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Sulfonated functionalization of carbon derived corncob residue via hydrothermal synthesis route for esterification of palm fatty acid distillate
被引:78
作者:
Ibrahim, S. Fadhilah
[1
,2
]
Asikin-Mijan, N.
[3
]
Ibrahim, M. Lokman
[4
,5
]
Abdulkareem-Alsultan, G.
[6
]
Izham, Saiman Mohd
[1
,2
]
Taufiq-Yap, Y. H.
[1
,7
]
机构:
[1] Univ Putra Malaysia, Fac Sci, Catalysis Sci & Technol Res Ctr PutraCAT, Upm Serdang 43400, Selangor, Malaysia
[2] Univ Putra Malaysia, Fac Sci, Dept Chem, Upm Serdang 43400, Selangor, Malaysia
[3] Univ Kebangsaan Malaysia, Fac Sci & Technol, Dept Chem Sci, Ukm Bangi 43600, Selangor Darul, Malaysia
[4] Univ Teknol MARA, Inst Sci, Ctr Nanomat Res, Shah Alam 40450, Selangor, Malaysia
[5] Univ Teknol MARA, Sch Chem & Environm, Fac Appl Sci, Shah Alam 40450, Selangor, Malaysia
[6] Univ Putra Malaysia, Chem & Environm Engn Dept, Fac Engn, Upm Serdang 43400, Selangor, Malaysia
[7] Univ Malaysia Sabah, Chancellery Off, Kota Kinabalu 88400, Sabah, Malaysia
关键词:
Biodiesel;
Corncorb;
Esterification;
Hydrothermal;
PFAD;
WASTE COOKING OIL;
BIODIESEL PRODUCTION;
JATROPHA-CURCAS;
OLEIC-ACID;
NONEDIBLE OIL;
CATALYST;
BIOMASS;
MECHANISM;
GLUCOSE;
SHELL;
D O I:
10.1016/j.enconman.2020.112698
中图分类号:
O414.1 [热力学];
学科分类号:
摘要:
Low-cost biodiesel was successfully produced through esterification of palm fatty acid distillate over corncob residue-derived heterogeneous solid acid catalyst. The sulfonated functionalized carbon derived from corncob was synthesized via hydrothermal carbonization followed by chemical activation using concentrated sulfuric acid. This technique allows efficient carbonization process and able to maintain active polar species of the catalyst hence effectively improves the acid strength of prepared catalyst. The esterification of palm fatty acid distillate over HTC-S catalyst was optimized via the one-variable-at-a-time technique, and 92% free fatty acid conversion with a biodiesel yield of 85% was achieved at optimum conditions of 2 h reaction time, 70 degrees C reaction temperature, 3 wt% catalyst loading, and 15:1 methanol-to-oil molar ratio. Various of catalyst regeneration techniques have been studied and sulfuric acid treatment is found to be the most effective approach for restoring the active sites for spent HTC-S catalyst in comparison to washing solvent and thermal treatment. The HTC-S catalyst regenerated via sulfuric acid treatment is capable to convert PFAD to biodiesel with free fatty acid conversion > 90% for two consecutive cycles. The synthesized PFAD-derived biodiesel has complied with the international biodiesel standard ASTM D6751.
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页数:12
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