Method for modifying and refining intermediate phase pitch through hydrogenation and chain transfer
A technology for mesophase asphalt and modified asphalt, which is applied in the processing of tar asphalt/petroleum asphalt/natural asphalt by distillation, and the processing of tar asphalt/petroleum asphalt/natural asphalt by chemical methods, etc., which can solve the difficulty in improving the quality of mesophase asphalt, etc. problem, to achieve the effect of low cost, guaranteed uniformity and good compatibility
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Embodiment 1
[0035] A new method for hydrogenation and chain transfer modification to refine mesophase pitch raw materials and a special reactor for pressurized polymerization, characterized in that it includes the following steps:
[0036] (1) Heat 500kg / h precursor pitch to 60°C through a heat exchanger, and pump it into the first-stage molecular still to separate the 240°C fraction by a gear pump. The operating temperature is 25°C, the operating pressure is 0.1mbar, and the rotation speed is 380r / min 25kg / h of light components and 475kg / h of heavy components were obtained, and the obtained heavy components were pumped into the second stage molecular still to cut fractions again. The operating temperature was 210°C, the operating pressure was 0.1mbar, and the rotating speed was 380r / min to obtain the A1 fraction 295kg / h, B1 fraction 180kg / h;
[0037] (2) Heat the obtained A1 fraction to 280°C and pump it into a three-stage hydrotreating reactor with a weighted average bed temperature of ...
Embodiment 2
[0044] A new method for hydrogenation and chain transfer modification to refine mesophase pitch raw materials and a special reactor for pressurized polymerization, characterized in that it includes the following steps:
[0045] (1) Heat 500kg / h precursor pitch to 60°C through a heat exchanger, and pump it into the first-stage molecular still to separate the 240°C fraction by a gear pump. The operating temperature is 25°C, the operating pressure is 0.1mbar, and the rotation speed is 380r / min 27kg / h of light components and 473kg / h of heavy components were obtained, and the obtained heavy components were pumped into the second-stage molecular still to cut fractions again. The operating temperature was 210°C, the operating pressure was 0.1mbar, and the rotating speed was 380r / min to obtain the A1 fraction 292kg / h, B1 fraction 181kg / h;
[0046] (2) Heat the obtained A1 fraction to 280°C and pump it into a three-stage hydrotreating reactor with a weighted average bed temperature of ...
Embodiment 3
[0053] A new method for hydrogenation and chain transfer modification to refine mesophase pitch raw materials and a special reactor for pressurized polymerization, characterized in that it includes the following steps:
[0054] (1) Heat 500kg / h precursor pitch to 60°C through a heat exchanger, and pump it into the first-stage molecular still to separate the 240°C fraction by a gear pump. The operating temperature is 25°C, the operating pressure is 0.1mbar, and the rotation speed is 380r / min 23kg / h of light components and 477kg / h of heavy components were obtained, and the resulting heavy components were pumped into the second-stage molecular still to cut fractions again. The operating temperature was 210°C, the operating pressure was 0.1mbar, and the rotating speed was 380r / min to obtain the A1 fraction 293kg / h, B1 fraction 184kg / h;
[0055] (2) Heat the obtained A1 fraction to 280°C and pump it into a three-stage hydrotreating reactor with a weighted average bed temperature of...
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