Preparation method of alkyl diphenyl ether
A technology of alkyl diphenyl ether and diphenyl ether, which is applied in the field of preparation of alkyl diphenyl ether, can solve problems such as insufficient yield of monosubstituted products, high concentration of ionic liquid, and low yield of monosubstituted products, and achieve the elimination of waste water Effects of emissions problems
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Embodiment 1
[0016] Inject 20 moles (3400 g) of diphenyl ether (Qingdao Weibang Chemical Co., Ltd.) and 1 mole (168 g) of normal α-dodecene (industrial product, product of AGRIFU, LAO C12) into a 5L reactor respectively. The catalyst consists of trimethylammonium chloride hydrochloride and aluminum trichloride with a molar ratio of 1:2. The catalyst is injected into the reactor respectively at a ratio of 0.004 (molar ratio) to the olefin. After stirring and raising the temperature to 180°C for 2 hours, the stirring was stopped, and after standing for stratification, the upper layer was transferred to a 3L distillation pot, and the excess diphenyl ether was distilled off under reduced pressure. The product was analyzed by gas chromatography and the yield of the monoalkyl substituted product was 92.5%.
Embodiment 2
[0018] Inject 15 moles (2550 g) of diphenyl ether and 1 mole (168 g) of normal α-dodecene (commercial product, product of Agrof, LAO C16) into a 5 L reactor respectively. The catalyst consists of pyridine and aluminum trichloride in a molar ratio of 1:2. The molar ratio of catalyst to olefin was 0.004. The reaction temperature was 185° C., and the rest of the steps were the same as in Example 1. The yield of monoalkyl substituted product was 91.0% according to gas chromatography analysis.
Embodiment 3
[0020] Inject 12 moles (2040 g) of diphenyl ether and 1 mole (168 g) of normal α-dodecene (commercial product, product of Agrof, LAO C12) into a 5 L reactor respectively. The catalyst consists of chlorobutylpyridine and aluminum trichloride in a molar ratio of 1:2. The molar ratio of catalyst to olefin was 0.004. The reaction temperature was 190° C., and the rest of the steps were the same as in Example 1. The yield of monoalkyl substituted product was 90.2% according to gas chromatography analysis.
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