H2 production from ethanol steam reforming using metallic nickel hollow fiber membrane reactor

被引:0
作者
Lu, Zuojun [1 ]
Yuan, Chen [1 ]
Li, Claudia [2 ]
Geng, Guanlong [1 ]
Song, Jian [1 ]
Yang, Naitao [1 ]
Kawi, Sibudjing [2 ]
Tan, Xiaoyao [3 ]
Sunarso, Jaka [4 ]
Liu, Shaomin [5 ]
机构
[1] Shandong Univ Technol, Dept Chem Engn, Zibo 255049, Peoples R China
[2] Natl Univ Singapore, Dept Chem & Biomol Engn, 4 Engn Dr 4, Singapore 117585, Singapore
[3] Tiangong Univ, Dept Chem Engn, State Key Lab Separat Membranes & Membrane Proc, Tianjin 300387, Peoples R China
[4] Swinburne Univ Technol, Res Ctr Sustainable Technol, Fac Engn Comp & Sci, Jalan Simpang Tiga, Kuching 93350, Sarawak, Malaysia
[5] Great Bay Univ, Sch Engn, Dongguan Key Lab Intelligent Equipment & Smart Ind, Dongguan 523000, Peoples R China
基金
中国国家自然科学基金; 新加坡国家研究基金会;
关键词
Ni hollow fiber membrane; Membrane reactor; Ethanol steam reforming; H-2; separation; Renewable energy; HYDROGEN-PRODUCTION; PURE HYDROGEN; CATALYSTS; COKE; GAS; DEACTIVATION; WATER;
D O I
10.1016/j.seppur.2025.132561
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Membrane catalysis is recognized as an ideal technology for H-2 production given its potential to integrate the production and separation into one unit. Recent research has pivoted to utilizing nickel (Ni) as an alternative membrane material to Pd and its alloys considering its high stability and low cost, as Ni also possesses H-2 adsorption and separation capabilities. In this work, gastight Ni hollow fiber membranes (NiHFMs) were prepared using the combined phase inversion and sintering technique, which was subsequently assembled into a membrane reactor for the H-2 production via liquid biomass (ethanol) steam reforming (ESR). The influence of temperature, feed flow rate, sweep gas flow rate, and steam/ethanol (S/E) molar ratio on the ESR performance of the metallic NiHFM reactor were systematically investigated. The metallic NiHFM reactor exhibited excellent ESR catalytic activity, as well as stability, and effective H-2 separation capability. At 900 degrees C, S/E of 3, aqueous ethanol solution feed of 18.389 mu L min(-1), and N-2 sweep of 30 mL min(-1), the conversion of ethanol remained stable at 94 % over 180 h. Moreover, the H-2 yield reached 45-50 %, and the H-2 flux was consistently stabilized at 0.55-0.58 mL cm(-2) min(-1) under sweep gas mode at ambient pressure. The inspiring long-term operational stability results underscore the potential of the metallic NiHFM reactor in ESR applications, paving the way forward for the direct production of H-2 with high-purity from renewable energy sources.
引用
收藏
页数:11
相关论文
共 60 条
  • [1] Gozgor G., Lau C.K.M., Lu Z., Energy consumption and economic growth: New evidence from the OECD countries, Energy, 153, pp. 27-34, (2018)
  • [2] Ma H., Zeng L., Tian H., Li D., Wang X., Li X., Gong J., Efficient hydrogen production from ethanol steam reforming over La-modified ordered mesoporous Ni-based catalysts, Appl. Catal. B, 181, pp. 321-331, (2016)
  • [3] Magnone E., Shin M.C., Lee J.I., Park J.H., Relationship between hydrogen permeability and the physical-chemical characteristics of metal alloy membranes, J. Membr. Sci., 674, (2023)
  • [4] Yuan D., Peng Y., Ma L., Li J., Zhao J., Hao J., Wang S., Liang B., Ye J., Li Y., Coke and sintering resistant nickel atomically doped with ceria nanosheets for highly efficient solar driven hydrogen production from bioethanol, Green Chem., 24, pp. 2044-2050, (2022)
  • [5] Kumar A., Daw P., Milstein D., Homogeneous catalysis for sustainable energy: Hydrogen and methanol economies, fuels from biomass, and related topics, Chem. Rev., 122, pp. 385-441, (2022)
  • [6] Chen G., Feldhoff A., Weidenkaff A., Li C., Liu S., Zhu X., Sunarso J., Huang K., Wu X.Y., Ghoniem A.F., Yang W., Xue J., Wang H., Shao Z., Duffy J.H., Brinkman K.S., Tan X., Zhang Y., Jiang H., Costa R., Friedrich K.A., Kriegel R., Roadmap on sustainable mixed ionic‐electronic conducting membranes, Adv. Funct. Mater., 32, (2021)
  • [7] Mazloomi K., Gomes C., Hydrogen as an energy carrier: Prospects and challenges, Renew. Sust. Energ. Rev., 16, pp. 3024-3033, (2012)
  • [8] Spallina V., Matturro G., Ruocco C., Meloni E., Palma V., Fernandez E., Melendez J., Pacheco Tanaka A.D., Viviente Sole J.L., van Sint Annaland M., Gallucci F., Direct route from ethanol to pure hydrogen through autothermal reforming in a membrane reactor: Experimental demonstration, reactor modelling and design, Energy, 143, pp. 666-681, (2018)
  • [9] Dai Z., Deng L., Membranes for CO<sub>2</sub> capture and separation: Progress in research and development for industrial applications, Sep. Purif. Technol., 335, (2024)
  • [10] Wang D., Wu H., Xu Y., Chen T., Zhang Y., Hu Z., Wang Z., Tan X., Liu S., Self-catalytic nickel hollow fiber membrane reactor for hydrogen production via toluene steam reforming, J. Membr. Sci., 686, (2023)