Fluidized catalytic method for toluene methylation
A technology of toluene methylation and fluidized catalysis is applied in the field of fluidized catalysis of toluene methylation, and can solve the problems of low utilization rate of methanol, many side reactions, large temperature rise of catalyst bed and the like
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Embodiment 1
[0029] Alkylation reagent methanol first enters the fixed bed reactor to contact with the dehydration catalyst, the reaction conditions are: methanol feed temperature 260°C, weight space velocity 2.0h -1 , the reaction pressure is 0.5MPa, and the catalyst loading is 696 grams. The specific composition of the catalyst is shown in Table 1, and the mixed effluent I containing dimethyl ether, water and unreacted methanol is generated; the toluene raw material and the reaction effluent I are mixed and vaporized to obtain Reaction mixture II then enters a fluidized bed reactor to contact with a methylation catalyst, the reaction conditions are: catalyst loading 2000 g, feeding temperature 400 ° C, aromatics weight space velocity 4.0 h -1 , the molar ratio of methanol to aromatics is 0.5, no hydrogen is present, the reaction pressure is 0.5MPa, and the alkylation catalyst used contains 20% by weight of Al 2 o 3 modifier and 15% SiO 2 Modifier, residual weight is hydrogen type ZSM-5...
Embodiment 2~4
[0031] The methylation reaction was carried out according to the steps and conditions described in Example 1, and different methanol dehydration catalysts were selected. The specific composition of the catalysts is shown in Table 1. The reaction evaluation results are listed in Table 1 for comparison.
[0032] Table 1
[0033]
[0034] The data in Table 1 shows that the pre-dehydration of methanol, the alkylation reagent, effectively controls the exothermicity of the alkylation process and the temperature rise of the catalyst bed, making the xylene selectivity and p-xylene selectivity significantly improved, and the utilization rate of methanol It is also slightly improved, and the conversion rate of aromatics has a small change.
Embodiment 5~7
[0036] The methylation reaction was carried out according to the steps and conditions described in Example 2, wherein the loading amount of the methanol dehydration catalyst was changed to 232 grams, and the dehydration reaction conditions were changed. The specific reaction conditions and evaluation results are listed in Table 2.
[0037] Table 2
[0038]
[0039] The data in Table 2 shows that the change of the methanol dehydration process will affect the conversion of methanol, and thus affect the control effect of the temperature rise of the alkylation. The higher the methanol dehydration conversion rate, the better the reaction result.
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