Method for preparing isotropic coke
A technology of isotropic coke and quinoline, which is applied in the field of preparation of isotropic coke, can solve the problems of increasing the inflation coefficient and difficulty in uniform distribution, and achieves the effects of easy operation, strong controllability and wide source of raw materials
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Embodiment 1
[0022] 700 grams of coal tar pitch with a quinoline insoluble content of 10.43% is placed in the reactor, heated at a rate of 120°C / hour, and stirred at 150°C. Continue to raise the temperature to 410° C. under the heating rate, and carry out the polymerization reaction at a constant temperature for 5 hours to obtain the asphalt polymerization mother liquor. Put the prepared asphalt polymerization mother liquor into a test tube under normal pressure, raise it to 500°C at a heating rate of 15°C / h, discharge the gas generated during carbonization through the control valve, and keep the pressure not exceeding 0.5Mpa until the end of carbonization. Take out the raw coke sample from the tube for measurement, crush the coke sample to a particle size of 0.2-1 mm, solidify with resin, and observe the microstructure as a fine mosaic structure after grinding and polishing the sample, see figure 1 . The obtained isotropic green coke is made into a volume of 1dm by a small vibration mold...
Embodiment 2
[0024] 500 grams of quinoline insoluble matter content is 15.78% asphaltene material and 1500g quinoline insoluble matter content is 2.35% soft bitumen, obtains quinoline insoluble matter content as 8.21% mixed pitch, it is placed in reactor In the process, heat at a heating rate of 180 °C / h, start stirring at 150 °C, continue to heat up to 420 °C at a stirring rate of 200 rpm and a heating rate of 120 °C / hour, keep the temperature for 8 hours, stop stirring, and start at 20 °C / h The heating rate of h is increased to 530°C, the gas generated during carbonization is discharged through the control valve, and the pressure is kept not exceeding 0.5Mpa until the carbonization is completed, and the coke is discharged for measurement. The obtained raw coke samples were crushed to a particle size of 0.2-1 mm, cured with resin, and the microstructure was observed to be a fine mosaic structure after grinding and polishing. The obtained isotropic green coke is made into a volume of 1dm b...
Embodiment 3
[0026] 1000 grams of asphaltenes with quinoline insoluble content of 13.73% and 1000 g of quinoline insoluble content of 13.42% medium temperature asphalt are uniformly mixed to obtain mixed pitch with quinoline insoluble content of 9.52%, which is placed in the reactor In the process, heat at a heating rate of 180 °C / h, start stirring at 150 °C, continue to heat up to 420 °C at a stirring rate of 200 rpm and a heating rate of 120 °C / h, keep the temperature for 10 hours, stop stirring, and start stirring at 20 °C / h The heating rate of h is increased to 520°C, and the gas generated during carbonization is discharged through the control valve, and the pressure is kept not exceeding 0.5Mpa until the carbonization is completed. out of focus for measurement. The resulting burnt sample was crushed to a particle size of 0.2-1 mm, cured with resin, and the microstructure was observed to be a fine mosaic structure after grinding and polishing. The obtained isotropic green coke is made...
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