SCEJ

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

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

E$B2q>l(B

$B:G=*99?7F|;~!'(B2009-03-11 14:01:08

$BBh(B1$BF|(B
$B9V1i(B
$B;~9o(B		$B9V1i(B
$BHV9f(B		$B9V1iBjL\!?H/I=$B%-!<%o!<%I(B$BJ,N`(B
$BHV9f(B		$B$BHV9f(B
$BJ,N%%W%m%;%9(B
(11:00$B!A(B12:00)$B!!(B($B:BD9(B $B;TB
11:00$B!A(B 11:20E107SPG$BKlF}2=K!$rMQ$$$?C1J,;6%-%H%5%s%^%$%/%m%+%W%;%k$ND4@=(B
($BElBg9)(B) $B!{(B($B3X(B)$B7s;R(B $BBg:n(B$B!&(B($B@5(B)$B@V>>(B $B7{$B!&(B($B@5(B)$B?{86(B $B9'(B$B!&(B($B@5(B)$B5FCO(B $BN4;J(B$B!&(B($B@5(B)$BCfHx(B $B??0l(B		chitosan
membrane emulsification
microcapsule
4-a616
11:20$B!A(B 11:40E108$B2M66$5$l$?%W%k%i%s!>%+%i%.!<%J%sJ#9gKl$N=c?eF)2a(B
($BF|Bg1!@8J*;q8;(B) $B!{(B($B3X(B)$B8eF#(B $B@5(B$B!&(B($B@5(B)$BF+(B $B7E(B$B!&(B($B@5(B)$B:#0f(B $B@5D>(B$B!&(B($B@5(B)$BNkLZ(B $B8y(B		membrane
pullulan
Ultrafiltration
4-a168
11:40$B!A(B 12:00E109$B?eG.=hM}$r;\$7$?%"%Q%?%$%HMO
($B>.;39b@lJ*$B!&(B($B3X(B)$BEOJU(B $BM&B@(B$B!&(B($B@5(B)$B>eLn(B $B7xEP(B$B!&(B($B@5(B)$B@n1[(B $BBgJe(B$B!&(B($B@5(B)$BIp(B $B@.>M(B		apatite
endotoxin
4-a58
12:00$B!A(B 13:00$BCk5Y$_(B
(13:00$B!A(B14:00)$B!!(B($B:BD9(B $B;T@n(B $BAO:n(B)
13:00$B!A(B 13:20E113$BG.M65/AjJ,N%K!$rMQ$$$?%J%$%m%sCf6u;eB?9&Kl$N3+H/$HFC@-I>2A(B
($B%f%K%A%+(B) $B!{(B($B@5(B)$B>.Ln(B $B5.Gn(B$B!&(B$B@nCf(B $BAo(B$B!&(B$BW"ED(B $B0lM:(B$B!&(B($B?@8MBg1!9)(B) ($B3X(B)Saeid R$B!&(B($B@5(B)$B>>;3(B $B=(?M(B		Nylon
Hollow fiber membrane
Thermally induced phase separation process
4-a116
13:20$B!A(B 13:40E114$BG.M65/AjJ,N%K!$rMQ$$$?(BPVDF$B7O%V%l%s%ICf6u;eKl$N:n@=$HKlFC@-I>2A(B
($B?@8MBg1!9)(B) $B!{(B($B3X(B)$BFs8.C+(B $BN<(B$B!&(B($B@5(B)$BBg8~(B $B5H7J(B$B!&(B($B@5(B)$B4];3(B $BC#@8(B$B!&(B($B@5(B)$BA>C+(B $BCN90(B$B!&(B($B@5(B)$B>>;3(B $B=(?M(B		hollow fiber membrane
thermally induced phase separation
PVDF blend membrane
4-a565
13:40$B!A(B 14:00E115$B9bG4@-G]M\1U$+$i$N%P%$%*%]%j%^!<$NKlJ,N%(B
($B4X@>Bg9)(B) $B8~0f(B $BJ8=S(B$B!&(B$B;3K\(B $B42;R(B$B!&(B($B4X@>Bg2=@89)(B) $B!{(B($B@5(B)$BLpLZ(B $B=(<#(B		microfiltration
PGA
alcohol precipitation
4-a128
(14:00$B!A(B15:00)$B!!(B($B:BD9(B $BLpLZ!!=(<#(B)
14:00$B!A(B 14:20E116UF+RO$B$K$h$k(BIMS$B%W%m%;%9(B
($BEl%l(B) $B!{A0ED(B $BCR9((B$B!&(B$BKL=P(B $BM-(B$B!&(B($B@5(B)$BJw4_(B $B?J0l(B$B!&(B($B@5(B)$B?"B<(B $BCiW"(B		Integrated Membrane System
Membrane fouling
Ultra-filtration
4-b517
14:20$B!A(B 14:40E117$BBQ%U%!%&%j%s%0@-$rM-$9$k%]%jF};@Cf6u;eKl$N3+H/(B
($B?@8MBg1!9)(B) $B!{(B($B3X(B)$B4?M(B$B!&(B($B@5(B)$BBg8~(B $B5H7J(B$B!&(B($B@5(B)$B4];3(B $BC#@8(B$B!&(B($B@5(B)$BA>C+(B $BCN90(B$B!&(B($B@5(B)$B>>;3(B $B=(?M(B		poly lactic acid
hollow fiber membrane
fouling
4-a167
14:40$B!A(B 15:00E118$BKl$K$h$k2
($BEl%l(B) $B!{>.4d(B $B2mOB(B$B!&(B$BJU8+(B $B>;90(B		RO Membrane
Anti Fouling
Waste Water Reclamation
4-a138
(15:00$B!A(B16:00)$B!!(B($B:BD9(B $B@V>>!!7{
15:00$B!A(B 15:20E119Metal-CMP$BGS?e=hM}$KE,$7$?9bBQ;@2=@-(BPVDF-UF$BKl(B
($B002=@.%1%_%+%k%:(B) $B!{;V4t(B $BCR(B$B!&(B$B8EK\(B $B8^O:(B		membrane
polyvinylidenfluoride
oxidative resistance
4-a344
15:20$B!A(B 15:40E120$BKlHy:Y9=B$$NM}O@2r@O$rL\E*$H$7$?M[EE;R>CLGK!%7%_%e%l!<%?$N3+H/(B
($BElKLBg1!9)(B) $B!{(B($B@5(B)$B9b1)(B $BMN=<(B$B!&(B($BElKLBgL$Mh%;(B) $BNkLZ(B $B0&(B$B!&(B($BElKLBg1!9)(B) Riadh Sahnoun$B!&(B($B6eBg0p@9%;(B) ($B@5(B)$B8E;3(B $BDL5W(B$B!&(B($BElKLBg1!9)(B) $BDZ0f(B $B=(9T(B$B!&(B$BH+;3(B $BK>(B$B!&(B($B@5(B)$B1sF#(B $BL@(B$B!&(BDel Carpio Carlos A.$B!&(B($B@5(B)$B5WJ](B $BI4;J(B$B!&(B($BElKLBgL$Mh%;%s%?!<(B/$BElKLBg1!9)(B) ($B@5(B)$B5\K\(B $BL@(B		Pore size distribution
Positron annihilation lifetime spectroscopy
large-scale quantum chemical calculation
4-a194
15:40$B!A(B 16:00E121$BCf6u;e7?5U?;F)%b%8%e!<%k$NJ*
($BElMNKB(B) $B!{(B($B@5(B)$B7'Ln(B $B=_IW(B$B!&(B($B@5(B)$B4XLn(B $B@/><(B$B!&(B($B?@8MBg1!9)(B) ($B@5(B)$B>>;3(B $B=(?M(B		membrane separation
reverse osmosis
hollow fiber
4-a205
(16:00$B!A(B16:40)$B!!(B($B:BD9(B $B9b1)!!MN=<(B)
16:00$B!A(B 16:20E122$B?e=hM}MQCf6u;eKl$NKlI=LL9=B$$HKl%U%!%&%j%s%0$NAj4X$K4X$9$k8&5f(B
($B?@8MBg1!9)(B) ($B3X(B)$BJR6M(B $B7r(B$B!&(B$B!{(B($B@5(B)$BBg8~(B $B5H7J(B$B!&(B($B@5(B)$B4];3(B $BC#@8(B$B!&(B($B@5(B)$BA>C+(B $BCN90(B$B!&(B($B@5(B)$B>>;3(B $B=(?M(B		hollow fiber membrane
fouling
sodium alginate
4-a398
16:20$B!A(B 16:40E123$B05NOB;<:$r9MN8$7$?KlJ,N%%W%m%;%9$N%7%_%e%l!<%7%g%s(B
($BElMNBg9)(B) $B!{(B($B3X(B)$B2CF#(B $B9b;V(B$B!&(B($B3X(B)$BFAB<(B $B2m90(B$B!&(B($B@5(B)$B@n@%(B $B5A6k(B		Membrane separation
simulation
pressure drop
4-a609

$BBh(B2$BF|(B
$B9V1i(B
$B;~9o(B		$B9V1i(B
$BHV9f(B		$B9V1iBjL\!?H/I=$B%-!<%o!<%I(B$BJ,N`(B
$BHV9f(B		$B$BHV9f(B
$BJ,N%%W%m%;%9(B
(9:20$B!A(B10:00)$B!!(B($B:BD9(B $BHf2E(B $B=<(B)
9:20$B!A(B 9:40E202Characterization of random and block copolymers of highly sulfonated poly(arylene ether sulfone) for proton exchange membrane
($B?@8MBg1!9)(B) $B!{(B($B3X(B)$BNB(B $B%5%$(B$B!&(B($B@5(B)$BBg8~(B $B5H7J(B$B!&(B($B@5(B)$B4];3(B $BC#@8(B$B!&(B($B@5(B)$BA>C+(B $BCN90(B$B!&(B($B@5(B)$B>>;3(B $B=(?M(B		proton exchange membrane
sulfonated poly(arylene ether sulfone)
copolymer
4-a188
9:40$B!A(B 10:00E203$B%P%$%]!<%iKl$rMQ$$$?EE5$F)@OK!$K$h$kGS?eCf$+$i$N%[%&AG=|5n%W%m(B $B%;%9$N3+H/(B
($BElBg?7NN0h(B) $B!{(B($B3X(B)$BD9_7(B $B425,(B$B!&(B($B@5(B)$BHSDM(B $B=_(B$B!&(B$B0f>e(B $BLwM:(B$B!&(B($B@.l~BgM}9)(B) ($B@5(B)$B;3:j(B $B>O90(B$B!&(B($BElBg?7NN0h(B) ($B@5(B)$BLxBt(B $B9,M:(B		Electrodialysis
Bipolar membrane
Boron removal
4-a163
(10:00$B!A(B11:00)$B!!(B($B:BD9(B $B>>;3!!=(?M(B)
10:00$B!A(B 10:20E204$BEE5$F)@O$rMQ$$$?Fs;@2=C:AGJ,N%!&2s<}K!$N2A(B
($BElBg9)(B) $B!{(B($B3X(B)$B66K\(B $B2BF`(B$B!&(B($BElBg?7NN0h(B) ($B3X(B)$BD9_7(B $B425,(B$B!&(B($B@5(B)$BHSDM(B $B=_(B$B!&(B($B@.l~BgM}9)(B) ($B@5(B)$B;3:j(B $B>O90(B$B!&(B($BElBg?7NN0h(B) ($B@5(B)$BLxBt(B $B9,M:(B		electrodialysis
CO2 capture
bipolar membrane
4-a571
10:20$B!A(B 10:40E205$B%]%j%^!<%V%l%s%IK!$K$h$j:n@=$7$?(BPVA$B7O1"%$%*%s8r49Kl$K$*$1$k%$%*%sM"AwFC@-(B
($B;38}Bg1!M}9)(B) $B!{(B($B3X(B)$B@>B<(B $B7CH~(B$B!&(B$B@6?e(B $B7CN$;R(B$B!&(B($B@5(B)$BHf2E(B $B=<(B		Ion-exchange membrane
permselectivity
poly(vinyl alcohol)
4-a745
10:40$B!A(B 11:00E206$B1"%$%*%s8r49Kl$K$*$1$kM-5!1x@wJ*
($B;38}Bg1!M}9)(B) $B!{(B($B3X(B)$BD9@%(B $B$_$J$_(B$B!&(B($B3X(B)$B@>B<(B $B7CH~(B$B!&(B($B@5(B)$BEDCf(B $B?-9,(B$B!&(B($B@5(B)$BHf2E(B $B=<(B		Anion-exchange membrane
Electro dialysis
Fouling
4-a746
(11:00$B!A(B12:00)$B!!(B($B:BD9(B $B$O$P$-!!9-82(B)
11:00$B!A(B 11:20E207$B@wNAGS?e$N%*%>%s;@2=J,2r$K$*$1$k%,%9N.NL$N1F6A(B
($BElMNBg9)(B) $B!{(B($B3X(B)$B2CF#(B $B9b;V(B$B!&(B$BBgH*(B $BGn5*(B$B!&(B($B3X(B)$BFAB<(B $B2m90(B$B!&(B($B@5(B)$B@n@%(B $B5A6k(B		ozone
colored effluent
simulation
4-d598
11:20$B!A(B 11:40E208Thermodynamic Properties of Potassium Serinate for Carbon Dioxide Absorption
(Yonsei U.) $B!{(B($B3X(B)Lee J.$B!&(B($B3X(B)Song H. J.$B!&(B($B@5(B)Lee S.$B!&(B($B3X(B)Ahn S.$B!&(B($B@5(B)Park J. W.		potassium serinate
carbon dioxide
absorption
4-d642
11:40$B!A(B 12:00E209Characterization of Potassium Serinate for Carbon Dioxide Absorption
(Yonsei U.) $B!{(B($B3X(B)Song H. J.$B!&(B($B@5(B)Lee S.$B!&(B($B3X(B)Lee J.$B!&(B($B3X(B)Ahn S.$B!&(B($B@5(B)Park J. W.		potassium serinate
carbon dioxide
absorption
4-d647

$BBh(B3$BF|(B
$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$$NF)2aJ,N%(B
($B?73cBg9)(B) $B!{(B($B3X(B)$B@>Eg(B $BBgM5(B$B!&(B($B@5(B)$B0KEl(B $B>O(B		liquid mambrane
vapor permeation
water vapor
4-a384
$B9V1i%W%m%0%i%`(B
$B2=3X9)3X2q(B $BBh(B74$BG/2q(B($B2#IM(B)
(C) 2009 ($B
Most recent update: 2009-03-11 14:01:08
For more information contact $B2=3X9)3X2q4XEl;YIt(B $BBh(B74$BG/2q(B $BLd$$9g$;78(B
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