Selective preparation method for 1, 3 ,5-tricumene
A tricumene and production method technology, applied in the direction of the addition of unsaturated hydrocarbons and saturated hydrocarbons, etc., can solve the problems of waste, complex production process, and difficulty in continuous production, and achieve simplified production methods and environmental protection. The effect of less pollution
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Embodiment 1
[0014] Embodiment 1, the selective preparation of 1,3,5-triisopropylbenzene production method is carried out according to the following steps: the first step, with cumene as raw material, under the effect of zeolite beta catalyst, in the alkylation reactor In, carry out alkylation reaction with raw material propylene to obtain mixed diisopropylbenzene, wherein, the molar ratio of cumene to propylene is 3:1 or 9:1 or 15:1, and the reaction temperature is 120°C or 180°C or 250℃, the pressure is 0.1Mpa or 2.0Mpa or up to 4.0MPa, the mixing volume space velocity is 3h -1 or 9h -1 or 25h -1 ; In the second step, under the action of zeolite beta catalyst, the mixed dicumene obtained in the first step is alkylated with raw material propylene in the alkylation reactor to obtain 1,3,5-triisopropylbenzene A mixture of propylbenzene, mixed diisopropylbenzene and cumene, wherein the molar ratio of mixed diisopropylbenzene to propylene is 5:1 or 18:1 or 30:1, and the reaction temperature...
Embodiment 2
[0015] Embodiment 2, the difference with embodiment 1 is: in embodiment 2, take benzene as raw material, under the effect of beta zeolite catalyst, in alkylation reactor, carry out alkylation reaction with raw material propylene, obtain Cumene; and this isopropyl benzene and raw material propylene carry out alkylation reaction again, obtain mixed dicumene, wherein, the molar ratio of benzene or isopropyl benzene and propylene is 3:1 or 9:1 or 15:1 .
Embodiment 3
[0016] Example 3, the difference from Example 1 is: using benzene and cumene as raw materials, under the action of a zeolite beta catalyst, in an alkylation reactor, carry out an alkylation reaction with raw material propylene to obtain a mixed Diisopropylbenzene, wherein the molar ratio of benzene and propylbenzene to propylene is 3:1 or 9:1 or 15:1.
[0017] In embodiments 1 to 3: the alkylation reaction is carried out in the same alkylation reactor respectively; or, the alkylation reaction of benzene and propylene, the alkylation reaction of cumene and propylene are all carried out in the first One alkylation reactor is carried out, and the alkylation reaction of mixed dicumyl and propylene is carried out in the second alkylation reactor; Or, the alkylation reaction of benzene and propylene is carried out in the first alkylation reaction The alkylation reaction of cumene and propylene, the alkylation reaction of mixed dicumene and propylene are carried out in the second alk...
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