Method of stopping for unloading when cutting reactor-regeneration system in process of preparing olefins from methanol
A methanol-to-olefins and regeneration system technology, applied in ethylene production, hydrocarbon production from oxygen-containing organic compounds, biological raw materials, etc., can solve the problem that the catalyst cannot be unloaded quickly and safely, and achieve good technical results
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[0016] Such as figure 1 In the methanol-to-olefins reaction-regeneration system shown, the reactor is a fast bed, the regenerator is a turbulent bed, the catalyst is SAPO-34 molecular sieve, and the feed rate of methanol is 4 tons / hour. After the reaction-regeneration system is cut off, it will gradually stop Methanol feedstock enters the reactor. At the same time or after the methanol raw material is stopped, 380 ° C medium-pressure steam is introduced into the reaction system, and the steam volume is 50% of the methanol raw material stopped, that is, for every 1 ton of methanol feed is reduced, 0.5 tons of methanol is added to the reactor of water vapor. Turn on the reactor auxiliary combustion chamber. When there is no methanol in the reactor, the air heated by the auxiliary combustion chamber of the reactor is introduced, and the steam entering the reactor is gradually stopped. The reactor temperature is controlled between 350-400°C. While maintaining the fluidization ...
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