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$B:G=*99?7F|;~!'(B2015-03-05 09:42:37
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13:20$B!A(B 15:20XE301Li1.5Mn2O4$B$N8GBN(BNMR$B!&(BHR-TEM$B$K$h$k9=B$4Q;!(B
($BKL6eBg9q4D9)(B) $B@>(B $B7{G7(B$B!&(B ($B@5(B)$B!{NkLZ(B $BBs(B
solid NMR
HR-TEM
LiMn2O4
4-e710
13:20$B!A(B 15:20XE302$B4629AjJ,N%?eMO@-1UBN$N3+H/$*$h$SM=B,(B
(KRI) ($BK!(B)$BC01)(B $B=_(B
temperature-sensitive phase separation
lower critical solution temperature
QSPR
4-i6
13:20$B!A(B 15:20XE303$BO"B3<0D61s?45!$rMQ$$$?%i%F%C%/%9%J%NN3;R$NJ,N%(B
($BF|N)9)5!(B) ($B@5(B)$B!{9b66(B $B$+$[$k(B$B!&(B $B8M0f(B $B428|(B$B!&(B $B>.B<(B $B?r?M(B$B!&(B $BJ!86(B $B1I0l(B$B!&(B $B:,K\(B $B7z0l(B$B!&(B $B:d>e(B $B9@(B$B!&(B $B:4F#(B $B9'Fs(B
Continuous Flow Ultracentrifuge
Density Gradient Separation
Nano particle
4-i167
13:20$B!A(B 15:20XE304Silicalite$BKl@-G=$K5Z$\$99g@.>r7o1F6A(B
($B4tIlBg1!9)(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 $BCS>e(B $BE0(B$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 $BLwB'(B
zeolite membrane
separation
bio-ethanol
4-a766
13:20$B!A(B 15:20XE305Molecular Design of High CO2 Reactivity and Low Viscosity Ionic Liquids for CO2 Separative Facilitated Transport Membrane
(U. Notre Dame) ($B3X(B)$B!{BgC+(B $BIK?M(B$B!&(B Zhang Y.$B!&(B ($B?@8MBg1!9)(B) ($B@5(B)$B?@Hx(B $B1Q<#(B$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B$B!&(B (U. Notre Dame) Maginn E.
Ionic Liquids
Viscosity
Molecular Dynamics Simulation
4-a259
13:20$B!A(B 15:20XE306$BD6J4:U=$rMQ$$$?(BMFI$B%<%*%i%$%HKl$N@=Kl(B
($B.Ln(B $BN5J?(B$B!&(B ($B3X(B)$BKLEh(B $B85$B!&(B ($B3X(B)$BCSED(B $BJb(B$B!&(B ($B3X(B)$B>>;3(B $B3(H~(B$B!&(B ($B@5(B)$BLnB<(B $B4490(B
MFI zeolite membranes
ultra-milled seed crystals
pervaporation
4-a549
13:20$B!A(B 15:20XE307$B:Y9&9=B$$N0[$J$k;Y;}BN>e$K@=Kl$7$?(BZSM-5$BKl$NF)2aFC@-$N8!F$(B
($BAaBg@h?JM}9)(B/$BAaBgM}9)Am8&(B/JST-CREST) ($B@5(B)$B>>J}(B $B@5I'!&(B ($BAaBg@h?JM}9)(B) ($B3X(B)$B!{5HED(B $BBg51(B$B!&(B ($B@5(B)$B@%2<(B $B2mGn(B
ZSM-5
permeation properties
support
4-a635
13:20$B!A(B 15:20XE308$B%?%s%K%s!&%j%0%K%sJ#9g:`NA$+$i$NJ,;R$U$k$$C:AGKl$N9g@.>r7o(B
($B;38}Bg9)(B) ($B3X(B)$B!{EDB<(B $B63M4(B$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 $B1QIR(B
Carbon membrane
Lignin
tannin
4-a297
13:20$B!A(B 15:20XE309$BD62;GHJ.L8>F7kK!$K$h$j:n@=$5$l$?%A%?%K%"Kl$N?e>x5$A*BrF)2a@-$N8&5f(B
($B2#9qBg1!(B) ($B3X(B)$B!{J?;3(B $BBg2p(B$B!&(B ($B3X(B)$BCfLn(B $BC#L&(B$B!&(B ($B2#9qBg(B) $BC*Hx(B $B98Bg(B$B!&(B ($B2#9qBg1!(B) ($B@5(B)$BAj86(B $B2mI'(B
separation membrane
ultrasonic spray sintering
gas separation
4-a249
13:20$B!A(B 15:20XE310$B%S%K%k%H%j%a%H%-%7%7%i%s$rA06nBN$H$7$?AB?e@-%7%j%+Kl$ND4@=$H?];@%(%A%k$NJ,N%FC@-(B
($B4X@>Bg4DET9)(B) ($B3X(B)$B!{8"F#(B $BBgN<(B$B!&(B $B>.@n(B $BMK(B$B!&(B ($B@5(B)$B9SLZ(B $BDgIW(B$B!&(B ($B@5(B)$B;3K\(B $B=(
Membrane separation
Pervaporation
Hydrophobicity
4-a116
13:20$B!A(B 15:20XE311$B$*$,$/$:$NDc294%Ag$K$*$$$F4%Ag6/EY$,4%Ag5sF0$K5Z$\$91F6A(B
($B?.=#Bg1!M}9)(B) ($B3X(B)$B!{Gk86(B $BNJB@O:(B$B!&(B ($B?.=#BgA!0](B) ($B@5(B)$BEhED(B $B8^I4N$(B$B!&(B ($B@5(B)$BJ!D9(B $BGn(B$B!&(B ($B@5(B)$B9b66(B $B?-1Q(B
constant drying period
fixed bed drier
energy efficiency
4-h879
13:20$B!A(B 15:20XE312$B5U?;F)Kl$X$N%j%s;i
($B?@8MBg9)(B) ($B3X(B)$BM?FaNf(B $B85$B!&(B ($B?@8MBg1!9)(B/$B@hC$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B
Reverse osmosis membrane
Atom transfer radical polymerization
Phosphorylcholine polymer
4-a770
13:20$B!A(B 15:20XE313$B%$%*%s8r49Kl$rMQ$$$?%l%I%C%/%97?H?1~4o$N3+H/(B
($B.J?(B $B3Y=((B$B!&(B $BBg1:(B $B6W2;(B$B!&(B ($B3X(B)$BCSED(B $BJb(B$B!&(B ($B3X(B)$B>.Ln(B $BN5J?(B$B!&(B ($B3X(B)$B>>;3(B $B3(H~(B$B!&(B ($B@5(B)$BLnB<(B $B4490(B$B!&(B ($B86;RNO5!9=(B) $B_7ED(B $B??0l(B$B!&(B $BH,4,(B $BE0Li(B$B!&(B $BEDCf(B $B?-9,(B$B!&(B $B5WJ](B $B??<#(B
thermochemical water splitting IS process
ion exchange membrane
redox reactor
4-a652
13:20$B!A(B 15:20XE314$B;Y;}BN>e$N=C4;}>uBV$,(BFAU$B7?%<%*%i%$%HKl$N@=Kl$K5Z$\$91F6A(B
($BAaBg@h?JM}9)(B/$BAaBgM}9)Am8&(B/JST-CREST) ($B@5(B)$B>>J}(B $B@5I'!&(B ($BAaBg@h?JM}9)(B) ($B3X(B)$B!{AR2<(B $B>-8w(B$B!&(B ($B@5(B)$B@%2<(B $B2mGn(B
FAU-type zeolite
Membrane
dehydration
4-a873
13:20$B!A(B 15:20XE315$B%P%$%*%,%92=;D^V%?!<%k$rMQ$$$?C:AGKl$N:n@=(B
($B;38}Bg1!M}9)(B) ($B3X(B)$B!{8eF#(B $B=Y2p(B$B!&(B ($B@5(B)$B4nB?(B $B1QIR(B$B!&(B ($B@5(B)$BEDCf(B $B0l9((B$B!&(B ($B@5(B)$B7'@Z(B $B@t(B$B!&(B ($BKL8+9)Bg(B) ($B@5(B)$BNkLZ(B $BJY(B
Carbon membrane
Biogas Tar
Gas separation
4-a311
13:20$B!A(B 15:20XE316$BCfOBD@EBK!$K$h$k?e;@2=%K%C%1%k$N@8@.$H$=$N8G1UJ,N%FC@-$NI>2A(B
($B2#9qBg1!9)(B) ($B3X(B)$B!{K-ED(B $BM*Zv(B$B!&(B ($B@5(B)$BCfB<(B $B0lJf(B
specific cake resistance
sedimentation
zeta potential
4-b329
13:20$B!A(B 15:20XE317HF-HCl$B?eMO1U$rMQ$$$?>=@O$K$h$k(BZr$B$*$h$S(BHf$B$NJ,N%>r7o$N8!F$(B
($B4X@>Bg4DET9)(B) ($B3X(B)$B!{W"ED(B $B7r0l(B$B!&(B ($B@5(B)$B9SLZ(B $BDgIW(B$B!&(B ($B%i%59)6H(B) $B2&(B $B5HK-(B$B!&(B $B1sF#(B $B9%;J(B$B!&(B ($B4X@>Bg4DET9)(B) ($B@5(B)$B;3K\(B $B=(
Crystallization
Zirconium
separation
4-g218
13:20$B!A(B 15:20XE318$B%j%0%K%sM3MhK'9aB22=9gJ*$NJ,;R$U$k$$%+!<%\%s$X$N1UAj5[C&Ce(B
($BElBg@88&(B) ($B3X(B)$B!{(BTran Linh Ngoc$B!&(B ($B@5(B)$BGwED(B $B>O5A(B$B!&(B $BF#ED(B $BMN?r(B
lignocellulose
lignin-derived aromatic chemicals
molecular sieving carbons
4-e826
13:20$B!A(B 15:20XE319MFI$B%<%*%i%$%HKlF)2a$K5Z$\$9%"%k%_%K%&%`E:2C$N1F6A(B
($B$B!&(B ($B3X(B)$B?y;3(B $BM:Ht(B$B!&(B ($B3X(B)$BCSED(B $BJb(B$B!&(B ($B3X(B)$B>.Ln(B $BN5J?(B$B!&(B ($B3X(B)$B>>;3(B $B3(H~(B$B!&(B ($B=;M'EE9)(B) $B:XF#(B $B?r9-(B$B!&(B $BI6;3(B $BGn6)(B$B!&(B $B7,86(B $B0lLi(B$B!&(B ($B
MFI zeolite membrane
porous silica substrate
aluminium
4-a855
13:20$B!A(B 15:20XE320AlPO4-18 $BKl$N(BCO2 / CH4 $BF)2aJ,N%5sF0$N8!F$(B
($BAaBg@h?JM}9)(B) ($B3X(B)$B!{BgEh(B $B5AOB(B$B!&(B ($B3X(B)$B$B!&(B ($BAaBg@h?JM}9)(B/$BAaBgM}9)Am8&(B/JST-CREST) ($B@5(B)$B>>J}(B $B@5I'(B
membrane separation
AlPO4-18
CO2 / CH4
4-a629
13:20$B!A(B 15:20XE321$B9bJ,;R(B/$B%7%/%m%G%-%9%H%j%sKt$O%<%*%i%$%HJ#9gKl$N:n@=$HF)2aJ*@-(B
($B;38}Bg1!M}9)(B) ($B3X(B)$B!{A}ED(B $BCNLi(B$B!&(B ($B1'It9b@l(B) $B;3K\(B $BM&Ka(B$B!&(B $B;3yu(B $BGn?M(B$B!&(B ($B;38}Bg1!M}9)(B) ($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 $B1QIR(B
polymer
cyclodextrin
zeolite
4-a318
13:20$B!A(B 15:20XE322$BE:2CJ*$K$h$kC:;@%+%k%7%&%`7k>=FC@-$NJQ2=$H%2A(B
($B2#9qBg1!9)(B) ($B3X(B)$B!{9b4_(B $BB@0l(B$B!&(B ($B@5(B)$BCfB<(B $B0lJf(B
shouseki
4-g328
13:20$B!A(B 15:20XE323$B%P%$%*%^%9GQ4~J*$r86NA$H$7$?3h@-C:$N@=B$(B
($B4X@>Bg1!M}9)(B) ($B3X(B)$B!{G_86(B $B7$B!&(B ($B4X@>Bg4DET9)(B) ($B@5(B)$BNS(B $B=g0l(B
activated carbon
surface area
pore volume
4-e62
13:20$B!A(B 15:20XE324$BD6NW3&Fs;@2=C:AG(B+$B?e7O$N%9%i%0N.$K$*$1$k%(%^%k%7%g%sCj=P$rMxMQ$7$?8GBNJ,;6MO1U$N:n@=(B
($BEl9)Bg9)(B) ($B3X(B)$B!{B<>e(B $BM5:H(B$B!&(B ($BEl9)Bg1!M}9)(B) ($B@5(B)$B2<;3(B $BM52p(B
supercritical drying
emulsion extraction
slug flow
4-f216
13:20$B!A(B 15:20XE325$B?e%A%c%s%M%k$NJ,;RM"Aw5!9=$rLO5<$7$?9b8zN(?eF)2aKl$NM}O@@_7W(B
($B9)3X1!Bg9)(B) ($B3X(B)$B!{>.NS(B $B=YG7=u(B$B!&(B ($B@5(B)$B9b1)(B $BMN=<(B
membrane
aquaporin
water chanel
4-a839
13:20$B!A(B 15:20XE326$B5[Ce;n83$rMQ$$$?(BNa-ZSM-5$BKl$NKl9=B$$HF)2a@-$N4X78$K$D$$$F$N8!F$(B
($BAaBg@h?JM}9)(B/$BAaBgM}9)Am8&(B/JST-CREST) ($B@5(B)$B>>J}(B $B@5I'!&(B ($BAaBg@h?JM}9)(B) ($B3X(B)$B!{HSEg(B $BM%5.(B$B!&(B ($B@5(B)$B@%2<(B $B2mGn(B
MFI-type zeolite membrane
Adsorption
Structure
4-a579
13:20$B!A(B 15:20XE327$BBQ5W@-!"BQ;@@-$KM%$l$??F?e@-(BMFI$B7?%<%*%i%$%HKl$N@=Kl$H%P%$%*%(%?%N!<%kG;=L%W%m%;%9$X$N1~MQ(B
($B;38}Bg1!M}9)(B) ($B3X(B)$B!{K'Ln(B $B98M$(B$B!&(B ($B;38}Bg1!G@(B) $B;3ED(B $B$B!&(B $B9b:d(B $BCRG7(B$B!&(B $BB$B!&(B ($B;38}Bg1!M}9)(B) ($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 $B1QIR(B
MFI zeolite mebranes
bio-ethanol
concentration process
4-a440
13:20$B!A(B 15:20XE328$BF)@OKl$N%U%!%&%j%s%0@)8f$K8~$1$??eOB?e$N%_%/%m5sF02r@O(B
($BL>9)Bg(B) ($B3X(B)$B!{NkLZ(B $BNCLi(B$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 $B=(
membrane separation
molecular dynamics
free energy
4-a51
13:20$B!A(B 15:20XE329$B@PL}%3!<%/%9$r86NA$H$9$k3h@-C:$N:Y9&$*$h$SI=LL2=3XFC@-(B
($BL>Bg1!9)(B) ($B3X(B)$B!{CfEg(B $B424p(B$B!&(B ($B@5(B)$B7&ED(B $B8w9((B$B!&(B ($B@5(B)$B>>ED(B $B?N
petroleum coke
activated carbon
KOH activation
4-e619
13:20$B!A(B 15:20XE330$BAB?e@-M-5!B?9&2$B5[<}B.EY$X5Z$\$91F6A(B
($B?.=#Bg1!M}9)(B) ($B3X(B)$B!{$B!&(B ($B?.=#BgA!0](B) ($B@5(B)$BD9ED(B $B8w@5(B$B!&(B ($B@5(B)$BEhED(B $B8^I4N$(B$B!&(B ($B@5(B)$BJ!D9(B $BGn(B$B!&(B ($B@5(B)$B9b66(B $B?-1Q(B
hydrophobic porous membrane
chemical absroption
EDX
4-a773
13:20$B!A(B 15:20XE331$BHy:YAt$NB8:_$,%;%H%i!
($BEl9)Bg1!M}9)(B) ($B3X(B)$B!{K*C+(B $B=$J?(B$B!&(B ($B@5(B)$B>>K\(B $B=(9T(B
batch settler
microalgae
liquid-liquid dispersion
4-f590
13:20$B!A(B 15:20XE332Si-CHA$B%<%*%i%$%H$ND4@=$H%,%95[CeFC@-(B
($BF`NI@hC$B!&(B $B2CF#(B $BH~F`;R(B$B!&(B (RITE) ($B@5(B)$BMhED(B $B9/;J(B$B!&(B ($B@5(B)$BM>8l(B $B9nB'(B
pure silica zeolite
chabazite
adsorption
4-e760
13:20$B!A(B 15:20XE333$B%?%s%Q%/=2=$KBP$9$kAX>u%1%$;@1vE:2C$N1F6A(B
($BAaBg@h?JM}9)(B) ($B3X(B)$B!{1]K\(B $BBs;x(B$B!&(B $B@P:d(B $BfFB@(B$B!&(B ($B@5(B)$BJ?Bt(B $B@t(B$B!&(B ($B@5(B)$B>.KY(B $B?<(B
crystallization
protein
layered silicate
4-g232
13:20$B!A(B 15:20XE334$B_I2a%1!<%/9=B$$KM?$($k%^%$%/%m%P%V%k$NE:2C8z2L(B
($B:eI\Bg1!9)(B) ($B3X(B)$B!{@8J}(B $B51(B$B!&(B ($B3X(B)$B5AK\(B $BL@I'(B$B!&(B ($B@5(B)$BEDCf(B $B9'FA(B$B!&(B ($B@5(B)$B4dED(B $B@/;J(B
Dead-end filtration
Microbubble
Cake strucuture
4-b508
13:20$B!A(B 15:20XE335$B6bB0;@2=J*N3;R$N2=3XE*@-2$B8:05J|;6B.EY$K5Z$\$91F6A(B
($B?.=#BgA!0](B) ($B3X(B)$B!{J]2J(B $BM-4u(B$B!&(B ($B@5(B)$BEhED(B $B8^I4N$(B$B!&(B ($B@5(B)$BD9ED(B $B8w@5(B$B!&(B ($B@5(B)$BJ!D9(B $BGn(B$B!&(B ($B@5(B)$B9b66(B $B?-1Q(B
diethanolamine
stripping
chemical absorption
4-d897
13:20$B!A(B 15:20XE336$B?eAGA*BrF)2a%7%j%+Kl$N9g@.5Z$S$=$NKlH?1~4o$H$7$F$N1~MQ(B
($BElBg1!9)(B) ($B3X(B)$B!{@DLn(B $B=U$B!&(B ($B@5(B)$B9b3@(B $BFX(B$B!&(B ($B@5(B)$B?{86(B $B9'(B$B!&(B ($B@5(B)$B5FCO(B $BN4;J(B$B!&(B Oyama S. Ted
silica membrane
CVD
membrane reactor
4-a695
13:20$B!A(B 15:20XE337$B:Y9&Fb=
($BF`NI@hC$B!&(B $BIp;3(B $BGnF;(B$B!&(B ($BCO5e4D6-8&(B) ($B@5(B)$BGO>l(B $BH~CR;R(B$B!&(B ($B@5(B)$BM>8l(B $B9nB'(B
Palladium
Hydrogen
Pore-Fill-type
4-a758
13:20$B!A(B 15:20XE338$B%P%C%ANd5Q>=@O$K$*$1$kN37BJ,I[$*$h$SB?7A@)8f$K4X$9$k8&5f(B
($BEl9)Bg(B) ($B3X(B)$B!{EZ0f(B $B7r;J(B$B!&(B $B5HED(B $B>090(B$B!&(B ($B@5(B)$B4X(B $B9(Li(B
crystal size distribution
polymorphism
population balance
4-g743
13:20$B!A(B 15:20XE339$BJ|
($BKL6eBg1!(B) ($B3X(B)$B!{>>@/(B $BM59b(B$B!&(B ($B@5(B)$B>e9>='(B $B0lLi(B
radiation-induced graft polymerization
polymer brush
sugar chain cluster effect
4-e646
13:20$B!A(B 15:20XE340$BAB?e@-%;%i%_%C%/Kl$rMQ$$$???6uKl>xN1K!$K$h$k%9%/%m!<%9?eMO1UG;=L(B
($BEl9)Bg1!M}9)(B) ($B3X(B)$B!{?@C+(B $BCR5,(B$B!&(B ($BEl9)Bg9)(B) $B9a;3(B $BKS7n(B$B!&(B ($BEl9)Bg1!M}9)(B) ($B@5(B)$BW"ED(B $BM:0lO/(B$B!&(B ($B@5(B)$B0KEl(B $B>O(B
membrane distillation
hydrophobic membrane
sucrose concentration
4-a410
13:20$B!A(B 15:20XE341PV$BKl(B+$B>xN1J#9g%W%m%;%9$K$h$k%R%I%i%8%s$NC&?e(B
($BL>9)Bg(B) ($B3X(B)$B!{>.NS(B $BH~Jf(B$B!&(B ($B@5(B)$B?9(B $B=($B!&(B ($B@5(B)$B4dED(B $B=$0l(B$B!&(B ($B@5(B)$BFn1@(B $BN<(B$B!&(B ($B85L>9)Bg(B) $B>.@>(B $BM:2p(B$B!&(B ($BNfFnM}9)Bg(B) $BM{(B $B_=h_(B
Pervaporation
Hybrid process
Azeotropic mixture
4-c74
13:20$B!A(B 15:20XE342$B%J%N%U%!%$%P!
($BL>Bg9)(B) ($B3X(B)$B!{9b66(B $B:L(B$B!&(B ($B@5(B)$B8~0f(B $B9/?M(B
nanofiber membrane
classification
colloidal particle
4-b362
13:20$B!A(B 15:20XE343$B%H%j%a%A%k%7%i%N!<%k=|5n$N$?$a$NFsNLBN2=H?1~(B
($BKL6eBg1!(B) ($B3X(B)$B!{;38}(B $BBg(B$B!&(B ($B@5(B)$B>e9>='(B $B0lLi(B
Radiation-induced graft polymerization
Trimethylsilanol
Dimerization
4-e543
13:20$B!A(B 15:20XE344$B3Fe$G$N?eJ,;R$N@EE*9=B$$*$h$SF0E*5sF0$K4X$9$kJ,;RO@E*8&5f(B
($B9)3X1!Bg9)(B) ($B3X(B)$B!{CfEg(B $B@?<#(B$B!&(B ($B@5(B)$B9b1)(B $BMN=<(B
antifouling
molecular dynamis
water
4-a829
13:20$B!A(B 15:20XE345$B%;%i%_%C%/GvKl$N4%Ag<}=L$K$h$k1~NO@8@.$HJQ7A5sF0$NM}O@E*8&5f(B
($B4tIlBg1!9)(B) ($B3X(B)$B!{:dED(B $BBs:H(B$B!&(B ($B@5(B)$B>.NS(B $B?.2p(B$B!&(B ($B@5(B)$BHDC+(B $B5A5*(B
ceramic
drying shrinkage
stress
4-g727
13:20$B!A(B 15:20XE346Shielding effect of electro-kinetic charge of PSL particle by the adsorption of neutral polymer
($BC^GHBg@8L?4D6-7O(B) ($B3X(B)$B!{(BWu Yunxiao$B!&(B ($B@5(B)$BB-N)(B $BBY5W(B
electrophoresis
polyethylene oxide
polystyrene latex
4-b361
13:20$B!A(B 15:20YE301$B9bJ,;R6E=8:^$N=|By@-G=$K5Z$\$9J,Cm2s?t!$E:2CNL!$J,;6>uBV$N1F6A-!!=C1=c2=%b%G%k$K$h$k%7%_%e%l!<%7%g%s(B
($B:eI\Bg9)(B) ($B3X(B)$B!{5\Eg(B $B>"(B$B!&(B ($B0B@Q_I;f(B) ($B@5(B)$BNw2,(B $BM5?M(B$B!&(B ($B:eI\Bg1!9)(B) ($B@5(B)$BEDCf(B $B9'FA(B$B!&(B ($B@5(B)$B4dED(B $B@/;J(B
flocculation
polymer flocculant
model simulation
4-b308
13:20$B!A(B 15:20YE302$B9bJ,;R6E=8:^$N=|By@-G=$K5Z$\$9J,Cm2s?t!$E:2CNL!$J,;6>uBV$N1F6A-"!=%b%G%k7|By7O$K$h$k6E=8
($B:eI\Bg9)(B) ($B3X(B)$B!{5\Eg(B $B>"(B$B!&(B ($B0B@Q_I;f(B) ($B@5(B)$BNw2,(B $BM5?M(B$B!&(B ($B:eI\Bg1!9)(B) ($B@5(B)$BEDCf(B $B9'FA(B$B!&(B ($B@5(B)$B4dED(B $B@/;J(B
flocculation
polymer flocculant
model simulation
4-b310
13:20$B!A(B 15:20YE303$B?;F)05$NH/8=$H<'@-2s<}$rN>N)$9$k5!G=@-HyN3;R$N3+H/(B
($B?@8MBg1!9)(B/$B@hC.@n(B $BBgCO(B$B!&(B ($B@5(B)$B;0Ln(B $BBY;V(B$B!&(B ($B@5(B)$B9b66(B $BCR51(B$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B
Draw solution
Magnetic particles
Forward osmosis
4-a764
13:20$B!A(B 15:20YE304$B?eAGF)2a%7%j%+J#9gKl$K$h$kKlH?1~4o3+H/(B
($B$B!&(B ($B3X(B)$B>.Ln(B $BN5J?(B$B!&(B ($B3X(B)$B>>;3(B $B3(H~(B$B!&(B ($B@5(B)$BLnB<(B $B4490(B$B!&(B ($B86;RNO5!9=(B) ($B@5(B)$BEDCf(B $B?-9,(B$B!&(B $B5WJ](B $B??<#(B
cuonter diffusion CVD method
silica hybrid membranes
membrane reactor
4-a588
13:20$B!A(B 15:20YE305$B=C4;}>uBV$,(BRHO$BKl$NF)2aJ,N%FC@-$K5Z$\$91F6A(B
($BAaBg@h?JM}9)(B) ($B3X(B)$B$B!&(B ($B3X(B)$B!{C0CO(B $B??M}(B$B!&(B ($BAaBg@h?JM}9)(B/$BAaBgM}9)Am8&(B/JST-CREST) ($B@5(B)$B>>J}(B $B@5I'(B
RHO
membrane
synthesis
4-a571
13:20$B!A(B 15:20YE306$B8w?(G^?eAG@=B$$KMQ$$$k8w2M66%]%j%$%_%IJ#9gKl$N:n@=>r7o$N8!F$(B
($B;38}Bg1!M}9)(B) ($B3X(B)$B!{NS(B $B7rB@O:(B$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 $B1QIR(B
photocrosslinked polyimide
composite membrane
4-a447
13:20$B!A(B 15:20YE307IPA-$B?e:.9g>x5$$N9bB.C&?e$N$?$a$NEy2CB.86NA6!5kK!(B
($B1'ET5\Bg1!9)(B) ($B3X(B)$B!{5FCO(B $BM*J?(B$B!&(B ($B3X(B)$B@PED(B $B=a(B$B!&(B ($B@5(B)$B:4F#(B $B9d;K(B$B!&(B ($B;:Am8&ElKL(B) ($B@5(B)$BD9C+@n(B $BBY5W(B$B!&(B ($B1'ET5\Bg1!9)(B) ($B@5(B)$B0KF#(B $BD>
zeolite membrane
vapor permeation
IPA and water
4-a32
13:20$B!A(B 15:20YE308Pd/Ag$BKl$N?eAGFs;@2=C:AG:.9g5$$+$i$N?eAGF)2a$K4X$9$k8&5f(B
($B7DXfBg1!M}9)(B) ($B3X(B)$B!{2OV?(B $BM-5#(B$B!&(B Hasan M. Faizal$B!&(B ($B7DXfBgM}9)(B) $B2#?9(B $B9d(B$B!&(B ($B@5(B)$B?"ED(B $BMx5W(B
Membrane Separation
Hydrogen
Carbon Dioxide
4-a395
13:20$B!A(B 15:20YE309Preparation of PVC/VC-co-PEGMA blend membranes and evaluation of their antifouling properties
(Kobe U.) ($B3X(B)$B!{(BZhou Zhuang$B!&(B ($B3X(B)Sun Yuchen$B!&(B ($B3$(B)Rajabzadeh Saeid$B!&(B ($B3$(B)Shaikh Abdul Rajjak$B!&(B ($B@5(B)Kakihana Yuriko$B!&(B ($B@5(B)Matsuyama Hideto
Amphiphilic copolymer
Antifouling membrane
Polyvinyl chloride
4-a674
13:20$B!A(B 15:20YE310$B%<%*%i%$%HKl$K$h$k%(%A%l%s%8%"%_%s?eMO1UJ,N%(B
($B$B!&(B $B1,7n(B $B0lJ?(B$B!&(B $B5\CO(B $BNJ(B$B!&(B ($B3X(B)$BCSED(B $BJb(B$B!&(B ($B3X(B)$B>.Ln(B $BN5J?(B$B!&(B ($B3X(B)$B>>;3(B $B3(H~(B$B!&(B ($B@5(B)$BLnB<(B $B4490(B
MOR zeolite membranes
ethylenediamine separation
pervaporation
4-a286
13:20$B!A(B 15:20YE311silicalite-1$BKl$NKl7A@.2aDx$N8!F$(B
($BAaBg@h?JM}9)(B) ($B3X(B)$B$B!&(B ($B3X(B)$B!{6b;R(B $BBsLp(B$B!&(B ($B3X(B)$BHSEg(B $BM%5.(B$B!&(B ($B3X(B)$B8M4,(B $B7=M4(B$B!&(B ($BAaBg@h?JM}9)(B/$BAaBgM}9)Am8&(B/JST-CREST) ($B@5(B)$B>>J}(B $B@5I'(B
zeolite
silicalite-1 membrane
growth process
4-a585
13:20$B!A(B 15:20YE312$B8w?(G^Kl%3%s%?%/%?!<$N@-G=$KM?$($kMOB81v$N1F6A(B
($B;38}Bg9)(B) ($B3X(B)$B!{FjLZ(B $BBk$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 $B1QIR(B
photocatalytic membrane
Formic acid
water treatment
4-a270
13:20$B!A(B 15:20YE313FAU$B7?$*$h$S(BCHA$B7?%<%*%i%$%HKl$K$h$kFs;@2=C:AGJ,N%$NHf3S8!F$(B
($B1'ET5\Bg1!9)(B) ($B3X(B)$B!{9bNS(B $BPRN<(B$B!&(B ($B@5(B)$B:4F#(B $B9d;K(B$B!&(B ($B;:Am8&ElKL(B) ($B@5(B)$BD9C+@n(B $BBY5W(B$B!&(B ($B1'ET5\Bg1!9)(B) ($B@5(B)$B0KF#(B $BD>
zeolite membrane
carbon dioxide separation
molecular sieving
4-a64
13:20$B!A(B 15:20YE314$B0[Aj7O3&LL$r!V>l!W$H$9$kL56K@-;i
($B:eBg1!4p9)(B) ($B3X(B)$B!{8^Eg(B $BOB9,(B$B!&(B ($B@5(B)$B?{(B $B7C;L(B$B!&(B ($B@5(B)$B2,K\(B $B9T9-(B$B!&(B ($B@5(B)$BGO1[(B $BBg(B
Membranome
Squalene
Monoepoxidation
4-f800
13:20$B!A(B 15:20YE315$B9b0505:q$K$h$kM-5!@-1xE%$NC&?eFC@-$H?;F)05$N4X78(B
($B2#9qBg1!9)(B) ($B3X(B)$B!{@DLZ(B $B0l??(B$B!&(B ($B@5(B)$BCfB<(B $B0lJf(B
Dewatering
organic sludge
high pressure expression
4-b870
13:20$B!A(B 15:20YE316$BB?9&
($BET>k9b@l(B) ($B3X(B)$B!{;{ED(B $BBs??(B$B!&(B ($B@5(B)$B4d7'(B $BH~F`;R(B$B!&(B ($B%a%?%k%F%/%N(B) $BT"I\(B $BIRB'(B$B!&(B ($BD92,5;Bg(B) $BNkLZ(B $BC#Li(B
adsorption
porous ceramics
nuclear residue
4-e419
13:20$B!A(B 15:20YE317Preparation of antifouling PVDF membrane by using a fluorinated amphiphilic copolymer via non-solvent induced phase separation (NIPS) method
(Kobe U.) ($B3X(B)$B!{(BSun Yuchen$B!&(B ($B3X(B)Zhou Zhuang$B!&(B ($B3$(B)Rajabzadeh Saeid$B!&(B ($B@5(B)Kakihana Yuriko$B!&(B (Daikin industries, LTD) ($BK!(B)Ohmukai Yoshikage$B!&(B ($BK!(B)Miki Jun$B!&(B (Kobe U.) ($B@5(B)Matsuyama Hideto
Amphiphilic copolymer
Antifouling membrane
Poly (vinylidene fluoride)
4-a694
13:20$B!A(B 15:20YE318$B%U%C2=J*E:2C$K$h$k9b?eAGF)2a%<%*%i%$%HKl$N2~NI(B
($B$B!&(B $BBg1:(B $B6W2;(B$B!&(B ($B3X(B)$BCSED(B $BJb(B$B!&(B ($B3X(B)$B>.Ln(B $BN5J?(B$B!&(B ($B3X(B)$B>>;3(B $B3(H~(B$B!&(B ($B=;M'EE9)(B) $B:XF#(B $B?r9-(B$B!&(B $BI6;3(B $BGn6)(B$B!&(B $B7,86(B $B0lLi(B$B!&(B ($B
MFI zeolite membrane
porous silica substrate
NaF
4-a474
13:20$B!A(B 15:20YE319FAU$B7?%<%*%i%$%HKl$N(BC3$BC:2=?eAG5[CeFC@-$N8!F$(B
($BAaBg@h?JM}9)(B) ($B3X(B)$B$B!&(B ($B3X(B)$B!{:4!9LZ(B $B9/?M(B$B!&(B ($B3X(B)$BHSEg(B $BM%5.(B$B!&(B ($BAaBg@h?JM}9)(B/$BAaBgM}9)Am8&(B/JST-CREST) ($B@5(B)$B>>J}(B $B@5I'(B
FAU-type membrane
adsorption properties
propylene
4-a591
13:20$B!A(B 15:20YE320Pore-plugging$BK!$K$h$j@=Kl$7$?(BMFI$B7?%<%*%i%$%HKl$NF)2aJ,N%@-G=(B
($B;38}Bg1!M}9)(B) ($B3X(B)$B!{;32<(B $BM5B@(B$B!&(B $Bn9(B 灵$BK'(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 $B1QIR(B$B!&(B (Zaragoza U.) Cacho Fernando$B!&(B Sorribas Sara$B!&(B Tellez Carlos$B!&(B Coronas Joaquin
zeolite
membrane
gas separation
4-a271
13:20$B!A(B 15:20YE321$BJQ@-$r@8$8$J$$KlFb:_@-%?%s%Q%/
($B:eBg1!4p9)(B) ($B3X(B)$B!{DTK\(B $BM*N<(B$B!&(B ($B@5(B)$B2,K\(B $B9T9-(B$B!&(B ($B@5(B)$B?{(B $B7C;L(B$B!&(B ($B@5(B)$BGO1[(B $BBg(B
Intrinsic Membrane Proteins
Electrophoretic Separation
Membranome
4-i791
13:20$B!A(B 15:20YE322$BA*BrE*%;%7%&%`5[CeG=$rM-$9$k5!G=2=IT?%I[Kl$NAO@=(B
($BL>Bg9)(B) ($B3X(B)$B!{?eLn(B $BJ8:Z(B$B!&(B ($B@5(B)$B8~0f(B $B9/?M(B
functionalized membrane
cesium removal
nanofiber nonwoven cloth
4-a849
13:20$B!A(B 15:20YE323$B?e>x5$A*BrF)2a:Y9&%U%#%j%s%0Kl$N3+H/(B
($BEl9)Bg;q8;8&(B) ($B3X(B)$B!{1|ED(B $BN6B@O/(B$B!&(B ($B@5(B)$BBg66(B $B=(Gl(B$B!&(B (KAST/$BEl9)Bg;q8;8&(B) ($B@5(B)$B9uLZ(B $B=(5-(B$B!&(B ($BEl9)Bg;q8;8&(B/KAST) ($B@5(B)$B;38}(B $BLT1{(B
Latent heat recovery
Pore-filling membrane
Water vapor / CO2 permselectivity
4-a640
13:20$B!A(B 15:20YE324$B4%<0C&N2%U%#%k%?!<$K$*$1$kGS%,%9AH@.3F
($B6bBtBg1!<+A3(B) ($B3X(B)$B!{I4!9(B $B912p(B$B!&(B ($B6bBtBgM}9)(B) ($B@5(B)$BBg:d(B $BPR8c(B$B!&(B ($B@5(B)$BDT8}(B $BBsLi(B$B!&(B ($B@5(B)$B;y6L(B $B>
Dry DeSOx filter
MnO2
Water vapor
4-d660
13:20$B!A(B 15:20YE325Analysis of mass transfer resistance in liquid phase on supercritical carbon dioxide drying
($BEl9)Bg9)(B) ($B3X(B)$B!{(BKunanusont Nattanai$B!&(B ($BEl9)Bg1!M}9)(B) ($B3X(B)$BLZ2<(B $B85Bg(B$B!&(B ($B@5(B)$B2<;3(B $BM52p(B
supercritical drying
mass transfer resistance
dimensionless number
1-a217
13:20$B!A(B 15:20YE326$B=E
($BElKLBg1!9)(B) ($B3X(B)$B!{Ip@n(B $BM/0l(B$B!&(B ($BElKLBg9)(B) ($B3X(B)$BDTB<(B $B>-(B$B!&(B ($BElKLBg1!9)(B) ($B@5(B)$B5WJ](B $B@5$B!&(B ($BIY;38)Bg9)(B) ($B@5(B)$B?y2,(B $B7r0l(B$B!&(B ($BElKLBg1!9)(B) ($B@5(B)$BDMED(B $BN4IW(B$B!&(B (JPEC) ($B@5(B)$B;{C+(B $B>48g(B
surface tension
heavy oil
distillate fraction
1-a339
13:20$B!A(B 15:20YE327$BCj=P>xN1$NMO:^$H$7$F%$%*%s1UBN(B[HMIM][TFSI]$B$rMQ$$$k$?$a$N$=$NMO:^8z2L$NB,Dj$H?d;;!>?];@%(%A%k(B + $B%(%?%N!<%k$rBP>]$H$7$F!>(B
($BF|BgM}9)(B) ($B3X(B)$B!{@>86(B $B7$B!&(B ($B3X(B)$B3QED(B $BGnJ8(B$B!&(B ($B@5(B)$B>>ED(B $B909,(B$B!&(B ($B@5(B)$B7*86(B $B@6J8(B$B!&(B ($B@5(B)$BFJLZ(B $B>!8J(B
vapor-liquid equilibrium
azeotropic mixture
extractive distillation
1-a702
13:20$B!A(B 15:20YE328$B%j%A%&%`%$%*%sEECSMQEE6K3hJ*
($B6bBtBg1!<+(B) ($B3X(B)$B!{C#@n(B $B1Q<#(B$B!&(B ($B3X(B)$BCSED(B $BCR=((B$B!&(B ($B6bBtBg1!M}9)(B) ($B@5(B)$BEDB<(B $BOB90(B
Lithium-ion battery
Equilibrium potential
Chemical diffusivity
1-a817
13:20$B!A(B 15:20YE329$B%(%A%k%"%/%j%l!<%H(B(EA)$BAH@.$,%a%A%k%a%?%/%j%l!<%H(B(MMA)/EA$B6&=E9gBN$N%(%A%l%sMO2rEY$*$h$S3H;678?t$KM?$($k1F6A(B
($BElKLBg1!9)(B) ($B3X(B)$B!{9S(B $BCRGn(B$B!&(B ($B@5(B)$B:4F#(B $BA1G7(B$B!&(B ($B@5(B)$BCv8T(B $B9((B$B!&(B ($BF|N)2=@.(B) $B;3K\(B $BN<0l(B$B!&(B $BGH9>Ln(B $B<"(B$B!&(B $B>eLL(B $B2m5A(B
Solubility
Diffusivity
Free volume theory
1-a868
13:20$B!A(B 15:20YE330Hansen$BMO2rEY%Q%i%a!<%?$rMQ$$$F;;=P$7$?3hNL78?t$N:.9gMOG^$KBP$9$k;@AGMO2rEY$X$NE,MQ(B
($B4X@>Bg4DET9)(B) ($B3X(B)$B!{:4F#(B $BN4;V(B$B!&(B ($B@5(B)$B9SLZ(B $BDgIW(B$B!&(B ($B@5(B)$B;3K\(B $B=(
Gas solubility
Hansen solubility parameter
Activity coefficient
1-a91
13:20$B!A(B 15:20YE331$B6&J(:.9gJ*$G$"$k?];@%a%A%k(B+$B%a%?%N!<%k7O$KBP$9$kF};@%(%A%k$NMO:^8z2L$N8!F$(B
($BF|BgM}9)(B) ($B3X(B)$B!{0pMU(B $B9-<#(B$B!&(B ($B@5(B)$B7*86(B $B@6J8(B$B!&(B ($B@5(B)$B>>ED(B $B909,(B$B!&(B ($B@5(B)$BFJLZ(B $B>!8J(B
vapor liquid equilibrium
extractive distillation
solvent effect
1-a647
13:20$B!A(B 15:20YE332$B
($B4X@>Bg4DET9)(B) ($B3X(B)$B!{KY>l(B $B=S9((B$B!&(B ($B3X(B)$B:4F#(B $BN4;V(B$B!&(B ($B@5(B)$B9SLZ(B $BDgIW(B$B!&(B ($B@5(B)$B;3K\(B $B=(
physical properties
Hansen solubility parameter
Calculation
1-e121
13:20$B!A(B 15:20YE333$BCf6u;eKl%b%8%e!<%k$rMQ$$$?(BPRO$BH/EE%7%9%F%`$N@5L#H/EE=PNO$H1?E>>r7o$H$N4X78(B
($B;38}Bg1!M}9)(B) $B@t@n(B $B?52p(B$B!&(B ($B3X(B)$B=BC+(B $B??;K(B$B!&(B $BCSJU(B $BM:5.(B$B!&(B $BKY9>(B $BN5fF(B$B!&(B ($B@5(B)$B!{Hf2E(B $B=<(B
Pressure retarded osmosis
Hollow fiber membrane module
Operating condition
4-a512
$B9V1iH/I=%W%m%0%i%`(B
$B2=3X9)3X2q(B $BBh(B80$BG/2q(B
(C) 2015 $B8x1W
Most recent update: 2015-03-05 09:42:37
For more information contact $B2=3X9)3X2q;vL36I(B $BBh(B80$BG/2q(B $BLd$$9g$;78(B
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