SCEJ

$B2=3X9)3X2q(B $BBh(B76$BG/2q(B ($BEl5~ET>.6b0f;T(B)

$B9V1i%W%m%0%i%`!J%;%C%7%g%sJL!K(B

$BJ,N%%W%m%;%9(B

E101-E123, E203-E209, E304-E318, F101-F125, F201-F210, F304-F324

$B:G=*99?7F|;~!'(B2011-03-06 19:49:12
$B9V1i(B
$B;~9o(B		$B9V1i(B
$BHV9f(B		$B9V1iBjL\!?H/I=$B%-!<%o!<%I(B$BJ,N`(B
$BHV9f(B		$B$BHV9f(B
E$B2q>l(B $BBh(B1$BF|(B
(9:00$B!A(B10:00)$B!!(B($B:BD9(B $B@P?@E0(B)
9:00$B!A(B 9:20E101Ammonia decomposition in microporous catalytic membrane reactors for COx-free hydrogen production
(Hiroshima U.) $B!{(B($B3X(B)Li Gang $B!&(B ($B@5(B)Kanezashi Masakoto $B!&(B ($B@5(B)Yoshioka Tomohisa $B!&(B ($B@5(B)Tsuru Toshinori
Ammonia decomposition
COx-free hydrogen
Catalytic membrane reactor
4-a377
9:20$B!A(B 9:40E102$B3&LL=E9gK!$K$h$kM-5!L55!%O%$%V%j%C%I(BRO/NF$BKl$N3+H/(B
($B9-Bg1!9)(B) ($B@5(B)$B8wEh(B $B>O(B $B!&(B ($B@5(B)$B6b;X(B $B@58@(B $B!&(B ($B@5(B)$B5H2,(B $BJ~5W(B $B!&(B $B!{(B($B@5(B)$BETN1(B $BL-N;(B
reverse osmosis
polyamide
membrane
4-a404
9:40$B!A(B 10:00E103BEA$B%<%*%i%$%HKt$O(BMCM-41/$BM-5!9bJ,;R%O%$%V%j%C%IKl$NF)2aJ*@-(B
($B;38}Bg1!M}9)(B) $B!{(B($B3X(B)$BEgFb(B $BH~9,(B $B!&(B ($B@5(B)$BEDCf(B $B0l9((B $B!&(B ($B@5(B)$B4nB?(B $B1QIR(B
hybrid membrane
mesoporous silica
gas separation
4-a322
(10:00$B!A(B11:00)$B!!(B($B:BD9(B $BETN1(B $BL-N;(B)
10:00$B!A(B 10:20E104$B6bB0Cf4VAX$rMxMQ$7$?9bBQ5W@-%Q%i%8%&%`GvKl$N:n@=(B
($B1'ET5\Bg9)(B) $B!{(B($B@5(B)$B0KF#(B $BD> $B!&(B $BFs?@(B $BNKB@O/(B $B!&(B ($B@5(B)$B:4F#(B $B9d;K(B
palladium membrane
hydrogen
separation
4-a16
10:20$B!A(B 10:40E105$B5U?;F)Kl$X$N1~MQ$rL\;X$7$?%j%s;i
($B?@8MBg1!9)(B) $B!{(B($B3X(B)$B2qDE(B $B?4G7N<(B $B!&(B ($B3X(B)$BF#0f(B $B><9((B $B!&(B ($B@5(B)$BBg8~(B $B5H7J(B $B!&(B ($B@5(B)$B@P?@(B $BE0(B $B!&(B ($B@5(B)$B4];3(B $BC#@8(B $B!&(B ($B@5(B)$B>>;3(B $B=(?M(B
biomimetic membrane
phospholipid bilayer
amphotericin B
4-a566
10:40$B!A(B 11:00E106$B9b$$%-%7%l%s0[@-BNJ,N%@-G=$r<($9(Bsilicalite-1$BKl$N9g@.(B
($BAaBgM}9)(B) ($B@5(B)$B>>J}(B $B@5I'(B $B!&(B $B!{(B($B3X(B)$B;0IJ(B $B7z8c(B $B!&(B ($B@5(B)$B4X:,(B $BBY(B $B!&(B ($B@5(B)$B5FCO(B $B1Q0l(B
silicalite-1
xylene isomers
separation
4-a522
(11:00$B!A(B12:00)$B!!(B($B:BD9(B $B0KF#(B $BD>
11:00$B!A(B 11:20E107$B:Y9&Fb=r7o$N8!F$(B
(RITE) ($B@5(B)$BM>8l(B $B9nB'(B $B!&(B (NAIST) $B!{(B($B3X(B)$BIp;3(B $BGnF;(B $B!&(B ($B3X(B)$B1JED(B $B7rM4(B
Gas separation membrane
Hydrogen
Palladium
4-a412
11:20$B!A(B 11:40E108$BBgLL@Q(B(12m2)$B%b%N%j%97?%7%j%+Kl$N3+H/(B
($BF|K\%,%$%7(B) $B!{D9:d(B $BN6FsO:(B $B!&(B $BOBED(B $B0lO/(B $B!&(B $B;{@>(B $B?5(B $B!&(B $B9b66(B $BD>;R(B $B!&(B $BNkLZ(B $B=(G7(B $B!&(B $B0kB<(B $B3X(B $B!&(B $B5HED(B $B=$0l(B
silica membrane
separation
multi-channel monolith
4-a262
11:40$B!A(B 12:00E109$BBgLL@Q(B(12m2)$B%b%N%j%97?C:AGKl$N3+H/(B
($BF|K\%,%$%7(B) $B!{LZ2<(B $BD>?M(B $B!&(B $B;T@n(B $BL@>;(B $B!&(B $B $B!&(B $B;{@>(B $B?5(B $B!&(B $BNkLZ(B $B=(G7(B $B!&(B $B0kB<(B $B3X(B $B!&(B $BIYED(B $B=S90(B $B!&(B $B5HED(B $B=$0l(B
carbon membrane
separation
multi-channel monolith
4-a263

(13:00$B!A(B14:00)$B!!(B($B:BD9(B $B0KEl(B $B>O(B)
13:00$B!A(B 13:20E113$BHsMOG^M65/7?AjJ,N%K!$rMQ$$$?9bJ,;RKl:n@=;~$K$*$1$k8G2=B.EY$N8!F$(B
($B?@8MBg1!9)(B) $B!{(B($B3X(B)$BCfDM(B $B7<2p(B $B!&(B ($B@5(B)$BBg8~(B $B5H7J(B $B!&(B ($B@5(B)$B@P?@(B $BE0(B $B!&(B ($B@5(B)$B?@Hx(B $B1Q<#(B $B!&(B ($B@5(B)$B4];3(B $BC#@8(B $B!&(B ($B@5(B)$B>>;3(B $B=(?M(B
Nonsolvent induced phase separation
solidification process
membrane
4-a582
13:20$B!A(B 13:40E114Na$B7?(BZSM-5$BKl$X$NC:2=?eAG5[CeFC@-$N8!F$(B
($BAaBgM}9)(B) ($B@5(B)$B>>J}(B $B@5I'(B $B!&(B $B!{(B($B3X(B)$B:4F#(B $B7=2p(B $B!&(B $BCSED(B $B3YO:(B $B!&(B ($B@5(B)$B4X:,(B $BBY(B $B!&(B ($B@5(B)$B5FCO(B $B1Q0l(B
ZSM-5 membrane
hydrocarbon separation
adsorption property
4-a573
13:40$B!A(B 14:00E115Preparation and characterization of Al-rich ZSM-5 membranes
($B;38}Bg1!M}9)(B) $B!{(B($B3X(B)$B $B!&(B ($B@5(B)$BEDCf(B $B0l9((B $B!&(B ($B@5(B)$B4nB?(B $B1QIR(B
zeolite membrane
pervaporation
ZSM-5 zeolite
4-a239
(14:00$B!A(B14:20)$B!!(B($B;J2q(B $B>>;3(B $B=(?M(B)
14:00$B!A(B 14:20E116[$B8&5f>)Ne>^(B]$B%7%j%+%M%C%H%o!<%/9=B$@)8f$K$h$k?75,?eAGJ,N%Kl$NAO@=(B
($B9-Bg(B) $B!{(B($B@5(B)$B6b;X(B $B@58@(B
award
0-c773
(14:20$B!A(B15:20)$B!!(B($B:BD9(B $B4nB?(B $B1QIR(B)
14:20$B!A(B 14:40E117$B%7%j%+Kl$rMQ$$$?M-5!%O%$%I%i%$%IC&?eAGKlH?1~4o$K$*$1$kDc29A`:n$N8!F$(B
($B9)3X1!Bg9)(B) $B!{(B($B@5(B)$B@%2<(B $B2mGn(B $B!&(B ($B@5(B)$B@FF#(B $B?r(B $B!&(B ($BElBg1!9)(B) ($B3X(B)$B?%ED(B $BOB7{(B $B!&(B ($B9)3X1!Bg9)(B) ($B@5(B)$B@V>>(B $B7{ $B!&(B (JX$BF|9[F|@P%(%M%k%.!<(B) $B@%@n(B $BFX;J(B $B!&(B ($B9)3X1!Bg9)(B) ($B@5(B)$BCfHx(B $B??0l(B
silica membrane
membrane reactor
chemical vapor deposition
4-a255
14:40$B!A(B 15:00E118$B3&LL$K3H;6B%?JAX$rM-$9$kM-5!!?L55!J#9gKl$N3+H/$H%V%?%N!<%k!??eJ,N%FC@-(B
(NAIST) $B!{(B($B3X(B)$B2CF#(B $BOBM5(B $B!&(B (RITE) ($B@5(B)$BCfB<(B $B5*H~Be(B $B!&(B ($B@5(B)$B9CHe(B $B>HI'(B $B!&(B ($B@5(B)$BIw4V(B $B?-8c(B $B!&(B ($B@5(B)$BF#2,(B $BM40l(B
butanol
membrane
pervaporation
4-a611
15:00$B!A(B 15:20E119$B%$%*%s1UBN4^?;B%?JM"AwKl$K$h$k%W%m%Q%s(B/$B%W%m%T%l%s$NJ,N%(B
($B?@8MBg1!9)(B) $B!{(B($B3X(B)$B6pC+(B $BD>5#(B $B!&(B ($B@5(B)$B;{K\(B $B@5L@(B $B!&(B ($B@5(B)$B?@Hx(B $B1Q<#(B $B!&(B ($B@5(B)$B@P?@(B $BE0(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)$B>>;3(B $B=(?M(B
supported liquid membrane
facilitated transport
ionic liquid
4-a329
(15:20$B!A(B16:40)$B!!(B($B:BD9(B $B6b;X(B $B@58@(B)
15:20$B!A(B 15:40E120$BAB?e@-9bL)EYHsB?9&
($B@iMU;:5;8&(B) $B!{(B($B@5(B)$B5\>k(B $B=_(B $B!&(B ($B?)Am8&(B) ($B@5(B)$BFiC+(B $B9@;V(B $B!&(B ($BC^GHBg(B) ($B@5(B)$BCfEh(B $B8wIR(B
PDMS-based dense membrane
permeability
regular solution model
4-a403
15:40$B!A(B 16:00E121$B%"%_%s1UBNKl$K$h$k6u5$Cf$NFs;@2=C:AG2s<}(B
($BEl9)Bg1!M}9)(B) Pinyarat Jindaratsamee $B!&(B ($B@5(B)$B2<;3(B $BM52p(B $B!&(B $B!{(B($B@5(B)$B0KEl(B $B>O(B
liquid membrane
carbon dioxide
amine
4-a474
16:00$B!A(B 16:20E122$B%]%j%$%_%IKl$K$h$kMO:^$N9bC&?e@:@=(B
($BF|2=5!(B) $B!{(B($B@5(B)$BFs5\(B $B9/J?(B
high-purified solvent
azeotropic distillation
nitorogen recycle parge
4-a515
16:20$B!A(B 16:40E123TEP Trap$BKl$rMQ$$$?3$?eC8?e2=A0=hM}K!$N3+H/(B
($B=;M'EE9)(B) $B!{(B($B@5(B)$BGp86(B $B=( $B!&(B $BJlAR(B $B=$;J(B $B!&(B $BLpGk(B $BAo(B $B!&(B $BCf0f(B $BN6;q(B $B!&(B ($B?@8MBg(B) ($B@5(B)$B>>;3(B $B=(?M(B $B!&(B ($B@5(B)$BBg8~(B $B5H7J(B $B!&(B ($BEl>0f(B $B8x0l(B $B!&(B $B;37A(B $B1Q82(B $B!&(B ($B3$MNBg(B) $B85ED(B $B?50l(B
sea water desalination
pretreatment membrane
TEP
4-a244
E$B2q>l(B $BBh(B2$BF|(B
(9:40$B!A(B11:00)$B!!(B($B:BD9(B $B:#0f(B $B@5D>(B)
9:40$B!A(B 10:00E203CVD$BK!$K$h$k%<%*%i%$%HKl$N2~NI(B
($B.Ln(B $BN5J?(B $B!&(B ($B@5(B)$BLnB<(B $B4490(B
MOR zeolite membrane
post-treatment
water/isopropanol
4-a76
10:00$B!A(B 10:20E204DMDPS$B$r%7%j%+8;$H$7$?%7%j%+Kl$X$N?e>x5$$N1F6A$HKl$N:F@8(B
($B9)3X1!Bg9)(B) $B!{(B($B@5(B)$B@FF#(B $B?r(B $B!&(B ($B@5(B)$B@%2<(B $B2mGn(B $B!&(B ($B@5(B)$B@V>>(B $B7{ $B!&(B ($B@5(B)$BCfHx(B $B??0l(B
silica membrane
membrane reactor
regeneration of membrane
4-a243
10:20$B!A(B 10:40E205SAPO-34$BKl$N9g@.$H>x5$F)2aFC@-(B
($B:eBg1!4p9)(B) $B!{(B($B3X(B)$BW"ED(B $BM:0lO/(B $B!&(B $BEOIt(B $BOB@8(B $B!&(B ($B@5(B)$B9>F,(B $BLw9,(B $B!&(B ($B@5(B)$B@>;3(B $B7{OB(B
zeolite membrane
SAPO-34
water/isopropanol
4-a214
10:40$B!A(B 11:00E206$B?eG.=hM}$r;\$7$?%W%i%:%^MO2A(B
($B>.;39b@l!&J* $B!&(B $BCSED(B $BFF;K(B $B!&(B $B $B!&(B $B@n1[(B $BBgJe(B $B!&(B $BIp(B $B@.>M(B
hydroxyapatite
plasma spraying
hydrothermal treatment
4-a147
(11:00$B!A(B12:00)$B!!(B($B:BD9(B $BLnB<(B $B4490(B)
11:00$B!A(B 11:20E207$B%9%k%[%s2==hM}$r$7$?C:AGKl$NF)2aJ*@-(B
($B;38}Bg1!M}9)(B) $B!{(B($B3X(B)$B@P@n(B $BM598(B $B!&(B ($B3X(B)$BF#0f(B $B7IMN(B $B!&(B ($B3X(B)$BCf:,(B $B7<2p(B $B!&(B ($B@5(B)$BEDCf(B $B0l9((B $B!&(B ($B@5(B)$B4nB?(B $B1QIR(B $B!&(B ($B;0=EBg1!@8J*;q8;(B) ($B@5(B)$BgU2,(B $B@58w(B $B!&(B ($BKL8+9)Bg9)(B) ($B@5(B)$BNkLZ(B $BJY(B
carbon membrane
pervaporation
gas separation
4-a304
11:20$B!A(B 11:40E208Surface modification of PES membrane for antibacterial surface design
(Kobe U.) $B!{(B($B3X(B)Razi F $B!&(B ($B6&(B)Sawada I $B!&(B ($B@5(B)Ohmukai Y $B!&(B ($B@5(B)Maruyama T $B!&(B ($B@5(B)Sotani T $B!&(B ($B@5(B)Matsuyama H
Surface functionalization
HF-PES membrane
Zwitterionic monomer
4-a312
11:40$B!A(B 12:00E209$B%"%k%.%s;@Kl$NJ*
($BF|Bg1!@8J*;q8;(B) $B!{(B($B3X(B)$B2CEg(B $B7IB@(B $B!&(B ($B@5(B)$BF+(B $B7E(B $B!&(B ($B@5(B)$B:#0f(B $B@5D>(B
Membrane
Calcium alginate
Mass transfer
4-a677
E$B2q>l(B $BBh(B3$BF|(B
(10:00$B!A(B11:00)$B!!(B($B:BD9(B $B@V>>(B $B7{
10:00$B!A(B 10:20E304$B%j%s;i
($B?@8MBg1!9)(B) $B!{(B($B3X(B)$B@>3@Fb(B $B=$(B $B!&(B (-) $BFs8.C+(B $BN<(B $B!&(B ($B?@8MBg1!9)(B) ($B@5(B)$BBg8~(B $B5H7J(B $B!&(B ($B@5(B)$B@P?@(B $BE0(B $B!&(B ($B@5(B)$B?@Hx(B $B1Q<#(B $B!&(B ($B@5(B)$B4];3(B $BC#@8(B $B!&(B ($B@5(B)$B>>;3(B $B=(?M(B
Membrane fouling
Phospholipid polymer
Dip coating
4-a300
10:20$B!A(B 10:40E305$B8r8_5[CeK!$rMQ$$$?(BRO$BKl$NI=LL2~
($B?@8MBg1!9)(B) $B!{(B($B3X(B)$BE7Ln(B $BK.><(B $B!&(B ($B@5(B)$BBg8~(B $B5H7J(B $B!&(B ($B@5(B)$B@P?@(B $BE0(B $B!&(B ($B@5(B)$B?@Hx(B $B1Q<#(B $B!&(B ($B@5(B)$B4];3(B $BC#@8(B $B!&(B ($B@5(B)$B>>;3(B $B=(?M(B
RO membrane
Layer-by-layer
surface modification
4-a315
10:40$B!A(B 11:00E306AFM$B$*$h$S(BQCM-D$B$rMQ$$$?%?%s%Q%/
($B?@8MBg1!9)(B) $B!{(B($B3X(B)$BJ?8+(B $B7 $B!&(B ($B002=@.%1%_%+%k%:(B) $B66Ln(B $B>;G/(B $B!&(B ($B@5(B)$B5WJ]ED(B $B>:(B $B!&(B ($B?@8MBg1!9)(B) ($B@5(B)$BBg8~(B $B5H7J(B $B!&(B ($B@5(B)$B@P?@(B $BE0(B $B!&(B ($B@5(B)$B?@Hx(B $B1Q<#(B $B!&(B ($B@5(B)$B4];3(B $BC#@8(B $B!&(B ($B@5(B)$B>>;3(B $B=(?M(B
Membrane fouling
Protein adsorption
Adhesion force
4-a379
(11:00$B!A(B12:00)$B!!(B($B:BD9(B $BCfB<(B $B0lJf(B)
11:00$B!A(B 11:20E307$B?e=hM}Kl$N%U%!%&%j%s%0@)8f$K8~$1$?I=LL2~
($BElKLBgL$Mh%;(B) $B!{(B($B@5(B)$BFn1@(B $BN<(B $B!&(B ($BElKLBg1!9)(B) ($B@5(B)$B;01:(B $BN4<#(B $B!&(B ($BElKLBgL$Mh%;(B) $BNkLZ(B $B0&(B $B!&(B ($BElKLBg1!9)(B) ($B@5(B)$BDZ0f(B $B=(9T(B $B!&(B ($B@5(B)$BH+;3(B $BK>(B $B!&(B ($B@5(B)$B1sF#(B $BL@(B $B!&(B ($B@5(B)$B9b1)(B $BMN=<(B $B!&(B ($B@5(B)$B5WJ](B $BI4;J(B $B!&(B ($BElKLBgL$Mh%;(B/$BElKLBg1!9)(B) ($B@5(B)$B5\K\(B $BL@(B
fouling
membrane
surface modifier
4-a319
11:20$B!A(B 11:40E308$B?e$N%_%/%m9=B$$KCeL\$7$?%U%!%&%j%s%0M^@)Kl$N3+H/(B
($B9)3X1!Bg9)(B) $B!{(B($B@5(B)$B@V>>(B $B7{ $B!&(B $B4Z(B $BK'(B $B!&(B $B;0?9(B $B7 $B!&(B ($B@5(B)$BCfHx(B $B??0l(B
fouling
wastewater treatment
water molecule
4-a635
11:40$B!A(B 12:00E309$B<>=a$7$?AB?e@-(BPTFE$B%U%#%k%?!<%a%s%V%l%s$N4%$->r7o$N8!F$(B
($BF|K\%]!<%k(B) $B!{(B($B@5(B)$BDM:j(B $BOB@8(B $B!&(B ($B@5(B)$B>B8}(B $BE0(B $B!&(B $BW"@%(B $BAo(B
PTFE membrane
dewetting
adhesive nergy
4-a348

(13:00$B!A(B14:00)$B!!(B($B:BD9(B $B9b1)(B $BMN=<(B)
13:00$B!A(B 13:20E313$B?];@$N%(%9%F%k2=$NKlH?1~4o$K$*$1$kH?1~5sF0$N2r@O(B
($BAaBgM}9)(B) ($B@5(B)$B>>J}(B $B@5I'(B $B!&(B $B!{(B($B3X(B)$BJ?0f(B $BB@0lO/(B $B!&(B ($B@5(B)$B4X:,(B $BBY(B $B!&(B ($B@5(B)$B5FCO(B $B1Q0l(B
membrane reactor
esterification
simulation
4-a546
13:20$B!A(B 13:40E314$B%$%*%s8r49Kl$rMQ$$$?%h%&2=?eAGG;=L$K$*$1$kM"N($N29EY0MB8@-(B
($B86;RNO5!9=(B) $B!{(B($B@5(B)$BEDCf(B $B?-9,(B $B!&(B $BH,4,(B $BE0Li(B $B!&(B $B@uLn(B $B2m=U(B $B!&(B $BA0@n(B $B9/@.(B $B!&(B ($B@5(B)$B>.4S(B $B70(B
Cation exchange membrane
Hydriodic acid
transport number
4-a419
13:40$B!A(B 14:00E315$B<+F0t1UCf$N%(%^%k%7%g%sL}J,=|5n$K$*$1$k%/%m%9%U%m!<$m2a$N8!F$(B
($BF|K\%]!<%k(B) $B!{(B($B@5(B)$BFqGH(B $BC]Va(B $B!&(B ($B@5(B)$BEOn5(B $B;KIp(B $B!&(B ($B@5(B)$BDM:j(B $BOB@8(B $B!&(B $BW"@%(B $BAo(B $B!&(B ($B@5(B)$B>B8}(B $BE0(B
Parts washing fluid
Emulsified oil removal
Cross flow filtration
4-a459
(14:00$B!A(B15:00)$B!!(B($B:BD9(B $BEDCf(B $B?-9,(B)
14:00$B!A(B 14:20E316$B>J%(%M%k%.!<1?E>$rL\E*$H$7$?Kl$m2a%7%_%e%l!<%?$N3+H/(B
($B2#9qBg9)(B) $B!{(B($B@5(B)$BCfB<(B $B0lJf(B $B!&(B $BLpLn(B $BM*B@(B $B!&(B ($B@5(B)$B?7ED8+(B $B6)(B $B!&(B ($B@5(B)$B>>K\(B $B44<#(B
energy saving
filtration
fouling
4-a649
14:20$B!A(B 14:40E3173D Modeling and Simulation of a Hollow fiber Membrane Module for IPA Purification from Water
(AIST) $B!{(B($B@5(B)Caravella Alessio $B!&(B ($B@5(B)Hara Shigeki $B!&(B ($B@5(B)Haraya Kenji $B!&(B ($B@5(B)Yoshimune Miki
hollow fiber membrane
membrane module
modeling
4-a5
14:40$B!A(B 15:00E318$B%j%A%&%`6u5$Fs
($BElKLBg1!9)(B) $B!{(B($B@5(B)$B9b1)(B $BMN=<(B $B!&(B $B2<(B $BCRH~(B $B!&(B ($BElKLBgL$Mh%;(B) ($B@5(B)$BFn1@(B $BN<(B $B!&(B ($BElKLBg1!9)(B) ($B@5(B)$B;01:(B $BN4<#(B $B!&(B ($BElKLBgL$Mh%;(B) $BNkLZ(B $B0&(B $B!&(B ($BElKLBg1!9)(B) ($B@5(B)$BDZ0f(B $B=(9T(B $B!&(B ($B@5(B)$BH+;3(B $BK>(B $B!&(B ($B@5(B)$B1sF#(B $BL@(B $B!&(B ($B@5(B)$B5WJ](B $BI4;J(B $B!&(B ($BElKLBgL$Mh%;(B/$BElKLBg1!9)(B) ($B@5(B)$B5\K\(B $BL@(B
lithium ion battery
separator
simulation
4-a727
F$B2q>l(B $BBh(B1$BF|(B
(9:00$B!A(B10:00)$B!!(B($B:BD9(B $B;0C+(B $BCN@$(B)
9:00$B!A(B 9:20F101$B%;%k%m!<%97O5[Ce:^$K$h$k6b$N5[Ce!&2s<}(B
($B:42lBg(B) $B!{(B($B@5(B)$B0f>e(B $B>!Mx(B $B!&(B Pangeni Bimala $B!&(B ($B:42lBg1!(B) $B0$It(B $BL-(B $B!&(B ($B@5(B)$B@n4nED(B $B1Q9'(B $B!&(B ($B@5(B)$BBgEO(B $B7<2p(B $B!&(B ($B%G%s%=!<(B) $B0/H~(B $B6ULi(B $B!&(B $BARED(B $BL-(B
$B%;%k%m!<%9(B
$B6b(B
$B5[Ce(B
4-e197
9:20$B!A(B 9:40F102$B1vE:Ce%a%=%]!<%i%9C:AG:`NA$ND4@=$H$=$N?e>x5$5[CeFC@-(B
($BFAEgBg1!9)(B) $B!{(B($B3X(B)$BCf86(B $BBgJe(B $B!&(B $BD9C+@n(B $BBsKa(B $B!&(B ($B@5(B)$BKY2O(B $B=S1Q(B $B!&(B ($B@5(B)$B2CF#(B $B2mM5(B
water vapor adsorption
mesoporous carbon
calcium chloride
4-e134
9:40$B!A(B 10:00F103$B%a%=%]!<%i%9C:AG:`NA$N?e>x5$5[CeFC@-(B
($BFAEgBg1!9)(B) $B!{(B($B@5(B)$BKY2O(B $B=S1Q(B $B!&(B (Queensland U.) Do D. D.
mesoporous carbon
water vapor adsorption
adsorption model
4-e136
(10:00$B!A(B11:00)$B!!(B($B:BD9(B $BKR(B $BBYJe(B)
10:00$B!A(B 10:20F104$BCbAG4^M-B?9&x5$5[CeFC@-(B
($BFAEgBg1!9)(B) $B!{(B($B3X(B)$B:dHx(B $BNQ9,(B $B!&(B ($B@5(B)$BKY2O(B $B=S1Q(B $B!&(B ($B@5(B)$B2CF#(B $B2mM5(B $B!&(B ($B4X@>Bg4D6-ET;T9)(B) ($B@5(B)$BNS(B $B=g0l(B
nitrogen dope
porous carbon
water vapor adsorption
4-e135
10:20$B!A(B 10:40F105$B9b3h@-%RAG5[Ce:^$K$h$k0!%R;@5Z$S%R;@$N5[Ce5sF0(B
($BEl5~9b@l(B) $B!{(B($B3X(B)$B9>;3(B $BM@><(B $B!&(B ($B@5(B)$B;0C+(B $BCN@$(B $B!&(B ($B%/%l%"%F%i(B) $BLxED(B $BM'N4(B $B!&(B $B9>(B $BMT=!(B
arsenic
adsorption
ferrihydrite
4-e18
10:40$B!A(B 11:00F106$BO"7k5e>u9&$rM-$9$kCj=P:^FbJq%^%$%/%m%+%W%;%k$rMQ$$$k0!1t$N%+%i%`J,N%FC@-(B
($B5\:jBg9)(B) $B!{(B($B@5(B)$B1v@9(B $B900lO:(B $B!&(B ($B3X(B)$B>>2<(B $BL@F|9a(B $B!&(B ($B@5(B)$B??(B $BN4;V(B $B!&(B ($BET>k9b@l(B) ($B@5(B)$B@6;3(B $B;KO/(B $B!&(B ($B;90(B
microcapsules
column separation
extractant
4-e663
(11:00$B!A(B12:00)$B!!(B($B:BD9(B $BKY2O!!=S1Q(B)
11:00$B!A(B 11:20F107$B3*$d3$O7$N3L$rMxMQ$7$?%l%"%a%?%k$N9bA*BrE*J,N%:`$N3+H/$H$=$N1~MQ(B
($B5\:jBg(B) $B!{(B($B@5(B)$B8MED(B $B>-;J(B $B!&(B ($B@5(B)$BBgEg(B $BC#Li(B $B!&(B ($B@5(B)$BGO>l(B $BM3@.(B
Rare Metal
Chitosan
Electronic wastes
4-e735
11:20$B!A(B 11:40F108$BB?9&
($B5~Bg1!9)(B) $B!{(B($B@5(B)$BKR(B $BBYJe(B $B!&(B ($B5~Bg1!CO4D(B) ($B3X(B)$BB $B!&(B ($B5~Bg1!9)(B) ($B@5(B)$BA0(B $B0lW"(B
Iron oxide
Sulfur Dioxide Removal
Hydrogen Sulfide Removal
4-e425
11:40$B!A(B 12:00F109Preparation of calcium ion-exchanged carbon cryogel as adsorbent for desulfurization
(AIST) $B!{(B($B@5(B)Thongprachan Napawon $B!&(B ($B@5(B)Yamamoto Takuji $B!&(B ($B@5(B)Ohmori Takao $B!&(B ($B@5(B)Endo Akira
carbon adsorbent
ion-exchange
packed-bed breakthrough curve
4-e165

(13:00$B!A(B14:00)$B!!(B($B:BD9(B $B;01:!!??0l(B)
13:00$B!A(B 13:20F113$B%W%l!<%H%l%C%H%+!<%\%s%J%N%U%!%$%P!<$N4T85@-%,%9$N5[Ce$KH<$&EE5$Dq93JQ2=(B
($BElBg@88&(B) $B!{(B($B3X(B)$BEr;3(B $B7rB@O:(B $B!&(B ($B3X(B)$B9b66(B $BM&2p(B $B!&(B ($B@5(B)$BF#ED(B $BMN?r(B $B!&(B ($B@5(B)$BF#0f(B $BN4IW(B $B!&(B ($B@5(B)$BGwED(B $B>O5A(B
carbon nanofiber
gas sensor
reductive gas
4-e354
13:20$B!A(B 13:40F114$B%U%'%N!<%k(B-$B%a%i%_%s
($B4X@>Bg4D6-ET;T9)(B) $B!{(B($B@5(B)$BNS(B $B=g0l(B $B!&(B $BEhH*(B $BAa5*(B $B!&(B $BA0_7(B $BLP7{(B $B!&(B $BEDCf(B $B>MB@O:(B $B!&(B ($B@5(B)$B<<;3(B $B>!I'(B
activated carbon
adsorption
chemical activation
4-e467
13:40$B!A(B 14:00F115$BLR=!C]$+$i$NJ,;R$U$k$$%+!<%\%s$ND4@=$H%P%$%*%,%9J,N%(BPSA$B$X$N1~MQ(B
($BElBg@88&(B) $B!{(B($B3X(B)$B3T(B $B;VD6(B $B!&(B ($B@5(B)$BF#ED(B $BMN?r(B $B!&(B ($B@5(B)$BF#0f(B $BN4IW(B $B!&(B ($B@5(B)$BGwED(B $B>O5A(B
bamboo charcoal
molecular sieve carbon
PSA
4-e359
(14:00$B!A(B15:00)$B!!(B($B:BD9(B $B1v@9(B $B900lO:(B)
14:00$B!A(B 14:20F116$B%U%j!<%:%I%i%$%2%kK!$K$h$k%P%$%b!<%@%k%7%j%+B?9&BN$N:n@=(B
($B $B!&(B ($B@5(B)$BLnB<(B $B4490(B
ice templating
dry gel conversion
bimodal porous silica
4-e77
14:20$B!A(B 14:40F117$BAjJQ2=J*
($BElBg@88&(B) $B!{(B($B3X(B)$BLn4V(B $BM:FsO/(B $B!&(B ($B@5(B)$BF#ED(B $BMN?r(B $B!&(B ($B@5(B)$BF#0f(B $BN4IW(B $B!&(B ($B@5(B)$BGwED(B $B>O5A(B
pressure swing adsorption
mesoporous silica
phase changing materials
4-e547
14:40$B!A(B 15:00F118PVSA$BK!$K$h$k%*%l%U%#%sG;=L!&2s<}%W%m%;%9$N3+H/(B
($B?@8M@=9]=j(B) $B!{(B($B@5(B)$B>>2,(B $BN<(B $B!&(B ($B@5(B)$B;01:(B $B??0l(B $B!&(B ($B?@9]%j%5!<%A(B) ($B@5(B)$BCfHx(B $B>:(B
PVSA
olefin
enrichment
4-e699
(15:00$B!A(B16:00)$B!!(B($B:BD9(B $BNS(B $B=g0l(B)
15:00$B!A(B 15:20F119NRTL$B<0$rMQ$$$FF3=P$7$?6u9&MO1U%b%G%k$K$h$k5[CeJ?9U$NAj4X(B
($B=)EDBg(B) $B!{(B($B@5(B)$B=!A|(B $B7r;0(B
NRTL
adsorption equilibrium
4-e485
15:20$B!A(B 15:40F120$B7W;;2=3X
($BElKLBg9)(B) $B!{(B($B3X(B)$B0KF#(B $BC$FA(B $B!&(B ($BElKLBg1!9)(B) $B>.NS(B $BBg(B $B!&(B ($BElKLBgL$Mh%;(B) ($B@5(B)$BFn1@(B $BN<(B $B!&(B ($BElKLBg1!9)(B) ($B@5(B)$B;01:(B $BN4<#(B $B!&(B ($BElKLBgL$Mh%;(B) $BNkLZ(B $B0&(B $B!&(B ($BElKLBg1!9)(B) ($B@5(B)$BDZ0f(B $B=(9T(B $B!&(B ($B@5(B)$BH+;3(B $BK>(B $B!&(B ($B@5(B)$B1sF#(B $BL@(B $B!&(B ($B@5(B)$B9b1)(B $BMN=<(B $B!&(B ($B@5(B)$B5WJ](B $BI4;J(B $B!&(B ($BElKLBgL$Mh%;(B/$BElKLBg1!9)(B) ($B@5(B)$B5\K\(B $BL@(B
zwitterionic material
biocompatibility
simulation
4-e236
15:40$B!A(B 16:00F121$B%;%k%i!<%<$N%;%k%m!<%9$X$N5[CeB.EY$HE|2=$X$N1F6A(B
($BElBg@88&(B) $B!{(B($B3X(B)$B=)K\(B $B2B4u(B $B!&(B ($B@5(B)$BF#ED(B $BMN?r(B $B!&(B ($B@5(B)$BF#0f(B $BN4IW(B $B!&(B ($B@5(B)$BGwED(B $B>O5A(B
cellulose hydrolysis
cellulase adsorption
rate limitaiton
4-e331
(16:00$B!A(B17:20)$B!!(B($B:BD9(B $B:4!9LZ!!K~(B)
16:00$B!A(B 16:20F122$B%P%$%*%^%9?eG.=hM}1U$+$i$N%R%I%m%-%7%a%A%k%U%k%U%i!<%k(B(HMF)$B$NAF5[CeJ,N%$H%]%j%^!<9g@.(B
($BElBg@88&(B) $B!{(B($B3X(B)$B@t(B $B5.90(B $B!&(B ($B@5(B)$BF#ED(B $BMN?r(B $B!&(B ($B@5(B)$BF#0f(B $BN4IW(B $B!&(B $B1|;3(B $B8w:n(B $B!&(B $BH*Cf(B $B8&0l(B $B!&(B ($B@5(B)$BGwED(B $B>O5A(B
5-hydroxymethylfurfural
bis-hydroxymethylfuran
polymerization
4-e350
16:20$B!A(B 16:40F123$B;@2=J*%J%NN3;R$NAj4V0\F0$KH<$&AjJ?9UJQ2=(B
($BFAEgBg1!9)(B) $B!{(B($B3X(B)$BA03@(B $B5.9((B $B!&(B $BLZFb(B $BM4B@(B $B!&(B ($B@5(B)$BKY2O(B $B=S1Q(B $B!&(B ($B@5(B)$B2CF#(B $B2mM5(B
nano particle
phase transfer
equilibrium
4-j133
16:40$B!A(B 17:00F124$BMO2rEY%Q%i%a!<%?(B(SP$BCM(B)$B$rMQ$$$?%H%&%,%i%7$+$i$N%+%W%5%$%7%s$NJ,N%@-I>2A$*$h$S9b=cEY2=(B
($B4X@>Bg4D6-ET;T9)(B) $B!{(B($B3X(B)$BCf@>(B $BN $B!&(B $BJ?Ln(B $BCR;R(B $B!&(B ($B4X@>Bg4D6-ET;T(B) $BJ!Eg(B $B@6H~(B $B!&(B ($B@5(B)$B;3K\(B $B=(
Capsaicin
Extraction
Solubility Parameter
4-i296
17:00$B!A(B 17:20F125$BM6EE1KF0$K$h$k1UBNCfJ,;6N3;R$NJ,N%$K$D$$$F(B:$B:?>u6E=8$N1F6A(B
($B5~Bg1!9)(B) $B!{(B($B@5(B)$B:4Ln(B $B5*>4(B $B!&(B ($B@5(B)$BCS;3(B $BM52p(B $B!&(B ($B@5(B)$BEDLg(B $BH%(B
dielectrophoresis
particle
separation
4-i154
F$B2q>l(B $BBh(B2$BF|(B
(9:00$B!A(B10:00)$B!!(B($B:BD9(B $B>>ED(B $B7=8g(B)
9:00$B!A(B 9:20F201$B<+8J>x5$05=LK!$K$h$k9b8zN(>xN1?e@=B$AuCV(B
($B8D?M(B) $B!{(B($B@5(B)$BC]ED(B $B@?0l(B
Vapor compression
efficient distillation
plate exchanger
4-c100
9:20$B!A(B 9:40F202$B05NOJ,I[$rMxMQ$7$?>xN1%7%9%F%`(B(1)$B!!(B-$B4pK\E*9=@.(B-
($BFAEgBg1!(BSTS$B8&(B) $B!{(B($B@5(B)$B30NX(B $B7r0lO:(B $B!&(B ($BFAEgBg9)(B) $BM'@.(B $B4nBeH~(B $B!&(B ($BFAEgBg1!@hC<650iIt(B) $BJ!?9(B $B9'E5(B $B!&(B ($BFAEgBg9)(B) $BCf_7(B $B9'B@(B $B!&(B ($BFAEgBg1!@hC<650iIt(B) ($B3X(B)$B@uED(B $B9,M4(B $B!&(B ($BJ!=wBg?M4V4D6-(B) ($B@5(B)$BApJI(B $B9n8J(B $B!&(B ($BFAEgBg1!(BSTS$B8&(B) ($B@5(B)$B?y;3(B $BLP(B $B!&(B ($B@5(B)$BCf@n(B $B7I;0(B
pressure
distillation
energy
4-c740
9:40$B!A(B 10:00F203$B05NOJ,I[$rMxMQ$7$?>xN1%7%9%F%`(B(2)$B!!(B-$B=>MhK!$H$NHf3S(B-
($BFAEgBg1!@hC<650iIt(B) $B!{(B($B3X(B)$B@uED(B $B9,M4(B $B!&(B ($BFAEgBg1!(BSTS$B8&(B) ($B@5(B)$B30NX(B $B7r0lO:(B $B!&(B ($B@5(B)$B?y;3(B $BLP(B $B!&(B ($B@5(B)$BCf@n(B $B7I;0(B
pressure
distillation
energy
4-c743
(10:00$B!A(B11:00)$B!!(B($B:BD9(B $B?9(B $B=(
10:00$B!A(B 10:20F2043$B@.J,7O>xN15;=Q$NJ,N%FC@-$H>J%(%M%k%.!2A(B
($B4X@>2=3X(B) $B!{(B($B@5(B)$BJR2,(B $BK.IW(B $B!&(B ($B@5(B)$BLnED(B $B=(IW(B $B!&(B ($B@5(B)$B;3O)(B $B42;J(B $B!&(B ($B@5(B)$B8~ED(B $BCi90(B $B!&(B ($B@5(B)$BARC+(B $B?-9T(B $B!&(B ($B@5(B)$B6bED(B $BK|J?(B
3-component Distillation
HIDiC
DWC
4-c2
10:20$B!A(B 10:40F205$B%R!<%H%]%s%W%"%7%9%H$K$h$k%P%C%A>xN1$N>J%(%M%k%.!<2=(B
($B;37ABg1!M}9)(B) ($B3X(B)$BNkLZ(B $BBYI'(B $B!&(B ($B3X(B)$B;3LZ(B $BM:Bg(B $B!&(B ($B3X(B)$BF#Hx(B $BE/@8(B $B!&(B $B!{(B($B@5(B)$B>>ED(B $B7=8g(B $B!&(B ($B;:Am8&(B) ($B@5(B)$BCf4d(B $B>!(B $B!&(B ($B;37ABg1!M}9)(B) ($B@5(B)$B9b66(B $B9,;J(B $B!&(B ($B4X@>2=3X(B) ($B@5(B)$BJR2,(B $BK.IW(B
Batch distillation
HIDiC
Energy saving
4-c201
10:40$B!A(B 11:00F206Synthesis of optimal distillation sequences with heat integration and compressor addition using multiobjective optimization
(Kyoto U.) $B!{(B($B3X(B)Alcantara-Avila J. R. $B!&(B ($B@5(B)Kano M. $B!&(B ($B@5(B)Hasebe S.
Heat integration
Compressor addition
Multiobjective optimization
4-c148
(11:00$B!A(B12:20)$B!!(B($B:BD9(B $B30NX(B $B7r0lO:(B)
11:00$B!A(B 11:20F207$B%J%,%*%+!!%Q%C%-%s%0!V%9!<%Q!<(BH$B%Q%C%/!W(B2$BG\$N=hM}NL$rC#@.$9$k5,B'=
($B>xN1MQ5,B'=
Linear Flow
High Operating Capacity
High Liquid Hold
4-c283
11:20$B!A(B 11:40F208$B%5%$%I%+%C%H$r;}$D>xN1%W%m%;%9$NJ,N%FC@-(B
($BL>9)Bg(B) $B!{(B($B@5(B)$B?9(B $B=( $B!&(B ($B3X(B)$BAa@n(B $BN5;J(B $B!&(B ($B@5(B)$B4dED(B $B=$0l(B $B!&(B $B:#0f(B $BBgJe(B $B!&(B ($B7
Petlyuk Process
Dividing Wall Column
Separation Characteristics
4-c199
11:40$B!A(B 12:00F209$B>xN1Ec$K$*$1$kHtKwF1H<$N5sF0(B
($BElM}Bg(B) $B!{(B($B@5(B)$BBg9>(B $B=$B$(B
distillation
entrainment
efficiency
4-c492
12:00$B!A(B 12:20F210$BxN1Ec$N35G0!"M}O@$J$i$S$K9)6H2=;X?K(B
($BF|4x(B) $B!{(B($B@5(B)$BCf;3(B $B6,(B
Drops dispersion
Multiple gas-liquid contact
Distillation column
21-b180
F$B2q>l(B $BBh(B3$BF|(B
(10:00$B!A(B11:00)$B!!(B($B:BD9(B $B>>K\F;L@(B)
10:00$B!A(B 10:20F304$B%"%k%-%k:?$rF3F~$7$?AB?e2=4^CbAGB?:BG[0L;R$h$k=E6bB0J,N%(B
($BEl9)Bg86;RO'8&(B) $B!{(B($B@5(B)$BC]2<(B $B7rFs(B $B!&(B $BO!(B $BN $B!&(B ($BEl9)Bg%=%k!<%7%g%s5!9=(B) $B0pMU(B $BM%2p(B
extraction
nitrogen donor
hydrophobic ligand
4-f742
10:20$B!A(B 10:40F305$BN22+86;R$H;@AG86;R$rM-$9$k9bJ,;R7?Cj=P:^$N9g@.$HF<$NCj=PJ?9U(B
($BET>k9b@l(B) $B!{(B($B@5(B)$B4d7'(B $BH~F`;R(B $B!&(B ($B5\:jBg9)(B) ($B@5(B)$BGO>l(B $BM3@.(B
extraction
equilibrium
4-f739
10:40$B!A(B 11:00F306$B%$%*%s1UBN$rMQ$$$?4uEZN`6bB0$NCj=PJ,N%$H$=$N1~MQ(B
($B6eBg1!9)(B) $B!{(B($B3X(B)$BGO>l(B $BM:;0(B $B!&(B $B2 $B!&(B ($B@5(B)$B5WJ]ED(B $BIY@8;R(B $B!&(B ($B86;RNO5!9=(B) ($B@5(B)$B2<>r(B $B98;JO:(B $B!&(B ($B6eBg1!9)(B) ($B@5(B)$B?@C+(B $BE5Jf(B $B!&(B ($B@5(B)$B8eF#(B $B2m9((B
rare earth metals
ionic liquid
liquid membrane
4-f240
(11:00$B!A(B12:00)$B!!(B($B:BD9(B $B4d7'(B $BH~F`;R(B)
11:00$B!A(B 11:20F307$B@PL}7OJ,2rL}$N1U1UCj=P(B
($BEl9)Bg1!M}9)(B) $B!{(B($B@5(B)$B$O$P$-(B $B9-82(B $B!&(B ($B3X(B)$B5\yu(B $BOBN<(B $B!&(B ($B@5(B)$B9>F,(B $BN50l(B
Liquid-liquid equilibrium
Cracked kerosene
Aromatic recovery
4-f783
11:20$B!A(B 11:40F308$B1U!98~N.7?1s?4Cj=PAuCV$NO"B3Cj=PA`:n$K$*$1$kL}?eN.F0FC@-(B
($BEl9)Bg86;RO'8&(B) $B!{(B($B3X(B)$BbCJI(B $BN<;J(B $B!&(B ($B@5(B)$BC]2<(B $B7rFs(B $B!&(B $B9b66(B $B=(<#(B $B!&(B $BLZAR(B $B9(@.(B
extraction
centrifugal extractor
Taylor-Couette flow
4-f715
11:40$B!A(B 12:00F309$B?e(B-$B%Y%7%/%k4V$N%$%*%s1UBN$NJ,G[J?9U(B
($BF1;V $B!&(B ($B@5(B)$B>>K\(B $BF;L@(B $B!&(B ($B@5(B)$B6aF#(B $BOB@8(B
ionic liquid
vesicle
distribution
4-f69

(13:00$B!A(B14:00)$B!!(B($B:BD9(B $BEDCf(B $B9'L@(B)
13:00$B!A(B 13:20F313$B%?%s%Q%/
($BKLBg1!?e(B) $B!{(B($B3X(B)$BN-(B $B3>(B $B!&(B ($B@5(B)$B4X(B $B=(;J(B $B!&(B ($B@5(B)$B4];3(B $B1QCK(B
bioflocculant
kanto loam
kaolin
4-b71
13:20$B!A(B 13:40F314$B%?%s%Q%/
($BKLBg1!?e(B) $B!{(B($B@5(B)$B4X(B $B=(;J(B
bioflocculant
food processing wastewater
soy milk
4-b72
13:40$B!A(B 14:00F315$BJ?KlAuCV$NF0FC@-$HKl4V:905$N4X78(B
($B%/%\%?(B) $B!{(B($B@5(B)$B>eCf(B $BE/Li(B $B!&(B $BEZK\(B $B@5L@(B $B!&(B $BBl@n(B $B9/?.(B
flat sheet
trans membrane pressure
dynamic characteristics
4-b26
(14:00$B!A(B15:00)$B!!(B($B:BD9(B $BCfAR(B $B1QM:(B)
14:00$B!A(B 14:20F316$BA!0]$m:`$r;H$C$?5^B.$m2a4o$NJa=88zN(1F6A0x;R$N@0M}$H%b%G%k2=(B
($B7*ED9)6H(B) $B!{B?ED(B $B7JFsO:(B $B!&(B $BBg_7(B $B8x?-(B $B!&(B ($BL>Bg1!(B) ($B@5(B)$BDX(B $B=_0lO:(B
rapid filtration
coagulation
modelling
4-b744
14:20$B!A(B 14:40F317$B1_Cl%3%l%/%?!<$KBP$9$k0[2YEE%3%m%$%I:.9g7O$ND@CeB.EY(B
($BC^GHBg1!@84D(B) $B!{(B($B3X(B)$BF|2<(B $BLwG7(B $B!&(B ($B@5(B)$BB-N)(B $BBY5W(B
Colloidal deposition
PDMS microfluidic chamber
Patch effect
4-b594
14:40$B!A(B 15:00F318$B4uGv%3%m%$%I$NA4AK;_7?DjB.@:L)%1!<%/_I2a$K$*$1$kKlJD:I$NI>2A(B
($BL>Bg1!9)(B) $B!{(B($B@5(B)$BJR6M(B $B@?G7(B $B!&(B ($B3X(B)$BC]Cf(B $BL-M*(B $B!&(B ($B@5(B)$BF~C+(B $B1Q;J(B
microfiltration
pore blocking
cake resistance
4-b609
(15:00$B!A(B16:00)$B!!(B($B:BD9(B $B>eCf(B $BE/Li(B)
15:00$B!A(B 15:20F319$BHsBP>N7?%G%W%9%U%#%k%?!<$K$h$kO":?7?:Y6]7|By1U$N@:L)_I2a(B
($B?73cBg(B) ($B@5(B)$B5HED(B $B@/@2(B $B!&(B ($B@5(B)$BC+8}(B $B@5G7(B $B!&(B $B!{(B($B@5(B)$BEDCf(B $B9'L@(B
depth filter
microfiltration
streptobacteria
4-b164
15:20$B!A(B 15:40F320$B%U%m%C%/$N$D$V$l$d%U%m%C%/$N%M%C%H%o!<%/7A@.$,D@9_B.EY$K5Z$\$98z2L(B
($BG@9)8&(B) $B!{(B($B@5(B)$BBg0f(B $B@aCK(B $B!&(B ($B0q>kBgG@(B) $BCf@P(B $B9nLi(B $B!&(B ($B4d.NS(B $B442B(B $B!&(B ($BG@9)8&(B) $BC.20(B $B7 $B!&(B ($B0q>kBgG@(B) $B@FF#(B $BBsLi(B $B!&(B $B?eLn(B $B9'B@O:(B
floc
structure
sedimentation
4-b503
15:40$B!A(B 16:00F321$BI=LLAFEY$,$m2aB.EY$K5Z$\$91F6A(B
($BL>Bg9)(B) $B!{(B($B3X(B)$B0Bc7(B $B>-5.(B $B!&(B ($B3X(B)$B?9ED(B $B2mLi(B $B!&(B $BIpED(B $BNOLo(B $B!&(B ($B3X(B)$B@u0f(B $B0l51(B $B!&(B ($B@5(B)$B?9(B $BN4>;(B $B!&(B ($B@5(B)$BDX(B $B=_0lO:(B
filtration
cakeless
surface roughness
4-b681
(16:00$B!A(B17:00)$B!!(B($B:BD9(B $B4X(B $B=(;J(B)
16:00$B!A(B 16:20F322$BKlLL79
($B;38}Bg1!M}9)(B) $B!{(B($B@5(B)$BCfAR(B $B1QM:(B $B!&(B ($B3X(B)$B66K\(B $B5.M:(B
centrifugation
ultrafiltration
nanoparticle
4-b355
16:20$B!A(B 16:40F323$BE`7kM;2rK!$K$h$k1UCf%J%NN3;R$ND6AFBg2=(B
($BL>Bg1!9)(B) $B!{(B($B3X(B)$B2,ED(B $BOBG7(B $B!&(B ($B@5(B)$BJR6M(B $B@?G7(B $B!&(B ($B@5(B)$BF~C+(B $B1Q;J(B $B!&(B ($B0&I2Bg1!M}9)(B) ($B@5(B)$B@n:j(B $B7rFs(B
freeze-thaw
nanoparticle
solid-liquid separation
4-b606
16:40$B!A(B 17:00F324$BHyN3;R7|By:`NA$N8:05G^BNN3;RN.F0AX4%Ag(B
($B@EBg9)(B) $B!{(B($B@5(B)$BN)85(B $BM:<#(B $B!&(B ($B3X(B)$B5\_7(B $B9nL@(B
fluidized bed
dilute suspension
inert particle
4-h405
$B9V1i%W%m%0%i%`(B
$B2=3X9)3X2q(B $BBh(B76$BG/2q(B ($BEl5~ET>.6b0f;T(B)
(C) 2011 $B8x1W
Most recent update: 2011-03-06 19:49:12
For more information contact $B2=3X9)3X2q(B $BBh(B76$BG/2q(B $BLd$$9g$;78(B
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