Method for preparing propylene from methanol
A technology for producing propylene and methanol from methanol, which is applied in chemical instruments and methods, hydrocarbon production from oxygen-containing organic compounds, chemical recovery, etc., can solve problems such as difficult control of reactor temperature, achieve high efficiency, reduce reaction types, The effect of reducing the exotherm of the reaction
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Embodiment 1
[0052] In order to evaluate the rationality of the new process based on methanol to propylene, such as figure 1 The shown model test device simulates the process conditions of industrial devices for experiments, wherein the catalyst in the first reactor (ie DME reactor) is γ-Al 2 o 3 (Select the DME-1 catalyst of Clariant Co., Ltd.), and fill in two layers. The catalyst in the second reactor is A, which is evenly packed in the first to sixth catalyst beds of the second reactor. Wherein, the feed amount of fresh methanol to the first reactor is 2.5kg / h, and the total amount of catalyst loaded in the first reactor is 1.8kg, and the reaction pressure is 0.8MPa. The total amount of catalyst loaded in the second reactor is 2.5kg, and the reaction pressure is 0.09MPa.
[0053] Fresh methanol is mixed with methanol from the top of the second distillation tower, wherein 50 wt% of the total amount of methanol is preheated to about 250 ° C, and enters from the top of the first reacto...
Embodiment 2
[0056] The difference from Example 1 is that the filling method of the catalyst in the second reactor is: the catalysts A and C with a mass ratio of 1:1 are evenly mixed and filled into the second reactor of the second reactor. One to sixth catalyst beds. The experimental results are shown in Table 1.
Embodiment 3
[0058] The difference from Example 1 is that the filling method of the catalyst in the second reactor is: the catalyst A is filled from the uppermost layer in the catalyst bed of the second reactor to the lower interlayer to the corresponding Catalyst bed, catalyst C is packed into the rest of the catalyst bed, and the mass ratio of catalysts A and C is 1:1. The experimental results are shown in Table 1.
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