$B9V1i(B $B;~9o(B | $B9V1i(B $BHV9f(B | $B9V1iBjL\!?H/I= | $B%-!<%o!<%I(B | $BJ,N`(B $BHV9f(B | $B$BHV9f(B |
$B%7%s%]%8%&%`(B $B!cG3NAEECS!&?7EECS$*$h$S$=$N4XO"5;=Q$N?7E83+!d(B |
(9:00$B!A(B10:00)$B!!(B($B:BD9(B $B8E;3DL5W(B) |
9:00$B!A(B 9:20 | E101 | 1kW$B5i8GBN9bJ,;R7AG3NAEECS$N%9%?%C%/FC@-$*$h$S%(%M%k%.!<<};Y(B ($BC^GHBg%7%9>p(B) $B!{(B($B3X(B)$B>>2<(B $B5ACK(B$B!&(B($B@5(B)$B2,Eg(B $B7I0l(B | PEFC fuel cell stack efficiency
| S-37 | 265 |
9:20$B!A(B 9:40 | E102 | PEFC$B%9%?%C%/$K$*$1$k8N>c1F6AI>2A$N4pACE*8!F$(B ($BC^GHBg%7%9>p(B) $B!{(B($B@5(B)$B2,Eg(B $B7I0l(B$B!&(B($B3X(B)$B>>2<(B $B5ACK(B | PEFC fuel cell stack failure mode
| S-37 | 266 |
9:40$B!A(B 10:00 | E103 | $B8GBN9bJ,;R7A2D5U%;%k$N?eEE2r!&G3NAEECS@-G=$NI>2A(B ($B9b:=G.3X(B) $B!{(B($B@5(B)$B2CF#(B $BFX;K(B$B!&(B($B@5(B)$BA}ED(B $B@5IW(B$B!&(B($B@5(B)$B9b66(B $BFW(B$B!&(B($B%"%?%+Bg5!(B) $B5HED(B $BE/Li(B$B!&(B($B;:Am8&$D$/$P(B) $B0KF#(B $BGn(B$B!&(B($B;:Am8&4X@>(B) $B8^I4B"(B $BJY(B | United Reversible Cell Fuel Cell Oxygen Transfer
| S-37 | 1108 |
(10:00$B!A(B11:00)$B!!(B($B:BD9(B $B0f>e(B $B85(B) |
10:00$B!A(B 10:20 | E104 | $B9bJ,;R%_%/%m9=B$$K4p$E$/G3NAEECSMQ:Y9&%U%#%j%s%0EE2r ($BElBg1!9)(B) $B!{(B($B3X(B)$BK-ED(B $B>-J?(B$B!&(B($B3X(B)$B86(B $B?-@8(B$B!&(B($BEl9)Bg;q8;8&(B) ($B@5(B)$B0KF#(B $BBgCN(B$B!&(B($BEl9)Bg;q8;8&!&ElBg1!9)(B) ($B@5(B)$B;38}(B $BLT1{(B | polymer electrolyte membrane fuel cells pore-filling electrolyte membrane micro phase separated structure
| S-37 | 828 |
10:20$B!A(B 10:40 | E105 | PEFC$BMQ%-%c%C%T%s%0EE2r ($BElBg1!9)(B) $B!{(B($B3X(B)$BF#0f(B $B7$B!&(B($B3X(B)$BM{(B $BClL@(B$B!&(B($BEl9)Bg;q8;8&(B) ($B@5(B)$B0KF#(B $BBgCN(B$B!&(B($BEl9)Bg;q8;8&!&ElBg1!9)(B) ($B@5(B)$B;38}(B $BLT1{(B | PEFC capping nano-interface
| S-37 | 854 |
10:40$B!A(B 11:00 | E106 | Nafion$B$rMQ$$$?%-%c%C%T%s%0EE2r2A(B ($BElBg1!9)(B) $B!{(B($B3X(B)$BM{(B $BClL@(B$B!&(B($BEl9)Bg;q8;8&(B) ($B@5(B)$B0KF#(B $BBgCN(B$B!&(B($BEl9)Bg;q8;8&!&ElBg1!9)(B) ($B@5(B)$B;38}(B $BLT1{(B | Fuel Cells Proton conductor nano particles
| S-37 | 887 |
(11:00$B!A(B12:00)$B!!(B($B;J2q(B $BCf@n?B9%(B) |
11:00$B!A(B 12:00 | E107 | [$BE8K>9V1i(B]$B!!C:AG:`NA$K$h$kHsGr6b%+%=!<%I?(G^$X$ND)@o(B ($B72Bg1!9)(B) $B!{(B($B@5(B)$BHx:j(B $B=c0l(B | carbon electrode catalyst non platinum
| S-37 | 1104 |
(13:00$B!A(B14:00)$B!!(B($B:BD9(B $B2,Eg7I0l(B) |
13:00$B!A(B 13:20 | E113 | PEFC$BMQC:AGC4;}(BPt$B?(G^$N%7%j%+HoJ$$K$h$k(BPt$BMO=PBQ@-$N8~>e(B ($B6eBg1!9)(B) $B!{>>?9(B $BM5;K(B$B!&(B($B@5(B)$BCf@n(B $B7I;0(B$B!&(B($B@5(B)$B>>:,(B $B1Q$B!&(B($B@5(B)$BC]Cf(B $BAT(B$B!&(B($B@5(B)$B4_ED(B $B>;9@(B | PEMFC cathode catalyst dissolution of Pt silica-coated Pt supported carbon
| S-37 | 936 |
13:20$B!A(B 13:40 | E114 | PEFC$BMQC:AGC4;}(BPt$B?(G^$N%7%j%+HoJ$$K$h$k(BCO$BHoFGBQ@-$N8~>e(B ($B6eBg1!9)(B) $B!{M-2H(B $BN4J8(B$B!&(B($B3X(B)$B2OEg(B $B7r<#(B$B!&(B($B@5(B)$BCf@n(B $B7I;0(B$B!&(B($B@5(B)$B>>:,(B $B1Q$B!&(B($B@5(B)$BC]Cf(B $BAT(B$B!&(B($B@5(B)$B4_ED(B $B>;9@(B | PEFC carbon-supported Pt catalysts coverage of Pt catalysts with silica
| S-37 | 940 |
13:40$B!A(B 14:00 | E115 | PEFC$B%+%=!<%IGr6b?(G^>e;@AGAX7A@.5!9=$N2rL@(B ($BElBg1!(B) $B!{(B($B3X(B)$B@P@n(B $B=a(B$B!&(B($BEl9)Bg1!(B) ($B@5(B)$B0KF#(B $BBgCN(B$B!&(B($BElBg1!(B) ($B@5(B)$B;38}(B $BLT1{(B | polymer electrolyte fuel cell oxygen layer
| S-37 | 108 |
(14:00$B!A(B15:00)$B!!(B($B:BD9(B $B;38}LT1{(B) |
14:00$B!A(B 14:20 | E116 | $B;0 ($BElKLBg9)(B) $B!{(B($B@5(B)$B8E;3(B $BDL5W(B$B!&(B$BI~It(B $BC#:H(B$B!&(B$B>b(B $B7EJv(B$B!&(BSahnoun Riadh$B!&(B($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!&(BDel Carpio Carlos$B!&(B($BElKLBgL$Mh%;(B/$BElKLBg9)(B) ($B@5(B)$B5\K\(B $BL@(B | Porous Structure Simulator Porous Electrode Optimization
| S-37 | 76 |
14:20$B!A(B 14:40 | E117 | $BIT6Q0l6u7d9=B$$r9MN8$7$?(BPEFC$B3H;6AXFb$NFsAjN.2r@O(B ($B6eBg9)(B) $B!{(B($B@5(B)$B0f>e(B $B85(B$B!&(B($B3X(B)$B5H85(B $B5.;V(B$B!&(B($B@5(B)$B>>7((B $BMN2p(B$B!&(B($B@5(B)$BJw85(B $B2m | PEFC flooding gas diffusion layer
| S-37 | 867 |
14:40$B!A(B 15:00 | E118 | $B%9%i%j! ($B%N%j%?%1%+%s%Q%K!<%j%_%F%I(B) $B0KF#(B $B@?(B$B!&(B$B!{5H@n(B $BBg;N(B$B!&(B$B0BF#(B $BBYE5(B$B!&(B$BED8}(B $B5WIY(B | gas diffusion layer Electroconductive Polymer carbon fiber
| S-37 | 295 |
(15:00$B!A(B16:00)$B!!(B($B:BD9(B $BBgM'=g0lO:(B) |
15:00$B!A(B 15:20 | E119 | DMFC$B%"%N!<%I$N?(G^AX9=B$$HH?1~AG2aDx(B ($B?.=#BgA!0](B) $B!{(B($B3X(B)$B3wC+(B $BM*J?(B$B!&(B$B9bM|(B $BM:B@(B$B!&(B($B@5(B)$B?70f(B $B?FIW(B$B!&(B($B@5(B)$BJ!D9(B $BGn(B$B!&(B($B@5(B)$B9bDM(B $BF)(B$B!&(B($BElBg(B) ($B@5(B)$B;3ED(B $B6=0l(B | Direct Methanol Fuel Cell mercury porosimeter AC impedance
| S-37 | 1077 |
15:20$B!A(B 15:40 | E120 | $B%+!<%\%s%J%N%U%!%$%P! ($B72Bg1!(B) $B!{(B($B3X(B)$B2,ED(B $B>-6F(B$B!&(B$B:0ED(B $BM4M}(B$B!&(B($B@5(B)$BCfN$(B $BJY(B$B!&(B($B@5(B)$BLnED(B $BNh<#(B$B!&(B($B@5(B)$BCf@n(B $B?B9%(B | DMFC carbon nanofiber electrode structure
| S-37 | 418 |
15:40$B!A(B 16:00 | E121 | THE ROLE OF CARBON DIOXIDE LAYER PREPARED BY A POROUS CARBON PLATE IN A PASSIVE DMFC AS A MASS TRANSPORT BARRIER ($B72Bg1!(B) $B!{(B($B3X(B)Abdelkareem Mohammad$B!&(B($B@5(B)$BCf@n(B $B?B9%(B | DMFC mass transport porous carbon plate
| S-37 | 411 |
(16:00$B!A(B16:40)$B!!(B($B:BD9(B $BJ!D9(B $BGn(B) |
16:00$B!A(B 16:20 | E122 | DMFC$B$N$?$a$N9bL)EYNe5/8w$K$*$kI=LL2~2A(B ($B@EBg9)(B) $B!{(B($B3X(B)$BDT(B $B42(B$B!&(B$BHx4X(B $B>M(B$B!&(B($B@5(B)$B?\F#(B $B2mIW(B | DMFC Nafion Electron beam
| S-37 | 210 |
16:20$B!A(B 16:40 | E123 | $BCf29:nF0D>@\%(%?%N!<%k7AG3NAEECS$N%"%N!<%I?(G^$N9g@.$HEE6KH?1~FC@-(B ($B9)3X1!Bg1!9)(B) $B!{(B($B3X(B)$B2CF#(B $BGn9T(B$B!&(B($BElBg1!?7NN0h(B) ($B@5(B)$BBgM'(B $B=g0lO:(B$B!&(B($B@5(B)$BBgEg(B $B5A?M(B$B!&(B($B9)3X1!Bg9)(B) ($B@5(B)$BD9K\(B $B1Q=S(B | direct ethanol fuel cell intermediate temperature anode catalyst
| S-37 | 399 |