Device for producing ethylene and propylene from oxygen-containing compounds
A compound and ethylene technology, applied in the direction of hydrocarbon production from oxygen-containing organic compounds, bulk chemical production, ethylene production, etc., can solve the problems of low selectivity, low yield of ethylene propylene, etc., to reduce side reactions and reduce by-products The amount, the effect of good technical effect
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Embodiment 1
[0021] The test is attached figure 1 The shown device uses SAPO-34 as a catalyst, methanol as a raw material, ethanol as a terminator, and carbon tetraolefins as a passivator, wherein the fluidized bed reactor II catalyst feed port is vertical to the bottom of the fluidized bed reactor II The height is 1 / 20 of the height of the fluidized bed reactor II, and the vertical distance between the catalyst outlet of the fluidized bed reactor II and the top of the fluidized bed reactor II is 1 / 20 of the height of the fluidized bed reactor II. The vertical height of the catalyst inlet of the regenerator 2 from the bottom of the regenerator 2 is 1 / 12 of the vertical length of the regenerator 2, and the vertical height of the catalyst outlet from the catalyst inlet of the regenerator 2 is 1 / 10 of the vertical length of the regenerator 2. The vertical height of the catalyst inlet of the fluidized bed reactor 1 from the bottom of the fluidized bed reactor 1 is 1 / 20 of the vertical height o...
Embodiment 2
[0023] The test is attached figure 1 The shown device uses SAPO-34 as a catalyst, dimethyl ether as a raw material, no terminator, and carbon tetraolefin as a passivating agent, wherein the catalyst inlet of fluidized bed reactor II is connected to the bottom of fluidized bed reactor II The vertical height is 1 / 20 of the height of the fluidized bed reactor II, and the vertical distance between the catalyst outlet of the fluidized bed reactor II and the top of the fluidized bed reactor II is 1 / 20 of the height of the fluidized bed reactor II. The vertical height of the catalyst inlet of the regenerator 2 from the bottom of the regenerator 2 is 1 / 12 of the vertical length of the regenerator 2, and the vertical height of the catalyst outlet from the catalyst inlet of the regenerator 2 is 1 / 10 of the vertical length of the regenerator 2. The vertical height of the catalyst inlet of the fluidized bed reactor 1 from the bottom of the fluidized bed reactor 1 is 1 / 20 of the vertical h...
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