Production method of highly aromatic environmental-friendly rubber oil
A technology of environmental protection rubber oil and production method, which is applied in the petroleum industry, processing hydrocarbon oil, etc., can solve the problems of low aromatic content of environmental protection oil, difficulty in refining carcinogens, low yield of environmental protection oil, etc.
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Embodiment 1
[0021] Mix the extracted oil and furfural in the comparative example evenly at 90°C, the mass ratio of furfural to extracted oil is 0.5:1, then lower the temperature of the mixture to 40°C and settle at this temperature for 20 minutes, and divide it into upper and lower two. layer, get the upper stratum eluate and carry out furfural extraction, and the extraction is carried out in the extraction tower, which is the same as that used in the comparative example. Furfural enters from the upper part of the extraction tower as a solvent, and the eductate enters from the lower part of the tower. The mass ratio of furfural / eductate is 1:1. Extracted liquid is obtained at the bottom of the tower, and the raffinate and extracted liquid are distilled and dried to obtain raffinate oil and secondary extracted oil. After 10 hours of operation, the calculation finds that the raffinate yield accounts for 57wt% of the raw material extracted oil, and its PCA content 2.7%, the content of benzo[...
Embodiment 2
[0023] Mix the extracted oil and furfural in the comparative example evenly at 60°C, the mass ratio of furfural to extracted oil is 0.7:1, then lower the temperature of the mixture to 40°C and settle at this temperature for 10 minutes, and divide it into upper and lower layer, get the upper layer eluate and carry out furfural extraction, and the extraction is carried out in the extraction tower, which is the same as that used in the examples. Furfural enters from the upper part of the extraction tower as a solvent, and the eluate enters from the lower part of the tower. The mass ratio of furfural / eluent is 0.8:1. The temperature of the upper part of the extraction tower is 60 °C, and the temperature of the lower part is 50 °C. The bottom of the tower obtains the extract, and the raffinate and the extract obtain raffinate and secondary extract oil after distillation and drying. After running for 10 hours, it is found that the raffinate yield accounts for 63wt% of the raw materia...
Embodiment 3
[0025]Mix the extracted oil and furfural in the comparative example evenly at 60°C, the mass ratio of furfural to extracted oil is 0.7:1, then lower the temperature of the mixture to 30°C and settle at this temperature for 100 minutes, and divide it into upper and lower two. layer, get the upper layer eluate and carry out furfural extraction, and the extraction is carried out in the extraction tower, which is the same as that used in the examples. Furfural enters from the upper part of the extraction tower as a solvent, and the eluate enters from the lower part of the tower. The mass ratio of furfural / eluent is 0.8:1. The temperature of the upper part of the extraction tower is 60 °C, and the temperature of the lower part is 50 °C. Extracted liquid is obtained at the bottom of the tower, and the raffinate and the extracted liquid are distilled and dried to obtain raffinate oil and secondary extracted oil. After 10 hours of operation, the calculation finds that the raffinate yie...
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Abstract
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