Cobalt-based catalysts and their applications in f-t synthesis
A cobalt-based catalyst and catalyst technology, applied in the preparation of liquid hydrocarbon mixtures, petroleum industry, etc., can solve the problems of multi-equipment investment, complex synthesis process, etc., and achieve simple preparation process, easy industrial production, high reactivity and liquid hydrocarbon The effect of product-like selectivity
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Embodiment (1)
[0036] will be 96cm 3 A mixed alcohol solution containing methanol and polyethylene glycol 400 (the volume ratio of methanol and polyethylene glycol 400 is 15 / 1) and 270cm 3 Deionized aqueous solution was made into a solution, and then 5.5 grams of cobalt nitrate hexahydrate and 0.06 grams of Ru(NO)(NO 3 ) 3 added to the above solution. After treatment at 90°C to form an impregnating solution, 9 g of Al 2 o 3 and SiO 2 mixture (mass ratio of SiO 2 / Al 2 o 3 =80) into the above impregnation solution. With stirring, the temperature was raised to 100°C to evaporate the solvent. The obtained paste solid was put into a muffle furnace, and calcined at 400° C. for 4 hours to obtain a cobalt-based catalyst. The specific surface area and pore volume of the catalyst were calculated using N 2 Determination of adsorption method. During the test, the sample was first degassed and pretreated at 250°C for 10 hours to remove the physically adsorbed moisture in the sample, and then...
Embodiment (2)
[0038]The F-T synthesis reaction performance evaluation test of the cobalt-based catalyst prepared in Example 1 was carried out in a slurry bed reactor. F-T synthesis reaction conditions are T=250℃, P=2MPa, H 2 / CO=2. Gas phase products are directly analyzed online for qualitative and quantitative analysis by gas chromatography. 15 grams of cobalt-based catalysts prepared in Example (1) were directly added to 1000 cm 3 Liquid paraffin slurry bed reactor. Then carry out the reduction treatment in the slurry bed reactor (T=260℃, normal pressure, H 2 Air velocity = 3600cm 3 (g-catalyst h) -1 ) for 16 hours. After the reduction treatment is finished, the temperature of the slurry bed reactor is gradually lowered to 250° C., and the pressure is raised to 2 MPa to carry out the F-T synthesis reaction. The reaction results show that within 30 hours after reaching the reaction temperature, the conversion rate of CO can reach ~65-49%, and the selectivity of liquid hydrocarbon pr...
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