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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
membrane3$B7o(B*
ionic liquid3$B7o(B*
carbon membrane3$B7o(B*
Reverse osmosis membrane2$B7o(B
Flocculation2$B7o(B
Recovery2$B7o(B
carbon dioxide2$B7o(B
Zeolite2$B7o(B
Polyamide2$B7o(B
composite membrane2$B7o(B
Gas separation2$B7o(B
Reactive distillation2$B7o(B
zeolite membrane2$B7o(B
Energy savings2$B7o(B
pervaporation2$B7o(B
draw solute2$B7o(B
Polymer Inclusion Membrane2$B7o(B
Process design2$B7o(B
MFI zeolite membrane2$B7o(B
forward osmosis2$B7o(B
hydrofluoric acid1$B7o(B

$B$BHV9f(B$B9V1iBjL\!?H/I=$B%-!<%o!<%I(B$BH/I=7A<0(B
117$B%7%j%+$H%"%k%_%J$NJ#AX2=$7$?Cf4VAX$rF3F~$7$?B?9&
($BFAEgBg1!@hC<(B) ($B3X(B)$B!{?y1:(B $B8w(B$B!&(B $B9A(B $BM&2p(B$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 $BLP(B		thin palladium membrane
porous stainless-steel tube
double intermediate layers
P
168$B?eAGF)2a%<%*%i%$%HKl$N@=KlJ}K!$N8!F$(B
($B$B!&(B $BGr0f(B $BKcN$Fa(B$B!&(B ($B3X(B)$BCSED(B $BJb(B$B!&(B ($B@5(B)$BLnB<(B $B4490(B$B!&(B ($B=;M'EE9)(B) $B1|Ln(B $BBsLi(B$B!&(B $B:XF#(B $B?r9-(B$B!&(B $BI6;3(B $BGn6)(B$B!&(B $B@P@n(B $B??Fs(B$B!&(B $B7,86(B $B0lLi(B		MFI zeolite membrane
porous silica substrate
organic hydrides
P
170$B%7%j%+J#9gKl$K$h$kC:2=?eAGJ,N%(B
($B$B!&(B $B@P0f(B $B9nE5(B$B!&(B $B$B!&(B ($B@5(B)$BLnB<(B $B4490(B		Silica based membrane
chemical vapor deposition
hydrocarbon separation
P
171$BF|K\
($B$B!&(B G. Figueiredo$B!&(B ($B3X(B)$BCSED(B $BJb(B$B!&(B ($B@5(B)$BLnB<(B $B4490(B		MFI zeolite membrane
Japanese SAKE
organic acid
P
188C3 splitter$B$rBP>]$H$7$?>xN1(B-$BKl%O%$%V%j%C%I%W%m%;%9$NA`:n!&@_7W>r7o$K4X$9$k8!F$(B
($B;37ABg1!M}9)(B) ($B3X(B)$B!{NkLZ(B $B7rB@(B$B!&(B ($B;:Am8&(B) ($B@5(B)$B;3LZ(B $BM:Bg(B$B!&(B ($B;37ABg1!M}9)(B) ($B@5(B)$B>>ED(B $B7=8g(B		Distillation
Hybrid process
Propylene separation
P
189$B9b@-G=5U?;F)Kl$N3+H/(B
($BEl%lCO5e4D6-8&(B) ($BK!(B)$B!{5\K\(B $BN5GO(B$B!&(B ($BK!(B)$B;VB<(B $B@25((B$B!&(B ($BK!(B)$B>.@n(B $B5.;K(B$B!&(B ($BK!(B)$B:4!9LZ(B $B?rIW(B$B!&(B ($BK!(B)$BLZB<(B $B>-90(B		reverse osmosis membrane
Inverse Gas Chromatograph
polyamide
P
255$B?e;:GQ4~J*$N;tNA2=$N$?$a$N%+%I%_%&%`=|5n5;=Q$N3+H/(B
($BKLBg1!?e(B) ($B3X(B)$B!{?y:j(B $BFF(B$B!&(B ($B@5(B)$B4X(B $B=(;J(B$B!&(B ($B@5(B)$B4];3(B $B1QCK(B		squid and scallop viscera
aquaculture feed
cadmium removal
P
270$BAjJ,N%7?5[<}1UCf$N(BCO2$BMOB87ABV$HJ?9UJ*@-$N8&5f(B
($BL>Bg1!9)(B) ($B3X(B)$B!{0BF#(B $BN5Li(B$B!&(B ($B@5(B)$B;38}(B $B5#(B$B!&(B $B9>:j(B $B>fM5(B$B!&(B ($B@5(B)$BKYE:(B $B9@=S(B$B!&(B ($B@5(B)$BD.ED(B $BMN(B		carbon dioxide
13C NMR
amine solution
P
322F$B%$%*%sB8:_2<$K?eG.9g@.$7$?%<%*%i%$%HKl$NF)2aJ*@-(B
($B;38}Bg1!M}(B) ($B3X(B)$B!{;3K\(B $BCR5.(B$B!&(B $B;3K\(B $BBvLi(B$B!&(B ($B@5(B)$B4nB?(B $B1QIR(B$B!&(B ($B@5(B)$B7'@Z(B $B@t(B$B!&(B ($B@5(B)$BEDCf(B $B0l9((B		zeolite membrane
pervaporation
fluoride
P
323$BE49]%9%i%0M3Mh1"%$%*%s=|5n:^$r=
($B4X@>Bg4DET9)(B) ($B3X(B)$B!{1|ED(B $BM%Li(B$B!&(B ($B@5(B)$BB<;3(B $B7{90(B$B!&(B ($B@5(B)$B		waste water treatment
layered double hydroxides
chromium
P
335$B%>%k%2%kK!$K$h$j:n@=$7$?uKl$N(BCO2$BJ,N%(B
($BElMN%4%`9)6HCf1{8&(B) ($BK!(B)$B!{D9C+@n(B $B42FF(B$B!&(B ($BK!(B)$B>.;3(B $B>$B!&(B ($BK!(B)$BEOn5(B $B8x9@(B$B!&(B ($B?@8MBg1!3$;v2J(B) $BB"2,(B $B9'<#(B		CO2 separation
silica membrane
sol-gel method
P
342$B6bB0%$%*%s2s<}$K8~$1$?BgD26]$NI=AX@_7WK!$N3+H/(B
($B6eBg1!9)(B) ($B3X(B)$B!{:Y\b(B $BPR5.Jf(B$B!&(B ($B@5(B)$B5WJ]ED(B $BIY@8;R(B$B!&(B ($B@5(B)$B$B!&(B ($B@5(B)$B?@C+(B $BE5Jf(B$B!&(B ($B@5(B)$B8eF#(B $B2m9((B		Escherichia coli
Biosorption
Modification
P
349$BM-5!J*$r4^$`1vMO1U$NE`7kG;=L8=>]$N8!F$(B
($B;37ABg1!M}9)(B) ($B3X(B)$B!{5FCO(B $BM&B@O/(B$B!&(B ($B@5(B)$B<58M(B $B>;9-(B		Freeze concentration
Salt solution
Dendrite
P
389$B?75,Cj=P:^$K$h$k7HBSEEOC?;=P1U$+$i$N5.6bB0$NJ,N%2s<}(B
($B6eBg1!9)(B) ($B3X(B)$B!{2OLn(B $BN$Jf(B$B!&(B ($B3X(B)$B5HED(B $B9R(B$B!&(B $B0zLn(B $B9,;^(B$B!&(B ($B@5(B)$B5WJ]ED(B $BIY@8;R(B$B!&(B ($B@5(B)$B?@C+(B $BE5Jf(B$B!&(B ($B@5(B)$B8eF#(B $B2m9((B		precious metals
solvent extraction
recovery
P
399$B%j%0%K%sA06nBN$X$NE4E:2C$,J,;R$U$k$$C:AGKl@-G=$KM?$($k1F6A(B
($B;38}Bg1!M}9)(B) ($B3X(B)$B!{EDB<(B $B63M4(B$B!&(B ($B@5(B)$B7'@Z(B $B@t(B$B!&(B ($B@5(B)$BEDCf(B $B0l9((B$B!&(B ($B;38}Bg1!M}(B) ($B@5(B)$B4nB?(B $B1QIR(B$B!&(B ($B;0=EBg1!(B) ($B@5(B)$BgU2,(B $B@58w(B		carbon membrane
gas separation
molecular sieve
P
456$B%$%*%s1UBN4^M-9bJ,;RKl$rMQ$$$?%U%'%K%k%"%i%K%s$NF)2a(B
($BF1;Ve(B $B7E(B$B!&(B ($B@5(B)$B>>K\(B $BF;L@(B$B!&(B ($B@5(B)$B6aF#(B $BOB@8(B		polymer inclusion membrane
Ionic liquid
Phenylalanine
P
494$B%(%?%N!<%k(B/$B1v7O?e@-(B2$BAj$K$h$k%3%O%/;@$NCj=P$H%(%9%F%k2=(B
($BF1;V$B!&(B ($B@5(B)$B>>K\(B $BF;L@(B$B!&(B ($B@5(B)$B6aF#(B $BOB@8(B		Aqueous two phase system
succinic acid
esterification
P
544$B?;F)05H/EE%W%m%;%9$K$*$1$kCf6u;eKl%b%8%e!<%k$NKl@-G=$*$h$S9=B$$N:GE,2=(B
($B?@8MBg1!9)(B/$B@hC$B!&(B ($B@5(B)$B0B@n(B $B@/9((B$B!&(B ($BElMNKB(B) $B9gED(B $B>;J?(B$B!&(B ($B?@8MBg1!9)(B/$B@hC$B!&(B ($B@5(B)$B9b66(B $BCR51(B$B!&(B ($B;38}Bg1!M}9)(B) ($B@5(B)$BHf2E(B $B=<(B$B!&(B ($B?@8MBg1!9)(B/$B@hC>;3(B $B=(?M(B		Pressure-retarded osmosis
Hollow fiber module
Module structure
P
545$BJ4KvE:2CK!$K$*$1$k9bJ,;R6E=8:^$N5[CeNL$ND4::(B
($B:eI\Bg1!9)(B) ($B3X(B)$B!{F#86(B $BNg;R(B$B!&(B ($B3X(B)$BNw2,(B $BM5?M(B$B!&(B ($B3X(B)$B5\Eg(B $B>"(B$B!&(B ($B:eEEDLBg9)(B) ($B@5(B)$BEDCf(B $B9'FA(B$B!&(B ($B:eI\Bg1!9)(B) ($B@5(B)$B4dED(B $B@/;J(B		Flocculation
Coagulation
Polyelectrolyte
P
561$BH?1~(B+$B>xN1J#9g%W%m%;%9$N9=B$$HJ,N%FC@-(B
($BL>9)Bg1!(B) ($B3X(B)$B!{?9(B $BJK3$(B$B!&(B ($B@5(B)$B4dED(B $B=$0l(B$B!&(B ($B@5(B)$BFn1@(B $BN<(B$B!&(B ($B@5(B)$B?9(B $B=(		Reactive distillation
Simulation
Separation characteristics
P
570Preparation of polyamide hollow fiber membranes via TIPS process
(Kobe U.) ($B3$(B)$B!{(BJeon Sungil$B!&(B Fukukawa Naruki$B!&(B ($B@5(B)Matsuyama Hideto$B!&(B (Unitika) ($B@5(B)Ono Takahiro$B!&(B ($B@5(B)Nakamura Ryota		Polyamide
Hollow fiber membrane
TIPS process
P
604$BLZ
($B;38}Bg1!(B) ($B3X(B)$B!{4_K\(B $BBsLi(B$B!&(B $B8E2l(B $BCR;R(B$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 ($B=)ED8)Bg(B) $B7*K\(B $B9/;J(B$B!&(B ($BKL8+9)Bg(B) $BNkLZ(B $BJY(B		Carbon membrane
Gas separation
Wood
P
611$BEZ>mN3;R$N6E=85sF0$K5Z$\$929EY1~Ez@-9bJ,;RE:2C$N1F6A(B
($B=)Bg1!M}9)(B) ($B@5(B)$B!{CfB<(B $B:LG5(B$B!&(B $B%0%'%s(B $B%H%%%$%,!<(B$B!&(B ($B;0OB%F%C%-(B) $BCfEg(B $B=U2p(B$B!&(B ($B=)Bg1!M}9)(B) ($B@5(B)$BB<>e(B $B8-<#(B		Temperature-responsive Polymer
Flocculation
Soil Particle
P
620$BCj=P>xN1$K$*$1$kAuCV9=B$$,=jMW%(%M%k%.!<5Z$S%3%9%H$KM?$($k1F6A$NI>2A(B
($BFAEgBg1!9)(B) ($B3X(B)$B!{2,ED(B $BBnLi(B$B!&(B($BFAEgBg1!M}9)(B) ($B3$(B)$B%"%k%+%s%?%i(B $B%"%S%i(B $B%X%9!<%9(B $B%i%U%!%(%k!&(B ($B@5(B)$B30NX(B $B7r0lO:(B$B!&(B ($B@5(B)$BKY2O(B $B=S1Q(B		Extractive distillation
Energy savings
Process Design
P
625$B%b%G%k%Y!<%9:GE,2=J}K!$K$h$kFbItG.8r497?>xN1Ec(B(HIDiC)$B$N@_7W(B
($BFAEgBg1!9)(B) ($B3X(B)$B!{EDCf(B $B@9Gn(B$B!&(B($BFAEgBg1!M}9)(B) ($B3$(B)$B%"%k%+%s%?%i(B $B%"%S%i(B $B%X%9!<%9(B $B%i%U%!%(%k!&(B ($B@5(B)$B30NX(B $B7r0lO:(B$B!&(B ($B@5(B)$BKY2O(B $B=S1Q(B		HIDiC
Energy savings
Process optimization
P
627Improved fouling and biofouling property of blend membranes using novel MPC copolymer
(Kobe U.) ($B3$(B)$B!{(BFang Lifeng$B!&(B ($B@5(B)Jeon Sungil$B!&(B ($B@5(B)Kakihana Yuriko$B!&(B ($B@5(B)Kakehi Jun-ichi$B!&(B ($B@5(B)Matsuyama Hideto		polyvinyl chloride (PVC)
fouling
biofouling
P
654$B@5?;F)Kl$rMQ$$$??e=hM}%W%m%;%9$X$NE,MQ$rL\;X$7$?%$%*%s1UBN7?6nF01U$N3+H/(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 $B=(?M(B		Ionic Liquid
Forward Osmosis
Draw Solution
P
665$B%7%j%+%i%$%HKl$N(Bi-$B%V%?%s!?(Bn-$B%V%?%sJ,N%@-G=$H2r@O(B
($B1'ET5\Bg(B) ($B3X(B)$B!{?{Ln(B $BM5Bg(B$B!&(B ($B3X(B)$B|bLZOB(B $BD>51(B$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)$B86C+(B $B8-<#(B		Silicalite membrane
butane isomer
Zeolite
P
681Development of tough gel membrane containing a CO2 reactive ionic liquid by casting method
(Kobe U.) ($B3$(B)$B!{(BMoghadam F.$B!&(B ($B@5(B)Kamio E.$B!&(B ($B@5(B)Matsuyama H.		Ion gel membrane
Task specific ionic liquids
CO2 capture
P
697$BAB?e@-%7%j%+Kl$rMQ$$$??eAG(B/$B%H%k%(%s:.9g%,%9J,N%%W%m%;%9$N3+H/(B
($B4X@>Bg(B) ($B3X(B)$B!{2,It(B $BM-L$(B$B!&(B ($B@5(B)$B9SLZ(B $BDgIW(B$B!&(B ($B@5(B)$B;3K\(B $B=(		Hydrophobic silica membrane
Hydrogen
Toluene
P
698$B2C?eJ,2rH?1~$K$h$k=[4D7?H?1~>xN1$rMQ$$$?F};@$N=cEY$KBP$9$k1F6A(B
($BFAEgBg1!9)(B) ($B3X(B)$B!{0BJ?(B $B2m(B$B!&(B ($B;:Am8&(B) ($B@5(B)$B;3LZ(B $BM:Bg(B$B!&(B($BFAEgBg1!M}9)(B) ($B@5(B)$B%"%k%+%s%?%i(B $B%"%S%i(B $B%X%9!<%9(B $B%i%U%!%(%k!&(B ($B@5(B)$B30NX(B $B7r0lO:(B$B!&(B ($B@5(B)$BKY2O(B $B=S1Q(B		Reactive distillation
Process design
Lactic acid production
P
701$B;@:F@8%W%i%s%H$K$*$1$k(BNaF$B=[4D%W%m%;%9$N3+H/(B
($B4X@>Bg(B) ($B3X(B)$B!{K-1`(B $B??Li(B$B!&(B ($B00@=:n=j(B) $BCSED(B $BLwG7(B$B!&(B ($B4X@>Bg(B) ($B@5(B)$B;3K\(B $B=(		hydrofluoric acid
sodium fluoride
acid regeneration
P
728Si-CHA$B7?%<%*%i%$%HKl$N:n@=$H%,%9J,N%$X$NE,MQ(B
(NAIST) ($B3X(B)$B!{5WLn(B $BB@0l(B$B!&(B ($B3X(B)$BA0ED(B $B9/;V(B$B!&(B (RITE) ($B@5(B)$BMhED(B $B9/;J(B$B!&(B ($B@5(B)$BM>8l(B $B9nB'(B		Zeolite
membrane
gas permeation
P
741$B4D6-G[N87?DcJ,;R%2%k2=:^$N=yJ|@-G@Lt$X$N1~MQ(B
($BKL6eBg1!9)(B) ($B3X(B)$B!{%$%s(B $B%;%$%;%$(B$B!&(B ($B@5(B)$B>e9>='(B $B0lLi(B		controlled release agent
gel
fatty acid
P
742$B@P847OK">C2P:^$N$?$a$NGQL}M3Mh;iKC;@%j%5%$%/%k%7%9%F%`(B
($BKL6eBg1!9)(B) ($B3X(B)$B!{9b:j(B $BNC;R(B$B!&(B ($B@5(B)$B>e9>='(B $B0lLi(B		long-chain saturated fatty acid
water hardness
foaming property
P
748$BM-5!4p4^M-%<%*%i%$%H$rMQ$$$?AB?e@-Kl$N3+H/(B
($B:eBg1!4p9)(B) ($B3X(B)$B!{@5LZ(B $B9/M:(B$B!&(B ($B@5(B)$BW"ED(B $BM:0lO/(B$B!&(B ($B@5(B)$B@>;3(B $B7{OB(B		zeolite membrane
hydrophobic membrane
pervaporation
P
765$B3Fx5$F)2a78?t(B
($BEl9)Bg1!M}9)(B) ($B3X(B)$B!{H+(B $BNJ1Q(B$B!&(B ($B3X(B)$B?@C+(B $BCR5,(B$B!&(B ($B@5(B)$B0KEl(B $B>O(B		gas and vapor permeation
liquid membrane
ionic liquid
P
768$B@8J*@\?($m2a2aDx$K$*$1$k%P%$%*%]%j%^!<$N5sF02r@O(B
($B?@8MBg@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?@8MBg@hC>;3(B $B=(?M(B		biological treatment
biopolymer
membrane
P
775$B<+8JG.:F@87?E`7k4%Ag%W%m%;%9$N3+H/(B
($BElBg1!9)(B) ($B3X(B)$B!{:dEl(B $B7rB@(B$B!&(B ($BElBg@8;:5;8&(B) ($B@5(B)$B4Eht(B $B$B!&(B ($B@5(B)$B@PB+(B $B??E5(B$B!&(B ($B@5(B)$BDi(B $BFX;J(B		freeze dry
energy saving
process engineering
P
794$BE|?eMO1U$N??6u4%Ag$K$*$1$k;DN1?eJ,$NAj8_:nMQ>uBV$HE|$N7k>=2=(B
($B2,;3Bg9)(B) ($B3X(B)$B!{CfLn(B $B9@Je(B$B!&(B $B2,ED(B $B??$B!&(B ($B@5(B)$B:#Cf(B $BMN9T(B$B!&(B ($B@5(B)$B@PED(B $B>0G7(B$B!&(B ($B@5(B)$B:#B<(B $B0]9n(B		hydration state
amorphous sugar
crystallization
P
802$BFZN.9T@-2
($BKL6eBg1!9)(B) ($B3X(B)$B!{EOn5(B $B;~Li(B$B!&(B ($B@5(B)$B>e9>='(B $B0lLi(B		polymer brush
Aminopeptidase N
Protein Data Bank
P
803$B%*%9%b%F%#%C%/%R!<%H%(%s%8%s$N?eF)2a@-$K5Z$\$91F6A0x;R$N2r@O(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
824$B0lJ}8~E`7k$rMxMQ$7$?J4Kv3h@-C:$N%O%K%+%`>u@.7A(B
($B5~Bg1!9)(B) ($B3X(B)$B!{5WJ]ED(B $B>-Lp(B$B!&(B ($B@5(B)$B:4Ln(B $B5*>4(B$B!&(B ($B@5(B)$BEDLg(B $BH%(B		unidirectional freezing
activated carbon
honeycomb
P
856$B
($B$B!&(B ($BL>Bg1!9)(B) ($B3X(B)$BC]Fb(B $B7<8g(B$B!&(B ($B$B!&(B ($B@5(B)$B?eED(B $B7I(B$B!&(B ($B@5(B)$BFs0f(B $B?8(B$B!&(B ($BL>Bg1!9)(B) ($B@5(B)$B8~0f(B $B9/?M(B$B!&(B ($B?9>>9)6H(B) ($B@5(B)$B:dEl(B $BK'9T(B		Packed bed
Coalescer
Emulsion
P
893$B%*%l%$%s;@(B/$B%b%N%*%l%$%s$rMQ$$$?(BCubosome$B$ND4@=$J$i$S$KM"AwC4BN$X$N1~MQ(B
($B:eBg1!4p9)(B) ($B3X(B)$B!{BgDM(B $BMU;R(B$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 $BBg(B		Membranome
cubosome
Membrane Property
P
919$B8w2M66%]%j%$%_%IJ#9gKl$N:n@=$H%,%9F)2aJ,N%@-G=(B
($B;38}Bg1!(B) ($B3X(B)$B!{F|9b(B $B??8c(B$B!&(B ($B3X(B)$BNS(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 $B1QIR(B		photocrosslinkable polyimide
membrane gas separation
composite membrane
P
922$B%]%j%$%_%IC:AGJ#9gKl$N:n@=>r7o$H?eAG%,%9F)2aJ,N%@-G=(B
($B;38}Bg1!(B) ($B3X(B)$B!{CfB<(B $BM*Je(B$B!&(B ($B3X(B)$B:dK\(B $B7rB@O:(B$B!&(B ($B;38}Bg(B) $B@uLn(B $BBsLi(B$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 $B1QIR(B		carbon membrane
polyimide
composite membrane
P
927p/m-$B%-%7%l%sJ,N%$N$?$a$N(BMFI$B7?%<%*%i%$%HKl$N@.KlK!$N8!F$(B
($B1'ET5\Bg(B) ($B3X(B)$B!{|bLZOB(B $BD>51(B$B!&(B ($B3X(B)$B?{Ln(B $BM5Bg(B$B!&(B ($B@5(B)$B:4F#(B $B9d;K(B$B!&(B ($B@5(B)$B0KF#(B $BD>		membrane
separation
MFI
P
935$B5U?;F)KlI=LL$K=$>~$5$l$?5!G=@-%]%j%^!<$N9=B$$,Hy@8J*IUCe@-$K5Z$\$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 $B=(?M(B		Reverse osmosis membrane
Bacterial adhesion
Surface modification
P
983$BEZCeHy:YAtN`$NG;=LK!$K4X$9$k8!F$(B
($BC^GHBg@84D(B) ($B3X(B)$B!{9S4,(B $BE0(B$B!&(B ($B3X(B)$B>>K\(B $B8g;V(B$B!&(B $BEOn5(B $B?.(B$B!&(B $BLn8}(B $BNIB$(B$B!&(B ($B@5(B)$BCfEh(B $B8wIR(B$B!&(B ($B@5(B)$B;T@n(B $BAO:n(B		Microalgae
Concentration
Biomass
P
991$B29EY(B/$BFs;@2=C:AG1~Ez@-%G%s%I%j%^!<7?@5?;F)6nF0MO1U$N@-G=I>2A(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) $BIMED(B $BK-;0(B$B!&(B ($B?@8MBg1!9)(B/$B@hC>;3(B $B=(?M(B		forward osmosis
draw solute
carbon dioxide
P
1003$B%l%"%a%?%k9bA*BrE*Cj=P7O$rJq4^$7$?9bJ,;RKl$N3+H/$H$=$NJ,N%2s<}$X$N1~MQ(B
($B6eBg1!9)(B) ($B3X(B)$B!{5HED(B $B9R(B$B!&(B ($BFAEgBg1!M}9)(B) ($B@5(B)$BGO>l(B $BM:;0(B$B!&(B ($B6eBg1!9)(B) ($B@5(B)$B5WJ]ED(B $BIY@8;R(B$B!&(B ($B@5(B)$B?@C+(B $BE5Jf(B$B!&(B ($B@5(B)$B8eF#(B $B2m9((B		Polymer Inclusion Membrane
Rare Metals
Recovery
P
$B9V1i?=$79~$_0lMw(B($B%7%s%]%8%&%`HV9f!&9V1iJ,N`HV9fJL(B)
$B
$B2=3X9)3X2q(B $BBh(B48$B2s=)5(Bg2q(B ($BFAEg(B 2016)
(C) 2016 $B8x1W
Most recent update: 2016-11-29 11:54:01
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