Continuous sedimentation process for production of needle coke
A needle coke and process technology, which is applied in the processing of tar pitch/petroleum pitch/natural pitch, processing tar pitch/petroleum pitch/natural pitch by distillation, and processing tar pitch/petroleum pitch/natural pitch by selective extraction, etc. It can solve the problems of long-term operation, blockage of equipment and pipelines, and large floor space, so as to achieve the effect of facilitating long-term operation, reducing equipment blockage and reducing floor space.
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Embodiment 1
[0019] Mix aliphatic hydrocarbon solvent oil and aromatic hydrocarbon solvent oil evenly in a weight ratio of 1, and preheat it to 150°C, and then use a pump to mix the preheated coal tar soft pitch with a weight ratio of 50kg / hour 1:1 is mixed, the mixed oil enters the sedimentation separation tank at a speed of 100kg / hour, the residence time of the mixed oil in the sedimentation separation tank is controlled to be about 8 hours, and the light phase that flows out is distilled to obtain qualified quinoline insolubles Refined asphalt is used as a raw material for the production of needle coke.
Embodiment 2
[0021] Mix kerosene and washing oil evenly at a weight ratio of 1, preheat it to 150°C, and then use a pump at a speed of 50kg / hour to mix the preheated coal tar soft asphalt with a weight ratio of 0.9:1 The mixed oil enters the settling and separating tank at a rate of 100kg / hour, and the residence time of the mixed oil in the settling and separating tank is controlled to be about 8 hours, and the light phase flowing out is then distilled to obtain qualified refined pitch with quinoline insolubles. As a raw material for the production of needle coke.
Embodiment 3
[0023] Aliphatic hydrocarbon solvent oil and aromatic hydrocarbon solvent oil are mixed uniformly at a weight ratio of 0.6:1, and preheated to 100°C, and then pumped at a speed of 50kg / hour with the preheated coal tar soft asphalt by weight The ratio is 1.2:1 for mixing, the mixed oil enters the sedimentation separation tank at a speed of 100kg / hour, the residence time of the mixed oil in the sedimentation separation tank is controlled to be about 8 hours, and the light phase that flows out is distilled to obtain quinoline insoluble Qualified refined asphalt is used as the raw material for the production of needle coke.
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Abstract
Description
Claims
Application Information
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