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Single-step conversion of levulinic acid to valeric acid over bimetallic Ni-Co/H-ZSM-5 catalysts
被引:1
|作者:
Nagu, Ajmeera
[1
,2
]
Raju, Ajmira
[1
,3
]
Vennela, Aluvala
[4
]
Varkolu, Mohan
[5
]
Raju, Burri David
Rao, Kamaraju Seetha Rama
[1
]
机构:
[1] Indian Inst Chem Technol, Catalysis & Fine Chem Div, CSIR, Hyderabad 500007, Telangana, India
[2] Indian Inst Technol Tirupati, Yerpedu Venkatagiri Rd,Yerpedu Post, Tirupati 517619, Andhra Pradesh, India
[3] Kakatiya Univ, Univ Arts & Sci Coll, Dept Phys, Hanamkonda 506001, Telangana, India
[4] Osmania Univ, Dept Chem, Amberpet, Hyderabad 500007, Telangana, India
[5] Koneru Lakshmaiah Educ Fdn, Dept Chem, Moinabad Rd,RVS Nagar,Azziz Nagar PO, Hyderabad 500075, Telangana, India
来源:
关键词:
Biofuels;
cobalt;
nickel;
valeric acid;
zeolites;
GAMMA-VALEROLACTONE;
PHASE HYDROGENATION;
SUPPORTED NI;
BIOMASS;
BIOFUELS;
ESTERS;
FUELS;
PLATFORM;
D O I:
10.1002/slct.202300509
中图分类号:
O6 [化学];
学科分类号:
0703 ;
摘要:
Single-step conversion of levulinic acid (LA) to valeric biofuel is extremely promising for the development of bio-refineries. Direct conversion of LA to valeric acid (VA) was investigated over H-ZSM-5 supported Ni, Co, and Ni-Co (different Ni/Co wt. % ratios) catalysts under ambient reaction conditions (543 K and atmospheric pressure) in the gas phase. Compared with supported monometallic catalysts, bimetallic Ni-Co catalysts exhibited more activity and selectivity toward VA production. Among Ni-Co/H-ZSM-5 catalysts, 15Ni-5Co/H-ZSM-5 catalyst is optimum with 97.5 % conversion of LA and 63 % selectivity to valeric acid even after 6 h time-on-stream (TOS). The active metallic sites are responsible for the hydrogenation of LA to gamma-valerolactone (GVL), and acidic sites catalyze the conversion of GVL to VA. All the catalysts were characterized using the XRD, H-2-TPR, N-2-adsorption-desorption isotherms, NH3-TPD, Py-IR, SEM, HR-TEM and XPS techniques.
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页数:10
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