Synthesis of magnetically solid base catalyst of NaOH/Chitosan-Fe3O4 for biodiesel production from waste cooking oil: Optimization, kinetics and thermodynamic studies

2021 ◽  
Vol 248 ◽  
pp. 114807
Author(s):  
Maryam Helmi ◽  
Alireza Hemmati
2007 ◽  
Vol 50 (2) ◽  
pp. 79-86 ◽  
Author(s):  
Masato Kouzu ◽  
Shinya Yamanaka ◽  
Takekazu Kasuno ◽  
Masahiko Tajika ◽  
Yoichi Aihara ◽  
...  

2016 ◽  
Vol 723 ◽  
pp. 594-598 ◽  
Author(s):  
Nichaonn Chumuang ◽  
Vittaya Punsuvon

In this study, the biodiesel production of waste cooking oil using calcium methoxide as solid base catalyst was investigated. The calcium methoxide catalyst was synthesized from calcined quick lime reacted with methanol. The XRD result showed that the catalyst was successfully synthesized with sufficient purity. The strength of catalyst was examined on the transesterification reaction of waste cooking oil and methanol. Parameters affecting on transesterification such as the catalyst concentration, methanol-to-oil-molar ratio, reaction time and reaction temperature were investigated. The results showed that the percentage of fatty acid methyl ester conversion of 99.06%. The optimum conditions were achieved within 3 h using 3wt% catalyst concentration, 12:1 methanol-to-oil molar ratio and 65°C reaction temperature. In addition, the kinetic study of transesterification reaction was carried out at the temperature from 30°C to 65°C. The pseudo-first order was good agreement with the experiment results. The reaction rate constant (k) and activated energy (Ea) were determined as 0.023 min-1 and 55.77 kJ/mol, respectively.


Author(s):  
Rehan Zainol Abidin ◽  
Gaanty Pragas Maniam ◽  
Mohd. Hasbi Ab. Rahim

Waste cooking oil has a high potential as a raw material in biodiesel production due to its abundant availability and cheapest among other feedstock. Hence transesterification reaction is carried out using waste cooking oil in this research. The objective of this study is to synthesize and characterize the catalyst. On the other hand, deoiled spent bleaching clay impregnated with 40% CaO utilized as a catalyst. Optimization was carried out on methanol to oil molar ratio (6:1-24:1), catalyst loading (3-10 wt.%) and reaction duration (2-10 h). The catalyst of deoiled spent bleaching clay doped with 40% CaO was prepared by wet impregnation method and calcined at 500 °C for 4 hours. The catalyst shows high activity under optimum condition of 5 hours of reaction time, 12:1 of methanol to oil molar ratio with 7 wt.% of catalyst. The transesterification yields 84.7% methyl ester. Therefore, this catalyst has potential to be used in the transesterification of waste cooking oil in producing biodiesel due to its high activity. Copyright © 2016 BCREC GROUP. All rights reserved <br /><p><em>Received: 21<sup>st</sup> January 2016; Revised: 3<sup>rd</sup> March 2016; Accepted: 6<sup>th</sup> March 2016</em></p><p><strong>How to Cite:</strong> Abidin, R.Z., Maniam G.P., Rahim, M.H.A. (2016). Transesterification of Waste Cooking Oil using Calcium Loaded on Deoiled Spent Bleaching Clay as A Solid Base Catalyst. <em>Bulletin of Chemical Reaction Engineering &amp; Catalysis</em>, 11 (2): 176-181 (doi:10.9767/bcrec.11.2.548.176-181)</p><p><strong>Permalink/DOI:</strong> http://dx.doi.org/10.9767/bcrec.11.2.548.176-181</p>


2021 ◽  
Vol 328 ◽  
pp. 124831 ◽  
Author(s):  
Abdul Naeem ◽  
Ihtisham Wali Khan ◽  
Muhammad Farooq ◽  
Tahira Mahmood ◽  
Israf Ud Din ◽  
...  

Energy ◽  
2021 ◽  
pp. 122536
Author(s):  
Majid Mohadesi ◽  
Babak Aghel ◽  
Ashkan Gouran ◽  
Mohammad Hamed Razmehgir

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