Method for converting polycyclic aromatic hydrocarbons into monocyclic aromatic hydrocarbons
A technology for polycyclic aromatic hydrocarbons and monocyclic aromatic hydrocarbons, applied in the field of conversion of polycyclic aromatic hydrocarbons into monocyclic aromatic hydrocarbons, can solve the problems of low selectivity, low yield of monocyclic aromatic hydrocarbons, low conversion depth of polycyclic aromatic hydrocarbons, etc., and achieve the improvement of unsaturated The effect of speed, delay inactivation rate, and good technical effect
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Embodiment 1
[0030] The dry basis is 30g FAU type zeolite (commercially available hydrogen type), 10g BEA type zeolite (commercially available hydrogen type) and 60g γ-Al 2 o 3 (Industrial product) Add to the mixer until uniform, then add 3g of scallop powder, 5g of HNO at a volume ratio of 1:1 to the mixture 3 solution and 40g deionized water, and grind evenly to make a dough suitable for extrusion. It is extruded through a die, and the shape is a slender cylinder (diameter 1.7mm). After drying at 120°C, it is baked at 550°C for 4h, and then it is cut into carrier particles (1.7×4.0mm) with the same size, recorded as Z1.
[0031] Make a solution of chloroplatinic acid and impregnate the carrier particles at 40°C. The amount of Pt contained in the impregnating solution is 0.1% of the weight of the dry basis of the carrier. After 8h of impregnation and drying, it is calcined at 450°C for 3h to obtain a finished catalyst. a.
Embodiment 2~6
[0033] According to the preparation method and process provided in Example 1, a series of finished catalysts were prepared by changing the types of metal precursors in the impregnation solution during the impregnation of Z1 carrier particles, as shown in Table 1.
[0034] Table 1
[0035] Catalyst number
[0036] F
Embodiment 7~12
[0038] According to the preparation method and process provided in Example 1, a series of finished catalysts were prepared by changing the amount of metal impregnated during the impregnation of Z1 carrier particles, as shown in Table 2.
[0039] Table 2
[0040] Catalyst number
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