Compound solvent for separating cycloalkanes and aromatic hydrocarbons from naphtha, and preparation method and application of compound solvent
A technology for producing naphthenes and naphtha, which is applied in the field of compound solvents for separating naphthenes and aromatics from naphtha and its preparation and application, can solve the problem that the demand for naphtha is increasing, and naphthenes are not widely obtained. Good utilization and other issues to achieve the effect of reducing costs
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[0054] The present invention also provides the preparation method of the above-mentioned compound solvent for separating naphthenes and aromatics from naphtha, the method comprising the steps of:
[0055] Keep the temperature of sulfolane constant at 60-80°C, then add 1-ethyl-3-methylimidazole bistrifluoromethanesulfonimide salt dropwise, and stir until the compound solvent is evenly mixed;
[0056] Wherein, the mass ratio of the 1-ethyl-3-methylimidazole bistrifluoromethanesulfonimide salt to sulfolane is 1:2-100.
[0057] The present invention further provides a method for separating naphthenes and aromatics from naphtha with the above-mentioned compound solvent. The method is to contact the compound solvent with naphtha countercurrently, and perform a liquid-liquid extraction process to obtain Yiene naphtha. A mixture of by-product compound solvents and cycloalkanes and aromatics;
[0058] Wherein, the compound solvent includes 1-ethyl-3-methylimidazole bistrifluoromethane...
Embodiment 1
[0084] 1-ethyl-3-methylimidazole bis-trifluoromethanesulfonimide salt and sulfolane are compounded to prepare a compound solvent, and the compounding ratio is ionic liquid: sulfolane=1:2 (quality), according to figure 1 The flow process extracts and separates the naphtha fraction. The ionic liquid and sulfolane are drawn from their respective storage tanks and enter the static mixer M. Naphtha countercurrent contact; after liquid-liquid extraction and extraction, the overhead stream of extraction tower 1 is naphtha (raffinate) from which part of the naphthenes and aromatics have been removed, while most of the naphthenes and aromatics and all compound solvents Together, they are drawn from the bottom of the extraction tower 1 to the vacuum distillation tower 2; after vacuum distillation, the compound solvent flows out from the bottom of the vacuum distillation tower 2 and circulates to the top of the extraction tower 1, and after mixing with the fresh compound solvent Together...
Embodiment 2
[0087] This embodiment is basically the same as Embodiment 1, and the specific steps are as follows:
[0088] 1-ethyl-3-methylimidazole bis-trifluoromethanesulfonimide salt and sulfolane are compounded to prepare a compound solvent, and the compounding ratio is ionic liquid: sulfolane=1:10 (quality), according to figure 1 The flow process extracts and separates the naphtha fraction. The ionic liquid and sulfolane are drawn from their respective storage tanks and enter the static mixer M. Naphtha countercurrent contact; after liquid-liquid extraction and extraction, the overhead stream of extraction tower 1 is naphtha (raffinate) from which part of the naphthenes and aromatics have been removed, while most of the naphthenes and aromatics and all compound solvents Together, they are drawn from the bottom of the extraction tower 1 to the vacuum distillation tower 2; after vacuum distillation, the compound solvent flows out from the bottom of the vacuum distillation tower 2 and ci...
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