A method for preparing alkylated gasoline by catalyzing the reaction of isobutane and C4 olefins
A technology for alkylating gasoline and catalyzing isobutane, which is applied in chemical instruments and methods, organic chemistry, chemical recycling, etc., can solve the problems of equipment corrosive environment, difficult to recycle, pollute catalysts, etc., and achieve simple processing and stable products. , the effect of stabilizing the catalytic capacity
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Embodiment 1
[0021] Embodiment 1: 5g (3-sulfonic acid)-propyltriethylammonium chloride zincate ionic liquid (wherein the mol ratio of (3-sulfonic acid) propyltriethylammonium salt and zinc chloride 1 : 4) drop into the high-pressure airtight reaction kettle, nitrogen replaces the air in the kettle, pump 15g of the mixed solution of isobutane and isobutene (the ratio of the substance is 10:1) into the kettle, heat to 60°C and stir for 2h, statically Place and cool to room temperature, and collect residual gas from the kettle. Open the kettle, transfer the mixture in the kettle to a separatory funnel for phase separation. The lower phase is an ionic liquid catalyst, which can be directly used for the next reaction, and the upper phase is alkylated gasoline. The conversion rate of isobutene is 98.2%, the selectivity of TMP is 89.5%, and the yield of alkylated gasoline is 87.6%.
Embodiment 2
[0025] Embodiment 2: 3g (3-sulfonic acid)-propyltriethylammonium chlorocuprate ionic liquid (wherein the mol ratio of (3-sulfonic acid)-propyltriethylammonium chloride to cupric chloride 1:3.5), replace the air in the kettle with nitrogen, pump 15g of the mixed solution of isobutane and isobutene (the ratio of substances is 20:1) into the kettle, heat to 70°C and stir for 2.5h, stand still and cool to room temperature , to collect the residual gas from the kettle. Open the kettle, transfer the mixture in the kettle to a separatory funnel for phase separation. The lower phase is an ionic liquid catalyst, which can be directly used for the next reaction. The upper layer is alkylated gasoline. The conversion rate of isobutene is 99.5%, the selectivity of TMP is 90.5%, and the yield of alkylated gasoline is 93%.
Embodiment 3
[0026] Embodiment 3: 5g (2-sulfonic acid)-ethyltriethylammonium ferric chloride ionic liquid (wherein the mol ratio of chloride (2-sulfonic acid)-ethyltriethylammonium salt to ferric chloride 1:5) into a high-pressure airtight reaction kettle, replace the air in the kettle with nitrogen, pump 20 g of a mixture of isobutane and 1-butene (the ratio of substances is 15:1) into the kettle, heat to 15°C and stir React for 3h, let it stand and cool to room temperature, and collect the residual gas in the kettle. Open the kettle, transfer the mixture in the kettle to a separatory funnel for phase separation. The lower phase is an ionic liquid catalyst, which can be directly used for the next reaction. The upper layer is alkylated gasoline. The conversion rate of isobutene is 90.5%, the selectivity of TMP is 93.1%, and the yield of alkylated gasoline is 91.2%.
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