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Separation method for phenol compounds and nitrogen-containing compounds in coal tar

A technology of phenolic compounds and nitrogen compounds, applied in tar processing through heat treatment, tar processing through chemical extraction, tar processing through selective solvent extraction, etc., can solve the problem of consuming large acid-base solution, increasing hydrogen consumption, and polluting the environment Pollution and other issues, to achieve the effect of low equipment investment and operating costs, reduced production costs, and simple process flow

Active Publication Date: 2015-07-01
WUHUAN ENG
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although the sodium hydroxide solution elution method has high selectivity, it needs to consume a large amount of acid-base solution and has high requirements for equipment anti-corrosion.
More importantly, after pickling, a large amount of phenol-containing wastewater is produced, which leads to serious pollution of the subsequent sewage treatment equipment and environmental pollution.
[0004] So far, the research of the researchers has mainly focused on how to use a separating agent to extract the phenols in the simulated oil in a laboratory stage without pollution. However, for coal tar, its composition is extremely complex, not only containing phenolic compounds, but also Contains nitrogen-containing compounds that affect the subsequent hydrogenation process. In the reports so far, no matter whether the traditional alkali washing method or the separation agent separation method is used, only the separation of phenolic compounds is considered, and the separation of phenolic compounds is not considered. Nitrogen compounds, and there is no useful report to point out how to separate nitrogen-containing compounds in coal tar
The existence of nitrogen-containing compounds in coal tar has the following hazards: 1. Hydrogenation of nitrogen-containing compounds will generate ammonia, which will increase hydrogen consumption; 2. The ammonia generated by hydrogenation of nitrogen-containing compounds will easily poison the hydrogenation catalyst; 3. Not involved in hydrogenation The nitrogen-containing compounds reacted by hydrogen will affect the quality of oil products. Therefore, when separating coal tar, it is hoped that both the removal of phenols and the removal of nitrogen-containing compounds can be achieved while overcoming the influence of other complex components in coal tar. to solve the above technical problems

Method used

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  • Separation method for phenol compounds and nitrogen-containing compounds in coal tar
  • Separation method for phenol compounds and nitrogen-containing compounds in coal tar

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0028] The process conditions described in this example are: at 10°C, complexing and separating agent A is added to coal tar (coal tar comes from Wuhan Iron and Steel Coking Plant, distillation range: 170-230°C), the mass ratio of the two is 1:10, After stirring for 50 minutes, it was allowed to stand still for 8 minutes, and the phenolic content and nitrogen content of the separated coal tar were measured. The separation efficiency of phenolic compounds was 81.2%, and the separation efficiency of nitrogenous compounds was 71.1%. The obtained complex was heated at 200° C. for 1 h to selectively separate nitrogen-containing compounds. According to elemental analysis, the separation efficiency of nitrogen-containing compounds was 82.7%.

[0029] Add 300g of organic solvent B to the complex after the nitrogen-containing compound is separated, stir at 40°C for 20 minutes, then let it stand for 10 minutes, and recover the complexing and separating agent A through a bag filter. Afte...

Embodiment 2

[0032] The process conditions described in this example are: at 60°C, add complexing and separating agent A to coal tar (coal tar comes from Wuhan Iron and Steel Coking Plant, distillation range: 170-230°C), the mass ratio of the two is 1:10, After stirring for 20 minutes, it was allowed to stand still for 8 minutes, and the phenol content and nitrogen content of the separated coal tar were measured. The separation efficiency of phenolic compounds was 79.7%, and the separation efficiency of nitrogen compounds was 70.4%. The obtained complex was heated at 140° C. for 0.2 h to selectively separate nitrogen-containing compounds. According to elemental analysis, the separation efficiency of nitrogen-containing compounds was 81.4%.

[0033] Add 300g of organic solvent B to the complex after the nitrogen-containing compound is separated, stir at 60°C for 1 min, then let it stand for 10 min, and recover the complexing and separating agent A through a bag filter. After the above proce...

Embodiment 3

[0035] The process conditions described in this example are: at 40°C, complexing and separating agent A is added to coal tar (coal tar comes from Wuhan Iron and Steel Coking Plant, distillation range: 170-230°C), the mass ratio of the two is 0.8:10, After stirring for 8 minutes, it was left standing for 8 minutes to measure the phenolic content and nitrogen content of the separated coal tar. The separation efficiency of phenolic compounds was 68.6%, and the separation efficiency of nitrogenous compounds was 64.4%. The obtained complex was heated at 110° C. for 1 h to selectively separate nitrogen-containing compounds. According to elemental analysis, the separation efficiency of nitrogen-containing compounds was 57.4%.

[0036] Add 300g of organic solvent B to the complex after the nitrogen-containing compound is separated, stir at 10°C for 30 minutes, then let it stand for 10 minutes, and recover the complexing and separating agent A through a bag filter. After the above proc...

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Abstract

The present invention discloses a separation method for phenol compounds and nitrogen-containing compounds in coal tar, wherein the problem that the coal tar is generally subjected to phenol compound separation is solved. The technical scheme comprises: adding a complexation separation agent to coal tar to carry out a complexation reaction, and then adopting an evaporation and back extraction manner to rapidly separate the nitrogen-containing compounds, the phenol compounds, the renewable separation agent and the solvent. The separation method has characteristics of simple process, environmental protection, no phenol-containing wastewater production, achievement of rapid and synchronous removal of phenol compounds and nitrogen-containing compounds, and good removal effect.

Description

technical field [0001] The invention relates to the separation field of coal chemical industry and petrochemical industry, in particular to a method for separating phenols and nitrogen-containing compounds in coal tar. Background technique [0002] The phenolic compounds and nitrogen-containing compounds in coal tar contain high-energy C-O and C-N bonds, which are difficult to hydrogenate, and the hydrogenation of phenols will generate water. Their existence in coal tar is not conducive to the hydrogenation of coal tar. quality. [0003] At present, the industry usually uses sodium hydroxide solution to separate the phenolic compounds in coal tar. The phenolic compounds are weakly acidic and react with a strong base to form a water-soluble phenolic sodium salt solution. The phenolic sodium salt uses carbon dioxide Or acidify with sulfuric acid solution to reduce phenols. Although the sodium hydroxide solution elution method has high selectivity, it needs to consume a large...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10C1/20C10C1/19C10C1/18
Inventor 庞昆李繁荣朱阳明夏吴徐建民陈风敬卢文新
Owner WUHUAN ENG
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