A method for refining mesophase pitch by hydrogenation and chain transfer modification

A mesophase asphalt and modified asphalt technology, which is applied in the direction of processing tar asphalt/petroleum asphalt/natural asphalt by distillation, and processing tar asphalt/petroleum asphalt/natural asphalt by chemical methods, which can solve the problem of difficult to improve the quality of mesophase asphalt, etc. problems, to achieve the effect of low cost, guaranteed uniformity, and high structural controllability

Active Publication Date: 2021-04-02
湖南东映长联科技有限公司 +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

Patent ZL 201710217039.2 discloses a method of petroleum-based spinnable mesophase pitch, using tetrahydronaphthalene, tetrahydroquinoline, hydrogenated anthracene oil, etc. as a hydrogenation solvent, mixed with high softening point pitch, and pressurized at 400-450°C The hydrogenated pitch is obtained by heat treatment, and the mesophase pitch with a relatively high softening point can be obtained after the hydrogenated pitch is heat treated. This method does not separate the hydrogenated pitch. In order to avoid coking, the degree of hydrogenation needs to be controlled at a low level. The final mesophase Asphalt quality is difficult to improve

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  • A method for refining mesophase pitch by hydrogenation and chain transfer modification

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Effect test

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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Abstract

The invention discloses a method for modifying and refining intermediate phase pitch through hydrogenation and chain transfer. The method comprises the following specific steps: putting precursor asphalt into a multistage molecular distillation device, separating out a fraction A1 and a residual tower bottom component B1, performing catalytic hydrogenation on the fraction A1, mixing the hydrogenated fraction A1 with the precursor asphalt according to a mass ratio of (1-4): 1, performing pressurized polymerization, and separating out fractions A2 and B2 from pressurized modified asphalt; wherein the initial boiling point of the fraction B2 is 400-500 DEG C, and the final boiling point of the fraction B2 is 540-600 DEG C; carrying out catalytic hydrogenation on a residual tower bottom component C2 and the fraction A2, mixing the product of the catalytic hydrogenation with a precursor, carrying out pressurized polymerization, and directly carrying out thermal polycondensation on the B2 fraction as an intermediate phase asphalt raw material to prepare intermediate phase asphalt. The reactor is a multi-stage distributable tubular reactor, and the interior of the reactor is composed of amulti-stage filter screen, a high-pressure heat flow channel and a lower space of the high-pressure heat flow channel. The intermediate phase pitch with a high hydrogen-carbon ratio and a low softening point can be obtained, is high in structural controllability and low in cost.

Description

technical field [0001] The invention belongs to the technical field of bitumen preparation, and more specifically relates to a method for refining mesophase pitch through hydrogenation and chain transfer modification. Background technique [0002] Mesophase pitch suitable for pitch carbon fiber and carbon foam is a polycyclic aromatic compound with extremely high performance requirements. In order to make the molecules highly oriented, the mesophase pitch needs to have low impurity content, uniform molecular weight distribution, good thermal stability of the molecular structure, and good flatness and flexibility at the same time. Due to the high impurity content and complex composition of natural oil slurry and bitumen, which contain a large amount of long-chain alkanes, olefins, sulfur-containing nitrogen-containing heterocyclic molecules, and a small amount of highly condensed polycyclic aromatic hydrocarbons with ultra-macromolecules, it is necessary to extract the oil sl...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10C3/02C10C3/06
CPCC10C3/02C10C3/06
Inventor 叶崇向逸风伍孝余洋黄东吴晃叶高明刘金水
Owner 湖南东映长联科技有限公司
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