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English page

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A201-A225, A301-A309, B201-B225, B301-B304

$B:G=*99?7F|;~!'(B2015-03-05 09:42:37
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A $B2q>l!&Bh(B 2 $BF|(B
(9:00$B!A(B10:20) ($B:BD9(B $B;3yu(B $B=_;J(B)
9:00$B!A(B 9:20A201$BM-5!9=B$5,Dj:^$rMQ$$$:$K9g@.$7$?%Y!<%?7?%<%*%i%$%H$N(BCO2$B5[CeFC@-(B
($B;:Am8&(B) ($B@5(B)$B!{>eB<(B $B2BBg(B$B!&(B $B2(B$B!&(B $BNkLZ(B $BK.IW(B$B!&(B ($B@5(B)$B1sF#(B $BL@(B
porous materials
CO2 capturing
template-free synthesis
4-e633
9:20$B!A(B 9:40A202$B%"%_%s7O8GBN5[<}:`$N(BCO2$B5[CeFC@-$K$*$1$kC4BN$N8z2L(B
(RITE) ($B@5(B)$B!{F#LZ(B $B=_J?(B$B!&(B ($B@5(B)$B;3ED(B $B=(>0(B$B!&(B ($B@5(B)$BM>8l(B $B9nB'(B
Carbon dioxide
Amine
Mesoporous silica
4-e774
9:40$B!A(B 10:00A203$B%"%_%s4^?;7?8GBN5[<}:`$,<($9(BCO2$B5[<}5sF0$NN'B.CJ3,2r@O(B
(RITE) ($B@5(B)$B!{>B8}(B $BNKJ?(B$B!&(B ($B@5(B)$B;3ED(B $B=(>0(B$B!&(B ($B@5(B)$B8eF#(B $BOBLi(B$B!&(B ($B@5(B)$BM>8l(B $B9nB'(B
CO2 absorption
Amine solid sorbent
rate-limiting process
4-e575
10:00$B!A(B 10:20A204$B%<%*%i%$%HC4BN$X$N0l;@2=CbAG$N5[Ce(B
($B:eI\Bg9)(B) ($B@5(B)$B!{0BED(B $B>;90(B$B!&(B ($BB?EDEE5!(B) $B;3Fb(B $B;MO:(B$B!&(B ($B8x32KI;_5!4o8&(B) $B@uLn(B $B=(><(B$B!&(B ($B:eI\Bg9)(B) ($B@5(B)$B2.Ln(B $BGn9/(B
nitrogen monooxide
zeolite

4-e540
10:20$B!A(B 10:40$B5Y7F(B
(10:40$B!A(B12:00) ($B:BD9(B $B0BED(B $B>;90!&>eB<(B $B2BBg(B)
10:40$B!A(B 11:00A206$B=-AGE:Ce3h@-C:$K$h$kET;T%,%9IU=-:^@.J,5[Ce@-G=$NI>2A(B
($BEl5~%,%9(B) ($B@5(B)$B!{Fn(B $BC$;V(B$B!&(B ($B@5(B)$B:#@>(B $B9(FA(B$B!&(B ($B@5(B)$B9b66(B $BE0(B$B!&(B (TGE) $BBg66(B $BL-@8(B
adsorption
activated carbons
odorant
4-e489
11:00$B!A(B 11:20A207$B2aG.?e>x5$$rMQ$$$FD4@=$7$?3h@-C:$K$*$1$kCe?'J*
($BOB2N;39b@lJ*:(B$B!&(B ($BOB2N;39b@l@l962J(B) $B0fC+(B $B??(B$B!&(B ($BOB2N;39b@lJ*$B!&(B $BCf;3(B $BfFB@(B
activated carbon
adsorption
colored substance
4-e358
11:20$B!A(B 11:40A208$BO"B3%/%m%^%H$NJ,N%8zN($N?dDjJ}K!(B
($B;38}Bg(B) ($B@5(B)$B!{?y;3(B $B@,51(B$B!&(B ($B@5(B)$B5HK\(B $BB';R(B$B!&(B ($B@5(B)$B;3K\(B $B=$0l(B
continuous chromatography
separation
productivity
4-e186
11:40$B!A(B 12:00A209$BBg$-$$M[%$%*%s8r49MFNL$rM-$9$k%_%/%mB?9&@-L55!%]%j%^!<5[Ce:^$N3+H/(B
($BAaBgAOB$M}9)(B) ($B@5(B)$B;3:j(B $B=_;J(B$B!&(B ($BAaBg@h?JM}9)(B) ($B@5(B)$B>>J}(B $B@5I'(B$B!&(B (AZMEC) ($B@5(B)$B!{@5ED(B $BIpB'(B$B!&(B ($BAaBg(B) $B>>2,(B $B0lM:(B
Cation Adsorbent
inorganic polymer
radioactive substance
4-e584

(13:00$B!A(B14:00) ($B:BD9(B $B@5ED(B $BIpB'!&F#LZ(B $B=_J?(B)
13:00$B!A(B 13:20A213LiMn2O4/Polypyrrole$BJ#9gEE5$3h@-Kl$rMQ$$$?3$?eCf%j%A%&%`%$%*%s$NA*BrJ,N%(B
($B90A0Bg(B) ($B3$(B)$B!{EN(B $B6G(B$B!&(B ($B90A0Bg?7%(%M!<8&(B) ($B@5(B)$B41(B $B9q@6(B$B!&(B ($BB@86M}9)Bg(B) Hao Xiaogang$B!&(B ($B90A0Bg?7%(%M!<8&(B) ($B@5(B)$B0$I[(B $BN$Ds(B
lithium ion
Electroactive film
Separation
4-e57
13:20$B!A(B 13:40A214$B%(%C%8%j%C%A%+!<%\%s%J%N%U%!%$%P!<$N%]%9%H%7%s%;%7%97?D>7B@)8f$H5[Ce:^$X$N1~MQ(B
($BElBg@8;:5;8&(B) ($B@5(B)$B!{9b66(B $BM&2p(B$B!&(B ($B@5(B)$BF#ED(B $BMN?r(B$B!&(B ($B@5(B)$BGwED(B $B>O5A(B
carbon nanofiber
diameter control
functional groups
4-e513
13:40$B!A(B 14:00A215D2EHAG$B$r%-%c%j%"$H$7$FJq4^$7$?(BPIM$B$K$h$k4uEZN`6bB0$NKlM"Aw(B
($B6eBg1!9)(B) ($B3X(B)$B!{GO>l(B $BM:;0(B$B!&(B ($B@5(B)$B5WJ]ED(B $BIY@8;R(B$B!&(B ($B@5(B)$B?@C+(B $BE5Jf(B$B!&(B (U. Melbourne) Cattrall R. W.$B!&(B Kolev S. D.$B!&(B ($B6eBg1!9)(B) ($B@5(B)$B8eF#(B $B2m9((B
Polymer Inclusion Membrane
Metal Separation
New Extractant
4-e632
(14:00$B!A(B15:00) ($B:BD9(B $B>.?{(B $B?M;|(B)
14:00$B!A(B 14:20A216$B%P%$%*%(%?%N!<%k$NG;=L!&L5?e2=%W%m%;%9$N>J%(%M%k%.!<$N8!F$(B
($B4X@>2=3X(B) ($B@5(B)$B!{JR2,(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 ($BK!(B)$B@>B<(B $B8aNI(B
HIDiC
Azeotropic Distillation
Bioethanol
4-c2
14:20$B!A(B 14:40A217Energy Saving of Single Column DWC for LNG Plant
(Dong-A U.) ($B3$(B)Kim Young Han
Side-rectifier DWC
Compact distillation column
Floating liquefied natural gas plant
4-c4
14:40$B!A(B 15:00A218$B4629AjJ,N%?eMO@-1UBN$N3+H/$*$h$SM=B,(B
(KRI) ($BK!(B)$BC01)(B $B=_(B
temperature-sensitive phase separation
lower critical solution temperature
QSPR
4-i5
15:00$B!A(B 15:20$B5Y7F(B
(15:20$B!A(B16:40) ($B:BD9(B $B9>F,(B $BN50l!&1v@9(B $B900lO:(B)
15:20$B!A(B 15:40A220$BO"7k7?%+%j%C%/%9(B[4]$B%"%l!<%s$K$h$k6bB0$NCj=PJ,N%(B
($B:42lBg1!9)(B) ($B@5(B)$B!{BgEO(B $B7<2p(B$B!&(B ($B3X(B)$B2VED(B $BBsLi(B$B!&(B ($B@5(B)$B?9Dg(B $B??B@O:(B$B!&(B ($B@5(B)$B@n4nED(B $B1Q9'(B
Metal separation
calixarene
alkali and alkali earth metals
4-f520
15:40$B!A(B 16:00A221$BO"B38~N.K"KwJ,N%EcFb0\F08=>]$K4X$9$k?tCM2r@O(B
($B:eBg1!4p9)(B) ($B@5(B)$B!{2,Ln(B $BBYB'(B$B!&(B ($B3X(B)$B9bB<(B $BNK(B$B!&(B ($B3X(B)$B;3K\(B $BBnLi(B$B!&(B ($B@5(B)$B9bLZ(B $BMNJ?(B$B!&(B ($BL>Bg1!9)(B) ($B3X(B)$BJ?;3(B $B44O/(B$B!&(B ($B@5(B)$BFs0f(B $B?8(B$B!&(B ($BL>8E20;T9)8&(B) ($B@5(B)$BLZ2<(B $BIpI'(B$B!&(B ($B6&(B)$B@P3@(B $BM';0(B$B!&(B ($B6&(B)$B$B!&(B ($BL>9)Bg1!9)(B) ($B6&(B)$BKL@n(B $B?5Li(B
foam separation
numerical simulation
fluid flow
4-f383
16:00$B!A(B 16:20A222$BH/8w@-4D>u%l%;%W%?!<$rMQ$$$?6(F1%$%*%s1UBNCj=P7O$N3+H/$HM-326bB08!=P(B
($B86;RNO5!9=(B) ($B@5(B)$B!{2<>r(B $B98;JO:(B$B!&(B $B2,B<(B $B9@G7(B$B!&(B ($B6bBtBgM}(B) $B0fB<(B $B5WB'(B$B!&(B ($B86;RNO5!9=(B) ($B@5(B)$BD9Fl(B $B90?F(B
solvent extraction
ionic liquids
synergistic effect
4-f191
16:20$B!A(B 16:40A223$BF};@$*$h$S(B3-$B%R%I%m%-%7%W%m%T%*%s;@$N(BTOA/TBP$B7O6(F1Cj=P(B
($BF1;V>K\(B $BF;L@(B$B!&(B $BEr@u(B $BN<(B$B!&(B ($B@5(B)$B6aF#(B $BOB@8(B
Extraction
Synergism
Lactic acid
4-f245
(16:40$B!A(B17:20) ($B:BD9(B $B@n4nED(B $B1Q9'(B)
16:40$B!A(B 17:00A224$B7y5$3h@-1xE%$NM-5!;@;:@8$HKl_I2aFC@-$K5Z$\$9GQ?e=hM}>r7o$N1F6A(B
($BL>Bg1!9)(B) ($B@5(B)$B!{JR6M(B $B@?G7(B$B!&(B ($B3X(B)$B;3Fb(B $B0lLi(B$B!&(B ($B@5(B)$BF~C+(B $B1Q;J(B
membrane filtration
anaerobic activated sludge
organic acid
4-b697
17:00$B!A(B 17:20A225$B3h@-1xE%$ND@9_FC@-$K5Z$\$9D62;GH>Hh8z2L(B
($BL>Bg1!9)(B) ($B@5(B)$B!{JR6M(B $B@?G7(B$B!&(B $B@>@n(B $B6);R(B$B!&(B ($B@5(B)$BF~C+(B $B1Q;J(B
settling
reflocculation
activated sludge
4-b687
A $B2q>l!&Bh(B 3 $BF|(B
(9:00$B!A(B10:20) ($B:BD9(B $BEDCf(B $B9'FA!&3Q20(B $B@5?M(B)
9:00$B!A(B 9:20A301$BGS?e=hM}$KMQ$$$kN.F0@-C4BN$N:`
($B0&I2Bg1!M}9)(B) ($B@5(B)$B!{@n:j(B $B7rFs(B$B!&(B ($B4X@>2=9)(B) $BK-ED(B $B1Q><(B
carrier
material
wastewater treatment
4-b680
9:20$B!A(B 9:40A302$BJ?HD7?(BMF$BKl$K$*$1$k%1!<%/AX8|$5$N@)8f(B(3)
($BBg:eEEDLBg(B) ($B@5(B)$B!{9b2,(B $BBgB$(B$B!&(B ($B3X(B)$BCSED(B $BD>$B!&(B ($B6&(B)$BCfED(B $BN<@8(B$B!&(B ($B6&(B)$BE:ED(B $B@2@8(B$B!&(B ($B6&(B)$B?9(B $B9,<#(B
microfiltration membrane
two-phase flow
visualization
4-b792
9:40$B!A(B 10:00A303$B>F7k6bB0%U%#%k%?!<$K$h$k
($BL>Bg9)(B) ($B@5(B)$B!{8~0f(B $B9/?M(B$B!&(B ($B3X(B)$Bjj(B $B3$1m(B$B!&(B ($BBgOB@=f%(B) $B:4F#(B $B9/9T(B
sintered metal filter
bacterial particle
filtration
4-b847
10:00$B!A(B 10:20A304$B9b@-G=J,;65!$rMQ$$$?C:;@%+%k%7%&%`N3;R3IYBK!$K$h$k%U%_%s;@MO1U$N%;%i%_%C%/%9_I2a(B
($B;38}Bg1!M}9)(B) ($B@5(B)$B!{CfAR(B $B1QM:(B$B!&(B ($B3X(B)$B?t0f(B $B?rI'(B$B!&(B ($B3X(B)$B:4F#(B $BBsGO(B
humic acid
calcium ion
high performance dispersion
4-b469
10:20$B!A(B 10:40$B5Y7F(B
(10:40$B!A(B12:00) ($B:BD9(B $B9b2,(B $BBgB$!&8~0f(B $B9/?M(B)
10:40$B!A(B 11:00A306$B%P%$%Q%9_II[$NMxMQ$K$h$k%P%9%1%C%H7?1s?4C&?e5!$NC&1U@-G=$N8~>e(B
($B:eI\Bg1!9)(B) ($B@5(B)$B!{EDCf(B $B9'FA(B$B!&(B $B%.%s%F%#%s(B $B%"%k%S%s(B$B!&(B ($B3X(B)$BJ!;3(B $BN<(B$B!&(B ($B@5(B)$B4dED(B $B@/;J(B
Centrifuge
Filter Medium
Sedimentation
4-b404
11:00$B!A(B 11:20A307$BDc$$EE2YL)EY$rM-$9$k9bJ,;R5[Ce$H(BPSL$BN3;R$N6E=8(B
($BC^GHBg1!@8L?(B) ($B@5(B)$B!{B-N)(B $BBY5W(B$B!&(B ($B3X(B)Feng Lili
Low charge density polyelectrolyte
Briging Flocculation
Ionic strength
4-b165
11:20$B!A(B 11:40A308$BN.BN$rF)2a$7$?Mf@{>u%A%e!<%V$K$h$k%3%m%$%IN3;R$NJ,N%(B
($B:42lBg1!9)(B) ($B@5(B)$B!{@n4nED(B $B1Q9'(B$B!&(B ($B3X(B)$BEDCf(B $BEl5*(B$B!&(B ($B@5(B)$B?9Dg(B $B??B@O:(B$B!&(B ($B@5(B)$BBgEO(B $B7<2p(B$B!&(B ($BJ%LnF+<'4o86NA(B) $BJ%Ln(B $BD>9,(B
coiled tube
colloid
separation
4-b162
11:40$B!A(B 12:00A309$B%2%kJaB*$K$h$k%U%#%k%?!
($BF|K\%]!<%k(B) ($B@5(B)$B3Q20(B $B@5?M(B
gel
filter blocking
blocking model
4-b43
B $B2q>l!&Bh(B 2 $BF|(B
(9:00$B!A(B10:20) ($B:BD9(B $BLnB<(B $B4490(B)
9:00$B!A(B 9:20B201$B:Y9&Fb=
(RITE) ($B@5(B)$B!{GO>l(B $BH~CR;R(B$B!&(B ($B@5(B)$BM>8l(B $B9nB'(B
membrane
hydrogen
permeation
4-a778
9:20$B!A(B 9:40B202$B%H%k%(%s$rMQ$$$?BP8~3H;6H?1~@-G.(BCVD$BK!$K$h$kC:AG=$>~%;%i%_%C%/Kl$N:n@=(B
($B9-Bg9)(B) ($B@5(B)$B!{5H2,(B $BJ~5W(B$B!&(B ($B3X(B)$B;3K\(B $B@54p(B$B!&(B ($B@5(B)$BD9_7(B $B425,(B$B!&(B ($B@5(B)$B6b;X(B $B@58@(B$B!&(B ($B@5(B)$BETN1(B $BL-N;(B
CVD
carbon
ceramic membrane
4-a751
9:40$B!A(B 10:00B203V$B9g6bKl$K$h$kCbAG!&?eAG:.9g%,%9$+$i$N?eAGJ,N%(B
($BJ*:`5!9=(B) ($B@5(B)$B!{@>B<(B $BKS(B$B!&(B ($BNkLZ>&4[(B) $BLZB<(B $B9@N4(B$B!&(B ($BJ*:`5!9=(B) $Bhq(B $B@/1d(B
vanadium
energy carrier
membrane
4-a763
10:00$B!A(B 10:20B204$BBQ05@-$H9bB.(BCO2$BA*BrF)2a@-$rJ;$;;}$D%"%_%N;@%$%*%s1UBN%2%kKl$NAO@=(B
($B?@8MBg1!9)(B/$B@hC$B!&(B Moghadam Farhad$B!&(B ($B3X(B)$B5H=;(B $B0>H~(B$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B
Amino acid ionic liquid
Gel
membrane
4-a799
10:20$B!A(B 10:40$B5Y7F(B
(10:40$B!A(B12:00) ($B:BD9(B $B?@Hx(B $B1Q<#!&86(B $B?-@8(B)
10:40$B!A(B 11:00B206$B%<%*%i%$%H$r=PH/86NA$H$7$FMQ$$$?9b%7%j%+(BCHA$BKl$N9g@.$HJ,N%FC@-(B
($BF|N)B$A%(B) ($BK!(B)$B!{:#:d(B $BNg;K(B$B!&(B ($BK!(B)$BHDAR(B $B@5Li(B$B!&(B ($BK!(B)$BLpLn(B $BOB9((B$B!&(B ($BK!(B)$BF#ED(B $BM%(B$B!&(B ($B;:Am8&(B) ($BK!(B)$BD9C+@n(B $BBY5W(B$B!&(B ($BK!(B)$B0$It(B $B@i;^(B
zeolite
membrane
chabazite
4-a304
11:00$B!A(B 11:20B207$B%^%$%/%mGH2CG.$rMxMQ$7$?(BSAPO-34$BKl9g@.(B
($BEl9)Bg1!M}9)(B) ($B@5(B)$B!{W"ED(B $BM:0lO/(B$B!&(B ($B3X(B)$BEDB<(B $B??8c(B$B!&(B ($B@5(B)$B0KEl(B $B>O(B
zeolite membrane
microwave heating
carbon dioxide separation
4-a291
11:20$B!A(B 11:40B208silicalite-1$BKl$N(Bxylene$B>x5$F)2aJ,N%FC@-$H@.D92aDx(B
($BAaBg@h?JM}9)(B) ($B3X(B)$B!{$B!&(B ($B3X(B)$B6b;R(B $BBsLp(B$B!&(B ($B3X(B)$BHSEg(B $BM%5.(B$B!&(B ($B3X(B)$B8M4,(B $B7=M4(B$B!&(B ($BAaBg@h?JM}9)(B/$BAaBgM}9)Am8&(B/JST-CREST) ($B@5(B)$B>>J}(B $B@5I'(B
silicalite-1 membrane
xylene separation
growth
4-a594
11:40$B!A(B 12:00B209Hansen$BMO2rEY%Q%i%a!<%?$K$h$kAB?e@-%7%j%+Kl$K$*$1$kF)2a@-$N8!F$(B
($B4X@>Bg4DET9)(B) ($B@5(B)$B!{9SLZ(B $BDgIW(B$B!&(B ($B3X(B)$B8"F#(B $BBgN<(B$B!&(B ($B@5(B)$B;3K\(B $B=(
Hansen Solubility Parameter
hydrohobic
silica
4-a148

(13:00$B!A(B15:00) ($B:BD9(B $B6b;R(B $B90>;!&;3ED(B $B=(>0(B)
13:00$B!A(B 13:20B213$BIT:.OB$NMO1U3&LL$rMQ$$$?(BZIF-8$BKl$N:n@=(B
($B;:Am8&(B) ($B@5(B)$B!{86(B $B?-@8(B$B!&(B ($B@5(B)$B5H=!(B $BH~5*(B$B!&(B ($B@5(B)$B:,4_(B $B=(G7(B$B!&(B ($B@5(B)$B86C+(B $B8-<#(B$B!&(B ($B@5(B)$B86(B $B=E$B!&(B ($BEl9)Bg(B) ($B@5(B)$B;38}(B $BLT1{(B
Gas separation membrane
Zeolitic imidazolate framework-8
Propylene/propane separation
4-a716
13:20$B!A(B 13:40B214$B05NOJd=u@5?;F)K!$K$*$1$k1?E>>r7o$,?eF)2a@-G=$KM?$($k1F6A(B
($B?@8MBg1!9)(B/$B@hC$B!&(B ($B@5(B)$B0B@n(B $B@/9((B$B!&(B ($B@5(B)$B9b66(B $BCR51(B$B!&(B ($B@5(B)$B;09%(B $BB@O:(B$B!&(B ($B;38}Bg1!M}9)(B/$B?@8MBg1!9)(B) ($B@5(B)$BHf2E(B $B=<(B$B!&(B ($B?@8MBg1!9)(B/$B@hC>;3(B $B=(?M(B
Pressure assisted osmosis
Hollow fiber membrane
Forward osmosis
4-a580
13:40$B!A(B 14:00$B9V1iCf;_(B
14:00$B!A(B 14:20B216$B%<%*%i%$%HKl$N%_%/%m:Y9&MF@Q$NI>2A$K4X$9$k8!F$(B
($BAaBg@h?JM}9)(B) ($B@5(B)$B!{@%2<(B $B2mGn(B$B!&(B ($B3X(B)$BHSEg(B $BM%5.(B$B!&(B ($B3X(B)$B>>K\(B $BOKJ?(B$B!&(B ($BAaBg@h?JM}9)(B/$BAaBgM}9)Am8&(B/JST-CREST) ($B@5(B)$B>>J}(B $B@5I'(B
ZSM-5 membrane
N2 adsorption
Micro-pore volume
4-a659
14:20$B!A(B 14:40B217$B%(%A%l%s%W%i%s%H2~NI$N$?$a$N%7%j%+J#9gKl$N8!F$(B
($B>;3(B $B3(H~(B$B!&(B ($B3X(B)$B>.Ln(B $BN5J?(B$B!&(B ($B3X(B)$BCSED(B $BJb(B$B!&(B ($B3X(B)$B:4!9LZ(B $BH~:;(B$B!&(B $BH*;3(B $B<~B"(B$B!&(B $B0pn5(B $BAaLi9a(B$B!&(B $B1|B<(B $B0&(B$B!&(B $BW"@%(B $BCR5W(B$B!&(B $B4XK\(B $B6F(B$B!&(B ($B@5(B)$BLnB<(B $B4490(B
counter diffusion CVD method
silica hybrid membranes
ozone concentration
4-a903
14:40$B!A(B 15:00B218$BBQ;@@-%7%j%+5U?;F)Kl$N3+H/(B
($B$B!&(B $B0pn5(B $BAaLi9a(B$B!&(B ($B3X(B)$BCSED(B $BJb(B$B!&(B $B4XK\(B $B6F(B$B!&(B $BW"@%(B $BCR5W(B$B!&(B ($B3X(B)$B>.Ln(B $BN5J?(B$B!&(B ($B3X(B)$B>>;3(B $B3(H~(B
silica RO membrane
acid stability
Ga addition
4-a534
15:00$B!A(B 15:20$B5Y7F(B
(15:20$B!A(B17:20) ($B:BD9(B $BW"ED(B $BM:0lO/!&@>B<(B $BKS(B)
15:20$B!A(B 15:40B220Reverse osmosis performance of layered-hybrid membranes consisting of organosilica separation layer on polymer supports
(Hiroshima U.) ($B3$(B)$B!{(BGong G. H.$B!&(B ($B@5(B)Nagasawa H.$B!&(B ($B@5(B)Kanezashi M.$B!&(B ($B@5(B)Yoshioka T.$B!&(B ($B@5(B)Tsuru T.
layered hybrid membrane
organosilica
desalination
4-a679
15:40$B!A(B 16:00B221$B@5?;F)Kl%b%8%e!<%k@-G=$NM=B,$,2DG=$J4J0W%b%G%k$N3+H/(B
($B?@8MBg1!9)(B/$B@hC$B!&(B ($BElMNKB(B) $B9gED(B $B>;J?(B$B!&(B ($B?@8MBg1!9)(B/$B@hC$B!&(B ($B@5(B)$B9b66(B $BCR51(B$B!&(B ($B@5(B)$B;09%(B $BB@O:(B$B!&(B ($B?@8MBg1!9)(B/$B;38}Bg1!M}9)(B) ($B@5(B)$BHf2E(B $B=<(B$B!&(B ($B?@8MBg1!9)(B/$B@hC>;3(B $B=(?M(B
Forward Osmosis
Hollow fiber membrane
Module performance
4-a618
16:00$B!A(B 16:20B222$B%U%'!<%:%U%#!<%k%I%b%G%k$rMQ$$$?(BO/W$B%(%^%k%7%g%s$NKlF)2a%7%_%e%l!<%7%g%s(B
($B?@8MBg1!9)(B/$B@hC$B!&(B ($B3X(B)$B9a@n(B $BM5Je(B$B!&(B ($BF|Bg1!@8J*;q8;(B) ($B@5(B)$B@P?@(B $BE0(B$B!&(B ($B?@8MBg1!9)(B/$B@hC>;3(B $B=(?M(B
Oil water separation
Numerical simulation
Phase-field model
4-a789
16:20$B!A(B 16:40B223$BGSG.MxMQ7??;F)05H/EE$KMQ$$$k29EY1~Ez@-9bJ,;R!?3$?e7O6nF0MO1U$NFC@-I>2A(B
($B?@8MBg1!9)(B/$B@hC$B!&(B ($B?@8MBg9)(B/$B@hC?9(B $B1vJfH~(B$B!&(B ($B?@8MBg1!9)(B/$B@hC$B!&(B $B>.LnED(B $BAp2p(B$B!&(B ($B@5(B)$B;09%(B $BB@O:(B$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B
forward osmosis
pressure retarded osmosis
thermoresponsive polymer
4-a831
16:40$B!A(B 17:00B224$B?tM}%b%G%k$r3hMQ$7$?(BMBR$B$K$*$1$k1?E>>r7o$N:GE,2=$N8!F$(B
($BElBg1!9)(B) ($B@5(B)$B!{6b;R(B $B90>;(B$B!&(B ($B@5(B)$BA%DE(B $B8x?M(B
Membrane bioreactor
Operating condition
Optimization
4-a49
17:00$B!A(B 17:20B225$BJ,;RF0NO3XK!$K$h$k?eJ,;R$N5sF02r@O$H%]%j%^!
($BL>9)Bg(B) ($B@5(B)$B!{Fn1@(B $BN<(B$B!&(B ($B3X(B)$B;0Bp(B $B9'L@(B$B!&(B ($B3X(B)$B;{Hx(B $BfFJ?(B$B!&(B ($B@5(B)$B4dED(B $B=$0l(B$B!&(B ($B@5(B)$B?9(B $B=(
hydration
membrane fouling
molecular dynamics
4-a501
B $B2q>l!&Bh(B 3 $BF|(B
(9:00$B!A(B10:20) ($B:BD9(B $B@%2<(B $B2mGn!&8E@n(B $BD>
9:00$B!A(B 9:20B301$BKl!&N3;R$X$NMO
($BElBg4D0B%;(B) ($B@5(B)$B!{C$L&(B $BNg(B$B!&(B ($BF|Bg@8;:9)(B) ($B@5(B)$B0BF#(B $BEX(B$B!&(B ($BElBg1!9)(B) ($B@5(B)$B>.CS(B $B=$(B$B!&(B ($BElBg4D0B%;(B/$BElBg1!9)(B) ($B@5(B)$BDT(B $B2B;R(B$B!&(B ($BElBg1!9)(B) ($B@5(B)$B;38}(B $BM34tIW(B
microfiltration
hydrodynamics
solute adsorption
4-a691
9:20$B!A(B 9:40B302$B%/%m%9%U%m!<@:L)$m2a$NDj>o%U%i%C%/%9$HN3;RBO@Q>uBV$K4X$9$k8&5f(B
($B9)3X1!Bg9)(B) ($B3X(B)$B!{bCJI(B $BNI(B$B!&(B ($B@5(B)$B@V>>(B $B7{$B!&(B ($B@5(B)$BCfHx(B $B??0l(B
microfiltration
steady state flux
particle deposition
4-a707
9:40$B!A(B 10:00B303Development of hydrogen-selective triphenylmethoxysilane-derived membranes by chemical vapor deposition
($B9)3X1!Bg9)(B) Zhang Xiaoliang$B!&(B (RITE) ($B@5(B)$B;3ED(B $B=(>0(B$B!&(B ($B@5(B)$B@FF#(B $B?r(B$B!&(B ($B@5(B)$B9CHe(B $B>HI'(B$B!&(B ($B9)3X1!Bg9)(B) ($B@5(B)$B!{@V>>(B $B7{$B!&(B ($B9)3X1!Bg9)(B/RITE) ($B@5(B)$BCfHx(B $B??0l(B
silica membrane
hydrogen
chemical vapor deposition
4-a352
10:00$B!A(B 10:20B304Bimodal catalytic membrane reactors for hydrogen production in the dehydrogenation of methylcyclohexane
($B9-Bg(B) ($B3$(B)$B!{(BMeng L.$B!&(B Yu X.$B!&(B $B?78+(B $BBsLp(B$B!&(B ($B@5(B)$BD9_7(B $B425,(B$B!&(B ($B@5(B)$B6b;X(B $B@58@(B$B!&(B ($B@5(B)$B5H2,(B $BJ~5W(B$B!&(B ($B@5(B)$BETN1(B $BL-N;(B
Membrane reactor
Organosilica membrane
Methylcyclohexane dehydrogenation
4-a656
$B9V1iH/I=%W%m%0%i%`(B
$B2=3X9)3X2q(B $BBh(B80$BG/2q(B
(C) 2015 $B8x1W
Most recent update: 2015-03-05 09:42:37
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