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杨 丽,刘 帅,辛春梅,等. 炭黑负载增加活性炭缺陷位点催化甲烷裂解制氢机理研究[J]. 煤炭科学技术,2024,52(3):300−310

. DOI: 10.12438/cst.2023-0320
引用本文:

杨 丽,刘 帅,辛春梅,等. 炭黑负载增加活性炭缺陷位点催化甲烷裂解制氢机理研究[J]. 煤炭科学技术,2024,52(3):300−310

. DOI: 10.12438/cst.2023-0320

YANG Li,LIU Shuai,XIN Chunmei,et al. Study on the mechanism of hydrogen production by methane decomposition catalyzed by activated carbon loaded by carbon black for increasing defect sites[J]. Coal Science and Technology,2024,52(3):300−310

. DOI: 10.12438/cst.2023-0320
Citation:

YANG Li,LIU Shuai,XIN Chunmei,et al. Study on the mechanism of hydrogen production by methane decomposition catalyzed by activated carbon loaded by carbon black for increasing defect sites[J]. Coal Science and Technology,2024,52(3):300−310

. DOI: 10.12438/cst.2023-0320

炭黑负载增加活性炭缺陷位点催化甲烷裂解制氢机理研究

Study on the mechanism of hydrogen production by methane decomposition catalyzed by activated carbon loaded by carbon black for increasing defect sites

  • 摘要: 在“双碳”目标时代背景下,甲烷催化裂解制氢因无CO2排放被认为是一种很有前途的高纯制氢技术。其中针对碳基催化剂改性的研究是一大关注热点。为提高活性炭(Activated Carbon, AC)催化剂的稳定性,提出了以椰壳活性炭负载科琴黑炭黑(Carbon Black, CB)制备的新型催化剂,并对其进行了表征测试分析、催化甲烷裂解实验以及分子模拟计算。实验结果表明:分散剂使用1 g、AC和CB质量配比8∶2时制备的催化剂具有较好的催化性能,反应温度在1 000 ℃时初始活性高达85%以上,延缓失活15 min,反应中期甲烷转化率比AC最高提升8%左右。这是因为CB负载在AC表面经反应生成具有缺陷位点的沉积碳。分子模拟计算结果显示,主要是拓扑缺陷的存在使得其s、p轨道非局域性增大,提高其甲烷吸附性能,促进反应进行。同时,AC表面的微孔以及羧基、羰基、羟基等含氧官能团也对甲烷分子的吸附有不同程度的促进作用。孔径为0.8 nm时吸附热最大,这意味着微孔的存在有利于甲烷在AC上吸附,特别是小微孔;3种官能团均可以促进甲烷在AC表面的吸附,其中羧基促进作用更好,羰基和羟基效果相差不大。

     

    Abstract: Under the background of the “dual carbon goal” era, hydrogen production from methane decomposition is considered to be a promising high-purity hydrogen production technology due to no CO2 emissions. The research on carbon catalyst modification is a hot spot in related fields. To improve the stability of activated carbon (AC) catalysts, the new catalysts prepared by coconut shell activated carbon supported with carbon black (CB) ketjen black EC300J was proposed and prepared. And its characterization test analysis, catalytic methane cracking experiment and molecular simulation calculation were carried out. The results show that the catalyst prepared when the amount of dispersant was 1 g and the AC and CB mass ratio was 8∶2 had better catalytic performance, the initial activity at 1 000 ℃ was up to 85%, the deactivation was delayed for 15 min, and the methane conversion in the middle stage of the reaction was about 8% higher than that in AC. This is because that CB is loaded on the surface of AC and generates deposited carbon with defect sites through reaction. The results of molecular simulation calculations show that the main reason is that the existence of topological defects increases the nonlocality of its s and p orbitals, which improves the adsorption performance of methane and promotes the reaction. In addition, the micropores on the surface of AC and oxygen-containing functional groups such as carboxyl, carbonyl, and hydroxyl groups also have different degrees of promotion on the adsorption of methane molecules. The heat of adsorption is the greatest when the pore size is 0.8 nm, which means that the presence of micropores is conducive to methane adsorption on AC, especially small micropores. All three functional groups can promote the adsorption of methane on the surface of AC, among which the carboxyl group promotion effect is better, and the carbonyl and hydroxyl effects are not much different.

     

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