Cracking carbon five selective hydrogenation catalyst
A selective hydrogenation and catalyst technology, applied in physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, hydrocarbon cracking and hydrocarbon production, etc., can solve the problems of cracking carbon five fractions, etc. Achieve good selectivity and high activity
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Embodiment 1
[0025] Use lanthanum-modified alumina as the carrier, wherein the content of lanthanum in the carrier is 2% by mass, the alumina carrier is calcined at 1000°C, the density of the carrier is measured to be 0.68g / ml, and the specific surface area is 155m 2 / g, the volume average pore diameter is 18nm.
[0026] Dissolve an appropriate amount of nickel nitrate, lanthanum nitrate and silver nitrate in water to make an aqueous solution according to the catalyst to be prepared, impregnate the carrier with the same amount of impregnation, and impregnate twice, and dry at 120°C after each impregnation, and dry at 450°C Calcined at lower temperature, thus Catalyst 1 was prepared. Catalyst 1 contained: 12% nickel, 2% lanthanum (not including that carried by the support) and 1% silver, the balance being support.
Embodiment 2
[0028] Use lanthanum-modified alumina as the carrier, wherein the content of lanthanum in the carrier is 2% by mass, the alumina carrier is calcined at 1100°C, the density of the carrier is measured to be 0.7g / ml, and the specific surface area is 110m 2 / g, the volume average pore diameter is 15nm.
[0029] Dissolve an appropriate amount of nickel nitrate, lanthanum nitrate and silver nitrate in water to make an aqueous solution according to the catalyst to be prepared, impregnate the carrier with the same amount of impregnation, and impregnate twice, and dry at 120°C after each impregnation, and dry at 450°C Calcined under lower pressure, thus preparing Catalyst 2. Catalyst 2 contained: 18% nickel, 1% lanthanum (not including that carried by the support) and 2% silver, with the balance being support.
Embodiment 3
[0031] Use lanthanum-modified alumina as the carrier, wherein the content of lanthanum in the carrier is 2% by mass, the alumina carrier is calcined at 1100°C, the density of the carrier is measured to be 0.7g / ml, and the specific surface area is 110m 2 / g, the volume average pore diameter is 15nm.
[0032] Dissolve an appropriate amount of nickel nitrate, lanthanum nitrate and silver nitrate in water to make an aqueous solution according to the catalyst to be prepared, impregnate the carrier with the same amount of impregnation, and impregnate twice, and dry at 120°C after each impregnation, and dry at 450°C The catalyst 3 was prepared by calcining at the bottom. Catalyst 3 contained: 25% nickel, 2% lanthanum (not including that carried by the support) and 0.5% silver, with the balance being support.
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