Method for preparing catalyst for compounding p-diethylbenzene by alkylation reaction of ethylbenzene and ethane or alcohol

A diethylbenzene catalyst, ethanol alkyl technology, applied in physical/chemical process catalysts, molecular sieve catalysts, chemical instruments and methods, etc., can solve the problems of low utilization rate of ethanol, high energy consumption for preparation, unfavorable industrialization, etc. high yield, simple preparation process and low cost of raw materials

Active Publication Date: 2010-01-06
SHANGHAI NOVEL CHEM TECH
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Problems solved by technology

But for HZSM-5 itself, its acid centers are dominated by strong acids, and the strong acid centers are all over the inner and outer surfaces of the catalyst: in addition, its pore size is slightly larger. If it is directly used as a p-diethylbenzene catalyst, a large number of isomers will be produced, making p-diethylbenzene Diethylbenzene has poor selectivity, so it is often necessary to modify its composition and pores
[0004] Chinese patent CN200410020397.7 adopts the alkylation reaction of ethylbenzene and ethanol to synthesize p-diethylbenzene, and SiO 2 /Al 2 o 3 =100 HZSM-5 molecular sieve is used as the matrix, and the surface acidity and pore structure of the molecular sieve are adjusted with components such as boron, magnesium and cobalt. In 10 hours, although the selectivity to diethylbenzene was close to 100%, the initial activity of ethylbenzene was not high, so that the yield of diethylbenzene was only 14%; and the mol ratio of ethylbenzene and ethanol reached 2: 1, so that Ethanol is less efficient
Chinese patent CN90101436.2 adopts the reaction of ethylbenzene and ethanol, and HZSM-5 molecular sieves are respectively modified with aluminum, magnesium and other components and then roasted. The highest conversion rate of ethylbenzene is only 10%, and the selectivity to diethylbenzene between 95% and 98%; the conversion rate of ethylbenzene in U.S. Patent No. 5,811,613 is 8%, and the selectivity of p-diethylbenzene is between 97% and 98%. The reaction yields in the above two patents are all low, which is unfavorable for ...

Method used

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  • Method for preparing catalyst for compounding p-diethylbenzene by alkylation reaction of ethylbenzene and ethane or alcohol
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  • Method for preparing catalyst for compounding p-diethylbenzene by alkylation reaction of ethylbenzene and ethane or alcohol

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1-4

[0014] Weigh a portion of extruded, SiO 2 / Al 2 o 3 Mole ratio = 55 HZSM-5 molecular sieve, add 1.6 parts by mass of cyclohexane solution containing ethyl orthosilicate, so that the silicon dioxide obtained after the decomposition of ethyl orthosilicate accounts for 5% to 30% of the mass of the catalyst, at room temperature After stirring and impregnating for 12 hours, cyclohexane was recovered by distillation and the catalyst was dried; then, air and water vapor were passed through at 650°C for 3 hours to passivate, and the air volume space velocity was controlled to 3000h -1 , water vapor volume space velocity 65h -1 , to prepare catalysts A1-A4.

[0015] The obtained catalyst is used in the alkylation reaction of ethylbenzene and ethylene (or ethanol), and the reaction conditions are as follows: normal pressure reaction, temperature 360-380°C, total space velocity of raw material liquid mass 3-7h -1 , The molar ratio of ethylbenzene to ethylene (or ethanol) is 2:1 to 6:...

Embodiment 5

[0023] The calcination passivation temperature of Example 2 was adjusted to 650, 700 and 750° C., and the obtained catalysts were named B1, B2 and B3 in sequence. The reaction results are shown in Table 3.

[0024] Table 3 Effects of different roasting and passivation conditions on the performance of ethylphenylethanol alkylation

[0025]

[0026] Reaction conditions: normal pressure, 360°C, total space velocity of raw material liquid mass 5h -1 , ethylbenzene / ethanol molar ratio 4:1, reacted for 1 hour.

Embodiment 6

[0028] The optimized catalyst B2 was obtained through the above examples, and the results of the alkylation reaction of ethylbenzene and ethylene using it as the catalyst are shown in Table 4; the catalytic performance of the alkylation reaction of ethylbenzene and ethanol is shown in Table 5.

[0029] Table 4 Ethylbenzene and ethylene alkylation reaction performance of B2 catalyst

[0030]

[0031]

[0032] Reaction conditions: normal pressure, total space velocity of raw material liquid mass 5h -1 , ethylbenzene / ethylene molar ratio 4.4:1.

[0033] Table 5 Ethylbenzene and ethanol alkylation reaction performance of B2 catalyst

[0034]

[0035] Reaction conditions: normal pressure, total space velocity of raw material liquid mass 5h -1 , ethylbenzene / ethanol molar ratio 4.4:1.

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Abstract

The invention relates to a method for preparing catalyst for compounding p-diethylbenzene by the alkylation reaction of ethylbenzene and ethane or alcohol, and the obtained catalyst can be used for compounding p-diethylbenzene by the alkylation reaction of ethylbenzene and ethane or compounding p-diethylbenzene by the alkylation reaction of the ethylbenzene and alcohol. The catalyst is formed in such a way that an HZSM-5 molecular sieve of SiO2/Al2O3 molar ratio=16-200 as a matrix to be loaded with silicon dioxide and then roasted and passivated by air and water vapor. The preparation of the catalyst only needs three-step operation; and compared with the prior method for preparing the similar catalyst, the invention greatly simplifies the preparation process. The method does not need to add other substances to further modify the HZSM-5 molecular sieve, thereby having low raw material cost and production energy consumption as well as less environmental pollution and obtaining favorable p-diethylbenzene selectivity and yield.

Description

technical field [0001] The invention relates to a preparation method of a modified HZSM-5 catalyst, which can be used in the alkylation reaction of ethylbenzene and ethylene, or the alkylation reaction of ethylbenzene and ethanol to synthesize p-diethylbenzene. The preparation method has the advantages of simple operation, low cost, less environmental pollution, high single-pass yield of p-diethylbenzene, high selectivity and the like. Background technique [0002] P-diethylbenzene is an essential analytical agent in the process of adsorption and separation of p-xylene, and its synthesis has very important social benefits and practical value. The industry requirement for p-diethylbenzene as a p-xylene desorbent is that its purity is greater than 95%. However, due to the similar boiling points of p-diethylbenzene, o-diethylbenzene and m-diethylbenzene, the rectification method is used to purify p-diethylbenzene products from mixed diethylbenzene (p-diethylbenzene content 30%...

Claims

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Application Information

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IPC IPC(8): B01J29/40C07C15/02C07C2/66C07C2/88
Inventor 文怀有许宁刘子玉蔡永玲谈赟
Owner SHANGHAI NOVEL CHEM TECH
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