高等学校化学学报2024,Vol.45Issue(9) :1-11.DOI:10.7503/cjcu20240125

Pd/LDH低温催化CH4-CO2直接合成乙酸

Direct Synthesis of Acetic Acid from CH4-CO2 over Pd/LDH at Low Temperature

吴怡枭 刘超波 昝雪玉 张超宇 陶诗琪 李智雯 王柯静 刘勇军 黄伟
高等学校化学学报2024,Vol.45Issue(9) :1-11.DOI:10.7503/cjcu20240125

Pd/LDH低温催化CH4-CO2直接合成乙酸

Direct Synthesis of Acetic Acid from CH4-CO2 over Pd/LDH at Low Temperature

吴怡枭 1刘超波 2昝雪玉 1张超宇 1陶诗琪 1李智雯 1王柯静 1刘勇军 1黄伟3
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作者信息

  • 1. 太原理工大学省部共建煤基能源清洁高效利用国家重点实验室,太原 030024
  • 2. 青岛海西环保科技有限公司,青岛 266424
  • 3. 太原理工大学省部共建煤基能源清洁高效利用国家重点实验室,太原 030024;山西浙大新材料与化工研究院,太原 030000
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摘要

利用CH4和CO2反应直接合成乙酸是一个100%原子经济同时转化CH4并减排CO2的有效方法.水滑石因具有比表面积大、热稳定性高、活性组分分散性好及适宜的酸-碱性被广泛用于CH4和CO2转化反应中,而Pd常被认为是C—C键偶联的活性中心.本文以Mg/Al摩尔比分别为1.5,3,5,7,9的镁铝水滑石(MgAl-LDH)为载体,采用离子交换法制备了Pd负载量(质量分数)为5%的Pd/LDH催化剂,并用于CH4-CO2两步梯阶转化直接合成乙酸;通过XRD,ICP,氮气吸附-脱附,XPS,NH3-TPD,CO2-TPD和in situ DRIFTS等表征方法对催化剂的结构和表面酸碱性进行了分析.结果表明,由Mg/Al摩尔比为5的LDH载体制备的MA5催化剂乙酸收率最高(61.8 μmol·g-1cat·h-1),且液相产物只有乙酸;其收率与催化剂中强酸量和表面Pd0/(Pd2++Pd0)比呈正相关.催化剂的快速失活源于水滑石结构的坍塌,进而引起催化剂表面中强酸量大幅减少.原位红外漫反射光谱结果显示,CH4在Pd/LDH催化剂表面解离生成CHx*中间体和H质子,CO2直接插入CHx*形成CHxCOO*,之后进一步加氢生成乙酸,或CO2与H质子结合生成COOH*中间体,之后与CHx*发生偶联形成CHxCOOH*,最后再加氢得到乙酸.

Abstract

The direct synthesis of acetic acid from CH4 and CO2 is an effective method for converting CH4 and reducing CO2 emissions in a 100%atom economy reaction.Hydrotalcite is widely used in CH4 and CO2 conversion reactions due to their large specific surface area,high thermal stability,good dispersion of active metals,and suitable acid-base properties,while Pd is often considered as the active center for C—C bond coupling.Herein,a series of Pd/LDH catalyst with Pd loading of 5%(mass fraction)was prepared by ion-exchange method using magnesium-aluminum hydrotalcite(MgAl-LDH)with Mg/Al molar ratios of 1.5,3,5,7 and 9 as the carrier,and applied for the direct synthesis of acetic acid from CH4-CO2 by a two step-wise technique.The structure and surface acidity-alkalinity of the catalyst were analyzed by XRD,ICP,N2 adsorption-desorption,XPS,NH3-TPD,CO2-TPD and in situ DRIFTS.The results showed that the yield of acetic acid over MA5 catalyst with Mg/Al molar ratio of 5 was the highest(61.8 μmol·g-1cat·h-1),and acetic acid was the only product in the liquid phase product.Its yield was positively correlated with the amount of medium strong acid and surface Pd0/(Pd2++Pd0)ratios.The rapid inactivation of the catalyst was due to the collapse of the hydrotalcite structure,which resulted in a significant decrease in the amount of medium strong acid.In situ DRIFTS experiments showed that CH4 was firstly dissociated to form CHx*intermediate and H proton on the catalyst surface,then CO2 was directly inserted into CHx* to form CHxCOO*,with further hydrogenated to yield acetic acid,or CO2 was combined with H protons to form COOH* intermediates which were then coupled with CHx* to form CHxCOOH*,and finally hydrogenated to obtain acetic acid.

关键词

甲烷/二氧化碳/镁铝水滑石//乙酸

Key words

Methane/Carbon dioxide/Magnesium-aluminum hydrotalcite/Pd/Acetic acid

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基金项目

国家自然科学基金(21908157)

山西浙大新材料与化工研究院研发项目(2021SX-FR009)

出版年

2024
高等学校化学学报
中华人民共和国教育部委托 吉林大学和南开大学

高等学校化学学报

CSTPCD北大核心
影响因子:1.067
ISSN:0251-0790
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