Synthesis and characterization of lime derived solid base catalyst for transesterification reaction

2019 ◽  
Author(s):  
Fei-ling Pua ◽  
Nur Afiqah Fauzan ◽  
Mohd Aizat Mohd Nasir ◽  
Rohaya Othman ◽  
Sharifah Nabihah Syed Jaafar ◽  
...  
Fuel ◽  
2011 ◽  
Vol 90 (6) ◽  
pp. 2083-2088 ◽  
Author(s):  
Deepti Jain ◽  
Chitralekha Khatri ◽  
Ashu Rani

2009 ◽  
Vol 12 (17) ◽  
pp. 91-99 ◽  
Author(s):  
Huong Thi Thanh Le ◽  
Tien Van Huynh ◽  
Tan Minh Phan ◽  
Hoa Thi Viet Tran

In our work, biodiesel was prepared from Tra fat by methanolysis reaction using activated calcium oxide as solid base catalyst. Effects of various process parameters on biodiesel production such as molar ratio of methanol to fat, catalyst concentration, temperature and time of reaction and the active mechanism of CaO catalyst for the transesterification reaction were investigated. The results show that CaO has strong basicity and high catalytic activity as a heterogeneous solid base catalyst and the transesterification reaction takes place on basic sites of calcium diglyceroxide formed due to the reaction between Cao and the by-produced glycerol. The biodiesel yield achieves 92.95 % at 60°C, 90 minutes, 8:1 molar ratio of fat to methanol, and 6 % CaO catalyst. Important fuel properties of the produced biodiesel meet the specifications of ASTM D 6751 biodiesel standard.


2008 ◽  
Vol 9 (4) ◽  
pp. 516-521 ◽  
Author(s):  
Wei Chen ◽  
Zhiliang Huang ◽  
Yu Liu ◽  
Qianjun He

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.


2018 ◽  
Vol 16 (2) ◽  
pp. 208 ◽  
Author(s):  
Suprapto Suprapto ◽  
Tikha Reskiani Fauziah ◽  
Meiske S Sangi ◽  
Titie Prapti Oetami ◽  
Imroatul Qoniah ◽  
...  

CaO catalysts were synthesized from limestone by thermal decomposition and coprecipitation methods. The CaO and MgO reference catalysts were also synthesized for comparison. The catalysts were characterized by X-ray diffractometer (XRD) and the analysis result was refined by Rietica software. CaO catalyst obtained by coprecipitation method has higher purity of CaO and lower MgO content than those of calcined CaO. The catalysts were also characterized by Fourier Transform Infrared (FTIR) spectroscopy. FTIR spectra showed that the catalysts can be easily hydrated and carbonated in air. The catalytic activity of the catalyst was studied in transesterification reaction of Reutealis trisperma (Kemiri Sunan) oil with methanol. Transesterification reaction was carried out at oil to methanol molar ratio 1:1 and 1% of catalyst at 60 °C for 2 h. Catalytic activity of CaO catalyst obtained by coprecipitation was higher than calcined CaO. The methyl ester yield obtained from synthesized CaO, CaO from coprecipitation, calcined CaO, and synthesized MgO catalysts were 56.13; 37.74; 15.97; and 3.61%, respectively.


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