Production method and system of coal-series needle coke

A production method and production system technology, which are applied in coke ovens, coking carbonaceous materials, petroleum industry, etc., can solve the problems of increased solvent loss, difficult operation, and difficulty in precise control of industrial devices, and achieve small solvent loss and clear interface. Effect

Active Publication Date: 2011-05-11
BAOWU CHARCOAL MATERIAL TECH CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] The method disclosed in the patent application with publication number CN1793287A is a solvent sedimentation method, using a stirred tank as a mixing and QI sedimentation equipment for raw materials and solvents, which causes the following problems: 1. The unclear interface between light and heavy two phases causes high QI content of purified asphalt ;2. In order to realize industrialized continuous operation, multiple stirred tanks must be switched and used. In this way, the investment in equipment is relatively large; When it is impossible to completely pump it out, it will cause the loss of the light phase to reduce the product yield, and the solvent loss will increase at the same time
The main disadvantages of this method are: 1. The yield of purified products is low, so the yield of needle coke is low; 2. The process is long, difficult to operate, and difficult to industrialize; 3. The product quality is poor
[0009] The main disadvantages of the carbonization process of the invention patent CN1793286 are 1. The heating procedure of carbonized raw materials is complicated, and it is difficult to implement precise control in industrial equipment. Difference
The disadvantage of this invention is that due to the carbonization of the raw material, temperature changes have to be used during carbonization, which makes the operation complicated and the equipment suffers a large thermal shock

Method used

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  • Production method and system of coal-series needle coke

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Experimental program
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Embodiment 1

[0074] In this embodiment, coal tar pitch and solvent are mixed to obtain a mixture of coal tar pitch and solvent, wherein the mass flow ratio of coal tar pitch and solvent is 1:0.8. The temperature of the settling tank was 120°C. The residence time of the mixture of coal tar pitch and solvent in the settling tank was 15 hours. The mass flow ratio of continuously discharging the light phase from the light phase outlet of the settling tank to continuously discharging the heavy phase from the heavy phase outlet of the settling tank is 5:2. The operating pressure of the combined tower is 180KPa, and the bottom temperature of the combined tower is 320°C. The outlet temperature of the heating furnace is 470° C., and the ratio of the steam injection amount of the heating furnace to the feeding amount of the heating furnace is 0.03:1. The operating pressure of the carbonization tower is 300KPa, the reaction time in the carbonization tower is 8 hours, and the reaction temperature is...

Embodiment 2

[0079] In this embodiment, coal tar pitch and solvent are mixed to obtain a mixture of coal tar pitch and solvent, wherein the mass flow ratio of coal tar pitch and solvent is 1:1.5. The temperature of the settling tank was 95°C. The residence time of the mixture of coal tar pitch and solvent in the settling tank was 6 hours. The mass flow ratio of continuously discharging the light phase from the light phase outlet of the settling tank to continuously discharging the heavy phase from the heavy phase outlet of the settling tank is 10:2. The operating pressure of the combined tower is 250KPa. The temperature at the bottom of the combined tower is 380°C. The outlet temperature of the heating furnace is 480°C, and the ratio of the steam injection amount of the heating furnace to the feeding amount of the heating furnace is 0.06:1. The operating pressure of the carbonization tower is 350Kpa, the reaction time in the carbonization tower is 4 hours, and the reaction temperature i...

Embodiment 3

[0084] In this embodiment, coal tar pitch and solvent are mixed to obtain a mixture of coal tar pitch and solvent, wherein the mass flow ratio of coal tar pitch and solvent is 1:1.2. The temperature of the settling tank was 60°C. The residence time of the mixture of coal tar pitch and solvent in the settling tank was 1 hour. The mass flow ratio of continuously discharging the light phase from the light phase outlet of the settling tank to continuously discharging the heavy phase from the heavy phase outlet of the settling tank is 5:2. The operating pressure of the combined tower is 100KPa. The temperature at the bottom of the combined tower is 300°C. The outlet temperature of the heating furnace is 440°C, and the ratio of the steam injection amount of the heating furnace to the feeding amount of the heating furnace is 0.02:1. The operating pressure of the carbonization tower is 200KPa, the reaction time in the carbonization tower is 24 hours, and the reaction temperature is...

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Abstract

The invention relates to a production method of needle coke, in particular to a production method of coal-series needle coke and a method for producing the coal-series needle coke by obtaining purified asphalt from which quinoline insoluble (QI) is removed by a solvent treatment method and carbonizing the purified asphalt. The invention also relates to a system for implementing the production method of the coal-series needle coke. In the production method of the coal-series needle coke, a settling tank is taken as settling equipment; the mixture of coal tar asphalt and a solvent is continuously introduced into the inlet of the settling tank; and a settled light phase and a settled heavy phase are continuously discharged out of the settling equipment respectively. In the production system of the coal-series needle coke, a settling tank is taken as settling equipment. Technical problems such as an unclear interface between the light phase and the heavy phase, realization of continuous production by using a plurality of stirring kettles alternatively, light phase loss during intermittent operation and large solvent loss caused by solvent settling by using the stirring kettles in the prior art are solved.

Description

technical field [0001] The present invention relates to a production method of needle coke, in particular to a production method of coal-based needle coke, in particular to obtaining purified pitch after removal of quinoline insolubles (QI) through a solvent treatment method, and carbonizing the purified pitch to produce coal The needle coke method. The invention also relates to a system for realizing the production method of the coal-based needle coke. Background technique [0002] Needle coke is a high-quality carbon species vigorously developed in carbon materials in the 1970s, and it is also one of the most important carbon species. Needle coke is more suitable for electrodes due to its lower electrical resistance and thermal expansion coefficient. Graphite electrodes are divided into ordinary electrodes, high power electrodes (HP) and ultra high power electrodes (UHP). Needle coke is mainly used to produce high-power and ultra-high-power graphite electrodes for elect...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10B55/02
Inventor 邹先忠许祥军张秀云吴承性单长春刘春法李乃民周金水李淳刘正华
Owner BAOWU CHARCOAL MATERIAL TECH CO LTD
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