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A kind of method for preparing p-tert-butyltoluene

A technology of p-tert-butyltoluene and toluene, which is applied in the field of continuous liquid-liquid two-phase alkylation reaction to synthesize p-tert-butyltoluene, which can solve the problem of low mass transfer efficiency, long reaction time and unfavorable mass transfer in multiphase reaction phase interface To achieve the effect of improving the yield of the target product, high yield of the target product, and promoting heat transfer and mass transfer

Active Publication Date: 2022-01-28
BEIJING INSTITUTE OF TECHNOLOGYGY +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This method has the problems of low mass transfer efficiency of multiphase reaction phase interface, slow reaction rate, discontinuous production process, high sulfuric acid content, serious side reactions, long reaction time, large equipment volume, low equipment production capacity, high production cost, etc. Sulfuric acid leakage and corrosion are likely to occur at the shaft. The viscosity of sulfuric acid is high under low temperature reaction conditions, which is not conducive to mass transfer, and the power required by the agitator increases sharply.

Method used

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  • A kind of method for preparing p-tert-butyltoluene

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0057] The venturi mixer and the tubular reactor with SV internals are alternately connected as a new reactor group. The single tube length of the tubular reactor is 3m, and the inner diameter of the tube is 12mm. The length of all tubular reactors with internals The sum is 6m, and it consists of two Venturi mixers and two tubular reactors with SV internals connected alternately in sequence.

[0058] The single feed of toluene enters from the main inlet of the first Venturi mixer 11, and the single feed of concentrated sulfuric acid enters from the side inlet of the first Venturi mixer 11. After the toluene and concentrated sulfuric acid are mixed in the first Venturi mixer 11 Enter the first tubular reactor 21 with internals for pre-mixing, and the first liquid-phase isobutene enters the new reactor group from the side inlet of the second Venturi mixer 12 .

[0059] The molar flow rate of toluene is 2 kmol / h, the molar flow rate of sulfuric acid is 0.25 kmol / h, and the total ...

Embodiment 2

[0063] The venturi mixer and the tubular reactor with SX internals are alternately connected as a new reactor group. The length of the tubular reactor is 2m, the inner diameter of the tube is 25mm, and the sum of the length of all tubular reactors with internals is 14m. , consisting of seven Venturi mixers and seven tubular reactors connected alternately in sequence.

[0064] The single feed of toluene enters from the main inlet of the first Venturi mixer 11, and the single feed of concentrated sulfuric acid enters from the side inlet of the first Venturi mixer 11. After the toluene and concentrated sulfuric acid are mixed in the first Venturi mixer 11 Enter the first tubular reactor 21 with internals for pre-mixing, and the liquid-phase isobutene is fed in 6 streams, which enter the new reactor group from the side inlets of the second to seventh Venturi mixers respectively.

[0065] The total molar flow rate of toluene is 4.06kmol / h, the total molar flow rate of sulfuric acid...

Embodiment 3

[0069] The venturi mixer and the tubular reactor with SV internals are alternately connected as a new reactor group. The length of the tubular reactor is 1.8m, and the inner diameter of the tube is 11mm. The sum of the lengths of all tubular reactors with internals is 19.8m, composed of eleven Venturi mixers and eleven tubular reactors connected alternately in sequence.

[0070] The single feed of toluene enters from the main inlet of the first Venturi mixer 11, and the single feed of concentrated sulfuric acid enters from the side inlet of the first Venturi mixer 11. After the toluene and concentrated sulfuric acid are mixed in the first Venturi mixer 11 Enter the first tubular reactor 21 with internals for pre-mixing, and the liquid-phase isobutene is divided into 10 feeds, which enter the new reactor group from the second to eleventh Venturi mixer side inlets respectively.

[0071] The total molar flow of toluene is 5.6kmol / h, the total molar flow of sulfuric acid is 0.4kmo...

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Abstract

The invention provides a method for preparing p-tert-butyltoluene, wherein the novel reactor includes a plurality of Venturi mixers connected alternately in sequence and a tubular reactor with internals, and the tubular reaction with internals The outer wall of the device is provided with a jacket. It also relates to a method for combining p-tert-butyltoluene with a novel reactor, using isobutylene and toluene as raw materials, under the catalysis of concentrated sulfuric acid, toluene is fed in a single strand, concentrated sulfuric acid is fed in a single strand, and isobutylene is fed in multiple strands. Synthesis of p-tert-butyltoluene by continuous liquid-liquid two-phase alkylation reaction through a novel reactor group. The invention creates the novel reactor group for synthesizing p-tert-butyltoluene and its use method. The novel reactor group is applied to the continuous liquid-liquid two-phase alkylation reaction process of toluene and isobutylene, which not only has the advantages of uniform material mixing , the reaction temperature is controllable, the target product yield is high, the catalyst consumption is small, etc., and it can realize efficient, low-cost and continuous production of p-tert-butyltoluene.

Description

technical field [0001] The invention belongs to the field of equipment related to the preparation of p-tert-butyltoluene, and in particular relates to a method for continuous liquid-liquid two-phase alkylation reaction to synthesize p-tert-butyltoluene. Background technique [0002] As an important organic synthesis intermediate and pharmaceutical intermediate, p-tert-butyltoluene, its derivatives p-tert-butylbenzoic acid, p-tert-butylbenzyl chloride, p-tert-butylbenzaldehyde, methyl p-tert-butylbenzoate, etc. All have a wide range of uses, and are widely used in chemical synthesis, cosmetics, pharmaceuticals, flavors and fragrances and other industries. The annual demand of the market is very large, therefore, research on the synthesis of tert-butyltoluene has important value. [0003] The production method of p-tert-butyltoluene is mainly produced by the alkylation reaction of toluene and isobutylene under the catalysis of an acid catalyst. The existing traditional synth...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J8/06C07C15/02C07C2/70
CPCB01J8/06C07C2/70C07C15/02Y02P20/52
Inventor 黎汉生贾晨光周广增吴芹梁文强史大昕矫庆泽
Owner BEIJING INSTITUTE OF TECHNOLOGYGY
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