Ga、Co双金属ZSM-5沸石催化剂制备及催化乙烷氧化脱氢制乙烯性能
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1.中国科学院上海高等研究院 二氧化碳光子科学研究中心;2.西南石油大学 化学化工学院

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中国科学院前瞻战略先导专项


Preparation of gallium-cobalt bimetallic ZSM-5 zeolite catalyst and its catalytic performance for ethane oxidative dehydrogen to ethylene
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1.Center for Carbon Dioxide Photon Science,Key Laboratory of Low-Carbon Conversion Science and Engineering,Shanghai Advanced Research Institute,Chinese Academy of Sciences;2.School of Chemistry and Chemical Engineering,Southwest Petroleum University

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Strategic Priority Research Program of the Chinese Academy of Science

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    摘要:

    以低硅铝比〔n(Si)/n(Al)=10〕的NaZSM-5沸石(简称ZSM-5)为载体,采用离子交换法制备了Ga、Co双金属ZSM-5沸石催化剂(GaxCoZ5,其中x%为Ga实测质量分数),并将其用于CO2介导的C2H6氧化脱氢反应(CO2-ODH)。采用XRD、BET、TEM、XPS、NH3-TPD和CO2-TPD对GaxCoZ5的结构组成、微观形貌、织构参数、酸性和CO2吸附性能进行表征和测试,基于CO2-ODH的C2H6转化率、C2H4收率和选择性结果,考察了Ga质量分数对GaxCoZ5催化性能的影响,分析GaxCoZ5催化C2H6氧化脱氢反应的反应网络,推测其催化反应机理。结果表明,GaxCoZ5在CO2-ODH反应中,Co2+为主要活性组分,Co的引入可以提高催化性能,与ZSM-5载体相比,CoZ5的乙烷转化率从20%提升到36%,乙烯产率从11%升到26%。Ga的引入有助于利用CO2消除积炭,增强催化剂的稳定性,与未引入Ga的CoZ5相比,引入Ga的GaxCoZ5整体酸性增强,相同反应条件下乙烷转化率和乙烯产率下降,但是催化剂的稳定性得到提升;Ga质量分数0.26%、Co质量分数1.03%的Ga0.26CoZ5表现出最佳的催化性能,反应340min后,C2H4产率仍保持20%,选择性接近100%。Ga质量分数为0~1.35%时,反应以乙烷间接氧化脱氢为主;当Ga质量分数为2.65%时,反应以乙烷干重整为主。反应后Ga0.26CoZ5的积炭量仅约为1%,Ga可以活化CO2,使CO2利用反向Boudouard反应来消除积炭。

    Abstract:

    Using NaZSM-5 zeolite with a low silica-to-alumina ratio 〔n(Si)/n(Al)=10〕 as the support, a Ga and Co bimetallic-modified catalyst, denoted as GaxCoZ5, was prepared via the ion-exchange method and applied to the CO2-mediated oxidative dehydrogenation of ethane (CO2-ODH). The structural composition, microscopic morphology, textural parameters, acidity, and CO2 adsorption properties of GaxCoZ5 were characterized and tested using techniques such as XRD, BET, TEM, XPS, NH3-TPD, and CO2-TPD. Based on the results of ethane conversion, ethylene yield, and selectivity in the CO2-ODH reaction, the influence of the Ga mass fraction on the catalytic performance of GaxCoZ5 was investigated. The reaction network for the oxidative dehydrogenation of ethane over GaxCoZ5 was analyzed, and its catalytic reaction mechanism was proposed. The results indicate that in the CO2-ODH reaction, Co2+ serves as the primary active component, and the introduction of Co enhances the catalytic performance. Compared with the ZSM-5 support, the ethane conversion rate of CoZ5 increases from 20% to 36%, and the ethylene yield rises from 11% to 26%. The incorporation of Ga facilitates the utilization of CO2 to eliminate coke deposition, thereby enhancing the catalyst"s stability. In comparison with CoZ5 without Ga, the overall acidity of Ga-introduced GaxCoZ5 increases, leading to a decrease in ethane conversion and ethylene yield under the same reaction conditions; however, the catalyst"s stability is improved. Ga0.26CoZ5, with a Ga mass fraction of 0.26% and a Co mass fraction of 1.03%, exhibits the best catalytic performance, maintaining an ethylene yield of 20% and a selectivity close to 100% after 340 minutes of reaction. When the Ga mass fraction ranges from 0% to 1.35%, the reaction primarily proceeds via indirect oxidative dehydrogenation of ethane. However, when the Ga mass fraction increases to 2.65%, the main reaction shifts to ethane dry reforming. The coke deposition on Ga0.26CoZ5 after the reaction is only about 1%. Ga can activate CO2, enabling its utilization in the Reverse Boudouard reaction to eliminate coke during the reaction.

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温皓珏,韩欣茹,张莉娜,陈永东,魏伟,孙楠楠. Ga、Co双金属ZSM-5沸石催化剂制备及催化乙烷氧化脱氢制乙烯性能[J].精细化工,2026,43(4):

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