Method and device for producing 3,4-dichloronitrobenzene through continuous kettle type reaction

A technology for dichloronitrobenzene and p-chloronitrobenzene is applied in chemical instruments and methods, preparation of organic compounds, organic chemistry, etc., and can solve problems such as prolonged production cycle, increased production cost, material and energy loss, etc. , to achieve the effect of simple process operation, low production cost and high level of automatic control

Inactive Publication Date: 2016-03-23
山东沾化天九化工有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

The market demand is 30,000 tons per year. At present, batch reactor reaction is adopted in China. Auxiliary operations such as loading and unloading are required in the production process of batch reactor. The labor intensity is high, and it is easy to cause the loss of materials and energy. The production cost increases, the production cycle is prolonged, and the product quality is not easy to be stable
Batch kettle production is not suitable for large-scale production and cannot meet market demand

Method used

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  • Method and device for producing 3,4-dichloronitrobenzene through continuous kettle type reaction

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Embodiment Construction

[0020] Accompanying drawing is a kind of specific embodiment of the present invention. The device for producing 3,4 dichloronitrobenzene by continuous tank reaction described in this embodiment includes reactor A1, reactor B2, reactor C3 and reactor D4 connected in series and having a liquid level difference before and after, and reactor D4 is connected to the storage tank 5, the storage tank 5 is connected to the washing kettle A7 through the mixing pump A6, the washing kettle A7, the washing kettle B8, and the washing kettle C9 are connected in series through the mixing pump B10 and the mixing pump C11 in sequence, and the outlet of the washing kettle C9 is provided with a liquid pump 12; the reactor A1, reactor B2, reactor C3 and reactor D4 are equipped with outer jacket, chlorine distribution pipe and stirring device; the reactor A1, reactor B2, reactor C4 and reactor D6 The horizontal position of each reactor lowers 8-25% of its own height successively; Described reactor ...

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Abstract

The invention relates to the field of chemical production and particularly discloses a method and device for producing 3,4-dichloronitrobenzene through a continuous kettle type reaction. According to the method, parachloronitrobenzene serves as a raw material. The method is characterized in that parachloronitrobenzene and ferric trichloride are prepared into mixed liquor, the mixed liquor enters reaction kettles continuously through a nitro compound pump, and meanwhile chlorine enters the bottom of a chlorination kettle; under the catalyst effect, parachloronitrobenzene and chlorine react to generate 3,4-dichloronitrobenzene; later, by the utilization of the high-order difference among all the reaction kettles, the materials overflow sequentially to enter the reaction kettles connected in series, enter a storage tank finally, and then enter a static mixer through a mixing pump to be mixed with water, multiple washing kettles are connected in series, and qualified materials enter a crude product tank. The process is easy to operate, high in automatic control level, low in production cost, high in stability, safe to operate and suitable for large-scale industrial production, and effectively saves labor, and the purpose of continuously chlorinating and washing 3,4-dichloronitrobenzene is achieved.

Description

(1) Technical field [0001] The invention relates to the field of chemical production, in particular to a method and a device for producing 3,4-dichloronitrobenzene by continuous tank reaction. (2) Background technology [0002] 3,4-Dichloronitrobenzene is an intermediate of various dyes, pigments, medicines, pesticides and fine chemical products. The market demand is 30,000 tons per year. At present, batch reactor reaction is adopted in China. Auxiliary operations such as loading and unloading are required in the production process of batch reactor. The labor intensity is high, and it is easy to cause the loss of materials and energy. The production cost increases, the production cycle is prolonged, and the product quality is not easy to be stable. Batch kettle production is not suitable for large-scale production and cannot meet market demand. (3) Contents of the invention [0003] In order to make up for the deficiencies of the prior art, the present invention provides...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C205/12C07C201/12C07C201/16
Inventor 张玉吉席庆银张金河张文革郑钧贞张敏
Owner 山东沾化天九化工有限公司
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