Method for preparing aromatics from raw material of methanol
A technology for methanol and raw materials, applied in the field of preparing aromatic hydrocarbons from methanol raw materials, can solve the problems of low aromatics selectivity and the like
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Embodiment 1
[0028] The methanol raw material enters the fluidized bed reactor and contacts with the Zn-La-P-ZSM-5 catalyst for reaction. The mass percent content of methanol in the methanol raw material is 10%. The temperature of each point in the fluidized bed reactor is 480°C, the reaction gauge pressure is 0 MPa, and the methanol weight space velocity is 0.2 hours -1 , the residence time of methanol in the catalyst bed is 32 seconds, the catalyst bed density is 470 kg / m3, and the residence time-catalyst bed density compensation factor is 15×10 3 Second Kilogram / Cubic Meter.
[0029] In the Zn-La-P-ZSM-5 catalyst, based on the mass percentage of the catalyst, the Zn element content is 7%, the La element content is 5%, and the P element content is 3%. The reaction results are shown in Table 1.
Embodiment 2
[0031] According to the method and step of embodiment 1, adopt the catalyst of embodiment 1. The mass percent content of methanol in the methanol raw material is 30%. The temperature of each point in the fluidized bed reactor is 450°C, the reaction gauge pressure is 0.2 MPa, and the methanol weight space velocity is 4 hours -1 . Other reaction conditions and reaction results are shown in Table 1.
Embodiment 3
[0033] According to the method and step of embodiment 1, adopt the catalyst of embodiment 1. The mass percent content of methanol in the methanol raw material is 100%. The temperature of each point in the fluidized bed reactor is 520°C, the reaction gauge pressure is 0.1 MPa, and the methanol weight space velocity is 2.5 hours -1 . Other reaction conditions and reaction results are shown in Table 1.
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