SCEJ

$B2=3X9)3X2q(B $BBh(B74$BG/2q(B($B2#IM(B)

$B9V1i%W%m%0%i%`!J2q>l!&F|DxJL!K(B

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$B:G=*99?7F|;~!'(B2009-03-11 14:01:08
$B9V1i(B
$B;~9o(B		$B9V1i(B
$BHV9f(B		$B9V1iBjL\!?H/I=$B%-!<%o!<%I(B$BJ,N`(B
$BHV9f(B		$B$BHV9f(B
$BJ,N%%W%m%;%9(B
(9:00$B!A(B10:00)$B!!(B($B:BD9(B $B5H2,!!J~5W(B)
9:00$B!A(B 9:20E301$B8w?(G^$rMQ$$$??e$N40A4J,2r$K$h$k?eAG@=B$$X$NKlJ,N%$N1~MQ(B
($B;38}Bg9)(B) $B!{HSED(B $B9b;K(B$B!&(B($B;38}Bg1!M}9)(B) ($B@5(B)$BEDCf(B $B0l9((B$B!&(B($B@5(B)$B4nB?(B $B1QIR(B$B!&(B$B		hydrogen production
membrane separation
photocatalyst
4-a615
9:20$B!A(B 9:40E302Pd$B<+N)GvKl$N?eAGJ,N%FC@-(B
($B9)3X1!Bg(B) $B!{(B($B3X(B)$B:4F#(B $B>;=S(B$B!&(B($B@5(B)$B2OB<(B $B8wN4(B$B!&(B($B;:Am8&(B) ($B@5(B)$B5W>>(B $B7I;R(B$B!&(B($B@5(B)$B@PDM(B $B$_$5$-(B$B!&(B($B@5(B)$B86(B $B=E$B!&(B($B@5(B)$B?\ED(B $BMN9,(B$B!&(B($B@5(B)$B86C+(B $B8-<#(B		Palladium
Membrane
Hydrogen
4-a55
9:40$B!A(B 10:00E303$B=c%Q%i%8%&%`$N?eAGF)2a78?t$N05NO0MB8@-(B
($B;:Am8&(B) $B!{(B($B@5(B)$B86(B $B=E$B!&(B$B@PDM(B $B$_$5$-(B$B!&(B($B@5(B)$B?\ED(B $BMN9,(B$B!&(B($B@5(B)$B8~ED(B $B2m0l(B$B!&(B($B@5(B)$B86C+(B $B8-<#(B		Hydrogen
metal membranes
palladium
4-a34
(10:00$B!A(B11:00)$B!!(B($B:BD9(B $B?\ED!!MN9,(B)
10:00$B!A(B 10:20E304$B:Y9&Fb=2A(B
($BF`NI@hC$B!&(B(RITE) ($B@5(B)$B5\K\(B $B3X(B$B!&(B(RITE,$BF`NI@hC8l(B $B9nB'(B$B!&(B($B@5(B)$BF#2,(B $BM40l(B		membrane
hydrogen
palladium
4-a253
10:20$B!A(B 10:40E305V$B7O9g6bKl$K$h$k?eAGJ,N%(B
($BJ*!&:`5!9=(B) $B!{(B($B@5(B)$B@>B<(B $BKS(B$B!&(B$B8EKR(B $B@/M:(B$B!&(B($B@iMU9)Bg(B) $B4d:4(B $B9nI'(B$B!&(B($BB@M[9]9)(B) $B5H1J(B $B1QM:(B		hydrogen
permeation
vanadium
4-a747
10:40$B!A(B 11:00E306CO2$BJ,N%B%?JM"AwKl$N3+H/$H%a%s%V%l%s%j%"%/%?!<$X$N1~MQ(B
($B%k%M%C%5%s%9!&%(%J%8!($B@5(B)$B;{K\(B $B@5L@(B$B!&(B$B3k2<(B $B$+$*$j(B$B!&(B($B@5(B)$B?@Hx(B $B1Q<#(B$B!&(B$B2,ED(B $B<#(B$B!&(B($B?@8MBg1!9)(B) ($B3X(B)$B1)@n(B $BOB4u(B$B!&(B($B@5(B)$BA>C+(B $BCN90(B$B!&(B($B@5(B)$B4];3(B $BC#@8(B$B!&(B($B@5(B)$B>>;3(B $B=(?M(B		facilitated transport membrane
membrane reactor
carbon dioxide
4-a680
(11:00$B!A(B12:00)$B!!(B($B:BD9(B $BEDCf!!0l9((B)
11:00$B!A(B 11:20E307Effect of membrane structure on gas separation performance of hollow fiber membrane contactor
(Kobe U.) $B!{(B($B3X(B)Rajabzadeh Saeid$B!&(B($B3X(B)Yoshimoto Shin-ya$B!&(B($B@5(B)Ohmukai Yoshikage$B!&(B($B@5(B)Maruyama Tatsuo$B!&(B($B@5(B)Sotani Tomohiro$B!&(B($B@5(B)Teramoto Masa-aki$B!&(B($B@5(B)Matsuyama Hideto		Hollow fiber membrane contactor
PVDF membrane
membrane structure
4-a301
11:20$B!A(B 11:40E308($B9V1iCf;_(B)

100700
11:40$B!A(B 12:00E309$B9b05>r7o$K$*$1$kB?9&@-%;%i%_%C%/Kl$N(BCO2$BF)2a$*$h$S(BCO2/N2$BJ,N%FC@-(B
($B9-Bg9)(B) $B!{(B($B3X(B)$B;e8}(B $BAo(B$B!&(B($B@5(B)$B5H2,(B $BJ~5W(B$B!&(B($B@5(B)$B6b;X(B $B@58@(B$B!&(B($B@5(B)$BETN1(B $BL-N;(B		inorganic membrane
CO2
high pressure
4-a109
12:00$B!A(B 13:00$BCk5Y$_(B
(13:00$B!A(B14:00)$B!!(B($B:BD9(B $BLnB
13:00$B!A(B 13:20E313$B%7%j%+Kl$K$h$k%a%?%N!<%k(B/$B%8%a%A%k%+!<%\%M!<%H$N(BPV$BJ,N%$H2A(B
($B9-Bg1!9)(B) $B:4!9LZ(B $BL@;K(B$B!&(B($B@5(B)$B5H2,(B $BJ~5W(B$B!&(B($B@5(B)$B6b;X(B $B@58@(B$B!&(B$B!{(B($B@5(B)$BETN1(B $BL-N;(B		silica membranes
pervaporation
transient response
4-a209
13:20$B!A(B 13:40E314$BB?9&@-%7%j%+Kl$K$*$1$k%"%s%b%K%"F)2aFC@-(B
($B9-Bg1!9)(B) $B!{(B($B@5(B)$B6b;X(B $B@58@(B$B!&(B$B;3K\(B $B>O(B$B!&(B($B@5(B)$B5H2,(B $BJ~5W(B$B!&(B($B@5(B)$BETN1(B $BL-N;(B		Silica membrane
Ammonia
Gas permeation
4-a293
13:40$B!A(B 14:00E315FAU$B7?%<%*%i%$%HKl$K$h$kM-5!1UBN:.9gJ*$NJ,N%(B
($B;38}Bg1!M}9)(B) $B!{(B($B@5(B)$B4nB?(B $B1QIR(B$B!&(B($B3X(B)$B0f>e(B $BM%;R(B$B!&(B$B>>;3(B $BIROB(B$B!&(B($B@5(B)$B?"B<(B $B0l9-(B$B!&(B($B@5(B)$BEDCf(B $B0l9((B		zeolite membrane
pervaporation
vaporpermeation
4-a294
(14:00$B!A(B15:00)$B!!(B($B:BD9(B $B0KEl!!>O(B)
14:00$B!A(B 14:20E316$B%7%j%k4p$rM-$9$k%]%j%$%_%IKl$N:n@=$H5$BNF)2aA*Br@-(B
($B;38}Bg1!M}9)(B) $B!{;3>e(B $B9LJ?(B$B!&(B($B@5(B)$B?"B<(B $B0l9-(B$B!&(B($B@5(B)$BEDCf(B $B0l9((B$B!&(B($B@5(B)$B4nB?(B $B1QIR(B		gas separation
polyimides
silyl side groups
4-a636
14:20$B!A(B 14:40E317$B:Y9&%U%#%j%s%07?(BPDMS/PMHS$BKl$K$h$k?;F)5$2=J,N%(B
($B4X@>Bg9)(B) $B!{(B($B@5(B)$BEDCf(B $B=SJe(B$B!&(B$BjO(B $BD6(B$B!&(B(Hitz$BF|N)B$A%(B) ($B@5(B)$B9SLZ(B $BDgIW(B$B!&(B($B4X@>Bg9)(B) ($B@5(B)$B;0Bp(B $B5AOB(B		pervaporation
PDMS/PMHS membranes
pore-filling
4-a336
14:40$B!A(B 15:00E318$B%j%0%N%/%l%>!<%k$rA06nBN$H$9$kC:AGKl$NF)2aJ*@-(B-$BI=LL=hM}$N8z2L(B
($B;38}Bg1!M}9)(B) $B!{(B($B@5(B)$B4nB?(B $B1QIR(B$B!&(B($B3X(B)$BIp5o(B $BM&4u(B$B!&(B$B8E2l(B $BCR;R(B$B!&(B($B@5(B)$B?"B<(B $B0l9-(B$B!&(B($B@5(B)$BEDCf(B $B0l9((B$B!&(B($B:e;T9)8&(B) $B@n=.(B $B8yO/(B$B!&(B($B;0=EBg1!@8J*;q8;(B) ($B@5(B)$BgU2,(B $B@58w(B		lignin
carbon membrane
surface treatment
4-a286
(15:00$B!A(B16:00)$B!!(B($B:BD9(B $B6b;X!!@58@(B)
15:00$B!A(B 15:20E319MFI$B%<%*%i%$%HKl$NN33&=hM}$H$=$NF)2a5!9=$N8!F$(B
($B$B!&(B$B?9(B $BAo;R(B$B!&(B($B@5(B)$BLnB<(B $B4490(B$B!&(B($B;38}Bg9)(B) ($B@5(B)$B4nB?(B $B1QIR(B		zeolite membrane
post-treatment
permeation mechanism
4-a258
15:20$B!A(B 15:40E320$B?75,%<%*%i%$%H(BCDS-1(CDO)$BKl$N9g@.$*$h$S%/%i%C%/H/@8860x$N9M;!(B
($BF|Bg9)(B) $B!{(B($B3X(B)$BJ?Ln(B $BD>?M(B$B!&(B$B@>=P(B $BMx0l(B$B!&(B($B;:Am8&(B) ($B@5(B)$BD9@%(B $BB?2C;R(B$B!&(B$BD9C+@n(B $BBY5W(B$B!&(B($B@5(B)$B@6=;(B $B2EF;(B		Zeolite membrane
layered silicate
Pervaporation
4-a396
15:40$B!A(B 16:00E321$B1UBNKl$K$h$k%(%?%N!<%k!??e:.9g>x5$$NF)2aJ,N%(B
($B?73cBg9)(B) $B!{(B($B3X(B)$B@>Eg(B $BBgM5(B$B!&(B($B@5(B)$B0KEl(B $B>O(B		liquid mambrane
vapor permeation
water vapor
4-a384
$B9V1i%W%m%0%i%`(B
$B2=3X9)3X2q(B $BBh(B74$BG/2q(B($B2#IM(B)
(C) 2009 ($B
Most recent update: 2009-03-11 14:01:08
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