Preparation method of coal based needle coke

A technology of needle coke and coal series, applied in coking ovens, coking carbonaceous materials, petroleum industry, etc., can solve the problems of easy formation of mosaic structure, easy slagging, small coke output, etc., to avoid pipeline blockage, reaction uniform effect

Active Publication Date: 2013-05-15
SHAANXI COAL & CHEM TECH INST
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0008] Although the above-mentioned patented technology can remove the impurities in the raw material asphalt, it has the following disadvantages in practice: (1) There are too many residues left by flash evaporation, the obtained raw material has low aromaticity, low coke value, and small coke yield , the yield of needle coke is low; (2) The fraction of the flash oil is wide, and during the polycondensation process, the heavier fraction is prone to slagging, causing pipeline blockage; (3) It is easy to form a mosaic structure, resulting in poor coke pulling effect, Reduced quality of needle coke

Method used

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  • Preparation method of coal based needle coke

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preparation example Construction

[0036] The preparation method of coal series needle coke of the present invention adopts such as figure 1 The device shown in Fig. 1 shows that the preparation device of coal-based needle coke includes a stirred tank 1 and a 1# heating furnace 3 connected to the stirred tank 1 through a raw material pump 2 and a pipeline, and the 1# heating furnace 3 is respectively connected to the stirred tank 1 through a pipeline. Connected with pressurized hot filter kettle 4, purified raw material tank 6 and reaction tower 8, 1# heating furnace 3 and purified raw material tank 6 are connected through polycondensation feed pump 7 and pipeline; pressurized hot filtered kettle 4 is two identical The bottom of the two kettle bodies is connected to the centrifuge 5, and the centrifuge 5 is connected to the purified raw material tank 6; the top of the reaction tower 8 is connected to the fractionation tank 9, and the fractionation tank 9 is connected to the feed port of the stirring tank 1 to fo...

Embodiment 1

[0052] Add coal tar and diluent washing oil into the stirring tank 1 according to the mass ratio of 1:1, and after being fully mixed, it is pumped out by the raw material pump 2 and sent to the 1# tubular heating furnace 3 for heating. Autoclaved filter kettle 4, the filter material layer is made of diatomite and stainless steel filter screen, the particle size of diatomite particles is 70 mesh, the mesh number of stainless steel filter screen is 300 mesh, and the thickness of the filter layer is 5 cm. 2 , pressurized to 0.2MPa, the filtrate after hot filtration enters the three-legged centrifuge 5, the filter cloth mesh of the centrifuge is 800 mesh, and is centrifugally filtered at a speed of 1000 rpm, and the purified raw material obtained is sent by the pump 7 Enter the 1# tubular heating furnace 3, after heating, enter the reaction tower 8 for polycondensation, the circulation ratio of the polycondensation concentrate extraction and the recycled material is 1:5, the operat...

Embodiment 2

[0054] Add coal tar and diluent washing oil into the stirring tank 1 according to the mass ratio of 1:10, and after being fully mixed, it is pumped out by the raw material pump 2 and sent to the 1# tubular heating furnace 3 for heating. Autoclaved filter kettle 4, the filter material layer is composed of expanded perlite and stainless steel filter screen, the particle size of expanded perlite particles is 400 mesh, the mesh number of stainless steel filter screen is 700 mesh, and the thickness of the filter layer is 10 cm. 2 , pressurized to 2MPa, the filtrate after hot filtration enters into the three-legged centrifuge 5, the filter cloth mesh number of the centrifuge is 1300 mesh, and is centrifugally filtered at a speed of 2000 rpm, and the purified raw material obtained is sent into by the pump 7 To 1# tubular heating furnace 3, after heating, enter the reaction tower 8 for polycondensation, the cycle ratio of polycondensation concentrate extraction and recycled material is...

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Abstract

The invention discloses a preparation method of coal based needle coke, which comprises the following steps of: 1) adding a raw material and a diluent into a stirring kettle, stirring and separating out the solvent insoluble matter; 2) heating the mixed liquid in a 1# tubular heating furnace, and feeding the mixed liquid into a pressing hot filtration kettle; 3) filtering, filling an inert gas, pressing and performing hot filtration; 4) performing centrifugal filtration of the filtrate, and feeding the obtained purified raw material into a purified raw material tank; 5) heating the purified raw material in the 1# tubular heating furnace and performing reaction tower circular condensation polymerization, fractionating the escape component to obtain gas, light oil and heavy oil, and recycling the light oil; 6) heating the condensation polymerization concentrate in a 2# tubular heating furnace, coking by a coke tower to obtain coke, and feeding the coke oil gas into a reaction tower; and 7) feeding the prepared green coke into a calcinator, heating and calcining to obtain the product needle coke. The content of quinoline insoluble (QI) in the prepared refined purified asphalt is less than 0.15%, the yield is improved by 10-20%, the coefficient of thermal expansion of the needle coke is low, the pipeline blockage can be avoided, and the material reaction is uniform.

Description

technical field [0001] The invention belongs to a method for preparing needle coke, in particular to a method for preparing coal series needle coke. Background technique [0002] Needle coke is a high-quality variety vigorously developed among carbon materials. Its appearance is a silver-gray porous solid with metallic luster. Its structure has obvious fibrous or needle-like texture. have a larger aspect ratio. Needle coke is a high-quality material for manufacturing high-power and ultra-high-power graphite electrodes. Graphite electrodes made of needle coke have low resistivity, small thermal expansion coefficient, strong thermal shock resistance, high mechanical strength, and strong oxidation resistance. It has the advantages of low electrode consumption and large allowable current density. [0003] According to different raw materials, needle coke is divided into two types: oil-based and coal-based. At present, the countries that produce oil-based needle coke in the wo...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10B55/00C10B57/04C10B57/08
Inventor 杨阳付东升尚建选
Owner SHAANXI COAL & CHEM TECH INST
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