Method for preparing propylene by catalyzing methanol/dimethyl ether with composite molecular sieve with core-shell structure
A molecular sieve catalyzed methanol and composite molecular sieve technology, applied in molecular sieve catalysts, chemical instruments and methods, chemical/physical processes, etc.
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Embodiment 1
[0011] Embodiment 1, methanol propylene reaction:
[0012] A core-shell molecular sieve with a silicon-aluminum ratio of 140 HZSM-5 molecular sieve as the core and SBA-15 molecular sieve as the shell (HZSM-5 particle size 400 nm, SBA-15 shell thickness 200 nm) was selected as the catalyst. After molding and granulating to 40-60 mesh, put it into a fixed-bed reactor with an inner diameter of 6mm, fill the upper and lower parts of the catalyst with quartz sand, heat the catalyst to about 460 °C with nitrogen, pretreat for 5 hours, and then pass methanol and water Steam mixed with feed gas, the liquid hourly space velocity is 2 h -1 , the molar ratio of methanol to water vapor is 1:3, and the reaction pressure is 0.1 MPa. The methanol conversion rate is 100%, the propylene selectivity reaches 54.1%, and the P / E ratio reaches 15.0.
Embodiment 2
[0013] Embodiment 2, reaction of methanol to propylene:
[0014] A core-shell molecular sieve with a silicon-aluminum ratio of 140 HZSM-5 molecular sieve as the core and SBA-15 molecular sieve as the shell (HZSM-5 particle size 400 nm, SBA-15 shell thickness 200 nm) was selected as the catalyst. After molding and granulating to 40-60 mesh, put it into a fixed-bed reactor with an inner diameter of 6mm, fill the upper and lower parts of the catalyst with quartz sand, heat the catalyst to about 400 °C with nitrogen, pretreat for 5 hours, and then pass methanol and nitrogen Mixed feed gas with a liquid hourly space velocity of 1 h -1 , the molar ratio of methanol to nitrogen is 5:1, and the reaction pressure is 0.1 MPa. The conversion rate is 97.6%, the propylene selectivity reaches 41.9%, and the P / E ratio is 7.6.
Embodiment 3
[0015] Embodiment 3, methanol propylene reaction:
[0016] HZSM-5 molecular sieve with a silicon-aluminum ratio of 280 was selected as the core, and SBA-15 molecular sieve was used as the shell (HZSM-5 particle size 800 nm, SBA-15 shell thickness 300 nm) as the catalyst. After molding and granulating to 40-60 mesh, put it into a fixed-bed reactor with an inner diameter of 6mm, fill the upper and lower parts of the catalyst with quartz sand, heat the catalyst to about 460 °C with nitrogen, pretreat for 5 hours, and then pass methanol and water Steam mixed with feed gas, the liquid hourly space velocity is 0.1 h -1 , the molar ratio of methanol to water vapor is 1:10, and the reaction pressure is 0.1 MPa. The conversion rate is 97.7%, the propylene selectivity reaches 48.0%, and the P / E ratio is 14.2.
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