A kind of method for preparing isoamylene
A technology of isopentene and isopentane, applied in the field of preparation of isopentene, can solve problems such as cracking side reactions, and achieve the effect of significant value-added and simple and easy separation
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Embodiment 1
[0023] The reaction conditions are: isopentane 720g / h, butene-rich (containing isobutane 0.97%, n-butane 44.53%, trans-butene 22.75%, n-butene 21.30%, isobutene 0.29%, butene 10.16%) 2000g / h, 600g / h acetic acid, through a fixed bed tube reactor filled with D001 macroporous acidic cation exchange resin, the reaction temperature is 60°C, the reaction pressure is 1.5MPa, and the total residence time is 1.5h. After the reaction was completed, samples were taken for analysis, among them, isopentane 8.51%, isopentene 12.40%, isobutane 0.53%, n-butane 37.45%, trans-butene 10.93%, n-butene 2.66%, isobutene 0.24%, cis Butene 2.95%, acetic acid 13.70%, sec-butyl acetate 13.70%. Through separation, about 704g / h of carbon five components can be obtained, which contains 59.37% of isopentene and 40.63% of isopentane. The total conversion rate of isopentane is calculated to be 60.28%, and the total selectivity of isopentene is 99.06% %.
Embodiment 2
[0025] The reaction conditions are: isopentane 720g / h, mixed butene (containing isobutane 1.36%, n-butane 47.80%, trans-butene 35.34%, n-butene 3.17%, isobutene 0.09%, butene 12.23%) 2000g / h, acetic acid 600g / h, passed through a fixed bed tube reactor filled with D001 macroporous acidic cation exchange resin, the reaction temperature was 100°C, the reaction pressure was 2.0MPa, and the total residence time was 1h. After the reaction was completed, samples were taken for analysis, of which, 6.12% isopentane, 13.89% isopentene, 0.82% isobutane, 41.42% n-butane, 14.18% trans-butene, 0.28% n-butene, 0.09% isobutene, cis Butene 1.42%, acetic acid 11.91%, sec-butyl acetate 9.87%. Through separation, about 702g / h of carbon five components can be obtained, which contains 69.66% of isopentene and 30.34% of isopentane. The total conversion rate of isopentane is calculated to be 70.42%, and the total selectivity of isopentene is 99.20% %.
Embodiment 3
[0027] The reaction conditions are: isopentane 720g / h, butene-rich (containing isobutane 0.97%, n-butane 44.53%, trans-butene 22.75%, n-butene 21.30%, isobutene 0.29%, butene 10.16%) 2000g / h, acetic acid 600g / h, passed through a fixed-bed tube reactor filled with keggin-type phosphotungstic acid (ie, phosphotungstic heteropoly acid), the reaction temperature was 130°C, the reaction pressure was 2.0MPa, and the total residence time was 2h. After the reaction was completed, samples were taken for analysis, of which, isopentane 15.06%, isopentene 6.02%, isobutane 0.56%, n-butane 32.16%, trans-butene 12.82%, n-butene 5.02%, isobutene 0.21%, cis Butene 4.64%, acetic acid 11.52%, sec-butyl acetate 11.99%. Through separation, about 709g / h of carbon five components can be obtained, which contains 28.63% of isopentene and 71.37% of isopentane. The total conversion rate of isopentane is calculated to be 29.72%, and the total selectivity of isopentene is 97.58% %.
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