Method for preparing BTX and co-producing tetramethylbenzene from C9<+> heavy aromatic hydrocarbons
A technology of mesitylene and heavy aromatics, applied in the field of aromatics chemical production, can solve the problems of high added value of products, low conversion rate of raw materials, large output of dry gas, etc., and achieve high yield of target products, high conversion rate of raw materials, dry gas The effect of low gas yield
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Embodiment 1
[0030] Take C from a refinery 9 + Heavy aromatics as raw material, load 2% La after 500℃ hydrothermal treatment 2 O 3 Nano ZSM-5 molecular sieve (SiO 2 / Al 2 O 3 The molar ratio is 30) as the catalyst, the reaction temperature is 460℃, the pressure is 0.5MPa, and the raw material mass space velocity is 1.0h -1 Under the conditions of the catalytic cracking reaction, C 9 + The properties of the raw materials and the composition of the liquid phase products after cracking are shown in Table 1.
Embodiment 2
[0032] Catalytic cracking catalyst adopts 450℃ hydrothermal treatment to load 3% La 2 O 3 Nano ZSM-5 molecular sieve (SiO 2 / Al 2 O 3 The molar ratio is 30) catalyst, the reaction conditions are: temperature 450℃, pressure 0.2MPa, raw material mass space velocity 0.5h -1 .
[0033] Alkylation reactor is filled with 2% P 2 O 5 Modified ZSM-5 / MCM-22 composite molecular sieve (the mass ratio of ZSM-5 molecular sieve to MCM-22 molecular sieve is 2:1) catalyst, the reaction conditions are: reaction temperature 360℃, pressure 0.1MPa, raw material mass space velocity 1.0h -1 , The molar ratio of trimethylbenzene to methanol is 1:1.
[0034] After the above catalytic cracking, alkylation and separation processes, the yield of each product is shown in Table 2.
Embodiment 3
[0036] Catalytic cracking catalyst adopts 500℃ hydrothermal treatment to load 2% La 2 O 3 Nano ZSM-5 molecular sieve (SiO 2 / Al 2 O 3 The molar ratio is 30) the catalyst, the reaction conditions are: temperature 500℃, pressure 0.3MPa, raw material mass space velocity 1.0h -1 .
[0037] Alkylation reactor is filled with 3% P 2 O 5 Modified ZSM-5 / MCM-22 composite molecular sieve (the mass ratio of ZSM-5 molecular sieve to MCM-22 molecular sieve is 2:1) catalyst, the reaction conditions are: reaction temperature 420℃, pressure 0.2MPa, raw material mass space velocity 1.5h -1 , The molar ratio of trimethylbenzene to methanol is 2:1.
[0038] After the above catalytic cracking, alkylation and separation processes, the yield of each product is shown in Table 2.
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