催化学报 ›› 2026, Vol. 88: 322-334.DOI: 10.1016/S1872-2067(26)65101-7

• 论文 • 上一篇    下一篇

催化微环境调控促进高效CO2捕集与原位乙烷氧化脱氢制乙烯

高梓皓a,1, 黄凯b,1, 徐庆玲a, 王鑫a, 刘志成c, 邵斌a,*(), 胡军a,*()   

  1. a 华东理工大学化学与分子工程学院, 绿色化工与工业催化国家重点实验室, 上海 200237
    b 台州学院药学与化学工程学院, 浙江台州 318000
    c 中国石化上海石油化工研究院, 绿色化工与工业催化国家重点实验室, 上海 201208
  • 收稿日期:2025-12-16 接受日期:2026-02-13 出版日期:2026-09-18 发布日期:2026-09-05
  • 通讯作者: *电子信箱: junhu@ecust.edu.cn (胡军),
    shaobin@ecust.edu.cn (邵斌).
  • 基金资助:
    国家自然科学基金(22278126);国家自然科学基金(22408095);国家自然科学基金(22250005);中国博士后创新人才支持计划(BX20240116);中国博士后科学基金(2023M741170);国家重点研发计划(2024YFA1509801);中央高校基本科研业务费.

Engineering catalytic microenvironments for enhancing ethylene production in CO2 capture and in-situ oxidative dehydrogenation of ethane

Zihao Gaoa,1, Kai Huangb,1, Qingling Xua, Xin Wanga, Zhicheng Liuc, Bin Shaoa,*(), Jun Hua,*()   

  1. a State Key Laboratory of Green Chemical Engineering and Industrial Catalysis, School of Chemistry and Molecular Engineering, East China University of Science and Technology, Shanghai 200237, China
    b School of Pharmaceutical and Chemical Engineering, Taizhou University, Taizhou 318000, Zhejiang, China
    c State Key Laboratory of Green Chemical Engineering and Industrial Catalysis, Sinopec Shanghai Research Institute of Petrochemical Technology, Shanghai 201208, China
  • Received:2025-12-16 Accepted:2026-02-13 Online:2026-09-18 Published:2026-09-05
  • About author:First author contact: 共同第一作者.
    Contributed equally to this work.
  • Supported by:
    National Natural Science Foundation of China(22278126);National Natural Science Foundation of China(22408095);National Natural Science Foundation of China(22250005);The China National Postdoctoral Program for Innovative Talents(BX20240116);The China Postdoctoral Science Foundation(2023M741170);The National Key R&D Program of China(2024YFA1509801);The Fundamental Research Funds for the Central Universities.

摘要: 二氧化碳捕集与原位转化(iCCC)技术为碳捕集利用与封存(CCUS)提供了新思路. 然而, 由于CO2分子热力学稳定, 其转化过程通常需要高温和过量H2, 导致整体成本居高不下. 值得注意的是, 石油化工中烷烃脱氢过程可副产大量H2. 若将乙烷氧化脱氢(ODHE)与iCCC过程耦合, 利用捕集后的CO2作为温和氧化剂, 既可突破脱氢反应的热力学平衡限制, 提升乙烯产率, 又可实现CO2的资源化利用, 形成具有前景的iCCC-ODHE新路径. 然而, 该过程面临CO2乙烷干重整(DRE)副反应的竞争, 其本质在于乙烷分子中C-H键与C-C键的选择性断裂, 且存在吸附与催化协同机制不明问题, 因此, 开发高选择性催化剂并合理设计吸附与催化位点的耦合方式, 是实现iCCC-ODHE高效运行的关键.
针对iCCC-ODHE体系中催化活性位点构筑以及局域催化环境调控两个关键问题, 本研究通过调节钴负载量精准构筑稳定分散的Co2+物种, 实现对C-H与C-C键选择性活化路径的调控; 并通过改变吸附位点与催化位点之间的接触距离, 调控传质行为, 使催化位点局域环境具有合理的CO2/C2H6比例, 系统阐明iCCC-ODHE过程中局域CO2浓度对ODHE与DRE竞争反应路径及中间体演化机制的影响. 首先, 在含有丰富羟基的H-ZSM-5分子筛载体上通过浸渍法引入不同负载量的钴物种, 制备得到Co-ZSM-5-x系列催化剂. 其中, Co-ZSM-5-1.5孔道内具备高密度且与分子筛内表面羟基强相互作用的Co2+物种, 具有高选择性活化乙烷中的C-H键的性能; 随后, 选择Ca4MgO5作为高温CO2吸附剂, 其操作温度与ODHE反应条件匹配, 同时MgO的引入有效抑制了CaO吸附组分在循环过程中的高温团聚失活. 通过将Co-ZSM-5-1.5与Ca4MgO5分别以颗粒堆积与粉末共混两种集成方式组成双功能材料(DFM)床层, 进而系统调节二者之间的空间几何距离, 从而改变CO2扩散路径、调控催化位点局域微环境的CO2浓度分布. 结果表明, 合理的接触距离(颗粒混合模式)可显著抑制DRE副反应, 在保持高CO2捕集量(10.8 mmol g‒1)同时, 实现目前已报道体系中较高水平的乙烯收率(45.4%), 并展现出优异的循环稳定性. 密度泛函理论计算结果表明, 在颗粒共混模式(即适度较低局域CO2浓度下), C2H6优先经历选择性C-H键断裂生成*CH2CH3中间体, 而非更易发生的C-C键断裂路径; 同时, 反应过程中生成的活性H*物种可攻击吸附态CO2, 进而通过HCOO*路径发生RWGS反应完成CO2的转化; 而当CO2局部浓度过高时, 则更有利于DRE路径的进行. 因此, 通过调控吸附-催化位之间的邻近性, 实现局部CO2/C2H6比例的动态优化, 是实现高效iCCC-ODHE的核心机制.
综上, 本研究提出了通过催化活性位点构筑以及吸附-催化位点间距局域环境调控以实现CO2捕集和高效利用, 获得高选择性烯烃目标产物生成, 突破了传统双功能材料一体化材料集成的设计思路. 该工作为iCCC-ODHE体系中选择性乙烯生成机制的理解与优化提供了理论与实验基础, 对构建高效、稳定的CO2捕集与原位转化制高附加值产品具有重要指导意义.

关键词: 碳捕集, 氧化乙烷脱氢, 双功能材料, 局域催化环境, C-H/C-C选择性活化

Abstract:

The integrated CO2 capture and conversion through oxidative dehydrogenation of ethane (iCCC-ODHE) utilizes the captured CO2 as a mild oxidant to promote value-added ethylene production. Nevertheless, it is still trapped by low efficiency owing to little understandings about the synergistic interaction between the CO2 capture and catalytic ODHE. Herein, we focus on exploring the contributions of local catalytic environments to the iCCC-ODHE performance through tailoring the catalyst itself and the proximity-governed effect. The Co-ZSM-5 catalysts are developed to achieve a selective cleavage of the C-H bond over the C-C bond in C2H6 through modulating the relative concentration of Co2+. When coupling the optimized Co-ZSM-5 catalyst with the CO2 adsorbent Ca4MgO5 by adjusting packing configurations in a fixed bed, a superior iCCC-ODHE performance with an excellent CO2 capture capacity of 10.8 mmol gadsorbent‒1 and a remarkable C2H4 yield of 45.4% is achieved at 650 °C in the granule-stacking configuration. Consistently, the density functional theory calculations reveal the pathway of these abnormal phenomena that the low local CO2 concentration around catalytic sites, corresponding to a relatively far proximity distance, shows a significant effect on decreasing the reaction energy of selective cleavage of the first C-H bond in C2H6. Meanwhile, the produced *H species can be consumed by the following adsorbed *CO2, facilitating the shift of reaction equilibrium forwardly for the formation of C2H4 and CO. Therefore, this insight into the local catalytic environment provides a promising iCCC-ODHE strategy toward carbon neutrality.

Key words: CO2 capture, Oxidative dehydrogenation of ethane, Co-ZSM-5/Ca4MgO5 dual functional materials, Local catalytic environment, C-H/C-C bonds selective cleavage