Gasoline selective desulfurization catalyst
A desulfurization catalyst and selective technology, applied in molecular sieve catalysts, physical/chemical process catalysts, petroleum industry, etc., can solve problems such as increased olefin saturation rate, low desulfurization rate, and low mechanical strength
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Embodiment 1
[0029] SiO 2 The SAPO-11 molecular sieve of 12wt% is mixed with silica sol, and in the carrier, the mass ratio of the molecular sieve and the silicon dioxide contained in the binder is 8.5: 1.5, adding 2.5% of the scallops accounted for the dry basis weight of the carrier The powder is kneaded and extruded into strips, dried and roasted to obtain a shaped carrier.
[0030] Using ammonium nitrate aqueous solution as the exchange agent, ion-exchange the formed carrier, and turn it into a hydrogen-type sample after roasting; impregnate the above-mentioned carrier with Mg(NO 3 ) 2 and Ca(NO 3 ) 2 solution, the amount of immersion Mg and Ca accounted for 1.5% and 0.2% of the catalyst weight in terms of its oxides, dried, and roasted; The content in the catalyst is CoO 0.5%, MoO 3 6.0%, dry, and bake at 540°C for 3 hours.
[0031] At a reaction temperature of 260°C, a pressure of 2.0MPa, and a space velocity of 3.0h -1 1. Under the condition of hydrogen-to-oil ratio of 300, ...
Embodiment 2
[0033] SiO 2 1.8wt% SAPO-5 molecular sieve is mixed with alumina in a mass ratio of 5:5, and after adding 3.0% of the dry weight of the carrier and nitric acid of 4% by dry weight, kneading and extruding , dried and calcined to obtain a molded carrier;
[0034] Use ammonium nitrate aqueous solution as an exchange agent to carry out ion exchange on the above-mentioned formed carrier, and turn it into a hydrogen-type sample after roasting; impregnate the above-mentioned carrier with Mg(NO 3 ) 2 and Ce(NH 4 ) 2 (NO 3 ) 6 solution, the amount of immersed Mg and Ce is MgO, CeO2 accounted for 3.0% and 1.0% by weight of the catalyst, dried, and roasted; then, the above samples were impregnated with cobalt nitrate and ammonium molybdate solutions by equal impregnation method, and the contents of cobalt and molybdenum in the catalyst were respectively CoO4. 0%, MoO 3 6.0%, dry, and bake at 520°C for 4 hours.
[0035] At a reaction temperature of 280°C, a pressure of 2.2MPa, an...
Embodiment 3
[0037] APO-11 molecular sieve is mixed with silica sol, and the mass ratio of molecular sieve and silica sol is 6:4, and 2.5% of the dry basis weight of the carrier is added with scallop powder, kneaded and extruded to form, dried and roasted to obtain molding carrier.
[0038] Using ammonium nitrate aqueous solution as an exchange agent, ion-exchange the above-mentioned formed carrier, and turn it into a hydrogen-type sample after roasting; impregnate the above-mentioned carrier with Ca(NO 3 ) 2 and La(NO 3 ) 3 solution, the amount of Ca and La immersed in CaO and La 2 o 3 accounted for 0.3% and 1.5% by weight of the catalyst, dried, and roasted; then, the above-mentioned samples were immersed in cobalt nitrate and ammonium molybdate solutions by equal impregnation method, and the contents of cobalt and molybdenum in the catalyst were respectively CoO 3.5% in terms of oxides. %, MoO 3 15.0%, dry, and bake at 560°C for 2 hours.
[0039] At a reaction temperature of 240...
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