A kind of method for synthesizing cyclohexylbenzene by liquid-phase alkylation of benzene and cyclohexene
A technology for cyclohexene liquid-phase alkylation and cyclohexylbenzene, which is applied in the field of liquid-phase alkylation of benzene and cyclohexene to synthesize cyclohexylbenzene. Hexane is expensive and other problems, to achieve the effect of prolonging the life and prolonging the operating life
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Embodiment 1
[0046] exist figure 2 The catalyst containing MCM-22 molecular sieve is loaded into the fixed-bed reactor of shown process I, and the upper and lower parts of the reactor are filled with porcelain balls respectively. First, continuously enter benzene into the reactor, raise the temperature to 190°C, and control the pressure at 3.0Mpa. -1 Under the condition, the raw materials are added into the reactor according to the molar ratio of benzene and cyclohexene of 12:1 for continuous reaction. Take the sample of the top effluent of the reactor and analyze the product composition with Shimadzu 2010 gas chromatography equipped with 50m×0.25mm capillary column and FID detector. The conversion rate of cyclohexene reaches 100%, and the selectivity of cyclohexylbenzene can reach 91.8 %, the selectivity of cyclohexylation is 95.2%, and the selectivity of methylcyclopentylbenzene is 4.5%. The lifetime of the catalyst is 1015h (the time when the conversion of cyclohexene is greater than...
Embodiment 2
[0050] exist figure 2 The catalyst containing MCM-22 molecular sieve is loaded into the fixed-bed reactor of shown process I, and the upper and lower parts of the reactor are filled with porcelain balls respectively. First, continuously enter benzene into the reactor, raise the temperature to 190°C, and control the pressure at 3.0Mpa. -1 Under the condition, the raw materials are added into the reactor with the molar ratio of benzene and cyclohexene being 12:1 and the molar ratio of cyclohexane and cyclohexene being 1:1 for continuous reaction. Take the sample of the reactor top effluent and analyze the product composition with a Shimadzu 2010 gas chromatograph equipped with a 50m × 0.25mm capillary column and FID detector. The conversion rate of cyclohexene reaches 100%, and the selectivity of cyclohexylbenzene can reach 91.5 %, the selectivity of cyclohexylation is 95.8%, and the selectivity of methylcyclopentylbenzene is 4.0%. The life of the catalyst is more than 2000 h...
Embodiment 3
[0054] exist figure 2 The catalyst containing MCM-22 molecular sieve is loaded into the fixed-bed reactor of shown process I, and the upper and lower parts of the reactor are filled with porcelain balls respectively. First, continuously enter benzene into the reactor, raise the temperature to 190°C, and control the pressure at 3.0Mpa. -1 Under the condition, the raw materials are added into the reactor for continuous reaction according to the molar ratio of benzene to cyclohexene of 12:1 and the molar ratio of cyclohexane to cyclohexene of 2:1. Take the sample of the top effluent of the reactor and analyze the product composition with Shimadzu 2010 gas chromatography equipped with 50m×0.25mm capillary column and FID detector. The conversion rate of cyclohexene reaches 100%, and the selectivity of cyclohexylbenzene can reach 91.2 %, the selectivity of cyclohexylation is 95.1%, and the selectivity of methylcyclopentylbenzene is 4.3%. The life of the catalyst is more than 2000...
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