SCEJ

$B2=3X9)3X2q(B $BBh(B82$BG/2q(B ($BEl5~(B 2017)

$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|;~!'(B2017-05-20 20:59:01

$B$3$NJ,N`$G$h$/;H$o$l(B
$B$F$$$k%-!<%o!<%I(B		$B%-!<%o!<%I(B$B
ionic liquid5$B7o(B*
Silica membrane4$B7o(B*
gas separation4$B7o(B*
zeolite membrane4$B7o(B*
forward osmosis4$B7o(B*
molecular dynamics4$B7o(B*
membrane3$B7o(B*
surface modification3$B7o(B*
hydrogen3$B7o(B*
membrane separation3$B7o(B*
CVD3$B7o(B*
Nonequilibrium Molecular Dynamics2$B7o(B

$B$BHV9f(B$B9V1iBjL\!?H/I=$B%-!<%o!<%I(B$BH/I=7A<0(B
76$BB?9&e$K@=Kl$7$?(BPd$BKl$N?eAGF)2a@-8~>e$r$a$6$7$?%7%j%+%i%$%HCf4VAX$N7A@.>r7o$N8!F$(B
($BFAEgBg1!@hC<650iIt(B) ($B3X(B)$B!{|bC+(B $B??90(B$B!&(B ($BFAEgBg1!M}9)(B) ($B@5(B)$B2CF#(B $B2mM5(B$B!&(B ($B@5(B)$BGO>l(B $BM:;0(B$B!&(B ($B@5(B)$B?y;3(B $BLP(B		Hydrogen permeation enhancement
Palladium membrane
Silicalite intermediate layer
P
83$B%<%*%i%$%HJ,N%Kl$N2A
(SEPINO) ($BK!(B)$B!{4];3(B $B7D;R(B$B!&(B ($BK!(B)$BOB@t(B $B9R(B$B!&(B ($B@5(B)$B8^%N0f(B $B9@Fs(B$B!&(B ($B@5(B)$B0f>e(B $B=!;N(B		zeolite membrane
Life evaluation
O
87$BN3;R$N%/%m%9%U%m!<@:L)$m2a$K$*$1$k8B3&N.B+$K4X$9$k8&5f(B
($B9)3X1!Bg9)(B) ($B3X(B)$B!{bCJI(B $BNI(B$B!&(B ($B9)3X1!Bg@h?J9)(B) ($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@h?J9)(B) ($B@5(B)$BCfHx(B $B??0l(B		microfiltration
limiting flux
simulation
O
122$BBQ;@@-?eAGF)2a%7%j%+Kl$N3+H/(B
($B$B!&(B ($B@5(B)$BLnB<(B $B4490(B		hydrogen
CVD
silica membrane
P
125$B<+N)7?%<%*%i%$%H@:L)$m2aKlMQ%<%*%i%$%H$N5[CeFC@-(B
($BH5W(B$B!&(B ($B@5(B)$BLnB<(B $B4490(B$B!&(B ($B%?%+%.(B) $BEDCf(B $B>OB@O:(B$B!&(B $B>>Hx(B $BM[(B$B!&(B $BHD0f(B $BK-=<(B$B!&(B $B3^(B $B?8Je(B		MORzeolite
Self Standing Membrane
Drygel Conversion
P
131$B%$%*%s8r49(BMOR$B%<%*%i%$%HKl$NF)2aFC@-(B
($B$B!&(B $BD9ED(B $BCN;N(B$B!&(B $B5HED(B $BM-4u(B$B!&(B ($B@5(B)$BLnB<(B $B4490(B		MORzeolite
membrane
ion exchange
P
132$B%7%j%+J#9gKl$NC:2=?eAGJ,N%(B
($B$B!&(B $B5HED(B $B??F`H~(B$B!&(B ($B@5(B)$BLnB<(B $B4490(B		hydrocarbon
CVD
silica membrane
P
150In-situ$B>.3Q(BX$B@~;6MpB,Dj$rMQ$$$?HsMOG^M65/AjJ,N%$N8&5f(B
($BEl%l(B) ($BK!(B)$B!{;VB<(B $B=S(B$B!&(B ($BK!(B)$B2V@n(B $B@59T(B$B!&(B ($BK!(B)$B0BED(B $B5.N<(B$B!&(B ($BEl%l%j%5!<%A%;%s%?!<(B) $BCfED(B $B9n(B$B!&(B $B2,ED(B $B0l9,(B$B!&(B ($BEl%l(B) ($BK!(B)$BLZB<(B $B>-90(B		phase separation
NIPS
SAXS
P
155$B?eAG@=B$(BIS$B%W%m%;%9Cf;@2=4T85H?1~MQ%$%*%s8r49Kl$N3+H/(B
($B$B!&(B ($B@5(B)$BLnB<(B $B4490(B$B!&(B $B@>Eh(B $BM[G7(B$B!&(B $B:#NS(B $B?50lO:(B$B!&(B ($BNL;R8&5f5!9=(B) $B_7ED(B $B??0l(B$B!&(B $BH,4,(B $BE0Li(B$B!&(B ($B86;RNO5!9=(B) $BEDCf(B $B?-9,(B$B!&(B $B5WJ](B $B??<#(B		Hydrogen production
Bunsen reaction
Ion exchange membrane
P
177$BL55!5U?;F)MQ%7%j%+B?9&
($B$B!&(B $BKLHx(B $BM5$B!&(B $B?yK\(B $B@i9I(B$B!&(B ($B@5(B)$BLnB<(B $B4490(B		reverse osmosis
inorganic membrane
acid separation
P
183$BL}(B/$B?eJ,N%MQ%J%N%;%k%m!<%9Kl$N:n@=(B
($B90A0BgM}9)(B) ($B3X(B)$B!{(BPhanthong Patchiya$B!&(B ($B@5(B)$B0$I[(B $BN$Ds(B$B!&(B ($B90A0Bg?7%(%M!<8&(B) ($B@5(B)$B41(B $B9q@6(B		Nanocellulose membrane
Oil separation
surface modification
P
185$B%<%*%i%$%HKlF)2a$K$*$1$k3F
($B$B!&(B $B5HB<(B $B=SMN(B$B!&(B ($B@5(B)$BLnB<(B $B4490(B		MFI zeolite membrane
Organic acid
Japanese SAKE
P
189$B?eAG(B/$B%H%k%(%s:.9g%,%9J,N%$KM?$($kCf6u;eC:AGKl$NF)2aFC@-$N1F6A(B
($B;:Am8&(B) ($B@5(B)$B!{5H=!(B $BH~5*(B$B!&(B ($B@5(B)$B86(B $B?-@8(B$B!&(B ($B@5(B)$B86C+(B $B8-<#(B		carbon membrane
hydrogen
gas separation
O
192AlPO-18 $BKl$N@=Kl$HF)2aJ*@-(B
($B;38}Bg1!M}(B) ($B3X(B)$B!{8b(B &#23159;$B!&(B ($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 $B1QIR(B		AlPO-18 membrane
Gas permeation
Pervaporation
O
208$B%P%$%*%(%?%N!<%k@8;:%W%m%;%9$K$*$1$kE|1UG;=L$r;X8~$7$?(BNF-FO$B%O%$%V%j%C%H%7%9%F%`$N9=C[(B
($B?@8MBg1!9)(B/$B@hC$B!&(B ($B?@8MBg1!2J5;%$%N%Y(B) ($B@5(B)$B:4!9LZ(B $B7z8c(B$B!&(B ($B;38}Bg1!(B) ($B@5(B)$B0B@n(B $B@/9((B$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) ($B@5(B)$B6aF#(B $B>$B!&(B ($B?@8MBg1!9)(B/$B@hC>;3(B $B=(?M(B		up-concentration
Forward osmosis
Nanofiltration
O
228$BC:2=?eAGJ,N%$rL\E*$H$7$?%<%*%i%$%H5U?;F)KlJ,N%$NJ,;R%7%_%e%l!<%7%g%s(B
($B9)3X1!Bg9)(B) ($B3X(B)$B!{@P86(B $B9-;L(B$B!&(B ($B@5(B)$B9b1)(B $BMN=<(B		Nonequilibrium molecular dynamics
Zeolite membranes
Hydrocarbons
P
229$BC:2=?eAGJ,N%MQ9bJ,;RKl$N%,%9MO2rFC@-$K4X$9$kJ,;RO@E*8&5f(B
($B9)3X1!Bg9)(B) ($B3X(B)$B!{2#20(B $BNC(B$B!&(B ($B@5(B)$B9b1)(B $BMN=<(B		Solvation free energy
Molecular dynamics
Polyimide film
P
238$B%7%i%s7O%$%*%s1UBN$+$i$N%*%k%,%N%7%j%+Kl$N:n@=$H$=$N>x5$F)2aFC@-(B
($B:eBg1!4p9)(B) ($B@5(B)$B!{W"ED(B $BM:0lO/(B$B!&(B ($B3X(B)$BA0ED(B $BMNJ?(B$B!&(B ($B3X(B)$B;3K\(B $BM42p(B$B!&(B ($B@5(B)$B@>;3(B $B7{OB(B		organosilica membrane
ionic liquid
vapor permeation
O
285RHO$B%<%*%i%$%HKl$N@=Kl$HF)2aJ*@-(B($B-6(B)
($B;38}Bg1!AO(B) ($B@5(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 $B1QIR(B		RHO zeolite membrane
Pervaporation
Gas permeation
O
291$BHsJ?9UJ,;RF0NO3XK!$K$h$k?75,D6J,;RKl$NF)?e@-$NM=B,(B
($B9)3X1!Bg9)(B) ($B3X(B)$B!{Hu8}(B $BH;?M(B$B!&(B ($B@5(B)$B9b1)(B $BMN=<(B		Water Selective Membrane
Nonequilibrium Molecular Dynamics
Supermolecule
P
361$B%$%*%s1UBN$N1UBNKl$K$h$kC:2=?eAG$N>x5$F)2aJ,N%(B
($BEl9)BgJ*$B!&(B ($B3X(B)$B?@C+(B $BCR5,(B$B!&(B ($B3X(B)$B@P@n(B $BBg5.(B$B!&(B ($B@5(B)$B0KEl(B $B>O(B		liquid membrane
hydrocarbon vapor permeation
ionic liquids
P
372$BJ,;RF0NO3XK!$rMQ$$$?(BTiO2$B%J%N:Y9&Fb?eF)2a5!9=$N8!F$(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 ($B2,;3Bg1!<+(B) ($B@5(B)$B;0Ln(B $BBY;V(B$B!&(B ($B?@8MBg1!9)(B/$B@hC$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B		Molecular dynamics
water permeation
nanoporous membrane
P
400CHA$B7?%T%e%"%7%j%+%<%*%i%$%HKl$N(BCO2$BJ,N%FC@-(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 separation
O
407$B%@%$%l%/%H%*%9%b%F%#%C%/%R!<%H%(%s%8%s$NH/EE@-G=$KM?$($k1?E>>r7o$N1F6A(B
($B?@8MBg1!9)(B/$B@hC$B!&(B ($B@5(B)$B9b66(B $BCR51(B$B!&(B ($B3X(B)$BEDCf(B $BM5Bg(B$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B		osmotic heat engine
pressure retarded osmosis
draw solute
P
409$B29EY(B/CO2$BFs=E1~Ez@-$r<($9%G%s%I%j%^!<7?(BDS$B$NF)?e@-G=(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
draw solute
stimuli-responsivity
P
414$B@5?;F)Kl%W%m%;%96nF0MO1U$X$N(BLCST$B7?AjE>0\%$%*%s1UBN(B/$B?e:.9g7O$NE,MQ$K4X$9$k4pACE*8!F$(B
($B?@8MBg1!9)(B/$B@hC$B!&(B ($B@5(B)$B?@Hx(B $B1Q<#(B$B!&(B ($B@5(B)$B9b66(B $BCR51(B$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B		Ionic liquid
Forward osmosis membrane process
Draw solution
P
419Thermal stability of Bis(triethoxysilyl)ethane-derived membranes and their gas permeation properties.
($B9-Bg(B) ($B3X(B)$B!{(BYu Xin$B!&(B ($B@5(B)Nagasawa Hiroki$B!&(B ($B@5(B)Kanezashi Masakoto$B!&(B ($B@5(B)Tsuru Toshinori		Membrane preparation
thermal stability
heat treatment
O
433TiO2-ZrO2-$BM-5!%-%l!<%HJ#9g:`NA$NFC@-I>2A$H(BCO2$BJ,N%Kl$X$N1~MQ(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
organic chelate
CO2 adsorption
P
439pH$B1~Ez@-%^%F%j%"%k$NAjJ,N%5sF0$K4X$9$k7W;;2=3XE*2r@O(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=(		LCST
molecular dynamics
pH-responsive
P
441$B5U?;F)KlI=LL$K%0%i%U%H$5$l$?5!G=@-%]%j%^!<$N9=B$$,%P%$%*%U%!%&%j%s%05sF0$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 $B=(?M(B		Reverse osmosis membrane
Biofouling
Surface modification
P
449CO2$BJ*M}5[<}1U$N%^%/%m$J3H;678?t$H%_%/%m$JBZN1;~4V$N4X78(B: $B7W;;2=3XE*2r@O(B
($BL>9)Bg(B) ($B@5(B)$B!{Fn1@(B $BN<(B$B!&(B ($B3X(B)$BB$B!&(B (RITE) ($B@5(B)$B;3ED(B $B=(>0(B$B!&(B ($BL>9)Bg(B) ($B@5(B)$B4dED(B $B=$0l(B$B!&(B ($B@5(B)$B?9(B $B=(		CO2 diffusivity
molecular dynamics
residence time
O
454$B?eAGA*BrF)2a%a%s%V%l%s%j%"%/%?!<$N%9%1!<%k%"%C%W(B
(RITE) ($B@5(B)$B!{@>Ln(B $B?N(B$B!&(B ($B@5(B)$B1:0f(B $B9(H~(B$B!&(B $B:4!9(B $BOBL@(B$B!&(B ($B@5(B)$B@>ED(B $BN<0l(B$B!&(B ($B@5(B)$BCfHx(B $B??0l(B		hydrogen
membrane reactor
methylcyclohexane
O
489$BFs2A(B
($B?@8MBg1!2J5;%$%N%Y(B/$B@hC$B!&(B ($BFAEgBg1!@hC<(B/$B?@8MBg1!9)(B) ($B3X(B)$B;32<(B $BMNNa(B$B!&(B ($B?@8MBg1!9)(B/$B@hC$B!&(B ($B?@8MBg1!2J5;%$%N%Y(B/$B@hC$B!&(B ($B@5(B)$B?7C+(B $BBn;J(B$B!&(B ($BFAEgBg1!M}9)(B) ($B@5(B)$B2CF#(B $B2mM5(B$B!&(B ($B@5(B)$B?y;3(B $BLP(B$B!&(B ($B?@8MBg1!9)(B/$B@hC$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B		layered nanosheet membrane
metal oxide
water treatment
O
512$B%U%C2=J*%U%j!<>r7o2<$K$*$1$k(BCHA$B7?%"%k%_%N%U%)%9%U%'!<%H$N9g@.$HKl2=(B
($BAaBg@h?JM}9)(B) ($B@5(B)$B!{@%2<(B $B2mGn(B$B!&(B ($B3X(B)$BJ!ED(B $B9IKo(B$B!&(B ($BAaBg@h?JM}9)(B/$BAaBgM}9)8&(B) ($B@5(B)$B>>J}(B $B@5I'(B		CHA-type aluminophosphate
Synthesis
Fluoride
O
520Influence of aging period for mother gel on permselectivities of SAPO-34 membrane for water/acetic acid mixture
($BAaBg@h?JM}9)(B) ($B3X(B)$B!{(BAtaher Ahmed$B!&(B ($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 $B@5I'(B		SAPO-34 membrane
acid
aging
P
521$BMM!9$JC:2=?eAG$+$i@8@.$9$kG.J,2rC:AG$,(Bsilicalite-1$BKl$NF)2aJ,N%@-G=$KM?$($k1F6A(B
($BAaBg@h?JM}9)(B) ($B@5(B)$B$B!&(B ($B3X(B)$B!{8M4,(B $B7=M4(B$B!&(B ($BAaBg@h?JM}9)(B/$BAaBgM}9)8&(B) ($B@5(B)$B>>J}(B $B@5I'(B		silicalite-1 membrane
control pore size
carbon-deposition
P
525Ag-*BEA$B7?%<%*%i%$%HKl$N%(%A%l%s!?%(%?%sF)2aJ,N%FC@-(B
($BAaBg@h?JM}9)(B) ($B@5(B)$B$B!&(B ($B3X(B)$B!{0BED(B $B71G7(B$B!&(B ($BAaBg@h?JM}9)(B/$BAaBgM}9)Am8&(B) ($B@5(B)$B>>J}(B $B@5I'(B		membrane separation
*BEA-type zeolite
ethylene separation
P
528ZSM-5$BKl$NKl9=B$$,F)2aJ,N%FC@-$K5Z$\$91F6A(B
($BAaBg@h?JM}9)(B/$BAaBgM}9)Am8&(B) ($B@5(B)$B>>J}(B $B@5I'(B$B!&(B ($BAaBg@h?JM}9)(B) ($B3X(B)$B!{>>K\(B $BOKJ?(B$B!&(B ($B@5(B)$B@%2<(B $B2mGn(B		zeolite membrane
permselectivity
membrane structure
P
539$BCf6u;eKl%b%8%e!<%k$N%b%8%e!<%k7A>u$,?;F)05H/EE%W%m%;%9$KM?$($k1F6A(B
($B?@8MBg1!9)(B/$B@hC$B!&(B ($B;38}Bg1!AO@.2J(B) ($B@5(B)$B0B@n(B $B@/9((B$B!&(B ($BElMNKB(B) ($BK!(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 ($B@5(B)$B4_K\(B $BDL2m(B$B!&(B ($B?@8MBg1!2J5;%$%N%Y(B/$B@hC$B!&(B ($B@5(B)$B?7C+(B $BBn;J(B$B!&(B ($B;38}Bg1!AO@.2J(B) ($B@5(B)$BHf2E(B $B=<(B$B!&(B ($B?@8MBg1!9)(B/$B@hC>;3(B $B=(?M(B		Pressure-retarded osmosis
Hollow fiber module
Operating condition
P
541$B3$?eC8?e2=MQ@5?;F)Kl%b%8%e!<%k$*$h$S1?E>>r7o$N@_7W;X?K(B
($BEl9)Bg2=@88&(B) ($B3X(B)$B!{E75\(B $B@60l(B$B!&(B ($B@5(B)$B;38}(B $BLT1{(B		Forward osmosis
Desalination
Membrane module
O
558$B?eG.K!$K$h$k%+!<%\%sKl$N:n@=$H%,%9J,N%$X$N1~MQ(B
($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 $B>O(B		Activated carbon
Gas separation
Glucose
P
567$B5[0z$m2aK!$K$h$j:n@=$5$l$?%K%*%V;@%J%N%7!<%H@QAXKl$NKl@-G=$K5Z(B $B$\$9:n@=>r7o$N1F6A(B
($BFAEgBg1!@hC<(B/$B?@8MBg1!9)(B) ($B3X(B)$B!{;32<(B $BMNNa(B$B!&(B ($B?@8MBg1!2J5;%$%N%Y(B/$B@hC$B!&(B ($B?@8MBg1!9)(B/$B@hC$B!&(B ($B?@8MBg1!2J5;%$%N%Y(B/$B@hC$B!&(B ($B@5(B)$B?7C+(B $BBn;J(B$B!&(B ($BFAEgBg1!M}9)(B) ($B@5(B)$B2CF#(B $B2mM5(B$B!&(B ($B@5(B)$B?y;3(B $BLP(B$B!&(B ($B?@8MBg1!9)(B/$B@hC$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B		layered nanosheet membrane
metal oxide
vacuum filtration
P
574$B1vAG2=%]%j1v2=%S%K%kJ?Kl$NKlFC@-$K5Z$\$9%W%m%k%K%C%/7O3&LL3h@-:^E:2C$N8z2L(B
($B%f%"%5%a%s%V%l%s%7%9%F%`(B) ($B@5(B)$B!{;3K\(B $B=SJe(B$B!&(B $Bc7F#(B $B7{0l(B$B!&(B ($B@5(B)$B:4Ln(B $BMxIW(B		Chlorinated Poly(Vinyl Chloride)
Pluronic Surfactant
Membrane Bioreactor
P
590$B@8J*3XE*A0=hM}$K$h$kKl%U%!%&%j%s%0860xJ*
($B?@8MBg1!9)(B/$B@hC$B!&(B ($B@5(B)$BD9C+@n(B $B?J(B$B!&(B ($B?@9]4D6-%=%j%e!<%7%g%s(B) $B>.LnED(B $BAp2p(B$B!&(B ($B?@8M;T?eF;6I(B) $B?9ED(B $B0l;J(B$B!&(B ($B?@8MBg1!9)(B/$B@hC>;3(B $B=(?M(B		membrane fouling
biological pretreatment
statistical analysis
P
599$BMO@\?tCM%7%_%e%l!<%7%g%s(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 ($BElBg4D0B%;(B) ($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 $B=E=S(B		crossflow
solute adsorption
simulation
P
615CVD$B%7%j%+Kl$N
(RITE) ($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@>ED(B $BN<0l(B$B!&(B ($B@5(B)$BCfHx(B $B??0l(B		silica membrane
CVD
gas separation
P
633$BJ?HD;Y;}BN>e$K9g@.$7$?(BZSM-5$BKl$N@=Kl>uBV(B
($BAaBg@h?JM}9)(B) ($B@5(B)$B$B!&(B ($B3X(B)$B!{Gk86(B $B?p4p(B$B!&(B ($BAaBg@h?JM}9)(B/$BAaBgM}9)Am8&(B) ($B@5(B)$B>>J}(B $B@5I'(B		ZSM-5
Membrane
Plate support
P
636$B?e>x5$J70O5$2<$K$*$1$k(BZSM-5$BKl$N0BDj@-(B
($BAaBg@h?JM}9)(B/$BAaBgM}9)Am8&(B) ($B@5(B)$B>>J}(B $B@5I'(B$B!&(B ($BAaBg@h?JM}9)(B) ($B3X(B)$B!{66D^(B $BM:M$(B$B!&(B ($B@5(B)$B@%2<(B $B2mGn(B		Na-ZSM-5
steam stability
methanol synthesis
P
676AlPO4-18$BKl$K$h$k?eAG(B/$B7Z
($BAaBg@h?JM}9)(B) ($B@5(B)$B$B!&(B ($B3X(B)$B!{5H86(B $B7D(B$B!&(B ($BAaBg@h?JM}9)(B/$BAaBgM}9)Am8&(B) ($B@5(B)$B>>J}(B $B@5I'(B		membrane separation
AEI-type zeolite
AlPO4-18
P
686$B?tCM%7%_%e%l!<%7%g%s$rMQ$$$?%3%"%l%C%5!<7?L}?eJ,N%Kl$N@_7W(B
($B?@8MBg1!9)(B/$B@hC$B!&(B ($B2,;3Bg1!<+(B) ($B@5(B)$B;0Ln(B $BBY;V(B$B!&(B ($B?@8MBg1!2J5;%$%N%Y(B) ($B@5(B)$B5H2,(B $BJ~5W(B$B!&(B ($B?@8MBg1!9)(B/$B@hC>;3(B $B=(?M(B		Lattice Boltzmann method
two-phase flow
coalescing
P
697$BJ#?t$N%2%kN3;RAX$+$i$J$k(BCO2/N2$BJ,N%Kl$ND4@=$HI>2A(B
($B6eBg9)(B) ($B3X(B)$B!{K\ED(B $BN5B@O/(B$B!&(B ($B6eBg1!9)(B) $B9TIt(B $BCRMN(B$B!&(B $B:#B<(B $BOB;K(B$B!&(B $B;32<(B $BCN7C(B$B!&(B ($B6eBg(BI2CNER) $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 $B2B;R(B		carbon dioxide
membrane separation
gel particles
P
709$B%$%*%s1UBN$N1UBNKl$K$h$k6u5$=|<>(B
($BEl9)BgJ*$B!&(B Kudasheva Alina$B!&(B ($B@5(B)$B0KEl(B $B>O(B		liquid membrane
dehumidification
ionic liquid
P
720$BJ,;R%7%_%e%l!<%7%g%s$K$h$k29EY1~Ez@-%$%*%s1UBN?eMO1U$NAjE>0\5sF02r@O(B
($B?@8MBg1!2J5;%$%N%Y(B/$B@hC($B@5(B)$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@hC$B!&(B ($B@5(B)$B?@Hx(B $B1Q<#(B$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B		ionic liquid
molecular simulation
draw solution
P
733$B%+%k%\%-%7%k4p$rIUM?$7$?(BUiO-66$BKl$N9g@.(B
($B4tIlBg1!9)(B) ($B3X(B)$B!{8^Eg(B $BN68-(B$B!&(B ($B4tIlBg(B) ($B@5(B)$B5\K\(B $B3X(B$B!&(B ($B4tIlBg@8L?%;(B) ($B@5(B)$B6a9>(B $BLwB'(B$B!&(B ($B4tIlBg(B) ($B@5(B)$B>e5\(B $B@.G7(B		UiO-66-(COOH)2
membrane
metal organic frameworks
P
737$BHsBP>N9=B$%7%j%+Kl$N?e>x5$GxO*$K$h$kNt2=5sF0(B
($B9)3X1!Bg(B) ($B3X(B)$B!{:4F#(B $B8-B@(B$B!&(B ($B@5(B)$B@V>>(B $B7{$B!&(B ($B@5(B)$BCfHx(B $B??0l(B		Silica membrane
Hydrothermal stability
Densification
O
748$B%]%j%"%_%I3h@-AX$NI=LL2~
($B?@8MBg1!2J5;%$%N%Y(B/$B@hC(B$B!&(B ($B@5(B)$BCf@n(B $B7I;0(B$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)$B?@Hx(B $B1Q<#(B$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B		bioethanol
forward osmosis
surface modification
P
757$B%7%i%s7O%$%*%s1UBN$+$i9g@.$7$?%*%k%,%N%7%j%+Kl$K$h$kA*BrE*%a%?%N!<%k2s<}(B
($B:eBg1!4p9)(B) ($B3X(B)$B!{;3K\(B $BM42p(B$B!&(B ($B3X(B)$BA0ED(B $BMNJ?(B$B!&(B ($B@5(B)$BW"ED(B $BM:0lO/(B$B!&(B ($B@5(B)$B@>;3(B $B7{OB(B		organosilica membrane
ionic liquid
methanol permeation
P
780$B>x5$E>49K!$rMQ$$$?Fsr7o2<$G$N(BSilicalite-1$BKl$N9g@.(B
($B4tIlBg1!9)(B) ($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) $B1|Ln(B $BBsLi(B$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 $BLwB'(B		zeolite membrane
MFI
steam assisted conversion
P
798$BCf6u;e7??M9)?UB!$rMQ$$$?8B30_I2a$KN.NL>r7o$,M?$($k1F6A(B
($BK!@/Bg1!M}9)(B) ($B3X(B)$B!{:#0f(B $B=f(B$B!&(B ($BK!@/Bg@8L?(B) ($B@5(B)$B;32<(B $BL@BY(B		Ultrafiltration
Hollow fiber filter
P
827$BG;=L3$?e$H2
($B;38}Bg1!AO@.2J3X(B) ($B@5(B)$B!{Hf2E(B $B=<(B$B!&(B ($B;38}Bg1!M}9)(B) ($B3X(B)$B]/ED(B $BJ~G7(B$B!&(B ($B;38}Bg1!AO@.2J3X(B) ($B3X(B)$B5WLn(B $B2mLo(B$B!&(B ($B@5(B)$B0B@n(B $B@/9((B		Reverse electrodialysis
Ion exchange membrane
Salinity gradient power
O
828$B?eF,:9$rMxMQ$7$??;DR7?Kl%7%9%F%`$K$h$kHy:YAtN`G;=L$N4pACI>2A(B
($BC^GHBg@84D(B) ($B3X(B)$B0B1J(B $B$"$+$M(B$B!&(B ($B3$(B)$B!{(BDjali Nurul Ainina$B!&(B ($B@5(B)$B;T@n(B $BAO:n(B$B!&(B ($B@5(B)$BCfEh(B $B8wIR(B		Microalgae concentration
Siphon-driven membrane system
Primary concentration
P
833$B?;F)05H/EE$r;V8~$7$?3F
($B;38}Bg1!AO@.2J3X(B) ($B@5(B)$B!{0B@n(B $B@/9((B$B!&(B ($B;38}Bg1!M}9)(B) ($B3X(B)$BKY9>(B $BN5fF(B$B!&(B ($B;38}Bg1!AO@.2J3X(B) ($B@5(B)$BHf2E(B $B=<(B		Pressure-retarded osmosis
Membrane module
Salinity gradient power
O
865$BG.M65/AjJ,N%K!$K$h$k9bJ,;RKlI=LL9=B$7A@.2aDx$N8!F$(B
($B2,;3Bg1!<+(B) ($B@5(B)$B!{;0Ln(B $BBY;V(B$B!&(B ($B?@8MBg9)(B) ($B3X(B)$BJ!@n(B $B@.51(B$B!&(B ($B?@8MBg1!9)(B) ($B@5(B)$B>>;3(B $B=(?M(B		thermally induced phase separation
polymer membrane
phase field method
O
876Molecular Design and Technology Development of Bio-inspired Membranes for Separation Engineering
(Chung Yuan U.) Chang Yung
O
877Roles of Mass Transport and Polymer Solution Rheology in Preparation of Polymeric Membranes
(Nat. Taiwan U.) Wang Da-Ming
O
$B9V1i?=$79~$_0lMw(B($B%7%s%]%8%&%`HV9f!&9V1iJ,N`HV9fJL(B)
$B
$B2=3X9)3X2q(B $BBh(B82$BG/2q(B ($BEl5~(B 2017)
(C) 2017 $B8x1W
Most recent update: 2017-05-20 20:59:01
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