Method for preparing fuel oil by waste plastic pyrolytic oil
A technology for pyrolysis of oil and waste plastics, which is only applied in the direction of multi-stage series refining process treatment, etc., can solve the problems of polluting the atmospheric environment and high impurity content, and achieve the effect of low operating cost, low investment and wide application prospects
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Embodiment 1
[0011] React 20% sodium hydroxide aqueous solution and waste plastic pyrolysis oil at a mass ratio of 1:2.0 at a temperature of 75°C for 5 hours, cool to 50°C, and separate the stationary oil and water phases. The above-mentioned pyrolysis oil is put into the reactor, and a silica gel adsorbent loaded with phosphotungstic acid is added to the pyrolysis oil. The mass ratio of phosphotungstic acid to silica gel is 0.2:1. After loading phosphotungstic acid, the adsorbent and pyrolysis oil are reacted and adsorbed at 50°C for 1 hour according to the mass ratio of 0.05:1, and then filtered and separated to obtain clean fuel oil. The contents of chlorine, bromine, nitrogen and sulfur in the fuel oil are all less than 6ppm.
Embodiment 2
[0013] React 70% potassium hydroxide aqueous solution and waste plastic pyrolysis oil at a mass ratio of 1:20 at a temperature of 350°C for 0.5h, then cool to 70°C, and the stationary oil and water phases are separated. The above pyrolysis oil is put into the reactor, and SBA-15 adsorbent loaded with phosphomolybdic acid is added to the pyrolysis oil, and the mass ratio of phosphomolybdic acid to SBA-15 is 0.1:1. After loading phosphomolybdic acid, the adsorbent and the pyrolysis oil are reacted and adsorbed at 70°C for 0.5 hours according to the mass ratio of 0.02:1, and then filtered and separated to obtain clean fuel oil. The contents of chlorine, bromine, nitrogen and sulfur in the fuel oil are all less than 3ppm.
Embodiment 3
[0015] React 3% barium hydroxide aqueous solution and waste plastic pyrolysis oil at a mass ratio of 1:10 at 150°C for 10 hours, cool to 70°C, and separate the stationary oil and water phases. The above-mentioned pyrolysis oil is put into the reactor, and MCM-41 adsorbent loaded with silicotungstic acid is added to the pyrolysis oil, and the mass ratio of silicotungstic acid to MCM-41 is 0.5:1. After loading silicotungstic acid, the adsorbent and pyrolysis oil are reacted and adsorbed at 90°C for 5 hours according to the mass ratio of 0.2:1, and then filtered and separated to obtain clean fuel oil. The contents of chlorine, bromine, nitrogen and sulfur in the fuel oil are all less than 8ppm.
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