SCEJ

$B2=3X9)3X2q(B $BBh(B80$BG/2q(B

$B9V1i?=$79~$_0lMw!J%7%s%]%8%&%`!&9V1iJ,N`JL!K(B

4) $BJ,N%%W%m%;%9(B

4-a. $BKl9)3X(B

$B:G=*99?7F|;~!'(B2015-07-10 15:24:01

$B$3$NJ,N`$G$h$/;H$o$l(B
$B$F$$$k%-!<%o!<%I(B		$B%-!<%o!<%I(B$B
Membrane8$B7o(B**
zeolite4$B7o(B*
zeolite membrane4$B7o(B*
hydrogen4$B7o(B*
membrane separation4$B7o(B*
forward osmosis4$B7o(B*
membrane reactor3$B7o(B*
Gas separation3$B7o(B*
pervaporation3$B7o(B*
Amphiphilic copolymer2$B7o(B
bio-ethanol2$B7o(B
silica hybrid membranes2$B7o(B
silicalite-1 membrane2$B7o(B
Operating condition2$B7o(B
microfiltration2$B7o(B
silica membrane2$B7o(B
Carbon membrane2$B7o(B
carbon dioxide separation2$B7o(B
pressure retarded osmosis2$B7o(B
Hollow fiber membrane2$B7o(B
MFI zeolite membrane2$B7o(B
porous silica substrate2$B7o(B
CVD2$B7o(B
Antifouling membrane2$B7o(B
molecular dynamics2$B7o(B
ozone concentration1$B7o(B

$B$BHV9f(B$B9V1iBjL\!?H/I=$B%-!<%o!<%I(B$BH/I=7A<0(B
32IPA-$B?e:.9g>x5$$N9bB.C&?e$N$?$a$NEy2CB.86NA6!5kK!(B
($B1'ET5\Bg1!9)(B) ($B3X(B)$B!{5FCO(B $BM*J?(B$B!&(B ($B3X(B)$B@PED(B $B=a(B$B!&(B ($B@5(B)$B:4F#(B $B9d;K(B$B!&(B ($B;:Am8&ElKL(B) ($B@5(B)$BD9C+@n(B $BBY5W(B$B!&(B ($B1'ET5\Bg1!9)(B) ($B@5(B)$B0KF#(B $BD>		zeolite membrane
vapor permeation
IPA and water
P
49$B?tM}%b%G%k$r3hMQ$7$?(BMBR$B$K$*$1$k1?E>>r7o$N:GE,2=$N8!F$(B
($BElBg1!9)(B) ($B@5(B)$B!{6b;R(B $B90>;(B$B!&(B ($B@5(B)$BA%DE(B $B8x?M(B		Membrane bioreactor
Operating condition
Optimization
O
51$BF)@OKl$N%U%!%&%j%s%0@)8f$K8~$1$??eOB?e$N%_%/%m5sF02r@O(B
($BL>9)Bg(B) ($B3X(B)$B!{NkLZ(B $BNCLi(B$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 $B=(		membrane separation
molecular dynamics
free energy
P
64FAU$B7?$*$h$S(BCHA$B7?%<%*%i%$%HKl$K$h$kFs;@2=C:AGJ,N%$NHf3S8!F$(B
($B1'ET5\Bg1!9)(B) ($B3X(B)$B!{9bNS(B $BPRN<(B$B!&(B ($B@5(B)$B:4F#(B $B9d;K(B$B!&(B ($B;:Am8&ElKL(B) ($B@5(B)$BD9C+@n(B $BBY5W(B$B!&(B ($B1'ET5\Bg1!9)(B) ($B@5(B)$B0KF#(B $BD>		zeolite membrane
carbon dioxide separation
molecular sieving
P
116$B%S%K%k%H%j%a%H%-%7%7%i%s$rA06nBN$H$7$?AB?e@-%7%j%+Kl$ND4@=$H?];@%(%A%k$NJ,N%FC@-(B
($B4X@>Bg4DET9)(B) ($B3X(B)$B!{8"F#(B $BBgN<(B$B!&(B $B>.@n(B $BMK(B$B!&(B ($B@5(B)$B9SLZ(B $BDgIW(B$B!&(B ($B@5(B)$B;3K\(B $B=(		Membrane separation
Pervaporation
Hydrophobicity
P
148Hansen$BMO2rEY%Q%i%a!<%?$K$h$kAB?e@-%7%j%+Kl$K$*$1$kF)2a@-$N8!F$(B
($B4X@>Bg4DET9)(B) ($B@5(B)$B!{9SLZ(B $BDgIW(B$B!&(B ($B3X(B)$B8"F#(B $BBgN<(B$B!&(B ($B@5(B)$B;3K\(B $B=(		Hansen Solubility Parameter
hydrohobic
silica
O
249$BD62;GHJ.L8>F7kK!$K$h$j:n@=$5$l$?%A%?%K%"Kl$N?e>x5$A*BrF)2a@-$N8&5f(B
($B2#9qBg1!(B) ($B3X(B)$B!{J?;3(B $BBg2p(B$B!&(B ($B3X(B)$BCfLn(B $BC#L&(B$B!&(B ($B2#9qBg(B) $BC*Hx(B $B98Bg(B$B!&(B ($B2#9qBg1!(B) ($B@5(B)$BAj86(B $B2mI'(B		separation membrane
ultrasonic spray sintering
gas separation
P
259Molecular Design of High CO2 Reactivity and Low Viscosity Ionic Liquids for CO2 Separative Facilitated Transport Membrane
(U. Notre Dame) ($B3X(B)$B!{BgC+(B $BIK?M(B$B!&(B Zhang Y.$B!&(B ($B?@8MBg1!9)(B) ($B@5(B)$B?@Hx(B $B1Q<#(B$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B$B!&(B (U. Notre Dame) Maginn E.		Ionic Liquids
Viscosity
Molecular Dynamics Simulation
P
270$B8w?(G^Kl%3%s%?%/%?!<$N@-G=$KM?$($kMOB81v$N1F6A(B
($B;38}Bg9)(B) ($B3X(B)$B!{FjLZ(B $BBk$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 $B1QIR(B		photocatalytic membrane
Formic acid
water treatment
P
271Pore-plugging$BK!$K$h$j@=Kl$7$?(BMFI$B7?%<%*%i%$%HKl$NF)2aJ,N%@-G=(B
($B;38}Bg1!M}9)(B) ($B3X(B)$B!{;32<(B $BM5B@(B$B!&(B $Bn9(B &#28789;$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 $B1QIR(B$B!&(B (Zaragoza U.) Cacho Fernando$B!&(B Sorribas Sara$B!&(B Tellez Carlos$B!&(B Coronas Joaquin		zeolite
membrane
gas separation
P
286$B%<%*%i%$%HKl$K$h$k%(%A%l%s%8%"%_%s?eMO1UJ,N%(B
($B$B!&(B $B1,7n(B $B0lJ?(B$B!&(B $B5\CO(B $BNJ(B$B!&(B ($B3X(B)$BCSED(B $BJb(B$B!&(B ($B3X(B)$B>.Ln(B $BN5J?(B$B!&(B ($B3X(B)$B>>;3(B $B3(H~(B$B!&(B ($B@5(B)$BLnB<(B $B4490(B		MOR zeolite membranes
ethylenediamine separation
pervaporation
P
291$B%^%$%/%mGH2CG.$rMxMQ$7$?(BSAPO-34$BKl9g@.(B
($BEl9)Bg1!M}9)(B) ($B@5(B)$B!{W"ED(B $BM:0lO/(B$B!&(B ($B3X(B)$BEDB<(B $B??8c(B$B!&(B ($B@5(B)$B0KEl(B $B>O(B		zeolite membrane
microwave heating
carbon dioxide separation
O
297$B%?%s%K%s!&%j%0%K%sJ#9g:`NA$+$i$NJ,;R$U$k$$C:AGKl$N9g@.>r7o(B
($B;38}Bg9)(B) ($B3X(B)$B!{EDB<(B $B63M4(B$B!&(B ($B@5(B)$B7'@Z(B $B@t(B$B!&(B ($B@5(B)$BEDCf(B $B0l9((B$B!&(B ($B@5(B)$B4nB?(B $B1QIR(B		Carbon membrane
Lignin
tannin
P
304$B%<%*%i%$%H$r=PH/86NA$H$7$FMQ$$$?9b%7%j%+(BCHA$BKl$N9g@.$HJ,N%FC@-(B
($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 ($B;:Am8&(B) ($BK!(B)$BD9C+@n(B $BBY5W(B$B!&(B ($BK!(B)$B0$It(B $B@i;^(B		zeolite
membrane
chabazite
O
311$B%P%$%*%,%92=;D^V%?!<%k$rMQ$$$?C:AGKl$N:n@=(B
($B;38}Bg1!M}9)(B) ($B3X(B)$B!{8eF#(B $B=Y2p(B$B!&(B ($B@5(B)$B4nB?(B $B1QIR(B$B!&(B ($B@5(B)$BEDCf(B $B0l9((B$B!&(B ($B@5(B)$B7'@Z(B $B@t(B$B!&(B ($BKL8+9)Bg(B) ($B@5(B)$BNkLZ(B $BJY(B		Carbon membrane
Biogas Tar
Gas separation
P
318$B9bJ,;R(B/$B%7%/%m%G%-%9%H%j%sKt$O%<%*%i%$%HJ#9gKl$N:n@=$HF)2aJ*@-(B
($B;38}Bg1!M}9)(B) ($B3X(B)$B!{A}ED(B $BCNLi(B$B!&(B ($B1'It9b@l(B) $B;3K\(B $BM&Ka(B$B!&(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 $B1QIR(B		polymer
cyclodextrin
zeolite
P
352Development of hydrogen-selective triphenylmethoxysilane-derived membranes by chemical vapor deposition
($B9)3X1!Bg9)(B) Zhang Xiaoliang$B!&(B (RITE) ($B@5(B)$B;3ED(B $B=(>0(B$B!&(B ($B@5(B)$B@FF#(B $B?r(B$B!&(B ($B@5(B)$B9CHe(B $B>HI'(B$B!&(B ($B9)3X1!Bg9)(B) ($B@5(B)$B!{@V>>(B $B7{$B!&(B ($B9)3X1!Bg9)(B/RITE) ($B@5(B)$BCfHx(B $B??0l(B		silica membrane
hydrogen
chemical vapor deposition
O
395Pd/Ag$BKl$N?eAGFs;@2=C:AG:.9g5$$+$i$N?eAGF)2a$K4X$9$k8&5f(B
($B7DXfBg1!M}9)(B) ($B3X(B)$B!{2OV?(B $BM-5#(B$B!&(B Hasan M. Faizal$B!&(B ($B7DXfBgM}9)(B) $B2#?9(B $B9d(B$B!&(B ($B@5(B)$B?"ED(B $BMx5W(B		Membrane Separation
Hydrogen
Carbon Dioxide
P
410$BAB?e@-%;%i%_%C%/Kl$rMQ$$$???6uKl>xN1K!$K$h$k%9%/%m!<%9?eMO1UG;=L(B
($BEl9)Bg1!M}9)(B) ($B3X(B)$B!{?@C+(B $BCR5,(B$B!&(B ($BEl9)Bg9)(B) $B9a;3(B $BKS7n(B$B!&(B ($BEl9)Bg1!M}9)(B) ($B@5(B)$BW"ED(B $BM:0lO/(B$B!&(B ($B@5(B)$B0KEl(B $B>O(B		membrane distillation
hydrophobic membrane
sucrose concentration
P
440$BBQ5W@-!"BQ;@@-$KM%$l$??F?e@-(BMFI$B7?%<%*%i%$%HKl$N@=Kl$H%P%$%*%(%?%N!<%kG;=L%W%m%;%9$X$N1~MQ(B
($B;38}Bg1!M}9)(B) ($B3X(B)$B!{K'Ln(B $B98M$(B$B!&(B ($B;38}Bg1!G@(B) $B;3ED(B $B$B!&(B $B9b:d(B $BCRG7(B$B!&(B $BB$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 $B1QIR(B		MFI zeolite mebranes
bio-ethanol
concentration process
P
447$B8w?(G^?eAG@=B$$KMQ$$$k8w2M66%]%j%$%_%IJ#9gKl$N:n@=>r7o$N8!F$(B
($B;38}Bg1!M}9)(B) ($B3X(B)$B!{NS(B $B7rB@O:(B$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 $B1QIR(B		photocrosslinked polyimide
composite membrane
P
474$B%U%C2=J*E:2C$K$h$k9b?eAGF)2a%<%*%i%$%HKl$N2~NI(B
($B$B!&(B $BBg1:(B $B6W2;(B$B!&(B ($B3X(B)$BCSED(B $BJb(B$B!&(B ($B3X(B)$B>.Ln(B $BN5J?(B$B!&(B ($B3X(B)$B>>;3(B $B3(H~(B$B!&(B ($B=;M'EE9)(B) $B:XF#(B $B?r9-(B$B!&(B $BI6;3(B $BGn6)(B$B!&(B $B7,86(B $B0lLi(B$B!&(B ($B		MFI zeolite membrane
porous silica substrate
NaF
P
501$BJ,;RF0NO3XK!$K$h$k?eJ,;R$N5sF02r@O$H%]%j%^!
($BL>9)Bg(B) ($B@5(B)$B!{Fn1@(B $BN<(B$B!&(B ($B3X(B)$B;0Bp(B $B9'L@(B$B!&(B ($B3X(B)$B;{Hx(B $BfFJ?(B$B!&(B ($B@5(B)$B4dED(B $B=$0l(B$B!&(B ($B@5(B)$B?9(B $B=(		hydration
membrane fouling
molecular dynamics
O
512$BCf6u;eKl%b%8%e!<%k$rMQ$$$?(BPRO$BH/EE%7%9%F%`$N@5L#H/EE=PNO$H1?E>>r7o$H$N4X78(B
($B;38}Bg1!M}9)(B) $B@t@n(B $B?52p(B$B!&(B ($B3X(B)$B=BC+(B $B??;K(B$B!&(B $BCSJU(B $BM:5.(B$B!&(B $BKY9>(B $BN5fF(B$B!&(B ($B@5(B)$B!{Hf2E(B $B=<(B		Pressure retarded osmosis
Hollow fiber membrane module
Operating condition
P
534$BBQ;@@-%7%j%+5U?;F)Kl$N3+H/(B
($B$B!&(B $B0pn5(B $BAaLi9a(B$B!&(B ($B3X(B)$BCSED(B $BJb(B$B!&(B $B4XK\(B $B6F(B$B!&(B $BW"@%(B $BCR5W(B$B!&(B ($B3X(B)$B>.Ln(B $BN5J?(B$B!&(B ($B3X(B)$B>>;3(B $B3(H~(B		silica RO membrane
acid stability
Ga addition
O
549$BD6J4:U=$rMQ$$$?(BMFI$B%<%*%i%$%HKl$N@=Kl(B
($B.Ln(B $BN5J?(B$B!&(B ($B3X(B)$BKLEh(B $B85$B!&(B ($B3X(B)$BCSED(B $BJb(B$B!&(B ($B3X(B)$B>>;3(B $B3(H~(B$B!&(B ($B@5(B)$BLnB<(B $B4490(B		MFI zeolite membranes
ultra-milled seed crystals
pervaporation
P
571$B=C4;}>uBV$,(BRHO$BKl$NF)2aJ,N%FC@-$K5Z$\$91F6A(B
($BAaBg@h?JM}9)(B) ($B3X(B)$B$B!&(B ($B3X(B)$B!{C0CO(B $B??M}(B$B!&(B($BAaBg@h?JM}9)(B/$BAaBgM}9)Am8&(B/JST-CREST) ($B@5(B)$B>>J}(B $B@5I'(B		RHO
membrane
synthesis
P
579$B5[Ce;n83$rMQ$$$?(BNa-ZSM-5$BKl$NKl9=B$$HF)2a@-$N4X78$K$D$$$F$N8!F$(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!{HSEg(B $BM%5.(B$B!&(B ($B@5(B)$B@%2<(B $B2mGn(B		MFI-type zeolite membrane
Adsorption
Structure
P
580$B05NOJd=u@5?;F)K!$K$*$1$k1?E>>r7o$,?eF)2a@-G=$KM?$($k1F6A(B
($B?@8MBg1!9)(B/$B@hC$B!&(B ($B@5(B)$B0B@n(B $B@/9((B$B!&(B ($B@5(B)$B9b66(B $BCR51(B$B!&(B ($B@5(B)$B;09%(B $BB@O:(B$B!&(B ($B;38}Bg1!M}9)(B/$B?@8MBg1!9)(B) ($B@5(B)$BHf2E(B $B=<(B$B!&(B ($B?@8MBg1!9)(B/$B@hC>;3(B $B=(?M(B		Pressure assisted osmosis
Hollow fiber membrane
Forward osmosis
O
585silicalite-1$BKl$NKl7A@.2aDx$N8!F$(B
($BAaBg@h?JM}9)(B) ($B3X(B)$B$B!&(B ($B3X(B)$B!{6b;R(B $BBsLp(B$B!&(B ($B3X(B)$BHSEg(B $BM%5.(B$B!&(B ($B3X(B)$B8M4,(B $B7=M4(B$B!&(B($BAaBg@h?JM}9)(B/$BAaBgM}9)Am8&(B/JST-CREST) ($B@5(B)$B>>J}(B $B@5I'(B		zeolite
silicalite-1 membrane
growth process
P
588$B?eAGF)2a%7%j%+J#9gKl$K$h$kKlH?1~4o3+H/(B
($B$B!&(B ($B3X(B)$B>.Ln(B $BN5J?(B$B!&(B ($B3X(B)$B>>;3(B $B3(H~(B$B!&(B ($B@5(B)$BLnB<(B $B4490(B$B!&(B ($B86;RNO5!9=(B) ($B@5(B)$BEDCf(B $B?-9,(B$B!&(B $B5WJ](B $B??<#(B		cuonter diffusion CVD method
silica hybrid membranes
membrane reactor
P
591FAU$B7?%<%*%i%$%HKl$N(BC3$BC:2=?eAG5[CeFC@-$N8!F$(B
($BAaBg@h?JM}9)(B) ($B3X(B)$B$B!&(B ($B3X(B)$B!{:4!9LZ(B $B9/?M(B$B!&(B ($B3X(B)$BHSEg(B $BM%5.(B$B!&(B($BAaBg@h?JM}9)(B/$BAaBgM}9)Am8&(B/JST-CREST) ($B@5(B)$B>>J}(B $B@5I'(B		FAU-type membrane
adsorption properties
propylene
P
594silicalite-1$BKl$N(Bxylene$B>x5$F)2aJ,N%FC@-$H@.D92aDx(B
($BAaBg@h?JM}9)(B) ($B3X(B)$B!{$B!&(B ($B3X(B)$B6b;R(B $BBsLp(B$B!&(B ($B3X(B)$BHSEg(B $BM%5.(B$B!&(B ($B3X(B)$B8M4,(B $B7=M4(B$B!&(B($BAaBg@h?JM}9)(B/$BAaBgM}9)Am8&(B/JST-CREST) ($B@5(B)$B>>J}(B $B@5I'(B		silicalite-1 membrane
xylene separation
growth
O
618$B@5?;F)Kl%b%8%e!<%k@-G=$NM=B,$,2DG=$J4J0W%b%G%k$N3+H/(B
($B?@8MBg1!9)(B/$B@hC$B!&(B ($BElMNKB(B) $B9gED(B $B>;J?(B$B!&(B ($B?@8MBg1!9)(B/$B@hC$B!&(B ($B@5(B)$B9b66(B $BCR51(B$B!&(B ($B@5(B)$B;09%(B $BB@O:(B$B!&(B ($B?@8MBg1!9)(B/$B;38}Bg1!M}9)(B) ($B@5(B)$BHf2E(B $B=<(B$B!&(B ($B?@8MBg1!9)(B/$B@hC>;3(B $B=(?M(B		Forward Osmosis
Hollow fiber membrane
Module performance
O
629AlPO4-18 $BKl$N(BCO2 / CH4 $BF)2aJ,N%5sF0$N8!F$(B
($BAaBg@h?JM}9)(B) ($B3X(B)$B!{BgEh(B $B5AOB(B$B!&(B ($B3X(B)$B$B!&(B($BAaBg@h?JM}9)(B/$BAaBgM}9)Am8&(B/JST-CREST) ($B@5(B)$B>>J}(B $B@5I'(B		membrane separation
AlPO4-18
CO2 / CH4
P
635$B:Y9&9=B$$N0[$J$k;Y;}BN>e$K@=Kl$7$?(BZSM-5$BKl$NF)2aFC@-$N8!F$(B
($BAaBg@h?JM}9)(B/$BAaBgM}9)Am8&(B/JST-CREST) ($B@5(B)$B>>J}(B $B@5I'!&(B ($BAaBg@h?JM}9)(B) ($B3X(B)$B!{5HED(B $BBg51(B$B!&(B ($B@5(B)$B@%2<(B $B2mGn(B		ZSM-5
permeation properties
support
P
640$B?e>x5$A*BrF)2a:Y9&%U%#%j%s%0Kl$N3+H/(B
($BEl9)Bg;q8;8&(B) ($B3X(B)$B!{1|ED(B $BN6B@O/(B$B!&(B ($B@5(B)$BBg66(B $B=(Gl(B$B!&(B (KAST/$BEl9)Bg;q8;8&(B) ($B@5(B)$B9uLZ(B $B=(5-(B$B!&(B ($BEl9)Bg;q8;8&(B/KAST) ($B@5(B)$B;38}(B $BLT1{(B		Latent heat recovery
Pore-filling membrane
Water vapor / CO2 permselectivity
P
652$B%$%*%s8r49Kl$rMQ$$$?%l%I%C%/%97?H?1~4o$N3+H/(B
($B.J?(B $B3Y=((B$B!&(B $BBg1:(B $B6W2;(B$B!&(B ($B3X(B)$BCSED(B $BJb(B$B!&(B ($B3X(B)$B>.Ln(B $BN5J?(B$B!&(B ($B3X(B)$B>>;3(B $B3(H~(B$B!&(B ($B@5(B)$BLnB<(B $B4490(B$B!&(B ($B86;RNO5!9=(B) $B_7ED(B $B??0l(B$B!&(B $BH,4,(B $BE0Li(B$B!&(B $BEDCf(B $B?-9,(B$B!&(B $B5WJ](B $B??<#(B		thermochemical water splitting IS process
ion exchange membrane
redox reactor
P
656Bimodal catalytic membrane reactors for hydrogen production in the dehydrogenation of methylcyclohexane
($B9-Bg(B) ($B3$(B)$B!{(BMeng L.$B!&(B Yu X.$B!&(B $B?78+(B $BBsLp(B$B!&(B ($B@5(B)$BD9_7(B $B425,(B$B!&(B ($B@5(B)$B6b;X(B $B@58@(B$B!&(B ($B@5(B)$B5H2,(B $BJ~5W(B$B!&(B ($B@5(B)$BETN1(B $BL-N;(B		Membrane reactor
Organosilica membrane
Methylcyclohexane dehydrogenation
O
659$B%<%*%i%$%HKl$N%_%/%m:Y9&MF@Q$NI>2A$K4X$9$k8!F$(B
($BAaBg@h?JM}9)(B) ($B@5(B)$B!{@%2<(B $B2mGn(B$B!&(B ($B3X(B)$BHSEg(B $BM%5.(B$B!&(B ($B3X(B)$B>>K\(B $BOKJ?(B$B!&(B($BAaBg@h?JM}9)(B/$BAaBgM}9)Am8&(B/JST-CREST) ($B@5(B)$B>>J}(B $B@5I'(B		ZSM-5 membrane
N2 adsorption
Micro-pore volume
O
674Preparation of PVC/VC-co-PEGMA blend membranes and evaluation of their antifouling properties
(Kobe U.) ($B3X(B)$B!{(BZhou Zhuang$B!&(B ($B3X(B)Sun Yuchen$B!&(B ($B3$(B)Rajabzadeh Saeid$B!&(B ($B3$(B)Shaikh Abdul Rajjak$B!&(B ($B@5(B)Kakihana Yuriko$B!&(B ($B@5(B)Matsuyama Hideto		Amphiphilic copolymer
Antifouling membrane
Polyvinyl chloride
P
679Reverse osmosis performance of layered-hybrid membranes consisting of organosilica separation layer on polymer supports
(Hiroshima U.) ($B3$(B)$B!{(BGong G. H.$B!&(B ($B@5(B)Nagasawa H.$B!&(B ($B@5(B)Kanezashi M.$B!&(B ($B@5(B)Yoshioka T.$B!&(B ($B@5(B)Tsuru T.		layered hybrid membrane
organosilica
desalination
O
691$BKl!&N3;R$X$NMO
($BElBg4D0B%;(B) ($B@5(B)$B!{C$L&(B $BNg(B$B!&(B ($BF|Bg@8;:9)(B) ($B@5(B)$B0BF#(B $BEX(B$B!&(B ($BElBg1!9)(B) ($B@5(B)$B>.CS(B $B=$(B$B!&(B ($BElBg4D0B%;(B/$BElBg1!9)(B) ($B@5(B)$BDT(B $B2B;R(B$B!&(B ($BElBg1!9)(B) ($B@5(B)$B;38}(B $BM34tIW(B		microfiltration
hydrodynamics
solute adsorption
O
694Preparation of antifouling PVDF membrane by using a fluorinated amphiphilic copolymer via non-solvent induced phase separation (NIPS) method
(Kobe U.) ($B3X(B)$B!{(BSun Yuchen$B!&(B ($B3X(B)Zhou Zhuang$B!&(B ($B3$(B)Rajabzadeh Saeid$B!&(B ($B@5(B)Kakihana Yuriko$B!&(B (Daikin industries, LTD) ($BK!(B)Ohmukai Yoshikage$B!&(B ($BK!(B)Miki Jun$B!&(B (Kobe U.) ($B@5(B)Matsuyama Hideto		Amphiphilic copolymer
Antifouling membrane
Poly (vinylidene fluoride)
P
695$B?eAGA*BrF)2a%7%j%+Kl$N9g@.5Z$S$=$NKlH?1~4o$H$7$F$N1~MQ(B
($BElBg1!9)(B) ($B3X(B)$B!{@DLn(B $B=U$B!&(B ($B@5(B)$B9b3@(B $BFX(B$B!&(B ($B@5(B)$B?{86(B $B9'(B$B!&(B ($B@5(B)$B5FCO(B $BN4;J(B$B!&(B Oyama S. Ted		silica membrane
CVD
membrane reactor
P
707$B%/%m%9%U%m!<@:L)$m2a$NDj>o%U%i%C%/%9$HN3;RBO@Q>uBV$K4X$9$k8&5f(B
($B9)3X1!Bg9)(B) ($B3X(B)$B!{bCJI(B $BNI(B$B!&(B ($B@5(B)$B@V>>(B $B7{$B!&(B ($B@5(B)$BCfHx(B $B??0l(B		microfiltration
steady state flux
particle deposition
O
716$BIT:.OB$NMO1U3&LL$rMQ$$$?(BZIF-8$BKl$N:n@=(B
($B;:Am8&(B) ($B@5(B)$B!{86(B $B?-@8(B$B!&(B ($B@5(B)$B5H=!(B $BH~5*(B$B!&(B ($B@5(B)$B:,4_(B $B=(G7(B$B!&(B ($B@5(B)$B86C+(B $B8-<#(B$B!&(B ($B@5(B)$B86(B $B=E$B!&(B ($BEl9)Bg(B) ($B@5(B)$B;38}(B $BLT1{(B		Gas separation membrane
Zeolitic imidazolate framework-8
Propylene/propane separation
O
751$B%H%k%(%s$rMQ$$$?BP8~3H;6H?1~@-G.(BCVD$BK!$K$h$kC:AG=$>~%;%i%_%C%/Kl$N:n@=(B
($B9-Bg9)(B) ($B@5(B)$B!{5H2,(B $BJ~5W(B$B!&(B ($B3X(B)$B;3K\(B $B@54p(B$B!&(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 $BL-N;(B		CVD
carbon
ceramic membrane
O
758$B:Y9&Fb=
($BF`NI@hC$B!&(B $BIp;3(B $BGnF;(B$B!&(B ($BCO5e4D6-8&(B) ($B@5(B)$BGO>l(B $BH~CR;R(B$B!&(B ($B@5(B)$BM>8l(B $B9nB'(B		Palladium
Hydrogen
Pore-Fill-type
P
763V$B9g6bKl$K$h$kCbAG!&?eAG:.9g%,%9$+$i$N?eAGJ,N%(B
($BJ*:`5!9=(B) ($B@5(B)$B!{@>B<(B $BKS(B$B!&(B ($BNkLZ>&4[(B) $BLZB<(B $B9@N4(B$B!&(B ($BJ*:`5!9=(B) $Bhq(B $B@/1d(B		vanadium
energy carrier
membrane
O
764$B?;F)05$NH/8=$H<'@-2s<}$rN>N)$9$k5!G=@-HyN3;R$N3+H/(B
($B?@8MBg1!9)(B/$B@hC.@n(B $BBgCO(B$B!&(B ($B@5(B)$B;0Ln(B $BBY;V(B$B!&(B ($B@5(B)$B9b66(B $BCR51(B$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B		Draw solution
Magnetic particles
Forward osmosis
P
766Silicalite$BKl@-G=$K5Z$\$99g@.>r7o1F6A(B
($B4tIlBg1!9)(B) ($B@5(B)$B!{>eLn(B $B63J?(B$B!&(B ($B;:Am8&(B) ($B@5(B)$B:,4_(B $B=(G7(B$B!&(B $BCS>e(B $BE0(B$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 $BLwB'(B		zeolite membrane
separation
bio-ethanol
P
770$B5U?;F)Kl$X$N%j%s;i
($B?@8MBg9)(B) ($B3X(B)$BM?FaNf(B $B85$B!&(B ($B?@8MBg1!9)(B/$B@hC$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B		Reverse osmosis membrane
Atom transfer radical polymerization
Phosphorylcholine polymer
P
773$BAB?e@-M-5!B?9&2$B5[<}B.EY$X5Z$\$91F6A(B
($B?.=#Bg1!M}9)(B) ($B3X(B)$B!{$B!&(B ($B?.=#BgA!0](B) ($B@5(B)$BD9ED(B $B8w@5(B$B!&(B ($B@5(B)$BEhED(B $B8^I4N$(B$B!&(B ($B@5(B)$BJ!D9(B $BGn(B$B!&(B ($B@5(B)$B9b66(B $B?-1Q(B		hydrophobic porous membrane
chemical absroption
EDX
P
778$B:Y9&Fb=
(RITE) ($B@5(B)$B!{GO>l(B $BH~CR;R(B$B!&(B ($B@5(B)$BM>8l(B $B9nB'(B		membrane
hydrogen
permeation
O
789$B%U%'!<%:%U%#!<%k%I%b%G%k$rMQ$$$?(BO/W$B%(%^%k%7%g%s$NKlF)2a%7%_%e%l!<%7%g%s(B
($B?@8MBg1!9)(B/$B@hC$B!&(B ($B3X(B)$B9a@n(B $BM5Je(B$B!&(B ($BF|Bg1!@8J*;q8;(B) ($B@5(B)$B@P?@(B $BE0(B$B!&(B ($B?@8MBg1!9)(B/$B@hC>;3(B $B=(?M(B		Oil water separation
Numerical simulation
Phase-field model
O
799$BBQ05@-$H9bB.(BCO2$BA*BrF)2a@-$rJ;$;;}$D%"%_%N;@%$%*%s1UBN%2%kKl$NAO@=(B
($B?@8MBg1!9)(B/$B@hC$B!&(B Moghadam Farhad$B!&(B ($B3X(B)$B5H=;(B $B0>H~(B$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B		Amino acid ionic liquid
Gel
membrane
O
829$B3Fe$G$N?eJ,;R$N@EE*9=B$$*$h$SF0E*5sF0$K4X$9$kJ,;RO@E*8&5f(B
($B9)3X1!Bg9)(B) ($B3X(B)$B!{CfEg(B $B@?<#(B$B!&(B ($B@5(B)$B9b1)(B $BMN=<(B		antifouling
molecular dynamis
water
P
831$BGSG.MxMQ7??;F)05H/EE$KMQ$$$k29EY1~Ez@-9bJ,;R!?3$?e7O6nF0MO1U$NFC@-I>2A(B
($B?@8MBg1!9)(B/$B@hC$B!&(B ($B?@8MBg9)(B/$B@hC?9(B $B1vJfH~(B$B!&(B ($B?@8MBg1!9)(B/$B@hC$B!&(B $B>.LnED(B $BAp2p(B$B!&(B ($B@5(B)$B;09%(B $BB@O:(B$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B		forward osmosis
pressure retarded osmosis
thermoresponsive polymer
O
839$B?e%A%c%s%M%k$NJ,;RM"Aw5!9=$rLO5<$7$?9b8zN(?eF)2aKl$NM}O@@_7W(B
($B9)3X1!Bg9)(B) ($B3X(B)$B!{>.NS(B $B=YG7=u(B$B!&(B ($B@5(B)$B9b1)(B $BMN=<(B		membrane
aquaporin
water chanel
P
849$BA*BrE*%;%7%&%`5[CeG=$rM-$9$k5!G=2=IT?%I[Kl$NAO@=(B
($BL>Bg9)(B) ($B3X(B)$B!{?eLn(B $BJ8:Z(B$B!&(B ($B@5(B)$B8~0f(B $B9/?M(B		functionalized membrane
cesium removal
nanofiber nonwoven cloth
P
855MFI$B%<%*%i%$%HKlF)2a$K5Z$\$9%"%k%_%K%&%`E:2C$N1F6A(B
($B$B!&(B ($B3X(B)$B?y;3(B $BM:Ht(B$B!&(B ($B3X(B)$BCSED(B $BJb(B$B!&(B ($B3X(B)$B>.Ln(B $BN5J?(B$B!&(B ($B3X(B)$B>>;3(B $B3(H~(B$B!&(B ($B=;M'EE9)(B) $B:XF#(B $B?r9-(B$B!&(B $BI6;3(B $BGn6)(B$B!&(B $B7,86(B $B0lLi(B$B!&(B ($B		MFI zeolite membrane
porous silica substrate
aluminium
P
873$B;Y;}BN>e$N=C4;}>uBV$,(BFAU$B7?%<%*%i%$%HKl$N@=Kl$K5Z$\$91F6A(B
($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!{AR2<(B $B>-8w(B$B!&(B ($B@5(B)$B@%2<(B $B2mGn(B		FAU-type zeolite
Membrane
dehydration
P
903$B%(%A%l%s%W%i%s%H2~NI$N$?$a$N%7%j%+J#9gKl$N8!F$(B
($B>;3(B $B3(H~(B$B!&(B ($B3X(B)$B>.Ln(B $BN5J?(B$B!&(B ($B3X(B)$BCSED(B $BJb(B$B!&(B ($B3X(B)$B:4!9LZ(B $BH~:;(B$B!&(B $BH*;3(B $B<~B"(B$B!&(B $B0pn5(B $BAaLi9a(B$B!&(B $B1|B<(B $B0&(B$B!&(B $BW"@%(B $BCR5W(B$B!&(B $B4XK\(B $B6F(B$B!&(B ($B@5(B)$BLnB<(B $B4490(B		counter diffusion CVD method
silica hybrid membranes
ozone concentration
O
$B9V1i?=$79~$_0lMw(B($B%7%s%]%8%&%`HV9f!&9V1iJ,N`HV9fJL(B)
$B
$B2=3X9)3X2q(B $BBh(B80$BG/2q(B
(C) 2015 $B8x1W
Most recent update: 2015-07-10 15:24:01
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