Hydrodeoxygenation of oleic acid into n- and iso-paraffin biofuel using zeolite supported fiuoro-oxalate modified molybdenum catalyst: Kinetics study

被引:29
作者
Ayodele, O. B. [1 ,4 ]
Farouk, Hamisu U. [2 ]
Mohammed, Jibril [3 ]
Uemura, Y. [4 ]
Daud, W. M. A. W. [1 ]
机构
[1] Univ Malaya, Fac Engn, Dept Chem Engn, Kuala Lumpur, Malaysia
[2] Bayero Univ Kano, Fac Sci, Dept Pure & Ind Chem, Kano, Kano State, Nigeria
[3] Abubakar Tafawa Balewa Univ, Dept Chem Engn, Bauchi, Bauchi State, Nigeria
[4] Univ Teknol PETRONAS, Dept Chem Engn, Ctr Biofuel & Biochem Res, Tronoh, Perak, Malaysia
关键词
Molybdenum oxalate; Hydrodeoxygenation; Oleic acid; Isomerization; Biofuel; SUNFLOWER OIL; DEOXYGENATION; DEGRADATION; FERRIOXALATE; HYDROTREATMENT; AMOXICILLIN; DIESEL;
D O I
10.1016/j.jtice.2014.12.014
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The activity of zeolite supported fluoride-ion functionalized molybdenum-oxalate catalyst (FMoOx/Zeol) and its kinetic study on the hydrodeoxygenation (HDO) of oleic acid (OA) is presented in this report. The FMoOx/Zeol was synthesized via simple dissolution method and characterized. The results revealed formation of highly reactive octahedral Mo species with enhanced textural and morphological properties. The FMoOx/Zeol activity on the HDO of OA at the best observed experimental conditions of 360 degrees C, 30 mg FMoOx/Zeol and 20 bar produces 64% n-C18H38 and 30% iso-C18H38 in 60 min. The acidity of FMoOx/Zeol was responsible for the production of the iso-C18H38. The kinetic data showed that sequential hydrogenation of OA into stearic acid (SA) was faster than the HDO of SA into biofuel with activation energies of 98.7 and 130.3 kJ/mol, respectively. The reusability studies showed consistency after three consecutive runs amounting to 180 min reaction time. The results are encouraging towards industrial application. (C) 2015 Taiwan Institute of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:142 / 152
页数:11
相关论文
共 37 条
[1]   Catalytic deoxygenation of oleic acid in continuous gas flow for the production of diesel-like hydrocarbons [J].
Arend, Matthias ;
Nonnen, Thomas ;
Hoelderich, Wolfgang F. ;
Fischer, Juergen ;
Groos, Jeremie .
APPLIED CATALYSIS A-GENERAL, 2011, 399 (1-2) :198-204
[2]   Development of kaolinite supported ferric oxalate heterogeneous catalyst for degradation of 4-nitrophenol in photo-Fenton process [J].
Ayodele, O. B. ;
Hameed, B. H. .
APPLIED CLAY SCIENCE, 2013, 83-84 :171-181
[3]   Synthesis of copper pillared bentonite ferrioxalate catalyst for degradation of 4-nitrophenol in visible light assisted Fenton process [J].
Ayodele, O. B. ;
Hameed, B. H. .
JOURNAL OF INDUSTRIAL AND ENGINEERING CHEMISTRY, 2013, 19 (03) :966-974
[4]   Artificial Neural Networks, Optimization and Kinetic Modeling of Amoxicillin Degradation in Photo-Fenton Process Using Aluminum Pillared Montmorillonite-Supported Ferrioxalate Catalyst [J].
Ayodele, O. B. ;
Auta, H. S. ;
Nor, N. Md .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2012, 51 (50) :16311-16319
[5]  
Ayodele OB, J TAIWAN I CHEM ENG
[6]  
Ayodele OB, PREPARATION CHARACTE
[7]   Catalytic activity of copper modified bentonite supported ferrioxalate on the aqueous degradation and kinetics of mineralization of Direct Blue 71, Acid Green 25 and Reactive Blue 4 in photo-Fenton process [J].
Ayodele, Olumide Bolarinwa ;
Togunwa, Olayinka S. .
APPLIED CATALYSIS A-GENERAL, 2014, 470 :285-293
[9]  
Azmi NHM, FE MODIFIED LOCAL CL
[10]   In situ TPO, TPD and XRD characterisation of a molybdenum oxycarbohydride catalyst for n-butane isomerisation [J].
Bouchy, C ;
Pham-Huu, C ;
Heinrich, B ;
Derouane, EG ;
Derouane-Abd Hamid, SB ;
Ledoux, MJ .
APPLIED CATALYSIS A-GENERAL, 2001, 215 (1-2) :175-184