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Fluidization reaction device and method for producing chlorothalonil by using same

A fluidized reaction and reactor technology, which is used in chemical instruments and methods, preparation of organic compounds, organic chemistry, etc., can solve the problems of removing heat from the fluidized bed, prone to local overheating, etc., to ensure the reaction Accuracy of temperature gradient, uniform internal temperature distribution, effect of increasing reaction yield

Pending Publication Date: 2021-04-09
JIANGSU XINHE AGROCHEM
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] CN101985089B discloses a tubular fluidized bed reactor in the production of chlorothalonil. The fluidized bed of the reactor includes a serpentine tube heat exchanger and a tubular heat exchanger, and the serpentine tube heat exchanger It is arranged under the lower head of the fluidized bed, and the tube-and-tube heat exchanger is arranged between the serpentine tube heat exchanger and the fluidized bed cylinder, but only contains a section of heat exchange tube, which is prone to local overheating areas
[0005] CN100404500C discloses a kind of production method of chlorothalonil with low hexachlorobenzene content, after isophthalonitrile is completely vaporized, it is taken out of the vaporizer with nitrogen, then mixed with chlorine and then entered into the fluidized bed for the first step reaction, the reaction product It is mixed with chlorine gas again, enters the fixed bed for chlorination, and the output mixed gas is condensed and collected to obtain chlorothalonil product, but does not involve the removal of heat in the fluidized bed

Method used

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  • Fluidization reaction device and method for producing chlorothalonil by using same
  • Fluidization reaction device and method for producing chlorothalonil by using same
  • Fluidization reaction device and method for producing chlorothalonil by using same

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Embodiment 1

[0069] This embodiment provides a fluidized reaction device, such as figure 1 As shown, the fluidized bed reaction device includes a reactor main body, which includes a first heat exchange tube group 5, a second heat exchange tube group 4, and a third heat exchange tube group that are independent from each other from top to bottom in the reactor body. Group 3, all are U-shaped heat exchange tubes with only a single inlet and outlet, and are all arranged in a regular octagon, such as figure 2 As shown; the catalyst outlet 1 is arranged at the bottom of the reactor main body, an air inlet channel 2 is arranged between the third heat exchange tube group 3 and the catalyst outlet 1, the outlet of the air inlet channel 2 faces the catalyst outlet 1, and the air inlet channel 2 is connected The gas inlet is set on the lower side of the reactor main body, the gas outlet 6 is set on the upper side of the reactor main body, and is set on the upper part of the first heat exchange tube ...

Embodiment 2

[0072] This embodiment provides a fluidized reaction device, the difference between the fluidized bed reaction device and embodiment 1 is only the height of the first heat exchange tube group, the second heat exchange tube group and the third heat exchange tube group and the reaction The ratio of the height of the main body of the device is respectively 0.125, 0.125 and 0.15, and the rest are the same as in Example 1.

Embodiment 3

[0074] This embodiment provides a fluidized reaction device, the difference between the fluidized bed reaction device and embodiment 1 is only the height of the first heat exchange tube group, the second heat exchange tube group and the third heat exchange tube group and the reaction The ratio of the height of the main body of the device is respectively 0.15, 0.15 and 0.1, and the rest are the same as in Example 1.

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Abstract

The invention provides a fluidization reaction device and a method for producing chlorothalonil by using the fluidization reaction device. The fluidization reaction device comprises a first heat exchange tube group, a second heat exchange tube group and a third heat exchange tube group which are independent of one another and are sequentially arranged in a reactor main body from top to bottom, the ratio of the heights of the first heat exchange tube group, the second heat exchange tube group and the third heat exchange tube group to the height of the reactor main body is (0.05-0.2): 1 independently, so that the reaction temperatures of the reactor main body at different axial heights can be well controlled, the temperature distribution in the reactor main body is uniform, no local overheating area exists, and the heat exchange efficiency is improved. The catalyst is prevented from coking in the reactor main body; according to the method for producing chlorothalonil by using the fluidization reaction device, the service life of a single batch of catalysts can be prolonged, and the proportion of chlorothalonil with hexachlorobenzene lower than 10ppm in the product is increased.

Description

technical field [0001] The invention relates to the technical field of fluidized reaction devices, in particular to a fluidized reaction device and a method for producing chlorothalonil. Background technique [0002] Chlorothalonil is a high-efficiency, low-toxicity, low-residue protective fungicide, which is widely used in the control of fungal diseases in agriculture and forestry, especially in economic crops such as vegetables and fruits. Twelve kinds of diseases have control effects. In addition, chlorothalonil also has important uses in the anti-mold industry, such as the manufacture of anti-mold paint and anti-mold wallpaper. The production scale of chlorothalonil in China is constantly expanding, and it has become one of the high-quality large-tonnage pesticide varieties in the world. [0003] The fluidized bed is the most critical equipment in the production of chlorothalonil, which is directly related to the output and product quality of chlorothalonil production....

Claims

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Application Information

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IPC IPC(8): B01J8/24B01J8/00C07C253/30C07C255/51
CPCB01J8/008B01J8/24C07C253/30C07C255/51
Inventor 王海波王振宇禚文峰
Owner JIANGSU XINHE AGROCHEM
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