$B$BHV9f(B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $BH/I=7A<0(B | |
9 | $B8GDj>2H?1~4o$K$h$k%9%/%"%l%s$N?eAG2=H?1~%W%m%;%9$N3+H/(B ($B;:Am8&(B) ($B@5(B)$B!{J?4V(B $B9(Ci(B$B!&(B $B:4F#(B $B0lI'(B$B!&(B ($BElBg(B) $B>.NS(B $B=$(B$B!&(B ($B;:Am8&(B) ($B@5(B)$B0f>e(B $BJ~Li(B | continuous manufacturing fixed bed reactor hydrogenation
| O |
38 | CuO-ZrO2 catalysts prepared by flame spray pyrolysis for CO2-to-methanol hydrogenation (Seikei U.) ($B@5(B)$B!{(BTada Shohei$B!&(B (ETH Zurich) Larmier Kim$B!&(B Buchel Robert$B!&(B Coperet Christophe | Methanol synthesis Copper Frame spray pyrolysis
| O |
73 | $BB?9&2A(B ($BL>Bg1!9)(B) ($B3X(B)$B!{EDn5(B $BM*GO(B$B!&(B ($B%H%h%?<+(B) ($BK!(B)$BD9Hx(B $BM!(B$B!&(B ($BK-EDCf8&(B) ($B@5(B)$B2CF#(B $B8g(B$B!&(B ($BL>Bg1!9)(B) ($B@5(B)$B;3ED(B $BGn;K(B$B!&(B ($B@5(B)$BED@n(B $BCRI'(B | Gas Diffusion mesopore catalyst
| P |
99 | $B%V%?%s$NC&?eAG$K$h$k%V%?%8%(%s@=B$?(G^$N3+H/(B (JXTG$B%(%M%k%.!<(B) ($BK!(B)$B!{0l[j(B $BN5Li(B$B!&(B ($BK!(B)$BLZB<(B $B?.7<(B$B!&(B ($BK!(B)$B@%@n(B $BFX;J(B$B!&(B ($BK!(B)$BLZ8M8}(B $BAo(B$B!&(B ($BK!(B)$B5H86(B $BF)MF(B$B!&(B ($BK!(B)$B5HB<(B $BM*(B$B!&(B ($BK!(B)$BLx@n(B $B??0lO/(B | butadiene PtSn catalyst butane
| O |
110 | Pt$BFbJqCf6u%7%j%+%J%N%A%e!<%V?(G^$ND4@=$HC&?eAGH?1~MQ?(G^Kl$X$NE,MQ(B ($B?@8MBg1!2J5;%$%N%Y(B/$B@hC$B!&(B ($B@5(B)$BCf@n(B $B7I;0(B$B!&(B ($B@5(B)$B?7C+(B $BBn;J(B$B!&(B ($B?@8MBg1!9)(B/$B@hC$B!&(B ($B@5(B)$B>>;3(B $B=(?M(B$B!&(B ($B?@8MBg1!2J5;%$%N%Y(B/$B@hC | catalytic membrane Pt-silica hollow nanotubes methylcyclohexane dehydrogenation
| P |
114 | $B%W%m%T%l%s$N5$Aj%(%]%-%72=H?1~$K$*$1$k6bB0=$>~(BSBA-15$B?(G^$N8!F$(B ($BFAEgBg1!@hC<650iIt(B) ($B3X(B)$B!{:47,(B $B9/B@(B$B!&(B ($B3X(B)$B2.Ln(B $BM'J](B$B!&(B ($BFAEgBg1!$B!&(B ($B@5(B)$B?y;3(B $BLP(B | Oxidative epoxidation SBA-15 Propylene
| P |
115 | $B%P%J%8%&%`$G2~ ($BFAEgBg1!@hC<650iIt(B) ($B3X(B)$B!{EgDE(B $B>"(B$B!&(B ($B;0I)%1%_%+%k(B) ($B@5(B)$B2CF#(B $BM5$B!&(B ($B@5(B)$BFs5\(B $B9R(B$B!&(B ($BFAEgBg1!$B!&(B ($B@5(B)$B?y;3(B $BLP(B | Oxidative Dehydrogenation Isobutane SBA-15
| P |
137 | Enhancement of hydrogen production via formic acid decomposition on carbon supported Pt-Ni alloy catalysts with high metal loading (Tokyo Tech) ($B3$(B)$B!{(BHanprerakriengkrai S.$B!&(B ($B3X(B)Nakagawa K.$B!&(B ($B@5(B)Fujitsuka H.$B!&(B (Kyoto U.) ($B@5(B)Nakagawa H.$B!&(B (Tokyo Tech) ($B@5(B)Tago T. | Ion-exchange resin Ni-Pt alloy formic acid decomposition
| P |
140 | $B%a%?%N!<%k(B-$BL};i(B2$BAjCf$G$NL};i%H%i%s%9%(%9%F%k2=$NAm3gH?1~B.EY%b%G%k(B ($B%Z%H%m%J%99)Bg(B) ($B3$(B)$B!{>eB<(B $BK';0(B$B!&(B ($B?r>kBg9)(B) $BD9Hx(B $B7<;K(B$B!&(B ($B%Z%H%m%J%99)Bg(B) Han Fon Yee$B!&(B Nguyen Thanh Tien$B!&(B Trinh Thanh Hoai$B!&(B ($B?r>kBg9)(B) ($B@5(B)$BApJI(B $B9n8J(B | transesterification palm oil mass transfer
| O |
148 | $BCbAGCV49(BSBA-15$B$N(BCO2$BJQ49H?1~$KBP$9$k?(G^I>2A$HH?1~B.EY2r@O(B ($BElBg@88&(B) ($B3X(B)$B!{;3:j(B $B@69T(B$B!&(B ($B@5(B)$BLPLZ(B $Bt!I'(B$B!&(B ($B@5(B)$B>.AR(B $B8-(B | Mesoporous silica Kinetics CO2 transformation
| P |
203 | $B%S%9%^%9(B-$B%b%j%V%G%sJ#9g;@2=J*?(G^$KBP$9$k5$Aj;@AG$N1F6A(B ($BFAEgBg1!@hC<650iIt(B) ($B3X(B)$B!{CfHx(B $BM'5*(B$B!&(B ($BFAEgBg9)(B) $B;0Bp(B $BL$2Q(B$B!&(B ($BFAEgBg1!$B!&(B ($B@5(B)$B?y;3(B $BLP(B | Complex Oxides Catalysts Bismuth-Molybdenum Gaseous Oxygen
| P |
247 | Cu-ZnO-Al2O3$B?(G^$K$*$1$k(BCu(0)$B ($B?@8MBg@hC$B!&(B ($B?@8MBg1!9)(B) $B@tLn(B $B9*(B$B!&(B $BKY9>(B $BBY90(B$B!&(B $BF#ED(B $BN<(B$B!&(B (Grenoble INP) Fontana Marie$B!&(B ($B?@8MBg1!9)(B) ($B@5(B)$B23K\(B $BFF;K(B$B!&(B ($B@5(B)$B;T66(B $BM40l(B$B!&(B ($B@5(B)$B@>;3(B $B3P(B | Oxidation behavior of Cu(0) species Water-gas shift reaction Cu-ZnO-Al2O3
| O |
274 | Ni$B7O9=B$BN?(G^$,%a%?%s$N%*!<%H%5!<%^%k%I%i%$2~ ($B@EBg1!9)(B) ($B@5(B)$B!{EOIt(B $B0=(B$B!&(B ($B3X(B)$BJ?Hx(B $B0lM[(B$B!&(B ($B3X(B)$B@nyu(B $BOK(B$B!&(B $B2OLn(B $BK'3$(B$B!&(B ($B@5(B)$BJ!86(B $BD9 | Auto-thermal reforming Structured catalyst Electroless plating
| O |
276 | Effect of boron and phosphor promoters on NiMo-based catalyst for hydrodeoxygenation of palm oil (Shizuoka U.) ($B3X(B)$B!{(BDwiratna Bralin$B!&(B (ITB) Subagjo$B!&(B Makertiharta Igbn$B!&(B Laniwati Melia$B!&(B (Shizuoka U.) ($B@5(B)Watanabe Ryo$B!&(B ($B@5(B)Fukuhara Choji | Vegetable oil Hydrodeoxygenation NiMo catalyst, Boron
| O |
284 | $B%j%0%K%s$rC:AG8;$H$7$F@=B$$7$?%b%j%V%G%s?(G^>e$G$N%.;@J,2rH?1~(B ($B90A0BgM}9)(B) ($B3X(B)$B!{(BKurnia Irwan$B!&(B ($B90A0Bg?7%(%M8&(B) $B5HED(B $BZ|90(B$B!&(B ($B90A0BgM}9)(B) ($B@5(B)$B0$I[(B $BN$Ds(B$B!&(B ($B90A0Bg?7%(%M8&(B) ($B@5(B)$B41(B $B9q@6(B | Lignin molybdenum carbide formic acid decomposition
| P |
318 | Fischer-Tropsch$B9g@.MQ%3%P%k%H(B-$BGr6bC4;}&B7?%<%*%i%$%H?(G^$NFC@-I>2A(B ($B2,;3Bg1!4D@8(B) ($B3X(B)$B!{Cf@>(B $B??F`H~(B$B!&(B ($B@5(B)Uddin Md. Azhar$B!&(B ($B@5(B)$B2CF#(B $B2E1Q(B$B!&(B ($B2,;3Bg(BRCIS/$B2,;3Bg1!<+(B) $B?N2J(B $BM&B@(B | Fischer-Tropsch synthesis cobalt catalyst gasoline
| P |
355 | $BF};@%a%A%k2C?eJ,2rH?1~$K$h$kF};@9g@.$NH?1~B.EYO@$N8!F$(B ($BFAEgBg1!9)(B) ($B3X(B)$B!{CfLn(B $BM/:H(B$B!&(B ($BFAEgBg1!M}9)(B) ($B3$(B)Alcantara Avila J. Rafael$B!&(B ($B@5(B)$B30NX(B $B7r0lO:(B$B!&(B ($B@5(B)$BKY2O(B $B=S1Q(B$B!&(B ($B;:Am8&(B) ($B@5(B)$B;3LZ(B $BM:Bg(B | Methyl lactate hydrolysis Heterogeneous catalyst Lactic acid concentration
| P |
388 | Mg1-xNixAl2O4$B%9%T%M%kJ#9g;@2=J*$rMQ$$$?%a%?%s(BCO2$B2~ ($BElBg1!9)(B) ($B@5(B)$B!{5FCO(B $BN4;J(B$B!&(B $BM{(B $BCR4A(B$B!&(B ($B@5(B)$B9b3@(B $BFX(B$B!&(B Oyama S. T. | Magnesium aluminate spinel Nickel catalyst CO2 reforming
| O |
435 | $B%O%$%7%j%+$J(BBeta$B%<%*%i%$%H$X$N0[ ($B:eBg1!4p9)(B) ($B3X(B)$B!{Cf0f(B $B2mBg(B$B!&(B ($B3X(B)$B;0Bp(B $B9@;K(B$B!&(B ($B3X(B)$B>.Ln(B $B3+EP(B$B!&(B ($B@5(B)$BW"ED(B $BM:0lO/(B$B!&(B ($B@5(B)$BFbED(B $B9,L@(B$B!&(B ($B@5(B)$B@>;3(B $B7{OB(B | zeolite gallosilicate PDH reaction
| P |
484 | OSDA$B%U%j!$B!v(BBEA$B7?%<%*%i%$%H$K$h$k1v4p?(G^H?1~(B ($BElBg@88&(B) ($B@5(B)$B!{LPLZ(B $Bt!I'(B$B!&(B ($B@5(B)$B>.AR(B $B8-(B | zeolite Knoevenagel reaction
| O |
499 | $B%k%F%K%&%`C4;};@2=%;%j%&%`?(G^$rMQ$$$?%P%$%*%^%9M3Mh4^;@AG2=9gJ*$NA*BrE*C:AG(B-$BC:AG7k9g@ZCGH?1~7O$N3+H/(B ($B:eBg1!4p9)(B) ($B@5(B)$B!{?e3@(B $B6&M:(B$B!&(B $B>e?y(B $B98J?(B$B!&(B $B?7ED(B $B98Bg(B$B!&(B ($B@5(B)$BA0Ln(B $BA5(B$B!&(B ($B@5(B)$BK~N1(B $B7I?M(B$B!&(B ($B@5(B)$BUi@n(B $B9@0lO:(B$B!&(B ($B:eBgB@M[%(%M(B) $B6bED(B $B@6?C(B | biomass C-C bond cleavage heterogeneous catalyst
| O |
500 | $B ($B;:Am8&(B) ($B@5(B)$B!{J!ED(B $B5.;K(B$B!&(B $B86ED(B $BN<(B$B!&(B ($B@5(B)$B@nGH(B $BH%(B$B!&(B $B5\Bt(B $BE/(B | methane reforming catalyst oxidation method
| O |
518 | $B9b3h@-!"9bA*BrE*$J(BPt/$B%8%s%3%7%j%1!<%H%<%*%i%$%H?(G^$rMQ$$$?%W%m%Q%s$NC&?eAGH?1~(B ($BElBg1!9)(B) ($B3X(B)$B!{@.ED(B $B2BM4(B$B!&(B ($B@5(B)Chaikittisilp Watcharop$B!&(B ($B@5(B)$BBg5WJ](B $BC#Li(B | Zeolite Propane dehydrogenation Pt/zincosilicate
| P |
562 | $B%0%j%;%m!<%kJQ49H?1~$r%1!<%9%9%?%G%#!<$H$7$?%j%]%=!<%`(B/$B6bB0?(G^J#9gBN$N5!G=I>2A(B ($B2,;3Bg1!4D@8(B) ($B3X(B)$B!{@>8}(B $BN=B@(B$B!&(B ($B@5(B)$BEgFb(B $B$B!&(B ($B@5(B)$BLZB<(B $B9,7I(B | Liposome glycerol Metal catalyst
| P |
569 | NH3$B40A4J,2r$rL\E*$H$7$?(BCNTs$BHoJ$N.F0G^BN(B ($B72BgM}9)(B) ($B3X(B)$B!{?7J](B $B5.Li(B$B!&(B ($B72Bg1!M}9)(B) ($B@5(B)$BLnED(B $BNh<#(B | CNTs Ammonia conversion Fluid catalytic cracking
| P |
585 | $B6bB0?(G^$N%Y%7%/%kKl>e$K$*$1$k<+8J=8@QFC@-$H=E9gH?1~$X$N1~MQ(B ($B2,;3Bg1!4D@8(B) ($B3X(B)$B!{c7F#(B $B>-J?(B$B!&(B ($B@5(B)$BEgFb(B $B$B!&(B ($B@5(B)$BLZB<(B $B9,7I(B | vesicle polymerization catalyst
| P |
614 | Pt$BC4;}%<%*%i%$%H?(G^$K$h$k(Bn-$B%G%+%s0[@-2=!&?eAG2=J,2r(B ($BEl9)Bg1!J*$B!&(B ($B@5(B)$BF#J/(B $BBgM5(B$B!&(B ($B@5(B)$BB?8P(B $B516=(B | zeolite isomerization hydrocarbon
| P |
634 | $B%Q%i%8%&%`$r8GDj2=$7$?B?9& ($B6eBg1!9)(B) ($B3X(B)$B!{>>K\(B $B8w(B$B!&(B ($B@5(B)$B@1Ln(B $BM'(B$B!&(B ($B@5(B)$B;01:(B $B2B;R(B | Flow synthesis Polymer gel Palladium
| P |
702 | $B%R%I%m%-%7%"%Q%?%$%H$NE:2C$,5Z$\$98GBN?(G^$N%"%s%b%K%"J,2r3h@-$X$N1F6A(B ($BBg:e5;8&(B) ($B@5(B)$B!{1JW"(B $BBn:H(B$B!&(B ($B@5(B)$BJR6M(B $B0l>4(B | ammonia decomposition hydrogen solid catalyst
| O |
712 | Cu-ZSM-5$B%<%*%i%$%H7k>=Fb$K$*$1$k(BNO$B$H(BNH3$B$N3H;678?tB,Dj(B ($BKLBg1!9)(B) ($B3X(B)$B!{?@ED(B $BBs3$(B$B!&(B ($B@5(B)$BCf:d(B $BM$B@(B$B!&(B ($B@5(B)$B5H@n(B $BBvLi(B$B!&(B ($B@5(B)$BA}ED(B $BN4IW(B | Intracrystalline diffusivity Cu-ZSM-5 NO
| P |
745 | $B29OB$J>r7o2<$G%"%_%I$r4T85$9$k%P%$%a%?%k%J%NN3;R?(G^$N3+H/(B ($B:eBg4p9)(B) ($B@5(B)$B!{K~N1(B $B7I?M(B$B!&(B $B9b66(B $B0l9-(B$B!&(B ($B@5(B)$BA0Ln(B $BA5(B$B!&(B ($B@5(B)$B?e3@(B $B6&M:(B$B!&(B ($B@5(B)$BUi@n(B $B9@0lO:(B$B!&(B ($B@5(B)$B6bED(B $B@6?C(B | heterogeneous catalyst nanoparticle green chemistry
| O |
779 | Ni$B%I!<%WE4;@2=J*7O9=B$BN?(G^>e$N?e@-%,%9%7%U%HH?1~5!9=$N2r@O(B ($B@EBg1!Am2J(B) ($B3X(B)$B!{EDEg(B $B7r:c(B$B!&(B ($B@EBg9)(B) $BIz8+(B $BM4:H(B$B!&(B ($B@EBg1!Am2J(B) $BJ?ED(B $BK>(B$B!&(B $B2OLn(B $BK'3$(B$B!&(B ($B@5(B)$BEOIt(B $B0=(B$B!&(B ($B@5(B)$BJ!86(B $BD9 | Structured catalyst Water gas shift Reaction mechanism
| P |
780 | NO$B4T85H?1~MQ(BPt$B7O?(G^$N%W%m!<%VJ,;R$rMxMQ$7$?3h@-%5%$%H$N2r@O(B ($B@EBg1!Am2J(B) ($B3X(B)$B!{9uED(B $B=$J?(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 | CO adsorption Pt-based catalyst FT-IR
| P |
800 | $B?(G^E*%U%m!<9g@.$r;X8~$7$?B?9& ($B6eBg9)(B) ($B3X(B)$B!{I~It(B $B=U9a(B$B!&(B ($B6eBg1!9)(B) ($B@5(B)$B>>K\(B $B8w(B$B!&(B ($B@5(B)$B@1Ln(B $BM'(B$B!&(B ($B@5(B)$B;01:(B $B2B;R(B | monolith flow reactor catalyst
| P |