B$B!&(B ($B@5(B)$B0kIt(B $BIR9((B$B!&(B (NIMS) $BLxED(B $B$5$d$+(B$B!&(B ($BEl9)Bg1!(B) $B>>2<(B $B>M;R(B$B!&(B $BCfEg(B $B>O(B | porous membrane CO2 separation ceramics
| 4-a | 172 |
9:20$B!A(B 11:20 | ZCA309 | $B%$%*%s1UBN4^M-(BPVA$B%<%i%A%sKl$K$h$k%(%?%N!<%k$NJ,N%(B
($BF1;V$B!&(B ($B@5(B)$B>>K\(B $BF;L@(B$B!&(B ($B@5(B)$B6aF#(B $BOB@8(B | Ionic liquid Ethanol Pervaparation
| 4-a | 179 |
9:20$B!A(B 11:20 | ZCA310 | FAU$B7?%<%*%i%$%HKl$rMQ$$$?2C05>r7o2<$K$*$1$k(BC3$BC:2=?eAGJ,N%FC@-$N8!F$(B
($BAaBg@h?JM}9)(B/$BAaBgM}9)Am8&(B/JST-CREST) ($B@5(B)$B>>J}(B $B@5I'!&(B ($BAaBg@h?JM}9)(B) ($B3X(B)$B!{:4!9LZ(B $B9/?M(B$B!&(B ($B3X(B)$B | FAU-type zeolite membrane pressurized conditions propylene separation
| 4-a | 346 |
9:20$B!A(B 11:20 | ZCA311 | OSDA$B$rMQ$$$J$$(BRHO$BKl$N9g@.$*$h$S>.J,;R:.9gJ*$KBP$9$kF)2aJ,N%FC@-(B
($BAaBg@h?JM}9)(B) ($B3X(B)$B$B!&(B ($B3X(B)$B!{C0CO(B $B??M}(B$B!&(B ($B3X(B)$BCz(B $B71Jv(B$B!&(B ($BAaBg@h?JM}9)(B/$BAaBgM}9)Am8&(B/JST-CREST) ($B@5(B)$B>>J}(B $B@5I'(B | zeolite RHO membrane synthesis
| 4-a | 347 |
9:20$B!A(B 11:20 | ZCA312 | $B%U%)%H%j%=%0%i%U%#!<$rMQ$$$?(BPd$BJ#9gKl$N:n@=$K$*$1$k
($B4tIlBg1!9)(B) ($B3X(B)$B!{B<@%(B $BC#Li(B$B!&(B ($B4tIlBg9)(B) ($B@5(B)$B5\K\(B $B3X(B$B!&(B ($B4tIlBg@8L?%;(B) ($B@5(B)$B6a9>(B $BLwB'(B$B!&(B ($B4tIlBg9)(B) ($B@5(B)$B>e5\(B $B@.G7(B$B!&(B ($BL>Bg1!9)(B) ($B@5(B)$B;3ED(B $BGn;K(B$B!&(B ($B@5(B)$BED@n(B $BCRI'(B | Pd Photolithography Surface modification
| 4-a | 440 |
9:20$B!A(B 11:20 | ZCA313 | Silicalite-1$BKl$N9g@.$K$*$1$kB?9&
($B4tIlBg1!9)(B) ($B3X(B)$B!{>eLn(B $B63J?(B$B!&(B ($B;:Am8&(B) ($B@5(B)$B:,4_(B $B=(G7(B$B!&(B ($B=;M'EE9)(B) $B:XF#(B $B?r9-(B$B!&(B $BI6;3(B $BGn6)(B$B!&(B $B@P@n(B $B??Fs(B$B!&(B ($B4tIlBg9)(B) ($B@5(B)$B5\K\(B $B3X(B$B!&(B ($B@5(B)$B>e5\(B $B@.G7(B$B!&(B ($B4tIlBg@8L?%;(B) ($B@5(B)$B6a9>(B $BLwB'(B | zeolite membrane separation support
| 4-a | 513 |
9:20$B!A(B 11:20 | ZCA314 | $B&A%"%k%_%J;Y;}BN$NFC@-$,(B*BEA$B7?%<%*%i%$%HKl@-G=$KM?$($k1F6A(B
($B4tIlBg1!9)(B) ($B3X(B)$B!{EOn4(B $BThLi(B$B!&(B ($B3X(B)$B>eLn(B $B63J?(B$B!&(B ($B;:Am8&(B) ($B@5(B)$B:,4_(B $B=(G7(B$B!&(B ($B4tIlBg9)(B) ($B@5(B)$B5\K\(B $B3X(B$B!&(B ($B@5(B)$B>e5\(B $B@.G7(B$B!&(B ($B4tIlBg@8L?%;(B) ($B@5(B)$B6a9>(B $BLwB'(B | zeolite membrane separation *BEA zeolite
| 4-a | 532 |
9:20$B!A(B 11:20 | ZCA315 | $B@5?;F)KlK!$K$h$kE|G;=L%W%m%;%9$N8!F$(B
($B?@8MBg1!9)(B/$B@hC$B!&(B ($B@5(B)$B0B@n(B $B@/9((B$B!&(B ($B3X(B)$BEDCf(B $BM5Bg(B$B!&(B ($B@5(B)$B9b66(B $BCR51(B$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B | Forward osmosis Up-concentration Saccharide
| 4-a | 579 |
9:20$B!A(B 11:20 | ZCA316 | $B%$%*%s1UBN$N1UBNKl$K$h$kK'9aB2C:2=?eAG$N>x5$F)2aJ,N%(B
($BEl9)Bg(B) ($B3X(B)$B!{?@C+(B $BCR5,(B$B!&(B ($B3X(B)$B@P@n(B $BBg5.(B$B!&(B ($B@5(B)$B0KEl(B $B>O(B | vapor permeation hydrocarbons ionic liquid
| 4-a | 647 |
9:20$B!A(B 11:20 | ZCA317 | $B05NO:9$r6nF0NO$H$9$k?e%A%c%s%M%k%b%G%k$K$*$1$k?eJ,;RF)2a5sF02r@O(B
($B9)3X1!Bg9)(B) ($B3X(B)$B!{8eF#(B $BBg$B!&(B ($B@5(B)$B9b1)(B $BMN=<(B | Molecular dynamics Aquaporin Water channel
| 4-a | 684 |
9:20$B!A(B 11:20 | ZCA318 | AlPO4-18$BKl$N(BCO2/CH4$BF)2aJ,N%$*$h$S5[CeFC@-$N8!F$(B
($BAaBg@h?JM}9)(B) ($B3X(B)$B$B!&(B ($B3X(B)$B!{BgEh(B $B5AOB(B$B!&(B ($BAaBg@h?JM}9)(B/$BAaBgM}9)Am8&(B/JST-CREST) ($B@5(B)$B>>J}(B $B@5I'(B | membrane separation AlPO4-18 CO2/CH4
| 4-a | 351 |
9:20$B!A(B 11:20 | ZCA319 | SiO2$BG;EY$,9b$$A06nBN%2%k$rMQ$$$?(BSAPO-18$BKl$N9g@.(B
($BAaBg@h?JM}9)(B/$BAaBgM}9)Am8&(B/JST-CREST) ($B@5(B)$B>>J}(B $B@5I'!&(B ($BAaBg@h?JM}9)(B) ($B3X(B)$B!{@P9u(B $BAOG72p(B$B!&(B $BK\AR(B $BTw(B$B!&(B ($B@5(B)$B@%2<(B $B2mGn(B | SAPO-18 Secondary-growth method Si content
| 4-a | 354 |