$B$BHV9f(B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $BH/I=7A<0(B | |
47 | $BC]$rAG:`$H$7$?C\;:GQ?eCf$N%j%s2s<}(B ($BM-L@9b@l(B) ($B@5(B)$BN-(B $BC0(B | Phosphorus recovery Bamboo Wastewater of livestock
| O |
82 | FCA(Fluid Catalytic Aromaforming:$BN.F0@\?(K'9aB2@=B$(B)$B%W%m%;%9$N3+H/(B (JX$B%(%M%k%.!<(B) ($B@5(B)$B!{bC5](B $BOBLi(B$B!&(B ($BK!(B)$B0KED(B $BNNFs(B$B!&(B ($BK!(B)$B4d:4(B $BBYG7(B$B!&(B ($B@iBeED2=9)7z@_(B) ($B@5(B)$B|bLn(B $B=!0lO:(B | Fluid bed Aromaforming Process development
| O |
120 | [$BE8K>9V1i(B] $B@\?(;@2=H?1~$r4pHW$H$7$?M-MQ2=3XIJ$N9g@.(B ($BFAEgBg1!M}9)(B) ($B@5(B)$B?y;3(B $BLP(B | Mesoporous silicas Oxidative dehydrogenation Glycerol
| O |
121 | [$BE8K>9V1i(B] $B%^%$%/%mGH2=3XH?1~AuCV$N3+H/(B ($B;M9q7WB,9)6H(B) $B!{A>2f(B $BGnJ8(B$B!&(B $BT"0f(B $B>!G7(B$B!&(B $B1vED(B $B1QOB(B | Microwave reactor Microwave heating Scale up
| O |
245 | $BC:AG7O8GBN;@?(G^$N1UAjH?1~$X$NMxMQ(B:$BI=LL$N?FAB?e@-$H:Y9&9=B$$,?(G^3h@-$XM?$($k1F6A(B ($BKLBg1!9)(B) ($B3X(B)$B!{NkLZ(B $BM$7<(B$B!&(B ($B@5(B)$B2.Ln(B $B7.(B$B!&(B ($B@5(B)$B8~0f(B $B?B(B | esterification catalyst sulfonated carbon
| O |
265 | $BD62;GH2=3XH?1~$K5Z$\$91zLLHD$HH?1~4oB&LL$NH? ($BL>9)Bg(B) ($B3X(B)$B!{$B!&(B ($B@5(B)$BB?ED(B $BK-(B$B!&(B ($B@5(B)$B2CF#(B $BDw?M(B | ultrasonic chemical reaction concave reflecting plate reflection of the reactor side wall
| O |
286 | DFT$B7W;;$rMQ$$$?%P%J%8%&%`:xBN?(G^$K$h$k;@AG3h@-2=2aDx$N2r@O(B ($B?@8MBg1!9)(B) ($B3X(B)$B!{23K\(B $BFF;K(B$B!&(B ($B3X(B)$B1'ET5\(B $BM-:i(B$B!&(B $B0f>e(B $B2l5.(B$B!&(B ($B@5(B)$BC+20(B $B7$B!&(B ($B@5(B)$B;T66(B $BM40l(B$B!&(B ($B@5(B)$B@>;3(B $B3P(B | Selective Oxidation Benzene to Phenol Density Function Theory
| O |
315 | $B3lC:M3Mh@.7?%3!<%/%9$N6/EY$K$*$h$\$986NA$N@->u(B ($B6eBg@hF38&(B) ($B@5(B)$B!{9)F#(B $B??Fs(B$B!&(B ($B6eBgAmM}9)(B) $BNS(B $B85B@O:(B$B!&(B ($B6eBg@hF38&(B) $B?9(B $BL@F|9a(B$B!&(B ($B?@8M@=9]=j(B) ($B@5(B)$B5HED(B $BBsLi(B$B!&(B $B1|;3(B $B7{9,(B$B!&(B ($B6eBg@hF38&(B) ($B@5(B)$BB'1J(B $B9TMG(B$B!&(B ($B@5(B)$BNS(B $B=a0lO:(B | Coal Coke Lignite
| O |
317 | $B;vA0HyJ4:U=hM}$K$h$k3lC:M3Mh@.7?%3!<%/%9$N6/EY8~>e(B ($B6eBg@hF38&(B) ($B@5(B)$B!{9)F#(B $B??Fs(B$B!&(B ($B6eBgAmM}9)(B) $BNS(B $B85B@O:(B$B!&(B ($B6eBg@hF38&(B) $B?9(B $BL@F|9a(B$B!&(B ($B?@8M@=9]=j(B) ($B@5(B)$B5HED(B $BBsLi(B$B!&(B $B1|;3(B $B7{9,(B$B!&(B ($B6eBg@hF38&(B) ($B@5(B)$BB'1J(B $B9TMG(B$B!&(B ($B@5(B)$BNS(B $B=a0lO:(B | Coal Coke Lignite
| O |
331 | $BFs ($B7'Bg(B/$B5~Bg?(G^EECS(B) ($B@5(B)$B!{K'ED(B $B2E;V(B$B!&(B ($B7'Bg(B) $B;03Q(B $B?N;V(B$B!&(B $B>>K\(B $B98E5(B$B!&(B $B:4F#(B $BE0:H(B$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 | Rhodium nanolayer arc-plasma
| O |
345 | $B;@=hM}$K$h$kGQB@M[EECS%b%8%e!<%kM3Mh$NJ4Kv$+$i$N%7%j%3%s=c2=(B ($B2,;3Bg1!4D@8(B) ($B3X(B)$B!{>>86(B $B51L@(B$B!&(B ($B@5(B)Uddin Md. Azhar$B!&(B ($B@5(B)$B2CF#(B $B2E1Q(B$B!&(B ($BElK.2=@.(B) $BNS(B $BE5L@(B$B!&(B $B@n@>(B $B9'B'(B | Solar cell Silicon Purification
| O |
372 | Fischer-Tropsch$B9g@.MQ(BCo$BC4;}&B7?%<%*%i%$%H?(G^$ND4@=K!$N8!F$(B ($B2,;3Bg1!4D@8(B) ($B3X(B)$B!{Cf@>(B $B??F`H~(B$B!&(B ($B@5(B)$B2CF#(B $B2E1Q(B$B!&(B ($B2,;3Bg(BRCIS/JST$B$5$-$,$1(B) $B?N2J(B $BM&B@(B$B!&(B ($B2,;3Bg1!4D@8(B) ($B@5(B)Uddin Md. Azhar | Fischer-Tropsch process cobalt supported beta-zeolite catalyst preparation
| O |
397 | Cu-ZnO/Al2O3$B?(G^$rMQ$$$?(BH2$B6&B82<$G$N(BCO$B%7%U%HH?1~$NB.EYO@E*2r@O(B ($B?@8MBg1!9)(B) ($B3X(B)$B!{KY9>(B $BBY90(B$B!&(B $BF#ED(B $BN<(B$B!&(B ($B3X(B)$B23K\(B $BFF;K(B$B!&(B ($B@5(B)$BC+20(B $B7$B!&(B ($B@5(B)$B;T66(B $BM40l(B$B!&(B ($B@5(B)$B@>;3(B $B3P(B | H2 production CO shift reaction Cu-ZnO/Al2O3
| O |
402 | $B;@AG%-%c%j%"$N4T85B.EY$K$*$h$\$91F6A0x;R$N8!F$(B ($B0l:b(B)$B@PC:%(%M%k%.!<%;%s%?!<(B) ($BK!(B)$BsnF#(B $BCND>(B | Coal Chemical Looping Oxygen carrier
| O |
407 | $B%"%s%b%K%"J,2r?(G^$NB.EYO@2r@O$K4p$E$$$?H?1~4o@_7W(B ($B;:Am8&(B) ($B@5(B)$B!{9b66(B $B8|(B$B!&(B ($B@5(B)$BF#C+(B $BCiGn(B | NH3 decomposition Reactor design Kinetic model
| O |
410 | [$BE8K>9V1i(B] $B@PC:MxMQ$HH?1~9)3X(B ($B5~Bg%(%MM}(B) ($B@5(B)$B;01:(B $B9'0l(B | Chemical reaction engineering Coal
| O |
461 | $BA+0\6bB0;@2=J*?(G^$N%W%m%Q%sC&?eAGFC@-$K5Z$\$9N2;@=hM}$N8z2L(B ($B@EBg1!(B) ($B@5(B)$B!{EOIt(B $B0=(B$B!&(B $BJ?ED(B $BK>(B$B!&(B $B2OLn(B $BK'3$(B$B!&(B ($B@5(B)$BJ!86(B $BD9 | Transition metal oxide Sulfation Propane dehydrogenation
| O |
556 | CO2$B?eAG2=H?1~$K5Z$\$9(BCu/ZrO2$B?(G^$X$N6bB0E:2C8z2L(B ($B@.l~Bg(B/$B3X?6(B) ($B@5(B)$B!{B?ED(B $B>;J?(B$B!&(B ($B@.l~Bg(B) $BAzED(B $BD>9((B$B!&(B $BN$@n(B $B=EIW(B | copper CO2 hydrogenation methanol
| O |
629 | $B%Q%i%8%&%`J#9gKl$rMQ$$$?KlH?1~4o$K$h$k%"%s%b%K%"Dc29J,2r$NB%?J(B ($B1'ET5\Bg(B) ($B@5(B)$B!{0KF#(B $BD>$B!&(B $BBgEg(B $B=_;V(B$B!&(B ($B@5(B)$B8E_7(B $B5#(B$B!&(B ($B@5(B)$B:4F#(B $B9d;K(B | Palladium Membrane reactor Ammonia
| O |
685 | $B%(%^%k%7%g%sK!$K$h$k(BRh$BD6HyN3;R$rFbJq$7$?(BMFI$B7?%<%*%i%$%H$N9g@.(B ($BEl9)Bg(B) ($B3X(B)$B!{8E20(B $B5.>O(B$B!&(B ($BKLBg(B) $B9bED(B $B=E;V(B$B!&(B ($BEl9)Bg(B) ($B@5(B)$BF#J/(B $BBgM5(B$B!&(B ($BKLBg(B) ($B@5(B)$B5H@n(B $BBvLi(B$B!&(B ($B@5(B)$BCf:d(B $BM$B@(B$B!&(B ($B@5(B)$BA}ED(B $BN4IW(B$B!&(B ($BEl9)Bg(B) ($B@5(B)$BB?8P(B $B516=(B | Rh nanoparticle MFI zeolite emulsion method
| O |
693 | $B7k>=%5%$%:$N0[$J$k(BMTW$B7?%<%*%i%$%H$rMQ$$$?(B2-$B%a%A%k%J%U%?%l%s$N%a%A%k2=H?1~$NB.EY2r@O(B ($BKLBg1!9)(B) ($B3X(B)$B!{EOIt(B $B3Y(B$B!&(B ($B@5(B)$BCf:d(B $BM$B@(B$B!&(B ($B3X(B)$BC+8}(B $BB@0l(B$B!&(B ($B@5(B)$B5H@n(B $BBvLi(B$B!&(B ($BEl9)Bg1!M}9)(B) ($B@5(B)$BB?8P(B $B516=(B$B!&(B ($BKLBg1!9)(B) ($B@5(B)$BA}ED(B $BN4IW(B | MTW-type zeolite Methylation Kinetics
| O |
715 | $B%^%$%/%mGH>H ($B;:Am8&(B) ($B@5(B)$B!{:4F#(B $B9d0l(B$B!&(B $B@>2,(B $B>-51(B$B!&(B $B5\Bt(B $BE/(B$B!&(B ($BLp:jAm6H(B) ($B@5(B)$BLSMx(B $B0B4u(B$B!&(B $B8M1)(B $BC$IW(B$B!&(B $BK-ED(B $BOB90(B$B!&(B $B?">>(B $B>40l(B | hydrogen microwave ammonia
| O |
717 | Ni$B?(G^I=LL$K$*$1$kC:AGAX@.D9%a%+%K%:%`$NNL;R2=3X7W;;2r@O(B ($B4X3XBg1!M}9)(B) ($B3X(B)$B!{DEEg(B $BBgJe(B$B!&(B ($B@5(B)$B>.AR(B $BE4J?(B | growth mechanism of graphene sheet steam methane reforming DFT calculation
| O |
726 | K/FeOx$B$K$h$k%0%j%;%j%s$+$i$N%"%j%k%"%k%3!<%k$NA*Br9g@.(B ($BEl9)Bg(B) ($B3X(B)$B!{NS(B $BAT5*(B$B!&(B ($BKLBg(B) $B;{0f(B $BOB9((B$B!&(B ($B@5(B)$B5H@n(B $BBvLi(B$B!&(B ($BEl9)Bg(B) ($B@5(B)$BF#J/(B $BBgM5(B$B!&(B ($BKLBg(B) ($B@5(B)$BCf:d(B $BM$B@(B$B!&(B ($B@5(B)$BA}ED(B $BN4IW(B$B!&(B ($BEl9)Bg(B) ($B@5(B)$BB?8P(B $B516=(B | Glycerol Allyl Alcohol iron oxide catalyst
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757 | $B%J%N%+!<%\%s$rMQ$$$?Fs ($BL>8E20;T9)8&(B) ($B@5(B)$B!{5\ED(B $B9/;K(B$B!&(B ($B9-Eg(B) $BT";^(B $BMN>0(B$B!&(B (TTI) $BBgJ!(B $B@?(B$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 | nanocarbon fuel cell catalyst negative electrode
| O |
778 | $BN.F0?(G^AXH?1~4o$G5/$-$k4qL/$J8=>]$HB?@.J,7O5$BN$NHsEy%b%k3H;6%b%G%k(B ($B | diffusion non-equimolar Graham's law
| O |
795 | $B%$%*%s8r49 ($BElKLBg1!9)(B) ($B3X(B)$B!{Nk9>(B $B??;N(B$B!&(B ($B@5(B)$BJ!Eg(B $B9/M5(B$B!&(B ($B@5(B)$BKL@n(B $B>0H~(B | fatty acid ethyl ester hydrous ethanol ion-exchange resin catalyst
| O |
836 | $B6!M?BN$H$7$F&A(B-HMBSA$B$rMQ$$$?%5%k%b%M%i6]M3Mh%"%j%k%9%k%[%H%i%s%9%U%'%i!<%<$K$h$k%9%k%[4pE>0\(B ($B:e;TBg1!9)(B) ($B3X(B)$B!{Cf;3(B $BfFJ?(B$B!&(B ($B@5(B)$B8^==Mr(B $B9,0l(B$B!&(B ($B@5(B)$BBgEh(B $B42(B | Enzyme Sulfation Green Process
| O |
852 | $B%"%k%+%jEZN`6bB0C:;@1vC4;}(BRu$B?(G^>e$G$N%H%k%(%s$N?e>x5$2~ ($B9)3X1!Bg(B) ($B@5(B)$B!{HSED(B $BH%(B$B!&(B $BM{(B $B0]??(B$B!&(B ($B@5(B)$B8^==Mr(B $BE/(B$B!&(B $B1|B<(B $BOB(B | Hydrogen production Steam reforming Alkaline earth metal carbonate
| O |
866 | $B9b<~GHD62;GH>Hl$rMxMQ$7$?%0%j%7%s$N7k>=2=5sF0(B ($B$B!&(B ($B3X(B)$B:nK\(B $BM40lO:(B$B!&(B ($B@5(B)$B?eED(B $B7I(B$B!&(B ($B@5(B)$B8^Eg(B $B?r(B | ultrasound antisolvent crystallization glycine
| O |
876 | $B%P%$%*%*%$%k%b%G%kJ*e$G$N?eAG2=C&;@AG(B ($B%Z%H%m%J%99)Bg(B) Tran Nga$B!&(B ($B3$(B)$B!{>eB<(B $BK';0(B$B!&(B Ramli Anita | Hydrodeoxygenation Guaiacol Catalyst
| O |
878 | $B?eAG0\9TH?1~$rMxMQ$7$?B?4DK'9aB2$N@\?(J,2r(B ($B?.=#BgA!0](B) ($B@5(B)$B!{EhED(B $B8^I4N$(B$B!&(B ($B?.=#Bg1!AmM}9)(B) $B1-Ln(B $B@i0!$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 ($B@iBeED2=9)(B) ($B@5(B)$B9bDM(B $BF)(B | catalytic cracking polycyclic aromatic hydrocarbons hydrogen transfer
| O |
920 | $BDc299g@.%A%?%s;@%J%N%A%e!<%V$r?(G^$H$7$FMQ$$$?%0%k%3!<%9$+$i$N(BHMF$BE>49H?1~(B ($B:eBg1!4p9)(B) ($B3X(B)$B!{B@ED(B $BL((B$B!&(B ($B@5(B)$BW"ED(B $BM:0lO/(B$B!&(B ($B:eBg1!4p9)(B/JST$B$5$-$,$1(B) ($B@5(B)$BFbED(B $B9,L@(B$B!&(B ($B:eBg1!4p9)(B) ($B@5(B)$B@>;3(B $B7{OB(B | hydrogen titanate nanotube solid acid catalyst 5-(Hydroxymethyl)furfural
| O |
937 | $BC4;}Gr6b?(G^$rMQ$$$?0!%R;@$N?eCf;@2=H?1~(B ($B6eBg1!9)(B) $Bld(B $B6b@g(B$B!&(B ($B@5(B)$B>>:,(B $B1Q$B!&(B ($BF1;V$B!&(B ($B6eBg1!9)(B) ($B@5(B)$B!{4_ED(B $B>;9@(B | Arsenious acid Oxidation in aqueous solution Platinum catalyst
| O |
958 | $B%$%*%s8r49 ($BElKLBg1!9)(B) ($B3X(B)$B!{:{;3(B $BCNNf(B$B!&(B ($B3X(B)$B>e?@ED(B $BM*EM(B$B!&(B ($B@5(B)$BKL@n(B $B>0H~(B | sugar fatty acid ester ion-exchange resin catalyst expanded-bed reactor
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959 | $B??6u;g30@~$K$h$k%"%s%b%K%"J,2r$H?eAG@8@.FC@-(B ($B4tIlBg(B) ($B3X(B)$B!{;T@n(B $B5.2m(B$B!&(B ($B3X(B)$BIp;3(B $B>49((B$B!&(B ($B3X(B)$BAa@n(B $B9,CK(B$B!&(B ($B@5(B)$B?@86(B $B?.;V(B$B!&(B ($B%"%/%H%j!<(B) ($B6&(B)$BA}0f(B $B2j(B | Vacuum ultra violet Ammonia Hydrogen
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