Development of Ni-Mo carbide catalyst for production of syngas and CNTs by dry reforming of biogas

被引:6
|
作者
Saconsint, Supanida [1 ]
Srifa, Atthapon [1 ]
Koo-Amornpattana, Wanida [1 ]
Assabumrungrat, Suttichai [2 ]
Sano, Noriaki [3 ]
Fukuhara, Choji [4 ]
Ratchahat, Sakhon [1 ]
机构
[1] Mahidol Univ, Fac Engn, Dept Chem Engn, Nakhon Pathom 73170, Thailand
[2] Chulalongkorn Univ, Fac Engn, Ctr Excellence Catalysis & Catalyt React Engn, Dept Chem Engn, Bangkok 10330, Thailand
[3] Kyoto Univ, Fac Engn, Dept Chem Engn, Kyoto 6158510, Japan
[4] Shizuoka Univ, Grad Sch Engn, Dept Appl Chem & Biochem Engn, Shizuoka 4328561, Japan
关键词
CARBON NANOTUBES; MOLYBDENUM CARBIDE; METHANE DECOMPOSITION; HYDROGEN-PRODUCTION; SYNTHESIS GAS; CO; PERFORMANCE; FE; TEMPERATURE; CONVERSION;
D O I
10.1038/s41598-023-38436-8
中图分类号
O [数理科学和化学]; P [天文学、地球科学]; Q [生物科学]; N [自然科学总论];
学科分类号
07 ; 0710 ; 09 ;
摘要
Biogas has been widely regarded as a promising source of renewable energy. Recently, the direct conversion of biogas over heterogeneous catalysts for the simultaneous production of syngas and carbon nanotubes exhibits a high potential for full utilization of biogas with great benefits. Involving the combined dry reforming of methane and catalytic decomposition of methane, the efficiency of process is strongly depended on the catalyst activity/stability, mainly caused by carbon deposition. In this study, Ni-Mo catalyst is engineered to provide a life-long performance and perform high activity in the combined process. The surface modification of catalysts by a controlled carburization pretreatment is proposed for the first time to produce a carbide catalyst along with improving the catalyst stability as well as the reactivity for direct conversion of biogas. The performance of as-prepared carbide catalysts is investigated with comparison to the oxide and metallic ones. As a result, the Ni-Mo2C catalyst exhibited superior activity and stability over its counterparts, even though the condensed nanocarbon was largely grown and covered on the surface. In addition, up to 82% of CH4 conversion and 93% of CO2 conversion could remain almost constant at 800 & DEG;C throughout the entire test period of 3 h under a high flowrate inlet stream of pure biogas at 48,000 cm(3) g(-1) h(-1). The XPS spectra of catalysts confirmed that the presence of Mo2C species on the catalyst surface could promote the stability and reactivity of the catalyst, resulting in higher productivity of carbon nanotubes over a longer time.
引用
收藏
页数:18
相关论文
共 50 条
  • [31] Syngas production from methane steam reforming and dry reforming reactions over sintering-resistant Ni@SiO2 catalyst
    Bolin Han
    Fagen Wang
    Linjia Zhang
    Yan Wang
    Weiqiang Fan
    Leilei Xu
    Hao Yu
    Zhongcheng Li
    Research on Chemical Intermediates, 2020, 46 : 1735 - 1748
  • [32] Syngas Production from Biogas Reforming: Role of the Support in Nickel-based Catalyst Performance
    Pham, Cham Q.
    Nguyen, Van-Phuoc
    Van, Thuan Tran
    Phuong, Pham T. T.
    Pham, Phuong T. H.
    Trinh, Thanh H.
    Nguyen, Tung M.
    TOPICS IN CATALYSIS, 2023, 66 (1-4) : 262 - 274
  • [33] Syngas production from methane steam reforming and dry reforming reactions over sintering-resistant Ni@SiO2 catalyst
    Han, Bolin
    Wang, Fagen
    Zhang, Linjia
    Wang, Yan
    Fan, Weiqiang
    Xu, Leilei
    Yu, Hao
    Li, Zhongcheng
    RESEARCH ON CHEMICAL INTERMEDIATES, 2020, 46 (03) : 1735 - 1748
  • [34] Syngas Production from Biogas Reforming: Role of the Support in Nickel-based Catalyst Performance
    Cham Q. Pham
    Van-Phuoc Nguyen
    Thuan Tran Van
    Pham T.T. Phuong
    Phuong T.H. Pham
    Thanh H. Trinh
    Tung M. Nguyen
    Topics in Catalysis, 2023, 66 : 262 - 274
  • [35] Ni-Mo catalyst synthesized by mechanical alloying
    Sosa, M
    Estrada-Guel, I
    Alonso, G
    Ornelas, C
    De la Torre, SD
    Martínez-Sánchez, R
    METASTABLE, MECHANICALLY ALLOYED AND NANOCRYSTALLINE MATERIALS, 2003, : 745 - 750
  • [36] Hydrodeoxygenation of Triglycerides over Ni-Mo Catalyst
    Cristea, Steliana
    Bolocan, Ion
    Bombos, Dorin
    Bombos, Mihaela
    Juganaru, Traian
    REVISTA DE CHIMIE, 2015, 66 (03): : 404 - 407
  • [37] Ethanol dry reforming for syngas production over Ir/CeO2 catalyst
    侯腾飞
    雷雨声
    张绍印
    张江华
    蔡伟杰
    Journal of Rare Earths, 2015, 33 (01) : 42 - 45
  • [38] Ethanol dry reforming for syngas production over Ir/CeO2 catalyst
    Hou Tengfei
    Lei Yusheng
    Zhang Shaoyin
    Zhang Jianghua
    Cai Weijie
    JOURNAL OF RARE EARTHS, 2015, 33 (01) : 42 - 45
  • [39] Ni and RhNi catalysts supported on Zeolites L for hydrogen and syngas production by biogas reforming processes
    Barrio, V.L. (laura.barrio@ehu.es), 1600, Elsevier B.V., Netherlands (238):
  • [40] Production of Nickel Oxalate Dihydrate from Spent Ni-Mo Hydrodesulfurization Catalyst
    Ilhan, Sedat
    JOURNAL OF POLYTECHNIC-POLITEKNIK DERGISI, 2020, 23 (01): : 105 - 110