Method for preparing low carbon olefins from oxygen-containing compound by conversion
A low-carbon olefin and production method technology, which is applied in the direction of hydrocarbon production from oxygen-containing organic compounds, ethylene production, hydrocarbon cracking, etc., can solve the problem of low yield of low-carbon olefins, many by-products of C4 and above hydrocarbons, etc. problems, achieve the effect of reducing separation cost, reducing the generation of by-products, and reducing energy supply
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Embodiment 1
[0018] in such as figure 1 In the reaction device shown, the fluidized bed reactor adopts a fast fluidized bed, the catalyst adopts SAPO-34, the reaction temperature is 500°C, the reaction pressure is 0.1MPa in gauge pressure, and the gas linear velocity in the reactor is 1.5m / s; tube side of the prereactor is filled with γ-Al 2 o 3 / SiO 2 Catalyst, the raw material is methanol, the raw material inlet temperature is 120°C, the reaction pressure is 0.4MPa in gauge pressure, and the weight hourly space velocity is 4h -1 ; The tube side of the fixed bed reactor is filled with ZSM-5 catalyst, carbon four and above hydrocarbons (C4 + ) mixed feed (the stock material comes from the mixed hydrocarbon cycle of the MTO product gas separation system), the reactor inlet temperature is 600 ° C, the reaction pressure is 0.15 MPa in gauge pressure, C4 + The weight hourly space velocity is 4h -1 . The regenerator adopts a turbulent flow bed, the regeneration medium is air, the regener...
Embodiment 2~5
[0020] According to the conditions described in Example 1, only the reaction temperature of the fluidized bed reactor was changed, and the experimental results are shown in Table 1.
[0021] Table 1
[0022]
Embodiment 6~7
[0024] According to the conditions described in Example 1, only the reaction pressure of the fluidized bed reactor was changed, and the experimental results are shown in Table 2.
[0025] Table 2
[0026]
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