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A kind of multi-layer fluidized bed for the alkylation reaction of phenolic compound and its application

A phenolic compound and alkylation reaction technology, applied in the field of multi-layer fluidized bed, can solve the problems of no fluidized bed reactor, such as alkylphenolic compound, easy penetration and escape of alkylating agent, difficult separation, etc. The effect of avoiding unstable product composition, reducing residence time and reducing side reactions

Inactive Publication Date: 2016-06-15
东营海源化工股份有限公司 +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The high content of 2,6-di-tert-butyl-p-cresol brings great waste of production capacity and difficulty in separation
However, for the alkylation reaction of phenolic compounds, the ordinary fluidized bed still has serious shortcomings: if the bed layer is shallow, the alkylating agent is easy to penetrate and escape, especially when isobutylene is used as the alkylating agent, isobutylene is easy to penetrate. Permeates the bed of solid catalyst particles and exits the fluidized bed with the reaction mixture
Therefore, there are no examples of fluidized bed reactors used in the industrial production of alkylphenols in China so far.

Method used

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  • A kind of multi-layer fluidized bed for the alkylation reaction of phenolic compound and its application
  • A kind of multi-layer fluidized bed for the alkylation reaction of phenolic compound and its application
  • A kind of multi-layer fluidized bed for the alkylation reaction of phenolic compound and its application

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0029] A cylindrical fluidized bed cylinder is used, in which 5 layers of composite baffles are placed. Each composite baffle is composed of horizontal pipes, coarse screens, and fine screens. From bottom to top, the horizontal pipes, coarse The order of the screen and the fine screen should be installed firmly. All the composite baffles are connected together through 4 risers (including the water inlet riser 2 and the water outlet riser 5) to form a baffle group together. All the horizontal pipes and standpipes forming the baffle group are connected internally and put into the fluidized bed cylinder as a whole from above. When the baffle plate group is put into the fluidized bed cylinder, catalyst particles are placed on each composite baffle, and the static height of the catalyst particle layer is equal to one-half of the inner diameter of the fluidized bed cylinder. Two of the water inlet standpipes are connected to the external water inlet pipes, and two of the water outl...

Embodiment 2

[0033] A cylindrical fluidized bed cylinder is used, in which 6 layers of composite baffles are placed. Each composite baffle is composed of horizontal pipes, coarse screens, and fine screens. From bottom to top, the horizontal pipes, coarse The order of the screen and the fine screen should be installed firmly. All the composite baffles are connected together through 4 risers (including the water inlet riser 2 and the water outlet riser 5) to form a baffle group together. All the horizontal pipes and standpipes forming the baffle group are connected internally and put into the fluidized bed cylinder as a whole from above. When the baffle group is put into the fluidized bed cylinder, catalyst particles are placed on each composite baffle, and the static height of the catalyst particle layer is equal to one-fifth of the inner diameter of the fluidized bed cylinder. Two of the water inlet standpipes are connected to the external water inlet pipes, two of the water outlet riser ...

Embodiment 3

[0037] A cylindrical fluidized bed cylinder is used, in which 4 layers of composite baffles are placed. Each composite baffle is composed of horizontal pipes, coarse screens, and fine screens. From bottom to top, the horizontal pipes, coarse The order of the screen and the fine screen should be installed firmly. All the composite baffles are connected together through 4 risers (including the water inlet riser 2 and the water outlet riser 5) to form a baffle group together. All the horizontal pipes and standpipes forming the baffle group are connected internally and put into the fluidized bed cylinder as a whole from above. When the baffle group is put into the fluidized bed cylinder, catalyst particles are placed on each composite baffle, and the static height of the catalyst particle layer is equal to one-third of the inner diameter of the fluidized bed cylinder. Two of the water inlet standpipes are connected to the external water inlet pipes, two of the water outlet riser ...

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Abstract

A multi-layer fluidized bed for the alkylation reaction of phenolic compounds is composed of more than two layers of composite baffles placed in a fluidized bed cylinder, the composite baffles are placed horizontally, and their peripheral edges are in contact with the fluidized bed. On the inner wall of the fluidized bed cylinder, above each composite baffle is a relatively independent compartment, and each compartment is filled with catalyst particles independently to form a first-stage fluidized bed; the composition of the composite baffle is as follows: The bottom layer is a horizontal row pipe composed of several short pipes welded. The interior of the short pipes is connected. One end of these short pipes is connected with the water inlet standpipe, and the other end is connected with the inside of the water outlet standpipe and welded firmly; the upper part of the horizontal row pipe is A layer of coarse screen, the outer diameter of the coarse screen is the same as the inner diameter of the fluidized bed cylinder; above the coarse screen is a layer of fine screen, the outer diameter of the fine screen is the same as the inner diameter of the fluidized bed cylinder; the fine screen The pore size of the fluidized bed is smaller than the particle size of the catalyst particles carried on it; the bottom of the fluidized bed is provided with a raw material inlet pipe, and the top is provided with a reaction product outlet pipe.

Description

technical field [0001] The invention relates to a multilayer fluidized bed for alkylation reaction of phenolic compounds and an application method thereof, which is especially suitable for continuous production of alkylphenolic compounds. Background technique [0002] Phenolic compounds (including phenol, m-cresol, p-cresol, o-cresol and other phenolic compounds, etc.) undergo an alkylation reaction to generate alkylphenol compounds. [0003] For phenolic compounds with benzene rings, the non-occupied carbon atoms may be connected with an alkyl group to generate alkylated products with different numbers of alkyl groups, so the alkylation of phenolic compounds is a very complicated reaction. For example, through an alkylation reaction, a tert-butyl group is attached to the 2- or 6-position on the benzene ring of p-cresol to generate 2-tert-butyl p-cresol; the 2-position and 6-position on the benzene ring of p-cresol Each position is connected with a tert-butyl group at the s...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J8/28C07C37/16C07C37/14C07C39/06
Inventor 刘彦丰刘锋李崇赵秋云王芳张力擎张大治张曾
Owner 东营海源化工股份有限公司
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