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Method for preparing general grade carbon fiber by using coal liquefaction residues

A technology of coal liquefaction residue and carbon fiber, which is applied to the chemical characteristics of fibers, textiles and papermaking, etc., can solve the problems of strong corrosion, high operating cost, and many operating steps, and achieve improved strength performance, simple preparation method, and low operating cost Effect

Active Publication Date: 2022-03-22
CHINA UNIV OF MINING & TECH (BEIJING)
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AI Technical Summary

Problems solved by technology

The document "Preparation of general-purpose pitch-based carbon fiber from catalytic oil slurry [D]. Beijing: Beijing Institute of Petrochemical Technology, 2015. Li Peipei." discloses that the catalytic oil slurry is used as raw material, the raw material is pretreated by heat treatment, and the precursor is prepared by extraction method Pitch is used for spinning to make carbon fiber. This method has many preparation steps and the process is cumbersome, and it is difficult to be used in continuous actual industrial production.
The document "Kim B J, Eom Y, Kato O, et al. Preparation of carbon fibers with excellent mechanical properties from isotropic pitches [J]. Carbon, 2014, 77: 747-755." is based on naphtha cracked oil as raw material, using Isotropic pitch with good spinnability was synthesized by bromination-debromination method, and isotropic pitch-based carbon fiber with a tensile strength of 1500 MPa was prepared by spinning, but the elemental bromine used in this method was expensive and corrosive strong, has a certain degree of danger and has high requirements for the anti-corrosion performance of the equipment
[0004] The Chinese invention patent with the application number 202010468692.8 "A method for preparing general-purpose pitch-based carbon fibers from coal liquefaction residues" reports a method for preparing general-purpose carbon fibers from coal liquefaction residues. Suction filtration and oxidative polycondensation to obtain a pitch precursor with a softening point of 240-340°C, and then prepare carbon fibers through melt spinning, non-melting treatment, and carbonization processes. The preparation process of this technology is cumbersome and there are many operating steps
The Chinese invention patent "Preparation method of pitch carbon fiber" with application number CN200910019693.8 reports a preparation method of pitch carbon fiber composed of polycondensation, spinning, non-melting, carbonization, high-temperature graphitization, surface modification and other processes. This technology uses the polycondensation method to prepare spinning pitch, and a large amount of synthetic agents are added in the polycondensation process, the operation cost is high, and the mixing of organic matter is potentially dangerous
[0005] It can be seen from this that the current preparation method of pitch-based carbon fiber is mainly the thermal condensation polymerization method, which is not effective in regulating the properties and performance of carbon fiber, resulting in that the strength and performance of carbon fiber made from coal liquefaction residue are still relatively large. Room for improvement

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0042] (1) Pretreatment: After grinding the tetrahydrofuran extract of coal liquefaction residue, mix it with benzyl chloride at a mass ratio of 1:0.1 and add it to the precursor preparation reaction kettle, and pass argon gas at a rate of 50ml / min to achieve an inert atmosphere Under protective conditions, ventilate and purge for 10 minutes.

[0043] (2) Chlorination reaction: In an inert atmosphere, raise the temperature of the reaction kettle to 180°C, and after the sample is completely melted and has good fluidity, turn on the motor to start the stirring paddle, and maintain a stirring speed of 50rpm. Then continue to heat up to 260°C and keep the temperature constant for 1h to carry out the chlorination reaction.

[0044] (3) Dechlorination reaction: raise the temperature of the reactor to 370° C., keep the temperature constant for 1.5 hours, and carry out the dechlorination reaction. Increase the purge flow rate of the inert gas argon to 200ml / min. During this period, ...

Embodiment 2

[0052] (1) Pretreatment: Grind the tetrahydrofuran extract of coal liquefaction residue, mix it with benzyl chloride at a mass ratio of 1:0.2 and add it to the precursor preparation reaction kettle, and pass argon gas at a rate of 50ml / min to achieve an inert atmosphere Under protective conditions, ventilate and purge for 10 minutes.

[0053] (2) Chlorination reaction: In an inert atmosphere, raise the temperature of the reaction kettle to 180°C, and after the sample is completely melted and has good fluidity, turn on the motor to start the stirring paddle, and maintain a stirring speed of 50rpm. Then continue to heat up to 260°C and keep the temperature constant for 1h to carry out the chlorination reaction.

[0054] (3) Dechlorination reaction: raise the temperature of the reactor to 370° C., keep the temperature constant for 1.5 hours, and carry out the dechlorination reaction. Increase the purge flow rate of the inert gas argon to 200ml / min. During this period, a stirrin...

Embodiment 3

[0062] (1) Pretreatment: Grind the tetrahydrofuran extract of coal liquefaction residue, mix it with benzyl chloride at a mass ratio of 1:0.3 and add it to the precursor preparation reaction kettle, and pass argon gas at a rate of 50ml / min to achieve an inert atmosphere Under protective conditions, ventilate and purge for 10 minutes.

[0063] (2) Chlorination reaction: In an inert atmosphere, raise the temperature of the reaction kettle to 180°C, and after the sample is completely melted and has good fluidity, turn on the motor to start the stirring paddle, and maintain a stirring speed of 50rpm. Then continue to heat up to 260°C and keep the temperature constant for 1h to carry out the chlorination reaction.

[0064] (3) Dechlorination reaction: raise the temperature of the reactor to 370° C., keep the temperature constant for 1.5 hours, and carry out the dechlorination reaction. Increase the purge flow rate of the inert gas argon to 200ml / min. During this period, a stirrin...

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PUM

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Abstract

The invention discloses a method for preparing general grade carbon fibers by using coal liquefaction residues, and relates to the technical field of preparation of general grade pitch-based carbon fibers. The preparation method comprises the following steps: mixing and purifying coal liquefaction residues and tetrahydrofuran, mixing an obtained coal liquefaction residue extract and a chlorinating agent in an inert atmosphere, heating and melting, chlorinating at a constant temperature of 120-260 DEG C, dechlorinating at a constant temperature of 320-370 DEG C, and cooling to room temperature after the reaction is completed to obtain an asphalt precursor; adjusting the softening point of the asphalt precursor to 220-260 DEG C, carrying out melt spinning to obtain asphalt fibers, and then carrying out pre-oxidation and carbonization treatment on the asphalt fibers to obtain the carbon fibers. The coal liquefaction residues are used as the raw material, the asphalt precursor is synthesized through a chlorination-dechlorination method, the preparation method is simple, the operation cost is low, no strong-corrosion raw material is adopted, and the strength performance of the prepared general-grade carbon fiber is remarkably superior to that of existing commercially available general-grade carbon fiber.

Description

technical field [0001] The invention relates to the technical field of preparation of general-purpose pitch-based carbon fibers, in particular to a method for preparing general-purpose carbon fibers from coal liquefaction residue. Background technique [0002] Coal direct liquefaction technology is a kind of clean coal technology, which can alleviate the current energy situation of lack of petroleum resources to a certain extent. A large amount of coal liquefaction residue will be produced in the process of direct coal liquefaction, accounting for about 30% of the total coal input. Coal liquefaction residue has high carbon content and high content of aromatic components, but high ash and sulfur limit the high value-added utilization of coal liquefaction residue. The efficient, reasonable and high value-added utilization of coal liquefaction residue is of great significance to the development and application of direct coal liquefaction technology. [0003] The preparation o...

Claims

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Application Information

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IPC IPC(8): D01F9/15
CPCD01F9/15
Inventor 刘金昌申辰阳李亚平刘琴王桐安小雅解强梁鼎成
Owner CHINA UNIV OF MINING & TECH (BEIJING)
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