“…Previous studies of the DRM activity of SmCoO 3 prepared by sol-gel techniques [28][29][30] showed that the increase in the syngas yield occurs upon heating to 800 °C, and pre-reduction by H 2 Scheme 1 Designation of the samples studied in this work. ‡ In the case of SmCo, theoretical pattern from previously reported structure (CCDC 2099934) can be additionally applied to prove single-phase state of the isolated sample.…”
Section: The Evaluation Of the Catalytic Activity Of Smcoo 3 And Sas_...mentioning
confidence: 99%
“…derived from corresponding LnMO 3 perovskites attract considerable attention. 9,[12][13][14][23][24][25][26][27][28][29][30] The main advantages of such catalysts are relatively low cost combined with the capability to achieve considerable activity. Concerning the design of stable catalysts, Co/Ln 2 O 3 composites and corresponding LnCoO 3 generally look prospective due to high coking resistance.…”
Section: Introductionmentioning
confidence: 99%
“…9,[12][13][14][15][16][17][18][19][20][21][22]25 This problem can be solved by modifying the route of LnCoO 3 production to directly vary micromorphological features, which are crucial concerning the catalytic activity. 27 Similarly to other complex oxides, LnCoO 3 are most commonly prepared via swift and simple sol-gel techniques 14,16,23,25,[28][29][30][31][32][33][34][35][36] based on the thermolysis of the in situ prepared gelous Ln-Co complexes with anions of citric acid and glycine; other polyfunctional carboxylic acids are rarely involved. However, the insolubility of such complexes hinders the direct modification of their composition and morphology.…”
Dry reforming of methane to Syngas (DRM) is of increasing significance concerning, first, the production of raw for commercial organic/petrochemical syntheses and for hydrogen energetic, and, second, the utilization of...
“…Previous studies of the DRM activity of SmCoO 3 prepared by sol-gel techniques [28][29][30] showed that the increase in the syngas yield occurs upon heating to 800 °C, and pre-reduction by H 2 Scheme 1 Designation of the samples studied in this work. ‡ In the case of SmCo, theoretical pattern from previously reported structure (CCDC 2099934) can be additionally applied to prove single-phase state of the isolated sample.…”
Section: The Evaluation Of the Catalytic Activity Of Smcoo 3 And Sas_...mentioning
confidence: 99%
“…derived from corresponding LnMO 3 perovskites attract considerable attention. 9,[12][13][14][23][24][25][26][27][28][29][30] The main advantages of such catalysts are relatively low cost combined with the capability to achieve considerable activity. Concerning the design of stable catalysts, Co/Ln 2 O 3 composites and corresponding LnCoO 3 generally look prospective due to high coking resistance.…”
Section: Introductionmentioning
confidence: 99%
“…9,[12][13][14][15][16][17][18][19][20][21][22]25 This problem can be solved by modifying the route of LnCoO 3 production to directly vary micromorphological features, which are crucial concerning the catalytic activity. 27 Similarly to other complex oxides, LnCoO 3 are most commonly prepared via swift and simple sol-gel techniques 14,16,23,25,[28][29][30][31][32][33][34][35][36] based on the thermolysis of the in situ prepared gelous Ln-Co complexes with anions of citric acid and glycine; other polyfunctional carboxylic acids are rarely involved. However, the insolubility of such complexes hinders the direct modification of their composition and morphology.…”
Dry reforming of methane to Syngas (DRM) is of increasing significance concerning, first, the production of raw for commercial organic/petrochemical syntheses and for hydrogen energetic, and, second, the utilization of...
“…31 In order to search for alternative DRM materials, Smcontaining catalysts have evolved as potentially promising. This is essentially referred to the fact that Sm 2 O 3 , like La 2 O 3 , is reported to be capable of forming a samarium oxycarbonate species [34][35][36] and that the Ni/Sm 2 O 3 interface showed superior ability in the DRM process. 37 A particular important sub-class of Sm-based perovskite catalysts are the associated cobalt-containing materials.…”
To elucidate the role of earth alkaline doping in perovskite-based dry reforming of methane (DRM) catalysts, we embarked on a comparative and exemplary study of a Ni-based Sm perovskite with...
“…A-site replacement with alkaline earth metal is expected to enhance the carbon susceptible and thermal stability, and the B-site alteration is expected to increase the activity of the catalyst [18,19]. In last decade, many researchers have been widely reported LaNiO 3 [20][21][22], LaFeO 3 [23], SmCoO 3 [24] and also partial substitution of B-site perovskite catalysts show the higher activity, stability, and resistance to coke formation even at elevated temperature. The perovskite catalysts increase the syngas production in dry reforming reaction [25][26][27].…”
The SrNiO3 perovskite catalyst was synthesized by the citrate sol-gel method and supported on γ-Al2O3 and Nickel foam, which was used to produce syngas (CO and H2) via dry reforming of propane (DRP). Several techniques characterized the physicochemical properties of the fresh and spent perovskite catalyst. The X-ray diffractograms (XRD) characterization confirmed the formation of the perovskite compound. Before the catalytic activity test, SrNiO3 perovskite catalyst was reduced in the H2 atmosphere. Results indicated that the H2 reduction slightly increased the activity of the SrNiO3 perovskite catalyst. The catalytic activity was examined for the CO2/C3H8 ratio of 3 and reaction temperatures in the range of 550 °C–700 °C. The results from the catalytic study achieved 88% conversion of C3H8 and 66% conversion of CO2 with SrNiO3/NiF at 700 °C. Also, syngas with a maximum concentration of 21 vol.% of CO and 29 vol.% of H2 was produced from the DRP. The strong basicity of SrNiO3 perovskite enhanced the CO selectivity, resulting in minimal carbon formation. Post reaction catalyst characterization showed the presence of carbon deposition which could have originated from propane decomposition.
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