SCEJ

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$B$3$NJ,N`$G$h$/;H$o$l(B
$B$F$$$k%-!<%o!<%I(B		$B%-!<%o!<%I(B$B
membrane5$B7o(B*
Nanofiltration4$B7o(B*
Silica membrane4$B7o(B*
Molecular Dynamics4$B7o(B*
membrane separation3$B7o(B*
ionic liquid3$B7o(B*
Separation3$B7o(B*
CO2 separation3$B7o(B*
Membrane reactor2$B7o(B
Fouling2$B7o(B
Low-fouling2$B7o(B
Pervaporation2$B7o(B
zeolite2$B7o(B
Reverse osmosis2$B7o(B
Polyamide2$B7o(B
organosilica membrane2$B7o(B
forward osmosis2$B7o(B
NF membrane1$B7o(B

$B$BHV9f(B$B9V1iBjL\!?H/I=$B%-!<%o!<%I(B$BH/I=7A<0(B
11$B%*%k%,%N%7%j%+Kl$N?eF)2aFC@-$H%b%G%k2r@O!A5U?;F)!&?;F)5$2=!&>x5$F)2a!A(B
($B9-Bg1!9)(B) ($B3X(B)$B!{?9;3(B $B65MN(B$B!&(B ($B9-Bg1!@h?JM}9)(B) ($B@5(B)$BD9_7(B $B425,(B$B!&(B ($B@5(B)$B6b;X(B $B@58@(B$B!&(B ($B@5(B)$BETN1(B $BL-N;(B		Water
Permeation model
Organosilica membrane
O
22Enhancing the H2-permselectivity of a composite SiO2-ZrO2 membrane via organic ligand carbonization pore volume control
(Hiroshima U.) ($B@5(B)$B!{(BLawal Sulaiman$B!&(B ($B@5(B)Kanezashi Masakoto$B!&(B ($B@5(B)Nagasawa Hiroki$B!&(B ($B@5(B)Tsuru Toshinori		Acetylacetone
Silica-zirconia
Carbonization
O
66$BKlJ,N%$*$h$S1v@O$K$h$k%U%#%3%S%j%W%m%F%$%s@:@=%W%m%;%9$N@_7W(B
($B:42lBg1!9)(B) ($B3X(B)$B!{F|$B!&(B ($B:42lBgM}9)(B) ($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 $B1Q9'(B		phycobiliprotein
Crossflow filtration
purification
O
89$B%7%j%+%S!<%:$rF3F~$7$?B?9&
($BFAEgBg1!AO@.2J3X(B) ($B3X(B)$B!{EDCf(B $B@i2l(B$B!&(B ($BFAEgBg1!		Dense Pd membrane on porous SUS tube
Vacuum-assisted electroless plating
Spherical silica particle
P
91$BDcG;EY(BVOC$B2s<}$G$N%$%*%s1UBN%*%k%,%N%7%j%+Kl$NF)2aFC@-(B
($BL>9)Bg1!9)(B) ($B3X(B)$B!{2#0f(B $B0l51(B$B!&(B ($B@5(B)$BW"ED(B $BM:0lO/(B		organosilica membrane
ionic liquid
VOC recovery
P
118$BFs;@2=C:AGJ,N%$N$?$a$N(BTetra-PEG$B%$%*%s%2%kGvKl$N3+H/(B
($B?@8MBg1!9)(B) ($B3X(B)$B!{zs@n(B $B=cJ?(B$B!&(B ($B@5(B)$B?@Hx(B $B1Q<#(B$B!&(B ($B@5(B)$B>>2,(B $B=_(B$B!&(B ($B?@8MBg1!%$%N(B) ($B@5(B)$B5H2,(B $BJ~5W(B$B!&(B ($B@5(B)$BCf@n(B $B7I;0(B$B!&(B ($B?@8MBg1!9)(B) ($B@5(B)$B>>;3(B $B=(?M(B		carbon dioxide separation
ionic liquid
gel membrane
P
119$BI=LL%0%i%U%H=E9gK!$rMQ$$$?Dc%U%!%&%j%s%05U?;F)Kl$N3+H/(B
($B9)3X1!Bg@h?J9)(B) ($B3X(B)$B!{2CF#(B $B6&@8(B$B!&(B ($B7*ED9)6H(B) ($B@5(B)$B@n>!(B $B9'Gn(B$B!&(B ($B9)3X1!Bg@h?J9)(B) ($B@5(B)$BCfHx(B $B??0l(B$B!&(B Wang Xiao-Lin$B!&(B ($B@5(B)$B@V>>(B $B7{		low-fouling
RO membrane
surface modification
P
121NIPS$BK!$rMQ$$$?(Bpoly(2-methoxyethyl acrylate)$B%V%l%s%I(BPVDF$BKl$N3+H/(B
($B9)3X1!Bg@h?J9)(B) ($B3X(B)$B!{BgLn(B $B@?Lo(B$B!&(B ($B@5(B)$BCfHx(B $B??0l(B$B!&(B Wang Xiao-Lin$B!&(B ($B@5(B)$B@V>>(B $B7{		NIPS
Low-fouling
PolyMEA
P
122$B%P%$%*%,%9$+$i9b=cEY?eAG$r@=B$$9$k%7%j%+KlH?1~4o$N3+H/(B
($B9)3X1!Bg@h?J9)(B) ($B3X(B)$B!{:#B<(B $B7=8c(B$B!&(B ($B@5(B)$BCfHx(B $B??0l(B$B!&(B Wang Xiao-Lin$B!&(B ($B@5(B)$B@V>>(B $B7{		membrane reactor
silica membrane
steam reforming
P
127Water Flux Enhancement of PVDF Membrane by a Facile Coating Method for Vacuum Membrane Distillation
(Kobe U.) ($B@5(B)$B!{(BLi Zhan$B!&(B ($B3X(B)Zhang Pengfei$B!&(B ($B@5(B)Guan Kecheng$B!&(B ($B@5(B)Yoshioka Tomohisa$B!&(B ($B@5(B)Matsuyama Hideto		membrane preparation
membrane modification
vacuum membrane distillation
O
128Novel method to immobilize zwitterionic materials onto PVDF hollow fiber membrane surface
(Kobe U.) ($B3X(B)$B!{(BZhang Pengfei$B!&(B ($B@5(B)Saeid Rajabzade$B!&(B ($B@5(B)Matsuyama Hideto		PVDF hollow fiber modification
zwitterionic copolymer
anti-fouling
P
129Construction polyphenol microstructure coatings for oil-in-water emulsion separation
(Kobe U.) ($B3X(B)$B!{(BJia Yuandong$B!&(B ($B@5(B)Guan Kecheng$B!&(B ($B@5(B)Matsuyama Hideto		nanostructures
superwetting membranes
oil/water separation
P
141$B%T%e%"%7%j%+(BCHA$BKl$K$h$kM-5!%O%$%I%i%$%IJ,2rMQKlH?1~4o$N3+H/(B
($B$B!&(B $B9b;3(B $BBg;K(B$B!&(B Figueiredo Gabriel Gama da Silva$B!&(B ($B3X(B)$B@P0f(B $B9nE5(B$B!&(B ($B=;M'EE9)(B) $B>.LnLZ(B $BGl70(B$B!&(B $B1|Ln(B $BBsLi(B$B!&(B $BI6;3(B $BGn6)(B$B!&(B $B@P@n(B $B??Fs(B		Pure silica CHA membrane
Organic hydride
Membrane reactor
O
148Development of a high CO2 permeance composite membrane with an ion gel layer
(Kobe U.) ($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
Composite membrane
CO2 separation
O
166$B
($B$B!&(B ($B		Silica membrane
Chemical vapor deposition
Membrane separation
O
235High performance polyamide nanofiltration membranes enabled by Ag-based nanocapsule-regulated interfacial polymerization process
(Kobe U.) ($B3$(B)$B!{(BIstirokhatun Titik$B!&(B ($BCf(B)Lin Yuqing$B!&(B ($B@5(B)Matsuyama Hideto		silver
nanofiltration
antibiofouling
P
236Graphene quantum dots engineered thin-film nanocomposite membrane for high-performance organic solvent nanofiltration
(Kobe U.) ($B3X(B)$B!{(BShen Qin$B!&(B ($BCf(B)Lin Yuqing$B!&(B ($B@5(B)Matsuyama Hideto		Graphene quantum dots
thin-film nanocomposite membrane
organic solvent nanofiltration
P
237$B%"%s%A%U%!%&%j%s%0KlI=LL@_7W$K8~$1$?%I!<%Q%_%s?;DR7?@:L)=$>~K!$N9=C[$HFC@-I>2A(B
($BEl9)Bg2=@88&(B) ($B3X(B)$B!{7*86(B $BM:Bg(B$B!&(B ($B@5(B)$BBg$B!&(B ($B@5(B)$B;38}(B $BLT1{(B		antifouling
QCM-D
dopamine
P
238Zwitterionic copolymer interlayer regulated nanofiltration membrane
(Kobe U.) ($B3X(B)$B!{(BSong Qiangqiang$B!&(B ($B@5(B)Matsuyama Hideto		Nanofiltration
Desalination
P
248Network pore engineering of non-porous bis(triethoxysilyl)propane (BTESP) membranes via fluorine doping and gas permeation properties
(Hiroshima U.) ($B3X(B)$B!{(BIkram Rana$B!&(B ($B@5(B)Kanezashi Masakoto$B!&(B ($B@5(B)Nagasawa Hiroki$B!&(B ($B@5(B)Tsuru Toshinori		Nonporous Organosilica; Bis(triethoxysily)propane
Fluorine doping; Network pore tuning
O
297$B%<%*%i%$%HKl$rMxMQ$7$?%(%9%F%k8r49H?1~$NB.EY2r@O(B
($B;:Am8&(B) ($B@5(B)$B!{CSED(B $BJb(B$B!&(B ($B@5(B)$BD9C+@n(B $BBY5W(B		Zeolite membrane
methanol removal
transesterification reaction
O
311$B7W;;2=3X$K$h$k3F
($B9)3X1!Bg@h?J9)(B) ($B3X(B)$B!{?\ED(B $B$"$+$M(B$B!&(B ($B3X(B)$BW"_7(B $B;KLi(B$B!&(B ($B@5(B)$B5\@n(B $B2mLp(B$B!&(B ($B@5(B)$B9b1)(B $BMN=<(B		fouling
Molecular dynamics
Extracellular polymeric substances
P
319$B%"%_%s4^M-%2%kN3;RKl$rEk:\$7$?(BCO2$BJ,N%AuCV$K$h$k(BCO2$BG;=L(B
($B6eBg(B) ($B@5(B)$B!{@1Ln(B $BM'(B$B!&(B ($B@5(B)$B0Bi:(B $BfFGO(B$B!&(B $BCSED(B $BM%;R(B$B!&(B $B:#B<(B $BOB;K(B$B!&(B $BKY0f(B $BNC2m(B$B!&(B ($BF|K\C:AG=[4D%i%\(B) $B;32<(B $BCN7C(B$B!&(B ($B6eBg(B) $BEOn5(B $BLT(B$B!&(B ($B3X(B)$BK\ED(B $BN5B@O/(B$B!&(B ($BEl9)Bg(B) ($B@5(B)$B>.6L(B $BAo(B$B!&(B ($B6eBg(B) ($B@5(B)$BC+8}(B $B0iM:(B$B!&(B ($B@5(B)$B;01:(B $B2B;R(B		CO2 separation
gel particles
membrane
O
339$B%8%"%_%s$X$N%+%k%\%-%74p$NF3F~$K$h$k9bF)?e@-%]%j%"%_%I%J%N$m2aKl$N:n@=(B
($B?.=#Bg1!AmM}9)(B/$B?.=#Bg(BRISM) ($B@5(B)$B!{:4Gl(B $BBgJe(B$B!&(B ($B?.=#Bg1!AmM}9)(B) ($B3X(B)$BEZED(B $BMNG7(B$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 $B9,5W(B		nanofiltration
polyamide
interfacial polymerization
O
370$BKlI=LLJ,6K@-$,Cf4V?e$N@8@.$K5Z$\$91F6A(B : $B7W;;2=3X$K$h$k8!F$(B
($B9)3X1!Bg@h?J9)(B) ($B3X(B)$B!{1|4V(B $B9(Bg(B$B!&(B ($B3X(B)$BHu8}(B $BH;?M(B$B!&(B ($B3X(B)$BW"_7(B $B;KLi(B$B!&(B ($B@5(B)$B5\@n(B $B2mLp(B$B!&(B ($B@5(B)$B9b1)(B $BMN=<(B		Fouling
Intermediate Water
Molecular Dynamics
P
388$BM-5!%-%l!<%HG[0L;R(B(OCL)$B$rMQ$$$?(BTiO2-SiO2-OCL$BJ#9g?eAGJ,N%Kl$N3+H/(B
($B?@8MBg1!2J5;%$%N%Y(B) ($B3X(B)$B!{4\(B $B;^DE;R(B$B!&(B ($B?@8MBg9)(B) $BF#LZ(B $B9':H(B$B!&(B ($B?@8MBg1!2J5;%$%N%Y(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@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 $B=(?M(B		hydrogen
TiO2-SiO2
organic chelating ligand
P
395$B0[$J$k?eAG7k9g@-41G=4p$rM-$9$k(BUCST$B7?29EY1~Ez@-%$%*%s1UBN$NAjJ,N%5sF0(B
($B?@8MBg1!9)(B/$B@hC>2,(B $B=_(B$B!&(B ($B3X(B)$B85;3(B $B0&M|(B$B!&(B ($B@5(B)$B?@Hx(B $B1Q<#(B$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B		forward osmosis
ionic liquid
UCST phase separation
O
431Hybrid nickel-coordinated aminosilica membranes for the selective pervaporation of methanol: tuning coordinated structure by a variety of amine types
(Hiroshima U.) ($B3X(B)$B!{(BAnggarini Ufafa$B!&(B ($B@5(B)Nagasawa Hiroki$B!&(B ($B@5(B)Kanezashi Masakoto$B!&(B ($B@5(B)Tsuru Toshinori		amine-functionalized organosilica precursors
nickel-dopant
pervaporation
O
435$BCf6u;eKl$rMQ$$$??e=hM}$m2aAuCV$K$*$1$kN.F0FC@-$N%b%G%k2=(B
($B%@%$%;%k(B) ($B@5(B)$B!{;3ED(B $B9d;K(B$B!&(B ($BK!(B)$B9bHx(B $BfFB@(B		Modeling
simulation
water treatment filtration
O
451Forward osmosis thin film composite membrane surface modification using tris(2-aminoethyl)amine (TAEA) for enhanced ammonium recovery
(Kobe U.) ($B3$(B)$B!{(BLi Jing$B!&(B ($B@5(B)Gonzales Ralph Rolly$B!&(B ($B@5(B)Matsuyama Hideto		Foward Osmosis
Thin film composite membrane
Resource recovery
P
455Fabrication of micro-sized artificial oxygen carriers with tunable morphology by SPG membrane emulsification techniques
($BElBg1!9)(B) ($B3X(B)$B!{D%(B $Bc2LD(B$B!&(B ($BElBg1!0e(B) ($B3X(B)Arvind Singh Chandel$B!&(B $B5HED(B $B9(H~(B$B!&(B ($BElBg1!0e(B/$BElBg1!9)(B) ($B@5(B)$B0KF#(B $BBgCN(B		Microcapsule
Oxygen carrier
SPG membrane emulsification
P
475TiO2-ZrO2-$BM-5!%-%l!<%HG[0L;R(B(OCL)$BJ#9gKl$K$*$1$k%J%N_I2aFC@-$K5Z$\$9(BOCL$B$N1F6A(B
($B?@8MBg1!2J5;%$%N%Y(B/$B@hC$B!&(B ($B@5(B)$B5H2,(B $BJ~5W(B$B!&(B ($B@5(B)$BCf@n(B $B7I;0(B$B!&(B ($B@5(B)$B?7C+(B $BBn;J(B$B!&(B ($B?@8MBg@hC>2,(B $B=_(B$B!&(B ($B@5(B)$B?@Hx(B $B1Q<#(B$B!&(B ($B?@8MBg1!2J5;%$%N%Y(B/$B@hC>;3(B $B=(?M(B		TiO2-ZrO2
Organic solvent
OCL
P
482$B?75,$JO;J}>=7?;@2=%?%s%0%9%F%sKl$K$h$k%,%9J,N%$N2DG=@-D4::(B
($BL>BgL$Mh$B!&(B ($BL>Bg1!9)(B) $BOBED(B $B?5B@O:(B$B!&(B $BT";J(B $B42?M(B$B!&(B ($BL>Bg9)(B) $B;3ED(B $BM:B@(B$B!&(B ($BL>BgL$Mh		Hexagonal tungsten oxide
Membrane
Separation
O
509$BJ,;RF0NO3X%7%_%e%l!<%7%g%s$K$h$k5,B'@-!?%"%b%k%U%!%9;@2=%0%i%U%'%sKl$K$*$1$k5$BNF)2a5!9=$N2rL@(B
($B?@8MBg1!2J5;%$%N%Y(B/$B@hC$B!&(B ($B@5(B)$B5H2,(B $BJ~5W(B$B!&(B ($B@5(B)$BCf@n(B $B7I;0(B$B!&(B ($B@5(B)$B?7C+(B $BBn;J(B$B!&(B ($B?@8MBg1!9)(B/$B@hC>2,(B $B=_(B$B!&(B ($B@5(B)$B?@Hx(B $B1Q<#(B$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B		Graphene oxide
Molecular dynamics simulation
Gas permeation
P
518$B?;F)05Jd=u5U?;F)$rMQ$$$?1v2=%"%s%b%K%&%`?eMO1UJ,N%%W%m%;%9$N9=C[(B
($B;37ABg1!M}9)(B) ($B3X(B)$B!{=)85(B $BNIM4(B$B!&(B ($B3X(B)$BJF;3(B $B=(:H(B$B!&(B ($B;37ABg9)(B) $B>.3^86(B $BM35((B$B!&(B ($B;37ABg1!M}9)(B) ($B@5(B)$BNkLZ(B $BBYI'(B$B!&(B ($B@5(B)$BCf4d(B $B>!(B$B!&(B ($B@5(B)$B>>ED(B $B7=8g(B		Reverse Osmosis
Separation
Membrane
P
532Silver dissolution from Ag-TiO2 membrane in saline condition
(Yamaguchi U.) ($B3X(B)$B!{(BChe Abdul Rahim Azzah Nazihah$B!&(B Maestre Sergio$B!&(B ($B@5(B)Kumakiri Izumi		Photocatalyst
Silver nanoparticle
Dissolved organics
O
568PVDF$BCf6u;eKl$rMxMQ$7$?(Bp-$B%K%H%m%U%'%N!<%k$NKlCj=P(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>2,(B $B=_(B$B!&(B($B?@8MBg1!2J5;%$%N%Y(B/$B@hC<%P%$%*9)3X%;(B) ($B@5(B)$BO!>B(B $B@?5W!&(B ($B?@8MBg1!2J5;%$%N%Y(B) $BHV>l(B $B?r90(B$B!&(B $B1@KL(B $BNCB@(B$B!&(B $B>.NS(B $BM%??(B$B!&(B ($B?@8MBg%*!<%W%s%$%N%Y(B) $B0B;^(B $B$B!&(B ($B?@8MBg1!9)(B/$B@hC$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B$B!&(B ($B?@8MBg1!2J5;%$%N%Y(B/$B@hC		Hollow fiber membrane
extraction
p-nitrophenol
P
589CO2$BJ,N%$K$*$1$kMWAG%W%m%;%9$NJ,N%@-G=$H7P:Q@-$K4X$9$k8!F$(B
($B;37ABg1!M}9)(B) ($B3X(B)$B!{F#ED(B $BfF(B$B!&(B ($B;37ABg9)(B) $BF#0f(B $BM[B@(B$B!&(B ($B;37ABg1!M}9)(B) ($B@5(B)$BCf4d(B $B>!(B$B!&(B ($B@5(B)$B>>ED(B $B7=8g(B		Separation
Membrane
Carbon dioxide
P
590$B%U%CAG4^M-%]%j%^!<$N%3!<%F%#%s%0$K$h$kJ#9gKl$N:n@=$H%J%N$m2aJ,N%(B
($B?@8MBg9)(B/$B@hC.ED(B $BM*2p(B$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>2,(B $B=_(B$B!&(B ($B@5(B)$B?@Hx(B $B1Q<#(B$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B		Fluorine contain polymer
NF membrane
organic solvent separation
P
593$B%+!<%\%s%j%5%$%/%k$K8~$1$?M-5!1UBN5U?;F)J,N%$N2DG=@-(B
($B$B!&(B ($B3X(B)$B@P0f(B $B9nE5(B$B!&(B ($B		Silica membrane
Reverse osmosis
Organic liquids
P
594$B?eAGF)2a%7%j%+Kl$N?e>x5$BQ5W@-6/2=(B
($B$B!&(B ($B3X(B)$B@P0f(B $B9nE5(B$B!&(B ($B		Silica membrane
Steam durability
Hydrogen permeance
P
597$B9b299b05?e>x5$J70O5$2<$K$*$1$k(BNa-ZSM-5$B$NBQ5W@-$N8!F$(B
($BAaBg@h?JM}9)(B) ($B3X(B)$B!{:dFb(B $BNI2p(B$B!&(B ($BAaBg%J%N%i%$%U(B) ($B@5(B)$B$B!&(B($BAaBg@h?JM}9)(B/$BAaBg%J%N%i%$%U(B/$BAaBgM}9)Am8&(B) ($B@5(B)$B>>J}(B $B@5I'(B		zeolite
membrane separation
P
605$B>.7?4I>uH?1~4o$rMQ$$$?(Bsilicalite-1$BKl$N?WB.9g@.$K$*$1$k9g@.>r7o$N1F6A(B
($B4tIlBg1!<+(B) ($B3X(B)$B!{4!@n(B $BM5B@(B$B!&(B ($B4tIlBg9)(B) ($B@5(B)$B5\K\(B $B3X(B$B!&(B ($B;:Am8&(B) ($B@5(B)$BD9C+@n(B $BBY5W(B$B!&(B ($B4tIlBg9bEy8&(B) ($B@5(B)$B6a9>(B $BLwB'(B$B!&(B ($B4tIlBg9)(B) ($B@5(B)$B>e5\(B $B@.G7(B		Rapid synthesis
Silicalite-1 membrane
Pervaporation
P
606Fischer-Tropsch$B9g@.$KBP$9$k%<%*%i%$%HKl$N1~MQ(B
($BAaBg@h?JM}9)(B) ($B3X(B)$B!{@i86(B $BD>?M(B$B!&(B ($BAaBg%J%N%i%$%U(B) ($B@5(B)$B$B!&(B (ENEOS) ($BK!(B)$B>>K\(B $BN4Li(B$B!&(B ($BK!(B)$B?y1:(B $B9T42(B$B!&(B ($BK!(B)$BD+Ln(B $B9d(B$B!&(B($BAaBg@h?JM}9)(B/$BAaBg%J%N%i%$%U(B/$BAaBgM}9)Am8&(B) ($B@5(B)$B>>J}(B $B@5I'(B		Fischer-Tropsch synthesis
membrane
ZSM-5
P
621$B%<%*%i%$%HKl$N@5?;F)FC@-$K4X$9$k8!F$(B
($BAaBg@h?JM}9)(B) ($B3X(B)$B!{LnB<(B $BM5B@(B$B!&(B ($BAaBg%J%N%i%$%U(B) ($B@5(B)$B$B!&(B ($BAaBg@h?JM}9)(B/$BAaBgM}9)Am8&(B) ($B@5(B)$B>>J}(B $B@5I'(B		zeolite
membrane separation
forward osmosis
P
632$B%J%N$m2a$K$h$k%"%s%b%K%"J,N%2aDx$NHsJ?9UJ,;RF0NO3X7W;;(B
($B9)3X1!Bg@h?J9)(B) ($B3X(B)$B!{Hu8}(B $BH;?M(B$B!&(B $BHDAR(B $BBs3$(B$B!&(B ($B3X(B)$BW"_7(B $B;KLi(B$B!&(B ($B@5(B)$B5\@n(B $B2mLp(B$B!&(B ($B@5(B)$B9b1)(B $BMN=<(B		Nanofiltration
Diffusion
Non-equilibrium Molecular Dynamics
P
644$BL)EY:9$r?d?JNO$H$9$k%]%j%"%_%IKl$K$*$1$k=`HsJ?9UF)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 ($B@5(B)$B>>2,(B $B=_(B$B!&(B ($B@5(B)$B?@Hx(B $B1Q<#(B$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B$B!&(B ($B7*ED9)6H(B) ($BK!(B)$BF#B<(B $BPR(B$B!&(B ($B@5(B)$B@n>!(B $B9'Gn(B		Molecular dynamics
Polyamide
Quasi-nonequilibrium permeation simulation
P
650$B7W;;2=3X$rMQ$$$?(BMixed matrix$BKl$K$*$1$k(BCO2$BF)2a5!9=$N2rL@(B
($B9)3X1!Bg1!9)(B) ($B3X(B)$B!{W"_7(B $B;KLi(B$B!&(B ($B9)3X1!Bg@h?J9)(B) ($B@5(B)$B5\@n(B $B2mLp(B$B!&(B ($B@5(B)$B9b1)(B $BMN=<(B		Mixed matrix membrane
CO2 separation
Non equibrium molecular dynamics
O
662$BHs6K@-MOG^$NJ,;6!&6E=85sF0$,%"%/%j%l!<%HAG:`$NBQ%U%!%&%j%s%0@-G=$KM?$($k1F6A(B:$B7W;;2=3XE*2r@O(B
($BL>9)Bg1!9)(B) ($B@5(B)$B!{Fn1@(B $BN<(B$B!&(B ($B3X(B)$BCfED(B $B0T?a(B$B!&(B $B>>2,(B $BBs3$(B$B!&(B ($B@5(B)$B4dED(B $B=$0l(B		Acrylate Materials
Antifouling Properties
Molecular Dynamics
O
680Effect of toluene vapor concentration on gas separation properties of carbon molecular sieve membranes modified by toluene CVD method
($B;38}Bg1!AO@.(B) ($B3X(B)$B!{(BNie Jing$B!&(B ($B@5(B)$BEDCf(B $B0l9((B		Carbon molecular sieve membranes
Toluene vapor modification
Gas separation
P
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(C) 2022 $B8x1W
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