Utilization method of catalytic slurry oil
A technology for catalyzing oil slurry and residual oil, which is applied in chemical processing of tar pitch/petroleum pitch/natural pitch, processing of tar pitch/petroleum pitch/natural pitch, petroleum industry, etc., and can solve temperature sensitivity and aging resistance Poor performance and other problems, to achieve the effect of improving anti-aging performance, high-temperature anti-rutting performance and excellent anti-aging performance, and improving temperature sensitivity
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Embodiment 1
[0033] Heat the catalytic oil slurry to 180°C, add powdered condensed aluminum phosphate (aluminum tripolyphosphate, fineness 800 mesh, the same below) into the catalytic oil slurry, of which the catalytic oil slurry accounts for 98.0wt% of the total, and the condensed phosphoric acid Aluminum accounted for 2.0wt% of the total amount. At 180°C, the mixture was mixed with ordinary stirring for 210 minutes, and then the modified catalytic oil slurry was obtained.
[0034] The above-mentioned modified catalytic oil slurry and vacuum residue (25°C density 1.021g / cm 3 , softening point 44.3 ° C, flash point 279 ° C, the same below) mixed and added to the solvent deasphalting device, the mixing temperature is 130 ° C, the solvent used is butane, and the total amount of modified catalytic oil slurry and residual oil mixture Quality is the benchmark, and the proportion of modified catalytic oil slurry accounts for 7wt% by mass fraction, and then solvent extraction is carried out to ex...
Embodiment 2
[0036] Heat the catalytic oil slurry to 160°C, add powdered condensed aluminum phosphate (aluminum dihydrogen tripolyphosphate, fineness 800 mesh) into the catalytic oil slurry, of which the catalytic oil slurry accounts for 97.1wt% of the total, and the condensed aluminum phosphate Accounting for 2.9wt% of the total, at 190°C, the reaction was completed after 160 minutes with ordinary stirring and mixing, and the modified catalytic oil slurry was obtained.
[0037] The modified catalytic oil slurry is mixed with the vacuum residue and then added to a solvent deasphalting device for solvent extraction. The extraction conditions are the same as in Example 1. The properties of the obtained deoiled bitumen are shown in Table 2.
Embodiment 3
[0039]Catalytic oil slurry accounted for 99.7wt% of the total, condensed aluminum phosphate (aluminum tripolyphosphate, fineness 600 mesh) accounted for 0.3wt% of the total, and other conditions were the same as in Example 1 to obtain modified catalytic oil slurry.
[0040] The modified catalytic oil slurry is mixed with the vacuum residue and then added to a solvent deasphalting device for solvent extraction. The extraction conditions are the same as in Example 1. The properties of the obtained deoiled bitumen are shown in Table 2.
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