Method and device for lightening vacuum residue/coal tar and producing heavy traffic asphalt
A technology of vacuum residue oil and heavy-cross asphalt, which is applied in the fields of coal chemical industry, petrochemical industry and oil refining, can solve the problem of inability to produce high-grade heavy-cross asphalt, etc., to improve the extraction efficiency, simplify the catalytic cracking unit, and reduce the investment. Effect
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Embodiment 1
[0035]A method for realizing the lightening of vacuum residue / coal tar and producing heavy-duty asphalt. The raw material oil 1 is firstly sent to the catalytic cracking unit (2) through the raw material oil delivery pipeline (1), and the catalytic cracking unit only includes In the reaction-regeneration system, the raw oil completes the catalytic reaction in the catalytic cracking unit (2), and the catalytic cracking catalysts used are ZSM-5 zeolite, omega zeolite, alumina and montmorillonite, and the catalytic cracking reaction temperature of the reaction-regeneration system is 500 ℃, the regeneration temperature is 700℃, the mass ratio of catalyst to raw oil is 4:1, the reaction time is 5s, and the reaction pressure (gauge pressure) is 0.5MPa. The feed liquid after catalytic cracking directly enters the solvent extraction device (3) without separation, and the solvent extraction device (3) adopts a one-stage extraction and one-stage sedimentation process, and the extraction ...
Embodiment 2
[0040] A method for realizing the lightening of vacuum residue / coal tar and producing heavy-duty asphalt. The raw material oil 2 is firstly sent to the catalytic cracking unit (2) through the raw material oil delivery pipeline (1), and the catalytic cracking unit only includes In the reaction-regeneration system, the raw oil completes the catalytic reaction in the catalytic cracking unit (2), and the catalytic cracking catalyst used is ultra-stable Y-type zeolite, ZRP zeolite, alumina, titanium oxide, diatomaceous earth and montmorillonite without rare earth elements. The catalytic cracking reaction temperature of the reaction-regeneration system is 480°C, the regeneration temperature is 670°C, the mass ratio of catalyst to raw oil is 7:1, the reaction time is 0.5s, and the absolute pressure is 0.1MPa. The feed liquid after catalytic cracking directly enters the solvent extraction device (3) without separation, and the solvent extraction device (3) adopts a one-stage extraction...
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