$BBh(B1$BF|(B
|
$B9V1i(B $B;~9o(B | $B9V1i(B $BHV9f(B | $B9V1iBjL\!?H/I= | $B%-!<%o!<%I(B | $BJ,N`(B $BHV9f(B | $B$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 |
$BBh(B2$BF|(B
|
$B9V1i(B $B;~9o(B | $B9V1i(B $BHV9f(B | $B9V1iBjL\!?H/I= | $B%-!<%o!<%I(B | $BJ,N`(B $BHV9f(B | $B$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 $BGr:j5AB'(B) |
9:00$B!A(B 9:20 | E201 | CO$B5[Ce:^$rMQ$$$?G3NAEECSMQ?eAG@:@=%W%m%;%9$N3+H/(B ($B?@8M@=9]=j(B) $B!{(B($B@5(B)$B;01:(B $B??0l(B$B!&(B($B@5(B)$BCfHx(B $B>:(B$B!&(B($B@5(B)$B;32<(B $B3Y;K(B$B!&(B($B@5(B)$BF#_7(B $B>4Mx(B | CO Adsorption Hydrogen Fuel Cell
| S-37 | 890 |
9:20$B!A(B 9:40 | E202 | $B?75,?eAG(BPSA$BAuCV$N8zN(I>2A(B ($B?@8M@=9]=j(B) $B!{CfHx(B $B>:(B$B!&(B$B;01:(B $B??0l(B$B!&(B$B;32<(B $B3Y;K(B$B!&(B$BF#_7(B $B>4Mx(B | CO Adsorption H2-PSA Fuel Cell
| S-37 | 1132 |
9:40$B!A(B 10:00 | E203 | $BHsJ?9U2~2$B5[<}:^:F@8%W%m%;%9$N9b8zN(2=(B ($BL>Bg%(%3%H%T%"(B) $B!{(B($B@5(B)$BKQ(B $B3$MN(B$B!&(B($BL>Bg9)(B) ($B6&(B)$BCfB<(B $B7K(B$B!&(B($BL>Bg%(%3%H%T%"(B) ($B@5(B)$B>.NS(B $B7I9,(B$B!&(B($BElK.%,%9(B) ($B6&(B)$B3k;3(B $B900l(B | Hydrogen production CO2 adsorbent Regeneration process
| S-37 | 78 |
(10:00$B!A(B11:00)$B!!(B($B:BD9(B $B0K86(B $B3X(B) |
10:00$B!A(B 10:20 | E204 | $B%F%s%W%l!<%HK!$K$h$k%O%$%Q%o!<%-%c%Q%7%?EE6K$N:Y9&9=B$@_7W(B ($B@EBg9)(B) $B!{(B($B3X(B)$BNkLZ(B $B@c9-(B$B!&(B($B3X(B)$B6\_7(B $BM[(B$B!&(B$BEOn5(B $B??;V(B$B!&(B($B@5(B)$B?\F#(B $B2mIW(B | Capacitor Template method Activated carbon
| S-37 | 208 |
10:20$B!A(B 10:40 | E205 | $B%O%$%Q%o!<%-%c%Q%7%?$N$?$a$N3h@-C:$NI=LL5Z$S:Y9&FC@-(B ($B@EBg9)(B) $B!{(B($B3X(B)$B6\_7(B $BM[(B$B!&(B($B3X(B)$BNkLZ(B $B@c9-(B$B!&(B$BBl@n(B $B9d;V(B$B!&(B$BEOn4(B $B??;V(B$B!&(B($B@5(B)$B?\F#(B $B2mIW(B | Capacitor Pore size Activated carbon
| S-37 | 209 |
10:40$B!A(B 11:00 | E206 | $B%+!<%\%s%2%k$N9bL)EY2=$K$h$k9bMFNL%-%c%Q%7%?EE6K$N3+H/(B ($B5~Bg1!9)(B) $B!{(B($B@5(B)$BEDLg(B $BH%(B$B!&(B($B3X(B)$BD;0f(B $BFX;K(B$B!&(B($BKLBg1!9)(B) ($B@5(B)$B8~0f(B $B?B(B | carbon gel electrical double layer capacitor
| S-37 | 235 |
(11:00$B!A(B12:00)$B!!(B($B;J2q(B $BH,Hx(B $B<"(B) |
11:00$B!A(B 12:00 | E207 | [$B>7BT9V1i(B]$B!!4D6-$N$?$a$N9b@-G=%j%A%&%`%$%*%sEECS$N8&5f3+H/(B ($BF|;:<+F0(B $B1QL@(B | Battery Automobile Energy
| S-37 | 1105 |
(13:00$B!A(B14:00)$B!!(B($B:BD9(B $B0KF#D> |
13:00$B!A(B 13:20 | E213 | $BG3NAEECSMQ%Q%i%8%&%`(B/$B%"%k%^%$%H79 ($BElG@9)Bg1!(B) $B!{(B($B3X(B)$B@%2<(B $B2mGn(B$B!&(B($B3X(B)$B>._7(B $BL-(B$B!&(B($BEl9)Bg@:8&(B) ($B@5(B)$BA>:,(B $B@5?M(B$B!&(B($BElG@9)Bg(B) ($B@5(B)$B:y0f(B $B@?(B$B!&(B($B@5(B)$B55;3(B $B=(M:(B | alumite palladium electroless plating
| S-37 | 611 |
13:20$B!A(B 13:40 | E214 | $BL5EE2r$a$C$-K!$K$h$k%Q%i%8%&%`$N@O=PB.EY$K$D$$$F$N8!F$(B ($BElM}Bg9)(B) $B!{(B($B3X(B)$B9l(B $BKcM%;R(B$B!&(B($B@5(B)$B>1Ln(B $B8|(B$B!&(B($B@5(B)$BBgC](B $B>!?M(B | palladium membrane electroless plating
| S-37 | 853 |
13:40$B!A(B 14:00 | E215 | $B%a%s%V%l%s%j%"%/%?! ($B4tIlBg9)(B) $B!{(B($B@5(B)$B>e5\(B $B@.G7(B$B!&(B$B2&(B $BNS>!(B$B!&(B$B0B0f(B $B8,0lO:(B$B!&(B$BC+8}(B $B2B2p(B$B!&(B($B@5(B)$B5A2H(B $BN<(B | Hydrogen Membrane Palladium
| S-37 | 237 |
(14:00$B!A(B15:00)$B!!(B($B:BD9(B $B>e5\@.G7(B) |
14:00$B!A(B 14:20 | E216 | $B%Q%i%8%&%`!&F<9g6b%a%s%V%l%s$N?eAGF)2aFC@-(B ($BEl9)Bg(B) $B!{(B($B3X(B)$B??Eg(B $BE5I'(B$B!&(B($B@5(B)$B2,:j(B $B7r(B | palladium membrane hydrogen permeation
| S-37 | 658 |
14:20$B!A(B 14:40 | E217 | $B%8%k%3%K%";Y;}BN$rMQ$$$?%Q%i%8%&%`?eAGJ,N%Kl$N3+H/(B ($BF|K\%,%$%7(B) $B!{(B($BIt(B)$BLnED(B $B7{0l(B$B!&(B($BIt(B)$BLnCf(B $B5W5A(B$B!&(B($BIt(B)$B$B!&(B($BIt(B)$B0kB<(B $B3X(B$B!&(B($BIt(B)$BIYED(B $B=S90(B | membrane hydrogen palladium
| S-37 | 152 |
14:40$B!A(B 15:00 | E218 | $BHsJ?9UG3NA2~ ($BEl9)Bg1!M}9)(B) $B!{(B($B3X(B)$B1::j(B $B;0@i?M(B$B!&(B$BEDCf(B $BAo(B$B!&(B($BEl9)Bg86;RO'8&(B) ($B@5(B)$BN-(B $B=f0l(B$B!&(B($B@5(B)$B2CF#(B $BG75.(B | Hydrogen permeation membrane Plating Palladium
| S-37 | 42 |
(15:00$B!A(B16:00)$B!!(B($B:BD9(B $B>1Ln(B $B8|(B) |
15:00$B!A(B 15:20 | E219 | $B5^Nd6E8GK!$rMQ$$$F:n@=$7$?(BNi-Nb-Zr-Ta$B%"%b%k%U%!%99g6b$N?eAGF)2a@-(B ($BElKLBg6b8&(B) $B!{(B($B@5(B)$B;31:(B $B??0l(B$B!&(B($B4tIlBg9)(B) ($B@5(B)$B>e5\(B $B@.G7(B$B!&(B($BElKLBg6b8&(B) $BLZB<(B $B5WF;(B$B!&(B$B0f>e(B $BL@5W(B | amorphous melt-spinning permeability
| S-37 | 859 |
15:20$B!A(B 15:40 | E220 | $B?(G^0lBN2=%b%8%e!<%k$N3+H/(B ($BEl5~%,%9(B) $B!{>oLZ(B $BC#Li(B$B!&(B($B@5(B)$BGr:j(B $B5AB'(B$B!&(B$B9u@n(B $B1Q?M(B$B!&(B($BF|K\FC$B!&(B$B;V3@(B $B=(OB(B$B!&(B$BEDCf(B $BM5G7(B$B!&(B$B;0Lp(B $B9LJ?(B | Hydrogen Membrane Reformer
| S-37 | 98 |
15:40$B!A(B 16:00 | E221 | $BM-5!%O%$%I%i%$%I$+$i$N?eAG2s<}$N$?$a$NB?4I<0%a%s%V%l%s%j%"%/%?!<(B ($B1'ET5\Bg9)(B) $B!{(B($B@5(B)$B0KF#(B $BD>$B!&(B$B@nE:(B $BMhL$(B$B!&(B$B?9(B $B>OB@(B$B!&(B($B@5(B)$B:4F#(B $B9d;K(B | hydrogen Chemical hydride membrane reactor
| S-37 | 842 |
$BBh(B3$BF|(B
|
$B9V1i(B $B;~9o(B | $B9V1i(B $BHV9f(B | $B9V1iBjL\!?H/I= | $B%-!<%o!<%I(B | $BJ,N`(B $BHV9f(B | $B$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 $B@>B<(B $B82(B) |
9:00$B!A(B 9:20 | E301 | $BN.F0AX$K$h$kDc293h@-7?%a%?%sItJ,;@2=?(G^$N@=B$(B ($B72Bg1!9)(B) $B!{(B($B@5(B)$BCfN$(B $BJY(B$B!&(B$B:dK\(B $B>"(B$B!&(B($B72Bg9)(B) $BCfEg(B $B?-0lO:(B$B!&(B($B72Bg1!9)(B) $BLnED(B $BNh<#(B$B!&(B$BCf@n(B $B?B9%(B | partial oxidation catalyst fluidized bed
| S-37 | 918 |
9:20$B!A(B 9:40 | E302 | $B%*%U%,%9$rMQ$$$?%a%?%N!<%k?e>x5$2~ ($B7DXfBgM}9)(B) $B!{(B($B3X(B)$BC01)(B $B9d9/(B$B!&(B($BBgF1%a%?%k9)6H(B) ($B@5(B)$B@.@%(B $B9,IW(B$B!&(B($B@5(B)$B0p8+(B $BLP(B$B!&(B($B@5(B)$B2CF#(B $B1QFs(B$B!&(B($B7DXfBgM}9)(B) ($B@5(B)Wardana Ing$B!&(B($B@5(B)$BBgB<(B $BN<(B$B!&(B($B@5(B)$B2#?9(B $B9d(B$B!&(B($B@5(B)$B?"ED(B $BMx5W(B$B!&(B($B@5(B)$B9BK\(B $B2mI'(B | steam reforming methanol heat balance
| S-37 | 872 |
9:40$B!A(B 10:00 | E303 | DME$B$NL5?(G^2~ ($BKLBg9)(B) $B!{(B($B3X(B)$B:4@n(B $B=VBg(B$B!&(B$BCfB<(B $BM4Fs(B$B!&(B$B0KEl(B $B909T(B | DME reforming hydrogen formation
| S-37 | 32 |
(10:00$B!A(B11:00)$B!!(B($B:BD9(B $B>e5\@.G7(B) |
10:00$B!A(B 10:20 | E304 | $B&C(B-$B%"%k%_%J$H(BCu/Zn$BC4;}C:AG?(G^$rMQ$$$?(BDME$B?e>x5$2~ ($B5~Bg9)(B) $B!{(B($B3X(B)$B9)F#(B $B??Fs(B$B!&(B($B@5(B)$BKR(B $BBYJe(B$B!&(B($B@5(B)$B;01:(B $B9'0l(B$B!&(B($B@5(B)$BA0(B $B0lW"(B | dimethyl ether fuel cell steam reforming
| S-37 | 68 |
10:20$B!A(B 10:40 | E305 | Cu$B7O%9%T%M%k%3%s%]%8%C%H?(G^$K$*$1$k(BDME$B?e>x5$2~ ($B5~Bg1!9)(B) $B!{(B($B@5(B)$B5FCO(B $BN4;J(B$B!&(B$BAzED(B $BD>9((B$B!&(B(JST) Faungnawakij Kajornsak$B!&(B$B2OEg(B $B=S0lO:(B$B!&(B($B=P8w6=;:(B) $BJ!1J(B $BE/Li(B$B!&(B($B5~Bg1!9)(B) ($B@5(B)$B9>8}(B $B9@0l(B | Cu spinel Dimethyl ether Steam reforming
| S-37 | 713 |
10:40$B!A(B 11:00 | E306 | $BG3NAEECS8~$1F<7O(BCO$BJQ@.?(G^$N3h@-$K5Z$\$9(BDSS$BA`:n$N1F6A(B ($BL>Bg1!9)(B) $B!{(B($B3X(B)$B8^Eg(B $B42J8(B$B!&(B($B@5(B)$BED@n(B $BCRI'(B$B!&(B($B@5(B)$B;3ED(B $BGn;K(B$B!&(B($B=P8wCf8&(B) ($B@5(B)$B2OEg(B $B5A | CO Shift Cu Catalyst Deactivation
| S-37 | 349 |
(11:00$B!A(B12:00)$B!!(B($B:BD9(B $B5FCON4;J(B) |
11:00$B!A(B 11:20 | E307 | $BG3NAEECS6!5kMQ(BH2$BCf(BCO$B$N8w?(G^$K$h$k;@2==hM}J}K!$N3NN)(B ($B;0=EBg1!9)(B) $B!{(B($B3X(B)$B5WED(B $BM'OB(B$B!&(B($B@5(B)$B@>B<(B $B82(B$B!&(B($B@5(B)$B2CF#(B $B@,;0(B | TiO2 Photocatalyst H2 CO Oxidization
| S-37 | 35 |
11:20$B!A(B 11:40 | E308 | $B%^%$%/%m%A%c%M%k%j%"%/%?$K$*$1$k?eAGH/@8@-G=8~>e(B ($BEl$B!&(B$B>.Ln(B $B>$B!&(B($B@5(B)$B$B!&(B$B8^==:j(B $B5AG7(B | micro channel reformaer gas solid reaction
| S-37 | 937 |
11:40$B!A(B 12:00 | E309 | $BN.DL<0H?1~4o$K$h$kM-5!%O%$%I%i%$%IC&?eAGH?1~FC@-$N2r@O(B ($BElM}Bg(B) $B!{(B($B3X(B)$B>>Eg(B $B59><(B$B!&(B$BDxEg(B $B??:H(B$B!&(B($B@5(B)$B>1Ln(B $B8|(B$B!&(B($B@5(B)$BBgC](B $B>!?M(B$B!&(B$B@FF#(B $BBYOB(B | Organic chemical hydride Methylcyclohexane dehydrogenation Superheated liquid-film-type catalysis
| S-37 | 695 |
(13:00$B!A(B14:00)$B!!(B($B;J2q(B $B;38}LT1{(B) |
13:00$B!A(B 14:00 | E313 | [$BE8K>9V1i(B]$B?e$rJ,2r$9$k8w?(G^$N8=>u$HE8K>(B ($BElBg1!9)(B) $B!{(B($B@5(B)$BF2LH(B $B0l@.(B | photocatalyst hydrogen solar energy
| S-37 | 1119 |
(14:00$B!A(B15:20)$B!!(B($B:BD9(B $BED@nCRI'(B) |
14:00$B!A(B 14:20 | E316 | $BHsDj>o29EYA`:n$K$h$k%F%H%i%j%sC&?eAGH?1~%7%9%F%`$N3+H/(B ($BElM}Bg(B) $B!{(B($B3X(B)$B5mEg(B $B1{$B!&(B($B@5(B)$BDxEg(B $B??:H(B$B!&(B($B@5(B)$B>1Ln(B $B8|(B$B!&(B($B@5(B)$BBgC](B $B>!?M(B$B!&(B($B@5(B)$B:XF#(B $BBYOB(B | tetralin dehydrogenation periodic temperature operation catalytic reactor
| S-37 | 832 |
14:20$B!A(B 14:40 | E317 | $B%a%A%k%7%/%m%X%-%5%s$N$?$a$N?(G^Kl7?H?1~4o$N3+H/(B ($B9-Bg1!9)(B) $B!{(B($B3X(B)$BLpED(B $BOBLi(B$B!&(B($B@5(B)$BETN1(B $BL-N;(B$B!&(B($B@5(B)$B5H2,(B $BJ~5W(B | catalytic-membrane membrane-reactor methylcyclohexane
| S-37 | 812 |
14:40$B!A(B 15:00 | E318 | $B%P%$%b!<%@%k9=B$$rM-$9$k%7%j%+?(G^Kl$K$h$k%a%?%s?e>x5$2~ ($B9-Bg1!9)(B) $B?9ED(B $BC$FA(B$B!&(B($B@5(B)$B5H2,(B $BJ~5W(B$B!&(B$B!{(B($B@5(B)$BETN1(B $BL-N;(B | membrane reactor silica membrane steam reforming of methane
| S-37 | 975 |
15:00$B!A(B 15:20 | E319 | $B%a%?%s?e>x5$2~ ($B2#9qBg1!9)(B) $B!{(B($B3X(B)$B9)F#(B $BM4J?(B$B!&(B($B@5(B)$BAj86(B $B2mI'(B$B!&(B($B@5(B)$B1)?<(B $BEy(B$B!&(B($B@5(B)$BC]Fb(B $BN4(B | methane steam reforming membrane reactor CFD
| S-37 | 1029 |
(15:20$B!A(B16:20)$B!!(B($B:BD9(B $BH,Hx(B $B<"(B) |
15:20$B!A(B 15:40 | E320 | $BN.F0>2?(G^$HKlJ,N%$rMQ$$$k9b@-G=2~ ($BEl5~%,%9(B) $B!{(B($B@5(B)$BGr:j(B $B5AB'(B$B!&(B$B>oLZ(B $BC#Li(B$B!&(B$B0BED(B $BM&(B | hydrogen membrane reformer
| S-37 | 754 |
15:40$B!A(B 16:00 | E321 | $B9bBQ5W@-%a%s%V%l%s7?(BLP$B%,%92~ ($B4dC+;:6H(B) $B!{3a86(B $B>;9b(B$B!&(B$BKRLn(B $BM}(B$B!&(B$B66K\(B $BC$I'(B | Hydrogen Fuel cell Membrane reactor
| S-37 | 371 |
16:00$B!A(B 16:20 | E322 | $B%j%A%&%`%7%j%1!<%H$rMQ$$$?HsJ?9U2~ ($BEl>(B $BIpI'(B$B!&(B($B@5(B)$B1[:j(B $B7r;J(B$B!&(B$B2CF#(B $B2mNi(B | hydrogen lithium silicate ethanol
| S-37 | 932 |