SCEJ

$B2=3X9)3X2q(B $BBh(B51$B2s=)5(Bg2q(B (2020)

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SY-61. [$BJ,N%%W%m%;%9It2q%7%s%]%8%&%`(B] (5) $BJ,N%Kl!&Kl%W%m%;%93+H/$N:G?7F08~(B

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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
membrane4$B7o(B*
organosilica membrane4$B7o(B*
Zeolite3$B7o(B*
gas separation2$B7o(B
Surface modification2$B7o(B
polymer gas separation membrane2$B7o(B
Vapor permeation2$B7o(B
mixed matrix membrane2$B7o(B
CO2 separation2$B7o(B
mesoporous1$B7o(B

$B$BHV9f(B$B9V1iBjL\!?H/I=$B%-!<%o!<%I(B$BH/I=7A<0(B
27[$B8&5f>)Ne>^(B] $B%$%*%s1UBN$NFC@-$r<($9%*%k%,%N%7%j%+Kl$N3+H/$H$=$N%,%9!&>x5$F)2a5!9=I>2A$K4X$9$k8&5f(B
($B:eBg1!4p9)(B) ($B@5(B)$BW"ED(B $BM:0lO/(B		The SCEJ Award for Outstanding Young Researcher
O
74FAU$B%<%*%i%$%HKl9g@.$K$*$1$kB?9&
($B$B!&(B $BD9ED(B $BCN;N(B$B!&(B $BLZB<(B $BM%9a(B$B!&(B ($B3X(B)$B@P0f(B $B9nE5(B		FAU zeolite membrane
Porous substrate
Statistics investigation
O
104[$BM%=(O@J8>^(B] $B9bJ,;RB?9&Kl$r;Y;}BN$H$9$k%*%k%,%N%7%j%+(Blayered hybrid$BKl$N%>%k(B-$B%2%k@=Kl$K$*$1$k=L=E9g29EY$N1F6A$H>x5$F)2aFC@-(B
($B9-Bg1!@h?JM}9)(B) ($B@5(B)$B!{D9_7(B $B425,(B$B!&(B ($B9-Bg1!9)(B) ($B3X(B)$BB$B!&(B ($B9-Bg1!@h?JM}9)(B) ($B@5(B)$B6b;X(B $B@58@(B$B!&(B ($B@5(B)$BETN1(B $BL-N;(B		organosilica membrane
layered hybrid membrane
vapor permeation
O
120$BBP8~3H;6(BCVD$B%7%j%+Kl$N>xCe%3%s%H%m!<%k(B
($B$B!&(B ($B@5(B)$BLnB<(B $B4490(B$B!&(B ($B9)3X1!Bg@h?J9)(B) ($B3X(B)$BHu8}(B $BH;?M(B$B!&(B ($B@5(B)$B9b1)(B $BMN=<(B		Silica membrane
Counter diffusion CVD
O
166$B%$%*%sHt@W%0%i%U%H=E9gK!$K$h$k%h%&2=?eAGG;=LMQ%+%A%*%s8r49Kl$N3+H/(B
($B$B!&(B ($B$B!&(B ($BNL8&5!9=(B) $B_7ED(B $B??0l(B$B!&(B $B1[@n(B $BGn(B$B!&(B $BH,4,(B $BE0Li(B		Ion exchange membrane
Ion-track graft polymerization
IS process
O
201$BI=LL=$>~%J%NN3;R$r4^M-$7$?9bJ,;RJ#9gKl$N5$BNF)2aFC@-(B:$BN3;R7A>u$H=$>~@$Be?t$N1F6A(B
($BETN)Bg1!ET;T4D6-(B) ($B3X(B)$B!{El(B $B$7$*$j(B$B!&(B $BEDCf(B $B3X(B$B!&(B ($B@5(B)$B;3EP(B $B@5J8(B$B!&(B ($B@5(B)$B@n>e(B $B9@NI(B		mixed matrix membrane
polymer gas separation membrane
surface modification
O
207$BI=LL=$>~%J%NN3;R$r4^M-$7$?9bJ,;RJ#9gKl$N5$BNF)2aFC@-(B:$B5$BNF)2a5!9=$K$D$$$F$N9M;!(B
($BETN)Bg1!ET;T4D6-(B) ($B@5(B)$B!{;3EP(B $B@5J8(B$B!&(B ($B@5(B)$B@n>e(B $B9@NI(B		mixed matrix membrane
polymer gas separation membrane
Xe NMR
O
250$BBQ;@2=@-$rM-$9$k(BSiOC$B9=B$@_7W$HJ,;R$U$k$$Kl$X$N1~MQ(B
($B9-Bg1!9)(B) ($B3X(B)$B!{5\yu(B $BCRG7(B$B!&(B ($B@5(B)$B6b;X(B $B@58@(B$B!&(B ($B@5(B)$BD9_7(B $B425,(B$B!&(B ($B@5(B)$BETN1(B $BL-N;(B		SiOC structure
gas permeation property
oxidation stability
O
320Controlling the formation of porous polyketone membranes via a cross-linkable alginate additive for oil-in-water emulsion separations
(Kobe U.) ($B@5(B)$B!{(BGuan Kecheng$B!&(B ($B3X(B)Zhang Lei$B!&(B ($B3X(B)Wang Shengyao$B!&(B ($B@5(B)Takagi Ryosuke$B!&(B ($B@5(B)Matsuyama Hideto		polyketone membrane
alginate
phase separation
O
343$BCf9b29$K$*$1$k?e>x5$2s<}$N$?$a$N%*%k%,%N%7%j%+Kl$N3+H/(B
($B9-Bg1!9)(B) ($B3X(B)$B!{?9;3(B $B65MN(B$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 $BL-N;(B		Steam recovery
Vapor permeation
Organosilica membrane
O
347Layered-hybrid$B6bB0%I!<%W%*%k%,%N%7%j%+Kl$rMQ$$$?%"%k%3!<%k?eMO1UC&?e(B
($B9-Bg1!9)(B) ($B3X(B)$B!{;{Hx(B $BN4;V(B$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 $BL-N;(B		layered-hybrid
metal dope
organosilica membrane
O
359CHA$BKl$N(BCO2$BJ,N%FC@-$N05NO0MB8@-$K4X$9$kJ,;RO@E*9M;!(B
($B9)3X1!Bg@h?J9)(B) ($B3X(B)$B!{W"_7(B $B;KLi(B$B!&(B ($B@5(B)$B5\@n(B $B2mLp(B$B!&(B ($B@5(B)$B9b1)(B $BMN=<(B		CHA membrane
Non equilibrium molecular dynamics
High pressure condition
O
388One step surfactant entrapment onto PVDF hollow fiber membrane surface before phases separation during air gap distance in the TIPS process by using a triple-layer orifice spinneret
(Kobe U.) ($B@5(B)$B!{(BRajabzadeh Saeid$B!&(B ($B@5(B)Fang Chuanjie$B!&(B ($B3X(B)Zhang Pengfei$B!&(B ($B@5(B)Kato Noriaki$B!&(B ($B@5(B)Matsuyama Hideto		surfactant entrapment
PVDF hollow fiber membrane
triple-layer orifice spinneret
O
435C2$B!A(BC4$BC:2=?eAG$H(BAg-X$BKl$N?FOB@-$HA*Br@-$N4X78(B
($BAaBg@h?JM}9)(B) ($B3X(B)$B!{ETC[(B $BM4?M(B$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 $B@5I'(B		zeolite
Ag
membrane
O
437$B%*%k%,%N%7%j%+Kl$K$h$kM-5!MOG^:.9g1U$N9bEYJ,N%(B
($B9-Bg1!9)(B) $BF!(B $B4'1Q(B$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 $BL-N;(B		organosilica membrane
organic solvent mixture
pervaporation
O
439$B%<%*%i%$%H?(G^Kl$N3+H/$HC:2=?eAGJ,2rG=$N8!F$(B
($BAaBg@h?JM}9)(B) ($B3X(B)$B!{66K\(B $BM/51(B$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 $B@5I'(B		zeolite
membrane
catalyst
O
457$B:Y9&7B@)8f$7$?%U%CAG%I!<%W%*%k%,%N%7%j%+Kl$NC:2=?eAGF)2aFC@-(B
($B9-Bg1!9)(B) ($B3X(B)$B!{C]Cf(B $BKcN$(B$B!&(B ($B@5(B)$B6b;X(B $B@58@(B$B!&(B ($B@5(B)$BD9_7(B $B425,(B$B!&(B ($B@5(B)$BETN1(B $BL-N;(B		Organosilica
Fluorine doping
Hydrocarbon separation
O
459Dual-Network$B9=B$$rM-$9$k%7%j%+7OKl$N:Y9&9=B$@)8f$H(BCO2$BF)2aFC@-(B
($B9-Bg1!9)(B) ($B3X(B)$B!{CfW"(B $B7CBg(B$B!&(B ($B@5(B)Liang Yu$B!&(B ($B@5(B)$B6b;X(B $B@58@(B$B!&(B ($B@5(B)$BD9_7(B $B425,(B$B!&(B ($B@5(B)$BETN1(B $BL-N;(B		Dual-network
Gas separation
Organic-inorganic hybrid membrane
O
462$B3&LL3h@-:^E:2C%"%k%+%j=hM}K!$,(BSilicalite-1$BKl$NF)2aJ,N%FC@-$K5Z$\$91F6A(B
($BAaBg@h?JM}9)(B) ($B3X(B)$B!{KY(B $BH;B@(B$B!&(B ($BAaBg%J%N%i%$%U(B) ($B@5(B)$B$B!&(B ($BAaBg@h?JM}9)(B/$BAaBgM}9)Am8&(B) ($B@5(B)$B>>J}(B $B@5I'(B		Zeolite
membrane separation
post treatment
O
498$B%+%k%\%-%7%Y%?%$%s%]%j%^!<$r%0%i%U%H$7$?Dc%U%!%&%j%s%0Kl$N3+H/(B
($B9)3X1!Bg@h?J9)(B) ($B3X(B)$B2C!98+(B $B`"(B$B!&(B ($B@5(B)$B!{@V>>(B $B7{$B!&(B Wang Xiao-Lin$B!&(B ($B@5(B)$BCfHx(B $B??0l(B		Membrane
Low-fouling
Carboxybetaine polymer
O
541$BAP@-%$%*%s%]%j%^!<$rMQ$$$?I=LL@:L)@)8fKl$N3+H/$H%"%s%A%U%!%&%j%s%0FC@-I>2A(B
($BEl9)Bg2=@88&(B) ($B@5(B)$B!{Bg$B!&(B $B86ED(B $BM*M$(B$B!&(B ($B3X(B)$B7*86(B $BM:Bg(B$B!&(B ($B@5(B)$B;38}(B $BLT1{(B		Membrane fouling
Surface modification
Zwitterionic polymer
O
564$B?e>x5$%9%$!<%W$rMQ$$$?(BCO2$BKlJ,N%%W%m%;%9$K$*$1$k?e>x5$=|5nK!$N1F6A(B
($BEl9)Bg1~2=(B) ($B@5(B)$B!{>.6L(B $BAo(B$B!&(B ($B6eBg9)(B) ($B@5(B)$B@1Ln(B $BM'(B$B!&(B ($B6eBg(BWPI-I2CNER) ($B@5(B)$BC+8}(B $B0iM:(B		CO2 capture
membrane
separation
O
601$BG;EY8{G[0lDj>r7o$GKlF)2a8=>]$KE,MQ$G$-$k?75,HsJ?9UJ,;RF0NO3XK!$N3+H/(B
($B9)3X1!Bg@h?J9)(B) ($B3X(B)$B!{Hu8}(B $BH;?M(B$B!&(B ($B@5(B)$B5\@n(B $B2mLp(B$B!&(B ($B@5(B)$B9b1)(B $BMN=<(B		reverse osmosis
mesoporous
diffusion
O
734$BBg7?%9%?%C%/$rMQ$$$?5UEE5$F)@O(B(RED)$B%7%9%F%`$N9b8zN(2=$N8!F$(B
($B;38}Bg1!AO(B/$B;38}Bg(BBEST) ($B@5(B)$B!{Hf2E(B $B=<(B$B!&(B ($B;38}Bg1!AO(B) $B@nH*(B $BNIBs(B$B!&(B $B;a2H(B $BNF(B$B!&(B ($B;38}Bg1!AO(B/$B;38}Bg(BBEST) ($B@5(B)$B3@2V(B $BI49g;R(B		reverse electrodialysis
salinity gradient energy
ion-exchange membrane
O
772$BG3Hq8~>e$r2DG=$H$9$kD69bF)2a@-%,%9J,N%Kl$rMQ$$$?(BN2$BIY2=%j!<%sG3>F%(%s%8%s%7%9%F%`$N8&5f(B
($BF|;:<+F0$B!&(B $B@n2<(B $B59O:(B$B!&(B ($BETN)Bg(B) ($B@5(B)$B@n>e(B $B9@NI(B$B!&(B ($BF|;:<+F0		polymer membrane
gas separation
Nitrogen enrichment
O
858$BI=LL$K3,AX9=B$$rM-$9$k%"%/%j%k7OHyB?9&Kl$rMQ$$$?(BCO2$BJ,N%Kl$N3+H/(B
($B6eBg1!9)(B) ($B@5(B)$B!{0Bi:(B $BfFGO(B$B!&(B ($B@5(B)$B@1Ln(B $BM'(B$B!&(B ($B@5(B)$B;01:(B $B2B;R(B		CO2 separation
Porous membrane
O
863$BDcJ,;R%"%_%s4^M-(BCO2$BJ,N%Kl$N4xH/FC@-I>2A$H4xH/M^@)2=(B
($B6eBg1!9)(B) ($B3X(B)$B!{KY0f(B $BNC2m(B$B!&(B ($B3X(B)$BK\ED(B $BN5B@O/(B$B!&(B ($B@5(B)$B0Bi:(B $BfFGO(B$B!&(B ($B6eBg(BI2CNER) ($B@5(B)$BC+8}(B $B0iM:(B$B!&(B ($B6eBg1!9)(B) ($B@5(B)$B;01:(B $B2B;R(B$B!&(B ($B@5(B)$B@1Ln(B $BM'(B		CO2 separation
nano gel particle
low-molecular amine
O
$B9V1i?=$79~$_0lMw(B($B%7%s%]%8%&%`HV9f!&9V1iJ,N`HV9fJL(B)
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$B2=3X9)3X2q(B $BBh(B51$B2s=)5(Bg2q(B (2020)
(C) 2021 $B8x1W
Most recent update: 2021-02-07 15:20:01
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