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| $B9b1)MN= |
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$B:G=*99?7F|;~!'(B2014-08-04 11:49:01
| $B$3$NJ,N`$G$h$/;H$o$l(B $B$F$$$k%-!<%o!<%I(B | $B%-!<%o!<%I(B | $B | |
|---|---|---|---|
| membrane | 3$B7o(B | | |
| Hydrogen separation | 3$B7o(B | | |
| microfiltration | 3$B7o(B | | |
| Defect-free | 2$B7o(B | | |
| Silica membrane | 2$B7o(B | | |
| gas permeation | 2$B7o(B | | |
| Zeolite membrane | 2$B7o(B | | |
| pervaporation | 2$B7o(B | | |
| Membrane Separation | 2$B7o(B | | |
| separation | 2$B7o(B | | |
| ion adsorption | 1$B7o(B | | |
| $B | $B9V1iBjL\!?H/I=| $B%-!<%o!<%I(B | $B | |
|---|---|---|---|
| 8 | $BC:AGA!0]$rMQ$$$?%<%*%i%$%H$m2aKl$N:n@=(B | zeolite filtration membrane carbon fiber water treatment | 4/22 08:49:52 |
| 13 | MF/UF$BCf6u;eKl%b%8%e!<%k$N$m2aFC@-M=B,5;=Q$N3+H/(B | microfiltration ultrafiltration hollow fiber membrane | 4/23 10:17:01 |
| 59 | [$BM%=(O@J8>^(B]$B%7%j%+Kl$K$*$1$k6E=L@-5$BN$N%_%/%m9&= | silica membrane gas permeation micropore filling | 5/1 10:04:01 |
| 96 | $B9b6u7dN(DcG.KDD%N(%U%l%-%7%V%kBQG.@-B?9&%]%j%$%_%I@=B$%W%m%;%9$N3+H/(B | porous flexible film | 5/4 22:23:01 |
| 117 | $BEE5$2=3XE* ($B6eBg%+!<%\%s%K%e!<%H%i%k!&%(%M%k%.!<9q:]8&(B) $B!{(B($B@5(B)$BC+8}(B $B0iM:!&(B | CO2 capture membrane electrodialysis | 5/7 12:54:19 |
| 262 | $BJ,;RF0NO3XK!$rMQ$$$?:Y9&I=LLFC@-$,%J%N:Y9&Fb1UBNF)2a@-$K5Z$\$91F6A$N2rL@(B | molecular dynamics nanofiltration viscous flow | 5/9 14:12:12 |
| 265 | $BH?1~@-G.(BCVD$BC:AG=$>~%7%j%+Kl$N5$BNF)2aFC@-$K5Z$\$9C:AGA06nBN$N1F6A(B | CVD carbon gas permeation | 5/9 14:28:55 |
| 271 | $B%W%i%:%^(BCVD$B%"%b%k%U%!%9%+!<%\%sKl$NJ,;R$U$k$$FC@-(B | plasma-enhanced CVD amorphous carbon membrane molecular sieve membrane | 5/9 15:05:30 |
| 274 | $B%R%I%m%7%j%k2=$K$h$kBQG.@-(BSiOC$BJ,N%Kl$N:n@=$HFC@-I>2A(B | hydrosilylation thermal stability hydrogen separation | 5/9 15:13:45 |
| 329 | C3H6/C3H8$BJ,N%$N$?$a$N6bB0%I!<%WM-5!L55!%O%$%V%j%C%IKl$N:n@=(B | sol-gel method organic-inorganic hybrid membrane metal doped | 5/9 18:30:16 |
| 366 | $B:Y9&%U%#%j%s%0Kl$rMQ$$$??75,?e>x5$A*BrF)2aKl$N3+H/(B | Ventilator system Pore-filling membrane Water vapor / CO2 permselectivity | 5/9 21:31:15 |
| 393 | $B9b29H/9Z!&%<%*%i%$%HKlJ,N%%O%$%V%j%C%I%7%9%F%`$N8!F$(B | Zeolite membrane Hightemperature ethanol fermentation Hybrid system | 5/10 14:01:00 |
| 412 | $B2C05>r7o2<$K$*$1$k(Bsilicalite-1$BKl$N%-%7%l%s0[@-BNF)2aJ,N%FC@-$N8!F$(B | silicalite-1 zeolite membrane separation pressurized conditions | 5/10 16:34:54 |
| 413 | $BM-5!9=B$5,Dj:^$rMQ$$$J$$(B*BEA$B7?%<%*%i%$%HKlD4@=K!$N8!F$(B | *BEA zeolite membrane separation OSDA-free synthesis | 5/10 16:36:07 |
| 414 | $BHsGK2u$G$N%<%*%i%$%HKl$KBP$9$k5[Ce$NB,Dj ($BAaBg@h?JM}9)(B/$BAaBgM}9)Am8&(B/JST-CREST) ($B@5(B)$B>>J}(B $B@5I'!&(B | Zeolite membrane Adsorption Structure analysis | 5/10 16:36:25 |
| 415 | $B2C052<$G$N%a%?%N!<%kJ,N%$KBP$9$k(BNa-ZSM-5$BKl$NFC@-$N8!F$(B ($BAaBg@h?JM}9)(B/$BAaBgM}9)Am8&(B/JST-CREST) ($B@5(B)$B>>J}(B $B@5I'!&(B | ZSM-5 membrane separation methanol mixture | 5/10 16:39:47 |
| 423 | $BC:2=?eAG7O9bJ,;REE2r | Alkaline fuel cell Molecular simulation Polymer | 5/10 19:17:02 |
| 447 | ZIF-8$BKl$N%W%m%T%l%s!?%W%m%Q%s:.9g%,%9J,N%FC@-(B | Gas separation membrane Zeolitic imidazolate framework-8 Propylene/propane separation | 5/11 17:47:27 |
| 486 | $B2M667?%*%k%,%N%7%j%+Kl$N%9%Z!<%5!<$,F)2aFC@-$K5Z$\$91F6A$*$h$S9bB.@=Kl(B | organosilica membranes permeation properties bridged alkoxides | 5/12 09:12:20 |
| 495 | $B%/%m%9%U%m!<@:L)$m2a$NBgN.NLDc05A`:n$K$h$kN3;R$NKlLLBO@QM^@)(B | cross-flow microfiltration particle | 5/12 09:34:38 |
| 528 | $BL55!B?9& | chemical absorption pressure reduction CO2 stripping | 5/12 10:57:08 |
| 595 | $BBQ05@-$H?WB.$J(BCO2$BF)2a@-$rN>N)$9$k%$%*%s%2%k%U%#%k%`$NAO@=(B | CO2 separation membrane Ion-gel interpenetrating polymer network structure | 5/12 13:04:30 |
| 602 | $B%$%*%s8r49Kl$*$1$k%W%m%H%sF)2a@-$KBP$9$k%h%&2=?eAG(B-$B%h%&AGMO1UG;EY$N1F6A(B | Ion-exchange membrane Hydriodic acid Proton permeability | 5/12 13:25:18 |
| 660 | $B>F7k6bB0$K;Y;}$5$l$?(BPd-Cu$B9g6bGvKl$NL57g4Y2=$H$=$N?eAGF)2aG=(B | Hydrogen separation Membrane Defect-free | 5/12 15:35:04 |
| 698 | $B@5?;F)Kl$rMQ$$$?%i%F%C%/%9N3;R$NG;=LA`:n$K$*$1$kJ* | Latex Particles Forward Osmosis Membrane Separation | 5/12 16:40:18 |
| 720 | $BHyN3;RJ,;61U$NKlJ,N%%W%m%;%9$K$*$1$k:Y9&9=B$$N1F6A(B | microfiltration Phase field model Direct numerical simulation | 5/12 17:07:07 |
| 747 | $B?eAGA*BrF)2a%7%j%+Kl$N3+H/5Z$S$=$N%(%?%sC&?eAGH?1~$X$N1~MQ(B | Silica membrane Defect-free Membrane reactor | 5/12 17:30:54 |
| 895 | $BAB?e@-%7%j%+Kl$NJ,N%@-G=$K5Z$\$9AB?e@-41G=4p$N1F6A(B | Pervaporation Hydrophobicity Silica | 5/12 19:57:15 |
| 977 | SPPO$BCf6u;e%+!<%\%sKl$K$h$kM-5!%O%$%I%i%$%I$+$i$N?eAGJ,N%(B | Carbon membrane Hydrogen separation Organic chemical hydrides | 5/12 21:53:42 |
| 982 | $B | membrane zeolite pervaporation | 5/12 21:55:15 |
| 988 | $B%J%N%U%!%$%P!<$rJl:`$H$7$?%$%*%s5[CeKl$N:n@=$HI>2A(B | functionalized membrane nanofiber ion adsorption | 5/12 22:01:42 |
| 993 | $B%7%/%m%G%-%9%H%j%s4^M-?];@%;%k%m!<%9J#9gKl$NF)2aJ*@-(B | cyclodextrin cellulose acetate composite membrane | 5/12 22:11:40 |
(C) 2014 $B8x1W
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easp 2.34; update.pl 2.33 (C)1999-2013 kawase