Method for increasing yield of ethylene and propylene
A technology of propylene and ethylene, applied in the field of propylene yield, catalytic conversion of methanol or dimethyl ether to improve ethylene, and can solve problems such as low selectivity and low yield
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Embodiment 1
[0015] Using methanol as raw material, the first reaction zone and the second reaction zone both use riser reactors, with SAPO-34 molecular sieve as the catalyst, the reaction temperature in the first reaction zone is 450°C, the contact time is 2 seconds, and the reaction pressure is 0.05MPa; The reaction temperature in the second reaction zone is 480° C., the contact time is 3 seconds, and the reaction pressure is 0.02 MPa. In the experiment, after the reaction gas mixture in the first reaction zone is separated from the solid catalyst, the gas phase directly enters the second reaction zone for reaction. The total reaction results are as follows: methanol conversion rate is 100%, ethylene yield is 45%, and propylene yield is 33%.
Embodiment 2
[0017] Using dimethyl ether as raw material, the first reaction zone and the second reaction zone both use riser reactors, with SAPO-34 molecular sieve as the catalyst, the reaction temperature in the first reaction zone is 400 ° C, the contact time is 1 second, and the reaction pressure is 0.4 MPa; the reaction temperature in the second reaction zone is 500° C., the contact time is 5 seconds, and the reaction pressure is 0.3 MPa. In the experiment, after the reaction gas mixture in the first reaction zone is separated from the solid catalyst, the gas phase directly enters the second reaction zone for reaction. The total reaction results are as follows: the conversion rate of dimethyl ether is 99%, the yield of ethylene is 47%, and the yield of propylene is 34%.
Embodiment 3
[0019] Methanol and dimethyl ether are used as raw materials, the weight ratio of methanol and dimethyl ether is 1:1, the first reaction zone and the second reaction zone both adopt fast fluidized bed reactors, and SAPO-34 molecular sieve is used as the catalyst. The reaction temperature in the reaction zone is 500°C, the contact time is 3 seconds, and the reaction pressure is 1.2MPa; the reaction temperature in the second reaction zone is 550°C, the contact time is 6 seconds, and the reaction pressure is 1.0MPa. In the experiment, after the reaction gas mixture in the first reaction zone is separated from the solid catalyst, the gas phase directly enters the second reaction zone for reaction. The total reaction results are: the conversion rate of methanol and dimethyl ether is 100%, the yield of ethylene is 51%, and the yield of propylene is 30%. %.
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