SCEJ

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$B%7%s%]%8%&%`(B $B!cKlMxMQ5;=Q$N?7E83+!d(B

C104-C109, C113-C124

$B:G=*99?7F|;~!'(B2007-07-24 09:36:53
$B9V1i(B
$B;~9o(B		$B9V1i(B
$BHV9f(B		$B9V1iBjL\!?H/I=$B%-!<%o!<%I(B$BJ,N`(B
$BHV9f(B		$B$BHV9f(B
C$B2q>l(B $BBh(B1$BF|(B
(10:00$B!A(B11:00)$B!!(B($B:BD9(B $BEDCf0l9((B)
10:00$B!A(B 10:20C104Development of CO2 selective membrane used in high temperature condition for application to membrane reactor
($B%k%M%C%5%s%9!&%(%J%8!$B!&(B($B@5(B)$B;{K\(B $B@5L@(B$B!&(B$BI10f(B $B9@L@(B$B!&(B$B2,ED(B $B<#(B$B!&(B($B?@8MBg1!9)(B) ($B@5(B)$BA>C+(B $BCN90(B$B!&(B($B@5(B)$BBgB<(B $BD>?M(B$B!&(B($B@5(B)$B>>;3(B $B=(?M(B		facilitated transport membrane
membrane reactor
carbon dioxide
S-19502
10:20$B!A(B 10:40C105$B%H%j%(%A%l%s%0%j%3!<%k1UBNKlAuCV$K$h$k6u5$Cf$N(BVOC$B=|5nA`:n(B
($B?73cBg9)(B) $B!{(B($B@5(B)$B0KEl(B $B>O(B$B!&(B$Bg!(B $B9qE/(B$B!&(B$B@P;3(B $B5#(B		liquid membrane
VOC
gas separation
S-19165
10:40$B!A(B 11:00C106$B4V7gEE>l$rMQ$$$?KlJ,N%3h@-1xE%K!$K$*$1$kKl%U%!%&%j%s%0$NM^@)(B
($BElBg9)(B) $B!{(B($B3X(B)Lu Wei$B!&(B($B@5(B)$B@V>>(B $B7{$B!&(B($B@5(B)$B?{86(B $B9'(B$B!&(B($B@5(B)$BCfHx(B $B??0l(B		membrane bioreactor
membrane fouling
electric pulse
S-19640
(11:00$B!A(B12:00)$B!!(B($B:BD9(B $B0KEl(B $B>O(B)
11:00$B!A(B 11:20C107$B<+F0tMQ%"%_%s7O3&LL3h@-:^Cf%(%^%k%8%g%sL}J,=|5n$X$N%/%m%9%U%m!<$m2aK!$N8!F$(B
($BF|K\%]!<%k(B) $B!{(B($B@5(B)$BFqGH(B $BC]Va(B$B!&(B($B@5(B)$B3Q20(B $B@5?M(B$B!&(B($B@5(B)$B>B8}(B $BE0(B		Cross flow
Parts washing fluid
Oil removal
S-19795
11:20$B!A(B 11:40C108$B9ZAG@QAXKl$rMQ$$$?%P%$%*%G%#!<%<%k$N@8@.(B
($BKL6e;TBg1!(B) $B!{(B($B3X(B)$BEDCf(B $B9'E5(B$B!&(B($BKL6e;TBg(B) ($B@5(B)$B>e9>='(B $B0lLi(B$B!&(B($B:42lBg(B) ($B@5(B)$B@n4nED(B $B1Q9'(B$B!&(B($BKL6e=#9b@l(B) ($B@5(B)$B8eF#(B $B=!<#(B		Biodiesel
Porous hollow-fiber membranes
Enzyme
S-19239
11:40$B!A(B 12:00C109$BG.M65/AjJ,N%K!$K$h$kNd5Q2aDx$G$NB?9&9=B$7A@.2aDx$N%7%_%e%l!<%7%g%s(B
($B?@8MBg1!9)(B) $BJR6M(B $B7r(B$B!&(B($B@5(B)$BA>C+(B $BCN90(B$B!&(B($B5~Bg1!9)(B) ($B@5(B)$BKR(B $BBYJe(B$B!&(B($B?@8MBg1!9)(B) $B!{(B($B@5(B)$B>>;3(B $B=(?M(B		thermally induced phase separation
spinodal decomposition
cooling process
S-19810
(13:00$B!A(B14:20)$B!!(B($B:BD9(B $B@V>>7{
13:00$B!A(B 13:20C113$BF};@H/9Z1U@:@=$K$*$1$k5U?;F)KlK!$N8!F$(B
($B;37ABg9)(B) $B!{(B($B3X(B)$B;{ED(B $BM:0l(B$B!&(B($B@5(B)$B8c6?(B $B7r0l(B$B!&(B$BElET(B $B2mE5(B$B!&(B($B@5(B)$B9b66(B $B9,;J(B		Lactic acid
Reverse osmosis
Electrodialysis
S-1957
13:20$B!A(B 13:40C114$BDc05(BRO$BKl$K$h$kG@Lt1x@wGS?e$NKlJ,N%FC@-(B
($B9)3X1!Bg9)(B) $B!{(B($B@5(B)$B@P@n(B $BE0(B		membrane filtration
agrochemical
waste water
S-19920
13:40$B!A(B 14:00C115$B9b@E?e052<$G$N9bJ,;RKl$N?eCfMOB8%a%?%sF)2aFC@-(B
($B;38}Bg9)(B) $B!{(B($B@5(B)$BEDCf(B $B0l9((B$B!&(B($B@5(B)$B4nB?(B $B1QIR(B$B!&(B($B%(%s%8%K%"%j%s%0?66=6(2q(B) $B2EG<(B $B9/Fs(B$B!&(B($B@P@nEg8!::7WB,(B) $B23C+(B $BG=;K(B$B!&(B$B?<_7(B $B6/(B		dissolved methane
hydraulic pressure
silicone rubber
S-191038
14:00$B!A(B 14:20C116$B%Q%i%8%&%`Kl$K$h$k?eAGJ,N%$X$N6&B85$BN$N1F6A(B
($BFAEgBg1!(B) $B!{(B($B3X(B)$BD9_@(B $B9(0l(B$B!&(B($B@5(B)$B2CF#(B $B2mM5(B$B!&(B($B3X(B)$B:dED(B $B1YH~(B$B!&(B($B@5(B)$BKY2O(B $B=S1Q(B$B!&(B($B@5(B)$BIZED(B $BB@J?(B		palladium membrane
hydrogen separation
hydrogen permeation
S-19171
(14:20$B!A(B15:40)$B!!(B($B:BD9(B $B@P@n(B $BE0(B)
14:20$B!A(B 14:40C117$BBP8~3H;6(BCVD$BK!$K$h$k?eAGF)2a%7%j%+Kl$N9bF)2aN(2=$HBQG.@-(B
($B%N%j%?%1%+%s%Q%K!<%j%_%F%I(B) $B!{5HLn(B $BBY(B$B!&(B$B0BF#(B $BBYE5(B$B!&(B($B1'ET5\Bg(B) ($B@5(B)$B0KF#(B $BD>		Silica membrane
Hydrogen separation
Counter diffusion CVD
S-206
14:40$B!A(B 15:00C118$B%J%NB?9&@-%A%?%K%"Kl$N:n@=$HEE2r
($B9-Bg1!9)(B) $B!{(B($B3X(B)$B>.@n(B $BOB5W(B$B!&(B($B@5(B)$BETN1(B $BL-N;(B$B!&(B($B@5(B)$B5H2,(B $BJ~5W(B		nanofiltration
titania membrane
salt retention
S-19723
15:00$B!A(B 15:20C119CO2$B?FOB@-$rIUM?$7$??75,%+!<%\%sKl$N3+H/$H(BCO2$BJ,N%FC@-(B
(RITE) $B!{(B($B@5(B)$B9CHe(B $B>HI'(B$B!&(BChowdhury F. A.$B!&(B($B@5(B)$BIw4V(B $B?-8c(B$B!&(B($B@5(B)$BF#2,(B $BM40l(B		carbon membrane
carbon dioxide
affinity
S-20309
15:20$B!A(B 15:40C120$B%j%0%K%sM6F3BN$rA06nBN$H$9$k6bB04^M-C:AGKl$NF)2aJ*@-(B
($B;38}Bg1!M}9)(B) $B!{(B($B3X(B)$BF#Ln(B $B6G@.(B$B!&(B($B@5(B)$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($B@5(B)$B4nB?(B $B1QIR(B$B!&(B($B;0=EBg@8J*;q8;(B) ($B@5(B)$BgU2,(B $B@58w(B		Lignin
Molecular sieve carbon membrane
Gas separation
S-19470
(15:40$B!A(B17:00)$B!!(B($B:BD9(B $B9CHe>HI'(B)
15:40$B!A(B 16:00C121PTFE$BB?9&e$G$N%+!<%\%sKl$N:n@=$HJ,N%@-G=$NI>2A(B
($BElBg@88&(B) $B!{(B($B@5(B)$BK>7n(B $BOBGn(B$B!&(B($B@5(B)$BGwED(B $B>O5A(B		carbon membrane
microporous membrane
pervaporation
S-20998
16:00$B!A(B 16:20C122MFI$B%<%*%i%$%HKl$N8e=hM}K!$N8!F$(B
($B$B!&(B$B5HNI(B $B2mI'(B$B!&(B$B?9(B $BAo;R(B$B!&(B$BFbED(B $B9-3$(B$B!&(B$BLg4V(B $B7DB@(B		MFI zeolite membrane
counter diffusion CVD method
High temperature gas separation
S-20182
16:20$B!A(B 16:40C123PHI$BKl$rMQ$$$??;F)5$2=K!$K$h$kM-5!MOG^$+$i$NC&?e9)Dx$N2=3X%W%m%;%9$X$N1~MQ(B
($BF|Bg9)(B) $B!{(B($B3X(B)$B:,K\(B $BM:B@(B$B!&(B($B6&(B)$B@>=P(B $BMx0l(B$B!&(B($B;:Am8&(B) ($B6&(B)$B0f>e(B $BJ~Li(B$B!&(B($B@5(B)$BD9@%(B $BB?2C;R(B$B!&(B($B@5(B)$BD9C+@n(B $BBY5W(B$B!&(B($B@5(B)$B@6=;(B $B2EF;(B		zeolite membrane
pervaporation
Esterification
S-20655
16:40$B!A(B 17:00C124$B%^%$%/%mGH2CG.$K$h$k(BX$B7?%<%*%i%$%HKl$N@=Kl$H?;F)5$2=J,N%(B
($B;38}Bg1!M}9)(B) $B!{(B($B3X(B)$B>>;3(B $BIROB(B$B!&(B($B@5(B)$B?"B<(B $B0l9-(B$B!&(B($B@5(B)$BEDCf(B $B0l9((B$B!&(B($B@5(B)$B4nB?(B $B1QIR(B		pervaporation
zeolite membrane
S-19865
$B9V1i%W%m%0%i%`(B
$B2=3X9)3X2q(B $BBh(B39$B2s=)5(Bg2q(B
(C) 2007 ($B
Most recent update: 2007-07-24 09:36:53
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