A method for removing olefins in aromatics raw materials
A technology for aromatic hydrocarbons and raw materials, applied in the field of removing olefins in aromatic hydrocarbon raw materials
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[0025] According to a preferred embodiment of the present invention, based on the total amount of the alkyl-substituted arene, the content of the methyl-substituted arene is not less than 75% by weight, preferably 85-99.9% by weight.
[0026] According to a preferred embodiment of the present invention, based on the total amount of the alkyl-substituted arene, the content of the propyl-substituted arene is not higher than 5% by weight, preferably 0-2% by weight.
[0027] The inventors of the present invention found that controlling the content of ethyl-substituted aromatic hydrocarbons, methyl-substituted aromatic hydrocarbons, and propyl-substituted aromatic hydrocarbons in the alkyl-substituted aromatic hydrocarbons is more conducive to further prolonging the service life of the catalyst.
[0028] According to a preferred embodiment of the present invention, in the aromatic hydrocarbon raw material, the colloid content is not more than 200mg / 100mL, preferably not more than 12...
Embodiment 1
[0081] The method for removing olefins in the aromatics raw material is carried out in a fixed-bed reactor, and the loading amount of the catalyst is 1 g. Under the alkylation reaction conditions, the catalysts A, B and C are respectively contacted with the raw material 1 and the raw material 2 for reaction, wherein, Alkylation reaction conditions include: the temperature is 180°C, the reaction pressure is 2.0MPa by gauge pressure, and the mass space velocity of the raw material is 3.0h -1 .
[0082] The preparation method of catalyst A comprises: get 50g commercially available MCM-22 powder samples (commercially purchased from Nanjing Xianfeng Nano Material Technology Co., Ltd., trade mark is XFF09, SiO 2 / Al 2 o 3 The molar ratio is 27) mixed with 15g of alumina, then added 18g of 5% by weight nitric acid and kneaded, then extruded on the extruder to form a strip of Φ1.6 × 2 mm, dried at 120 ° C, and passed through Ammonium nitrate with a mass concentration of 5% is excha...
Embodiment 2
[0091] Xylene is used to dilute the raw material 3, and after dilution, it is filtered to reduce the colloid content to 90mg / 100ml. In the obtained raw material 4, based on the total amount of the alkyl-substituted aromatic hydrocarbons, the methyl-substituted aromatic hydrocarbons The content was 85.2% by weight, the ethyl-substituted arene content was 12.9% by weight, and the propyl-substituted arene content was 1.9% by weight. According to the method of Example 1, the difference is that raw material 1 is replaced by raw material 4, that is, catalysts A, B and C are contacted with raw material 4 for reaction. The result of reaction 24h is listed in Table 2, and the result of reaction 240h is listed in Table 3.
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