Modified pitch, pitch coke and preparation methods and application thereof
A technology for modifying pitch and pitch coke, which is applied in chemical processing of tar pitch/petroleum pitch/natural pitch, chemical instruments and methods, electrical components, etc. The internal structure of the product is uneven and the content of volatile components is high, so as to achieve the effect of reducing the preparation cost, low volatile content and uniform internal structure.
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Embodiment 1
[0034] Coal tar pitch with a softening point of 60°C and isopolyvanadate catalyst (NH 4 ) 4 V 4 o 12 2H 2 O, mixed at a mass ratio of 1:0.001, added to a reactor with a reflux device and an air distributor at the bottom, fed with air, the air flow rate was 10L / h, and the temperature was raised to 340 at a heating rate of 3°C / min. ℃, keep the temperature at 340℃ for 1h. Stop the air flow after the constant temperature is over, switch to nitrogen flow, the nitrogen flow rate is 1L / h, continue to raise the temperature of the reactor to 490°C at a heating rate of 3°C / min, and keep the temperature at 490°C for 3h to obtain pitch coke. figure 1 is the polarized photo of the obtained pitch coke, from figure 1 It can be seen that the prepared pitch coke has a fine mosaic structure, isotropy, uniform internal structure, and no local coking phenomenon.
Embodiment 2
[0036] Coal tar pitch with a softening point of 60°C and isopolyvanadate catalyst (NH 4 ) 4 V 4 o 12 2H 2 O, mixed at a mass ratio of 1:0.002, added to a reactor with a reflux device and an air distributor at the bottom, fed with air, the air flow rate was 10L / h, and the temperature was raised to 340 at a heating rate of 3°C / min °C, keep the temperature at 340 °C for 3 hours. Stop the air flow after the constant temperature is over, switch to nitrogen flow, the nitrogen flow rate is 1L / h, continue to raise the temperature of the reactor to 490°C at a heating rate of 3°C / min, and keep the temperature at 490°C for 6h to obtain pitch coke.
Embodiment 3
[0038] Coal tar pitch with a softening point of 60°C and isopolyvanadate catalyst (NH 4 ) 4 V 10 o 26 ·6H 2O, mixed at a mass ratio of 1:0.002, added to a reactor with a reflux device and an air distributor at the bottom, fed with air, the air flow rate was 20L / h, and the temperature was raised to 340 at a heating rate of 3°C / min ℃, keep the temperature at 340℃ for 1h. Stop the air flow after the constant temperature is over, switch to nitrogen flow, the nitrogen flow rate is 1L / h, continue to raise the temperature of the reactor to 490°C at a heating rate of 3°C / min, and keep the temperature at 490°C for 3h to obtain pitch coke.
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