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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

Active Publication Date: 2013-12-04
CHINA PETROLEUM & CHEM CORP +1
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AI Technical Summary

Problems solved by technology

[0006] The technical problem to be solved by the present invention is that in the prior art, the catalyst in the reactor cannot be quickly and safely unloaded when the two reactors are cut off, and it provides a new method for shutting down when the reaction-regeneration system is cut off in the methanol-to-olefins process method

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  • Method of stopping for unloading when cutting reactor-regeneration system in process of preparing olefins from methanol

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Embodiment Construction

[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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Abstract

The invention relates to a method of stopping for unloading when cutting reactor-regeneration system in a process of preparing olefins from methanol, mainly solving the problem of being incapable of rapidly and safely uploading catalyst for reactor when cutting the reactor and regenerator existing in the prior art. The method comprises the following steps: (1) providing a reactor-regeneration system comprising a reactor, a generator, two auxiliary combustion chambers, an auxiliary heating furnace, and a catalyst storage tank, wherein, the reactor and the generator are provided with a auxiliary combustion chamber respectively; (2) cutting the catalyst circulation in the reactor-regeneration system, stopping the methanol charging, starting the auxiliary heating furnace for heating steam which enters the reactor, simultaneously switching on the auxiliary combustion chamber of the generator for supplying heat to the generator; (3) switching on the auxiliary combustion chamber of the reactor, heating the replacement medium, then cutting in the reactor, simultaneously stopping the steam charging; (4) controlling the temperature of the reactor within 300-500 DEG C, controlling the temperature of the generator within 350-550 DEG C, respectively starting the catalyst unloading lines at the bottom of the reactor to start to unload catalyst; and (5) when the temperature of the reactor-regeneration system is below 150 DEG C, opening each vent valve to purge. The method disclosed in the invention solves the problems and can be used for the industrial production of low carbon olefins.

Description

technical field [0001] The invention relates to a method for unloading and shutting down the reaction-regeneration system when the reaction-regeneration system is cut off in the methanol-to-olefins process. technical background [0002] Olefins, the present invention refers to ethylene and propylene, are two important basic chemical raw materials, and their demand is constantly increasing. Generally, ethylene and propylene are produced through petroleum routes, but due to the limited supply and high price of petroleum resources, the cost of producing ethylene and propylene from petroleum resources continues to increase. In recent years, people have begun to vigorously develop the technology of converting alternative raw materials into ethylene and propylene. Among them, an important class of alternative raw materials for the production of low-carbon olefins is oxygenated compounds, such as alcohols (methanol, ethanol), ethers (dimethyl ether, methyl ethyl ether), esters (di...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C1/20C07C11/04C07C11/06
CPCY02P20/584Y02P30/20Y02P30/40
Inventor 齐国祯杨远飞陈伟俞志楠
Owner CHINA PETROLEUM & CHEM CORP
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