A kind of preparation method of alkylated gasoline
A technology for alkylating gasoline and alkylated oil, which is applied in the petroleum industry and the production of liquid hydrocarbon mixtures, and can solve problems such as limiting the development of industrialization and irreversible deactivation of catalysts
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Embodiment 1
[0018] Example 1: The synthesis of polyetheramine ionic liquid adopts a one-pot method. First, 20g of polyetheramine D-2000 is dissolved in 30mL of dichloromethane, stirred evenly, and then 2.44g of 1,3-propanesulfonic acid is added dropwise therein Lactone, after the dropwise addition is completed, the temperature rises to 50°C, and the reaction is refluxed for 2 hours. Thereafter, 3.01 g of trifluoromethanesulfonic acid was added dropwise thereto, and the reaction was continued at 50° C. for 4 h, and the reaction was stopped. The solvent dichloromethane was removed by rotary evaporation, and the obtained product was vacuum-dried to obtain the polyetheramine ionic liquid catalyst. The synthetic route of polyetheramine ionic liquid is as follows:
[0019]
[0020] (2) Preparation of Alkylated Gasoline
Embodiment 2
[0021] Example 2: Add 10 mL of polyetheramine ionic liquid and 3 mL of trifluoromethanesulfonic acid into a stainless steel mechanically stirred reaction kettle, seal the kettle, and replace the air in the kettle with 4 MPa high-purity nitrogen for 3 times. Then pump 20mL of a mixed liquid of isobutane and isobutene with an alkane / ene ratio of 10:1, and react with mechanical stirring at 25°C for 20min. quantitative analysis. The conversion rate of isobutene is 99%, the selectivity of C8 products in the alkylate reaches 87%, and the proportion of trimethylpentane accounts for 98%.
[0022] (3) Reuse of catalyst
Embodiment 3-15
[0023] Examples 3-15: using the ionic liquid phase after the first reaction in Example 2 as a catalyst, without adding trifluoromethanesulfonic acid, after separating the alkylate oil, directly seal the kettle, and replace the air in the kettle with nitrogen, Pump in fresh 20 mL of a mixed liquid of isobutane and isobutene with an alkane / ene ratio of 10:1 to carry out the catalytic reaction. The experimental conditions are the same as in Example 2. After repeated use of the ionic liquid phase catalyst in this way, after 13 repeated experiments, the conversion rate of isobutene is still above 95%, and the selectivity of C8 products in the alkylate is still above 84%.
[0024] (4) Catalyst regeneration
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