“…The peak at 2920 cm −1 (denoted as I 2920 ) can be mainly assigned to asymmetric CH 3 stretching groups from the deposited long-chain hydrocarbons, and the peak at 2850 cm −1 (assigned to I 2850 ) can be originated from symmetric stretching of CH 2 groups of polymethylene chains attributed to the relatively short-chain hydrocarbons [54,59,60], which are hardly removable due to strong adsorption characters on the cobalt surfaces during the FTS reaction. The observed larger peak intensity of the CH 3 band (larger peak intensity at around 2920 cm −1 ) on the meso-Co 3 O 4 and Mn/meso-Co 3 O 4 after the FTS reaction suggests that stronger adsorption characters of amorphous heavier wax components by encapsulating the cobalt surfaces as reported from our previous works [24,34,61]. The peak intensity ratios of I 2920 /I 2850 , which represent the integrated area ratios of peak at 2920 cm −1 and 2850 cm −1 , were also shown in Fig.…”
Section: Stability Of the Ordered Mesoporous Co 3 O 4 Under Reductivementioning
“…The peak at 2920 cm −1 (denoted as I 2920 ) can be mainly assigned to asymmetric CH 3 stretching groups from the deposited long-chain hydrocarbons, and the peak at 2850 cm −1 (assigned to I 2850 ) can be originated from symmetric stretching of CH 2 groups of polymethylene chains attributed to the relatively short-chain hydrocarbons [54,59,60], which are hardly removable due to strong adsorption characters on the cobalt surfaces during the FTS reaction. The observed larger peak intensity of the CH 3 band (larger peak intensity at around 2920 cm −1 ) on the meso-Co 3 O 4 and Mn/meso-Co 3 O 4 after the FTS reaction suggests that stronger adsorption characters of amorphous heavier wax components by encapsulating the cobalt surfaces as reported from our previous works [24,34,61]. The peak intensity ratios of I 2920 /I 2850 , which represent the integrated area ratios of peak at 2920 cm −1 and 2850 cm −1 , were also shown in Fig.…”
Section: Stability Of the Ordered Mesoporous Co 3 O 4 Under Reductivementioning
“…[1][2][3][4][5] In general,c obalt-based FTS catalysts have been known to have the advantageous characteristics of producing heavy hydrocarbons with ah ighera ctivity and al ower water gas shift activity [6] compared to ironbased FTS catalysts. [1][2][3][4][5] In general,c obalt-based FTS catalysts have been known to have the advantageous characteristics of producing heavy hydrocarbons with ah ighera ctivity and al ower water gas shift activity [6] compared to ironbased FTS catalysts.…”
Section: Introductionmentioning
confidence: 99%
“…To design efficient FTS catalysts, the optimum particles izes of active cobalt speciesw ith af acile reducibility and al ower deactivation rate should be properly adjusted by employing suitable modifiers of supports such as the commercially available Al 2 O 3 ,T iO 2 ,a nd SiO 2 . [5] The present study,b ased on our previousw orks, [5,11] focuses on identifying the methodologies for increasing the thermal stabilityo fc obalt-based FTS catalysts especially to verify the effects of calcination temperatures on the catalytic activity and stability. Therefore, proper modification of the supports has been largely investigated by employing various metal additives on the catalysts urfaces to enhancea ctive metal dispersions as well as to prevent strong metal-support interactions by maintaining the catalyst stability even after regeneration treatment under oxidation conditions for burning out depositedh ydrocarbons.…”
Ap hosphorous-modified Al 2 O 3 support was prepared by the impregnation methoda nd applied for the preparation of cobalt-based Fischer-Tropsch synthesis (FTS) catalysts (Co/P-Al 2 O 3 ), which were calcined at different temperatures. The Co/ P-Al 2 O 3 showed as ignificant increaseo ft hermals tability with ah igher catalytic performance without severe deactivation even above ac alcination temperature of 600 8Cc ompared with the unmodified Co/Al 2 O 3 .T hese findings are explained by the suppressed cobalt aluminate formation and less pronounced aggregation of cobaltp articles. The suppressed aggregation of cobalt particles is attributed to the localized presence of aluminump hosphate by forming at hermally stable metal-phosphorous oxo-species on Al 2 O 3 surfaces thus suppressing the migration of cobalt particles to the outer pore mouths of the support. These effects significantly enhance the catalytic activity with ah igher thermal stabilityo ft he catalysts.
“…These structural stabilities were mainly attributed to the partial formation of thermally stable spinel-type metal aluminates at an optimal molar ratio of M/Co = 0.25 (M = Al or Zr). [13][14][15][16] In addition, the synergy effects of phosphorous species on Co/Al 2 O 3 catalysts were also reported by our previous extensive works, [19][20][21][22][23] and a superior catalytic activity on the phosphorusmodified Al 2 O 3 was observed with an improved activity and stability with less aggregation of the supported cobalt nanoparticles by partially forming hydrophobic aluminum phosphate (AlPO 4 ) species, [19][20][21] The partially formed AlPO 4 phases on the outermost γ-Al 2 O 3 surfaces inhibited the transformation of cobalt oxides to inactive cobalt aluminates due to its SiO 2 -like tridymite hydrophobic AlPO 4 surface natures by altering metal-support interactions through a stronger affinity between Al and P species than that of Al and Co species. [24] Those AlPO 4 phases can also effectively prevent the re-oxidation and aggregation of the supported cobalt nanoparticles by minimizing the phase transformations of γ-alumina to brittle boehmite (AlOOH) phase as well.…”
Section: Introductionmentioning
confidence: 70%
“…[20,21] The advantages of phosphorus incorporation on the Co/Al 2 O 3 were also reported to increase the thermal stability of active metallic cobalt nanoparticles by adjusting metalsupport interactions through a possible formation of the thermally stable spinel-type CoAl 2 O 4 phases and by enhancing the reducibility of cobalt oxide nanoparticles. [19][20][21][22][23][24] In the present study, the effects of phosphorus-modified highly ordered mesoporous Co 3 O 4 À Al 2 O 3 binary metal oxides (P/m-CoAl) during FTS reaction were investigated in terms of their structural durability [13][14][15][16][17][18]25] and outermost surface property changes to explain different catalytic activity and stability, which were not precisely reported till now as far as we know. The synergy effects of an optimal phosphorous content on the P/m-CoAl were explained by elucidating the possible phase transformations of cobalt and aluminum species as well as their positive contributions to the robust structural stability of the ordered mesoporous Co 3 O 4 À Al 2 O 3 metal oxide structures.…”
The synergy effects of phosphorus modifier on highly ordered mesoporous binary metal oxides of Co 3 O 4 À Al 2 O 3 (m-CoAl), prepared by nanocasting method using a hard template of KIT-6, were observed by an enhanced catalytic and structural stability of the m-CoAl during CO hydrogenation to hydrocarbons. The enhanced structural stability of the ordered mesoporous structures on the phosphorous-modified m-CoAl at an optimal amount of phosphorous modifier below 0.3 wt%P (P (3)/m-CoAl) was attributed to the partial formation of thermally stable metal phosphates under a reductive Fischer-Tropsch synthesis (FTS) reaction condition. The positive effects of the phosphorous modifier were originated from the partially formed SiO 2 -like AlPO 4 phases on the outer surfaces of the m-CoAl, as well as from partially formed irreducible and thermally stable spinel-type cobalt aluminates (CoAl 2 O 4 ). The hydrophobic SiO 2 -like tridymite AlPO 4 surfaces on the ordered matrices of the P/m-CoAl also effectively prevented the heavy wax (or coke precursors) depositions. The structural instability of the P/m-CoAl was observed at a higher phosphorous content above 0.5wt%P by preferentially forming the largely segregated mixed metal oxides such as Co 3 O 4 À CoAl 2 O 4 À Co 3 (PO 4 ) 2 through the phase transformations of the surface excess AlPO 4 .
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