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α al2o3

Manufactured by Thermo Fisher Scientific
Sourced in United States

α-Al2O3 is a type of aluminum oxide that exists in the alpha crystal structure. It is a hard, chemically inert material with a high melting point. α-Al2O3 is commonly used as a refractory material and in the production of abrasives and cutting tools.

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4 protocols using α al2o3

1

Synthesis of Ni-Based Catalysts on Various Supports

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Ni-Based catalysts supported on CeO2 (Sigma Aldrich Co.), α-Al2O3 (Alfa Aesar Co.), Y2O3 (Sigma Aldrich Co., St. Louis, MO, USA) and TiO2 (G-5, Cristal Global Co.) were prepared by a wet impregnation method. Nickel nitrate hexahydrate (Ni(NO3)2·6H2O; Sigma Aldrich Co.) was dissolved in distilled water at 80 °C. After impregnation, the moisture was removed at 80 °C using a rotary vacuum evaporator and then dried at 103 °C oven for 12 h. The samples were calcined at 400 °C for 2 h and then samples were reduced at 420 °C for 2 h with a 30% H2/N2. The obtained samples were grounded and sieved using a 40–50 mesh. Ni loading was fixed at 10 wt%.
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2

Catalyst Preparation and Reduction

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Diphenylacetylene (Sigma-Aldrich, St. Louis, MO, USA, >98%) and n-hexane (Merck KGaA, Darmstadt, Germany, 98%) were used without further purification. Gases and gaseous mixtures used for catalyst reduction and catalytic tests were supplied by Linde Gas Rus (Balashikha, Russia): 5%H2/Ar, H2 (99.9999% grade) and He (99.999% grade). For the catalyst preparation α-Al2O3 (Alfa Aesar, Haverhill, MA, USA, Ssp = 8 m2/g) was used as a carrier.
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3

Coimpregnated Fe-Mn-Cu/Ni/K Catalysts

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All catalysts comprising Fe as active metal, Mn as first promoter and either of Cu, Ni or K as second/third promoter were synthesized using coimpregnation method. Active metal and promoters were coimpregnated on α-Al2O3 (Alfa Aesar, 99.9%) support. Support, Fe(NO3)3.9H2O (Merck, ACS), Mn(NO3)2.4H2O (Merck, >98.5%) and either of Cu(NO3)2.3H2O (Merck, >99.5%), Ni(NO3)2.6H2O (Merck, ACS) or KNO3 (Merck, ISO) were first taken into an Erlenmeyer flask. Then, this powder mixture was slurried either in deionized water or n-pentane (Sigma-Aldrich, reagent grade, 98%). Aqueous mixture was mixed in an ultrasonic bath, whereas n-pentane comprising solution was stirred overnight. Prepared catalysts were dried at 110 °C and calcined at 430 °C under dry air atmosphere for 3 h. Catalyst were named according to the type and amount of metal used, and the type of solvent as follows: xFeyMnzAkB-s where x, y, z and k are the weight percentage of the metal used, A and B represent the second and third promoter (Cu, Ni or K), s indicates the type of solvent used (w-water, p-pentane). In this study, the weight percentage of Fe (x) and Mn (y) in the catalysts were determined to be 15 and 0.3, respectively; z and k were used as 0.5, 1, 1.5, 2, and 2.5. A representative notation for a catalyst comprising 0.3 wt.% Mn, 0.5 wt%Cu prepared by n-pentane is: 15Fe0.3Mn0.5Cu-p.
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4

Preparation and Characterization of Ru Catalysts

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In-house supported Ru catalysts were prepared on activated carbon (Jacobi Carbons), α-Al2O3 (Alfa Aesar), rutile-TiO2 (Norpro Saint-Gobain) and monoclinic-ZrO2 (Norpro Saint-Gobain). The catalysts were synthesised by wet impregnation (4 h, 40 °C, continuous agitation) of the sieved supports (0.5–0.8 mm) with an aqueous 1.5% (wt/vol) RuNO(NO3)3 solution (Alfa Aesar). The suspension was then evaporated at 60 °C by progressively decreasing the pressure on a rotary evaporator. The catalysts were left at RT and 150 mbar overnight to fully evaporate the solvent. The impregnated supports were then dried overnight in an oven at 110 °C in air. The metal oxide-supported catalysts were calcined in a quartz tube at 450 °C (10 °C min−1, 4 h) in N2/O2 (80 : 20, 250 mL min−1). Eventually, all catalysts were reduced at 400 °C (5 °C min−1, 6 h) in a flow of N2/H2 (80 : 20, 500 mL min−1). After reduction, they were passivated by letting air diffuse through the open reactor. The catalysts obtained were used without further treatment. Three commercial catalysts – 5 wt% Ru supported on activated carbon, Ru/AC-BM (BASF), Ru/AC-A, and Ru/AC-B (both proprietary) – were also evaluated in this study. Ru/AC-BM is the benchmark catalyst used for gasification campaigns on PSI's cHTG demonstration unit.6,53
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