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
organosilica membrane3$B7o(B*
gas separation3$B7o(B*
forward osmosis3$B7o(B*
Zeolite2$B7o(B
membrane1$B7o(B

$B$BHV9f(B$B9V1iBjL\!?H/I=$B%-!<%o!<%I(B$BH/I=7A<0(B
44$B?75,%W%j%+!<%5!<$K$h$kN2;@5U?;F)%7%j%+Kl$N3+H/(B
($B$B!&(B $BKLHx(B $BM5$B!&(B ($B3X(B)$BC]Fb(B $B=_EP(B$B!&(B ($B3X(B)$B?yK\(B $B@i9I(B		silica reverse osmosis membrane
counter diffusion CVD
sulfuric acid separation
O
312$B?eAGA*BrF)2a%a%s%V%l%s%j%"%/%?!<$NBg7?2=(B
(RITE) ($B@5(B)$B!{@>Ln(B $B?N(B$B!&(B $B:4!9(B $BOBL@(B$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 $B??0l(B		hydrogen
membrane reactor
methylcyclohexane
O
328$B29EY(B/CO2$BFs=E1~Ez@-$r<($9%G%s%I%j%^!<7?@5?;F)6nF0MO
($B?@8MBg1!9)(B) ($B3X(B)$B!{@>?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@5(B)$B>>;3(B $B=(?M(B		forward osmosis
draw solute
stimuli-responsivity
O
330$B%"%_%N;@%$%*%s1UBN4^M-%2%kGvKl$N:n@=$H$=$N%,%9J,N%@-G=I>2A(B
($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 $B=(?M(B		Gas separation
Thin film
Ionic liquids
O
332$B;@AG5[<}@-6bB0:xBN7O%$%*%s1UBN$N%,%9F)2a@-$K$*$1$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 $B=(?M(B		Oxygen separation membrane
Ionic liquid
Metal complex
O
359A novel preparation and fundamental characterization of polyamide 6 self-supporting hollow fiber membranes for OSN (organic separation nanofiltration) via TIPS process
(Kobe U.) ($B@5(B)$B!{(BJeon S.$B!&(B Karkhanechi H.$B!&(B ($B3$(B)Fang L.-F.$B!&(B ($B@5(B)Cheng L.$B!&(B ($B@5(B)Matsuyama H.$B!&(B (Unitika) ($B@5(B)Ono T.$B!&(B ($B@5(B)Nakamura R.		polyamide 6
thermally induced phase separation
hollow fiber membrane
O
394AEI/AFI $B%O%$%V%j%C%IKl$N%,%9F)2aFC@-(B
($B;38}Bg1!(B) ($B3X(B)$B!{(B&#21556; &#23159;$B!&(B ($BCf9q9>@>;UHOBg(B) $BDD(B $B{D$B!&(B ($B;38}Bg1!(B) ($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 $B1QIR(B		AEI and AFI hybrid membranes
CO2/CH4 separation
N2/CH4 separation
O
404The study on co-extrusion to tailor pore structure of PVDF hollow fiber membranes via TIPS process: the effect of solvents
(Kobe U.) ($B3X(B)$B!{(BFang Chuanjie$B!&(B ($B@5(B)Jeon Sungil$B!&(B ($B@5(B)Fang Lifeng$B!&(B ($B@5(B)Cheng Liang$B!&(B ($B@5(B)Matsuyama Hideto		Co-extrusion
TIPS process
PVDF hollow fiber membrane
O
424$BM-5!2M664p$rM-$9$k%*%k%,%N%7%j%+Kl$N:Y9&7B@)8f$H5$BNFC@-I>2A(B
($B9-Bg1!9)(B) ($B3X(B)$B!{9>8}(B $B8y>-(B$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 $BL-N;(B		gas separation
pore size control
organosilica membrane
O
427F$B%I!<%W$K$h$k%*%k%,%N%7%j%+Kl$N:Y9&7B@)8f$HF)2aFC@-(B
($B9-Bg1!9)(B) ($B3X(B)$B!{B->O(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 $BL-N;(B		organosilica membrane
pore size control
fluorine
O
549$B%;%i%_%C%/B?9&Kl$K$h$k%*%$%k4^M-?e$N$m2aFC@-(B
($B9-Bg1!9)(B) ($B3X(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 ($B@5(B)$BETN1(B $BL-N;(B		oil water emulsion filtration
ceramic membrane
O
550$B:Y9&9=B$$N0[$J$kB?9&e$K@=Kl$7$?(BAlPO4-18$BKl$NF)2aFC@-(B
($BAaBg@h?JM}9)(B) ($B3X(B)$B!{5H86(B $B7D(B$B!&(B ($BAaBg%J%N%i%$%U(B) ($B@5(B)$B$B!&(B ($BAaBg@h?JM}9)(B/$BAaBgM}9)8&(B) ($B@5(B)$B>>J}(B $B@5I'(B		AlPO4-18
permeation properties
porous support
O
566$BM6EEBN%P%j%"J|EE$rMQ$$$?%7%j%+Kl$NBg5$05%W%i%:%^(BCVD$B@=Kl(B
($B9-Bg1!9)(B) ($B3X(B)$B!{9a@n(B $B5.I'(B$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 $BL-N;(B		atmospheric pressure plasma
silica membrane
chemical vapor deposition
O
570$BM-5!MOG^BQ@-$rM-$9$k9bJ,;R7OJ#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)$B:4Gl(B $BBgJe(B$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/$B@hC		Organic solvent filtration
Thin-film composite membrane
Polyamide active layer
O
633$BD62;GHJ.L8K!$K$h$k%A%?%K%"@=%,%9J,N%Kl$K$*$1$kF)2a@-G=$N%,%905NO0MB8@-(B
($B2#9qBg1!(B) ($B3X(B)$B!{<5AR(B $B;KLo(B$B!&(B ($B3X(B)$BOBED(B $B=_;V(B$B!&(B ($B2#9qBg(B) $BJ?Hx(B $BN$B!&(B ($B2#9qBg1!(B) ($B@5(B)$BAj86(B $B2mI'(B		Separation membrane
Ultrasonic spray method
Gas pressure dependence of permeability
O
653$B%<%*%i%$%HB?9&2A(B
($B4X@>Bg(B) ($B@5(B)$B!{9SLZ(B $BDgIW(B$B!&(B (ICL) Li Kang$B!&(B Li Tao$B!&(B ($B4X@>Bg(B) ($B@5(B)$B;3K\(B $B=(		Zeolite
Hollow fiber
Phase inversion
O
664STT$B7?%<%*%i%$%HKl$N9g@.$H%,%9F)2aFC@-(B
($B4X@>Bg(B) ($B@5(B)$B!{9SLZ(B $BDgIW(B$B!&(B $BCf0f(B $B6F;V(B$B!&(B $B:#:d(B $BNg;K(B$B!&(B ($B@5(B)$B;3K\(B $B=(		Zeolite
STT
Hydrothermal synthesis
O
674$BKl$r3V$F$?@5?;F)!&5U?;F)8=>]$NJ,;R%7%_%e%l!<%7%g%s(B
($B9)3X1!Bg9)(B) ($B3X(B)$B!{Hu8}(B $BH;?M(B$B!&(B ($B@5(B)$B9b1)(B $BMN=<(B		Water selective membrane
Non-equilibrium molecular dynamics
Osmotic pressure
O
730$B%W%i%:%^%0%i%U%H=E9gK!$rMQ$$$?Dc%U%!%&%j%s%08B30$m2aKl$N3+H/(B
($B9)3X1!Bg@h?J9)(B) ($B@5(B)$B!{@V>>(B $B7{$B!&(B $BG=EP(B $B>D(B$B!&(B $BJ!_7(B $BGnG7(B$B!&(B ($B@5(B)$BCfHx(B $B??0l(B		fouling
plasma graft polymerization
ultrafiltration
O
804$BBQ;@2=@-(BSiOC$B9=B$$rM-$9$k5$BNJ,N%Kl$N:n@=$HFC@-I>2A(B
($B9-Bg1!9)(B) ($B3X(B)$B!{0u=P(B $BMN$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 $BL-N;(B		organosilica membrane
gas separation
oxidation resistance
O
817$B@5?;F)KlK!$K$h$kE|1UG;=L$*$h$S%P%$%*%(%?%N!<%k@8;:$K5Z$\$9%]%j%"%_%IAX$NJ,N%@-G=$N1F6A(B
($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/$B%P%$%*%W%m%@%/%;(B) ($B@5(B)$B:4!9LZ(B $B7z8c!&(B ($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)$B?@Hx(B $B1Q<#(B$B!&(B($B?@8MBg1!2J5;%$%N%Y(B/$B%P%$%*%W%m%@%/%;(B) ($B@5(B)$B6aF#(B $B>($B?@8MBg1!9)(B/$B@hC>;3(B $B=(?M(B		bioethanol
forward osmosis
surface modification
O
849$B%J%$%m%s%J%N%U%!%$%P!
($BL>Bg9)(B) ($B3X(B)$B!{EDJU(B $BCRN<(B$B!&(B ($B@5(B)$B8~0f(B $B9/?M(B		nanofiber membrane
gold ion adsorption
recovery process
O
850$BEE3&KB;e;~$NEE2r
($BL>Bg9)(B) ($B3X(B)$B!{:d(B $BM&B@(B$B!&(B ($B@5(B)$B8~0f(B $B9/?M(B		electrospinning
fiber diameter
electrolyte
O
874$B?e>x5$$,(BNa-ZSM-5$BKl$N0BDj@-$K5Z$\$91F6A(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 ($BAaBg@h?JM}9)(B/$BAaBgM}9)Am8&(B) ($B@5(B)$B>>J}(B $B@5I'(B		Na-ZSM-5 membrane
steam stability
methanol synthesis
O
917Effect of the supporting layer structures on antifouling properties of forward osmosis membranes in AL-DS mode
(Kobe U.) ($B3$(B)$B!{(BFang Li-Feng$B!&(B Cheng Liang$B!&(B ($B3$(B)Jeon Sungil$B!&(B Wang Sheng-Yao$B!&(B ($B@5(B)Takahashi Tomoki$B!&(B ($B@5(B)Matsuyama Hideto		forward osmosis
antifouling properties
AL-DS mode
O
939Facile creation of dual super-lyophobic membranes in solid-oil-water triphase systems from aliphatic polyketone via phase inversion
(Kobe U./MaF Tech. C.) ($B@5(B)$B!{(BCheng Liang$B!&(B ($B@5(B)Shaikh Abdul Rajjak$B!&(B ($B3$(B)Fang Li Feng$B!&(B (Nat. Taiwan U.) Wang Da Ming$B!&(B (Kobe U./MaF Tech. C.) ($B@5(B)Matsuyama Hideto$B!&(B ($B@5(B)Jeon Sungil$B!&(B ($B@5(B)Saeki Daisuke		polyketone
superlyophobicity
membrane
O
$B9V1i?=$79~$_0lMw(B($B%7%s%]%8%&%`HV9f!&9V1iJ,N`HV9fJL(B)
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$B2=3X9)3X2q(B $BBh(B49$B2s=)5(Bg2q(B
(C) 2018 $B8x1W
Most recent update: 2018-02-12 17:39:01
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