SCEJ

$B2=3X9)3X2q(B $BBh(B83$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|;~!'(B2018-09-07 21:29:01

$B$3$NJ,N`$G$h$/;H$o$l(B
$B$F$$$k%-!<%o!<%I(B		$B%-!<%o!<%I(B$B
gas separation8$B7o(B**
forward osmosis5$B7o(B*
Membrane4$B7o(B*
ionic liquid4$B7o(B*
molecular dynamics4$B7o(B*
hydrothermal3$B7o(B*
Polyamide3$B7o(B*
carbon membrane3$B7o(B*
membrane separation3$B7o(B*
separation3$B7o(B*
Reverse osmosis membrane2$B7o(B

$B$BHV9f(B$B9V1iBjL\!?H/I=$B%-!<%o!<%I(B$BH/I=7A<0(B
29$B%O%$%V%j%C%I9bJ,;RJ,N%Kl:`NA$K$h$kFs;@2=C:AGJ,N%(B
($BG@9)Bg1!9)(B) ($B@5(B)$B!{7s66(B $B??Fs(B$B!&(B ($BG@9)Bg1!(BBASE) $B2.Ln(B $B8-;J(B$B!&(B (U. Melbourne) Kentish Sandra		Membrane separation
Carbon dioxide
Global warming
O
31$B%P%$%*%,%9$+$i$N?eAG@=B$$N%+!<%\%s%U%j!<2=$rL\E*$H$7$?(BCO2$BJ,N%Kl$N8&5f3+H/(B
($B6eBg(BI2CNER) ($B@5(B)$B!{C+8}(B $B0iM:(B$B!&(B $B0a3^(B $B2B7C(B$B!&(B ($B6eBgE}9g?7NN0h(B) ($B3X(B)$BJw:j(B $B9R4u(B		alkanolamine
CO2
gas separation
O
35$B1UBNJ,N%MQ%7%j%+7OKl$NF)2a%a%+%K%:%`(B
($B$B!&(B ($B3X(B)$B@P0f(B $B9nE5(B$B!&(B ($B3X(B)$BC]Fb(B $B=_EP(B$B!&(B ($B$B!&(B $B5HED(B $B??F`H~(B$B!&(B $B55ED(B $BMNJe(B$B!&(B $B5H1:(B $BkN;R(B$B!&(B ($B@5(B)$BLnB<(B $B4490(B		silica hybrid membrane
permeation mechanism
counter diffusion CVD method
O
49$BBP8~3H;6(BCVD$BK!$K$h$k%,%9J,N%MQ%7%j%+Kl$N@_7W(B
($B$B!&(B ($B3X(B)$BCSED(B $BJb(B$B!&(B ($B$B!&(B $B55ED(B $BMNJe(B$B!&(B $B5H1:(B $BkN;R(B$B!&(B ($B		Counter diffusion CVD method
Gas separation
Silica hybrid membrane
P
51$B%"%/%F%#%V%^%?!<$rMQ$$$?4uEZN`85AG$N8!=P$K$*$1$kNL;R8z2L(B
($B:eBg1!4p9)(B) ($B@5(B)$B!{H<(B $B5.I'(B$B!&(B $B?y;3(B $BNQ>O(B		Active matter
Rare earth elements
Motion-based sensing
O
59$B;THN$N(BPd$B$a$C$-;nLt$rMQ$$$?B?9&
($BFAEgBg1!@hC<650iIt(B) ($B3X(B)$B!{;0Bp(B $BN4B@(B$B!&(B ($BFAEgBg1!$B!&(B ($BT|Ln@=Lt9)6H(B) ($BItK!(B)$B@>0f(B $B>49((B$B!&(B ($BItK!(B)$B4d:j(B $BJ]5*(B$B!&(B ($BItK!(B)$BD9Hx(B $BIR8w(B$B!&(B ($BFAEgBg1!@hC<650iIt(B) ($B@5(B)$B?y;3(B $BLP(B		Pd membrane
porous SUS tube
commercial Pd plating reagent
P
85$B>J%(%MJ?Kl(BMBR$B%b%8%e!<%k$N3+H/(B
($BEl%l(B) ($BK!(B)$B!{2CF#(B $B7E(B$B!&(B ($BK!(B)$B2,K\(B $B595-(B$B!&(B ($BEl%l%7%s%,%]!<%k?e=hM}8&(B) Latt Kyaing Kyaing$B!&(B ($BEl%l(B) ($BK!(B)$B2VED(B $BLP5W(B$B!&(B ($BK!(B)$BLZB<(B $B>-90(B		membrane bioreactor
wastewater treatment
low energy comsumption
O
97$B9b@-G=5U?;F)Kl%(%l%a%s%H(B
($BEl%l(B) ($B@5(B)$B!{9-Bt(B $BMNHA(B$B!&(B ($BK!(B)$B>.@n(B $B5.;K(B$B!&(B ($BK!(B)$B;3ED(B $BGnG7(B$B!&(B ($B@5(B)$BLZB<(B $B>-90(B		Water Treatment
Reverse Osmosis Membrane
spacer
P
118Preparation and formation mechanism of polyethersulfone/sulfonated polyethersulfone ultrafiltration membranes
(Kobe U./MaF Tech C.) ($B3X(B)$B!{(BYang Hui-Yan$B!&(B ($B3$(B)Fang Li-Feng$B!&(B ($B3$(B)Cheng Liang$B!&(B (Nat. Taiwan U.) Wang Da-Ming$B!&(B (Kobe U./MaF Tech C.) ($B@5(B)Matsuyama Hideto		sulfonated polyethersulfone (SPES)
high molecular weight
blend membranes
P
122$BG.2=3X?eAG@=B$$N$?$a$NJ|
($B$B!&(B ($B$B!&(B ($BEh(B $BM[G7(B$B!&(B $B:#NS(B $B?50lO:(B$B!&(B ($BNL8&5!9=(B) $B_7ED(B $B??0l(B$B!&(B $BH,4,(B $BE0Li(B$B!&(B ($B86;RNO5!9=(B) $B5WJ](B $B??<#(B$B!&(B ($B@5(B)$BEDCf(B $B?-9,(B		hermochemical water splitting IS process
ion exchange membrane
Bunsen reaction
O
162$B;@J,N%MQ%7%j%+7O5U?;F)Kl$NF)2a@-$*$h$SBQ5W@-$N8~>e(B
($B$B!&(B ($B3X(B)$BCSED(B $BJb(B$B!&(B ($B3X(B)$B?yK\(B $B@i9I(B$B!&(B $B5H1:(B $BkN;R(B$B!&(B ($B@5(B)$BLnB<(B $B4490(B		reverse osmosis
ceramic
IS process
P
174$B%-%l!<%HG[0L;R$rCr7?$H$9$k%J%NB?9&@-(BTiO2-ZrO2$BJ#9gKl$N:n@=$H@-G=I>2A(B
($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 ($B@5(B)$B?7C+(B $BBn;J(B$B!&(B ($B?@8MBg1!9)(B/$B@hC$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B		Ceramic membrane
Chelating ligand
Nanofiltration
P
186$B%]%j%1%H%sKl$N%"%_%s=$>~$K$h$kBQ05@-8~>e$NMW0x$H@5?;F)Kl$X$N1~MQ(B
($B?@8MBg1!2J5;%$%N%Y(B/$B@hCUNn@n(B$B!&(B ($B@5(B)$BCf@n(B $B7I;0(B$B!&(B ($B@5(B)$BJ}(B $BN)Jv(B$B!&(B ($B?@8MBg1!9)(B/$B@hC$B!&(B ($B?@8MBg1!2J5;%$%N%Y(B/$B@hC$B!&(B ($B@5(B)$B5H2,(B $BJ~5W(B$B!&(B ($B?@8MBg1!9)(B/$B@hC$B!&(B ($B@5(B)$B?@Hx(B $B1Q<#(B$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B		polyketone membrane
pressure resistance
amine modification
P
197$BM-5!MOG^BQ@-$rM-$9$k%]%j%"%_%I7OJ#9gGvKl$N3+H/(B
($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)$BD9C+@n(B $B?J(B$B!&(B ($B?@8MBg1!2J5;%$%N%Y(B/$B@hC$B!&(B ($B?@8MBg1!9)(B/$B@hC>;3(B $B=(?M(B$B!&(B ($B?@8MBg1!2J5;%$%N%Y(B/$B@hC		Organic solvent resistance
Polyamide
Thin-film composite
P
199$B%"%_%I;@7?%-%c%j%"Jq@\9bJ,;RKl$K$h$k%9%+%s%8%&%`$NKlJ,N%$HKlF)2a5!9=$N2r@O(B
($B6eBg1!9)(B) ($B3X(B)$B!{5HED(B $B9R(B$B!&(B ($B@5(B)$B5WJ]ED(B $BIY@8;R(B$B!&(B (U. Melbourne) Kolev S. D$B!&(B ($B6eBg1!9)(B) ($B@5(B)$B8eF#(B $B2m9((B		Polymer Inclusion Membrane
Critical Metals
Separation
O
206$BJ,;R%7%_%e%l!<%7%g%s$K$h$k%]%j%"%_%IKl@_7W$H(BFO/RO$BF)?e@-G=I>2A(B
($B?@8MBg1!2J5;%$%N%Y(B) ($B3X(B)$B!{8E9b(B $B7<2p(B$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 ($B7*ED9)6H(B) ($BK!(B)$B@n>!(B $B9'Gn(B$B!&(B ($BK!(B)$BF#B<(B $BPR(B$B!&(B ($B?@8MBg1!9)(B) ($B3X(B)Wu Hao-Chen$B!&(B ($B@5(B)$B:4Gl(B $BBgJe(B$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B		Molecular dynamics
Polyamide
Water permeability
P
212$B?;F)5$2=K!$K$h$k?e(B/$B?];@:.9g1U$NC&?e$rL\E*$H$7$?BQ;@@-Kl$N9g@.(B
($B4tIlBg9)(B) ($B3X(B)$B!{0f>e(B $BNhF`(B$B!&(B ($B4tIlBg1!9)(B) ($B3X(B)$B>eLn(B $B63J?(B$B!&(B ($B3X(B)$B7*ED(B $BM'Je(B$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 $BLwB'(B		layered silicate membrane
separation
acetic acid
P
217$B%"%_%N;@%$%*%s1UBN4^M-%2%kGvKl$NAO@=$H$=$N(BCO2$BF)2a5!9=$N2rL@(B
($B?@8MBg1!9)(B) ($B3X(B)$B!{C+8}(B $B=((B$B!&(B ($B@5(B)$B?@Hx(B $B1Q<#(B$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B		gas separation
ionic liquid
gel
P
221$BJ,;RF0NO3XK!$rMQ$$$?%$%*%s1UBN?eMO1U$NFC@-I>2A$H@5?;F)KlF)2a%7%_%e%l!<%7%g%s(B
($B?@8MBg1!2J5;%$%N%Y(B) ($B3X(B)$B!{:4ED5W(B $B$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 ($B2,;3Bg1!<+(B) ($B@5(B)$B;0Ln(B $BBY;V(B$B!&(B ($B?@8MBg1!9)(B) ($B@5(B)$B9b66(B $BCR51(B$B!&(B ($B@5(B)$B?@Hx(B $B1Q<#(B$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B		ionic liquid
molecular dynamics
forward osmosis
P
226$B@5?;F)Kl$NA*BrF)2a@-$N8~>e$HE|1UG;=L$*$h$S%P%$%*%(%?%N!<%k@8;:$K5Z$\$98z2L(B
($B?@8MBg1!2J5;%$%N%Y(B/$B@hC(B$B!&(B ($B@5(B)$BCf@n(B $B7I;0(B$B!&(B ($B?@8MBg1!2J5;%$%N%Y(B) $B:4!9LZ(B $B7z8c(B$B!&(B ($B?@8MBg1!9)(B/$B@hC$B!&(B ($B@5(B)$B9b66(B $BCR51(B$B!&(B ($B?@8MBg1!2J5;%$%N%Y(B/$B@hC$B!&(B ($B@5(B)$B5H2,(B $BJ~5W(B$B!&(B ($B?@8MBg1!9)(B/$B@hC$B!&(B ($B@5(B)$B4_K\(B $BDL2m(B$B!&(B ($B@5(B)$B?@Hx(B $B1Q<#(B$B!&(B ($B?@8MBg1!2J5;%$%N%Y(B) ($B@5(B)$B6aF#(B $B>$B!&(B ($B?@8MBg1!9)(B/$B@hC>;3(B $B=(?M(B		bioethanol
forward osmosis
surface modification
P
227LCST$B7?AjE>0\:`NA$r:nMQG^BN$H$9$k%*%9%b%F%#%C%/%R!<%H%(%s%8%s$NH/EE%]%F%s%7%c%kI>2A(B
($B?@8MBg1!9)(B/$B@hC$B!&(B ($B@5(B)$B9b66(B $BCR51(B$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B		pressure retarded osmosis
LCST
osmotic heat engine
P
271$BCf6u;eKl$rMxMQ$7$?@5?;F)K!$*$h$S5U?;F)K!$K$*$1$kKl%U%!%&%j%s%0FC@-$NHf3S8!F$(B
($B?@8MBg1!2J5;%$%N%Y(B/$B@hC->0(B$B!&(B ($B@5(B)$BCf@n(B $B7I;0(B$B!&(B ($B?@8MBg1!9)(B/$B@hC$B!&(B ($B?@8MBg1!2J5;%$%N%Y(B/$B@hC$B!&(B ($B@5(B)$B5H2,(B $BJ~5W(B$B!&(B ($B?@8MBg1!9)(B/$B@hC$B!&(B ($B@5(B)$B?@Hx(B $B1Q<#(B$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B		membrane fouling
forward osmosis
hollow fiber membrane
P
272$B6bB0:xBN7O%$%*%s1UBN$N;@AG5[<}B.EY$K$*$1$k%+%A%*%s%5%$%:$N1F6A(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 $B=(?M(B		ionic liquids
oxygen carrier
absorption kinetics
P
273$B%U%C2=J*%U%j!<9g@.>r7o2<$K$*$1$k(BAlPO4-34$BKl$N7A@.$K9g@.%2%k$NAH@.$,5Z$\$91F6A(B
($BAaBg@h?JM}9)(B) ($B3X(B)$B!{J!ED(B $B9IKo(B$B!&(B (RITE) ($B@5(B)$B@%2<(B $B2mGn(B$B!&(B ($BAaBg@h?JM}9)(B/$BAaBgM}9)8&(B) ($B@5(B)$B>>J}(B $B@5I'(B		Fluoride-free
AlPO4-34 membrane
Gel composition
P
277$B;0
($B?@8MBg(B) ($B@5(B)$B!{D9C+@n(B $B?J(B$B!&(B ($B@5(B)$B;09%(B $BB@O:(B$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B		Membrane fouling
EEM
Fouling
O
307$B29EY(B/CO2$B1~Ez@-$rM-$9$k%G%s%I%j%^!<$NJ,;R@_7W$H@5?;F)6nF0MO2A(B
($B?@8MBg1!9)(B/$B@hC?9(B $B1vJfH~(B$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 $B=(?M(B		forward osmosis
LCST
tertiary amine
P
316$B?F?e@-%$%*%s1UBN=$>~%7%j%+Kl$N3+H/$H%a%?%N!<%kJ,N%$X$N1~MQ(B
($B:eBg1!4p9)(B) ($B@5(B)$B!{W"ED(B $BM:0lO/(B$B!&(B ($B3X(B)$B;3K\(B $BM42p(B$B!&(B ($B3X(B)$BCf5o(B $BBsEM(B$B!&(B ($B:eBg4p9)(B) $BB.?e(B $BfFJ?(B$B!&(B ($B:eBg1!4p9)(B) ($B@5(B)$B@>;3(B $B7{OB(B		organosilica membrane
ionic liquid
methanol separation
O
317$B%$%*%s1UBN=$>~%7%j%+Kl$N%,%9J,N%$X$N1~MQ(B
($B:eBg1!4p9)(B) ($B3X(B)$B!{Cf5o(B $BBsEM(B$B!&(B ($B:eBg4p9)(B) ($B3X(B)$BB.?e(B $BfFJ?(B$B!&(B ($B:eBg1!4p9)(B) ($B3X(B)$B;3K\(B $BM42p(B$B!&(B ($B@5(B)$BW"ED(B $BM:0lO/(B$B!&(B ($B%$!<%;%C%W(B) ($B@5(B)$B_7B<(B $B7r0l(B$B!&(B ($B:eBg1!4p9)(B) ($B@5(B)$B@>;3(B $B7{OB(B		organosilica membrane
ionic liquid
gas separation
P
321$BJ,;R%7%_%e%l!<%7%g%s$K$h$k?75,%]%j%$%_%IKl$N9=B$@_7W$H5$BNF)2aFC@-I>2A(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 ($B%+%M%+(B) ($BK!(B)$BF#86(B $B42(B$B!&(B ($B?@8MBg1!9)(B/$B@hC$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B		polyimide membrane
molecular simulation
gas separation
P
362$BC:2=?eAGJ,N%$rBP>]$H$7$?(BMFI$B7?%<%*%i%$%H$K$*$1$kB?@.J,%,%9F)2a%b%G%k$N9=C[(B
($B9)3X1!Bg@h?J9)(B) ($B3X(B)$B!{W"_7(B $B;KLi(B$B!&(B ($B@5(B)$B9b1)(B $BMN=<(B		Zeolite membrane
Non Equilibrium Molecular Dynamics
Multicomponent gas
P
367AlPO $B%<%*%i%$%HKl$N:n@=$HF)2aFC@-(B
($B;38}Bg1!M}(B) ($B3X(B)$B!{8b(B &#23159;$B!&(B ($B9>@>;UHOBg(B) $BDD(B $B>M$B!&(B ($B;38}Bg1!M}(B) ($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 $B1QIR(B		AlPO zeolite membranes
single DIPEA template
separation properties
O
371$BJ,;RF0NO3XK!$K$h$k9bJ,;R:`NAI=LL$NCf4V?e!&ITE`?e$NDjNL2=(B
($B9)3X1!Bg@h?J9)(B) ($B3X(B)$B!{$B!&(B ($BF|K\?(G^(B) ($BK!(B)$B>.NS(B $BD>5-(B$B!&(B ($BK!(B)$B@PED(B $BCN;K(B$B!&(B ($BK!(B)$BCfED(B $BA1CN(B$B!&(B ($B9)3X1!Bg@h?J9)(B) ($B@5(B)$B9b1)(B $BMN=<(B		Intermediate Water
Non-freezing Water
Molecular Dynamics
P
407$B9b299b05?e>x5$$,(BNa-ZSM-5$BKl9=B$$KM?$($k1F6A(B
($BAaBg@h?JM}9)(B) ($B3X(B)$B!{66D^(B $BM:M$(B$B!&(B ($BAaBg%J%N%i%$%U(B) ($B@5(B)$B@%2<(B $B2mGn(B$B!&(B ($BAaBg@h?JM}9)(B) ($B3X(B)$BM'ED(B $B2mBg(B$B!&(B ($BAaBg@h?JM}9)(B/$BAaBgM}9)Am8&(B) ($B@5(B)$B>>J}(B $B@5I'(B		Na-ZSM-5
steam stability
membrane
P
411$B%<%*%i%$%H$+$i$N(BN2$BC&Ce8=>]$N?75,B,DjK!$N8!F$(B
($BAaBg@h?JM}9)(B) ($B3X(B)$B!{>.NS(B $B8<51(B$B!&(B ($BAaBg%J%N%i%$%U(B) ($B@5(B)$B$B!&(B ($BAaBg@h?JM}9)(B/$BAaBgM}9)8&(B) ($B@5(B)$B>>J}(B $B@5I'(B		desorption
carbon-deposition
silicalite-1
P
412$B%<%*%i%$%HKl>e$KC4;}$5$l$?(BAg+$B%+%A%*%s$N@-
($BAaBg@h?JM}9)(B) ($B3X(B)$B!{F#4,(B $B>0;V(B$B!&(B ($BAaBg%J%N%i%$%U(B) ($B@5(B)$B$B!&(B ($BAaBg@h?JM}9)(B/$BAaBgM}9)8&(B) ($B@5(B)$B>>J}(B $B@5I'(B		zeolite
Ag
membrane
P
419$B>t?eMQ%<%*%i%$%HKl>u5[Ce:`$N3+H/(B
($BH5W(B$B!&(B ($B$B!&(B ($B$B!&(B ($B$B!&(B ($B%?%+%.(B) $BHD0f(B $BK-=<(B$B!&(B $BEDCf(B $B9/M5(B$B!&(B $B>>Hx(B $BM[(B$B!&(B $B3^(B $B?8Je(B		membrane
MFI
water purification
P
426$BFs=$,5Z$\$91F6A(B
($B4tIlBg1!<+(B) ($B3X(B)$B!{ClLn(B $BBsLi(B$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 $B@.G7(B		Metal Organic Framework
Membrane separation
Secondary growth
P
428$BEE5$F)@OGS?eCf$N(B2$B2AM[%$%*%s$H(B2$B2A1"%$%*%s$rJ,N%$9$k?75,%J%N_I2aKl$N3+H/(B
($B?@8MBg1!2J5;%$%N%Y(B/$B@hC($B?@8MBg1!2J5;%$%N%Y(B) ($B@5(B)$B?7C+(B $BBn;J(B$B!&(B ($B9)3X1!Bg@h?J9)(B) ($B@5(B)$B@V>>(B $B7{$B!&(B ($B?@8MBg1!2J5;%$%N%Y(B) ($B@5(B)$BCf@n(B $B7I;0(B$B!&(B ($B?@8MBg1!9)(B) ($B@5(B)$B9b66(B $BCR51(B$B!&(B ($B@5(B)$BD9C+@n(B $B?J(B$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B$B!&(B ($B?@8MBg1!2J5;%$%N%Y(B) ($B@5(B)$B5H2,(B $BJ~5W(B		Nanofiltration
Ion separation
Polyamide
P
445CO2$BJ,N%Kl$X$N1~MQ$rL\;X$7$?%$%*%s1UBN4^M-L55!!?M-5!(Bdouble network$B%2%k$N3+H/(B
($B?@8MBg1!9)(B/$B@hC$B!&(B ($B@5(B)$B?@Hx(B $B1Q<#(B$B!&(B ($B3X(B)$BHSED(B $BM4(B$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B		Ion gel
Double network gel
Gas separation membrane
O
453ATRP$B$K$h$k;THN%]%j%"%_%I5U?;F)Kl$NI=LL2~2A(B
($B?@8MBg1!9)(B/$B@hC$B!&(B $BML(B $BE/(B$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B		Polyamide reverse osmosis membranes
Surface-initiated atom transfer radical polymerization
Anti-biofouling
O
468$B%*%$%k4^M-?e$N%;%i%_%C%/Kl_I2a$K4X$9$k8&5f(B
($B9-Bg1!9)(B) $B>.B<(B $BBsLi(B$B!&(B ($B@5(B)$BD9_7(B $B425,(B$B!&(B ($B@5(B)$B6b;X(B $B@58@(B$B!&(B ($B@5(B)$B!{ETN1(B $BL-N;(B		ceramic membranes
O/W emulsion
produced water
O
477$B%0%k%3!<%9?eG.K!$G:n@=$7$?%+!<%\%sKl$N:Y9&7B@)8f$H%,%9F)2a@-$NI>2A(B
($BEl9)BgJ*$B!&(B ($B@5(B)$B0kIt(B $BIR9((B$B!&(B ($B6eBgCf1{J,@O(B) $B0pED(B $B44(B$B!&(B ($BEl9)BgJ*>2<(B $B>M;R(B$B!&(B $BCfEg(B $B>O(B		carbon membrane
hydrothermal
gas separation
P
480$BKl:Y9&$rLOJo$7$?%^%$%/%m%A%c%M%kFb$K$*$1$k%@%V%k%(%^%k%7%g%s$NJ,Nv5sF0(B
($B9)3X1!Bg@h?J9)(B) ($B@5(B)$B!{@V>>(B $B7{$B!&(B $BJw:j(B $B9R4u(B$B!&(B ($B@iMUBg1!9)(B) ($B@5(B)$B;3ED(B $B??@!(B$B!&(B ($B@5(B)$B4X(B $B$B!&(B ($B9)3X1!Bg@h?J9)(B) ($B@5(B)$BCfHx(B $B??0l(B		double emulsion
splitting
pore
O
485$BE|N`?eG.K!$K$h$k%+!<%\%sKl$N:n@=$H%,%9F)2a@-$NI>2A(B
($BEl9)BgJ*$B!&(B ($B3X(B)$B:4Ln(B $BfF:H(B$B!&(B ($BEl9)Bg9)(B) ($B3X(B)$BCfB<(B $BMN2p(B$B!&(B ($B6eBgCf1{J,@O(B) $B0pED(B $B44(B$B!&(B ($BEl9)BgJ*>2<(B $B>M;R(B$B!&(B $BCfEg(B $B>O(B		carbon membrane
hydrothermal
gas separation
O
495$B9b29>r7o2<$G$N?eAG!?C:2=?eAGJ,N%MQ%<%*%i%$%HKl$N3+H/(B
($BAaBg@h?JM}9)(B) ($B3X(B)$B!{5H86(B $B7D(B$B!&(B ($BAaBg%J%N%i%$%U(B) ($B@5(B)$B$B!&(B ($BAaBg@h?JM}9)(B/$BAaBgM}9)8&(B) ($B@5(B)$B>>J}(B $B@5I'(B		zeolite membrane
dehydrogenation
membrane reactor
P
524Fabrication and performance optimization of alkylamine-silica membranes for high-efficiency CO2 transport
(Hiroshima U.) ($B3$(B)$B!{(BYu Liang$B!&(B ($B@5(B)Kanezashi Masakoto$B!&(B ($B@5(B)Nagasawa Hiroki$B!&(B ($B@5(B)Tsuru Toshinori		alkylamine-silica membrane
mild affinity
carbon dioxide separation
O
525$B%0%k%3!<%9(B-$B%"%s%b%K%":.9g?eMO1U$+$i:n@=$7$?%+!<%\%sKl$N%,%9F)2a@-$NI>2A(B
($BEl9)Bg9)(B) ($B3X(B)$B!{CfB<(B $BMN2p(B$B!&(B ($BEl9)BgJ*$B!&(B ($B6eBgCf1{J,@O(B) $B0pED(B $B44(B$B!&(B ($BEl9)BgJ*>2<(B $B>M;R(B$B!&(B $BCfEg(B $B>O(B		carbon membrane
hydrothermal
gas separation
P
527$BM6EEBN%P%j%"J|EEH?1~4o$K$h$k%7%j%+Kl$N%W%i%:%^(BCVD$B@=Kl(B
($B9-Bg1!9)(B) ($B@5(B)$B!{D9_7(B $B425,(B$B!&(B ($B3X(B)$B9a@n(B $B5.I'(B$B!&(B ($B@5(B)$B6b;X(B $B@58@(B$B!&(B ($B@5(B)$BETN1(B $BL-N;(B		Silica membranes
Dielectric barrier discharge
Plasma-enhanced CVD
O
534$B%S%K%k%T%m%j%I%s7O%*%j%4%^!<$N=E9gEY$H3H;678?t$N4X78(B: $B7W;;2=3XE*2r@O(B
($BL>9)Bg(B) ($B3X(B)$B!{;3K\(B $B7rB@(B$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 $B=(		diffusion coefficient
molecular dynamics
vinyl pyrrolidone
P
607$BBP8~3H;6(BCVD$BK!$K$h$k9b?eAGA*BrF)2a@-%7%j%+Kl$N3+H/(B
(RITE) ($B@5(B)$B!{1:0f(B $B9(H~(B$B!&(B ($B@5(B)$B@>Ln(B $B?N(B$B!&(B ($B@5(B)$B@%2<(B $B2mGn(B$B!&(B ($B@5(B)$B@>ED(B $BN<0l(B$B!&(B ($B@5(B)$BCfHx(B $B??0l(B		silica membrane
CVD
hydrogen
O
624$B%/%m%9%U%m!<@:L)Kl$m2a%7%_%e%l!<%7%g%s$K$h$k9b$;$sCG>l$G$NKlLLBO@QN3;R$N5sF0(B
($BF|Bg@8;:9)(B) ($B3X(B)$B!{F#J?(B $BBsO/(B$B!&(B ($B@5(B)$B0BF#(B $BEX(B$B!&(B (PIA) ($B@5(B)$B>.CS(B $B=$(B$B!&(B ($BElBg4D0B%;(B) ($B@5(B)$BC$L&(B $BNg(B		crossflow
high shear field
simulation
P
663$B%0%j%;%m!<%k9|3J$rM-$9$k(BLCST$B7?AjE>0\%]%j%^!<$N3+H/$H@5?;F)%I%m!2A(B
($B?@8MBg1!9)(B/$B@hC$B!&(B ($B?@8MBg9)(B/$B@hC$B!&(B ($B?@8MBg1!9)(B/$B@hC$B!&(B ($B%@%$%;%k(B) ($BK!(B)$B66D^(B $BM[;R(B$B!&(B ($B?@8MBg1!9)(B/$B@hC>;3(B $B=(?M(B		forward osmosis
draw solute
thermoresponsive polymer
O
666$BAB?e@-%7%j%+Kl$rMQ$$$?M-5!MOG^%J%N$m2a%W%m%;%9$N3+H/(B
($B4X@>Bg4DET9)(B) ($B@5(B)$B!{9SLZ(B $BDgIW(B$B!&(B $BCfED(B $B>;?-(B$B!&(B ($B@5(B)$B;3K\(B $B=(		OSN
silica membrane
hydrophobic
O
669CHA$B7?%<%*%i%$%HKl$rMQ$$$?M-5!Fs@.J,7O$NJ,N%(B
($B4X@>Bg4DET9)(B) ($B3X(B)$B!{Bg5WJ](B $BM%EM(B$B!&(B $B5\K\(B $B?NH~(B$B!&(B ($BF|N)B$A%(B) ($BK!(B)$B:#:d(B $BNg;K(B$B!&(B ($B4X@>Bg4DET9)(B) ($B@5(B)$B9SLZ(B $BDgIW(B$B!&(B ($B@5(B)$B;3K\(B $B=(		Zeolite
Chabazite
Membrane
P
676$B:?D9$N0[$J$k;i2A(B
($B?@8MBg1!9)(B/$B@hC$B!&(B ($B@5(B)$B:4Gl(B $BBgJe(B$B!&(B $B7'C+(B $BOBIW(B$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B		Amphotericin B
Liposome
Water permeability
P
681ZnO$BCf6u;e$N9g@.$H(BZIF-8$BE>49$X$N8!F$(B
($B4X@>Bg4DET9)(B) ($B3X(B)$B!{:4F#(B $BD>EP(B$B!&(B ($B3X(B)$BBg5WJ](B $BM%EM(B$B!&(B $B:#:d(B $BNg;K(B$B!&(B ($B@5(B)$B9SLZ(B $BDgIW(B$B!&(B ($B@5(B)$B;3K\(B $B=(		ZnO
Hollow fiber
ZIF-8
P
692$B@5?;F)Kl$K$*$1$kJ,;RF)2a$N%@%$%J%_%/%9(B
($B9)3X1!Bg@h?J9)(B) ($B3X(B)$B!{Hu8}(B $BH;?M(B$B!&(B ($B@5(B)$B9b1)(B $BMN=<(B		Water Selective Membrane
Nonequilibrium Molecular Dynamics
Osmotic Pressure
P
693$B>xN1BeBX$rL\;X$7$?(BY$B7?%<%*%i%$%HKl$K$h$k5U?;F)J,N%$NJ,;R%7%_%e%l!<%7%g%s(B
($B9)3X1!Bg9)(B) ($B3X(B)$B!{CfC+(B $BM%EM(B$B!&(B ($B@5(B)$B9b1)(B $BMN=<(B		Reverse osmosis membrane
zeolite-Y
Non-equilibrium molecular dynamics
P
703$B9bJ,;RJq4^Kl$rMQ$$$?5.6bB0$NJ,N%2s<}(B
($B6eBg1!9)(B) ($B3X(B)$B!{2OLn(B $BN$Jf(B$B!&(B ($B3X(B)$B5HED(B $B9R(B$B!&(B ($B@5(B)$B5WJ]ED(B $BIY@8;R(B$B!&(B ($B@5(B)$B8eF#(B $B2m9((B		Polymer Inclusion Membrane
precious metals
separation
P
727$B%]%j%$%_%IM3MhC:AGJ#9gKl$N%,%9F)2aFC@-$K5Z$\$9(BCVD$B>r7o$N1F6A(B
($B;38}Bg1!AO@.2J3X(B) ($B3X(B)$B!{@uLn(B $BBsLi(B$B!&(B ($B;38}Bg9)(B) $B5H_7(B $BE5??(B$B!&(B ($B;38}Bg1!AO@.2J3X(B) ($B3X(B)$BCfB<(B $BM*Je(B$B!&(B ($B@5(B)$BEDCf(B $B0l9((B$B!&(B ($B@5(B)$B4nB?(B $B1QIR(B		carbon membranes
hydrogen separation
P
761$BKlMxMQO"B3H/9Z%W%m%;%9$K$*$1$kDc%U%!%&%j%s%0Kl$N3+H/(B
($BEl%l(B) ($BK!(B)$B!{;VB<(B $BIgH~(B$B!&(B ($BK!(B)$B>.4d(B $B2mOB(B$B!&(B ($BK!(B)$BH+J?(B $BCR;R(B$B!&(B ($BK!(B)$BLZB<(B $B>-90(B		low fouling
membrane separation
fermentation
P
762$B%J%N%2%kEII[Kl$NB?9&@-;Y;}Kl$N9&7B$H3+9&N($,(B $B@.Kl7k2L$*$h$SKlJ,N%@-G=$KM?$($k1F6A(B
($B6eBg1!9)(B) ($B@5(B)$B!{:#B<(B $BOB;K(B$B!&(B ($B3X(B)$B9TIt(B $BCRMN(B$B!&(B ($B3X(B)$BK\ED(B $BN5B@O/(B$B!&(B ($B6eBg(BI2CNER) ($B@5(B)$BC+8}(B $B0iM:(B$B!&(B ($B6eBg1!9)(B) ($B@5(B)$B@1Ln(B $BM'(B$B!&(B ($B@5(B)$B;01:(B $B2B;R(B		support membrane
porosity
CO2
P
784TiO2-ZrO2-$BM-5!%-%l!<%HG[0L;RJ#9g%,%9J,N%Kl$N:n@=$H(BCO2$BF)2aFC@-$NI>2A(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>>;3(B $B=(?M(B		TiO2-ZrO2
Carbon dioxide separation
Organic chelate ligand
P
$B9V1i?=$79~$_0lMw(B($B%7%s%]%8%&%`HV9f!&9V1iJ,N`HV9fJL(B)
$B
$B2=3X9)3X2q(B $BBh(B83$BG/2q(B
(C) 2018 $B8x1W
Most recent update: 2018-09-07 21:29:01
For more information contact $B2=3X9)3X2q(B $BBh(B83$BG/2q(B $B
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