$B9V1i(B $B;~9o(B | $B9V1i(B $BHV9f(B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $BJ,N`(B $BHV9f(B | $B$BHV9f(B | |
P$B2q>l(B $BBh(B1$BF|(B |
17:25$B!A(B 18:45 | P135 | Pt-Rh$B?(G^$K$h$k<+F0t2=H?1~$X$N?e>x5$$N1F6A(B
($B5~Bg9)(B) $B!{(B($B3X(B)$B5HLnC+(B $BBs:H(B $B!&(B ($B3X(B)$B2,(B $BMN51(B $B!&(B ($B@5(B)$B0f>e(B $B85(B $B!&(B (ICT) $B5H@n(B $BN5Lo(B $B!&(B ($B5~Bg9)(B) ($B@5(B)$B2O@%(B $B85L@(B | automotive catalyst reaction model steam
| 5-a | 85 |
17:25$B!A(B 18:45 | P136 | $B%$%=%V%?%s;@2=C&?eAGH?1~$KBP$9$k%^%0%M%7%&%`%b%j%V%G!<%H?(G^$ND4@=>r7o$N1F6A(B
($BFAEgBg1!@hC<650iIt(B) $B!{(B($B3X(B)$B8E@n(B $B9,H~(B $B!&(B ($BFAEgBg1!(BSTS$B8&5fIt(B) ($B@5(B)$BCf@n(B $B7I;0(B $B!&(B ($B@5(B)$B30NX(B $B7r0lO:(B $B!&(B ($B@5(B)$B?y;3(B $BLP(B $B!&(B ($B;0I)%l%$%h%s(B) $B2CF#(B $BM5 $B!&(B $BFs5\(B $B9R(B | oxidative dehydrogenation magnesium molybdates preparation conditions
| 5-a | 15 |
17:25$B!A(B 18:45 | P137 | $B?75,$J%K%C%1%kC4;}C:AG?(G^$rMxMQ$7$?(BCO$B%a%?%M!<%7%g%s(B
($B5~Bg9)(B) $B!{(B($B3X(B)$B2,ED(B $B7CH~(B $B!&(B ($B@5(B)$BiCED(B $BN40l(B $B!&(B ($B@5(B)$B:{2,(B $B1Q;J(B $B!&(B ($B@5(B)$B;01:(B $B9'0l(B | nickel/carbon catalyst CO methanation ion exchange
| 5-a | 125 |
17:25$B!A(B 18:45 | P138 | $B%"%k%+%j?(G^$N@PC:%A%c!<4V$K$*$1$k0\F0$H%,%92=B%?J8z2L(B
($B72Bg1!9)(B) $B!{(B($B3X(B)$B;3ED(B $BM% $B!&(B ($B@5(B)$BAb(B $B7J]o(B $B!&(B ($B@5(B)$B>.@n(B $BM35*;R(B $B!&(B ($B@5(B)$B:4F#(B $BOB9%(B $B!&(B ($B@5(B)$BJuED(B $B63G7(B | Alkali metal Steam gasification Reaction kinetics
| 5-a | 41 |
17:25$B!A(B 18:45 | P139 | $B%^%$%/%m%j%"%/%?!<$K$h$kGr6b(B-$BC:AGJ#9g:`NA$ND4@=(B-$B86:`NA$NG;EY$N1F6A(B-
($B2,;3Bg(B) $B!{(B($B3X(B)$B>eLn(B $BMNJ?(B $B!&(B ($B:eI\Bg(B) ($B@5(B)$BIpF#(B $BL@FA(B $B!&(B ($B2,;3Bg(B) ($B@5(B)$B?{(B $B@?<#(B | microreactor composite material porous carbon
| 5-f | 62 |
17:25$B!A(B 18:45 | P140 | $B29EY<~4|A`:n2<$K$*$1$k%(%?%N!<%kC&?eH?1~(B
($BFAEgBg1!@hC<650iIt(B) $B!{(B($B3X(B)$BCNED(B $BD> $B!&(B ($BFAEgBg1!(BSTS$B8&(B) ($B@5(B)$B30NX(B $B7r0lO:(B $B!&(B ($B@5(B)$B?y;3(B $BLP(B $B!&(B ($B@5(B)$BCf@n(B $B7I;0(B | ethanol dehydration forced temperature cycling conversion
| 5-e | 39 |
17:25$B!A(B 18:45 | P141 | $B%8%c%H%m%U%!L}$N%P%$%*%G%#!<%<%k2=$K$*$1$k%[%k%\!<%k%(%9%F%k$NJ,2r(B
($B6bBt9)Bg1!(B) $B!{(B($B3X(B)$BEh:j(B $B7<2p(B $B!&(B ($B6bBt9)Bg(B) ($B@5(B)$BEZ:4(B $B8w;J(B | Jatropha Biodiesel Fuel phorbol ester
| 5-g | 81 |
17:25$B!A(B 18:45 | P142 | $B%_%K%(%^%k%7%g%s7O$K$*$1$k2D5UE*IT3h@-2=%i%8%+%k=E9g$NB.EYO@(B:1. SRMP, ATRP$B$K$*$1$kFCD'E*N3;R7B(B
($BJ!0fBg1!9)(B) $B!{(B($B3X(B)$BEDCf(B $BGnG7(B $B!&(B $B>eLn(B $BM4;L(B $B!&(B ($B@5(B)$BHtED(B $B1Q9'(B | living radical polymerization emulsion polymerization kinetics
| 5-c | 66 |
17:25$B!A(B 18:45 | P143 | $B%_%K%(%^%k%7%g%s7O$K$*$1$k2D5UE*IT3h@-2=%i%8%+%k=E9g$NB.EYO@(B:2. RAFT$B$K$*$1$kFCD'E*N3;R7B(B
($BJ!0fBg1!9)(B) $B!{(B($B3X(B)$BC+ED(B $BM$Li(B $B!&(B $BBgDP(B $B@?Li(B $B!&(B $B?y;3(B $BBnLo(B $B!&(B ($B@5(B)$BHtED(B $B1Q9'(B | living radical polymerization emulsion polymerization kinetics
| 5-c | 68 |
17:25$B!A(B 18:45 | P144 | RAFT$B=E9gM^@)5!9=$N%_%K%(%^%k%7%g%s=E9g$K$h$k8!F$(B
($BJ!0fBg1!9)(B) $B!{(B($B3X(B)$B7s>>(B $BM$B?(B $B!&(B $B@>B<(B $BM4;R(B $B!&(B ($BJ!0fBg9)(B) $BA}ED(B $B2B7C(B $B!&(B $B;01:(B $B?r;L(B $B!&(B $B6b3$(B $B9MM4(B $B!&(B ($BJ!0fBg1!9)(B) $B:4F#(B $B=(:8%qLg(B $B!&(B ($B@5(B)$BNkLZ(B $B@6(B $B!&(B ($B@5(B)$BHtED(B $B1Q9'(B | RAFT polymerization reaction mechanism miniemulsion polymerization
| 5-c | 104 |
17:25$B!A(B 18:45 | P145 | $BH>2sJ,F}2==E9g$K$*$1$kO":?0\F0:^$N3H;6$N1F6A(B
($BJ!0fBg1!9)(B) $B!{(B($B3X(B)$B $B!&(B $B:4F#(B $B=(:8%qLg(B $B!&(B ($B@5(B)$BNkLZ(B $B@6(B $B!&(B ($B@5(B)$BHtED(B $B1Q9'(B | Emulsion polymerization Chain transfer agent Diffusion
| 5-c | 106 |