Catalyst for converting sulfur-containing polycyclic aromatic hydrocarbons into monocyclic aromatic hydrocarbons and preparation method thereof
A technology for polycyclic aromatic hydrocarbons and monocyclic aromatic hydrocarbons, which is applied in the field of catalysts and their preparation, and can solve the problems of low selectivity, low yield of monocyclic aromatic hydrocarbons, and low conversion depth of polycyclic aromatic hydrocarbons.
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Embodiment 1
[0033] On a dry basis, 25 g FAU type zeolite (commercially available hydrogen type), 25 g ZSM-12 molecular sieve (commercially available hydrogen type) and 50 g γ-Al 2 o 3(Industrial product) Add to the mixer until uniform, then add 3 g of scallop powder, 5 g of HNO at a volume ratio of 1:1 to the mixture 3 solution and 40 g deionized water, and grind evenly to make a dough suitable for extrusion. It was extruded through a die in the shape of an elongated cylinder (diameter 1.7 mm), dried at 120 °C and calcined at 550 °C for 4 h, and then cut into carrier particles (1.7 × 4.0 mm) with the same size. for Z1.
[0034] Prepare a solution of chloroplatinic acid and cerium nitrate to impregnate the carrier particles at 40°C. The impregnating solution contains 0.25% of Pt and 0.25% of Ce on a dry basis of the carrier. After impregnating for 8 hours and drying , and calcined at 450°C for 3 h to obtain the finished catalyst A.
Embodiment 2~10
[0036] According to the preparation method and process provided in Example 1, a series of finished catalysts were prepared by changing the carrier composition and the type and content of metal precursors in the impregnation solution, as shown in Table 1.
[0037] Table 1
[0038]
Embodiment 11~20
[0040] Catalysts A~J prepared by Examples 1~10 are investigated on a supercritical fixed-bed reactor (maximum reaction pressure 10MPa, operating temperature is room temperature~600°C) and the mixture of sulfur-containing polycyclic aromatic hydrocarbons is converted into BTX (wherein B is Benzene, T is toluene, X is xylene) and other single-ring aromatic hydrocarbons. Table 2 is the evaluation raw material composition. The catalyst is loaded with 5 g, and at a reaction temperature of 370 ° C, a reaction pressure of 6 MPa, and a weight hourly space velocity of 2.0 hr -1 , Hydrogen / hydrocarbon molar ratio of 6.0 and contact with the catalyst, the product is recovered and component detection, the conversion results are shown in Table 3.
[0041] Table 2
[0042] Raw material composition
Non-Fang
Dimethyldibenzothiophene
Content (wt%)
0.02
24.54
24.61
...
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