Method and device for preparing high-purity pyridine series products from crude pyridine by refining

A series of products, pyridine technology, applied in the field of coal chemical industry, can solve the problems that the production process cannot be carried out smoothly, trace moisture cannot be removed, plugging packing and reboiler, etc., so as to reduce equipment investment and process energy consumption, reduce investment and Effect of energy consumption, simplification of processes and equipment

Active Publication Date: 2019-06-21
CHINA CONSTR IND & ENERGY ENG GRP CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0003] Current research mainly focuses on the simple separation of phenolic compounds or the simultaneous separation of phenolic compounds and pyridine compounds. For example, the domestic patent CN102731264 discloses a continuous distillation to obtain two high-purity phenolic products and one high-content mixed phenolic product. A method for separating crude phenols from medium and low temperature coal tar, and CN107721826 further discloses a method and device for separating various phenols from crude phenols from medium and low temperature coal tar. The crude phenol products are mainly obtained through a pretreatment system, and the crude phenol products are then processed through continuous Four kinds of high-purity phenol series products are obtained by the rectification system; and the domestic patent CN104893750 discloses a method for extracting pyridine compounds from coal tar. Phenolic compounds and dephenolized oil, and then use solvent extraction to extract all the crude pyridine compounds in the phenolic compounds and dephenolized oil, and finally obtain pyridine compounds through dehydration, slag removal and rectification; although there are many studies, but There is no specific method on how to refine high-purity pyridine series products from pyridine compounds. Therefore, it is of great significance to separate and refine high-purity pyridine series products from medium and low temperature coal tar crude pyridine
[0004] The existing process of producing pyridine from coal tar has the disadvantage of not being able to remove trace moisture, but the existence of trace moisture will greatly affect product quality
In addition, coal tar crude pyridine raw materials generally contain residues with a mass percentage of about 3%. In addition to high boiling point components (boiling point more than 225 ° C), it also contains Na2SO4, Na2CO3 and other inorganic salts. If it is not removed first, it will be directly used If the continuous tower is used, the packing and reboiler will inevitably be blocked, and the production process cannot be carried out smoothly.

Method used

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  • Method and device for preparing high-purity pyridine series products from crude pyridine by refining
  • Method and device for preparing high-purity pyridine series products from crude pyridine by refining

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Embodiment 1

[0031] Embodiment 1: a kind of method for crude pyridine refining high-purity pyridine series products, comprises the following steps:

[0032] S1. Mix the crude pyridine raw material from medium and low temperature coal tar with part of the entrainer, and use low-pressure steam or other low-temperature heat sources to enter the drying tower T101 after being preheated by the feed preheater 1 of the drying tower T101; in this embodiment, the crude The flow rate of pyridine raw material is 8421kg / h, the pressure is 0.4MPa and the temperature is 40℃, its mass composition is water 6.5%, benzene 15.0%, pyridine 40.5%, o-picoline 3.7%, 2,6-lutidine 3.5% %, m-picoline 7%, o-ethylpyridine 0.3%, 2,4-lutidine 7%, 2,3,6-collidine 6%, indane 0.1%, aniline 5.8%, benzyl Amine 2.4%, m-methylaniline 2% and quinoline 0.2%.

[0033] S2. Using azeotropic distillation technology, azeotropic distillation is carried out through the drying tower T101. The gas phase at the top of the drying tower T1...

Embodiment 2

[0043] Embodiment 2: In this embodiment, the crude pyridine raw material flow rate is 8421kg / h, the pressure is 0.4MPa and the temperature is 40°C, and its mass composition is water 8%, benzene 10.0%, pyridine 46%, o-picoline 3 %, 2,6-lutidine 3.2%, m-picoline 5%, o-ethylpyridine 0.3%, 2,4-lutidine 8%, 2,3,6-collidine 6% , indane 0.1%, aniline 5.8%, benzylamine 2.4%, m-methylaniline 2% and quinoline 0.2%; other technological process is identical with embodiment 1, and pyridine tower T104 tower top obtains 3874kg / h purity and is 99.5wt% Pyridine product, pyridine tower T104 tower kettle obtains 232kg / h purity is the o-picoline product of 99.8wt%; The picoline tower T105 obtains 711kg / h content exceeds 96.5wt% picoline product mixture material, dimethyl Pyridine tower T106 was refined to obtain 671kg / h of 2,4-lutidine product with a purity of 99.8wt%, and 498kg / h of 2,3,6-trimethylpyridine with a purity of 98.3wt% was extracted from the top of colloidal tower T107 A picoline pr...

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Abstract

The invention discloses a method for preparing high-purity pyridine series products from crude pyridine by refining. The method comprises following steps: (1), drying: a crude pyridine raw material and an entrainer are mixed and preheated to enter a drying tower for azeotropic distillation, water phase and the entrainer are obtained at the top of the drying tower, the entrainer is recycled or extracted for standby application, and a crude pyridine material is obtained at the bottom of the drying tower; (2), heavy component removal: the crude pyridine material obtained in step (1) enters an evaporation kettle and is subjected to the heavy component removal treatment, part of gas phase at the top of the evaporation kettle returns to the drying tower, and the other part enters a pre-fractionation tower and is subjected to light and heavy material fractionation; (3), distillation of the pyridine series products. The pyridine series products with high added value are separated out with adoption of azeotropic distillation, atmospheric and vacuum distillation and heat integration technologies, purity of pyridine, o-methylpyridine, methylpyridine, dimethyl pyridine and trimethyl pyridine reaches 96wt% or higher, and one energy-saving and high-efficiency technical method for preparing the high-purity pyridine series products from crude pyridine by refining is obtained.

Description

technical field [0001] The invention belongs to the technical field of coal chemical industry, and in particular relates to a method and a device for refining high-purity pyridine series products from crude pyridine. Background technique [0002] Coal tar is a very valuable chemical raw material, and medium and low temperature coal tar contains a certain amount of crude pyridine and crude phenolic raw materials, such as pyridine, o-picoline, lutidine, collidine and other crude pyridine compounds and Crude phenolic compounds such as phenol, o-cresol, m-cresol, p-cresol, xylenol, ethylphenol, tricresol, etc. Although the content of these compounds is not very high, they are all high value-added fine chemical products, and synthetic Such substances need to pay higher environmental costs or economic costs. [0003] Current research mainly focuses on the simple separation of phenolic compounds or the simultaneous separation of phenolic compounds and pyridine compounds. For examp...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07D213/16
CPCY02P20/10
Inventor 王佳兵杨万典刘勇军岳昌海陶荣秦凤祥倪明周俊超
Owner CHINA CONSTR IND & ENERGY ENG GRP CO LTD
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