$B9V1i(B $B;~9o(B | $B9V1i(B $BHV9f(B | $B9V1iBjL\!?H/I= | $B%-!<%o!<%I(B | $BJ,N`(B $BHV9f(B | $B$BHV9f(B |
$B%(%M%k%.!<(B |
(9:00$B!A(B10:00)$B!!(B($B:BD9(B $B5\K\(B $B=_0l(B) |
9:00$B!A(B 9:20 | L301 | PEFC$B3H;6AXFb$KBZN1$9$k1UE)$NF0E*5sF0B,Dj(B ($B6eBg9)(B) $B!{(B($B3X(B)$BBD(B$B!&(B($B@5(B)$B0f>e(B $B85(B$B!&(B($B@5(B)$B>>7((B $BMN2p(B$B!&(B($B@5(B)$BJw85(B $B2m | PEFC gas diffusion layer droplet
| 9-e | 703 |
9:20$B!A(B 9:40 | L302 | PEFC$B3H;6AX3&LL$N9=B$(B/$B@->u$K1F6A$9$k(BMPL$B$NFC@-I>2A(B ($B6eBg9)(B) $B!{(B($B3X(B)$B>k%N>e(B $B7rB@(B$B!&(B($B@5(B)$B0f>e(B $B85(B$B!&(B($B@5(B)$B>>7((B $BMN2p(B$B!&(B($B@5(B)$BJw85(B $B2m | PEFC gas diffusion layer micro porous layer
| 9-e | 705 |
9:40$B!A(B 10:00 | L303 | 3D$B%]%"%M%C%H%o!<%/2r@O$K$h$k(BGDL$BFb1UE)5sF02r@O(B ($B6eBg9)(B) $B!{(B($B@5(B)$B0f>e(B $B85(B$B!&(B($B@5(B)$B>>7((B $BMN2p(B$B!&(B($B@5(B)$BJw85(B $B2m | PEFC gas diffusion layer numerical analysis
| 9-e | 709 |
(10:00$B!A(B11:00)$B!!(B($B:BD9(B $B@>B<(B $B82(B) |
10:00$B!A(B 10:20 | L304 | $B8GBN9bJ,;R7AG3NAEECS$K$*$1$kAX4V@\?(Dq93(B ($B5~Bg9)(B) $B!{(B($B@5(B)$B2O@%(B $B85L@(B$B!&(B($B@5(B)$B0p3@(B $BC#Li(B$B!&(B($B@5(B)$B;01:(B $B9'0l(B | PEFC nonisothermal modeling temperature measurement
| 9-e | 678 |
10:20$B!A(B 10:40 | L305 | $B:Y9&%U%#%j%s%0EE2r ($BElBg1!9)(B) $B!{(B($B3X(B)$BK-ED(B $B>-J?(B$B!&(B($BEl9)Bg;q8;8&(B) ($B@5(B)$BBg66(B $B=(Gl(B$B!&(B($B@5(B)$B0KF#(B $BBgCN(B$B!&(B($BElBg(B/$BEl9)Bg(B) ($B@5(B)$B;38}(B $BLT1{(B | alkaline fuel cells polymer electrolyte pore-filling membrane
| 9-e | 601 |
10:40$B!A(B 11:00 | L306 | A Novel modeling based on secondary pore and microscopic reaction models for PEFCs ($BElBg1!9)(B) $B!{(B($B3X(B)Limjeerajarus Nuttapol$B!&(B($BEl9)Bg;q8;8&(B) ($B@5(B)$BBg66(B $B=(Gl(B$B!&(B($B@5(B)$B0KF#(B $BBgCN(B$B!&(B($BElBg(B/$BEl9)Bg(B) ($B@5(B)$B;38}(B $BLT1{(B | PEFCs Modeling Adsorbed oxygen-speices
| 9-e | 582 |
(11:00$B!A(B12:00)$B!!(B($B:BD9(B $B0f>e(B $B85(B) |
11:00$B!A(B 11:20 | L307 | $BA48GBN9bJ,;R7A%"%k%+%jG3NAEECSMQ?75,K'9aB27O:Y9&%U%#%j%s%0Kl$N(BOH-$BEAF3FC@-(B ($BElBg1!9)(B) $B!{(B($B3X(B)$BF#0f(B $B7$B!&(B($BEl9)Bg;q8;8&(B) ($B@5(B)$BBg66(B $B=(Gl(B$B!&(B($B@5(B)$B0KF#(B $BBgCN(B$B!&(B($BEl9)Bg;q8;8&!&ElBg1!9)(B) ($B@5(B)$B;38}(B $BLT1{(B | fuel cell anion-exchange membrane pore-filling membrane
| 9-e | 586 |
11:20$B!A(B 11:40 | L308 | PEFC$B%,%93H;6AX$NG.EAF3N(0[J}@-B,Dj(B ($B;:Am8&(B) $B!{(B($B@5(B)$B5\K\(B $B=_0l(B$B!&(B$BBg;3(B $B=_J?(B | Polymer Electrolyte Fuel Cell Gas Diffusion Layer thermal conductivity
| 9-e | 137 |
11:40$B!A(B 12:00 | L309 | $B8GBN9bJ,;R7AG3NAEECSC1%;%kFbO"@.8=>]$N;YG[0x;R2rL@(B ($B;0=EBg1!9)(B) $B!{(B($B@5(B)$B@>B<(B $B82(B$B!&(B($B3X(B)$B_'C+(B $B7r0l(B$B!&(B$B?9K\(B $B=_;V(B$B!&(B($B;0=EBg9)(B) $BEDCf(B $B@.5((B$B!&(B($B;0=EBg1!9)(B) $BW"ED(B $B??;K(B$B!&(B($BElK.%,%9(B) $BCfB<(B $B5A90(B$B!&(B$B>.Eg(B $B@5;L(B$B!&(B$B@.ED(B $B2mI'(B | PEFC in situ measurement CFD
| 9-e | 242 |
12:00$B!A(B 13:00 | $BCk5Y$_(B |
(13:00$B!A(B14:00)$B!!(B($B:BD9(B $BEOn5(B $B??;V(B) |
13:00$B!A(B 13:20 | L313 | $B9bG;EYG3NA$rMxMQ$7$?(BPassive$B7?(BDMFC$B%9%?%C%/$NH/EEFC@-$KM?$($k<~0O<>EY$N1F6A(B ($B72Bg9)(B) $B!{(B($B@5(B)$BDT8}(B $BBsLi(B$B!&(B($B3X(B)$B9)F#(B $BBnLi(B$B!&(BMohammad Abdelkareem$B!&(B($B@5(B)$BCf@n(B $B?B9%(B | Passive DMFC stack Methanol crossover Porous carbon plate
| 9-a | 356 |
13:20$B!A(B 13:40 | L314 | $B?75,(BDMFC$B$KE,$7$?B?9& ($B72Bg9)(B) $B!{(B($B3X(B)$B5HMx(B $B;J(B$B!&(B($B@5(B)$BDT8}(B $BBsLi(B$B!&(B($B@5(B)$BLnED(B $BNh<#(B$B!&(B($B@5(B)$BCf@n(B $B?B9%(B | DMFC Porous Carbon Plate
| 9-a | 385 |
13:40$B!A(B 14:00 | L315 | $BD>@\%.;@7?G3NAEECS(B(DFAFC)$B$NG3NA6!5kJ}K!$N8!F$(B ($B72Bg9)(B) $B!{(B($B3X(B)$B9)F#(B $BBnLi(B$B!&(B($B@5(B)$BDT8}(B $BBsLi(B$B!&(B($B@5(B)$BCf@n(B $B?B9%(B | DFAFC Crossover Vapor feed
| 9-a | 695 |
(14:00$B!A(B15:00)$B!!(B($B:BD9(B $BBgM'(B $B=g0lO:(B) |
14:00$B!A(B 14:20 | L316 | $B9&$"$-GvGs$rMQ$$$?(BDMFC$B$K$*$1$k1F6A0x;R$N8!F$(B ($B72Bg9)(B) $B!{(B($B3X(B)$B@n5WJ](B $BJbH~(B$B!&(B($B@5(B)$BDT8}(B $BBsLi(B$B!&(B($B@5(B)$BCf@n(B $B?B9%(B | DMFC perforated metal sheet wettability
| 9-a | 699 |
14:20$B!A(B 14:40 | L317 | $BG3NAEECS?(G^NLDc8:$N$?$a$NB?AX2=%"%N!<%I$N@_7W(B ($B@EBg9)(B) $B!{(B($B3X(B)$Bc7F#(B $BM59T(B$B!&(B($B3X(B)$BCfEh(B $B91NI(B$B!&(B$BBgAR(B $B9-Ch(B$B!&(B($B@5(B)$B?\F#(B $B2mIW(B$B!&(B($B@5(B)$BJ!86(B $BD9 | DMFC Anode design Catalyst layer
| 9-e | 251 |
14:40$B!A(B 15:00 | L318 | $B%W%i%:%^=E9g%"%K%*%sKl$N(BDMFC$BH/EEFC@-(B ($B@EBg9)(B) $B!{(B($B3X(B)$B9b2,(B $BD>90(B$B!&(B($B3X(B)$B?7H~(B $B9,(B$B!&(B($B@5(B)$B?\F#(B $B2mIW(B | Anion membrane Plasma method Alkaline DMFC
| 9-e | 252 |
(15:00$B!A(B16:00)$B!!(B($B:BD9(B $BDT8}(B $BBsLi(B) |
15:00$B!A(B 15:20 | L319 | $BEE5$Fs=EAX%-%c%Q%7%?$N@-G=8~>e$N$?$a$NEE6K9=B$@_7W(B ($B@EBg9)(B) $B!{(B($B@5(B)$BEOn5(B $B??;V(B$B!&(B($B3X(B)$BBl@n(B $B9d;V(B$B!&(B$B>.@>(B $B2D0&(B$B!&(B($B@5(B)$B?\F#(B $B2mIW(B | Electric double layer capacitor Activated carbon Carbon black
| 9-e | 691 |
15:20$B!A(B 15:40 | L320 | $BEE5$Fs=EAX%-%c%Q%7%?$N:Y9&9=B$$r9MN8$7$?%b%G%j%s%0(B ($B@EBg9)(B) $B!{(B($B3X(B)$B6\_7(B $BM[(B$B!&(B($B@5(B)$BEOn4(B $B??;V(B$B!&(B($B@5(B)$B?\F#(B $B2mIW(B | Porous electrode theory Modeling Electric double layer capacitor
| 9-e | 262 |
15:40$B!A(B 16:00 | L321 | $BCfDc290h$K$*$1$k%j%s;@0!1t7O%,%i%9J#9gBN$N%W%m%H%sEAF3FC@-$H3&LL8z2L(B ($BElBg9)(B) $B!{(B($B3X(B)$B8E66(B $BM%Ka(B$B!&(B($BElBg1!?7NN0h(B) ($B3X(B)$BEhED(B $B8^I4N$(B$B!&(B($B@5(B)$BBgM'(B $B=g0lO:(B$B!&(B($B@5(B)$BBgEg(B $B5A?M(B | zinc phosphate glass proton conductor intermediate temperature fuel cell
| 9-e | 245 |