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Dye continuous diazotization process

A technology of diazotization and dyes, which is applied in the direction of azo dyes, organic dyes, monoazo dyes, etc., can solve the problems of high cost in environmental protection, impossibility of cooling down very stably, and instability of adding liquid raw materials, etc., to achieve the best results Good, reduce the cost of environmental protection treatment, reduce the effect of emissions

Active Publication Date: 2016-03-02
ZHEJIANG RUNTU INST
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  • Abstract
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  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] A common problem in these patents is that a large amount of sulfuric acid is used to dissolve aromatic amine raw materials, so that a large amount of low-concentration inorganic acids will be produced in subsequent production, and the cost of environmental protection is relatively high; The change is more sensitive, and often need to use a lot of cooling facilities, such as adding coils in the reaction pot and cooling the outer jacket of the pot at the same time to control the reaction efficiency. , so the effect is still not ideal

Method used

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  • Dye continuous diazotization process
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  • Dye continuous diazotization process

Examples

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Embodiment 1

[0043] A 2-stage series continuous diazo loop reactor is adopted, with a single tank volume of 2000L, an external cooling jacket, and an external heat exchanger with a heat exchange area of ​​10M 2 ; 2-level parallel central control reaction pot; aromatic amines are 2,4-dinitro-6-bromoaniline, and the concentration of nitrosyl sulfuric acid solution (w / w) is 40%; the reaction residence time of the loop reactor is 3h.

[0044]Add the finished diazonium salt into the mixing pot, then put in powdered 2,4-dinitro-6-bromoaniline, and control the temperature at 15-25°C; control the diazonium salt: aromatic amine: nitrosyl sulfuric acid into The molar ratio of material is 2:1:1.02, and it is determined that the mixed feed rate in the primary loop reactor is 358.5kg / h (being diazonium salt 293kg / h, 2,4-dinitro-6-bromoaniline 65.5kg / h), the feed rate of nitrosyl sulfuric acid in the primary loop reactor is 48.6kg / h, and the control is realized through the combination of flow meter, re...

Embodiment 2

[0048] A 2-stage series continuous diazo loop reactor is adopted, with a volume of 3000L for a single tank, a cooling jacket outside, and a heat exchange area of ​​25M for the external heat exchanger. 2 ; 2-level parallel central control reaction pot; aromatic amines are 2,4-dinitro-6-bromoaniline, and the concentration of nitrosyl sulfuric acid solution (w / w) is 40%; the reaction residence time of the loop reactor is 3h.

[0049] Add the finished diazonium salt into the mixing pot, then put in powdered 2,4-dinitro-6-bromoaniline, and control the temperature at 15-25°C; control the diazonium salt: aromatic amine: nitrosyl sulfuric acid into The molar ratio of material is 2:1:1.02, and it is determined that the mixed feed rate in the primary loop reactor is 538kg / h (being diazonium salt 439kg / h, 2,4-dinitro-6-bromoaniline 99kg / h), the feed rate of nitrosylsulfuric acid in the primary loop reactor is 72kg / h, and the control is realized through the combination of flowmeter, reg...

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Abstract

The invention discloses a dye continuous diazotization process. The process comprises the following steps: (1) adding a diazonium liquid as a bottom liquid to a mixing pot, then adding aromatic amine to conduct mixing dispersion to obtain a mixture; (2) respectively and continuously inputting the mixture and nitrosyl sulfuric acid into multiple stages of series loop reactors for a diazotization reaction to obtain a reaction liquid; inputting the mixture from the inlet of a first stage of loop reactor, inputting nitrosyl sulfuric acid from the inlet of each stage of loop reactor, and outputting the reaction liquid from the outlet of a final stage of a loop reactor; and (3) detecting the reaction liquid in a center control detection reaction pot; if the diazotization reaction is complete, sending the reaction liquid directly into a diazonium liquid product groove; and if the diazotization reaction is not complete, continuing the reaction in a center control reaction reactor. The diazotization process employs an outer circulation heat exchanger to achieve effective temperature control effect, improve the stability, uniformity and controllability of diazotization reaction, and improve the quality of dye products.

Description

technical field [0001] The invention belongs to the field of dye synthesis, and in particular relates to a continuous diazotization process of dyes. Background technique [0002] In the diazotization reaction of dye synthesis, under normal circumstances, aromatic amine raw materials are reacted with sodium nitrite in the presence of inorganic acids, and the product diazonium salt produced by the reaction is an important intermediate for azo compounds. This diazotization reaction is widely used in organic synthesis processes such as medicines, pesticides, and dyes, especially in the dye industry, where more than 60% of dyes are produced through diazotization reactions. [0003] At present, the diazonium salt synthesis methods adopted by dyestuff enterprises are basically batch processes, which are mainly cis-feeding method and reverse-feeding method, cis-feeding method such as sodium nitrite added dropwise to the inorganic acid Diazotization is carried out in solution or sus...

Claims

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Application Information

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IPC IPC(8): C07C245/20C09B29/01C09B29/085
CPCC07C245/20C09B29/0003C09B29/0838
Inventor 叶华明高立江陈伟东
Owner ZHEJIANG RUNTU INST
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