4.8 Article

Rationally Designing Bifunctional Catalysts as an Efficient Strategy To Boost CO2 Hydrogenation Producing Value-Added Aromatics

Journal

ACS CATALYSIS
Volume 9, Issue 2, Pages 895-901

Publisher

AMER CHEMICAL SOC
DOI: 10.1021/acscatal.8b01344

Keywords

CO2 conversion; aromatics synthesis; bifunctional catalysts; tandem process; single pass

Funding

  1. JST-ACT-C project of the Japan Science and Technology Agency, Japan [JPMJCR12YT]
  2. JST-MIRAI project of the Japan Science and Technology Agency, Japan [JPMJMI17E2]
  3. National Natural Science Foundation of China [91645113, U1510110]
  4. Key Research Program of Frontier Sciences, CAS [QYZDB-SSW-JSC043]

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The efficient conversion of CO2 to useful chemicals is a promising way to reduce atmospheric CO2 concentration and also reduce reliance on fossil-based resources. Although much progress has been made toward the production of basic chemicals, like methanol, through CO2 hydrogenation, the direct conversion of CO2 to value-added aromatics, especially p-xylene (PX), is still a great challenge due to the inert nature of CO2 and high barrier for C-C coupling. Herein, a bifunctional catalyst composed of Cr2O3 and H-ZSM-5 zeolite (Cr2O3/H-ZSM-5) was designed for the direct conversion of CO2 to aromatics. Due to the concertedly synergistic effect between the two components in this bifunctional catalyst, aromatics selectivity of, similar to 76% at CO2 conversion of 34.5% was achieved, and there was no catalyst deactivation after 100 h of long-term stability testing. Moreover, a modified bifunctional catalyst Cr2O3/H-ZSM-5@S-1 (silicalite-1) consisting of a core-shell structured H-ZSM-5@S-1 zeolite capsule component was proposed to realize the target synthesis of BTX (benzene, toluene, and xylene), especially PX. The precise suppression of undesired side reactions was accomplished on Cr2O3/H-ZSM-5@S-1 because neutralizing acidic sites at outer surface of H-ZSM-5 by S-1 stopped isomerization of PX to o- or m-xylene as well as other side reactions. Consequently, the fractions of BTX and PX in aromatics products were increased from 13.2% and 7.6% to 43.6% and 25.3%, respectively, with almost unchanged catalyst activity and total aromatics selectivity.

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