Method for producing p-tert-Butyltoluene by using mordenite for catalyzing toluene and tertiary butanol
A technology of p-tert-butyltoluene and mordenite, which is applied in the field of production of p-tert-butyltoluene, can solve problems such as environmental pollution, low yield, and corrosion of equipment, and achieve the effect of overcoming corrosion of equipment
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Embodiment 1
[0012] Reaction conditions: the molar ratio of raw materials is 1:4 (toluene: tert-butanol), and the volumetric liquid space velocity is 2 ml / g cat ·H, the catalyst is a mordenite molecular sieve catalyst that has been activated at 550°C for 3 hours. The gas-solid phase continuous reaction is carried out at different reaction temperatures for 10 hours. The results are shown in Table 1.
[0013] Attached Table 1 Catalytic performance at different reaction temperatures
[0014]
Embodiment 2
[0016] Reaction conditions: reaction temperature is 180°C, raw material molar ratio (toluene: tert-butanol) 1:4, catalyst is mordenite molecular sieve catalyst activated at 550°C for 3 hours, and different liquid space velocities are used for continuous gas-solid reaction 10 hours, the results are shown in Table 2.
[0017] Attached Table 2 Catalytic performance under different liquid space velocity
[0018]
Embodiment 3
[0020] Reaction conditions: feed space velocity 4 ml / g cat ·H. The reaction temperature is 180°C. The catalyst is a mordenite molecular sieve catalyst that has been activated at 550°C for 3 hours. Different raw material ratios (toluene: tert-butanol) are used for continuous gas-solid reaction for 10 hours. The results are shown in Table 3.
[0021] Attached Table 3 Catalytic performance under different toluene / tert-butanol ratios
[0022]
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