催化学报 ›› 2019, Vol. 40 ›› Issue (s1): 149-157.

• 综述 • 上一篇    下一篇

甲烷催化制氢进展

杨敬贺1, 彭觅2, 马丁2   

  1. 1 郑州大学化工与能源学院, 河南郑州 450001;
    2 北京大学化学与分子工程学院, 北京 100871
  • 出版日期:2019-12-17 发布日期:2019-10-10
  • 通讯作者: 马丁
  • 基金资助:
    国家自然科学基金(21725301,91645115).

Hydrogen Production from Methane Reforming

YANG Jinghe1, PENG Mi2, MA Ding2   

  1. 1 School of Chemical Engineering and Energy, Zhengzhou University, Zhengzhou 450001, Henan, China;
    2 College of Chemistry and Molecular Engineering, Peking University, Beijing 100871, China
  • Online:2019-12-17 Published:2019-10-10
  • Supported by:
    This work was supported by the National Natural Science Foundation of China (21725301, 91645115).

摘要: 氢气是一种高效的绿色化学品,作为加氢反应的氢源,广泛用于合成氨、石油催化加氢、甲醇合成等大型加氢工业;作为绿色能源,燃烧热值高,燃烧产物洁净,同时还是新能源氢氧燃料电池的阳极气源,在人类社会起着举足轻重的作用.天然气被认为是制氢的最佳原料,其制氢路径包括甲烷部分氧化制氢、甲烷蒸汽重整制氢、甲烷催化裂解制氢、甲烷绝热转化制氢、甲烷二氧化碳重整制氢和甲烷自热重整制氢.甲烷蒸汽重整是一种高效、经济的制氢方法、并已大规模工业化,在世界范围内,约有一半的氢气是通过该法制取.但是,目前该过程仍然有待于降低生产成本、减少积碳发生、深入理解反应机理、减少传热消耗、降低反应温度等技术革新.特别是燃料电池技术兴起以来,对H2纯度要求苛刻,甲烷蒸汽重整产气中CO含量必须低至10 ppm以下,以避免燃料电池Pt电极中毒,这对甲烷蒸汽重整制氢领域提出了新的要求.另一个值得注意的反应是甲烷无氧脱氢.甲烷催化裂解直接脱氢可将甲烷直接分解为固体碳和氢气,工艺过程简单,可得到高纯氢,该工艺耗能较少、对环境无污染,是最具潜力的高纯氢制备工艺.除此之外,甲烷还可直接做氢源,进行煤-气共转化甚至油气共炼.本文简略介绍了甲烷制氢的相关背景、总结了近期研究进展、重点综述了甲烷催化裂解直接脱氢、甲烷蒸汽重整制氢的国际前沿与发展趋势、指出了制约该领域发展的关键问题、简单介绍了我国研究现状与研究特色以及研究队伍状况、指明了在此方向我国存在的“卡脖子”问题、建议了今后重点发展的研究领域和方向.并简要介绍了煤-甲烷共转化概念及油-甲烷共炼的设想,应当指出的是,由于此研究领域相当广泛,此综述并非面面俱到.

关键词: 甲烷, 重整, 裂解, 制氢, 煤-气共转化, 油气共炼

Abstract: Hydrogen is a highly efficient green chemical. It is widely used as a feedstock for ammonia synthesis, petroleum catalytic hydrogenation, and methanol synthesis. As a green energy source, hydrogen has high combustion heat value, clean combustion products, and also act as gas source for anode of fuel cell. Hydrogen plays a pivotal role in human society. Natural gas is considered as the best raw material for hydrogen production, whose hydrogen production paths include partial oxidation,steam reforming, catalytic cracking, adiabatic conversion, dry reforming with carbon dioxide, and thermal reforming. Methane steam reforming is an efficient and economical method for hydrogen production and has been utilized on an industrialscale, which covers about half of the world's hydrogen production. However, as to the current process, challenges still exhist, such as reducing production costs, reducing carbon deposits, understanding the reaction mechanism, reducing heat transfer consumption, and reducing reaction temperature. Especially since the rise of fuel cell technology, the purity of H2 is demanding, and the CO content in methane steam reforming gas must be as low as 10 ppm or less to avoid poisoning of fuel cell Pt electrode, which puts new requirements on the field of hydrogen production from methane steam reforming. Direct dehydrogenation of methane by catalytic cracking can directly decompose methane into solid carbon and hydrogen. The process is simple and high-purity hydrogen can be obtained. This process consumes less energy and has no pollution to the environment. It is the most promising high-purity hydrogen preparation process. Methane can also be used directly as a hydrogen source for coal-gas co-transformation or even oil-gas co-refining. This paper briefly introduces the background of hydrogen production from methane steam reforming, direct dehydrogenation of methane through catalytic cracking, summarizes the papers of international mainstream journals from January 20 to March 2019, and the international frontiers and development trends, and points out the key issues. This paper also introduces the research status and research characteristics in China and the status of the research team, points out the "strangulation" problem in China, and suggests the research fields and directions for key development in the future. By the way, the concept of coal-methane co-transformation and the idea of oil-methane co-refining are briefly introduced. It should be noted that due to the rather vast of the research fields, this modest review is not intended to be comprehensive.

Key words: methane, reforming, pyrolysis, hydrogen production, combined coal gasification and methane reforming, oil and methane co-refining