$B$BHV9f(B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $BH/I=7A<0(B | |
73 | $BB?9&e$K%Q%i%8%&%`GvKl$r7A@.$9$k$?$a$NCf4VAXHyN3;R$NC5:w(B ($BFAEgBg1!AO@.(B) ($B3X(B)$B!{;{yu(B $B>!70(B$B!&(B $B9a@>(B $BJ~:H(B$B!&(B ($BFAEgBg1! | Pd thin membrane Porous SUS support Intermediate layer particle
| P |
104 | $B%/%m%9%U%m!<$K$h$k%$%7%/%i%2M3Mh%U%#%3%S%j%W%m%F%$%s$NKlJ,N%(B ($B:4Bg1!9)(B) ($B3X(B)$B!{F|$B!&(B ($B@5(B)$B?9Dg(B $B??B@O:(B$B!&(B ($B@5(B)$BBgEO(B $B7<2p(B$B!&(B ($B@5(B)$B@n4nED(B $B1Q9'(B | Membrane separation Microalgae phycobiliprotein
| P |
108 | Stripping$BK!$H(BUVC$B>H ($B:42lBg1!9)(B) ($B3X(B)$B!{0KF#(B $B8wJ?(B$B!&(B ($B:42lBg(B) ($B@5(B)$B?9Dg(B $B??B@O:(B$B!&(B ($B@5(B)$BBgEO(B $B7<2p(B$B!&(B ($B@5(B)$B@n4nED(B $B1Q9'(B | 1,4-Dioxane Stripping UVC
| P |
111 | pH$B1~Ez@-9bJ,;RHoJ$B?9& ($B1'ET5\Bg1!CO(B) ($B3X(B)$B!{KRLn(B $B6WH~(B$B!&(B ($B1'ET5\Bg9)(B) ($B@5(B)$B:4F#(B $B9d;K(B$B!&(B $B`*Kv(B $B?58c(B$B!&(B ($B@5(B)$B0KF#(B $BD> | pH responsive polymer coated membrane permeation of carbonic acid
| P |
114 | $B9aNA%(%9%F%k9g@.$N$?$a$NN.DL<0KlH?1~4o$N3+H/(B ($B1'ET5\Bg(B) ($B3X(B)$B!{Cf;3(B $B9d(B$B!&(B ($B@5(B)$B:4F#(B $B9d;K(B$B!&(B ($B@5(B)$B0KF#(B $BD>$B!&(B ($BF|K\%<%*%s(B) ($B@5(B)$B;0LZ(B $B1QN;(B | Flow Membrane reactor esterification
| P |
117 | Au(III)$B$X$N%$%*%sMOG^OBCj=P:^C5:w$K$*$1$k5!3#3X=,$NF3F~(B ($B5\:jBg9)(B) ($B3X(B)$B!{4d@Z(B $BM:Ht(B$B!&(B ($B@5(B)$BBgEg(B $BC#Li(B$B!&(B ($B@5(B)$B0pED(B $BHtD;(B | machine learning extraction Au(III)
| P |
122 | $B3F ($B5\:jBg9)(B) ($B3X(B)$B!{@P66(B $BN5Li(B$B!&(B ($B@5(B)$BBgEg(B $BC#Li(B$B!&(B ($B@5(B)$BBg\F(B $B70(B$B!&(B ($B:42lBg1!9)(B) ($B@5(B)$BBgEO(B $B7<2p(B | calixarene metal
| P |
138 | Effect of functional groups on FO membrane surface for ammonium selectivity ($B?@8MBg9)(B/$B@hC$B!&(B ($B@5(B)$B:4!9LZ(B $BM:;K(B$B!&(B ($B?@8MBg1!2J5;%$%N%Y(B/$B@hC$B!&(B ($B@5(B)$BCf@n(B $B7I;0(B$B!&(B ($B?@8MBg9)(B/$B@hC>;3(B $B=(?M(B | Forward Osmosis ammonium selectivity carboxylic groups
| P |
140 | Li(I)$B5[Ce$KMQ$$$k&K(B-MnO2$BB$N35[Ce:^$KBP$9$k;@=hM}$N1F6A(B ($B5\:jBg9)(B) ($B3X(B)$B!{Gr@P(B $B8-;KO/(B$B!&(B ($B@5(B)$BBgEg(B $BC#Li(B$B!&(B ($B@5(B)$BBg\F(B $B70(B$B!&(B ($BKL6eBg9)(B) ($B@5(B)$B@>IM(B $B>OJ?(B$B!&(B ($B@5(B)$B5HDM(B $BOB<#(B | column adsorption Li(I)
| P |
150 | $BE7A39[J*5[Ce%;%7%&%`$N8G1UCj=P$KM?$($kCj=P29EY$N1F6A(B ($B?73cBg<+(B) ($B3X(B)$B!{9SLZ(B $BM*M$(B$B!&(B ($B3X(B)$B;0C+(B $BBsLi(B$B!&(B ($B@5(B)$B>.>>(B $BGn9,(B$B!&(B ($B@5(B)$B;3:](B $BOBL@(B$B!&(B ($B@5(B)$BB?Eg(B $B=(CK(B | Cesium Desorption Extraction
| P |
175 | $B5?;w%P%$%*%G%#!<%<%kG3NA$NH/4@A`:n$K$*$1$kE:2CJ*$N1F6A(B ($B?73cBg<+(B) ($B3X(B)$B!{EOJU(B $BM[B@(B$B!&(B ($B3X(B)$B2O9g(B $Bb+2p(B$B!&(B ($B3X(B)Bagini Simon Ubengi Elnour$B!&(B ($B3X(B)$BEZED(B $BB@0l(B$B!&(B ($B@5(B)$B>.>>(B $BGn9,(B$B!&(B ($B@5(B)$B;3:](B $BOBL@(B$B!&(B ($B@5(B)$BB?Eg(B $B=(CK(B | Biodiesel sweating operation cold flow properties
| P |
176 | BDF$B$NE:2CJ*2~ ($B?73cBg<+(B) ($B3X(B)$B!{EZED(B $BB@0l(B$B!&(B ($B3X(B)$B2O9g(B $Bb+2p(B$B!&(B ($B3X(B)$BEOJU(B $BM[B@(B$B!&(B ($B3X(B)$B%P%.%K(B $B%5%$%b%s%&%Y%s%.%(%k%N%"(B$B!&(B ($B@5(B)$B>.>>(B $BGn9,(B$B!&(B ($B@5(B)$B;3:](B $BOBL@(B$B!&(B ($B@5(B)$BB?Eg(B $B=(CK(B | Biodiesel winterization
| P |
202 | $B;iKC;@%a%A%k%(%9%F%k$NDc29$G$NN3;R@8@.$X$N?eE:2C$HNd5QB.EY$N1F6A(B ($B?73cBg<+(B) ($B3X(B)$B!{2O9g(B $Bb+2p(B$B!&(B ($B3X(B)$BEOJU(B $BM[B@(B$B!&(B ($B3X(B)$BEZED(B $BB@0l(B$B!&(B ($B3X(B)Bagini Simon Ubengi Elnour$B!&(B ($B@5(B)$B>.>>(B $BGn9,(B$B!&(B ($B@5(B)$B;3:](B $BOBL@(B$B!&(B ($B@5(B)$BB?Eg(B $B=(CK(B | Biodiesel Cold flow Separation effciency
| P |
216 | $BH/9Z%(%?%N!<%kG;=L$X$N%<%*%i%$%HKl$NE,MQ(B ($B;38}Bg1!AO(B) ($B3X(B)$B!{EhED(B $BM5(B$B!&(B ($B;38}Bg(BURA) ($B@5(B)$B2#ED(B $B$B!&(B ($B;38}Bg1!G@(B) $B;3ED(B $B$B!&(B ($B;38}Bg1!AO(B) ($B@5(B)$B7'@Z(B $B@t(B | Bio-ethanol Separation Zeolite
| P |
217 | $B%<%*%i%$%HKl$HGr6b$NJ#9g2=$K$h$kMOB8M-5!J*$N?eCf;@2=J,2r(B ($B;38}Bg1!AO(B) ($B3X(B)$B!{B<:j(B $B9IJ?(B$B!&(B $B6yK\(B $BNQFA(B$B!&(B ($B@5(B)$B7'@Z(B $B@t(B | zeolite Pt water treatment
| P |
218 | $B%O%$%I%l!<%H2=%,%95[<}AuCV$K$*$1$kJ* ($B?73cBg<+(B) ($B3X(B)$B!{9>O"(B $BNCM'(B$B!&(B $BCfLn(B $BBg51(B$B!&(B ($B@5(B)$B>.>>(B $BGn9,(B$B!&(B ($B@5(B)$B;3:](B $BOBL@(B$B!&(B ($B@5(B)$BB?Eg(B $B=(CK(B | Gas hydrate Gas separation Mass transfer
| P |
219 | $B%]%j%"%/%j%k;@HoJ$%"%k%_%JN3;RAX$K$*$1$kF)2aDq93$NMO1U(BpH$B0MB8@-(B ($B1'ET5\Bg1!CO(B) ($B3X(B)$B!{2.Ln(B $BN6:H(B$B!&(B ($B3X(B)$BKRLn(B $B6WH~(B$B!&(B ($B1'ET5\Bg9)(B) ($B@5(B)$B:4F#(B $B9d;K(B$B!&(B ($B@5(B)$B0KF#(B $BD> | pH responsive polymer alumina particle polyacrylic acid
| P |
228 | Influence of salts on photocatalytic oxidation performance of silver-doped TiO2 membrane (Yamaguchi U.) ($B3X(B)$B!{(BChe Abdul Rahim Azzah Nazihah$B!&(B (Jaime I Univesity) Sergio Mestre$B!&(B (Yamaguchi U.) ($B@5(B)Kumakiri Izumi | Photocatalyst Salinity Ag-TiO2
| P |
240 | $B%$%*%s1UBN$r;HMQ$7$?<+F0 ($B6eBg1!9)(B) ($B3X(B)$B!{9b5V(B $B$B!&(B ($B3X(B)$B2VED(B $BN4J8(B$B!&(B ($B@5(B)$B8eF#(B $B2m9((B | Ionic Liquids Platinum Group Metals Selective Recovery
| P |
282 | Au(III)$B$X$N%$%*%sMOG^OBCj=P:^$H$7$F$NK'9aB2%1%H%s$NHf3S8!F$(B ($B5\:jBg1!9)(B) ($B3X(B)$B!{;0Bp(B $B98B@(B$B!&(B ($B5\:jBg9)(B) ($B@5(B)$B0pED(B $BHtD;(B$B!&(B ($B@5(B)$BBg\F(B $B70(B$B!&(B ($B@5(B)$BBgEg(B $BC#Li(B | extraction metal ketone
| P |
295 | Development of ultrathin polyamide nanofilm with enhanced inner-pore interconnectivity via graphene quantum dots-assembly intercalation for high-performance organic solvent nanofiltration (Kobe U.) ($BCf(B)$B!{(BShen Qin$B!&(B ($B@5(B)Lin Yuqing$B!&(B ($B@5(B)Matsuyama Hideto | graphene quantum dot thin-film nanocomposite membrane organic solvent nanofiltration
| P |
301 | One-step entrapment of amphiphilic copolymer on the outer surface of PVDF hollow fiber membrane via TIPS process using triple-orifice spinneret (Kobe U.) ($B3X(B)$B!{(BZhang Pengfei$B!&(B ($B@5(B)Saeid Rajabzade$B!&(B ($B@5(B)Matsuyama Hideto | Surface entrapment Hollow fiber membrane Triple-orifice spinneret
| P |
302 | Multifunctional Thin-Film Nanofiltration Membrane Incorporated AgMOF for High Desalination Performance, Antifouling and Antibacterial Properties (Kobe U.) ($B3X(B)$B!{(BIstirokhatun Titik$B!&(B ($B@5(B)Lin Yuqing$B!&(B ($B@5(B)Matsuyama Hideto | nanofiltration silver biofouling
| P |
304 | In-situ ultrafine mineralization engineer inter-mediated nano filtration membrane (Kobe U.) ($BCf(B)$B!{(BSong Qiangqiang$B!&(B ($B@5(B)Lin Yuqing$B!&(B ($B@5(B)Matsuyama Hideto | Nanofiltration SiO2 interlayer Interfacial polymerization
| P |
317 | $B1v2=?eAG$N:F=[4D$K$h$kGQ$+$s?eCf%^%0%M%7%&%`$NO"B3J,N%A`:nK!$N8!F$(B ($BAaBg1!M}9)(B) ($B3X(B)$B!{66D^(B $BM%M4(B$B!&(B ($B%5%5%/%i(B) ($BK!(B)$B;0J](B $B7DL@(B$B!&(B ($BF|4x(B) ($BK!(B)$BF#K\(B $BfF(B$B!&(B ($BAaBg1!M}9)(B) Myers C. A.$B!&(B ($B@5(B)$BCf3@(B $BN4M:(B | Carbon Capture and Utilization Acid gas recovery Super-azeotropic condition
| P |
326 | $B%G%+%s%?$rMQ$$$?(BABE$BJ,N%%W%m%;%9$N:GE,2=(B ($B5~Bg9)(B) ($B3X(B)$B!{4X(B $BM%:n(B$B!&(B ($B3$(B)$B$"$k$+$s$?$i$"$S$i(B $B$X$9!<$9$i$U$!$($k(B | Linear programming Heterogeneous azeotropic distillation Process optimization
| P |
332 | Effects of Polymer Branching Structure on the Hydrodynamic Layer Thickness of Adsorbed Layer Formed on the Colloidal Particles (U. Tsukuba) ($B3X(B)$B!{(BMuhammad Vito Brata$B!&(B ($B3X(B)Lim Voon Huey$B!&(B ($B@5(B)Adachi Yasuhisa | Branched polymer Hydrodynamic layer thickness Adsorption
| P |
339 | $B%7%9%F%$%s$r%$%s%?!<%+%l!<%H$7$?(BMg-Fe$BAX>uJ#?e;@2=J*$K$h$k6b$N2s<}(B ($B5\:jBg9)(B) ($B@5(B)$B!{Bg\F(B $B70(B$B!&(B $B2,B<(B $BbCM3(B$B!&(B $BKY9>(B $B7DB@(B$B!&(B ($B@5(B)$BBgEg(B $BC#Li(B | gold recovery layered double hydroxide cysteine
| P |
341 | UCST$B7?29EY1~Ez@-%$%*%s1UBN$N2=3X9=B$$,AjE>0\5sF0$K5Z$\$91F6A(B ($B?@8MBg1!9)(B/$B@hC$B!&(B ($B@5(B)$B>>2,(B $B=_(B$B!&(B ($B@5(B)$B?@Hx(B $B1Q<#(B$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B | thermo-responsive UCST-type phase transition ionic liquids
| P |
357 | Gel-free SAC$BK!$rMQ$$$?(Bsilicalite-1$BKl9g@.$K$*$1$kG[8~@-@)8f(B ($B4tIlBg1!<+A3(B) ($B3X(B)$B!{0p3@(B $B914u(B$B!&(B ($B3X(B)$BMn9g(B $B42$B!&(B ($BD+F|Bg;u(B) ($B@5(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) $B1|Ln(B $BBsLi(B$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 ($B4tIlBg9bEy8&(B) ($B@5(B)$B6a9>(B $BLwB'(B | steam-assisted conversion silicalite-1 pervaporation
| P |
395 | $B8:05$m2aK!$K$h$j:n@=$7$?%A%?%s;@%J%N%7!<%HKl$K$*$1$k@QAX9=B$$H(B $BJ,N%@-G=$N4X78(B ($B?@8MBg1!2J5;%$%N%Y(B) ($B3X(B)$B!{Kv0f(B $BM-@?(B$B!&(B ($B?@8MBg1!2J5;%$%N%Y(B/$B@hC$B!&(B ($B@5(B)$B?7C+(B $BBn;J(B$B!&(B ($B?@8MBg1!9)(B/$B@hC>2,(B $B=_(B$B!&(B ($B@5(B)$B?@Hx(B $B1Q<#(B$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B$B!&(B ($B?@8MBg1!2J5;%$%N%Y(B/$B@hC$B!&(B ($BBgDM2=3X(B) ($BK!(B)$B?9(B $B9(?N(B$B!&(B ($BK!(B)$B;e0f(B $B?-$B!&(B ($BK!(B)$B8eF#(B $B=S | membrane titanate nanosheet water treatment
| P |
408 | $B?e>x5$6!5kE>49K!$K$h$j9g@.$7$?(BCHA$B7?%<%*%i%$%H$N(BCO2$BF0E*5[CeFC@-(B ($B4X@>Bg1!M}9)(B) ($B3X(B)$B!{Hu8}(B $BM:EM(B$B!&(B ($B4X@>Bg(B) ($B@5(B)$BEDCf(B $B=SJe(B | CHA zeolite breakthrough curve adsorption
| P |
415 | Novel tough ion gel-based CO2 separation membrane with interpenetrating polymer network (Kobe U.) ($B3$(B)$B!{(BZhang Jinhui$B!&(B ($B@5(B)Kamio Eiji$B!&(B ($B@5(B)Matsuoka Atsushi$B!&(B ($B@5(B)Nakagawa Keizo$B!&(B ($B@5(B)Yoshioka Tomohisa$B!&(B ($B@5(B)Matsuyama Hideto | Tough ion gel Interpenetrating polymer network CO2 separation membrane
| P |
461 | $B5$K"$rJ,N%G^BN$H$9$k%/%m%m%-%s$N?WB.@:@=5;=Q(B ($BKL8+9)Bg(B) ($B3X(B)$B!{;y6L(B $B9/51(B$B!&(B ($B3X(B)$BBg4d(B $B??;R(B$B!&(B ($B@5(B)$Bc7F#(B $BE0(B | Flotation Chloroquine Rapid purification
| P |
468 | $B%+!<%\%s%j%5%$%/%k$rL\E*$H$7$?%"%k%+%j?eMO1U$K$h$k(BCO2$BJ,N%$N2DG=@-(B ($B6eBg(BI2CNER) ($B@5(B)$B!{K-ED(B $BK`M};R(B$B!&(B $B5\T"(B $B3(M}F`(B$B!&(B ($B@5(B)$BC+8}(B $B0iM:(B | Alkaline solution CO2 capture CaCO3
| P |
492 | $B936]@-J,;R=$>~$K$h$k5U?;F)(B(RO)$BKl$N%P%$%*%U%!%&%j%s%0M^@)(B ($B?@8MBg1!2J5;%$%N%Y(B/$B@hC$B!&(B ($B@5(B)$B?7C+(B $BBn;J(B$B!&(B ($B@5(B)$BCf@n(B $B7I;0(B$B!&(B ($B?@8MBg@hC$B!&(B ($B?@8MBg1!9)(B/$B@hC>2,(B $B=_(B$B!&(B ($BD9@%;:6H(B) $BC+(B $B90;V(B$B!&(B ($BF`NI@hC$B!&(B ($B?@8MBg1!9)(B/$B@hC>;3(B $B=(?M(B$B!&(B ($B?@8MBg1!2J5;%$%N%Y(B/$B@hC | fouling RO antimicrobial
| P |
495 | $B%7%j%1!<%H%J%N%7!<%H@QAXKl$N:n@=$H%J%N_I2aFC@-$NI>2A(B ($B?@8MBg2J5;%$%N%Y(B/$B@hC$B!&(B ($B@5(B)$BCf@n(B $B7I;0(B$B!&(B ($B@5(B)$B?7C+(B $BBn;J(B$B!&(B ($B?@8MBg1!9)(B/$B@hC>2,(B $B=_(B$B!&(B ($B@5(B)$B?@Hx(B $B1Q<#(B$B!&(B ($BF|;:2=3X(B) ($BK!(B)$BKL@n(B $BM5>f(B$B!&(B ($BK!(B)$B9b7'(B $B5*G7(B$B!&(B ($B?@8MBg1!9)(B/$B@hC>;3(B $B=(?M(B$B!&(B ($B?@8MBg2J5;%$%N%Y(B/$B@hC | membrane nanofiltration nanosheet
| P |
522 | TiO2$B%J%N:Y9&$K$*$1$kFC@-$N0[$J$kM-5!MOG^J,;R$NF)2a%7%_%e%l!<%7%g%s(B ($B?@8MBg1!2J5;%$%N%Y(B/$B@hC$B!&(B ($B@5(B)$B5H2,(B $BJ~5W(B$B!&(B ($B@5(B)$BCf@n(B $B7I;0(B$B!&(B ($B@5(B)$B?7C+(B $BBn;J(B$B!&(B ($B?@8MBg1!9)(B/$B@hC$B!&(B ($B@5(B)$B>>2,(B $B=_(B$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B | NEMD Organic solvent Nanopores
| P |
528 | $B3h@-%(%9%F%kK!$K$h$k@5?;F)Kl$NI=LL2~4+$BAK;_@-I>2A(B ($B?@8MBg1!2J5;%$%N%Y(B/$B@hC$B!&(B ($B?@8MBg1!9)(B/$B@hC$B!&(B ($B?@8MBg1!2J5;%$%N%Y(B/$B@hC$B!&(B ($B@5(B)$BCf@n(B $B7I;0(B$B!&(B ($B?@8MBg1!9)(B/$B@hC>2,(B $B=_(B$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B$B!&(B ($B?@8MBg1!2J5;%$%N%Y(B/$B@hC | Forward osmosis membrane Polyamide ammonium
| P |
533 | Effect of toluene vapor modification on gas separation properties for carbon molecular sieve membranes ($B;38}Bg1!AO@.2J3X(B) ($B3X(B)$B!{(BNie Jing$B!&(B $B5H_7(B $BE5??(B$B!&(B ($B@5(B)$BEDCf(B $B0l9((B | Carbon molecular sieve membranes Pyrolysis Gas separation
| P |
535 | $B%7%j%k2=%<%*%i%$%H$rMQ$$$?(BMMM$B$N:n@=$H%,%9F)2aJ,N%FC@-(B ($B;38}Bg1!AO@.2J3X(B) ($B3X(B)$B!{:#B<(B $BM*;K(B$B!&(B Liu Yongsheng$B!&(B ($B@5(B)$BEDCf(B $B0l9((B | sililated zeolite particles mixed matrix membranes gas separation
| P |
537 | $BB?9& ($B;38}Bg1!AO@.2J3X(B) ($B3X(B)$B!{2,ED(B $BIw2m(B$B!&(B ($B3X(B)Nie Jing$B!&(B ($B@5(B)$B4nB?(B $B1QIR(B$B!&(B ($B@5(B)$BEDCf(B $B0l9((B$B!&(B ($BEl%l@hC<:`NA8&(B) ($BK!(B)$B?{C+(B $BGnG7(B$B!&(B ($BK!(B)$B;086(B $B?r98(B$B!&(B ($BK!(B)$B6aF#(B $BBg(B$B!&(B ($BK!(B)$B;32<(B $BM4$B!&(B ($BK!(B)$BLpGj(B $BF`Jf;R(B | Porous carbon support Carbon molecular sieve membrane wood tar
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541 | $BBg5$$+$i$N;@AGIY2=6u5$D>@\@=B$%W%m%;%9$NDs0F$H%(%M%k%.!2A(B ($BL>Bg(B) ($B3X(B)$B!{>.NS(B $B=Y2p(B$B!&(B ($B@5(B)$BJ!K\(B $B0l@8(B$B!&(B ($B3$(B)Choi Cheolyong$B!&(B ($B@5(B)$BD.ED(B $BMN(B$B!&(B ($B@5(B)$BB'1J(B $B9TMG(B | Oxygen-enriched combustion Process simulation Air separation
| P |
550 | T$B;z9gN.$rJ#?tMxMQ$7$?%9%i%0N.$N:.9gB%?J$HCj=PFC@-$X$N1F6A(B ($B2,;3Bg1!4D@8(B) ($B3X(B)$B!{2.Ln(B $BN4;K(B$B!&(B ($B@5(B)$BEgFb(B $B$B!&(B ($B7DXfBgM}9)(B) ($B@5(B)$BF#2,(B $B:;ET;R(B$B!&(B ($B@5(B)$B;{:d(B $B9(0l(B$B!&(B ($B2,;3Bg1!4D@8(B) ($B@5(B)$BLZB<(B $B9,7I(B | slug flow mixing extraction
| P |
623 | $B%a%A%k%(%9%F%k4p$rM-$9$k%8%"%_%s$+$i$J$k%]%j%"%_%I(BNF$BKl$KBP$9$k%"%k%+%j=hM}$N1F6A(B ($B?.=#Bg1!AmM}9)(B) ($B3X(B)$B!{EZED(B $BMNG7(B$B!&(B ($B?.=#Bg(BRISM/$B?.=#Bg1!AmM}9)(B) ($B@5(B)$B:4Gl(B $BBgJe(B$B!&(B ($B7*ED9)6H(B) ($B@5(B)$B@n>!(B $B9'Gn(B$B!&(B ($BK!(B)$BF#B<(B $BPR(B$B!&(B ($B?.=#Bg1!AmM}9)(B) $B1|B<(B $B9,5W(B | nanofiltration polyamide interfacial polymerization
| P |
644 | $BB?9&@-%]%j%1%H%sKl$N9=B$@)8f$H(BW/O$B%(%^%k%7%g%sJ,N%@-G=$NI>2A(B ($B?@8MBg1!9)(B/$B@hC$B!&(B ($B?@8MBg1!2J5;%$%N%Y(B/$B@hC$B!&(B ($B@5(B)$B?7C+(B $BBn;J(B$B!&(B ($B?@8MBg1!9)(B/$B@hC$B!&(B ($B@5(B)$B>>2,(B $B=_(B$B!&(B ($B?@8MBg1!2J5;%$%N%Y(B/$B@hC$B!&(B ($B?@8MBg1!9)(B/$B@hC$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B | membrane polyketone emulsion
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698 | $B6&=E9gBN9bJ,;RKl$NF)2a@-$X$N9bJ,;R9=B$0MB8@-$NJ,;R%7%_%e%l!<%7%g%s$K$h$k2r@O(B ($B:eBg1!4p9)(B) ($B@5(B)$B!{>.Eh(B $B=(OB(B$B!&(B $BH>ED(B $BOBLi(B$B!&(B ($B@5(B)$B;3ED(B $B0lM:(B$B!&(B ($B@5(B)$B>>NS(B $B?-9,(B | membrane permeation copolymer membrane molecular simulation
| P |
782 | TiO2-Al2O3-$BM-5!%-%l!<%HG[0L;RJ#9gKl$N:n@=$H$=$NFC@-I>2A(B ($B?@8MBg2J5;%$%N%Y(B/$B@hC$B!&(B ($B@5(B)$B5H2,(B $BJ~5W(B$B!&(B ($B@5(B)$BCf@n(B $B7I;0(B$B!&(B ($B@5(B)$B?7C+(B $BBn;J(B$B!&(B ($B?@8MBg1!9)(B/$B@hC>2,(B $B=_(B$B!&(B ($B@5(B)$B?@Hx(B $B1Q<#(B$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B | titania-alumina membrane organic chelate ligand
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835 | UiO-66-NH2$BKl$N@.D9$K9g@.>r7o$,5Z$\$91F6A(B ($B4tIlBg9)(B) ($B3X(B)$B!{5.Eg(B $B$^$_(B$B!&(B ($B4tIlBg1!<+(B) $BGO^<(B $B9aF`(B$B!&(B ($B4tIlBg9)(B) ($B@5(B)$B5\K\(B $B3X(B$B!&(B ($B4tIlBg9bEy8&(B) ($B@5(B)$B6a9>(B $BLwB'(B$B!&(B ($B4tIlBg9)(B) ($B@5(B)$B>e5\(B $B@.G7(B | UiO-66-NH2 membrane synthesis conditions
| P |
838 | $BJ,;R%7%_%e%l!<%7%g%s$K$h$k%<%*%i%$%HKl$K$*$1$k%*%l%U%#%s(B/$B%Q%i%U%#%s:.9g%,%9F)2a@-$K5Z$\$96bB0%+%A%*%s$N1F6A$N8!F$(B ($B?@8MBg1!2J5;%$%N%Y(B) ($B3X(B)$B!{?"ED(B $B7IJ8(B$B!&(B ($B?@8MBg1!2J5;%$%N%Y(B/$B@hC$B!&(B ($B@5(B)$BCf@n(B $B7I;0(B$B!&(B ($B@5(B)$B?7C+(B $BBn;J(B$B!&(B ($B?@8MBg1!9)(B/$B@hC$B!&(B ($B@5(B)$B>>2,(B $B=_(B$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B | Hydrocarbon separation Zeolite Molecular dynamics
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850 | Dry gel conversion$BK!$rMQ$$$?(Bpure-silica *BEA$B7?%<%*%i%$%HKl9g@.$K$*$1$k=$N1F6A(B ($B4tIlBg1!<+A3(B) ($B3X(B)$B!{Mn9g(B $B42$B!&(B ($BD+F|Bg;u(B) ($B@5(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) $B1|Ln(B $BBsLi(B$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 ($B4tIlBg9bEy8&(B) ($B@5(B)$B6a9>(B $BLwB'(B | *BEA type zeolite membrane dry gel conversion silica support
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852 | $B%?%s%Q%/e$NCf4V?e$N%@%$%J%_%/%9(B ($B9)3X1!Bg@h?J9)(B) ($B3X(B)$B!{W"_7(B $B;KLi(B$B!&(B $B?\ED(B $B$"$+$M(B$B!&(B $B2,K\(B $B=S$B!&(B ($B@5(B)$B5\@n(B $B2mLp(B$B!&(B ($B@5(B)$B9b1)(B $BMN=<(B | Molecular dynamics Intermediate water Fouling
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859 | $BJ,;RG'<1NN0h$K%R%9%A%8%sG[Ns$rM-$9$k@\Ce@-%Z%W%A%I$rMQ$$$?J,;R%$%s%W%j%s%HK!$K$h$k(BPd$BA*BrE*5[CeBN$ND4@=(B ($B=)EDBg1!M}9)(B) ($B3X(B)$B!{D9;3(B $BOB42(B$B!&(B ($B=)EDBgCOJ}AO@8%;(B) Morlu GF Stevens$B!&(B ($B=)EDBg1!M}9)(B) ($B@5(B)$B2#ED(B $BAa4u(B$B!&(B ($B=)EDBg(B) ($B@5(B)$B8eF#(B $BLT(B | molecular imprinting adhesive peptides adsorption carrier
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880 | Preparation of electrospun nanofibrous membrane for recovery and concentration of extracellular polymeric substances from excess sludge ($BCf9qKL7zBg(B) ($BCf(B)$B!{4Z(B $B2BpC(B$B!&(B ($B3$(B)$BAb(B $BC#7<(B$B!&(B 郝 $B6GCO(B | excess sludge extracellular polymer substances recovery
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