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Frontiers of Chemical Science and Engineering

ISSN 2095-0179

ISSN 2095-0187(Online)

CN 11-5981/TQ

邮发代号 80-969

2019 Impact Factor: 3.552

Frontiers of Chemical Science and Engineering  2022, Vol. 16 Issue (3): 384-396   https://doi.org/10.1007/s11705-021-2045-y
  本期目录
Alkylation of benzene with carbon dioxide to low-carbon aromatic hydrocarbons over bifunctional Zn-Ti/HZSM-5 catalyst
Xiangyu Liu1, Yanling Pan2, Peng Zhang1, Yilin Wang1, Guohao Xu1, Zhaojie Su1, Xuedong Zhu1(), Fan Yang1()
1. Engineering Research Center of Large-Scale Reactor Engineering and Technology, Ministry of Education, East China University of Science and Technology, Shanghai 200237, China
2. Department of Product Engineering, School of Chemical Engineering, East China University of Science and Technology, Shanghai 200237, China
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Abstract

Alkylation of benzene to value-added, high octane number and low toxic toluene and xylenes provides a way to lower benzene content in gasoline pool, and is hence a method to promote fuel quality. On the other hand, CO2 accumulation in the atmosphere causes global warming and requires effective route for its valorization. Utilization of CO2 as a carbon source for benzene alkylation could achieve both goals. Herein, alkylation of benzene with CO2 and H2 was realized by a series of low-cost bifunctional catalysts containing zinc/titanium oxides (Zn/Ti oxides) and HZSM-5 molecular sieves in a fixed-bed reactor. By regulating and controlling oxygen vacancies of Zn/Ti oxides and the acidities of HZSM-5, benzene conversion and CO2 conversion reached 28.7% and 29.9% respectively, along with a total selectivity of toluene and xylene higher than 90%. In this process, more than 25% CO2 was effectively utilized and incorporated into the target products. Moreover, the mechanism of the reaction was analyzed and the course was simultaneously traced. CO2 was transformed into methanol firstly, and then methanol reacted with benzene generating toluene and xylene. The innovation provides a new method for upgrading of fuels and upcycling the emissions of CO2, which is of great environmental and economic benefits.

Key wordscarbon dioxide    benzene    alkylation    bifunctional catalyst    mechanism
收稿日期: 2020-11-19      出版日期: 2022-02-24
Corresponding Author(s): Xuedong Zhu,Fan Yang   
 引用本文:   
. [J]. Frontiers of Chemical Science and Engineering, 2022, 16(3): 384-396.
Xiangyu Liu, Yanling Pan, Peng Zhang, Yilin Wang, Guohao Xu, Zhaojie Su, Xuedong Zhu, Fan Yang. Alkylation of benzene with carbon dioxide to low-carbon aromatic hydrocarbons over bifunctional Zn-Ti/HZSM-5 catalyst. Front. Chem. Sci. Eng., 2022, 16(3): 384-396.
 链接本文:  
https://academic.hep.com.cn/fcse/CN/10.1007/s11705-021-2045-y
https://academic.hep.com.cn/fcse/CN/Y2022/V16/I3/384
Fig.1  
Fig.2  
Fig.3  
Sample ABET1
/(m2?g?1)
Vpore
/(mL?g?1)
Dporea)
/nm
Zn/Ti ratio b) Sample ABET2
/(m2?g?1)
Vpore
/(mL?g?1)
Dporea)
/nm
ΔAc)
/(m2?g?1)
Surface Bulk
TiO2 22 0.16 3.98 0 0 TiO2-HZ5 180 0.23 1.82 158
Zn0.01Ti 45 0.20 3.81 0.04 0.01 Zn0.01Ti-HZ5 183 0.29 1.82 138
Zn0.1Ti 63 0.33 2.91 0.25 0.11 Zn0.1Ti-HZ5 184 0.29 1.84 121
Zn0.3Ti 104 0.24 5.75 n.dd) 0.34 Zn0.3Ti-HZ5 225 0.33 1.82 121
Zn0.5Ti 151 0.30 5.02 n.dd) 0.54 Zn0.5Ti-HZ5 244 0.29 1.83 93
Zn1.0Ti 115 0.28 5.04 0.96 1.05 Zn1.0Ti-HZ5 202 0.27 1.82 87
ZnO 40 0.02 8.02 ZnO-HZ5 142 0.14 1.84 102
γ-Al2O3 176 0.31 2.65 n.dd) n.dd) HZSM-5 313 0.14 1.84 n.dd)
Tab.1  
Fig.4  
Fig.5  
Fig.6  
Catalyst Conversion/% Selectivity/% Phenyl ring yield b)
/%
Benzene Toluene Xylene EBZ c) C9+ PX/X d)
TiO2-HZ5(30) 1.1 86.0 6.8 4.5 2.7 24.4 99.8
Zn0.01Ti-HZ5(30) 8.4 88.5 6.7 2.7 2.1 24.5 98.3
Zn0.1Ti-HZ5(30) 23.8 77.4 16.1 2.8 3.7 24.4 94.9
Zn0.3Ti-HZ5(30) 22.4 76.0 18.2 2.1 3.7 25.1 95.1
Zn0.5Ti-HZ5(30) 16.8 80.4 11.0 3.6 5.0 23.9 96.4
Zn1.0Ti-HZ5(30) 15.2 79.2 11.4 5.0 4.4 24.5 96.7
ZnO-HZ5(30) 13.5 81.3 6.7 5.6 6.5 24.4 97.0
HZSM-5(30) 1.3 86.8 4.7 8.3 0.2 23.1 99.7
Tab.2  
Catalyst CO2 Conv/% Selectivity of product/% CO2 efficiency/% b)
CO CH4 C2 C3 C4+ EBZ+ C9+
TiO2-HZ5(30) 12.0 29.7 60.2 2.7 4.6 0.0 0.4 2.3
Zn0.01Ti-HZ5(30) 23.9 31.4 47.0 3.6 7.0 0.9 1.1 9.0
Zn0.1Ti-HZ5(30) 25.7 35.0 21.7 2.6 8.5 3.0 3.8 25.4
Zn0.3Ti-HZ5(30) 27.5 50.0 14.1 2.5 7.1 3.9 2.9 21.4
Zn0.5Ti-HZ5(30) 28.9 55.5 12.5 1.4 7.3 5.1 3.2 14.9
Zn1.0Ti-HZ5(30) 30.3 59.8 5.7 1.9 9.6 7.3 2.93 12.8
ZnO-HZ5(30) 21.9 62.9 3.1 1.1 8.9 4.8 4.7 14.6
Tab.3  
Fig.7  
Catalyst Conversion/% Selectivity/% Phenyl ring yield/% b)
Benzene Toluene Xylene EBZ C9+ PX/X
Zn0.1Ti-HZ5(13.5) 28.7 72.9 17.6 4.6 4.9 25.0 93.6
Zn0.1Ti-HZ5(30) 23.8 77.4 16.1 2.8 3.7 24.4 94.9
Zn0.1Ti-HZ5(100) 8.6 90.7 7.7 0.6 1.0 26.7 98.3
Tab.4  
Catalyst CO2 Conv./% Selectivity of products/% CO2
efficiencyb)/%
CO CH4 C2 C3 C4+ EBZ+ C9+
Zn0.1Ti-HZ5(13.5) 29.9 39.6 10.1 2.9 11.5 4.2 5.8 25.9
Zn0.1Ti-HZ5(30) 25.7 35 21.7 2.6 8.5 3.0 3.8 25.4
Zn0.1Ti-HZ5(100) 25.3 55.3 34.5 0.5 0.2 0.1 0.4 9
Tab.5  
Fig.8  
Fig.9  
Fig.10  
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