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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

Active Publication Date: 2019-03-12
CHNA ENERGY INVESTMENT CORP LTD +2
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Problems solved by technology

[0011] The main purpose of this application is to provide a shutdown method for the methanol-to-olefins reaction-regeneration system to solve the problems of longer startup time and more energy consumed in the shutdown method in the prior art

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  • Start and stop method of methanol to olefin reaction-regeneration system

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Embodiment 1

[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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Abstract

The invention provides a start and stop method of a methanol to olefin reaction-regeneration system. The methanol to olefin reaction-regeneration system comprises a reactor, a regenerator and catalyststorage equipment, wherein the reactor is communicated with the regenerator; and the catalyst storage equipment is communicated with the reactor and the regenerator. The start and stop method comprises a stop process and a start process. The stop process comprises: controlling the fixed carbon content of a catalyst in the regenerator between 1.5 percent and 3.0 percent, and conveying the catalyst, having the fixed carbon content between 1.5 percent and 3.0 percent, in the regenerator to the catalyst storage equipment. The start process comprises: conveying the catalyst in the catalyst storageequipment into the regenerator for combustion reaction. According to the start and stop method, the catalyst in the regenerator is controlled to have the highest fixed carbon content in the stop process, and the part of the catalyst is conveyed into the regenerator for the combustion reaction in the subsequent start process, thereby reducing the consumption of fuel required for heating the reactor and regenerator and saving the start time.

Description

technical field [0001] The present application relates to the field of methanol-to-olefins, in particular, to a method for shutting down a methanol-to-olefins reaction-regeneration system. Background technique [0002] Methanol to Olefin (MTO for short) technology uses methanol as raw material to contact with silicoaluminophosphate molecular sieve catalyst under low reaction pressure and suitable reaction temperature conditions to produce ethylene and propylene as the main products Technology. This technology by-products methane, ethane, propane, hydrogen and other combustible gases, C4, C5 and above components, as well as trace amounts of carbon dioxide, formic acid and acetic acid and other acid gases. When passing through the quenching and washing tower, most of the acid gas is neutralized by the alkali solution, while the heavy components above carbon five and organic substances such as aldehydes, ketones and alcohols soluble in water are partially condensed, and the te...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C1/20C07C11/04C07C11/06
CPCC07C1/20C07C11/04C07C11/06Y02P20/584Y02P30/20Y02P30/40
Inventor 宁英辉袁春亮王为林孙维金张飞飞
Owner CHNA ENERGY INVESTMENT CORP LTD
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