Preparation method of aromatic rubber oil
A technology for aromatic rubber oil and raw material oil, which is applied in the direction of multi-stage series refining process treatment, etc., can solve the problem of high total content and achieve the effect of meeting environmental protection requirements.
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[0008] According to the preparation method of the aromatic rubber oil provided by the present invention, the method comprises that the raw material oil and the first extraction solvent are fully contacted in the first extraction tower, and the raffinate of the first extraction tower is mixed with the second extraction solvent Fully contact in the second extraction tower, separate the extraction oil from the extract liquid of the second extraction tower; the first extraction solvent contains a main solvent and an anti-solvent, and the solubility of the main solvent to aromatics is greater than that to The solubility of alkanes, the anti-solvent can improve the selectivity of the first extraction solvent to condensed ring aromatics; the second extraction solvent contains the same solvent as the main solvent.
[0009] Preferably, the second extraction solvent is the same as the main solvent.
[0010] Preferably, the anti-solvent is selected from one or more of water, methanol, et...
Embodiment 1
[0033] The second-line distillate oil is used as the raw material, and its properties are shown in Table 1. Aromatics are extracted in parallel double towers (packed towers, the theoretical number of extraction stages is three, tower model Φ60×2400×4), the solvent and raw materials of the first extraction tower The total feed flow of oil was 4000 g / h.
[0034]Raw oil enters the first extraction tower 1 through the pipeline 4, and the upper effluent of the first extraction tower 1 enters the second extraction tower 2 through the pipeline 6, which is the raw material of the second extraction tower 2; the main solvent passes through the pipeline 3 and The antisolvent from pipeline 10 is mixed into the first extraction solvent and enters the first extraction tower 1, and the second extraction solvent enters the second extraction tower 2 through the pipeline 7; the first extraction tower 1 and the second extraction tower 2 The lower part of the effluent is transported to the first ...
Embodiment 2
[0036] Aromatic rubber oil was prepared according to the same method as in Example 1, except that the dewaxed oil minus the third-line distillate was used as the raw material, and its properties are shown in Table 1. The extraction conditions are as follows: the temperature at the top of the first extraction tower 1 is 100°C, the temperature at the bottom of the first extraction tower 1 is 80°C, and the first extraction solvent is a mixed solvent of furfural and ethylene glycol, wherein the first The mass percent of extraction solvent containing ethylene glycol is 3%, and the mass ratio of the first extraction solvent and raw oil is 1.5: 1; The bottom temperature is 85°C, the second extraction solvent is furfural, and the mass ratio of the second extraction solvent to raw oil is 2.5:1.
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