Start and stop method of methanol to olefin reaction-regeneration system
A methanol-to-olefins and regeneration system technology, which is applied in ethylene production, hydrocarbon production from oxygen-containing organic compounds, biological raw materials, etc., can solve the problems of long start-up time and high energy consumption, so as to reduce the consumption of fuel gas and save The effect of start time
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[0045] Such as figure 1 The shown methanol-to-olefins reaction-regeneration system includes a methanol vaporizer 1, a vertical heat exchanger 2, a heating furnace 3, a reactor 4, a regenerator 5, a waiting catalyst circulation pipe 6, a regenerated catalyst circulation pipe 7, Combustion chamber 8, main fan 9, reactor loading and unloading agent line 10, regenerator loading and unloading agent line 11, catalyst tank 12, methanol pipeline 13, nitrogen pipeline 14, steam pipeline 15, reaction gas output pipeline 16, and regeneration flue gas Output line 17.
[0046] When the methanol-to-olefins reaction-regeneration system is shut down, the methanol load is reduced, and the air volume of the main fan 9 passing into the regenerator 5 is reduced in time. When the load is reduced to 200t / h, the dilution steam is added, and the heating furnace 3 is ignited; when the load drops to 90-140t / h, the flow rate of the dilution steam is increased to 20-40t / h; the amount of nitrogen gas hea...
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