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Stepped fluidized bed gas distribution plate

A gas distribution plate and gas distribution technology, applied in chemical/physical processes, chemical instruments and methods, etc., can solve the problems of abrasion of internal components, low heat and mass transfer efficiency, and low operating elasticity, and reduce erosion and erosion. , The structure is simple and sturdy, and the effect of the movement is relaxed.

Active Publication Date: 2019-12-31
WANHUA CHEM GRP CO LTD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the above-mentioned invention has low operating flexibility. In order to make the large-particle materials start to fluidize, the gas velocity in the entire ventilation area can only be increased. The solid particles with low particle density or small particle size have a large momentum, which will make the side wall area of ​​the fluidized bed Severe abrasion of internal components such as hood and hood
[0010] Therefore, it is necessary to develop a gas distribution plate that can not only overcome the low heat transfer and mass transfer efficiency caused by non-uniform materials in the fluidized bed, but also avoid the serious abrasion problem caused by excessive gas velocity, and also has high operating flexibility. becomes very important

Method used

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  • Stepped fluidized bed gas distribution plate
  • Stepped fluidized bed gas distribution plate
  • Stepped fluidized bed gas distribution plate

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0034] A pilot fluidized bed reactor with a diameter of 1 m and a height of 6 m is equipped with a gas distribution plate such as figure 1 and image 3 As shown, the central area 1a is a circular area located in the center of the distribution plate 1, accounting for 20% of the total area of ​​the distribution plate; the main area 1b is a circular area, accounting for 60% of the total area of ​​the distribution plate, and it passes through the central area 1a The inclined surface is connected, the thickness of the distribution plate is 30mm, the height difference H1 is 12mm, and the angle between the inclined surface and the horizontal plane of the central area is 60°; the wall area 1c is a circular area, accounting for 20% of the total area of ​​the distribution plate, located on the outer edge of the distribution plate 1, and connected to the main body area 1b through an inclined surface, the height difference H1 is 30mm, the inclined surface and the main body The angle bet...

Embodiment 2

[0039] A pilot fluidized bed reactor with a diameter of 1 m and a height of 6 m is equipped with a gas distribution plate such as figure 1 and image 3 As shown, the central area 1a is a circular area located in the center of the distribution plate 1, accounting for 50% of the total area of ​​the distribution plate; the main body area 1b is an annular area, accounting for 40% of the total area of ​​the distribution plate, and it is the same as the central area 1a Connected by an inclined surface, the thickness of the distribution plate is 25mm, the height difference H1 is 10mm, and the angle between the inclined surface and the horizontal plane of the central area is 30°; the wall area 1c is a ring-shaped area, accounting for 10% of the total area of ​​the distribution plate. The outer edge of the plate 1 is connected to the main area 1b through an inclined surface, the height difference H1 is 10mm, and the angle between the inclined surface and the horizontal plane of the mai...

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Abstract

The invention provides a novel gas distribution plate suitable for a fluidized bed reactor of a strong corrosion and strong exothermic reaction system. The distribution plate comprises a circular central area, a circular main body area and a circular wall surface area which rise in a stepped manner from inside to outside, and reducing short pipe type gas distribution holes which are uniformly distributed in each area; and each reducing short pipe type gas distribution hole comprises a bottom contraction section, a middle straight section and an upper expansion section. The ratios of the bottominlet diameters to the throat diameters of the bottom contraction sections of the distribution holes in the three areas are continuously increased from the central area to the wall area, and the gasflow rate in the corresponding ventilation area is continuously reduced, so the wall surface area is in a moving bed state, and the central area and the main body area are in a fluidized state, thereby the heat transfer and mass transfer efficiency of the fluidized bed is improved, catalyst active component loss caused by local overheating is avoided, and reactor corrosion caused by wall surface abrasion and local fluidization dead zones of the fluidized bed can be reduced.

Description

technical field [0001] The invention belongs to the field of chemical synthesis devices, in particular to a novel fluidized bed reactor gas distribution plate. Background technique [0002] Fluidized bed technology is widely used in chemical industry, metallurgy, medicine and other industries. In many application fields of fluidized beds, highly corrosive and exothermic reaction systems are involved, such as hydrogen chloride oxidation reaction, ethylene oxychlorination reaction, pulverized coal fluidized bed gasification reaction, etc. In order to achieve long-term stable operation of such highly corrosive and exothermic fluidized bed reactors, the following countermeasures must be taken: [0003] (1) Prevent the occurrence of dead zones in the fluidized bed from reducing the efficiency of heat transfer and mass transfer; [0004] (2) Prevent local overheating of the fluidized bed from consolidating catalyst particles or losing active components; [0005] (3) Prevent the...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J8/18B01J8/24
CPCB01J8/1818B01J8/24
Inventor 刘一周波衡华刘俊秦中宇张宏科华卫琦
Owner WANHUA CHEM GRP CO LTD
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