Method for preparing low-carbon olefins from oxides
A technology of low-carbon olefins and oxides, applied in the direction of producing hydrocarbons from oxygen-containing organic compounds, dehydration of hydroxyl-containing compounds to prepare ethers, chemical instruments and methods, etc., can solve the problems of low ethylene production and high cost, and achieve increased yield, Good temperature rise, the effect of controlling temperature rise
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Embodiment 1
[0025] Fusel oil refined from methanol is used, and its composition is shown in Table 1. Fusel oil is pretreated by strong acid cation exchange resin and distillation cutting to remove harmful impurities, and then enters the main reactor after mixing and preheating. Methanol is pre-reacted on a medium-sized fixed-bed reaction device, the inlet temperature of the pre-reactor is 260°C, the outlet temperature is 370°C, and the weight hourly space velocity of refined methanol in the pre-reactor is 2.0. The outlet materials (methanol, dimethyl ether, water) of the pre-reactor are mixed with the pretreated fusel oil and water vapor, and then enter the main reactor after preheating. The weight hourly space velocity of methanol and dimethyl ether in the main reactor is 0.8h -1 , the weight hourly space velocity of fusel alcohol is 0.6h -1 , the total carbon treatment space velocity caused by the addition of the two is equivalent to the methanol weight hourly space velocity of 1.2h -...
Embodiment 2
[0027] Fusel oil from Fischer-Tropsch synthetic water is used, and its composition is shown in Table 2. Fusel oil is pretreated by strongly acidic cation exchange resin and distillation cutting to remove harmful impurities, and then enters the main reactor after mixing and preheating. The refined methanol is pre-reacted on a medium-sized fixed-bed reaction device. The inlet temperature of the pre-reactor is 260°C, the outlet temperature is 370°C, and the weight hourly space velocity of the refined methanol in the pre-reactor is 2.0. The materials (methanol, dimethyl ether, water) at the outlet of the pre-reactor are mixed with fusel alcohol and water vapor, and then enter the main reactor after preheating. The weight hourly space velocity of methanol (and dimethyl ether) in the main reactor is 0.8h -1 , the weight hourly space velocity of fusel oil is 0.5h -1 , the space velocity of the total carbon (including methanol, dimethyl ether, fusel alcohol, etc.) treated in the main...
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