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Hydrogen separation4$B7o(B*
adsorption4$B7o(B*
Membrane3$B7o(B*
zeolite3$B7o(B*
ionic liquid3$B7o(B*
Gold3$B7o(B*
gas separation3$B7o(B*
membrane separation3$B7o(B*
Biodiesel3$B7o(B*
Separation3$B7o(B*
Phase equilibrium3$B7o(B*
ettringite2$B7o(B

$B$BHV9f(B$B9V1iBjL\!?H/I=$B%-!<%o!<%I(B$BH/I=7A<0(B
9Energy saving in an azeotropic distillation column with a side stripper for acetic acid concentration
(Dong-A U.) ($B@5(B)Kim Young Han		Energy saving
Azeotropic distillation
Acetic acid production
P
26HI$BJ,N%MQ%7%j%+J#9gKl$N%b%8%e!<%k2=(B
($B$B!&(B ($B$B!&(B ($B$B!&(B ($B@5(B)$BLnB<(B $B4490(B		CVD
silica membrane
hydrogen separation
P
27$BJ|
($B$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 ($BNL8&5!9=(B) $B_7ED(B $B??0l(B$B!&(B $BH,4,(B $BE0Li(B$B!&(B ($B86;RNO5!9=(B) $B5WJ](B $B??<#(B$B!&(B $BEDCf(B $B?-9,(B		Hydrogen production
cation exchange membrane
Durability
P
79$B8:05BPN.EAG.4%AgK!$K$h$kE`7k:`NA$N4%AgFC@-$K5Z$\$9A`:n>r7o$N1F6A(B
($B@EBg1!9)(B) ($B3X(B)$B!{J!ED(B $BD>51(B$B!&(B ($B@5(B)$BN)85(B $BM:<#(B$B!&(B ($B?)IJ5!3#3+H/(B) ($B@5(B)$B$B!&(B ($B981I;:6H(B) ($B@5(B)$B@u0f(B $B?.5A(B$B!&(B $B:4F#(B $B0lI'(B$B!&(B ($BCfB<@5=)5;=Q;vL3=j(B) ($B@5(B)$BCfB<(B $B@5=)(B$B!&(B ($B?9>>9)6H(B) ($B@5(B)$B:dEl(B $BK'9T(B		Drying
Convective heat transfer
Freeze drying
P
81$BHnNA@=B$9)Dx$+$iGS=P$5$l$k%j%s;@7OGQ1U$+$i$N%j%s;@$N:F@8(B
($B4X@>Bg4DET9)(B) ($B3X(B)$B!{@>8}(B $B98;J(B$B!&(B ($B@5(B)$B;3K\(B $B=(		phosphoric acid
waste
lime hydrate
P
86$B;THN$N5e>u%7%j%+HyN3;R$rCf4VAX$H$7$FF3F~$7$?B?9&
($BFAEgBg1!@hC<(B) ($B3X(B)$B!{?y1:(B $B8w(B$B!&(B ($BFAEgBg1!$B!&(B ($B@5(B)$B?y;3(B $BLP(B		thin palladium membrane
porous stainless-steel tube
commercial spherical silica particle
P
161$B%$%*%s1UBN4^?;%P%/%F%j%"%;%k%m!<%9Kl$rMQ$$$?;i4D<02=9gJ*$NA*BrE*F)2a(B
($BF1;VO?M(B$B!&(B ($B@5(B)$B>>K\(B $BF;L@(B		Liquid membrane
Ionic liquid
Bacterial cellulose
P
219$B%"%_%s=$>~%^%0%M%?%$%H%J%NN.BN$N(BCO2$B5[<}5sF0(B
($BF`NI@hC0Li(B$B!&(B (RITE) ($B@5(B)$B8eF#(B $BOBLi(B$B!&(B ($B@5(B)$BM>8l(B $B9nB'(B		chemical absorption
carbon dioxide capture
nanoparticles
P
221CHA$B7?%T%e%"%7%j%+%<%*%i%$%H$N%W%m%T%l%s(B/$B%W%m%Q%sJ,N%FC@-(B
($BF`NI@hC$B!&(B (RITE) ($B@5(B)$BMhED(B $B9/;J(B$B!&(B ($B@5(B)$BM>8l(B $B9nB'(B		Pure Silica Zeolite
CHA-type
Propylene Separation
P
245$B1v;@7O$K$*$1$k(BAu(III)$BCj=P:^$H$7$F$N%7%/%m%Z%s%A%k%a%A%k%(!<%F%k$NJ*@-I>2A(B
($B5\:jBg9)(B) ($B3X(B)$B!{>.;3(B $B5.@8(B$B!&(B ($B@5(B)$BBgEg(B $BC#Li(B$B!&(B ($B@5(B)$BGO>l(B $BM3@.(B$B!&(B ($BF|K\%<%*%s(B) ($BK!(B)$BBgDP(B $B5-Lw(B		Cyclopentyl methyl ether
Extractant
Gold
P
248$B%$%*%s8r49A!0]$rMQ$$$?$a$C$-%9%i%C%8$+$i$N(BNi$B5Z$S(BSn$B$NJ,N%2s<}(B
($BF`NI9b@lJ*$B!&(B ($B@5(B)$BNS(B $B7$B!&(B ($B@5(B)$BCfB<(B $B=(H~(B		Metal separation
Ion exchange
Plating sludge
P
297$B8GBNI=LL$KIUCe$7$?L}@v>t$K5Z$\$96u5$%U%!%$%s%P%V%k$N1F6A(B
($BL>Bg1!9)(B) ($B3X(B)$B!{B<>>(B $B0j9a(B$B!&(B ($B@5(B)$B0BED(B $B7<;J(B		finebubble
air
oil washing
P
313$B;iKC;@%a%A%k%(%9%F%k:.9gJ*$NE:2CJ*%&%#%s%?%j%u$KBP$9$kE:2CJ*$NJ,;R9=B$$K$h$k1F6A(B
($B?73cBg<+(B) ($B3X(B)$B!{0$It(B $B2m90(B$B!&(B ($B@5(B)$B>.>>(B $BGn9,(B$B!&(B ($B@5(B)$B;3:](B $BOBL@(B$B!&(B ($B@5(B)$BB?Eg(B $B=(CK(B		Biodiesel
Additive
Winterization
P
314$BDc05%O%$%I%l!<%H2=Fs;@2=C:AG2s<}K!3NN)$K8~$1$?J,N%@-G=I>2A(B
($B?73cBg<+(B) ($B3X(B)$B!{4];3(B $B7rB@(B$B!&(B ($B3X(B)$B>.NS(B $BM&?M(B$B!&(B ($B@5(B)$B>.>>(B $BGn9,(B$B!&(B ($B@5(B)$B;3:](B $BOBL@(B$B!&(B ($B@5(B)$BB?Eg(B $B=(CK(B		carbon dioxide
semiclathrate hydrate
phase equilibrium
P
317$B3h@-C:I=LL$N2=3X=$>~$K$h$k9b5!G=@-5[Ce:^$N3+H/$H?e4D6->t2=$X$N1~MQ(B
($B5\:jBg9)(B) ($B3X(B)$B!{$B!&(B ($B@5(B)$BBgEg(B $BC#Li(B$B!&(B ($B@5(B)$BGO>l(B $BM3@.(B		adsorbent
activated carbon
water purification
P
355$B5?;w(BBDF$B$G$N%&%#%s%?%j%
($B?73cBg<+(B) ($B3X(B)$B!{CfB<(B $BN<2p(B$B!&(B ($B3X(B)$B0$It(B $B2m90(B$B!&(B ($B@5(B)$B>.>>(B $BGn9,(B$B!&(B ($B@5(B)$B;3:](B $BOBL@(B$B!&(B ($B@5(B)$BB?Eg(B $B=(CK(B		Biodiesel
Additive
Winterization
P
360$B%O%$%I%l!<%H@8@.Cf$NJ*
($B?73cBg<+(B) ($B3X(B)$B!{>>K\(B $BM%EM(B$B!&(B ($B@5(B)$B>.>>(B $BGn9,(B$B!&(B ($B@5(B)$B;3:](B $BOBL@(B$B!&(B ($B@5(B)$BB?Eg(B $B=(CK(B		Hydrate
Mass transfer
Gas separation
P
372$BIbNOGiNLK!$K$h$kB.EYJ?6Q7B$K$*$h$\$9N37BJ,I[$N1F6A(B
($B<$B!&(B $BEgDE(B $B>;8w(B$B!&(B ($B@5(B)$BBgJ?(B $BM&0l(B$B!&(B ($BFQ>.KR9b@l(B) ($B@5(B)$BJ?Ln(B $BGn?M(B		Particle size
Suspension
Buoyancy weighing-bar method
P
374$B
($B?73cBg<+(B) ($B3X(B)$B!{5FCO(B $B0*(B$B!&(B ($B@5(B)$B>.>>(B $BGn9,(B$B!&(B ($B@5(B)$B;3:](B $BOBL@(B$B!&(B ($B@5(B)$BB?Eg(B $B=(CK(B		Desorption
Cesium
Clinoptilolite
P
380Ionic liquid-based gel membrane for volatile organic compounds separation
(Kobe U./MaF Tech. C.) ($B3X(B)$B!{(BRanjbaran Fatemeh$B!&(B ($B@5(B)Kamio Eiji$B!&(B ($B3X(B)Yasui Tomoki$B!&(B Minami Reiko$B!&(B ($B@5(B)Matsuyama Hideto		Gas separation membrane
Ionic liquid
VOC
P
384Relating osmotic performance and pressure resistance of thin-film composite membranes to the properties of reinforcing non-woven fabrics
(Kobe U.) ($B3X(B)$B!{(BSun Yuchen$B!&(B ($B@5(B)Fang Lifeng$B!&(B ($B@5(B)Cheng Liang$B!&(B ($B@5(B)Shintani Takuji$B!&(B ($B@5(B)Nakagawa Keizo$B!&(B ($B@5(B)Matsuyama Hideto		pressure retarded osmosis
thin-film composite membrane
aliphatic polyketone
P
418Water Removal of W/O Model Emulsions of Microalgae Bio-crude Oil using Electrostatic Demulsification
(U. Tsukuba) ($B3$(B)$B!{(BRamadhan Muhammad Gilang$B!&(B (UMT) Khalid Nauman$B!&(B (U. Tsukuba) ($B@5(B)Nakajima Mitsutoshi		model emulsions
microalgae bio-crude
electrostatic demulsification
P
436Liquefaction of Sugarcane Bagasse Components for Value Addition
(U. Tsukuba) ($B3X(B)$B!{(BVodo Sekove$B!&(B ($B@5(B)Neves Marcos$B!&(B ($B@5(B)Kobayashi Isao$B!&(B Uemura Kunihiko$B!&(B ($B@5(B)Nakajima Mitsutoshi		bagasse
hydrothermal liquefaction
sugars
P
445$B5$K"Ec7?AuCV$K$*$1$k(BTBAB$B%;%_%/%i%9%l!<%H%O%$%I%l!<%H%9%i%j!<$N(BCO2$B5[<}5sF0(B
($B?73cBg<+(B) ($B3X(B)$B!{EOn5(B $BH;Je(B$B!&(B ($B@5(B)$BB?Eg(B $B=(CK(B$B!&(B ($B@5(B)$B;3:](B $BOBL@(B$B!&(B ($B@5(B)$B>.>>(B $BGn9,(B		Semi-clathrate Hydrate
Gas Absorption
Gas Separation
P
462$B9bJ,;R6E=8:^$K$h$k%3%m%$%I7|By1U$N@6@!2=(B
($B:eI\Bg1!9)(B) ($B3X(B)$B!{@1Ln(B $B@.I'(B$B!&(B ($B@5(B)$B4d:j(B $BCR9((B$B!&(B ($B@5(B)$B4dED(B $B@/;J(B		Flocculation
Stepwise dose
Polymer flocculant
P
491$B<'@-%a%=%]!<%i%9;@2=E4$N9g@.>r7o$N8!F$5Z$S@wNA5[Ce@-G=$NI>2A(B
($B=)Bg1!M}9)(B) ($B3X(B)$B!{0BLn(B $B7CM}(B$B!&(B ($B=)BgM}9)(B) $B?{86(B $BNJM4(B$B!&(B ($B=)Bg1!M}9)(B) ($B@5(B)$BCfB<(B $B:LG5(B$B!&(B ($B@5(B)$BB<>e(B $B8-<#(B		Mesoporous iron oxide
Ferromagnetism
adsorption
P
496$BN22+86;R$HCbAG86;R$rG[0L;R$H$9$k(B2$B:B9bJ,;R7?Cj=P:^$N?75,9g@.$H6b(B(III)$B$NCj=PJ?9U(B
($BET>k9b@l(B) ($B3X(B)$B!{2VED(B $BN4J8(B$B!&(B ($B@5(B)$B4d7'(B $BH~F`;R(B$B!&(B ($B5\:jBg9)(B) ($B@5(B)$BGO>l(B $BM3@.(B		Solvent extraction
Gold(III)
Polymer type extractant
P
505Mixed Matrix Membrane$B$N:n@=$HF)2aJ*@-$K4X$9$k8&5f(B
($B;38}Bg1!(B) ($B3X(B)$B!{AjED(B $B>M0l(B$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 ($B1'It9b@l(B) $BC+@n(B $BJ8:Z(B$B!&(B $B;3yu(B $BGn?M(B		Mixed Matrix Membrane
gas separation
MOF
P
523$B%"%/%j%l!<%H(B/$B%a%?%/%j%l!<%HAG:`$N2q9g>uBV$KCeL\$7$?Kl%U%!%&%j%s%05sF0$NM}O@2r@O(B
($BL>9)Bg(B) ($B3X(B)$B!{@6?e(B $B=_;K(B$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 $B=(		fouling
membrane separation
molecular dynamics
P
544$B4629@-%]%j%^!<(B/$B%^%0%M%?%$%H%J%NN3;RJ#9g:`$ND4@=$H=E6bB0%$%*%s2s<}$X$N1~MQ(B
($BAO2ABg1!9)(B) ($B3X(B)$B!{$B!&(B ($BAO2ABgM}9)(B) ($B@5(B)$B0fED(B $B=\0l(B$B!&(B ($B@5(B)$B>>;3(B $BC#(B		thermoresponsive polymer
magnetite nanoparticle
heavy metal ions
P
559$B%J%N%;%i%_%C%/Kl$rMQ$$$??eMO@-@v>t:^$NC&?e:F@8%7%9%F%`$N3+H/(B
($BF`NI9b@lJ*$B!&(B ($B%"%/%"2=3X(B) $BCgLn(B $B??0l(B$B!&(B ($BF`NI9b@lJ*$B!&(B ($B@5(B)$BCfB<(B $B=(H~(B		Nanoceramic membrane
Dehydration
Water-soluble detergent
P
575$B8GBNM;2r$K$h$k5?;w(BBDF$BJ,N%@:@=$N$?$a$NNd5Q>r7o$N8!F$(B
($B?73cBg<+(B) ($B3X(B)$B!{;3K\(B $B7<2p(B$B!&(B ($B3X(B)$B0$It(B $B2m90(B$B!&(B ($B@5(B)$B>.>>(B $BGn9,(B$B!&(B ($B@5(B)$B;3:](B $BOBL@(B$B!&(B ($B@5(B)$BB?Eg(B $B=(CK(B		Biodiesel
Sweating
Cooling conditions
P
592$B3F
($B1'ET5\Bg(B) ($B3X(B)$B!{W"@%(B $BBsLi(B$B!&(B $B5FCS(B $BM*J?(B$B!&(B ($B@5(B)$B:4F#(B $B9d;K(B$B!&(B ($B@5(B)$B0KF#(B $BD>$B!&(B ($B;:Am8&(B) ($B@5(B)$BD9C+@n(B $BBY5W(B		dehydration
alcohol solution
zeolite membrane
P
593$B%7%j%+%i%$%HKl$K$h$k%-%7%l%s:.9gJ*$+$i$N(Bp-$B%-%7%l%sJ,N%;n83$H4pACE*2r@O(B
($B1'ET5\Bg(B) ($B3X(B)$B!{F#0f(B $BOB5.(B$B!&(B $B9bLZOB(B $BD>51(B$B!&(B ($B@5(B)$B:4F#(B $B9d;K(B$B!&(B ($B@5(B)$B0KF#(B $BD>		Xylene separation
Silicalite-1 membrane
p-xylene
P
598FAU$B7?%<%*%i%$%HKl$N7A@.$*$h$S@-G=$KM?$($k=$NJ4:U$N1F6A(B
($B;38}Bg1!(B) ($B3X(B)$B!{:41RED(B $BBsLi(B$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 $B1QIR(B		zeolite
membrane
pervaporation
P
612$B%(%H%j%s%,%$%H6/2=(BPAdeCS$B$N@8@.$H$=$NGS?eCf1"%$%*%s=|5nG=$NI>2A(B
($B@.l~Bg1!M}9)(B) ($B3X(B)$B!{@6?e(B $BMc(B$B!&(B ($B@.l~Bg(B) $BLn8}(B $BH~M35.(B$B!&(B ($B@5(B)$B>1;J(B $B?N(B$B!&(B ($B@5(B)$B;3:j(B $B>O90(B$B!&(B ($BElKLBgB?858&(B) ($B@5(B)$BHSDM(B $B=_(B$B!&(B ($BF|K\%3%s%/%j!<%H9)6H(B) ($B@5(B)$B:4!9LZ(B $BLT(B$B!&(B $B5HED(B $B9@G7(B		Anion
Ettringite
Removal
P
613$B%P%$%]!<%iKlEE5$F)@OK!$rMQ$$$?%[%&AGGS?e=hM}!A6&B8%$%*%sB8:_2<$G$N%[%&AG$NA*BrE*$JJ,N%
($B@.l~Bg1!M}(B) ($B3X(B)$B!{CfB<(B $BM-N$:Z(B$B!&(B ($B@.l~Bg(B) ($B@5(B)$B;3:j(B $B>O90(B$B!&(B $BLn8}(B $BH~M35.(B$B!&(B ($B@5(B)$B>1;J(B $B?N(B$B!&(B ($BElKLBgB?858&(B) ($B@5(B)$BHSDM(B $B=_(B		boron
separation
membrane
P
637$B=c(BSF6$B5Z$S(BSF6+N2$B:.9g%,%9%O%$%I%l!<%H$NAjJ?9UB,Dj$HM}O@E*7W;;(B
($B?73cBg<+(B) ($B3X(B)$B!{>.NS(B $BM&?M(B$B!&(B ($B3X(B)$B4];3(B $B7rB@(B$B!&(B ($B@5(B)$B>.>>(B $BGn9,(B$B!&(B ($B@5(B)$B;3:](B $BOBL@(B$B!&(B ($B@5(B)$BB?Eg(B $B=(CK(B		sulfur hexafluoride
clathrate hydrate
phase equilibrium
P
647$B%W%i%:%^;Y1g(BMnO2$B%U%#%k%?!<$rMQ$$$F$NF1;~C&N2C&>K$N4pAC8&5f(B
($B6bBtBg1!M}9)(B) ($B3X(B)$B!{4d0f(B $B7rB@O:(B$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 $B>		exhaust gas purification
MnO2
Plasma
P
675$B%Q%s9ZJl$rMQ$$$k3F
($B:eI\Bg1!9)(B) ($B3X(B)$B!{;3Ln(B $B@i2F(B$B!&(B $Bc7F#(B $BHO;0(B$B!&(B ($B@5(B)$BLnB<(B $B=SG7(B$B!&(B ($B@5(B)$B>.@>(B $B9/M5(B		biosorption
gold
yeast
P
685$B6d1v:.9g%$%*%s1UBNKl$K$h$k%*%l%U%#%s7OC:2=?eAG%,%9J,N%(B
($BEl9)BgJ*$B!&(B ($B@5(B)$B0KEl(B $B>O(B		ionic liquid
olefin gas
membrane separation
P
698High performance polyethersulfone/sulfonated polyethersulfone ultrafiltration membranes: Preparation and formation mechanism
(Kobe U./MaF Tech. C.) ($B3X(B)$B!{(BYang Hui-Yan$B!&(B ($B3$(B)Fang Li-Feng$B!&(B Cheng Liang$B!&(B (Nat. Taiwan U.) Wang Da-Ming$B!&(B (Kobe U./MaF Tech. C.) ($B@5(B)Matsuyama Hideto		sulfonated polyethersulfone (SPES)
molecular weight
blend membranes
P
706$BEE5$EAF3EYK!$K$h$k%;%_%/%i%9%l!<%H%O%$%I%l!<%H%9%i%j!<$NAjJ?9UB,Dj(B
($B?73cBg<+(B) ($B3X(B)$B!{4I(B $B?5B@O:(B$B!&(B ($B@5(B)$BB?Eg(B $B=(CK(B$B!&(B ($B@5(B)$B;3:](B $BOBL@(B$B!&(B ($B@5(B)$B>.>>(B $BGn9,(B		Solid fraction
Semi-clathrate hydrate slurry
Phase equilibrium
P
707$B%;%_%/%i%9%l!<%H%O%$%I%l!<%H%9%i%j!<$NJ,;6>uBV$KM?$($k(Bpolyvinyl alcohol$B$N1F6A(B
($B?73cBg<+(B) ($B3X(B)$B!{0$It(B $BCRBg(B$B!&(B ($B@5(B)$BB?Eg(B $B=(CK(B$B!&(B ($B@5(B)$B;3:](B $BOBL@(B$B!&(B ($B@5(B)$B>.>>(B $BGn9,(B		Semi-clathrate hydrate slurry
viscosity
dispersion states
P
708$B%W%j%3!<%H$m2a$K$*$1$k%U%!%$%s%P%V%kE:2C$K$h$k%W%j%3!<%HAX$N2~
($B:eI\Bg1!9)(B) ($B3X(B)$B!{$B!&(B ($B3X(B)$BAW(B $BI'=.(B$B!&(B ($B@5(B)$B4dED(B $B@/;J(B$B!&(B ($B;0?J@=:n=j(B) ($BK!(B)$B>.7*(B $B=(0lO:(B$B!&(B ($BK!(B)$BKL@n(B $BIYB'(B$B!&(B ($BK!(B)$BLx2<(B $B9,0l(B		Filtration
Fine Bubble
Pre-coat
P
713$B%K%*%V;@%J%N%7!<%H@QAX7?J,N%Kl$N%7!<%H%5%$%:$,5Z$\$9Kl@-G=$X$N1F6A(B
($B?@8MBg1!2J5;%$%N%Y(B/$B@hC$B!&(B ($B@5(B)$BCf@n(B $B7I;0(B$B!&(B ($B?@8MBg1!9)(B/$B@hC$B!&(B ($B?@8MBg1!2J5;%$%N%Y(B/$B@hC$B!&(B ($B@5(B)$B?7C+(B $BBn;J(B$B!&(B ($B?@8MBg1!9)(B/$B@hC$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B		layered nanosheet membrane
metal oxide
nanosheet size
P
717$B%<%*%i%$%HJ,;6%]%j%^!<%U%#%k%`$rMQ$$$??75,$J=EII[J}K!$K$h$k9b@-G=(BSilicalite-1$BKl$N9g@.(B
($B4tIlBg1!9)(B) ($B3X(B)$B!{>eLn(B $B63J?(B$B!&(B $BKY8}(B $B7k0J(B$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 ($B@5(B)$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 $BIpLn(B $BL@5A(B$B!&(B ($B4tIlBg@8L?%;(B) ($B@5(B)$B6a9>(B $BLwB'(B		silicalite-1 zeolite membrane
novel seeding method
separation
P
740Fe-Y$B<'@-HyN3;R$K$h$kM-32H>6bB0$N5[Ce=|5n(B
($B5\:jBg9)(B) ($B3X(B)$B!{>(B $B$"$`(B$B!&(B ($B@5(B)$BBg\F(B $B70(B$B!&(B ($B@5(B)$BBgEg(B $BC#Li(B$B!&(B ($B@5(B)$BGO>l(B $BM3@.(B		Adsorption
Arsenic
Binary oxide
P
747$BC:AGKl$N?eAGF)2aJ,N%@-$K5Z$\$96&B8?e>x5$$N1F6A(B
($B;38}Bg1!AO@.2J3X(B) ($B3X(B)$B!{$B!&(B ($B@5(B)$BEDCf(B $B0l9((B$B!&(B ($B@5(B)$B4nB?(B $B1QIR(B		carbon membranes
hydrogen separation
humidity
P
750$BG.J,2rC:AG=$>~$K$h$kC:AGKl$N(BH2/O2$BJ,N%@-G=$N8~>e(B
($B;38}Bg1!AO@.2J3X(B) ($B3X(B)$B!{@uLn(B $BBsLi(B$B!&(B ($B;38}Bg9)(B) $B5H_7(B $BE5??(B$B!&(B ($B;38}Bg1!AO@.2J3X(B) ($B@5(B)$BEDCf(B $B0l9((B$B!&(B ($B@5(B)$B4nB?(B $B1QIR(B		carbon membranes
hydrogen separation
P
777$B%"%k%_%I%m%9$r=PH/86NA$H$9$k%(%H%j%s%,%$%H$N9g@.$H1"%$%*%s=|5n:^$X$NE,MQ(B
($B4X@>Bg(B) ($B3X(B)$B!{NkLZ(B $BNC(B$B!&(B ($B@5(B)$B>>2,(B $B8w><(B$B!&(B ($B@5(B)$BB<;3(B $B7{90(B		aluminum dross
ettringite
anion removal agent
P
779$B@=9]%9%i%0M3Mh1"%$%*%s=|5n:^$rMQ$$$?M-321"%$%*%s$N=|5n%W%m%;%9$K$D$$$F(B
($B4X@>Bg(B) ($B3X(B)$B!{Bg>e(B $BM4EM(B$B!&(B ($B@5(B)$B>>2,(B $B8w><(B$B!&(B ($B@5(B)$BB<;3(B $B7{90(B		steelmaking slag
anion removal agent
layered double hydroxides
P
791$B%O%$%7%j%+%<%*%i%$%H$rMQ$$$?0l;@2=CbAG$N?(G^E*;@2=H?1~$N2r@O(B
($B:eI\Bg9)(B) ($B3X(B)$B!{Bg0B(B $B98(B$B!&(B ($B8x32KI;_5!4o8&(B) $B@uLn(B $B??(B$B!&(B ($B:eI\Bg9)(B) ($B3X(B)$B;3Cf(B $B=SLo(B$B!&(B ($B@5(B)$B2.Ln(B $BGn9/(B$B!&(B ($B@5(B)$B0BED(B $B>;90(B		nitrogen monoxide
zeolite
reaction kinetics
P
792$BN.$l>l$rMxMQ$7$?L)EY:9J,5i(B
($B:eI\Bg1!9)(B) ($B3X(B)$B!{M-5H(B $B`"J?(B$B!&(B ($B@5(B)$B4d:j(B $BCR9((B$B!&(B ($B@5(B)$B4dED(B $B@/;J(B		Classification
Density difference
Flow field
P
794$BCfDc29GQG.8;$rM-8zMxMQ$7$?%<%*%i%$%H$+$i$N9bG;EYCbAG;@2=J*$NC&Ce(B
($B:eI\Bg9)(B) ($B3X(B)$B!{Kv_7(B $BD>$B!&(B ($B3X(B)$BBg0B(B $B98(B$B!&(B ($B8x32KI;_5!4o8&(B) $B@uLn(B $B??(B$B!&(B ($B:eI\Bg9)(B) ($B@5(B)$B0BED(B $B>;90(B		Nitrogen Oxides
Thermal desorption
zeolite
P
795$B%*%k%,%N%2%k$NDj0505:q(B
($B:eI\Bg1!9)(B) ($B3X(B)$B!{;e0f(B $B>OB@O/(B$B!&(B ($B@5(B)$B4d:j(B $BCR9((B$B!&(B ($B@5(B)$B4dED(B $B@/;J(B		Organogel
Expression
Medium resistance
P
796$B%,%i%9A!0]%U%#%k%?!<<0%,%95[<}AuCV$rMQ$$$?N22+;@2=J*!&CbAG;@2=J*$N?e5[<}(B
($B:eI\Bg9)(B) ($B3X(B)$B!{9bED(B $BMc(B$B!&(B ($B3X(B)$BBg0B(B $B98(B$B!&(B ($B8x32KI;_5!4o8&(B) $B@uLn(B $B??(B$B!&(B ($B:eI\Bg9)(B) ($B@5(B)$B0BED(B $B>;90(B		Nitrogen oxides
Sulfur oxides
Water absorption
P
851$B%+!<%\%s%J%N%U%!%$%P!<5[CeKl$K$h$k?e>t2=$K4X$9$k4pAC8&5f(B
($BL>Bg9)(B) ($B3X(B)$B!{2+(B $BHf7/(B$B!&(B $BBg_7(B $B0l??(B$B!&(B ($B@5(B)$BF~_7(B $B$B!&(B ($B@5(B)$B8~0f(B $B9/?M(B		carbon nanofiber
adsorption
water purification
P
873$B%-%A%s$r86NA$H$7$?%]%j%*!<%k%-%H%5%sM6F3BN$N9g@.$H(BAs, Se$B$*$h$S(BSb$B$N5[CeFC@-(B
($B5\:jBg1!9)(B) ($B3X(B)$B!{0&9C(B $B>0@5(B$B!&(B ($B@5(B)$BBgEg(B $BC#Li(B$B!&(B ($B@5(B)$BGO>l(B $BM3@.(B$B!&(B ($B@5(B)$BBg\F(B $B70(B		Chitosan
adsorption
semi-metals
P
878$B%P%$%*%(%?%N!<%k4^M-%,%=%j%s$NKlJ,N%(B
($B@.l~Bg1!M}(B) ($B3X(B)$B!{>.Ln(B $BKc0a;R(B$B!&(B ($B@.l~Bg(B) ($B@5(B)$B;3:j(B $B>O90(B$B!&(B ($B@5(B)$B>1;J(B $B?N(B$B!&(B $BLn8}(B $BH~M35.(B		Membrane
Separation
Bioethanol
P
884$B9bJ,;RJq4^Kl$K$h$kFs
($B6eBg1!9)(B) ($B3X(B)$B!{2OLn(B $BN$Jf(B$B!&(B ($B3X(B)$B5HED(B $B9R(B$B!&(B ($B@5(B)$B5WJ]ED(B $BIY@8;R(B$B!&(B ($B@5(B)$B8eF#(B $B2m9((B		Polymer Inclusion Membrane
Gold
Recovery
P
937$B8w2M66%]%j%$%_%IGvKl$N:n@=$H%,%9F)2aJ,N%@-(B
($B;38}Bg1!AO@.2J3X(B) ($B3X(B)$B!{F|9b(B $B??8c(B$B!&(B ($B@5(B)$BEDCf(B $B0l9((B$B!&(B ($B@5(B)$B4nB?(B $B1QIR(B		Hydrogen separation
polyimide
photocrosslinking
P
1005$B%-%H%5%s(B-$B%"%k%.%s;@J#9gKl$ND4@=$HI>2A(B
($BElM}Bg(B) ($B3X(B)$B!{@PEg(B $BZo8h(B$B!&(B ($B@5(B)$BG;OB(B$B!&(B ($B@5(B)$BEhED(B $BM'0lO:(B$B!&(B ($B@5(B)$BBgC](B $B>!?M(B$B!&(B ($B@5(B)$B>1Ln(B $B8|(B		membrane separation
natural polymer
P
1013$B29EYAjE>0\J*
($B?@8MBg1!9)(B/$B@hC$B!&(B ($B@5(B)$B9b66(B $BCR51(B$B!&(B ($B@5(B)$B?@Hx(B $B1Q<#(B$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B		forward osmosis
reverse osmosis
phase transition materials
P
$B9V1i?=$79~$_0lMw(B($B%7%s%]%8%&%`HV9f!&9V1iJ,N`HV9fJL(B)
$B
$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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