$BBh(B1$BF|(B | |||||
---|---|---|---|---|---|
$B9V1i(B $B;~9o(B | $B9V1i(B $BHV9f(B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $BJ,N`(B | $BHV9f(B $B | |
$B!cG3NAEECS!&?7EECS$*$h$S$=$N4XO"5;=Q$N?7E83+!d(B | |||||
(9:00$B!A(B10:00)$B!!(B($B:BD9(B $B>1Ln(B $B8|(B) | |||||
O101 | $B%/%i%9%l!<%H%O%$%I%l!<%H$rMQ$$$??eAGCyB"$K4X$9$k4pACE*8&5f(B | hydrogen gas hydrate storage | S-36 | 878 | |
O102 | $B?eAGCyB":`NA$H$7$F$N%7%/%m%X%-%5%s(B+$B%a%A%k%7%/%m%X%-%5%s:.9g7O$N=tJ*@-(B | Fuel Cell Solid-liquid Equilibria Hydrogen Solubility | S-36 | 163 | |
O103 | $B?eAGCyB":`NA$H$7$F$N%7%/%m%X%-%5%s!<%a%A%k%7%/%m%X%-%5%s:.9g7O$NC&?eAGH?1~(B | hydrogen storage cyclohexane dehydrogenation | S-36 | 150 | |
(10:00$B!A(B10:40)$B!!(B($B:BD9(B $B>e5\(B $B@.G7(B) | |||||
O104 | $B%G%+%j%sC&?eAGH?1~$K$*$1$k4pxH/B.EY$NB,Dj(B | Organic chemical hydride Superheated liquid-film state Evaporation rate | S-36 | 825 | |
O105 | $B2~ | preparation of standard gas for reformed gas gas analysis solid oxide fuel cell (SOFC) | S-36 | 888 | |
(10:40$B!A(B11:20)$B!!(B($B:BD9(B $B>.3^86(B $B7<0l(B) | |||||
O106 | $BD6NW3&$a$C$-K!$K$h$k%Q%i%8%&%`(B-$B6d9g6bGvKl$ND4@=$H?eAGJ,N%F)2aFC@-$NI>2A(B | membrane Pd hydrogen | S-36 | 405 | |
O107 | $BD6NW3&%J%N%W%l!<%F%#%s%0K!$rMQ$$$?!"%"%k%^%$%H(B/Pd$B79 | fuel cell super critical nano plating palladium | S-36 | 678 | |
(11:20$B!A(B12:00)$B!!(B($B;J2q(B $B0KF#(B $BD> | |||||
O108 | [$B>7BT9V1i(B] $BG3NAEECSMQ?eAG@=B$5;=Q$N3+H/>u67$H>-MhE8K>(B | $BG3NAEECS(B | S-36 | 567 | |
(13:00$B!A(B14:20)$B!!(B($B:BD9(B $B55;3(B $B=(M:(B) | |||||
O113 | $B%;%i%_%C%/%94p:`%Q%i%8%&%`?eAGJ,N%Kl$NGvKl2=$N8!F$(B | membrane Pd hydrogen | S-36 | 424 | |
O114 | $B9b8zN($J(BCO$B%U%j! | membrane reactor hydrogen catalytic reaction | S-36 | 192 | |
O115 | $B%Q%i%8%&%`!&6d9g6bEE5$$a$C$-$K$h$k?eAGJ,N%Kl$N@=:n(B | hydrogen separation membrane palladium silver alloy | S-6 | 765 | |
O116 | $B%^%$%/%m?(G^G3>FAuCV$rMQ$$$?(BLPG$B$NG3>F;n83(B | catalytic combustor deactivation NOx | S-36 | 256 | |
(14:20$B!A(B15:20)$B!!(B($B:BD9(B $BApJI(B $B9n8J(B) | |||||
O117 | $B%a%?%N!<%k$rMQ$$$?ItJ,;@2=2~ | partial oxidation methanol reformer | S-36 | 563 | |
O118 | $BA*Br;@2=?(G^Kl%j%"%/%?!<$rMQ$$$?2~ | CO Selective Oxidation Membrane Reactor Fuel Cell | S-36 | 693 | |
O119 | CO2$B5[<}:^$rC4;}$7$?DLEE2CG.%"%k%^%$%H?(G^$K$h$k%(%?%N!<%k$N?e>x5$2~ | ethanol steam reforming Nonequilibrium operation CO2 absorption | S-36 | 806 | |
(15:20$B!A(B16:00)$B!!(B($B;J2q(B $B;38}(B $BLT1{(B) | |||||
O120 | [$B>7BT9V1i(B] $BJ,;67?EE5$%(%M%k%.!<%M%C%H%o!<%/$K$*$1$k%7%9%F%`LL$+$i8+$?G3NAEECS!&?7EECS3hMQ$X$N4|BT(B | fuel cell | S-36 | 581 | |
(16:00$B!A(B16:40)$B!!(B($B:BD9(B $B0f>e(B $B85(B) | |||||
O122 | $B%"%k%^%$%H?(G^$rMQ$$$?G3NAEECSMQ(BCO$B=|5n4o$K4X$9$k8&5f(B | Selective CO Oxidation Alumite Catalyst Serrated Fin Reactor | S-36 | 638 | |
O123 | $B8GBN9bJ,;R7?G3NAEECS$X$NCbAG4^M-?eAGG3NAMxMQ$K4X$9$k8&5f(B | PEFC Hydrogen Fuel mixed Nitrogen Fuel Flow | S-36 | 961 | |
(16:40$B!A(B17:40)$B!!(B($B:BD9(B $B2O@%(B $B85L@(B) | |||||
O124 | PEFC$BH/EE@-G=$K5Z$\$9N.O)Fb1UE)BZN1>uBV$N4V@\B,Dj(B | PEFC flooding relative humidity | S-36 | 736 | |
O125 | PEFC$BH/EE@-G=$K5Z$\$93H;6AXFb%U%i%C%G%#%s%0$N8!F$(B | PEFC flooding gas diffusion layer | S-36 | 741 | |
O126 | PEFC$B3H;6AXFbFsAjN.F0$N(BLBM$B?tCM%7%_%e%l!<%7%g%s(B | PEFC Two-phase flow Lattice Boltzmann Method | S-36 | 987 | |
(17:40$B!A(B18:40)$B!!(B($B:BD9(B $B:y0f(B $B@?(B) | |||||
O127 | $B8GBN9bJ,;R7AG3NAEECS$N%,%93H;6AXFb$N29EYJ,I[$H?e$NN.B+J,I[$N?dDj(B | PEFC One-dimensional nonisothermal model Gas diffusion layer | S-36 | 770 | |
O128 | $BC:AGA!0]@QAX9=B$$r9MN8$7$?(BPEFC$B3H;6AXFb$NFsAjN.2r@O(B | PEFC flooding gas diffusion layer | S-36 | 746 | |
O129 | $B?eAG5[B"9g6b%"%N!<%I$N?eAG9bB.%,%9= | fuel cell metal hydride hydrogen | S-36 | 818 | |
$BBh(B2$BF|(B | |||||
$B9V1i(B $B;~9o(B | $B9V1i(B $BHV9f(B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $BJ,N`(B | $BHV9f(B $B | |
$B!cG3NAEECS!&?7EECS$*$h$S$=$N4XO"5;=Q$N?7E83+!d(B | |||||
(9:00$B!A(B10:00)$B!!(B($B:BD9(B $BBgM'=g0lO:(B) | |||||
O201 | $B%9%-%c%K%s%0%"%K!<%k$K$h$kAjJQ2=$r9MN8$7$?B@M[EECSMQ%J%N(BFeSi2/Si$BGvKl$N:n@=(B | Solar Cell Zone Melting Crystallization nano-particle | S-36 | 868 | |
O202 | $BGvKl(BZMC$BK!$K$h$kB@M[EECSMQGvKl$N7k>=2=$H(BSiO2/Si/SiO2$B;0AX9=B$$H$N4X78(B | Zone Melting Crystallization Silicon Solar Cell | S-36 | 891 | |
O203 | $B?'AGA}467?B@M[EECSMQ%J%N%A%?%K%"$ND4@=$H8wEEJQ49FC@-(B | dye-sensitized solar cell anatase-type titanium dioxide nano particle | S-36 | 419 | |
(10:00$B!A(B11:00)$B!!(B($B:BD9(B $B?\F#(B $B2mIW(B) | |||||
O204 | $B0[$J$k(BAg$B%J%NN3;R$r8w5[<}AX$KC4;}$7$??'AGA}46B@M[EECS$NH/EEFC@-(B | Solar cell Nanoparticle Dye sensitized | S-36 | 863 | |
O205 | $B6d%J%NN3;R$rC4;}$7$?8w5[<}AX$N9=B$$,?'AGA}46B@M[EECS$NH/EEFC@-$K5Z$\$91F6A(B | Solar cell Nanoparticle Dye sensitized | S-36 | 869 | |
O206 | $B%l%I%C%/%9%-%c%Q%7%?EE6K:`NA$H$7$F$N%^%s%,%s;@2=J*$NEE5$2=3XFC@-(B | electrochemical capacitor manganese oxide pseudocapacitance | S-36 | 804 | |
(11:00$B!A(B12:00)$B!!(B($B:BD9(B $B0K86(B $B3X(B) | |||||
O207 | $BM-5!7OEE2r1U%O%$%Q%o!<%-%c%Q%7%?EE6K$N$?$a$N3h@-C:I=LL%W%i%:%^=hM}8z2L(B | Supercapacitor nonaqueous electrolyte plasma treatment | S-36 | 343 | |
O208 | $BEE5$Fs=EAX%-%c%Q%7%?$NEE2r1U$X$N3&LL3h@-:^$NE:2C$,= | Electric double layer capacitor surfactant aqueous solution | S-36 | 535 | |
O209 | $BFs;@2=%^%s%,%s$rMQ$$$?%"%k%+%j7AG3NAEECS%+%=!<%I$NEE6KFC@-(B | manganese dioxide cathode fuel cell | S-36 | 812 | |
(14:40$B!A(B15:40)$B!!(B($B:BD9(B $B5FCO(B $BN4;J(B) | |||||
O218 | MCFC/$B%^%$%/%m%,%9%?!<%S%s%O%$%V%j%C%IH/EE%7%9%F%`$N=PNOJQF0;~$N0BDj1?E>>r7o$NCN8+(B | fuel cell electric(al) generation hybrid | S-36 | 774 | |
O219 | $BB?9& | solid oxide fuel cell porous structure simulator multi-scale simulation | S-36 | 186 | |
O220 | Ni/ScSZ$BG3NA6K$rMQ$$$?8GBN;@2=J*G3NAEECS$K$*$1$kG3NAEECSH?1~5!9=$N8!F$(B | fuel cell solid oxide fuel cell ScSZ | S-36 | 862 | |
(15:40$B!A(B16:40)$B!!(B($B:BD9(B $BJ!D9(B $BGn(B) | |||||
O221 | SOFC$B>.7?H/EE;n83$K$*$1$k%;%k=8EEJ}K!$N8!F$(B | SOFC fuel cell current density | S-36 | 524 | |
O222 | SOFC$BEE2r | microwave heating SOFC electrolyte sintering | S-36 | 674 | |
O223 | SOFC$B>.7?H/EE;n83AuCV$NG.N.BN%7%_%e%l!<%7%g%s2r@O(B | SOFC test CFD analysis heat and mass transfer | S-36 | 687 | |
(16:40$B!A(B17:40)$B!!(B($B:BD9(B $B8E;3(B $BDL5W(B) | |||||
O224 | $B8GBN;@2=J*7AG3NAEECS$NG3NAB?MM2=$N8!F$(B | Solid oxide fuel cell Propane Decane | S-36 | 466 | |
O225 | $B0[$J$kEE2r%@%$%l%/%H%+!<%\%sG3NAEECS$NH/EEFC@-$N8!F$(B | solid oxide fuel cell fuel cell RDC-FC | S-36 | 795 | |
O226 | $B8GBN;@2=J*7AG3NAEECSG3NA6K$NEE6K9=B$$HM-8zH?1~>l(B | solid oxide fuel cell cermet anode effective reaction zone | S-36 | 900 | |
$BBh(B3$BF|(B | |||||
$B9V1i(B $B;~9o(B | $B9V1i(B $BHV9f(B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $BJ,N`(B | $BHV9f(B $B | |
$B!cG3NAEECS!&?7EECS$*$h$S$=$N4XO"5;=Q$N?7E83+!d(B | |||||
(9:00$B!A(B10:00)$B!!(B($B:BD9(B $B;38}(B $BLT1{(B) | |||||
O301 | DMFC$BH/EEFC@-$K5Z$\$9%a%?%N!<%k%/%m%9%*!<%P!<$N1F6A(B | DMFC Methanol crossover Numerical simulation | S-36 | 316 | |
O302 | $BD>@\%a%?%N!<%k7AG3NAEECS$N$?$a$NGr6b%9%Q%C%?%j%s%0GvAX%+%=!<%I$NFC@-I>2A(B | Direct methanol fuel cell Mass activities Sputter-deposition | S-36 | 342 | |
O303 | Efficient DMFC using high methanol concentration | DMFC neat methanol porous plate | S-36 | 633 | |
(10:00$B!A(B11:20)$B!!(B($B:BD9(B $BCf@n(B $B?B9%(B) | |||||
O304 | $B%P%$%*G3NAEECS$K$*$1$k9ZAG8GDj2=EE6K$N@-G=8~>e$X8~$1$?8!F$(B | biofuel cell enzyme reaction redox polymer | S-36 | 116 | |
O305 | PEFC$BMQA4K'9aB2C:2=?eAG7O:Y9&%U%#%j%s%0EE2r | pore-filling electrolyte membrane aromatic hydrocarbon structure of water | S-36 | 249 | |
O306 | [$B>7BT9V1i(B]$B7HBS5!4oMQG3NAEECS$N3+H/(B | fuel cell | S-36 | 577 | |
(11:20$B!A(B12:00)$B!!(B($B:BD9(B $B9>F,(B $BLw9,(B) | |||||
O308 | $B%a%=%]!<%i%9%+!<%\%s$X$N?(G^6bB0C4;}$H$=$N%"%k%3!<%k;@2=3h@-(B | electrode catalyst mesoporous carbon direct alcohol fuel cell | S-36 | 597 | |
O309 | PtRuRh/C$B?(G^$N9g@.$H$=$N;@2=FC@-(B | electrode catalyst direct alcohol fuel cell | S-36 | 655 | |
(13:00$B!A(B14:00)$B!!(B($B:BD9(B $BGk86L@K<(B) | |||||
O313 | $B?bD>G[8~@-$rM-$9$k6bB0(B-$B%7%j%+J#9gGvKl$N@.Kl2aDx$H%a%=B?9& | mesoporous silica sputtering inorganic composite electrolyte | S-36 | 694 | |
O314 | [$B>7BT9V1i(B] $BG3NAEECSMQEE6K?(G^$N3+H/$N8=>u$H:#8e$N2]Bj(B | Fuel Cell | S-36 | 572 | |
(14:00$B!A(B14:40)$B!!(B($B:BD9(B $BBgM'(B $B=g0lO:(B) | |||||
O316 | $BCf290h$K$*$1$k%j%s4^M-%A%?%K%"J#9gKl$N%W%m%H%sEAF3FC@-$HH/EEFC@-(B | proton conductivity titanium-phosphorus oxide membrane fuel cell | S-36 | 251 | |
O317 | $B9b29:nF0(BPEMFC$BMQ?75,M-5!L55!%O%$%V%j%C%IEE2r | PEMFC hybrid interface | S-36 | 127 | |
(14:40$B!A(B15:40)$B!!(B($B:BD9(B $BETN1(B $BL-N;(B) | |||||
O318 | $B<~4|E*%J%N9=B$%j%s;@%7%j%1!<%HGvKl$N>x5$9g@.$H%W%m%H%sEAF3@-(B | Vapor Infiltration synthesis Proton conductivity Phosphoric silicate | S-36 | 661 | |
O319 | $B9-29EY0h:nF0MQ8GBN9bJ,;R7AG3NAEECSEE6K$N3+H/$H$=$N9=B$@)8f(B | PEFC Hybrid SPES | S-36 | 895 | |
O320 | $B%7%j%+HoJ$(BPt$B%J%NN3;R$rMQ$$$?(BPEFC$BEE6K$NH/EEFC@-(B | Silica-coated Pt nanoparticle PEFC anode electrode catalyst three-phase interface | S-36 | 479 | |
(15:40$B!A(B16:20)$B!!(B($B:BD9(B $B4_ED(B $B>;9@(B) | |||||
O321 | $BGr6b(B-$B6bB0;@2=J*J#9g:`NA$N3+H/$HG3NAEECSMQ?(G^$H$7$F$NFC@-I>2A(B | Metal oxide Catalyst Fuel cells | S-36 | 815 | |
O322 | MRI$BEE2r ($BEl9)BgC:AG=[4D%(%M%k%.!<8&5f%;(B) $B!{(B($B@5(B)$B@nED(B $B7rB@O:!&(B | Polymer electrolyte membrane magnetic resonance imaging water transport | S-36 | 991 |