The preparation method of alpha-methyl styrene
A kind of technology of methyl styrene and propyl benzene flow, applied in the field of preparation of α-methyl styrene, can solve problems such as shortage, increase of AMS production volume, etc., and achieve the effect of improving selectivity and
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Embodiment 1 and 2
[0075] according to figure 2 The process diagram shown, prepares α-methylstyrene.
[0076] First, the phenol process utilizes three oxidation reactors, and the oxidation of cumene with an oxidizing agent is carried out by the following conditions to produce a stream containing cumene hydroperoxide (CHP) at a concentration of 25% by weight.
[0077] (1) Conditions for putting in the first oxidizer (firstoxidizer)
[0078] Supply (CHP0.4%+cumene 99.6%) 1ml / min, 02:100ml / min, pressure: 3bar, reaction temperature: 100°C.
[0079] (2) Conditions for putting in the second oxidizer (secondoxidizer)
[0080] Supply (CHP8.42%+cumene 91.58%) 1ml / min, 02:100ml / min, pressure: 3bar, reaction temperature: 96°C.
[0081] (3) Conditions for putting in the third oxidizer (thirdoxidizer)
[0082] Supply (CHP16.27%+cumene 83.73%) 1ml / min, 02:100ml / min, pressure: 3bar, reaction temperature: 94°C.
[0083] At this time, as shown in Table 1 below, the concentration of the CHP stream was chang...
experiment example
[0106] In said Example 1, after the addition of CHP during the hydrogenation process, the composition of the reactant solution was analyzed over time. According to its composition analysis, the CHP conversion rate and CA increase rate in the catalytic hydrogenation process were measured by the following method, and the results are shown in Table 3.
[0107] [mathematical formula 1]
[0108] CHP conversion rate (%) = (CHP supply (weight %) - CHP product (weight %)) / (CHP supply (weight %))
[0109] [mathematical formula 2]
[0110] CA increase rate (%) = (CA product (weight %) - CA supply (weight %)) / (CA supply (weight %))
[0111] [table 3]
[0112]
[0113]
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