$B$BHV9f(B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $BH/I=7A<0(B | |
7 | Ni$B$J$i$S$K(BRu$B?(G^>e$G$N%"%s%b%K%"$NJ,2rB.EYO@2r@O(B ($B;:Am8&(B) ($B@5(B)$B!{9b66(B $B8|(B$B!&(B ($B@5(B)$BF#C+(B $BCiGn(B | ammonia decomposition Hydrogen production Kinetic model
| O |
38 | $B9bHfI=LL@Q;@2=%;%j%&%`$N?eG.9g@.$H%"%k%3!<%kC&?e$K$*$1$k?(G^FC@-(B ($BFAEgBg1!@hC<650iIt(B/$B0$Fn2=@.(B) ($B@5(B)$B!{BgC](B $B>09'(B$B!&(B ($BFAEgBg1!@hC<650iIt(B) ($B3X(B)$B;3:,(B $B7=5.(B$B!&(B ($BFAEgBg1!(BSTS$B8&(B) ($B@5(B)$BCf@n(B $B7I;0(B$B!&(B ($B@5(B)$B2CF#(B $B2mM5(B$B!&(B ($B@5(B)$B?y;3(B $BLP(B | Cerium oxide Hydrothermal synthesis Catalytic dehydration
| O |
39 | $B%$%*%s8r49K!$GD4@=$7$?(BCr-FSM-16$B$N9=B$2r@O$H%$%=%V%?%s;@2=C&?eAG?(G^3h@-(B ($BFAEgBg1!@hC<650iIt(B) ($B3X(B)$B!{HD3@(B $B0&(B$B!&(B ($BFAEgBg1!(BSTS$B8&(B) $BAR2J(B $B>;(B$B!&(B ($B@5(B)$BCf@n(B $B7I;0(B$B!&(B ($B@5(B)$B2CF#(B $B2mM5(B$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 $B9R(B | Isobutane Oxidative dehydrogenation FSM-16
| P |
40 | MCM-41$B$N%$%=%V%?%s$N;@2=C&?eAGH?1~$KBP$9$k?(G^3h@-$N2~A1(B ($BFAEgBg1!@hC<650iIt(B) ($B3X(B)$B!{1JW"(B $BBn:H(B$B!&(B ($BFAEgBg9)(B) ($B3X(B)$B;0@4(B $B1{ps(B$B!&(B ($BFAEgBg1!(BSTS$B8&(B) $BAR2J(B $B>;(B$B!&(B ($B@5(B)$BCf@n(B $B7I;0(B$B!&(B ($B@5(B)$B2CF#(B $B2mM5(B$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 isobutane MCM-41
| P |
152 | $BE49[@P$rMQ$$$?%0%j%;%j%sJ,2r$K$h$k9bG.NL%,%9$N@=B$(B ($B6eBg(B) ($B@5(B)$B!{@F4V(B $BEy(B$B!&(B ($BKL6e;TBg(B) ($B@5(B)$BD+8+(B $B8-Fs(B$B!&(B (JFE$B%9%A!<%k(B) ($BK!(B)$BLPLZ(B $B9/90(B | glycerol iron ore decomposition
| O |
169 | $B%9%Q%$%i%k7?(BPt/TiO2$B7O9=B$BN?(G^$K$h$k%a%A%k%7%/%m%X%-%5%s$NC&?eAGH?1~(B ($B@EBg1!9)(B) ($B3X(B)$B!{EDCf(B $B98B@(B$B!&(B $B5W>>(B $B5AOB(B$B!&(B ($B3X(B)$B;3K\(B $BOB@5(B$B!&(B $B2OLn(B $BK'3$(B$B!&(B ($B@5(B)$BEOIt(B $B0=(B$B!&(B ($B@5(B)$BJ!86(B $BD9 | methylcyclohexane dehydrogenation spiral-type structured catalyst
| P |
171 | $B;@2==hM}$d(BRe$BE:2C$,(BPt/TiO2$B?(G^$N%a%A%k%7%/%m%X%-%5%sC&?eAGH?1~$K5Z$\$91F6A(B ($B@EBg1!9)(B) ($B3X(B)$B!{;3K\(B $BOB@5(B$B!&(B ($B@EBg9)(B) $Bh_Be(B $BM4Li(B$B!&(B ($B@EBg1!9)(B) $B2OLn(B $BK'3$(B$B!&(B ($B@5(B)$BEOIt(B $B0=(B$B!&(B ($B@5(B)$BJ!86(B $BD9 | Organic chemical hydride Methylcyclohexane Pt-based catalyst
| P |
194 | Cu/CeO2$B?(G^$N(BCO$B;@2=3h@-$K$*$1$k(BCr$BE:2C8z2L(B ($B7'Bg(B/$B5~Bg?(G^EECS(B) ($B@5(B)$B!{K'ED(B $B2E;V(B$B!&(B ($B7'Bg(B) $B2,It(B $BM-N$(B$B!&(B $B;32<(B $BE5;R(B$B!&(B ($B7'Bg(B/$B5~Bg?(G^EECS(B/JST$B$5$-$,$1(B) $BF|7((B $BAo;N(B$B!&(B ($B7'Bg(B/$B5~Bg?(G^EECS(B) $BD.ED(B $B@5?M(B | CO oxidation composite metal oxide copper
| O |
239 | $B79 ($B:eBg1!4p9)(B) ($B3X(B)$B!{;3ED(B $BKcM32B(B$B!&(B ($B@5(B)$BFbED(B $B9,L@(B$B!&(B ($B@5(B)$B@>;3(B $B7{OB(B | zeolite MFI para-xylene
| P |
273 | $BC4;}(BPt-Pd$B?(G^D4@=;~$N%_%j%9%A%s;@E:2C$K$h$k3h@-8~>e8z2L(B ($B6eBg1!9)(B) ($B3X(B)$BD%(B $BJ8%3%s(B$B!&(B ($B@5(B)$B>>:,(B $B1Q$B!&(B ($B@5(B)$BC]Cf(B $BAT(B$B!&(B ($B@5(B)$B!{4_ED(B $B>;9@(B | Pt-Pd Catalyst Myristic Acid Decane Oxidation
| O |
284 | $B8GBN9bJ,;R7AG3NAEECSH?1~4o$rMQ$$$?%"%k%3!<%k$NA*Br;@2=H?1~(B ($BL>Bg1!9)(B) ($B3X(B)$B!{A%66(B $BOB$B!&(B ($B@5(B)$B5\ED(B $B9/;K(B$B!&(B ($B@5(B)$B;3ED(B $BGn;K(B$B!&(B ($B@5(B)$BED@n(B $BCRI'(B | fuel cell reactor selective oxidation cyclic voltammetry
| P |
287 | $B;@2=E47O?(G^$rMQ$$$?@\?(J,2rH?1~$K$h$k%j%0%K%s2DMO2=1U$+$i$N%U%'%N!<%kN`@=B$(B ($BKLBg1!9)(B) ($B3X(B)$B!{>.@>(B $BN$B!&(B $B@nKt(B $BM&Mh(B$B!&(B $B$B!&(B $BH,LZ(B $BB@0l(B$B!&(B ($B=P8w6=;:(B) ($B@5(B)$B>.;3(B $B7$B!&(B ($BKLBg1!9)(B) ($B@5(B)$BCf:d(B $BM$B@(B$B!&(B ($B@5(B)$BB?8P(B $B516=(B$B!&(B ($B@5(B)$BA}ED(B $BN4IW(B | Lignin Phenolic compounds Iron Oxide
| P |
307 | $B%U%'%N!<%k9g@.H?1~$KMQ$$$k(BCu/HZSM-5$B?(G^$X$N6bB0E:2C8z2L(B ($B?@8MBg1!9)(B) ($B@5(B)$B!{;T66(B $BM40l(B$B!&(B ($B3X(B)$BEOJU(B $B=Y(B$B!&(B $B5L(B $B@/9((B$B!&(B ($B3X(B)$B23K\(B $BFF;K(B$B!&(B ($B@5(B)$BC+20(B $B7$B!&(B ($B@5(B)$B@>;3(B $B3P(B | partial oxidation phenol synthesis Cu/HZSM-5
| O |
322 | $BDc>x5$1?E>2<$G$N%5%o!<%7%U%H?(G^$NH?1~A*Br@-(B ($BF|N)F|8&(B) ($B@5(B)$B!{:4!9LZ(B $B?r(B$B!&(B ($B@5(B)$BNkLZ(B $BJ~;R(B | shift catalyst reaction rselectivity side reaction
| O |
377 | $B<+F0 ($BF|K\<+F005W(B$B!&(B ($BK-EDCf8&(B) ($B@5(B)$B2CF#(B $B8g(B$B!&(B $BEDJU(B $BL-5.(B$B!&(B ($B%H%h%?<+(B) $B;01:(B $B??=((B$B!&(B $BNkLZ(B $B9(>;(B | catalyst washcoat simulation
| O |
475 | $B%j%]%=!<%`$H6bB0$NJ#9g?(G^$ND4@=$HH?1~FC@-$NI>2A(B ($B2,;3Bg1!4D6-@8L?(B) ($B3X(B)$B!{9b66(B $BM&5.(B$B!&(B ($B@5(B)$BEgFb(B $B$B!&(B ($B3X(B)$B=P8}(B $B9,;J(B$B!&(B ($B@5(B)$BLZB<(B $B9,7I(B | liposome catalyst
| P |
526 | $B%$%*%s1UBN$,7A@.$9$kH?1~>l$,%j%Q!<%(G^$KM?$($k1F6A(B ($B6eBg1!9)(B) ($B3X(B)$B!{@nO2(B $BBn;N(B$B!&(B ($B3X(B)$BGO>l(B $BM:;0(B$B!&(B ($B@5(B)$B8eF#(B $B2m9((B$B!&(B ($B@5(B)$B?@C+(B $BE5Jf(B | ionic liquids enzymatic reaction lipase hydrolysis
| P |
560 | $B%$%*%s1UBN!>(BTEOS $B=E=L9gBN?(G^$N3+H/(B ($BElKLBgB?858&(B) ($B3X(B)$BLn4V(B $B?9B@O:(B$B!&(B ($B?73cBg<+A32J(B) $BGk86(B $B5WBg(B$B!&(B ($BElKLBgB?858&(B) ($B@5(B)$BIZED(B $BBgJe(B$B!&(B $B6,(B $B_c(B$B!&(B ($B@5(B)$B!{2#;3(B $B@i><(B | ionic liquid TEOS polymer catalyst
| O |
601 | $B%\%H%`%"%C%WK!$K$h$kC1AX%K%*%V;@%J%N%7!<%H8w?(G^$ND4@=$H?e(B/$B%a%?%N!<%kMO1U$+$i$N?eAG@8@.(B ($BFAEgBg1!(BSTS$B8&(B) ($B@5(B)$B!{Cf@n(B $B7I;0(B$B!&(B ($B@5(B)$B2CF#(B $B2mM5(B$B!&(B ($B@5(B)$B?y;3(B $BLP(B$B!&(B (U. Oxford) Tsang S. C. E. | nanosheet photocatalyst niobate
| O |
739 | $B%$%s%I%M%7%"$KE,9g$7$?Dc%3%9%H%a%?%N!<%k9g@.?(G^(B ($B72Bg9)(B) ($B3X(B)$B!{0f8}(B $B[Y(B$B!&(B ($B72BgM}9)(B) ($B@5(B)$BLnED(B $BNh<#(B | catalyst methanol synthesis
| P |
797 | $B%7%j%3%s%^%$%/%m?(G^H?1~4o$NH?1~FC@-$KBP$9$kC4;}?(G^D4@=K!$N1F6A(B ($BL>Bg1!9)(B) ($B3X(B)$B!{;3yu(B $BBsLi(B$B!&(B ($B@5(B)$B;3ED(B $BGn;K(B$B!&(B ($B@5(B)$BED@n(B $BCRI'(B | micro reactor catalyst silicon
| P |
806 | GTBE$B9g@.H?1~B%?J$N$?$a$N%+!<%\%s7O?(G^3+H/5Z$SM6EEN(B,Dj(B ($B7'Bg1!<+(B) $B!{FbLg(B $B??G72p(B$B!&(B ($B@5(B)Quitain Armando$B!&(B ($B7'Bg%Q%k%9%Q%o!<8&(B) ($B@5(B)$B:4!9LZ(B $BK~(B$B!&(B ($B7'Bg1!<+(B) $BLZED(B $BE0Li(B | glycerin microwave carbon catalysts
| O |
818 | $B8GBN9bJ,;R7AG3NAEECS%+%=!<%I$NL5 ($B5~Bg9)(B) ($B@5(B)$B!{2O@%(B $B85L@(B$B!&(B ($B3X(B)$B0$A>>B(B $BHt97(B$B!&(B ($B3X(B)$BD9hS(B $B4p@8(B$B!&(B ($B@5(B)$B1F;3(B $BH~HA(B$B!&(B ($B@5(B)$B0f>e(B $B85(B | Polymer electrolyte fuel cell Cathode model Oxygen reduction reaction
| O |
819 | $BN.F0AX(BNH3$BJ,2r$rL\E*$H$7$?(BCNTs$BC4BN$N@=B$(B ($B72Bg9)(B) ($B3X(B)$B!{OL^<(B $B63Li(B$B!&(B ($B72BgM}9)(B) ($B3X(B)$BG.3$(B $BNIJe(B$B!&(B ($B@5(B)$BLnED(B $BNh<#(B | NH3 decomposition CNTs fluidized-bed
| P |
821 | $BIT6Q0l?(G^H?1~$K$*$1$k3h@-%5%$%HG;EYI>2AK!$N3+H/(B ($BJ!Eg9b@l(B) ($B@5(B)$B@DLZ(B $B | heterogeneous catalytic reaction active site concentration reaction kinetics
| O |