Fluidized catalytic method of p-xylene by methylation of aromatic hydrocarbon
A p-xylene and fluidized catalysis technology, which is applied in the fields of condensation between hydrocarbons and non-hydrocarbons, organic chemistry, bulk chemical production, etc., can solve the problem of high temperature rise of the reaction bed, low utilization rate, and poor catalyst stability And other issues
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Embodiment 1~4
[0028] According to the steps and conditions described in Comparative Example 1, the aromatic hydrocarbon methylation reaction was carried out, wherein the pure toluene feed was replaced by a mixture of benzene and toluene, and dimethyl ether was used as an alkylating agent instead of methanol. The molar ratio of dimethyl ether to aromatic hydrocarbon is 0.25. The specific reaction conditions and evaluation results are listed in Table 1 for comparison.
[0029] Table 1
[0030]
[0031] The data in Table 1 show that, compared with methanol, the use of dimethyl ether as an alkylating agent significantly reduces the temperature rise of the catalyst bed. Using benzene and toluene as the mixed aromatics feed, although it has no effect on the control of the temperature rise of the catalyst bed, the side reaction of methanol itself and the deep alkylation reaction are still obviously suppressed, and the methyl utilization rate and xylene selectivity Significantly increased, p-x...
Embodiment 5~8
[0033] The aromatic hydrocarbon methylation reaction was carried out according to the steps and conditions described in Example 3, and the molar ratio of dimethyl ether to aromatic hydrocarbon feed was changed. The specific reaction conditions and evaluation results were listed in Table 2 for comparison.
[0034] Table 2
[0035]
[0036] The data in Table 2 shows that the amount of alkylating agent has a great influence on various performance indicators. The larger the amount is, the higher the conversion of aromatics is, but the worse the product selectivity and methyl utilization are.
Embodiment 9~14
[0038] The aromatic hydrocarbon methylation reaction was carried out according to the steps and conditions described in Example 3, and the reaction temperature, space velocity, hydrogen / aromatic hydrocarbon molar ratio and reaction pressure were adjusted. The specific reaction conditions and evaluation results were listed in Table 3 for comparison.
[0039] table 3
[0040]
[0041] The data in Table 3 shows that the alkylation reaction conditions have a great influence on the product distribution, and also have an influence on the temperature rise of the catalyst bed. Through the above process optimization, the selectivity of xylene can be raised up to 91.67%, the selectivity of p-xylene can be up to 88.17%, the utilization rate of methanol can be up to 78.89%, and the temperature rise can be as low as 17.5°C.
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