SCEJ

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

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

SY) $BIt2q%7%s%]%8%&%`(B

SY-57. [$BJ,N%%W%m%;%9It2q%7%s%]%8%&%`(B] (1) $B%]%9%?!<%;%C%7%g%s(B

$B%*!<%,%J%$%6!<(B: $BEDCf(B $B9'FA!JBg:eEE5$DL?.Bg3X!K(B

$BJ,N%%W%m%;%9It2ql9g$K$O!$?3::$K$h$j?tL>$NM%=(^$r

$B:G=*99?7F|;~!'(B2021-02-07 15:20:01

$B$3$NJ,N`$G$h$/;H$o$l(B
$B$F$$$k%-!<%o!<%I(B		$B%-!<%o!<%I(B$B
Gas separation5$B7o(B*
membrane4$B7o(B*
filtration3$B7o(B*
fouling2$B7o(B
Surface modification2$B7o(B
organic solvent2$B7o(B
reverse osmosis2$B7o(B
Glass fiber filter type gas absorber2$B7o(B
Nitrogen monoxide2$B7o(B
NF membrane2$B7o(B
Adsorption2$B7o(B
microorganism1$B7o(B

$B$BHV9f(B$B9V1iBjL\!?H/I=$B%-!<%o!<%I(B$BH/I=7A<0(B
36CO2$B5[<}EcC&C:;@%,%9$NHyNL%"%_%s>x5$2s<}$K8~$1$?4pAC%G!<%?$N
($BAaBg1!AOB$M}9)(B) ($B3X(B)$B!{M-@n(B $BBg8g(B$B!&(B $BCfB<(B $B9@B@O:(B$B!&(B ($B85AaBg1!AOB$M}9)(B) $BD9C+@n(B $BBg2p(B$B!&(B ($BAaBg1!AOB$M}9)(B) ($B3X(B)$B0kC+(B $B9@9'(B$B!&(B ($B@5(B)$BCf3@(B $BN4M:(B$B!&(B ($BEl$B!&(B ($BK!(B)$BF#ED(B $B8J;W?M(B$B!&(B ($B@5(B)$BKLB<(B $B1QIW(B		amine emissions
mass transfer coefficient
packed column
P
53$B@:L)$m2aKl$NN3;RAK;_@-G=I>2A$K$*$1$k2r@O
($BEl%l(B) ($BK!(B)$B!{>.:j(B $BM[0lO:(B$B!&(B ($BK!(B)$BH+J?(B $BCR;R(B$B!&(B ($BK!(B)$BLZB<(B $B>-90(B		membrane
microfiltration
P
91$BM-5!1UBNJ,N%MQ%7%j%+Kl$N3+H/(B
($B$B!&(B ($B3X(B)$B5H1:(B $BkN;R(B$B!&(B ($B$B!&(B ($B$B!&(B ($B		Counter diffusion CVD
Inorganic membrane
Organic solvent
P
94$BB?9&
($BFAEgBg1!@hC<650iIt(B) ($B3X(B)$B!{0pDE(B $B2B4u(B$B!&(B ($B3X(B)$BBgFn(B $B9IB@(B$B!&(B ($BFAEgBg1!$B!&(B ($B@5(B)$BAzED(B $BD>9((B$B!&(B ($B@5(B)$B?y;3(B $BLP(B		Dense Pd membrane on porous SUS tube
Titania powder
Vacuum-assisted electroless plating
P
95$B6E=8$7$?(BNaA$B%<%*%i%$%HJ4Kv$NF3F~$K$h$kB?9&
($BFAEgBg1!@hC<650iIt(B) ($B3X(B)$B!{;{yu(B $B>!70(B$B!&(B ($B3X(B)$B0pDE(B $B2B4u(B$B!&(B ($BFAEgBg1!$B!&(B ($B@5(B)$BAzED(B $BD>9((B$B!&(B ($B@5(B)$B?y;3(B $BLP(B		Pd thin membrane
Porous SUS tube
Aggregated NaA zeolite powder
P
117$B9b@-G=5U?;F)Kl%(%l%a%s%H(B
($BEl%l(B) ($BK!(B)$B!{C+8}(B $B=((B$B!&(B ($BK!(B)$B2VED(B $BLP5W(B$B!&(B ($BK!(B)$B;3ED(B $BGnG7(B$B!&(B ($BK!(B)$BLZB<(B $B>-90(B		Reverse osmosis
concentration polarization
Scaling
P
129$B<'@-N3;RF3F~%2%k=
($B:42lBg1!9)(B) ($B3X(B)$B!{OILn(B $B3YBg(B$B!&(B ($B:42lBg(B) ($B@5(B)$B?9Dg(B $B??B@O:(B$B!&(B ($B@5(B)$BBgEO(B $B7<2p(B$B!&(B ($B@5(B)$B@n4nED(B $B1Q9'(B		magnetite-containing gel
microorganism
filtration
P
177$B%]%j%"%/%j%k;@I=LL2~
($B1'ET5\Bg1!CO(B) ($B3X(B)$B!{KRLn(B $B6WH~(B$B!&(B $B2.Ln(B $BN6:H(B$B!&(B ($B1'ET5\Bg9)(B) ($B@5(B)$B:4F#(B $B9d;K(B$B!&(B ($B@5(B)$B0KF#(B $BD>		Dolomite
Polyacrylic Acid
Filtration
P
200$BI=LL3+;O(BATRP$BK!$K$h$kB?9&BNI=LL$X$N9bJ,;RGvAX$N7A@.$K$*$1$k3+;O:^8GDj2=>r7o$N8!F$(B
($B?.=#Bg1!AmM}9)(B) ($B3X(B)$B!{Jw(B $B?FNI(B$B!&(B ($B?.=#Bg(BRISM/$B?.=#Bg1!AmM}9)(B) ($B@5(B)$B:4Gl(B $BBgJe(B$B!&(B ($B?.=#Bg1!AmM}9)(B) $B1|B<(B $B9,5W(B		Water purification
surface-initiated atom transfer radical polymerization
polymeric thin layer
P
202$BN3;R4^M-5$BNJ,N%HsBP>NKl$N:n@=(B:$B4%<><0AjE>49K!$K$*$1$k%9%-%sAX$G$NN3;R6E=8M^@)(B
($BETN)Bg1!ET;T4D6-(B) ($B3X(B)$B!{El(B $B$7$*$j(B$B!&(B ($B@5(B)$B;3EP(B $B@5J8(B$B!&(B ($B@5(B)$B@n>e(B $B9@NI(B		mixed matrix membrane
polymer gas separation membrane
dry-wet phase inversion method
P
315Enabling polyketone membrane with underwater superoleophobicity via a hydrogel-based modification for high-efficiency oil-in-water emulsion separation
(Kobe U.) ($B3X(B)$B!{(BJia Yuandong$B!&(B ($B@5(B)Guan Kecheng$B!&(B ($B3X(B)Zhang Lei$B!&(B ($B@5(B)Lin Yuqing$B!&(B ($B3X(B)Shen Qin$B!&(B ($B3X(B)Zhang Pengfei$B!&(B ($B@5(B)Matsuyama Hideto		polyketone membrane
hydrogel
oil-in-water emulsion separation
P
322Custom-Tailoring of Zero-Dimensional Graphene Oxide Quantum Dots Incorporated Thin-film Nanocomposite Membranes for Highly-Permeable Reverse Osmosis
(Kobe U.) ($B3X(B)$B!{(BShen Qin$B!&(B ($B@5(B)Lin Yuqing$B!&(B ($B@5(B)Matsuyama Hideto		thin-film nanocomposite membrane
graphene oxide quantum dots
reverse osmosis
P
327Effect of polymer molecular weight on structure and performance of PVDF hollow fiber membranes prepared by TIPS process with co-extrusion of solvent using triple orifice spinneret
(Kobe U.) ($B3X(B)$B!{(BZhang Pengfei$B!&(B ($B@5(B)Fang Chuanjie$B!&(B ($B@5(B)Saeid Rajabzadeh$B!&(B ($B@5(B)Kato Noriaki$B!&(B ($B@5(B)Matsuyama Hideto		Thermally induced phase separation (TIPS)
Triple orifice spinneret
Extrued solvent
P
364UiO-66$B$NI=LLEE2Y2~
($B4tIlBg1!<+(B) ($B3X(B)$B!{>!;3(B $B^fJ?(B$B!&(B $BGO^<(B $B9aF`(B$B!&(B ($B4tIlBg9)(B) ($B@5(B)$B5\K\(B $B3X(B$B!&(B ($B4tIlBg6&MQ%;(B) ($B@5(B)$B6a9>(B $BLwB'(B$B!&(B ($B4tIlBg9)(B) ($B@5(B)$B>e5\(B $B@.G7(B		UiO-66
Adsorption
Silylation
P
400TiO2-ZrO2-$BM-5!%-%l!<%HG[0L;R(B(OCL)$BJ#9gKl$N3F
($B?@8MBg1!9)(B/$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 $B=(?M(B		TiO2-ZrO2
NF membrane
organic solvent
P
403$B;@2=%0%i%U%'%s@QAXKl$K$*$1$kM-5!MOG^F)2a$NJ,;RF0NO3X%7%_%e%l!<%7%g%s(B
($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 $B=(?M(B		graphene oxide
stacked nanosheet membrane
molecular dynamics simulation
P
409$B%$%*%s8r49$7$?(BY$B7?%<%*%i%$%H$KBP$9$k0l;@2=CbAG$N5[Ce(B
($B:eI\Bg9)(B) ($B3X(B)$B!{KLAjLO(B $B@?(B$B!&(B ($B:eI\Bg9b@l(B) ($B@5(B)$BJ?NS(B $BBg2p(B$B!&(B ($B:eI\Bg9)(B) ($B@5(B)$B2-ED(B $B0&Mx9a(B$B!&(B ($B@5(B)$B0BED(B $B>;90(B		Ion exchanged Y-type zeolite
Nitrogen monoxide
Adsorption
P
413$B%,%i%9A!0]<05[<}AuCV$G$N2a;@2=?eAG?e$rMQ$$$?0l;@2=CbAG$N5[<}(B
($B:eI\Bg9)(B) ($B3X(B)$B!{;0;^(B $BMN2p(B$B!&(B ($B:eI\Bg9b@l(B) ($B@5(B)$BJ?NS(B $BBg2p(B$B!&(B ($B:eI\Bg9)(B) ($B@5(B)$B2-ED(B $B0&Mx9a(B$B!&(B ($B@5(B)$B0BED(B $B>;90(B		Glass fiber filter type gas absorber
Nitorogen monoaxide
Oxidation by hydrogen peroxide
P
419$B%O%$%7%j%+%<%*%i%$%H$rMQ$$$?O"B3E*(BNO$B;@2=(B
($B:eI\Bg9)(B) ($B3X(B)$B!{CfC+(B $BN<(B$B!&(B ($B:eI\Bg9b@l(B) ($B@5(B)$BJ?NS(B $BBg2p(B$B!&(B ($B:eI\Bg9)(B) ($B@5(B)$B2-ED(B $B0&Mx9a(B$B!&(B ($B@5(B)$B0BED(B $B>;90(B		Nitrogen monoxide
Oxidation
High silica zeolite
P
420$B%,%i%9A!0]%U%#%k%?!KAuCV$rMQ$$$?(BNOx$B?e5[<}%W%m%;%9$K$*$1$k29EY$N1F6A(B
($B:eI\Bg9)(B) ($B3X(B)$B!{:#0f(B $B@?(B$B!&(B ($B:eI\Bg9b@l(B) ($B@5(B)$BJ?NS(B $BBg2p(B$B!&(B ($B:eI\Bg9)(B) ($B@5(B)$B2-ED(B $B0&Mx9a(B$B!&(B ($B@5(B)$B0BED(B $B>;90(B$B!&(B ($B8x32KI;_5!4o8&(B) $B@uLn(B $B??(B		Nitrogen onoxide
Water absorption
Glass fiber filter type gas absorber
P
426$B%$%*%s8r49(B/$B%-%l!<%HA!0]$rMQ$$$?$a$C$-GS?e$+$i$N(BZn$BJ,N%2s<}%7%9%F%`$N3+H/(B
($BF`NI9b@l@l962J(B) ($B3X(B)$B!{5*%N2,(B $B7r(B$B!&(B ($BF`NI9b@l(B) ($B@5(B)$BNS(B $B7$B!&(B ($B@5(B)$BCfB<(B $B=(H~(B		Adsorption separation
Ion exchange/chelate fibers
Plating waste water
P
447$B:.9gM-5!MOG^J,N%$rL\;X$7$?%7%j%3!<%sKl$N3+H/(B
($B?@8MBg1!9)(B/$B@hC$B!&(B $B2CF#(B $BE5><(B$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B		separation of organic mixtures
silicone
crosslink
P
455$B%I!<%Q%_%s$rMQ$$$??;DR7?%"%s%A%U%!%&%j%s%0Kl$N@:L)I=LL@)8f(B
($BEl9)Bg2=@88&(B) ($B3X(B)$B!{9-@%(B $BIRG7(B$B!&(B ($B@5(B)$BBg$B!&(B $B;3@n(B $B?JFs(B$B!&(B ($B@5(B)$B;38}(B $BLT1{(B		surface modification
block copolymer
polydopamine
P
471$B%]%j%"%_%IKl$rMQ$$$?=`HsJ?9U5U?;F)%7%_%e%l!<%7%g%s$K$*$1$k(BNaCl$B$N1F6A(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>;3(B $B=(?M(B$B!&(B ($B7*ED9)6H(B) ($BK!(B)$BF#B<(B $BPR(B$B!&(B ($B@5(B)$B@n>!(B $B9'Gn(B		Molecular dynamics
Polyamide
quasi-nonequilibrium simulation
P
478$B%Q%s9ZJl(BSaccharomyces cerevisiae$B$K$h$k%Q%i%8%&%`$N2s<}(B
($B:eI\Bg1!9)(B) ($B3X(B)$B!{2V;T(B $BM42p(B$B!&(B $B:XF#(B $BHO;0(B$B!&(B $BLnB<(B $B=SG7(B$B!&(B ($B@5(B)$B>.@>(B $B9/M5(B		Recovery
Palladium
Bioreduction
P
487$BAjJ,N%7?(BCO2$B5[<}:^$N5[<}FC@-$K5Z$\$9E:2C:^$N1F6A(B
($BL>Bg1!9)(B) ($B3X(B)$B!{Av=P(B $BN6@1(B$B!&(B ($B@5(B)$BLx@%(B $B7D0l(B$B!&(B ($B@5(B)$BD.ED(B $BMN(B$B!&(B ($B@5(B)$BB'1J(B $B9TMG(B		phase separation
CO2 absorption
dispersion
P
503COSMO-RS$BK!$K$h$k(BCO2$B5[<}$KH<$$1U(B-$B1UAjJ,N%$9$k%"%_%s!&%(!<%F%k!&?e(B3$B@.J,7OMO1U$NC5:w(B
($BL>Bg1!9)(B) ($B3X(B)$B!{Cf2,(B $B??:Z(B$B!&(B ($B3$(B)Tran Khuyen V. B.$B!&(B ($B@5(B)$BLx@%(B $B7D0l(B$B!&(B ($B@5(B)$BD.ED(B $BMN(B$B!&(B ($B@5(B)$BB'1J(B $B9TMG(B		COSMO-RS
liquid-liquid equilibrium
CO2 capture
P
510Development of double-network ion gel-based CO2 separation membrane from non-volatile network precursors
(Kobe U.) ($B3X(B)$B!{(BZhang Jinhui$B!&(B ($B@5(B)Kamio Eiji$B!&(B ($B3X(B)Kinoshita Masayuki$B!&(B ($B3X(B)Yasui Tomoki$B!&(B ($B@5(B)Matsuyama Hideto		ion gel membrane
double-network
gas separation
P
553Novel membrane with well-dispersed polyampholytic copolymer via a composite coagulation process
($B?@8MBg1!9)(B) ($B3X(B)$B2&(B $B@;`v(B$B!&(B ($B3$(B)$BJ}(B $BN)Jv(B$B!&(B ($B@5(B)$B!{>>;3(B $B=(?M(B		zwitterionic
antifouling
membrane surface modification
P
554$B9g@.M-5!2=9gJ*$NJ,N%@:@=$N$?$a$N?75,(BNF$BKl5Z$S%W%m%;%93+H/(B
($B?@8MBg1!2J5;%$%N%Y(B/$B@hC$B!&(B ($B@5(B)$B?7C+(B $BBn;J(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)$B>>;3(B $B=(?M(B$B!&(B ($B?@8MBg1!2J5;%$%N%Y(B/$B@hC		NF membrane
separation and purification
synthetic organic compounds
P
586$BFsN22=%b%j%V%G%s%J%N%7!<%H@QAXKl$N2C05=hM}$K$h$k%J%N$m2aFC@-$N8~>e(B
($B?@8MBg1!2J5;%$%N%Y(B/$B@hC$B!&(B ($B@5(B)$BCf@n(B $B7I;0(B$B!&(B ($B%*%C%/%9%U%)!<%IBg(B) Kulhavy Jiri$B!&(B Tsang Shik Chi Edman$B!&(B ($B?@8MBg1!2J5;%$%N%Y(B/$B@hC$B!&(B ($B?@8MBg1!9)(B/$B@hC$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B$B!&(B ($B?@8MBg1!2J5;%$%N%Y(B/$B@hC		membrane
nanosheet
MoS2
P
5882$B5i%"%_%I2=9gJ*$N9g@.$H1v;@7O$K$*$1$k%,%j%&%`$NCj=PFC@-(B
($B:42lBg1!9)(B) ($B3X(B)$B!{(B逄 $B3J(B辉$B!&(B ($B:42lBgM}9)(B) ($B@5(B)$B?9Dg(B $B??B@O:(B$B!&(B ($B@5(B)$B@n4nED(B $B1Q9'(B$B!&(B ($B@5(B)$BBgEO(B $B7<2p(B		Secondary amide compound
Gallium extraction
Dissociation constant
P
591Hollow fiber membranes with hierarchical spherulite surface structure by thermally induced phase separation using triple-orifice spinneret for membrane distillation
($B?@8MBg(B) ($B3X(B)$B!{(BLiu Wenyi$B!&(B ($B@5(B)Fang Chuanjie$B!&(B ($B3X(B)Zhang Pengfei$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B		membrane distillation
hollow fiber membranes
thermally induced phase separation
P
596$B%"%_%s!&%(!<%F%k!&?e(B3$B@.J,7O1U1UAjJ?9UB,Dj(B
($BL>Bg9)(B) ($B3X(B)$B!{BW(B $BMOCS(B$B!&(B ($B@5(B)$B%A%c%s(B $B%/%%%$%s(B$B!&(B ($B@5(B)$BLx@%(B $B7D0l(B$B!&(B ($B@5(B)$BD.ED(B $BMN(B$B!&(B ($B@5(B)$BB'1J(B $B9TMG(B		amine
Measure the phase diagram
P
602$B2YEEKl$K$*$1$k(B1$B2A(B/2$B2A%$%*%sJ,N%$NJ,;R%7%_%e%l!<%7%g%s(B
($B9)3X1!Bg@h?J9)(B) ($B3X(B)$B!{@';^(B $B0l51(B$B!&(B ($B3X(B)$BHu8}(B $BH;?M(B$B!&(B ($B@5(B)$B5\@n(B $B2mLp(B$B!&(B ($B@5(B)$B9b1)(B $BMN=<(B		Nano filtration membrane
Non Equilibrium Molecular Dynamics
Monovalent and divalent cations
P
633$BM-5!%-%l!<%HG[0L;R$rMQ$$$?(BTiO2-SiO2$BJ#9g:`NA$NFC@-I>2A$H5$BNJ,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 $B=(?M(B		TiO2-SiO2
gas separation
organic chelating ligands
P
685$B%?%s%Q%/~Kl$N%"%s%A%U%!%&%j%s%0FC@-I>2A(B
($BEl9)Bg2=@88&(B) ($B3X(B)$B!{7*86(B $BM:Bg(B$B!&(B ($B@5(B)$BBg$B!&(B ($B@5(B)$B;38}(B $BLT1{(B		Fouling
Surface modification
Protein
P
692AEI $B7?%<%*%i%$%HKl$N9g@.J}K!$H$=$NF)2aJ,N%FC@-$N8!F$(B
($BAaBg@h?JM}9)(B) ($B3X(B)$B66D^(B $BM%M4(B$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 $B@5I'(B		zeolite
membrane
gas separation
P
696Gel-free SAC$BK!$rMQ$$$?(BMFI$B7?Kl9g@.$K$*$1$k=$N1F6A(B
($B4tIlBg1!<+A3(B) ($B3X(B)$B!{Mn9g(B $B42$B!&(B ($B4tIlBg9)(B) $BHS:d(B $B:L2C(B$B!&(B ($BD+F|Bg;u(B) ($B@5(B)$B>eLn(B $B63J?(B$B!&(B ($B;:Am8&(B) ($B@5(B)$B:,4_(B $B=(G7(B$B!&(B ($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 ($B4tIlBg6&MQ%;(B) ($B@5(B)$B6a9>(B $BLwB'(B		MFI type zeolite membrane
steam-assisted conversion
silica support
P
712$B%9%F%"%j%s;@1v%^%$%/%mN3;R(BPickering$B%(%^%k%7%g%sAj$N$m2a@-I>2A(B
($BF`NI9b@l@l962J(B) ($B3X(B)$B!{?@86(B $B=UB@(B$B!&(B ($BB@J?2=3X;:6H(B) $B2,Ln(B $B9@L@(B$B!&(B $B>>ED(B $B?.G7(B$B!&(B ($BF`NI9b@l(B) ($B@5(B)$BD>9>(B $B0l8w(B$B!&(B ($BF|Bg@8J*;q8;3X(B) ($B@5(B)$B:#0f(B $B@5D>(B		Pickering emulsion
stearate
filtration
P
714Pt$B?(G^$rF3F~$7$?%7%j%+7O?(G^Kl$N:n@=$H(BMCH$BC&?eAGH?1~(B
($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 $B=(?M(B$B!&(B ($B?@8MBg1!2J5;%$%N%Y(B/$B@hC		catalytic membrane reactor
organic hydride
hydrogen storage
P
715FO$B%U%!%&%j%s%0$G$NF)?e5sF0$K5Z$\$9%U%!%&%i%s%HAH@.$N1F6A(B
($B?@8MBg1!2J5;%$%N%Y(B/$B@hC>MU(B $B??M3(B$B!&(B ($B@5(B)$BCf@n(B $B7I;0(B$B!&(B ($B@5(B)$B?7C+(B $BBn;J(B$B!&(B ($B@5(B)$B5H2,(B $BJ~5W(B$B!&(B ($B?@8MBg1!9)(B/$B@hC$B!&(B ($B@5(B)$BD9C+@n(B $B?J(B$B!&(B ($B@5(B)$B?@Hx(B $B1Q<#(B$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B		membrane
forward osmosis
fouling
P
726Engineering of Antifouling Thin Film Composite Nanofitration Membrane with Enhanced Separation Property via Surface Silicification
(Kobe U.) ($B3X(B)Istirokhatun Titik$B!&(B ($B@5(B)Lin Yuqing$B!&(B ($B@5(B)$B!{(BMatsuyama Hideto		nanofiltration
silica layer
electrostatic force
P
730$B8w%U%!%$%P!<%W%m!<%V$rMQ$$$?1UKlN.Cf$G$N8|$57WB,$K4X$9$k9M;!(B
($B@EBg1!(B) ($B3X(B)$B!{1|0f(B $B5.G7(B$B!&(B ($B@5(B)$B??ED(B $B=SG7(B$B!&(B ($B@5(B)$B?eEh(B $BM44p(B		Liquid film flow
Thickness measurement
Optical-fiber-based Reflectance Probe
P
815$BAB?e@-?<6&>=MOG^$K$h$k6(F1Cj=P7O$N3NN)$H%j%A%&%`J,N%$X$N1~MQ(B
($B6eBg1!9)(B) ($B3X(B)$B!{2VED(B $BN4J8(B$B!&(B ($B@5(B)$B8eF#(B $B2m9((B		Deep eutectic solvents
Liquid-liquid extraction
Lithium
P
834Enhancing the Separation Performance of Polyimide based Mixed Matrix Membranes by Miniaturization and Silane Surface Modification of Filler Particles
($B;38}Bg1!AO@.2J3X(B) ($B3X(B)$B!{(BLiu Yongsheng$B!&(B $B8~0f(B $BM/(B$B!&(B ($B3X(B)$B9b66(B $B9V$B!&(B ($B@5(B)$B4nB?(B $B1QIR(B$B!&(B ($B@5(B)$BEDCf(B $B0l9((B		mixed matrix membranes
zeolites
gas separation
P
835Effect of carbonization condition on gas permeation properties of carbon membranes prepared from a polyimide hollow fiber membrane
($B;38}Bg1!4D6-6&@87O(B) ($B3X(B)$B!{(BNie Jing$B!&(B ($B;38}Bg1!AO@.2J3X(B) $B5H_7(B $BE5??(B$B!&(B ($B@5(B)$BEDCf(B $B0l9((B		Carbon molecular sieve membranes
Pyrolysis
Gas separation
P
847$B%"%_%I;@7?Cj=P:^$rMQ$$$?GQ(BLIB$B%b%G%kMO1U$+$i$N(BCo$B$*$h$S(BNi$B$N2s<}(B
($B6eBg1!9)(B) ($B3X(B)$B!{KeHx(B $B9I2p(B$B!&(B ($B3X(B)$B2VED(B $BN4J8(B$B!&(B ($B@5(B)$B8eF#(B $B2m9((B		separation
lithium ion battery
critical metals
P
$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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