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19 | 2$B857O6bB0=$>~(BSBA-15$B?(G^$K$h$k%$%=%V%?%s$N;@2=C&?eAGH?1~(B ($BFAEgBg1!@hC<650iIt(B) ($B3X(B)$B!{@^It(B $B7rB@(B$B!&(B $B?7ED(B $B??Li(B$B!&(B ($B;0I)%1%_%+%k(B) ($B@5(B)$B2CF#(B $BM5$B!&(B ($B@5(B)$BFs5\(B $B9R(B$B!&(B ($BFAEgBg9((B$B!&(B ($B@5(B)$B2CF#(B $B2mM5(B$B!&(B ($B@5(B)$B?y;3(B $BLP(B | SBA-15 Oxidative dehydrogenation Isobutane
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20 | $B4T85=hM}$r;\$7$?3F~?(G^$K$h$k%W%m%T%l%s$N%(%]%-%72=H?1~(B ($BFAEgBg1!@hC<650iIt(B) ($B3X(B)$B!{NS(B $BBYHO(B$B!&(B ($B3X(B)$B:47,(B $B9/B@(B$B!&(B ($BFAEgBg1!9((B$B!&(B ($B@5(B)$B2CF#(B $B2mM5(B$B!&(B ($B@5(B)$B?y;3(B $BLP(B | Epoxidation Propylene Metal-doping catalysts
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21 | $B%S%9%^%9(B-$B%b%j%V%G%s7OJ#9g;@2=J*$K$h$k%W%m%T%l%s$N@\?(JQ49$K4X$9$k5$Aj;@AG$N1F6A(B ($BFAEgBg1!@hC<650iIt(B) ($B3X(B)$B!{;0Bp(B $BL$2Q(B$B!&(B ($B3X(B)$BCfHx(B $BM'5*(B$B!&(B ($BFAEgBg1!9((B$B!&(B ($B@5(B)$B2CF#(B $B2mM5(B$B!&(B ($B@5(B)$B?y;3(B $BLP(B | Propylene Catalytic oxidation Bismuth-molybdenum
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22 | $B7\J5>F5Q3%$+$i$N%j%s;@%+%k%7%&%`2s<}$K4X$9$k4pAC8&5f(B ($BFAEgBg1!@hC<650iIt(B) ($B3X(B)$B!{OF:d(B $B8-Fs(B$B!&(B ($BFAEgBg1!9((B$B!&(B ($B@5(B)$B2CF#(B $B2mM5(B$B!&(B ($B@5(B)$B?y;3(B $BLP(B | Calcium Phosphate Chicken Manure Incineration Ash
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77 | $BG[8~@-$rM-$9$k;@2=J*$N2=3X=hM}$rMQ$$$?B?9&2=(B ($B:eI\Bg1!9)(B) ($B3X(B)$B!{2CEg(B $B=iFA(B$B!&(B ($B@5(B)$B2,K\(B $B>0$B!&(B ($B@5(B)$BsnF#(B $B>fLw(B | Porous Chemical Treatment
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250 | $BN.F0?(G^AX$K$*$1$k%,%95[Ce$K5/0x$7$?0l;~E*$JHsN.F02=8=>](B ($B$B!&(B ($B@5(B)$B9CHe(B $B7IH~(B$B!&(B ($B@5(B)$BCfN$(B $BJY(B | Reactor Fluidized bed Defluidization
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343 | $BN.F0?(G^AXH?1~4o$K$*$$$F%,%9J*@-$,5$K"5sF0$X1F6A$r5Z$\$9%a%+%K%:%`$K$D$$$F(B ($B$B!&(B ($B@5(B)$B9CHe(B $B7IH~(B$B!&(B ($B@5(B)$BCfN$(B $BJY(B | Reactor Fluidized bed Bubble
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344 | $B29OB$J>r7o2<$G$N%"%k%+%j?(G^$K$h$kC:;@%8%a%A%k$rMQ$$$?%J%?%ML}$N%(%9%F%k8r49H?1~(B ($BeED(B $BM*N$(B$B!&(B ($B@5(B)$B9CHe(B $B7IH~(B$B!&(B ($B@5(B)$BCfN$(B $BJY(B | Esterification Biodiesel Dimethyl carbonate
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350 | $B9b299b05?e$rMQ$$$?HyJ4:U%P%,%9$+$i$N%-%7%m!<%9$*$h$S%-%7%m%*%j%4E|$N9g@.(B ($B0l4X9b@l(B) ($B3X(B)$B!{;01:(B $BKcN$F`(B$B!&(B ($B2-Fl9b@l(B) ($B@5(B)$BJ!B<(B $BBnLi(B$B!&(B ($B0l4X9b@l(B) ($B@5(B)$BFs3,F2(B $BK~(B | Hydrothermal Treatment Bagasse Xylose and Xylo-oligosaccharide
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467 | $BG3>F7W;;$K$*$1$kHs%K%e!<%H%sK!E*$J7W;;K!(B ($B;:Am8&(B) ($B@5(B)$B;0Eg(B $B42(B | combustion calculation technique
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474 | $B%^%$%/%m%U%m!<%j%"%/%?!<$rMQ$$$?%1%H%s$N%"%k%I!<%k=L9gH?1~(B (JNC) ($BK!(B)$B!{8EN$(B $B?-0l(B$B!&(B ($BK!(B)$B@nn5(B $B=S9T(B$B!&(B ($BK!(B)$BN)2V(B $B9LJ?(B | micro flow reactor aldol condensation ketone
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483 | $BC4;}(BPd$B?(G^$rMQ$$$?(B4-$B%1%H%$%=%[%m%s$NA*BrE*?eAG2=$K$*$1$kMOG^8z2L(B ($BKLBg1!9)(B) ($B3X(B)$B!{2#Hx(B $BAOB@(B$B!&(B ($B@5(B)$BF#ED(B $B?J0lO:(B | heterogeneous catalysis hydrogenation selectivity
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579 | $BL5?(G^%a%?%s9b05;@2=FC@-$N\:YH?1~B.EY%b%G%k$K4p$E$/?tCM2r@O(B ($BL>Bg1!9)(B) ($B3X(B)$B!{6yED(B $BH;M$(B$B!&(B ($B@5(B)$BD.ED(B $BMN(B$B!&(B ($B@5(B)$BB'1J(B $B9TMG(B | methane oxidation high pressure flow reactor
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614 | $B%,%9H/@8FC@-$H%A%c!<2=3X9=B$$N>pJsE}9g$K4p$E$/@PC:G.J,2r5!9=$N2r@O(B ($BL>Bg1!9)(B) ($B3X(B)$B!{J!2,(B $BE4Li(B$B!&(B ($B@5(B)$BD.ED(B $BMN(B$B!&(B ($B@5(B)$BB'1J(B $B9TMG(B | coal pyrolysis chemistry
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617 | SPCP$BH?1~4o$rMQ$$$?3F ($BAO2ABg1!9)(B) ($B3X(B)$B!{9>F#(B $BfF(B$B!&(B ($BAO2ABgM}9)(B) ($B@5(B)$B0fED(B $B=\0l(B$B!&(B ($B@5(B)$B>>;3(B $BC#(B$B!&(B ($B@5(B)$B;3K\(B $B1QIW(B | nonthermal plasma VOC decomposition power frequency
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724 | $B?eAG2=$HC&?eAG$rAH$_9~$`%W%m%;%9@_7W$N$?$a$N(BPt/TiO2$B$H(BNi/CeO2$B>e$G$NF0NO3XB,Dj(B ($B@EBg1!(B) ($B3X(B)$B!{;3yu(B $B70(B$B!&(B ($BE7Ln9)8&(B) ($B3$(B)Ratchahat Sakhon$B!&(B ($B@EBg1!(B) ($B@5(B)$BEOIt(B $B0=(B$B!&(B $B2OLn(B $BK'3$(B$B!&(B ($B@5(B)$BJ!86(B $BD9 | Methylcyclohexane dehydrogenation CO2 methanation Kinetic analysis
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826 | $B8:05G.(BCVD$BK!$G:n@=$7$?%"%k%_%K%&%`%I!<%W;@2=0!1tGvKl$NHfDq93(B ($BEl3$Bg1!9)(B) ($B3X(B)$B!{:,4_(B $B9RM4(B$B!&(B ($B@5(B)$B=);3(B $BBY?-(B | CVD Al-dope zinc oxide resisitivity
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839 | Y$BE:2C(BPt$B?(G^>e$K$*$1$k%a%A%k%7%/%m%X%-%5%sC&?eAGH?1~(B ($B6eBg1!9)(B) ($B3X(B)$B!{5HED(B $BOB98(B$B!&(B $B6b(B $B9d;3(B$B!&(B ($B@5(B)$B>>:,(B $B1Q$B!&(B ($B@5(B)$B;3K\(B $B9d(B$B!&(B ($B@5(B)$B4_ED(B $B>;9@(B | methylcyclohexane dehydrogenation Yttrium Platinum catalyst
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863 | $BC:AGC4;}6bB0?(G^$NN3;R7ABV$,3h@-$K5Z$\$91F6A(B ($B;37ABg1!M}9)(B) ($B3X(B)$B!{@PDM(B $BBg98(B$B!&(B ($B@5(B)$B<58M(B $B>;9-(B$B!&(B ($B@5(B)$BBgC](B $BE/Li(B | Catalyst Methanol steam reforming reaction Woody biomass
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975 | $B%W%m%H%sEAF3BN$r?(G^C4BN$KMQ$$$?%U%'%N!<%k$N?eAG2=C&;@AG(B ($B?.=#Bg1!AmM}9)(B) ($B3X(B)$B!{NkLZ(B $B;V?%(B$B!&(B ($B?.=#BgA!0](B) ($B@5(B)$BD9ED(B $B8w@5(B$B!&(B ($B@5(B)$BJ!D9(B $BGn(B$B!&(B ($B@5(B)$B9b66(B $B?-1Q(B$B!&(B ($B@5(B)$BEhED(B $B8^I4N$(B | hydrodeoxygenation phenol proton conductor
| P |
983 | $B2CMOG^J,2r$rMQ$$$?%Q!<%`3K3L(B(PKS)$B$+$i$N%P%$%*%*%$%k@=B$(B ($B?.=#Bg1!AmM}9)(B) ($B3X(B)$B!{8MED(B $BN6B@(B$B!&(B ($B%f!<%0%l%J(B) $B>>K\(B $BBsLi(B$B!&(B $BB@ED(B $B@25W(B$B!&(B $BNkLZ(B $B7r8c(B$B!&(B ($B@iBeED2=9)(B) ($B@5(B)$B9bDM(B $BF)(B$B!&(B ($B?.=#BgA!0](B) ($B@5(B)$BEhED(B $B8^I4N$(B | palm kernel shell (PKS) liquefaction solvolysis
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1022 | FCC$B?(G^>e$G$N?"J*L}$NC&;@AGH?1~(B ($B?.=#Bg1!AmM}9)(B) ($B3X(B)$B!{IY2,(B $BBsLi(B$B!&(B $BJ?_7(B $BD>$B!&(B ($B%f!<%0%l%J(B) $B>>K\(B $BBsLi(B$B!&(B $BB@ED(B $B@25W(B$B!&(B $BNkLZ(B $B7r8c(B$B!&(B ($B@iBeED2=9)(B) ($B@5(B)$B9bDM(B $BF)(B$B!&(B ($B?.=#BgA!0](B) ($B@5(B)$BEhED(B $B8^I4N$(B | catalytic cracking deoxygenation vegetable oil
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