A radial reactor and a process method of chemical chain reaction

A process method and reactor technology applied in the field of radial reactors to achieve the effects of simple process flow, uniform distribution of raw material gas, and short service life

Active Publication Date: 2021-07-09
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] In order to solve the problems that most of the chemical chain reactors in the prior art are axially moving bed or fluidized bed reactors, there are large pressure drop and uneven gas distribution in the reaction, the present invention provides a radial reactor, which is applied to The chemical chain reaction can effectively reduce the pressure drop, solve the problem of gas distribution, the reaction efficiency is higher, and the problem of gas-solid separation is also solved

Method used

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  • A radial reactor and a process method of chemical chain reaction
  • A radial reactor and a process method of chemical chain reaction
  • A radial reactor and a process method of chemical chain reaction

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Embodiment 1

[0031] A radial reactor such as figure 1As shown, it includes three layers of inner cylinder 11, middle cylinder 12 and outer cylinder 13, several openings are uniformly distributed on the cylinder wall of the inner cylinder 11 and the middle cylinder 12, and the cylinder wall of the outer cylinder 13 is a closed entity; the reaction The device is divided into an upper reaction zone 100 and a lower reaction zone 200, and a closed zone 300 is set between the two reaction zones. The closed zone 300 is in the central space of the inner cylinder 11, and in the wall space of the middle cylinder 12 and the outer cylinder 13. There is a refractory brick filling section 301, two upper reaction zone inlets 101, 102 symmetrically distributed are arranged at the bottom of the upper reaction zone 100, and two upper reaction zone outlets 103, 104 symmetrically distributed are arranged at the top of the upper reaction zone 100; Yes, the lower reaction zone is also provided with lower reacti...

Embodiment 2

[0033] A radial reactor such as figure 2 As shown, it includes three layers of inner cylinder 11, middle cylinder 12 and outer cylinder 13, several openings are uniformly distributed on the cylinder wall of the inner cylinder 11 and the middle cylinder 12, and the cylinder wall of the outer cylinder 13 is a closed entity; the reaction The device is divided into an upper reaction zone 100 and a lower reaction zone 200, and a closed zone 300 is set between the two reaction zones. The closed zone 300 is in the central space of the inner cylinder 11, and in the wall space of the middle cylinder 12 and the outer cylinder 13. Each has a refractory brick filling section 301, a dumbbell-shaped buffer device 302 is provided between the inner cylinder and the middle cylinder corresponding to the closed area 300, and two upper reaction area inlets 101, 102 symmetrically distributed are arranged at the lower part of the upper reaction area 100 , the top of the upper reaction zone 100 is ...

Embodiment 3

[0035] A radial reactor such as figure 1 As shown, it includes three layers of inner cylinder 11, middle cylinder 12 and outer cylinder 13, several openings are uniformly distributed on the cylinder wall of the inner cylinder 11 and the middle cylinder 12, and the cylinder wall of the outer cylinder 13 is a closed entity; the reaction The device is divided into an upper reaction zone 100 and a lower reaction zone 200, and a closed zone 300 is set between the two reaction zones. The closed zone 300 is in the central space of the inner cylinder 11, and in the wall space of the middle cylinder 12 and the outer cylinder 13. There is a refractory brick filling section 301, two upper reaction zone inlets 101, 102 symmetrically distributed are arranged at the bottom of the upper reaction zone 100, and two upper reaction zone outlets 103, 104 symmetrically distributed are arranged at the top of the upper reaction zone 100; Yes, the lower reaction zone is also provided with lower react...

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Abstract

A radial reactor and a process method for chemical chain reaction, the reactor includes an inner cylinder, a middle cylinder and an outer cylinder, a plurality of openings are uniformly distributed on the walls of the inner cylinder and the middle cylinder, and the wall of the outer cylinder is a closed entity; The reactor has at least two reaction zones, a closed zone is arranged between each reaction zone, and an inlet and an outlet are arranged on the outer cylinder wall of each reaction zone. The above-mentioned reactor is used for the chemical chain reaction, and the oxygen carrier is densely piled between the inner cylinder and the wall of the middle cylinder, and the reaction gas in each reaction stage is fed from the lower inlet of each reaction zone, and radially counterflows with the oxygen carrier. contact reaction. Using the chemical chain reaction process of this reactor, it has the advantages of uniform distribution of raw material gas and small bed pressure drop; combining multiple or two reactors into one body reduces the gas-solid separation device and realizes valveless operation. It not only solves the separation of gas and solid, but also solves the problems of short valve life under high temperature and easy wear of oxygen carrier in the valve.

Description

technical field [0001] The invention relates to a radial reactor and a process method using the radial reactor for chemical chain reaction, which belongs to the technology in the field of chemical chain hydrogen production. Background technique [0002] Hydrogen is an important process raw material for refineries. It is widely used in gasoline, diesel, residual oil hydrogenation and other processes to adjust the hydrogen-carbon ratio of products and desulfurization and denitrogenation. From a global perspective, crude oil is becoming more and more heavy and inferior. For large-scale refineries, the hydrocracking and hydrotreating process routes in the processing of heavy and inferior crude oil are beneficial to "eat dry squeezed raw materials." The efficiency is better than that of the coking route. With the continuous acceleration of oil product quality upgrading, the demand for hydrogen in refineries is increasing rapidly. [0003] Hydrogen production from natural gas has...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01B3/34
CPCC01B3/34C01B2203/0205C01B2203/06C01B2203/0805
Inventor 方向晨梁皓尹泽群刘全杰张锦桦
Owner CHINA PETROLEUM & CHEM CORP
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