The catalytic decomposition of CH4 using Ce-doped Fe/CaO-Ca12Al14O33 catalyst and its regeneration performance for H2 production

被引:0
作者
Chu, Zhiwei [1 ]
Zhao, Wenhan [1 ]
Xu, Duo [1 ]
Liu, Wenqiang [2 ]
Han, Kuihua [1 ]
He, Zirui [3 ,4 ]
Li, Yingjie [1 ]
机构
[1] Shandong Univ, Shandong Engn Res Ctr High Efficiency Energy Stora, Sch Energy & Power Engn, Jinan 250061, Peoples R China
[2] Huazhong Univ Sci & Technol, State Key Lab Coal Combust, Wuhan 430074, Peoples R China
[3] CNOOC Gas & Power Grp Co Ltd, Beijing 100028, Peoples R China
[4] Nanyang Technol Univ, Sch Chem Chem Engn & Biotechnol, Singapore City 637459, Singapore
关键词
Catalytic decomposition of CH4; H-2; production; Regeneration; CeO(2)doped Fe/CaO-Ca(12)Al(14)O(33)catalyst; CO2; capture; METHANE DECOMPOSITION; HYDROGEN-PRODUCTION; CARBON NANOTUBES; SUPPORTED NI; FE; EPR; CO; ACTIVATION; MECHANISM; MO;
D O I
10.1016/j.seppur.2024.129670
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The catalytic decomposition of CH4 using low cost and non-toxicity Fe-based catalysts is a prospective method for H-2 production. The regeneration process of iron-based catalysts involves CO2 emission and incomplete conversion of carbon deposition. In this work, a novel catalytic decomposition of CH4/regeneration process was proposed using the Ce-doped Fe/CaO-Ca12Al14O33 catalyst for H-2 production. To remove the carbon deposition in the catalyst, the regeneration stage includes four steps: solid carbon production by vibratory separation, steam gasification of residual carbon deposition to produce H-2 where CO2 is captured by CaO to form CaCO3, calcination of CaCO3 to produce CaO and pure CO2, methanol production by CO2 and H-2 from carbon deposition gasification. The effects of Ce doping on the catalysis/regeneration performance of Fe/CaO-Ca12Al14O33 catalysts were studied, and the Ce-doped Fe/CaO-Ca12Al14O33 catalyst was compared with Cu-, Zn-, and Mn- doped Fe/CaO-Ca12Al14O33 catalysts. The solid carbon obtained from the catalytic decomposition of CH4/regeneration cycles was characterized. The Ce-doped Fe/CaO-Ca12Al14O33 catalyst shows excellent catalysis, CO2 capture, and stability performance in the catalytic decomposition of CH4/regeneration cycles. The average CH4 conversion is 90.02% in the first cycle, which decreases to 80.01% after 8 cycles. Carbon nanotubes are the main forms of obtained solid carbon with the favorable pore structure. The doping of Ce improves the effective adsorption sites for CH4 and CO2. Carbon deposition in the catalyst is efficiently removed by steam gasification. In addition, CeO2 promotes the electron transfer, oxygen vacancy generation, and Fe3C decomposition, which leads to superior catalytic performance and resistance to deactivation of the catalyst. The CeO2-doped Fe/CaO-Ca12Al14O33 catalyst is promising for H-2 production via catalysis/regeneration cycles.
引用
收藏
页数:17
相关论文
共 31 条
  • [21] COx-free H2 Production via Catalytic Decomposition of CH4 over Fe Supported on Tungsten oxide-activated Carbon Catalyst: Effect of Tungsten Loading
    Bayahia, Hossein
    Fakeeha, Anis H.
    Al-Zahrani, Salma A.
    Alreshaidan, Salwa B.
    Al-Awadi, Abdulrhman S.
    Alotibi, Mohammed F.
    Kumar, Rawesh
    Al-Fatesh, Ahmed S.
    ARABIAN JOURNAL OF CHEMISTRY, 2023, 16 (06)
  • [22] Hydrogen production by methane decomposition over Co-Al mixed oxides derived from hydrotalcites: Effect of the catalyst activation with H2 or CH4
    Zardin, Luiza
    Perez -Lopez, Oscar W.
    INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2017, 42 (12) : 7895 - 7907
  • [23] Hollow Submicrospherical Ni/Co-Promoted CaO/Ca12Al14O33 for H2 Production from Sorption-Enhanced Water-Gas Shift with In Situ CO2 Conversion via CH4 Reforming of CaCO3
    Zhang, Chunxiao
    Li, Yingjie
    Deng, Yumeng
    Liu, Wenqiang
    Han, Kuihua
    Wang, Yuzhuo
    He, Zirui
    Wu, Jun Jie
    ACS CATALYSIS, 2025, 15 (05): : 4208 - 4228
  • [24] Ca12Al14O33 or MgO supported Ni-carbide slag bi-functional materials for H2 production and CO2 capture in sorption-enhanced steam gasification of cellulose/polyethylene mixture
    Wang, Yuzhuo
    Li, Yingjie
    Yang, Liguo
    Fan, Xiaoxu
    Chu, Leizhe
    FUEL, 2022, 328
  • [25] Solar driven two-step CH4 reforming and H2O splitting using Al2O3 for Co-production of Al, syngas, and H2
    Bhosale, Rahul R.
    SOLAR ENERGY, 2018, 172 : 232 - 241
  • [26] H2 and CO production over a stable Ni-MgO-Ce0.8Zr0.2O2 catalyst from CO2 reforming of CH4
    Jang, Won-Jun
    Jeong, Dae-Woon
    Shim, Jae-Oh
    Roh, Hyun-Seog
    Son, In Hyuk
    Lee, Seung Jae
    INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2013, 38 (11) : 4508 - 4512
  • [27] Enhancing the catalytic H2 production performance of magnetic Ni-Fe2O3-C catalyst in biomass steam gasification using electromagnetic induction heating
    Wu, Long
    Yan, Zhijun
    Xie, Jing
    Xu, Qing
    Li, Zhanyong
    BIORESOURCE TECHNOLOGY, 2024, 402
  • [28] Highly Selective Syngas/H2 Production via Partial Oxidation of CH4 Using (Ni, Co and Ni-Co)/ZrO2-Al2O3 Catalysts: Influence of Calcination Temperature
    Fakeeha, Anis Hamza
    Arafat, Yasir
    Ibrahim, Ahmed Aidid
    Shaikh, Hamid
    Atia, Hanan
    Abasaeed, Ahmed Elhag
    Armbruster, Udo
    Al-Fatesh, Ahmed Sadeq
    PROCESSES, 2019, 7 (03)
  • [29] Catalytic partial oxidation of CH4 to syn gas (H2/CO) in presence of N2O over periclase type SiO2@Ni(Mg,Al)O catalyst synthesized by non aqueous route
    Saikia, Pinky
    Goswamee, Rajib Lochan
    CATALYSIS COMMUNICATIONS, 2019, 119 : 1 - 5
  • [30] Bio-oil production from sequential two-step microwave-assisted catalytic fast pyrolysis of water hyacinth using Ce-doped γ-Al2O3/ZrO2 composite mesoporous catalyst
    Zhang, Bo
    Zhong, Zhaoping
    Li, Tong
    Xue, Zeyu
    Ruan, Roger
    JOURNAL OF ANALYTICAL AND APPLIED PYROLYSIS, 2018, 132 : 143 - 150