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Process method for preparing needle coke through kettle type charring

A process method and needle coke technology, which can be used in the coking of carbonaceous materials, coke ovens, petroleum industry, etc., and can solve problems such as bumping, unfavorable coking conditions, and solidification.

Active Publication Date: 2014-04-16
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This method requires that the material be heated from room temperature to 480-550°C within 2-30 seconds, which is difficult to realize industrially. In addition, this rapid heating method is also likely to cause internal bumping and solidification of the system during the industrial scale-up process, which is not conducive to Creates smooth, soft coke conditions to produce porous coke
[0005] None of the above methods paid attention to the two key factors of the full growth of the mesophase and the subsequent tensile deformation at the same time, so needle coke with excellent performance and well-developed needle-like streamline texture could not be produced.

Method used

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  • Process method for preparing needle coke through kettle type charring
  • Process method for preparing needle coke through kettle type charring

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0027] Before producing needle coke, the raw material of catalytic cracking oil slurry is subjected to the following experimental process to determine the total exhaust volume: put the catalytic oil slurry into the coking reactor after filtration or sedimentation treatment, and start to heat up at a pressure of 1.5MPa , (1) In the first stage, the raw materials are sent to the kettle-type coking reactor, and the temperature is raised to 400 °C; in the second stage, the temperature is raised from the end temperature of the first stage, and the reaction temperature is 20 h according to the exhaust volume of the reaction system -1 Control, the temperature rises to 460°C; the third stage is kept at 460°C for 10 hours; the fourth stage is heated from 460°C at 10°C / h to 500°C; the fifth stage is heated from 500°C at 20°C / h to 520°C , burn at constant temperature for 2 hours. The total exhaust volume of the above-mentioned process is measured as the total exhaust volume of the needle...

Embodiment 2

[0037] Before the production of needle coke, the coal tar with quinoline insolubles removed from the harmful components is carried out in the following experiment to determine the total exhaust volume: the coal tar with quinoline insolubles removed from the harmful components is put into the coking reactor, and the pressure is The temperature starts to rise under the condition of 2.0MPa. (1) In the first stage, the raw materials are sent to the kettle-type coking reactor, and the temperature is raised to 420°C; (2) The second stage starts to heat up from the end temperature of the first stage, and the reaction temperature is The exhaust volume of the reaction system is 25 h -1 Control, the temperature rises to 440°C; (3) The third stage is 440 constant temperature stage, the constant temperature time is 10 hours; (4) The fourth stage is completed from 440°C at 5°C / h to 510°C; the fifth stage is from 510°C Raise the temperature to 540°C at 10°C / h, and burn at a constant tempera...

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Abstract

The invention discloses a process method for preparing needle coke through kettle type charring. The method comprises the following steps: (1) at a first stage, conveying raw materials to a kettle type charring reactor, and heating to a temperature of 380-420 DEG C; (2) at a second stage, heating to a temperature of 430-480 DEG C from the end point temperature of the first stage, and controlling the reaction temperature according to a reaction system air exhaust amount of 10-30 h<-1>; (3) completing constant temperature maintaining when the exhausted air amount is 50-90% of the total air exhaust amount, wherein a third stage is a constant temperature stage; (4) at the fourth stage, heating to a temperature of 490-510 DEG C from the end point temperature of the third stage; and (5) at the fifth stage, heating to a charring temperature from the end point temperature of the fourth stage, and carrying out constant temperature maintaining for 1-5 h to complete the charring, wherein the generated needle coke is deposited on the bottom of the tower. With the temperature control method, it can be ensured that small spheres in the system can be subjected to complete growth and fusion at the right time to obtain the needle coke having a high fiber needle structure.

Description

technical field [0001] The invention relates to a process for preparing needle coke, in particular to a process for preparing needle coke by still coking. Background technique [0002] The world produces more than one billion tons of steel every year to meet the needs of social development. The increase in steel scrap resources, the application of direct reduced iron technology, the increase in demand for special steel, and the requirements for energy conservation and emission reduction all make the share of electric furnace steel production maintain a momentum of continuous growth. The operating conditions of electric arc furnaces are very harsh, and high-performance graphite electrodes are required to operate safely and reduce the manufacturing cost of electric furnace steel. Needle coke is not only used for ultra-high power graphite electrodes, but also used as raw materials for thermal structure graphite and special carbon products. American Great Lakes Company first i...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10B55/00
Inventor 初人庆蒋立敬杜正军矫德卫张学萍勾连忠
Owner CHINA PETROLEUM & CHEM CORP