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Reaction system and reaction method of oxide recycling in mto process

A reaction system and oxide technology, applied in chemical instruments and methods, hydrocarbon production from oxygen-containing organic compounds, chemical recovery, etc., can solve the problem of low conversion rate of oxides and achieve high selectivity of ethylene and propylene

Active Publication Date: 2022-07-12
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] One of the technical problems to be solved by the present invention is the technical problem of low oxide conversion rate in the prior art when oxides are smelted back, and a reaction system for oxides smelted back in the MTO process is provided

Method used

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  • Reaction system and reaction method of oxide recycling in mto process
  • Reaction system and reaction method of oxide recycling in mto process
  • Reaction system and reaction method of oxide recycling in mto process

Examples

Experimental program
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Embodiment 1

[0026] using as figure 1 , 2 The device shown includes a reactor (17), a regenerator (18), a degassing tank (16), a regeneration up-sloping pipe (9), a regeneration down-sloping pipe (11), and a regenerated inclined pipe (19); wherein: The reactor (17) is composed of the dilute phase section (12) of the reactor and the dense phase section (13) of the reactor, and the dilute phase section (12) of the reactor is located above the dense phase section (13) of the reactor; the regenerator (18) It consists of a regenerator dilute phase section (14) and a regenerator dense phase section (15), the regenerator dilute phase section (14) is located above the regenerator dense phase section (15); the regeneration upslope pipe (9) is connected to the degassing The upper tank area (1) and the dense phase section (15) of the regenerator; the regeneration down-sloping pipe (11) is connected to the lower area (2) of the degassing tank and the dense phase section (13) of the reactor; The dens...

Embodiment 2

[0037] using as figure 1 , 2 The device shown includes a reactor (17), a regenerator (18), a degassing tank (16), a regeneration up-sloping pipe (9), a regeneration down-sloping pipe (11), and a regenerated inclined pipe (19); wherein: The reactor (17) is composed of the dilute phase section (12) of the reactor and the dense phase section (13) of the reactor, and the dilute phase section (12) of the reactor is located above the dense phase section (13) of the reactor; the regenerator (18) It consists of a regenerator dilute phase section (14) and a regenerator dense phase section (15), the regenerator dilute phase section (14) is located above the regenerator dense phase section (15); the regeneration upslope pipe (9) is connected to the degassing The upper tank area (1) and the dense phase section (15) of the regenerator; the regeneration down-sloping pipe (11) is connected to the lower area (2) of the degassing tank and the dense phase section (13) of the reactor; The dens...

Embodiment 3

[0048] using as figure 1 , 2 The device shown includes a reactor (17), a regenerator (18), a degassing tank (16), a regeneration up-sloping pipe (9), a regeneration down-sloping pipe (11), and a regenerated inclined pipe (19); wherein: The reactor (17) is composed of the dilute phase section (12) of the reactor and the dense phase section (13) of the reactor, and the dilute phase section (12) of the reactor is located above the dense phase section (13) of the reactor; the regenerator (18) It consists of a regenerator dilute phase section (14) and a regenerator dense phase section (15), the regenerator dilute phase section (14) is located above the regenerator dense phase section (15); the regeneration upslope pipe (9) is connected to the degassing The upper tank area (1) and the dense phase section (15) of the regenerator; the regeneration down-sloping pipe (11) is connected to the lower area (2) of the degassing tank and the dense phase section (13) of the reactor; The dens...

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Abstract

The invention relates to a reaction system and a reaction method for oxide back refining in the MTO process, and mainly solves the problem of low oxide conversion rate during oxide back refining in the prior art. In the present invention, the mixed oxide aqueous solution raw material produced by the MTO separation unit enters the lower area of ​​the degassing tank and the regenerated catalyst is contacted and reacted after degassing, the obtained pre-coking catalyst enters the reaction section of the MTO reactor through the regeneration inclined pipe, and the obtained reaction product returns to the MTO The dilute phase section of the reactor; the regenerated catalyst enters the upper area of ​​the degassing tank through the regeneration inclined pipe and contacts with the degassing medium, and the degassed product returns to the dilute phase section of the regenerator. After degassing, the regenerated catalyst enters the degassing tank through the overflow pipe of the degassing tank The technical solution in the lower area solves this problem well and can be used in MTO industrial production.

Description

technical field [0001] The invention relates to a reaction system and a reaction method for oxide back refining in an MTO process. Background technique [0002] Light olefins, namely ethylene and propylene, are two important basic chemical raw materials, and their demand is increasing. Generally, ethylene and propylene are produced through the petroleum route. However, due to the limited supply of petroleum resources and higher prices, the cost of producing ethylene and propylene from petroleum resources is increasing. In recent years, people have begun to vigorously develop technologies for converting alternative raw materials to ethylene and propylene. Among them, a class of important alternative raw materials for the production of light olefins are oxygenated compounds, such as alcohols (methanol, ethanol), ethers (dimethyl ether, methyl ethyl ether), esters (dimethyl carbonate, methyl formate) These oxygenated compounds can be converted from coal, natural gas, biomass ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C1/20C07C1/207C07C11/04C07C11/06
CPCC07C1/20C07C1/207C07C2529/85C07C11/04C07C11/06Y02P20/584
Inventor 李晓红齐国祯金永明王艳学
Owner CHINA PETROLEUM & CHEM CORP