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Needle coke and its technology prepared by medium and low temperature coal tar refined pitch by variable temperature thermal polymerization

A technology for low-temperature coal tar and refined pitch, applied in the field of coal chemical industry, can solve problems such as the lack of research on needle coke technology, and achieve the effects of reducing thermal polycondensation reaction activity, stable growth and excellent quality

Active Publication Date: 2021-05-28
陕西榆能集团能源化工研究院有限公司 +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] At present, the process of preparing needle coke by multi-stage thermal polymerization focuses on the research of high-temperature coal tar and petroleum-based raw materials, but there are few studies on the preparation of needle coke by multi-stage thermal polymerization of medium-low temperature coal tar

Method used

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  • Needle coke and its technology prepared by medium and low temperature coal tar refined pitch by variable temperature thermal polymerization
  • Needle coke and its technology prepared by medium and low temperature coal tar refined pitch by variable temperature thermal polymerization
  • Needle coke and its technology prepared by medium and low temperature coal tar refined pitch by variable temperature thermal polymerization

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0029] Put 2.5kg of medium and low temperature coal tar in the rectification reactor, and cut the medium and low temperature coal tar under reduced pressure to obtain a softening point of 45°C and an aromaticity of f A 0.73 360-480°C fractional asphalt, take 100g of asphalt for pulverization, mix the pulverized asphalt, 300g of extractant and 8g of modifier, put it in a reaction kettle, first raise the temperature to 85°C for solvent extraction, at 100r·min -1 Stir at a constant temperature for 1 hour, after stirring, let stand at constant temperature for 4 hours, discharge macromolecular impurities from the bottom of the kettle, continue to raise the temperature to 150°C, let stand at constant temperature for 4 hours, remove insoluble matter from the bottom of the kettle, and continue to raise the temperature to separate the solvent from the top of the kettle , to obtain refined raw pitch at the bottom of the kettle; at 3°C·min -1 The heating rate is raised to 430°C, the pre...

Embodiment 2

[0032] Put 2.5kg of medium and low temperature coal tar in the rectification reactor, and cut the medium and low temperature coal tar under reduced pressure to obtain a softening point of 45°C and an aromaticity of f A 0.73 360-480°C fractional asphalt, take 100g of asphalt for pulverization, mix the pulverized asphalt, 300g of extractant and 6g of modifier, put it in a reaction kettle, first raise the temperature to 85°C for solvent extraction, at 100r·min -1 Stir at a constant temperature for 1 hour. After stirring, let stand at constant temperature for 4 hours, discharge macromolecular impurities from the bottom of the kettle, continue to raise the temperature to 145°C, let stand at constant temperature and heat for 4 hours, remove insoluble matter from the bottom of the kettle, and continue to raise the temperature to separate the solvent from the top of the kettle. , to obtain refined raw pitch at the bottom of the kettle; at 3°C·min -1 The heating rate is raised to 430°...

Embodiment 3

[0035] Put 2.5kg of medium and low temperature coal tar in the rectification reactor, and cut the medium and low temperature coal tar under reduced pressure to obtain a softening point of 47°C and an aromaticity of f A 0.75 360-480°C fractional asphalt, take 100g of asphalt for pulverization, mix the pulverized asphalt, 380g of extractant and 8g of modifier, put it in a reaction kettle, first raise the temperature to 75°C for solvent extraction, at 100r·min -1 Stir at a constant temperature for 1 hour. After stirring, let stand at constant temperature for 4 hours, discharge macromolecular impurities from the bottom of the kettle, continue to raise the temperature to 140°C, let stand at constant temperature and heat for 4 hours, remove insoluble matter from the bottom of the kettle, and continue to raise the temperature to separate the solvent from the top of the kettle. , to obtain refined raw pitch at the bottom of the kettle; at 3°C·min -1 The heating rate is raised to 440°...

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Abstract

The invention relates to a needle coke prepared by medium and low temperature coal tar refined asphalt by variable temperature thermal polymerization method and its process. The process uses medium and low temperature coal tar pitch as raw material, selects its specific coal tar fraction, and solvent refines to remove macromolecular impurities. React with heavy components and phenolic modifiers to remove highly reactive oxygen-containing compounds. During the process of variable temperature thermal polymerization of refined raw materials, the molecules first generate mesophase carbon microsphere nuclei, and then lower the temperature and add light hydrocarbons to adjust The viscosity of the system reduces the reaction activity of thermal condensation polymerization, and the secondary temperature-raising thermal polymerization increases the relative content of aromatic compounds in the mother liquor, and promotes the secondary growth of mesophase carbon microspheres. Finally, the high-temperature thermal polymerization utilizes the light oil and gas produced in the system to form a wide-area streamlined structure. . Compared with the traditional technology, the raw material asphalt in the present invention has a good thermal polymerization effect at variable temperature, and the growth process of the mesophase is stable, which is conducive to the formation of a wide-area streamlined structure under the action of coke pulling by airflow, and the preparation of high-quality needle coke.

Description

technical field [0001] The invention belongs to the technical field of coal chemical industry, and in particular relates to the preparation of needle coke, in particular to a needle coke prepared by medium-low temperature coal tar refined pitch by a variable temperature heat polymerization method and a process thereof. Background technique [0002] In the process of producing semi-coke by low-temperature dry distillation, a large amount of medium-low temperature coal tar is by-produced. With the rapid development of the coal chemical industry, its output has increased significantly. Compared with high-temperature coal tar, medium-low temperature coal tar has lower content of quinoline insolubles, higher aromatic potential, and smaller molecular weight of aromatic hydrocarbons. It is an ideal raw material for preparing needle coke. Medium and low temperature coal tar pitch mainly undergoes two chemical reactions, thermal cracking and thermal polymerization, which directly aff...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10B55/00C10B57/08
CPCC10B55/00C10B57/08
Inventor 黄晔毕亚军高生辉田亚飞高峰郝巧娥李立刘杰崔楼伟李冬
Owner 陕西榆能集团能源化工研究院有限公司