$B9V1i(B $B;~9o(B | $B9V1i(B $BHV9f(B | $B9V1iBjL\!?H/I=| $B%-!<%o!<%I(B | $BJ,N`(B $BHV9f(B | $B$BHV9f(B | |
| I$B2q>l(B $BBh(B1$BF|(B |
| (10:20$B!A(B12:00)$B!!(B($B:BD9(B $BC]Cf(B $BAT(B) |
| 10:20$B!A(B 10:40 | I105 | Ni-$B?e;@%"%Q%?%$%H?(G^$N?WB.=O@.$H%a%?%sItJ,;@2=FC@-$H$N4X78(B
($B $B!&(B ($B@5(B)$BCfN$(B $BJY(B $B!&(B ($B3X(B)$B@1Ln(B $BE/Li(B $B!&(B ($B@5(B)$B9CHe(B $B7IH~(B | calcium hydroxyapatite nickel methane partial oxidation
| 5-a | 620 |
| 10:40$B!A(B 11:00 | I106 | $B%Q%k%9H?1~$rMQ$$$?(BNi$B7O?(G^$K$*$1$k%a%?%sItJ,;@2=H?1~7PO)$N8!F$(B
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| 5-a | 136 |
| 11:00$B!A(B 11:20 | I107 | $BC4;}5.6bB0?(G^$K$h$k(BCO$BA*Br%a%?%s2=H?1~(B
($BElBg1!9)(B) $B!{(B($B@5(B)$B5FCO(B $BN4;J(B $B!&(B $BB?ED(B $B>;J?(B $B!&(B ($B@5(B)$B@V>>(B $B7{ $B!&(B ($B@5(B)$B?{86(B $B9'(B $B!&(B ($B9)3X1!Bg(B) ($B@5(B)$BCfHx(B $B??0l(B $B!&(B ($B@.l~Bg(B) ($B@5(B)$B1::j(B $B9@J?(B $B!&(B ($B@5(B)$BN$@n(B $B=EIW(B | Ruthenium catalyst Methanation TiO2
| 5-a | 610 |
| 11:20$B!A(B 11:40 | I108 | $BEtL}?e>x5$2~
($BElBg1!9)(B) $B!{(B($B3X(B)$B?yBt(B $B2mB'(B $B!&(B ($B@5(B)$B9bFi(B $BOB90(B $B!&(B ($B9q:]@PL}3+H/Dk@P(B) ($B@5(B)$B86ED(B $BN<(B $B!&(B ($BElBg1!9)(B) $B5WJ]ED(B $B=c(B $B!&(B ($B@5(B)$BF2LH(B $B0l@.(B | kerosen steam reforming Ni-La catalyst carbon deposition
| 5-a | 278 |
| 11:40$B!A(B 12:00 | I109 | $B@QJ,J}Dx<0$rMQ$$$??eAG2=C&CbAG?(G^$N3h@-E@J,I[2r@O(B
($BElG@9)Bg(B) $B5\ED(B $BM[(B $B!&(B ($B6&(B)$BIZ1J(B $B90G7(B $B!&(B $B!{(B($B@5(B)$B1J0f(B $B@5IR(B | non-parametric analysis active site distribution hydrodenitrogenation
| 5-a | 245 |
|
| (13:00$B!A(B14:20)$B!!(B($B:BD9(B $B;3ED(B $BGn;K(B) |
| 13:00$B!A(B 13:20 | I113 | $B;@AG2C052<(BPd/C$B?(G^$K$h$kF};@%J%H%j%&%`$N;@2=C&?eAGH?1~$X$NBhFs@.J,$NE:2C8z2L(B
($BFAEgBg1!@hC<650iIt(B) $B!{(B($B3X(B)$BEDCf(B $B=U $B!&(B $B5FK\(B $BE/M:(B $B!&(B ($BFAEgBg1!(BSTS$B8&(B) ($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) $BA086(B $B7K;R(B $B!&(B $BI1Ln(B $B2EG7(B $B!&(B $BFs5\(B $B9R(B | sodium lactate oxidative dehydrogenation Pd/C
| 5-a | 19 |
| 13:20$B!A(B 13:40 | I114 | $B%K%C%1%k=$>~3F
($BFAEgBg1!@hC<650iIt(B) $B!{(B($B3X(B)$B>.@n(B $B;KO:(B $B!&(B ($B3X(B)$BOBED(B $BN49((B $B!&(B ($BFAEgBg9)(B) $BCfB<(B $BfFB@(B $B!&(B ($BFAEgBg1!(BSTS$B8&(B) ($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 $BLP(B | mesoporous silica ethanol conversion Ni-doped catalysts
| 5-a | 20 |
| 13:40$B!A(B 14:00 | I115 | $BN.DLH?1~>l$K$*$1$k%T%k%S%s;@9g@.H?1~>r7o$N:GE,2=(B
($B;0I)%l%$%h%s(B) $B!{(B($B@5(B)$B0B@n(B $BH;Li(B $B!&(B $BBgC+Fb(B $B7r(B $B!&(B ($B5~Bg9)(B) ($B@5(B)$BA0(B $B0lW"(B | Slug flow Lactate ester O2-oxidation
| 5-a | 145 |
| 14:00$B!A(B 14:20 | I116 | $B%>%k%2%k!&%G%#%C%W%3!<%F%#%s%0K!$K$h$j:n@=$7$?(BTiO2/Cr$B8w?(G^$N2D;k8w1~Ez@-$H(BCO2$B2~2A(B
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| 5-a | 102 |
| (14:20$B!A(B15:40)$B!!(B($B:BD9(B $B@>B<(B $B82(B) |
| 14:20$B!A(B 14:40 | I117 | $B;@2=E47O?(G^$K$h$k?e>x5$(B/$BD6NW3&?eJ70O5$2<$G$ND6=E
($BKLBg1!9)(B) $B!{(B($B3X(B)$B:4F#(B $BM42p(B $B!&(B ($B3X(B)$BKL8}(B $BC#Li(B $B!&(B ($B3X(B)$B $B!&(B ($B3X(B)$B=.0f(B $B7<(B $B!&(B ($B@5(B)$BB?8P(B $B516=(B $B!&(B ($B@5(B)$BA}ED(B $BN4IW(B | heavy oil iron oxide catalytic cracking
| 5-a | 93 |
| 14:40$B!A(B 15:00 | I118 | $B%7%j%+$GHoJ$$5$l$?%+!<%\%s%J%N%A%e!<%VC4;}(BPd$B?(G^$N(BPEFC$B%+%=!<%I?(G^$X$N1~MQ(B
($B6eBg1!9)(B) $B!{(B($B@5(B)$BC]Cf(B $BAT(B $B!&(B ($B@5(B)$BGv(B $BD>?M(B $B!&(B ($B@5(B)$B>>:,(B $B1Q $B!&(B ($B@5(B)$B4_ED(B $B>;9@(B | Carbon-supported Pd silica-coating fuel cell
| 5-a | 125 |
| 15:00$B!A(B 15:20 | I119 | $B%A%?%K%"%J%NN3;R$K$h$k%+!<%\%s%J%N%A%e!<%V$NHoJ$(B
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| 5-a | 244 |
| 15:20$B!A(B 15:40 | I120 | $B<+F0
($BL>Bg9)(B) $B!{(B($BIt(B)$B66K\(B $BNI?r(B $B!&(B ($B@5(B)$B;3ED(B $BGn;K(B $B!&(B ($B@5(B)$BED@n(B $BCRI'(B $B!&(B ($BK-EDCf8&(B) ($B@5(B)$B2CF#(B $B8g(B | diffusion adsorption automotive catalyst
| 5-a | 355 |
| (15:40$B!A(B16:40)$B!!(B($B:BD9(B $B0KF#(B $BD> |
| 15:40$B!A(B 16:00 | I121 | $BD>@\C&?e=L=E9g$K$h$k%]%jF};@$N9g@.(B
($BElG@9)Bg9)(B) $B!{(B($B@5(B)$BK\B?(B $BB@ $B!&(B Le Dinh Tuy Diem $B!&(B ($B@5(B)$B9q4c(B $B9'M:(B | lactic acid polylactic acid polymerization
| 5-d | 616 |
| 16:00$B!A(B 16:20 | I122 | $BH?1~J,N%$rMQ$$$?%Y%s%<%s$NItJ,;@2=$K$h$k%U%'%N!<%k9g@.%7%9%F%`$K$*$1$kA`:n0x;R$N1F6A(B
($BL>Bg1!9)(B) $B!{(B($B3X(B)$BC]Fb(B $BC#Lp(B $B!&(B ($B@5(B)$B;3ED(B $BGn;K(B $B!&(B ($B@5(B)$BED@n(B $BCRI'(B | benzen reaction-extraction system partial oxidation
| 5-d | 149 |
| 16:20$B!A(B 16:40 | I123 | $B%Q%i%8%&%`Fs857O9g6bKl$N?eAGF)2a@-G=(B
($BEl5~%,%9(B) $B!{(B($B@5(B)$BGr:j(B $B5AB'(B $B!&(B $B0BED(B $BM&(B | Palladium Membrane Hydrogen
| 5-d | 516 |
| (16:40$B!A(B17:40)$B!!(B($B:BD9(B $BK\B?(B $BB@ |
| 16:40$B!A(B 17:00 | I124 | $B%7%/%m%X%-%5%sC&?eAG$N$?$a$NB?4I<0%a%s%V%l%s%j%"%/%?!<$N(BCFD$B2r@O(B
($B1'ET5\Bg9)(B) $B!{(B($B@5(B)$B0KF#(B $BD> $B!&(B $B5HED(B $BD> $B!&(B ($B@5(B)$BL#B<(B $B7r0l(B $B!&(B ($B@5(B)$B:4F#(B $B9d;K(B | Membrane reactor Dehydrogenation CFD
| 5-d | 601 |
| 17:00$B!A(B 17:20 | I125 | $B?eAG@=B$MQ?(G^0lBN2=%b%8%e!<%k$N2~
($BEl5~%,%9(B) $B!{@>0f(B $B>"(B $B!&(B $B0f4X(B $B9'Lo(B $B!&(B $BGr:j(B $B5AB'(B $B!&(B $B0BED(B $BM&(B $B!&(B ($BF|K\FC $B!&(B $B9bLZ(B $BJ]9((B $B!&(B $B;V3@(B $B=(OB(B $B!&(B $BI':d(B $B1Q><(B $B!&(B $BEDCf(B $BM5G7(B | hydrogen membrane catalyst
| 5-d | 480 |
| 17:20$B!A(B 17:40 | I126 | $B?eAG@=B$MQ?(G^0lBN2=%b%8%e!<%k$N2~
($BEl5~%,%9(B) $B!{Cf@n(B $BM'5.(B $B!&(B $BIZ1J(B $BN40l(B $B!&(B $B@>0f(B $B>"(B $B!&(B $B0f4X(B $B9'Li(B $B!&(B $BGr:j(B $B5AB'(B $B!&(B $B0BED(B $BM&(B | hydrogen catalyst numerical analysis
| 5-d | 468 |