Solvent | Advantages | Disadvantages | Application |
Liquid sulphur dioxide | Good selectivity, low solubility of lubricating oil components, can be used with 15–16% benzene | High vapour pressure, low solubility | Extraction of aromatic hydrocarbons (benzene, toluene, xylene) from reformed naphtha and refining of kerosene, crude diesel oil, and lubricating oil |
Aniline | Good selectivity and solubility | High toxicity | Refining of lubricating oil |
Phenol | Chemically stable, easy to recover, selectivity and solubility can be adjusted according to moisture content, usage is 1–2 times the amount of raw oil | High toxicity, high freezing point, raw oil with high aromatic content is not suitable for use | Refining of lubricating oil |
Toluene | High solubility of aromatic hydrocarbons, can precisely separate alkanes and cycloalkanes | High boiling point, difficult to recover Due to high solubility, extraction must be carried out at low temperatures | Refining of lubricating oil |
Formaldehyde | Excellent selectivity between 32–138°C, suitable for high-viscosity, high-wax content feedstock oils, capable of removing asphalt, sulphides, and coloured substances | Slightly toxic | Modification of light oil and catalytic cracking feedstock oil for lubricating oil refining |
Dichloroethane | Thermally stable, resistant to hydrolysis, good selectivity and solubility, easy to separate from refined oil, extraction dosage is 1/2–3/4 of the feedstock oil, temperature 75–100°C | Acid is generated during recovery | Modification of light oil and catalytic cracking feedstock oil for lubricating oil refining |
Methylphenol | Phenol dissolves aromatic hydrocarbons and cycloalkanes; propane dilutes the feedstock oil, causing asphalt to precipitate | | Refining of lubricating oil, deasphalting. |
Ethylene glycol-water composite | It exhibits excellent selectivity and solubility for aromatic hydrocarbons, with adjustable mixing ratios, and is non-corrosive | | Extraction of aromatic components in petroleum fractionation |