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Circulating method for cold regenerated catalyst and catalytic cracking reaction regenerating system

A technology for catalyst circulation and reaction regeneration, which is applied in the petrochemical field and can solve the problems of mixing hot and cold catalysts, inability to strip two solid particles, and short heat transfer time.

Active Publication Date: 2014-02-19
CHINA UNIV OF PETROLEUM (BEIJING)
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] The present invention aims to provide a catalytic cracking reaction regeneration system and a cold regenerated catalyst circulation method to solve the problems of mixing hot and cold catalysts, short heat transfer time, uneven mixing and heat transfer existing in the prior art
At the same time, the present invention also solves the problem that the prior art cannot strip the two kinds of solid particles while mixing, so that the present invention realizes stripping while fully mixing and exchanging the two solid particles.

Method used

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  • Circulating method for cold regenerated catalyst and catalytic cracking reaction regenerating system
  • Circulating method for cold regenerated catalyst and catalytic cracking reaction regenerating system
  • Circulating method for cold regenerated catalyst and catalytic cracking reaction regenerating system

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Embodiment Construction

[0062] In order to have a clearer understanding of the technical features, purposes and effects of the present invention, the specific implementation manners of the present invention will now be described with reference to the accompanying drawings.

[0063] Such as Figure 10 to Figure 14 As shown, the present invention provides five catalytic cracking reaction regeneration systems, and these catalytic cracking reaction regeneration systems all include: a riser reactor 40, a pre-lift section 30, a regenerator 60, and a heat collector arranged outside the regenerator 60 70. These catalytic cracking reaction regeneration systems also include: a gas-solid circulation mixed stripper arranged outside the riser reactor and the pre-lift section, and the gas-solid circulation mixed stripper can be used in the regeneration form of the fluidized catalytic cracking process Mix the first solid particles and the second solid particles at different temperatures, and strip off the flue gas ...

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Abstract

The invention provides a circulating method for a cold regenerated catalyst and a catalytic cracking reaction regenerating system. The catalytic cracking reaction regenerating system comprises a hoisting pipe reactor, a pre-hoisting section, a regenerator, a heater and a gas-solid annular flow mixing stripper, wherein the gas-solid annular flow mixing stripper is used for mixing a first solid grain and a second solid grain at different temperatures during a regenerating form fluid catalytic cracking process and stripping the smoke and air taken by the solid grains after being mixed; the first solid grain is a low-temperature catalyst or low-temperature to-be-generated agent; and the second solid grain is a high-temperature catalyst. The circulating method for the cold regenerated catalyst comprises the following steps of: mixing and exchanging heat of the first solid grain from the heater and the second solid grain from the regenerator in the gas-solid annular flow mixing stripper, and meanwhile, stripping the taken smoke and air, forming the mixed catalyst and then entering into the pre-hoisting section.

Description

technical field [0001] The invention relates to the field of petrochemicals, and relates to the cooling cycle technology and stripping of catalysts in the fluid catalytic cracking process. Mixing of two catalysts (between regenerated and / or spent) at different temperatures between tube and fluidized bed and stripping of solid particles in the mixture. Background technique [0002] The catalytic cracking reaction regeneration system usually consists of a riser reactor, a regenerator and a transfer pipeline. After the raw oil is atomized through the nozzle, it contacts with the high-temperature regenerated catalyst in the riser reactor, gasifies, undergoes thermal cracking reaction and catalytic reaction, at the same time, condensation reaction occurs and coke is produced, and the coke adheres to the surface of the catalyst to deactivate the catalyst , the deactivated catalyst (deactivated catalyst) is separated by the gas-solid separation equipment at the outlet of the riser...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10G11/18
Inventor 刘梦溪卢春喜王祝安范怡平
Owner CHINA UNIV OF PETROLEUM (BEIJING)
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