Production method of environment-friendly rubber oil
An environmentally friendly rubber oil and production method technology, applied in the direction of refining with two or more solvents, can solve the problems of difficult production, unqualified eight kinds of aromatic hydrocarbons, low yield of environmentally friendly rubber oil, etc.
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Embodiment 1
[0041] Adopt the raw material oil and extracting column identical with comparative example. A solvent is N-methylpyrrolidone (NMP for short), and B solvent is water. A: Raw oil: B=1.5:1:0.4 (weight). A solvent (70°C) enters from the upper feed port of the extraction tower, raw oil (55°C) enters from the middle and lower feed port of the extraction tower, and B solvent (50°C) enters from the lower feed port of the extraction tower. The temperature of the precipitation section is 50-55°C from bottom to top, and the temperature of the extraction section is 55-70°C from bottom to top. The refined liquid is obtained from the top of the tower, and the extract is obtained from the bottom of the tower. The refined liquid is evaporated to recover the solvent to obtain the refined oil as environmentally friendly rubber oil, the yield is 66.2%, the content of benzo[a]pyrene is 0 μg / g, the total content of 8 kinds of carcinogens is 0 μg / g, and the aromatic carbon rate is C A It is 26.0%...
Embodiment 2
[0043] Using the same extraction tower and feed oil as in Example 1, solvent A is respectively furfural, phenol, dimethyl sulfoxide, sulfolane, N-formyl morpholine, solvent B is water, and solvent A (70° C.) is extracted from The upper feed port of the extraction tower enters, the raw material oil (55°C) enters from the middle and lower feed port of the extraction tower, and the B solvent (50°C) enters from the lower feed port of the extraction tower. A: Raw oil: B=2.5:1:0.3 (weight), the temperature of the precipitation section is 50-60°C from bottom to top, and the temperature of the extraction section is 60-75°C from bottom to top. Get the extract at the bottom. The refined oil obtained by recovering the solvent from the refined liquid is environmentally friendly rubber oil. The refined oil accounts for the yield of raw oil, the content of benzo[a]pyrene, the content of 8 kinds of carcinogens, and the aromatic carbon rate C A They are listed in Table 4 respectively.
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Embodiment 3
[0048] Using the same extraction tower and raw oil as in Example 1, the flow process is as shown in the accompanying drawings. A solvent is furfural, NMP, phenol, dimethyl sulfoxide, sulfolane, N-formyl morpholine respectively, and B solvent is ethanol. A: Raw oil: B=2.5:1:1 (weight), the temperature of the precipitation section is 60-70°C from bottom to top, and the temperature of the extraction section is 70-90°C from bottom to top. Get the extract at the bottom. The refined oil obtained by recovering the solvent from the refined liquid is environmentally friendly rubber oil. The refined oil accounts for the yield of raw oil, the content of benzo[a]pyrene, the content of 8 kinds of carcinogens, and the aromatic carbon rate C A They are listed in Table 5 respectively.
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