SCEJ

$B2=3X9)3X2q(B $BBh(B81$BG/2q(B (2016)

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$B:G=*99?7F|;~!'(B2016-05-19 11:21:01

$B$3$NJ,N`$G$h$/;H$o$l(B
$B$F$$$k%-!<%o!<%I(B		$B%-!<%o!<%I(B$B
membrane10$B7o(B***
Zeolite7$B7o(B**
Zeolite membrane6$B7o(B**
microfiltration5$B7o(B*
Gas separation5$B7o(B*
forward osmosis5$B7o(B*
ionic liquid4$B7o(B*
gas permeation4$B7o(B*
Pervaporation4$B7o(B*
Pressure retarded osmosis4$B7o(B*
membrane reactor3$B7o(B*

$B$BHV9f(B$B9V1iBjL\!?H/I=$B%-!<%o!<%I(B$BH/I=7A<0(B
36$BM-5!MOG^$r%I%m!
($BEl$B!&(B $B:4Ln(B $B7rFs(B$B!&(B ($B@5(B)$BNkLZ(B $B><;R(B$B!&(B ($B@5(B)$B:#ED(B $BIR90(B		Forward Osmosis
Draw Solution
P
116$BG.2=3X?eAG@=B$$N$?$a$NJ|
($B$B!&(B ($B3X(B)$B>.J?(B $B3Y=((B$B!&(B ($B3X(B)$BBg1:(B $B6W2;(B$B!&(B ($B3X(B)$BCSED(B $BJb(B$B!&(B $BL>2E(B $BBY;K(B$B!&(B $B@>Eh(B $BM[G7(B$B!&(B $B:#NS(B $B?50lO:(B$B!&(B ($B86;RNO5!9=(B) $B_7ED(B $B??0l(B$B!&(B $BH,4,(B $BE0Li(B$B!&(B ($B@5(B)$BEDCf(B $B?-9,(B$B!&(B $B5WJ](B $B??<#(B		thermochemical water splitting IS process
ion exchange membrane
Bunsen reaction
O
117$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 $B4490(B		counter diffusion CVD method
silica hybrid membranes
alkaline particles
P
118$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 ($B		MFI zeolite membrane
porous silica substrate
organic hydrides
P
143$BJ?Kl7?(BMBR$B$NGx5$$K$h$k@v>t8z2L$N2r@O(B
($BEl%l(B) ($B@5(B)$B!{2,K\(B $B595-(B$B!&(B ($BK!(B)$B2CF#(B $B7E(B$B!&(B ($B@5(B)$BKL=P(B $BM-(B$B!&(B ($B@5(B)$BLZB<(B $B>-90(B		MBR
shear stress
Particle Image Velocimetry(PIV)
O
150$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 $BLP(B		Palladium thin membrane
Porous SUS tube support
Double intermediate layers
P
166$BEE5$%(%M%k%.!<$rD>@\MxMQ$9$k%,%9J,N%MQB?9&BN$N:n@=(B
($BEl9)Bg1!(B) ($B@5(B)$B!{0kIt(B $BIR9((B$B!&(B $B9b66(B $B9(OB(B$B!&(B $BC+K\(B $BNgH~(B$B!&(B $B>>2<(B $B>M;R(B$B!&(B $BCfEg(B $B>O(B		nafion
electric chemistry
hydrogen separation
O
172$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 $B>O(B		porous membrane
CO2 separation
ceramics
P
174CO2$B1~Ez@-%]%j%^!<$N?eOB5sF0$HB&:?4VAj8_:nMQ$K4X$9$kJ,;R%7%_%e%l!<%7%g%s(B
($BL>9)Bg(B) ($B3X(B)$B!{@pED(B $BFW;K(B$B!&(B ($B@5(B)$BFn1@(B $BN<(B$B!&(B ($B@5(B)$B4dED(B $B=$0l(B$B!&(B ($B@5(B)$B?9(B $B=(		CO2 switchable
LCST
molecular dynamics
P
179$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 $BOB@8(B		Ionic liquid
Ethanol
Pervaparation
P
202$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 $B=(		all silica zeolite
zeolite membrane
pervaporation
P
222$B:Y9&=
($BF|K\FC$B!&(B ($B@5(B)$B3aC+(B $B>;90(B$B!&(B ($B@5(B)$B0KF#(B $B@5Li(B		Hydrogen
membrane
palladium
O
251$B9b6/EY!&Dc%U%!%&%j%s%0Cf6u;eKl$N3+H/$HKlMxMQH/9Z%W%m%;%9$X$NE83+(B
($BEl%l(B) ($BK!(B)$B!{>.NS(B $BFX(B$B!&(B ($BK!(B)$BIpFb(B $B5*9@(B$B!&(B ($BK!(B)$BH+J?(B $BCR;R(B$B!&(B ($BK!(B)$B<*DM(B $B9'(B$B!&(B ($BK!(B)$BLZB<(B $B>-90(B		hollow fiber membrane
fermentation
O
259$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 $B1QIR(B		Zeolite
membrane
gas separation
P
267$BHy:YAtN`$r@:L)$m2a$9$k:]$NKl4V:905$,Kl$N%U%!%&%j%s%08=>]$K5Z$\$91F6A(B
($BElKLBg1!(B) ($B3X(B)$B!{2#9B(B $B$^$I$J(B$B!&(B $BDi(B $B=Y(B$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 $B=(G7(B		microfiltration
microalgae
fouling
P
277Clear solution$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 $B1QIR(B		zeolite
membrane
pervaporation
P
280$B%j%0%K%s$rA06nBN$H$7$?C:AGKl$N%,%9F)2a@-G=$KM?$($kE:2CJ*$N8z2L(B
($B;38}Bg1!M}9)(B) ($B@5(B)$B!{7'@Z(B $B@t(B$B!&(B ($B3X(B)$BEDB<(B $B63M4(B$B!&(B ($B3X(B)$B>h0B(B $B9/J?(B$B!&(B ($B@5(B)$BEDCf(B $B0l9((B$B!&(B ($B@5(B)$B4nB?(B $B1QIR(B$B!&(B ($B;0=EBg1!@8J*;q8;(B) ($B@5(B)$BgU2,(B $B@58w(B		carbon membrane
gas separation
lignin
O
287$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 $B1QIR(B		Zeolite membranes
Pervaporation
Dehydration
P
346FAU$B7?%<%*%i%$%HKl$rMQ$$$?2C05>r7o2<$K$*$1$k(BC3$BC:2=?eAGJ,N%FC@-$N8!F$(B
($BAaBg@h?JM}9)(B/$BAaBgM}9)Am8&(B/JST-CREST) ($B@5(B)$B>>J}(B $B@5I'!&(B ($BAaBg@h?JM}9)(B) ($B3X(B)$B!{:4!9LZ(B $B9/?M(B$B!&(B ($B3X(B)$B		FAU-type zeolite membrane
pressurized conditions
propylene separation
P
347OSDA$B$rMQ$$$J$$(BRHO$BKl$N9g@.$*$h$S>.J,;R:.9gJ*$KBP$9$kF)2aJ,N%FC@-(B
($BAaBg@h?JM}9)(B) ($B3X(B)$B$B!&(B ($B3X(B)$B!{C0CO(B $B??M}(B$B!&(B ($B3X(B)$BCz(B $B71Jv(B$B!&(B($BAaBg@h?JM}9)(B/$BAaBgM}9)Am8&(B/JST-CREST) ($B@5(B)$B>>J}(B $B@5I'(B		zeolite
RHO membrane
synthesis
P
350Ag-FAU$B7?%<%*%i%$%HKl$N%W%m%T%l%s(B/$B%W%m%Q%sF)2aJ,N%5sF0$KBP$9$k05NO$N1F6A(B
($BAaBg@h?JM}9)(B) ($B3X(B)$B!{$B!&(B ($B3X(B)$B:4!9LZ(B $B9/?M(B$B!&(B($BAaBg@h?JM}9)(B/$BAaBgM}9)Am8&(B/JST-CREST) ($B@5(B)$B>>J}(B $B@5I'(B		FAU-type zeolite membrane
propylene separation
pressurized conditions
O
351AlPO4-18$BKl$N(BCO2/CH4$BF)2aJ,N%$*$h$S5[CeFC@-$N8!F$(B
($BAaBg@h?JM}9)(B) ($B3X(B)$B$B!&(B ($B3X(B)$B!{BgEh(B $B5AOB(B$B!&(B($BAaBg@h?JM}9)(B/$BAaBgM}9)Am8&(B/JST-CREST) ($B@5(B)$B>>J}(B $B@5I'(B		membrane separation
AlPO4-18
CO2/CH4
P
354SiO2$BG;EY$,9b$$A06nBN%2%k$rMQ$$$?(BSAPO-18$BKl$N9g@.(B
($BAaBg@h?JM}9)(B/$BAaBgM}9)Am8&(B/JST-CREST) ($B@5(B)$B>>J}(B $B@5I'!&(B ($BAaBg@h?JM}9)(B) ($B3X(B)$B!{@P9u(B $BAOG72p(B$B!&(B $BK\AR(B $BTw(B$B!&(B ($B@5(B)$B@%2<(B $B2mGn(B		SAPO-18
Secondary-growth method
Si content
P
359Na-ZSM-5$BKl$rMQ$$$?%a%?%N!<%k9g@.%a%s%V%l%s%j%"%/%?!<$N2DG=@-(B
($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!{5HED(B $BBg51(B$B!&(B ($B3X(B)$B66D^(B $BM:M$(B$B!&(B ($B@5(B)$B@%2<(B $B2mGn(B		methanol synthesis
membrane reactor
Na-ZSM-5
P
365$B%-%7%l%sM3Mh$NG.J,2rC:AG$rMQ$$$?(Bsilicalite-1$BKl$N%_%/%m:Y9&7B@)8f(B
($BAaBg@h?JM}9)(B) ($B3X(B)$B$B!&(B ($B3X(B)$B!{8M4,(B $B7=M4(B$B!&(B($BAaBg@h?JM}9)(B/$BAaBgM}9)Am8&(B/JST-CREST) ($B@5(B)$B>>J}(B $B@5I'(B		silicalite-1 membrane
control pore size
carbon-deposition
P
367ZSM-5$BKl$K$*$1$kF)2a@-G=$HKl9=B$$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 $B2mGn(B		zeolite membrane
permeability
membrane structure
P
369OSDA$B$rMQ$$$J$$(B*BEA$B7?%<%*%i%$%HKl$N9g@.K!$HC:2=?eAGF)2aFC@-$N8!F$(B
($BAaBg@h?JM}9)(B) ($B3X(B)$B$B!&(B ($B3X(B)$B!{0BED(B $B71G7(B$B!&(B($BAaBg@h?JM}9)(B/$BAaBgM}9)Am8&(B/JST-CREST) ($B@5(B)$B>>J}(B $B@5I'(B		*BEA-type zeolite membrane
OSDA-free synthesis
permeation properties
P
377FAU$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 $BN6%N2p(B		FAU-type zeolite
Membrane
Dehydration
P
379$B;I7c1~Ez@-%9%i%j!<$rMQ$$$?:FMxMQ2DG=$J%I%m!
($BK!@/Bg(B) ($B3X(B)$B!{KLB<(B $B8&B@(B$B!&(B ($B@5(B)$B?9(B $BN4>;(B		desalination
forward osmosis
Stimuli-responsive polymer
P
398$B5U?;F)Kl$X$N?F?e@-%]%j%^!<$N=$>~$,Hy@8J*IUCe$K5Z$\$91F6A(B
($B?@8MBg1!9)(B/$B@hC$B!&(B ($B@5(B)$B:4Gl(B $BBgJe(B$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B		Reverse osmosis membrane
Hydrophilic polymer
Bacterial adhesion
P
428RHO$B%<%*%i%$%HKl$N@=Kl$HF)2aJ*@-(B
($B;38}Bg1!M}9)(B) ($B3X(B)$B!{Lx(B $BGH(B$B!&(B ($B@5(B)$B7'@Z(B $B@t(B$B!&(B ($B@5(B)$BEDCf(B $B0l9((B$B!&(B ($B@5(B)$B4nB?(B $B1QIR(B		RHO zeolite membrane
Pervaporation
Gas permeation
O
440$B%U%)%H%j%=%0%i%U%#!<$rMQ$$$?(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 $BCRI'(B		Pd
Photolithography
Surface modification
P
448$BMO@\?tCM%7%_%e%l!<%7%g%s(B
($BF|Bg@8;:9)(B) ($B@5(B)$B!{0BF#(B $BEX(B$B!&(B $B;38}(B $BIR@8(B$B!&(B ($BElBg4D0B%;(B) ($B@5(B)$BC$L&(B $BNg(B$B!&(B (PIA) ($B@5(B)$B>.CS(B $B=$(B$B!&(B ($B?@F`9)Bg1~%P%$%*(B) ($B@5(B)$B;TB<(B $B=E=S(B		microfiltration
simulation
solute adsorption
O
451$B%/%m%9%U%m!<@:L)$m2a$ND>@\?tCM%7%_%e%l!<%7%g%s(B
($BF|Bg@8;:9)(B) ($B@5(B)$B!{0BF#(B $BEX(B$B!&(B $B2CF#(B $B5W5.(B$B!&(B (PIA) ($B@5(B)$B>.CS(B $B=$(B$B!&(B ($BElBg4D0B%;(B) ($B@5(B)$BC$L&(B $BNg(B		microfiltration
simulation
crossflow
O
454$B05NO>l$G$N(BCO2$BJ,N%$r;X8~$7$?DcG4@-H?1~@-%$%*%s1UBN4^M-%2%kKl$NAO@=(B
($B?@8MBg1!9)(B/$B@hC>LZ(B $BC#Li(B$B!&(B ($B@5(B)$B?@Hx(B $B1Q<#(B$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B		gas separation
ionic liquid
gel
P
482$B%7%j%+%i%$%HKl$N?eAGJ,N%FC@-$N8!F$(B
($B;38}BgM}9)(B) ($B3X(B)$B!{n9(B &#13969;$BK'(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 $B1QIR(B		Zeolite membrane
Hydrogen separation
Silicalite-1
O
499$B%<%*%i%$%H4^M-(BMixed Matrix Membrane$B$NF)2aJ*@-(B
($B;38}Bg1!M}9)(B) ($B3X(B)$B!{8b(B &#23159;$B!&(B ($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 $B1QIR(B		Mixed Matrix Membrane
Gas permeation
Zeolite
P
506$B?;F)05H/EE$r;X8~$7$?0[$J$kCf6u;eKl%b%8%e!<%k$rMQ$$$?F)?e$N2r@O(B
($B?@8MBg1!9)(B/$B@hC$B!&(B ($B@5(B)$B0B@n(B $B@/9((B$B!&(B ($BElMNKB(B) $B9gED(B $B>;J?(B$B!&(B ($B?@8MBg1!9)(B/$B@hC$B!&(B ($B3X(B)$B;0Eh(B $BfF;J(B$B!&(B ($B@5(B)$B9b66(B $BCR51(B$B!&(B ($B@5(B)$BHf2E(B $B=<(B$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B		Osmotic power generation
Hollow fiber module
Pressure retarded osmosis
P
510$BEE5$F)@OK!$rMQ$$$?(BCO2$BJ,N%2s<}%7%9%F%`$K$*$1$kJ|;62aDx$N?e>x5$$N1F6A(B
($B6eBg1!E}9g?7NN0h(B) ($B3X(B)$B!{;3ED(B $B5.Bg(B$B!&(B ($B6eBg(BI2CNER) ($B@5(B)$BC+8}(B $B0iM:(B$B!&(B ($B;38}Bg1!M}9)(B) ($B@5(B)$BHf2E(B $B=<(B		CO2 capture
Electrodialysis
Energy
P
513Silicalite-1$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 $BLwB'(B		zeolite membrane
separation
support
P
517$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 &#23159;$B!&(B ($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 $B1QIR(B		Cyclodextrin
Mixed Matrix Membrane
Gas separation
P
520$BHsJ?9UG.NO3X%b%G%k$K$h$k@5?;F)3$?eC8?e2=%W%m%;%9$N2r@O(B
($BEl9)Bg;q8;8&(B) ($B3X(B)$B!{E75\(B $B@60l(B$B!&(B ($B@5(B)$BBg66(B $B=(Gl(B$B!&(B ($B@5(B)$B;38}(B $BLT1{(B		Forward osmosis
Desalination
Non-equilibrium thermodynamics
O
532$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 $BLwB'(B		zeolite membrane
separation
*BEA zeolite
P
538$B%"%K%*%s%I!<%W$K$h$k%7%j%+%M%C%H%o!<%/9=B$@)8f$H5$BNJ,N%Kl$N:n@=(B
($B9-Bg1!9)(B) ($B@5(B)$B!{6b;X(B $B@58@(B$B!&(B ($B3X(B)$B>>C+(B $BBvLp(B$B!&(B ($BElBg1!9)(B) ($B@5(B)$BOF86(B $BE0(B$B!&(B ($B=;M'EE9)(B) $BI6;3(B $BGn6)(B$B!&(B ($B9-Bg1!9)(B) ($B@5(B)$BD9_7(B $B425,(B$B!&(B ($B@5(B)$B5H2,(B $BJ~5W(B$B!&(B ($BElBg1!9)(B) ($B@5(B)$BBg5WJ](B $BC#Li(B$B!&(B ($B9-Bg1!9)(B) ($B@5(B)$BETN1(B $BL-N;(B		Amorphous silica
Pore size control
Gas separation
O
550CHA/STT$B7?%T%e%"%7%j%+%<%*%i%$%HKl$ND4@=$H%,%9F)2aFC@-(B
(RITE) ($B@5(B)$B!{MhED(B $B9/;J(B$B!&(B (NAIST) ($B3X(B)$BA0ED(B $B9/;V(B$B!&(B (RITE) ($B@5(B)$BM>8l(B $B9nB'(B		Pure silica zeolite
Zeolite membrane
Gas permeation
O
571$B%"%_%s4^M-%2%kN3;R$N(BCO2$BA*BrF)2aKl$X$N1~MQ2DG=@-$N8!F$(B
($B6eBg1!9)(B) ($B@5(B)$B!{@1Ln(B $BM'(B$B!&(B $B9TIt(B $BCRMN(B$B!&(B $B:#B<(B $BOB;K(B$B!&(B $BIM:j(B $B1{(B$B!&(B $B;32<(B $BCN7C(B$B!&(B $BEOn5(B $BLT(B$B!&(B ($B6eBg(BI2CNER) ($B@5(B)$BC+8}(B $B0iM:(B$B!&(B ($B6eBg1!9)(B) ($B@5(B)$B;01:(B $B2B;R(B		CO2
Gel Particles
Membrane
O
573$B%/%m%9%U%m!<@:L)$m2a$K$*$1$kG4@-DlAX0h$NN3;R5sF0$H8B3&N.B+$K4X$9$k8&5f(B
($B9)3X1!Bg9)(B) ($B3X(B)$B!{bCJI(B $BNI(B$B!&(B ($B9)3X1!Bg@h9)(B) ($B@5(B)$B@V>>(B $B7{$B!&(B ($BElBg4D0B%;(B) ($B@5(B)$BC$L&(B $BNg(B$B!&(B (PIA) ($B@5(B)$B>.CS(B $B=$(B$B!&(B ($B9)3X1!Bg@h9)(B) ($B@5(B)$BCfHx(B $B??0l(B		microfiltration
limiting flux
simulation
O
579$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 $B=(?M(B		Forward osmosis
Up-concentration
Saccharide
P
601$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 $BMN=<(B		polyimide membranes
1,3-butaziene
Frist principles molecular dynamics
P
610$BBg5$05%W%i%:%^(BCVD$BK!$K$h$k%7%j%+Kl$N:n@=(B
($B9-Bg1!9)(B) ($B@5(B)$B!{D9_7(B $B425,(B$B!&(B ($B3X(B)$B;3K\(B $BM5B@(B$B!&(B ($B@5(B)$B6b;X(B $B@58@(B$B!&(B ($B@5(B)$B5H2,(B $BJ~5W(B$B!&(B ($B@5(B)$BETN1(B $BL-N;(B		$B%7%j%+Kl(B
$BBg5$05%W%i%:%^(B
CVD
O
613$B%"%_%sC4;}9bJ,;RKl:`NA$N9g@.$H(BCO2$BJ,N%@-G=(B
($B6eBg(BWPI-I2CNER) ($B@5(B)$B!{C+8}(B $B0iM:(B$B!&(B ($B6eBg1!E}9g?7NN0h(B) ($B3X(B)$B5H_7(B $BIq(B		CO2
membrane separation
amine
O
647$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 $B>O(B		vapor permeation
hydrocarbons
ionic liquid
P
684$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 $BMN=<(B		Molecular dynamics
Aquaporin
Water channel
P
698[$B8&5f>)Ne>^(B] $B6bB0M-5!9=B$BN$rMQ$$$?5$BNJ,N%Kl$N:n@=$HF)2a5!9=$K4X$9$k8&5f(B
($B;:Am8&(B) ($B@5(B)$B86(B $B?-@8(B		gas separation membrane
metal-organic framework
propylene/propane separation
O
708$B?eAG!&CbAG!&%"%s%b%K%"$r4^$`:.9g%,%9$+$i$N(BV-Ni$B9g6bKl$K$h$k?eAGJ,N%(B
(NIMS) ($B@5(B)$B!{@>B<(B $BKS(B$B!&(B $Bhq(B $B@/1d(B$B!&(B ($BNkLZ>&4[(B) ($B@5(B)$BLZB<(B $B9@N4(B$B!&(B (NIMS) $BA}ED(B $BBnLi(B		vanadium
membrane
energy carrier
O
713$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 $B4490(B		MOR zeolite membrane
ion exchange
water permeation
P
717$B9bF)?e@-$H9bBQ05@-$rM-$9$k(BTFC$B7?(BFO$BKl$N3+H/(B
($B?@8MBg1!9)(B/$B@hC$B!&(B ($B@5(B)$B0B@n(B $B@/9((B$B!&(B ($B3X(B)$B=BC+(B $B??;K(B$B!&(B ($B@5(B)$B9b66(B $BCR51(B$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B		Forward osmosis membrane
Pressure resistance
Pressure retarded osmosis
P
724$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 $B=(?M(B		lattice Boltzmann method
microfiltration
cross-flow
P
732Organosilica membranes on hydrophobic intermediate layers for wet gas separation
(Hiroshima U.) ($B3$(B)$B!{(BRen Xiuxiu$B!&(B ($B@5(B)Kanezashi Masakoto$B!&(B ($B@5(B)Nagasawa Hiroki$B!&(B ($B@5(B)Tsuru Toshinori		wet gas separation
hydrophobic intermediate layer
organosilica membranes
O
733$B?75,6bB0:xBN7O%$%*%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 $B=(?M(B		ionic liquid
gas absorption
metal complex
P
740$B%<%*%i%$%H7?:xBN7k>=(BZIF-8$B$N=%U%j!<@=Kl$H%,%9F)2aFC@-(B
($B4X@>Bg9)(B) ($B3X(B)$B!{Bg5WJ](B $B7rB@(B$B!&(B ($B@5(B)$B;0Bp(B $B5AOB(B$B!&(B ($B@5(B)$BEDCf(B $B=SJe(B		ZIF-8
membrane
in situ crystallization
P
741$BHyN3;RJ,;61U$NKlJ,N%2aDx$K$*$1$k%1!<%/AX7A@.%7%_%e%l!<%7%g%s(B
($B?@8MBg1!9)(B/$B@hC$B!&(B ($B3X(B)$B@>C+(B $BkNB@(B$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		$BKlJ,N%(B
$B%1!<%/7A@.(B
$B3J;R%\%k%D%^%sK!(B
O
784$B9b%7%j%+(BCHA$B7?%<%*%i%$%HKl$N%,%9J,N%FC@-(B
($BF|N)B$A%(B) ($BK!(B)$B!{:#:d(B $BNg;K(B$B!&(B ($BK!(B)$BHDAR(B $B@5Li(B$B!&(B ($BK!(B)$BLpLn(B $BOB9((B$B!&(B ($BK!(B)$BF#ED(B $BM%(B$B!&(B ($B;:Am8&(B) ($B@5(B)$BD9C+@n(B $BBY5W(B$B!&(B $B0$It(B $B@i;^(B$B!&(B ($B4X@>Bg(B) ($B@5(B)$B;3K\(B $B=($B!&(B ($B@5(B)$B9SLZ(B $BDgIW(B		zeolite
membrane
chabazite
O
794LCST$B7?AjE>0\:`NA$rMQ$$$?%*%9%b%F%#%C%/%R!<%H%(%s%8%s$K4X$9$k4pACE*8&5f(B
($B?@8MBg1!9)(B/$B@hC$B!&(B ($B?@8MBg9)(B/$B@hC$B!&(B ($B?@8MBg1!9)(B/$B@hC>;3(B $B=(?M(B		osmotic heat engine
pressure retarded osmosis
draw solute
O
804$B@5?;F)6nF0MO1U$r;X8~$7$?Fs;@2=C:AG1~Ez@-AjE>0\:`NA$K4X$9$k4pACE*8&5f(B
($B?@8MBg9)(B/$B@hC?9(B $B1vJfH~(B$B!&(B ($B?@8MBg1!9)(B/$B@hC$B!&(B ($B@5(B)$B9b66(B $BCR51(B$B!&(B ($B%@%$%;%k(B) ($BK!(B)$BIMED(B $BK-;0(B$B!&(B ($B?@8MBg1!9)(B/$B@hC>;3(B $B=(?M(B		forward osmosis
draw solute
carbon dioxide
P
825Polymer-supported organosilica layered-hybrid membranes for reverse osmosis desalination
(Hiroshima U.) ($B3$(B)$B!{(BGong Genghao$B!&(B ($B@5(B)Nagasawa Hiroki$B!&(B ($B@5(B)Kanezashi Masakoto$B!&(B ($B@5(B)Yoshioka Tomohisa$B!&(B ($B@5(B)Tsuru Toshinori		layered hybrid membrane
HCl vapor treatment
desalination
O
829$BD62;GHJ.L8>F7kK!$K$h$k%;%i%_%C%/(B-$B6bB0J#9g9=B$$r$b$DJ,N%Kl$N%,%9F)2aFC@-(B
($B2#9qBg1!(B) ($B3X(B)$B!{C*Hx(B $B98Bg(B$B!&(B ($B3X(B)$BJ?;3(B $BBg2p(B$B!&(B ($B2#9qBg(B) $BOBED(B $B=_;V(B$B!&(B ($B2#9qBg1!(B) ($B@5(B)$BAj86(B $B2mI'(B		separation membrane
ultrasonic spray sintering
ceramic-metal composite
P
834$B3h@-C:$rJqKd$7$?%"%k%.%s;@%2%kKl$K$h$k%a%A%l%s%V%k!<5[CeG=$NI>2A(B
($B>.;39b@lJ*$B!&(B $BBg_7(B $B7r?M(B$B!&(B ($BJ!Eg9b@lJ*$B!&(B ($BF|Bg1!@8J*;q8;(B) ($B@5(B)$B:#0f(B $B@5D>(B		alginate
activated carbon
adsorption membrane
O
896$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 $B1QIR(B		arbon molecular sieve membranes
polyimides
gas permeation
P
899$BBg7?5UEE5$F)@O%7%9%F%`$K$*$1$kH/EEFC@-I>2A$H$=$N2r@O(B
($B;38}Bg1!M}9)(B) ($B3X(B)$B!{]/ED(B $BJ~G7(B$B!&(B ($B;38}Bg9)(B) $B5WLn(B $B2mLo(B$B!&(B ($B;38}Bg1!M}9)(B) ($B@5(B)$BHf2E(B $B=<(B		ion exchange membrane
reverse electrodialysis
salinity gradient power
P
900FO$BKl%b%8%e!<%k$rMQ$$$??;F)05H/EE%7%9%F%`$K$*$1$kH/EEFC@-I>2A$H$=$N2r@O(B
($B;38}Bg1!M}9)(B) $BCSJU(B $BM:5.(B$B!&(B $BKY9>(B $BN5fF(B$B!&(B ($B@5(B)$B!{Hf2E(B $B=<(B		Pressure retarded osmosis
Hollow fiber membrane module
Spiral wound membrane module
O
913$B?eG.K!$K$h$k%+!<%\%sKl$N:n@=(B
($BEl9)Bg(B) ($B3X(B)$B!{:4Ln(B $BfF:H(B$B!&(B ($B@5(B)$B0kIt(B $BIR9((B$B!&(B $B>>2<(B $B>M;R(B$B!&(B $BCfEg(B $B>O(B		activated carbon
water/ethanol separation
glucose
P
939$B%7%j%+Kl$rMQ$$$?KlH?1~4o$K$h$k9bO'%,%9M-8z3hMQ(B
(RITE) ($B@5(B)$B!{B?8U(B $BCR5.(B$B!&(B ($B@5(B)$B>>;3(B $B3(H~(B$B!&(B ($B@5(B)$B@>ED(B $BN<0l(B$B!&(B ($B@5(B)$BCfHx(B $B??0l(B		silica membrane
membrane reactor
water gas shift reaction
O
943$B%7%j%+KlH?1~4o%b%8%e!<%k$K$h$k%a%A%k%7%/%m%X%-%5%s$+$i$NC&?eAG$N8!F$(B
(RITE) ($B@5(B)$B!{>>;3(B $B3(H~(B$B!&(B ($B@5(B)$B>B8}(B $BNKJ?(B$B!&(B ($B@5(B)$B1:0f(B $B9(H~(B$B!&(B ($B@5(B)$B@>ED(B $BN<0l(B$B!&(B ($B@5(B)$BCfHx(B $B??0l(B		silica membrane
organic chemical hydride
membrane reactor
O
9462$B2/CH4$BJ,N%(B
($B1'ET5\Bg9)(B) ($B3X(B)$B!{?{Ln(B $BM5Bg(B$B!&(B ($B3X(B)$B2CF#(B $B?rJ8(B$B!&(B ($B1'ET5\Bg1!9)(B) ($B@5(B)$B:4F#(B $B9d;K(B$B!&(B ($B@5(B)$B0KF#(B $BD>		zeolite
membrane
separation
P
947$B%"%_%N;@%$%*%s1UBN4^?;Kl$N(BCO2$BF)2a78?t?d;;%b%G%k$N9=C[(B
($B?@8MBg1!9)(B/$B@hC$B!&(B ($B3X(B)$BBgC+(B $BIK?M(B$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B		CO2 separation membrane
Amino acid ionic liquid
Permeation model
O
949CFD$B$rMxMQ$7$?%<%*%i%$%HKl$K$h$k(BCO2/CH4$B:.9g7OJ,N%$K$*$1$k%Q!<%_%"%s%9$NG;EY0MB8@-$N?dDj(B
($B1'ET5\Bg9)(B) ($B3X(B)$B!{2CF#(B $B?rJ8(B$B!&(B ($B3X(B)$B?{Ln(B $BM5Bg(B$B!&(B ($B1'ET5\Bg1!9)(B) ($B@5(B)$B:4F#(B $B9d;K(B$B!&(B ($B@5(B)$B0KF#(B $BD>		CFD
Zeolite
membrane
P
972Preparation and characterization of antifouling PVC hollow fiber membrane by blending an amphiphilic copolymer
($B?@8MBg(B) ($B3X(B)$B!{<~(B $B>1(B$B!&(B (Kobe U.) ($B3$(B)Rajabzadeh Saeid$B!&(B ($B?@8MBg(B) ($B@5(B)$B>>;3(B $B=(?M(B		PVC membrane
antifouling
blend ratio
P
$B9V1i?=$79~$_0lMw(B($B%7%s%]%8%&%`HV9f!&9V1iJ,N`HV9fJL(B)
$B
$B2=3X9)3X2q(B $BBh(B81$BG/2q(B (2016)
(C) 2016 $B8x1W
Most recent update: 2016-05-19 11:21:01
For more information contact $B2=3X9)3X2q(B $BBh(B81$BG/2q(B $B
E-mail: inquiry-81awww3.scej.org
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