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Coal-based needle coke preparation process

A process method and technology of preparation process, which are used in coke ovens, petroleum industry, coking carbon-containing materials, etc., can solve the problems of small processing capacity and unsatisfactory purification effect, and achieve the effect of low thermal expansion coefficient

Active Publication Date: 2013-05-22
SHAANXI COAL & CHEM TECH INST
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] Among the above-mentioned raw material pretreatment processes, the flash evaporation method and the sedimentation method are relatively simple in operation and low in equipment investment cost, but the purification effect cannot meet the requirements. The centrifugation method has a moderate process and a good purification effect, but the treatment capacity is small

Method used

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  • Coal-based needle coke preparation process

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Experimental program
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Effect test

Embodiment 1

[0052] The raw coal tar is heated by the 1# tubular heating furnace 2 and enters the 1# flash tower 3, the feed temperature is 400°C, the vacuum degree at the top of the tower is 10KPa, the empty tower flow velocity is 0.5m / s, and the escaping from the top of the tower is The flash oil enters the 2# flash tower, the feed temperature is 340°C, and the vacuum degree at the top of the tower is 50KPa. The refined asphalt raw material obtained is sent to the pressurized hot filter kettle 6, and the feed inlet temperature is 150°C. It is composed of diatomite and stainless steel filter. The particle size of diatomite is 50 mesh, the stainless steel filter is 500 mesh, and the thickness of the filter layer is 5 cm. Inject N 2 , pressurized to 0.5MPa, the filtrate after hot filtration enters the three-legged centrifuge 7, the filter cloth mesh number of the centrifuge is 1600 mesh, and is centrifugally filtered at a speed of 2000 rpm, and the obtained refined purified asphalt quinoline...

Embodiment 2

[0054] The raw coal tar pitch is heated by the 1# tubular heating furnace 2 and then enters the 1# flash tower 3, the feed temperature is 490°C, the vacuum degree at the top of the tower is 50KPa, the empty tower flow rate is 1m / s, and the flash tower escapes from the top of the tower Distilled oil enters the 2# flash distillation tower, the feed temperature is 400°C, and the vacuum degree at the top of the tower is 90KPa. The obtained refined asphalt raw material is sent to the pressurized hot filter kettle 6, and the feed inlet temperature is 240°C. It is made of a mixture of diatomite and expanded perlite and a stainless steel filter. Diatomite crushed to 100 mesh and expanded perlite crushed to 100 mesh is mixed at a mass ratio of 1:1. The mesh of the stainless steel filter is 700 mesh. The layer thickness is 8 centimeters, inject Ar, pressurize to 2MPa and the hot filtered filtrate enters in the three-legged centrifuge 7, and the filter cloth mesh number of the centrifuge ...

Embodiment 3

[0056] The raw material is remixed with soft asphalt and heated by 1# tubular heating furnace 2, and then enters 1# flash tower 3, the feed temperature is 450°C, the vacuum degree at the top of the tower is 90KPa, the empty tower flow rate is 2m / s, and the top of the tower escapes The flash oil enters the 2# flash tower, the feed temperature is 380°C, and the vacuum degree at the top of the tower is 130KPa. The refined asphalt raw material obtained is sent to the pressurized hot filter kettle 6, and the temperature of the feed inlet is 200°C. The layer is composed of expanded perlite and stainless steel filter mesh, the particle size of expanded perlite particles is 200 mesh, the mesh number of stainless steel filter mesh is 600 mesh, and the thickness of the filter layer is 10 cm. 2 , pressurized to 1MPa, the filtrate after hot filtration enters the three-legged centrifuge 7, the filter cloth mesh number of the centrifuge is 900 mesh, and is centrifugally filtered at a speed o...

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Abstract

The invention discloses a coal-based needle coke preparation process which comprises the following steps: 1) feeding raw materials into a No.1 tube heating furnace, heating, feeding into a No.1 flash distillation tower, performing flash distillation, feeding flash distillation oil into a No.2 flash distillation tower, and performing flash distillation to produce refined asphalt; 2) filtering the refined asphalt, injecting inert gas to perform pressurization, and performing hot filtration; 3) performing centrifugal filtration on the filtrate to obtain refined and purified asphalt, and feeding into a purified asphalt tank; 4) feeding the refined and purified asphalt into the No.1 tube heating furnace, heating, performing polycondensation through a polycondensation reaction kettle, fractionating escaping components to obtain oil gas, light oil and heavy oil, mixing the heavy oil and the refined asphalt material produced by the No.2 flash distillation tower, and feeding into the pressurization hot filtration kettle; 5) pumping the polycondensed asphalt into a No.2 tube heating furnace, heating, coking, and feeding coking oil gas and components escaping from the top of the polycondensation reaction kettle into a fractionating tower; and 6) calcining green coke in a calcining furnace to obtain the needle coke product. For the refined and purified asphalt prepared by the method, the quinoline insoluble matter content is less than 0.1%, and the thermal expansion coefficient is low, thereby ensuring that the asphalt can be used for large steel-making electric furnaces.

Description

technical field [0001] The invention belongs to a coking chemical technology, in particular to a process for preparing needle coke with coal tar, coal tar pitch, remixed soft pitch or coal tar fractions as raw materials. Background technique [0002] With the large-scale electric furnace steelmaking and the accelerated growth rate of global electric furnace steelmaking production, the use of ultra-high power electrodes (UHP) is rapidly increasing, and the requirements for carbon raw materials are also getting higher and higher. Needle coke is the aggregate for making ultra-high-power electrodes. When using ultra-high-power electrodes for electric furnace steelmaking, the smelting time can be shortened by 30% to 50%, and electricity can be saved by more than 10% to 50%. The economic benefits are very significant. Needle coke can be divided into oil-based needle coke and coal-based needle coke according to different raw materials. They are respectively made from petroleum resi...

Claims

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Application Information

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IPC IPC(8): C10B55/00
Inventor 杨阳付东升尚建选
Owner SHAANXI COAL & CHEM TECH INST
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