Preparation method and application of catalyst for producing mixed propylbenzene through alkylation of benzene and C4 olefin

A carbon tetraolefin and catalyst technology, which is applied to the catalyst and the preparation field of the aforementioned method, can solve the problems of poor selectivity, unstable catalyst and the like, and achieves the effects of fast reaction speed and high olefin conversion rate

Pending Publication Date: 2022-07-19
洛阳市科创石化科技开发有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The invention patent with the publication number CN103102240A relates to a synthesis method of sec-butylbenzene, which uses carbon tetralinear organic compounds and benzene to undergo an alkylation reaction at a temperature of 100-280°C and a pressure of 1.0-6.0MPa to synthesize sec-butylbenzene. It mainly solves the problem of unstable catalyst and poor selectivity in molecular sieves existing in the prior art

Method used

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  • Preparation method and application of catalyst for producing mixed propylbenzene through alkylation of benzene and C4 olefin
  • Preparation method and application of catalyst for producing mixed propylbenzene through alkylation of benzene and C4 olefin
  • Preparation method and application of catalyst for producing mixed propylbenzene through alkylation of benzene and C4 olefin

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0032] Get 75 grams of HZSM-5 zeolite powder (produced by Qi Chuang Chemical Co., Ltd., the same below) with a molar ratio of silica / alumina of 45, 33.55 grams of aluminum hydroxide powder (produced by Yuneng Catalytic Company, and the content of alumina on a dry basis is 74.5% by mass) , the same below), an appropriate amount of 5wt% nitric acid solution is kneaded, extruded into strips, dried at 120°C for 4 hours, and calcined at 550°C for 4 hours. The composition of the prepared contrast agent A is shown in Table 1.

Embodiment 2

[0034] Get 60 grams of HZSM-5 zeolite powder with a silica / alumina mol ratio of 45 and 15 grams of Hβ zeolite powder with a silica / alumina mol ratio of 50 (produced by Qi Chuang Chemical Company, the same below), 33.55 grams of aluminum hydroxide The powder was kneaded with an appropriate amount of 5wt% nitric acid solution, extruded into strips, dried at 120°C for 4 hours, and calcined at 550°C for 4 hours. The calcined catalyst was immersed in 120 mL (6.5 wt% lanthanum nitrate and 4.26 wt% ammonium dihydrogen phosphate) mixed solution for 8 hours, drying at 120°C for 4 hours, and calcining at 550°C for 4 hours. The composition of the prepared catalyst B is shown in Table 1.

Embodiment 3

[0036]Take 43.5 grams of HZSM-5 zeolite powder with a silica / alumina molar ratio of 45, 8.25 grams of Hβ zeolite powder with a silica / alumina mol ratio of 50, and 8.25 grams of MCM-22 with a silica / alumina mol ratio of 45 Zeolite powder (produced by Qi Chuang Chemical Co., Ltd., the same below), 53.69 grams of aluminum hydroxide powder, and an appropriate amount of 5wt% nitric acid solution were kneaded, extruded into strips, dried at 120°C for 4 hours, and calcined at 550°C for 4 hours. The composition of the prepared catalyst C is shown in Table 1.

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Abstract

The preparation method of the catalyst comprises the following steps: mixing at least one zeolite with a binder, adding water and a peptizing agent, kneading, extruding and molding, and then sequentially drying and roasting, finally, the roasted catalyst is subjected to metal or nonmetal oxide modification through an impregnation method, and the required catalyst is obtained. According to the present invention, benzene and C4 olefin are adopted as reaction raw materials, the catalyst obtained by using the preparation method is adopted to catalyze the reaction of benzene and butene so as to generate the target product mixed propylbenzene, the reaction can be performed under the mild reaction condition, the reaction speed is high, and the olefin conversion rate is high. Through measurement, under the conditions that the reaction temperature is 360 DEG C, the reaction pressure is 0.8 MPa, the total weight hourly space velocity is 5.0 h <-1 > and the molar ratio of benzene to alkene is 5.5: 1, the conversion rate of C4 olefin reaches 99.8%, the selectivity of the product mixed propylbenzene reaches 72.6%, the proportion of isopropyl benzene in the mixed propylbenzene is 52.69%, and the proportion of n-propylbenzene in the mixed propylbenzene is 47.31%.

Description

technical field [0001] The invention relates to a method for producing mixed propylbenzene by alkylation of benzene and carbon tetraolefin, and also relates to a catalyst applied to the aforementioned method and a preparation method thereof. Background technique [0002] With the rapid development of petroleum refining and coal chemical industry, the output of C4 in my country has increased year by year, but the amount of fine chemical utilization of C4 fraction in my country is very small, and the effective chemical utilization rate is very low, resulting in huge waste of resources. Therefore, the comprehensive utilization of the by-product mixed C4 is an important subject of petrochemical technology research and process development at home and abroad. [0003] With the advent of my country's "Great Refining and Chemical Era", thanks to the liberalization of domestic crude oil import quotas, refining and chemical enterprises have put into operation one after another, result...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J29/40B01J29/80C07C2/66C07C15/085C07C15/02
CPCB01J29/405B01J29/80C07C2/66B01J29/7057B01J29/7088B01J29/7007B01J29/7038C07C15/085C07C15/02
Inventor 滕刘中龚旭辉马余璐史杰雷王银亮娄青青李宗杰李海洋王近近
Owner 洛阳市科创石化科技开发有限公司
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