Transesterification of Degummed Jatropha curcas Oil Using Tri-potassium Phosphate as Base Catalyst

2015 ◽  
Vol 13 (3) ◽  
pp. 395-406 ◽  
Author(s):  
Y. V. V. Satyanarayana Murthy ◽  
Rajeswara R. Resapu ◽  
M. R. S. Satyanarayana ◽  
Ramakrishna Jogi
Keyword(s):  
Reaction Temperature ◽  
Jatropha Curcas ◽  
Methyl Esters ◽  
Potassium Phosphate ◽  
Molar Ratio ◽  
Base Catalyst ◽  
Optimum Conditions ◽  
Drastic Reduction ◽  
Biodiesel Standards ◽  
Atomic Absorption Spectra

Abstract Jatropha curcas oil and methanol are transesterified using potassium triphosphate as base catalyst. The effects of methanol to oil molar ratio, reaction temperature, stirring speed, catalyst concentration, solubility and its reusability on the yield of biodiesel are investigated. The base catalyst tri-potassium phosphate (K3PO4) is found to be highly suitable for oils having less than 1.5% free fatty acids (FFA). Highest biodiesel yield (approximately 92%) is acquired under optimum conditions of 9:1 methanol to oil molar ratio, 2% catalyst at 70°C reaction temperature at a stirring speed of 650 rpm. The chemical activity of K3PO4 is found to be similar to that of base catalyst potassium hydroxide (KOH) and the catalyst solubility in biodiesel as determined by atomic absorption spectra is only 4.81 ppm. It has been found that K3PO4 is highly hygroscopic and its reusability drastically decreases upon further usage and it can be reused only in wetted condition for three continuous usages with drastic reduction in catalytic strength. The biodiesel samples prepared were tested for several physicochemical properties and compared with the values of European biodiesel standards. The fatty acid methyl esters (FAME), also referred to as jatropha methyl esters (JME) in this paper, have been analyzed by gas chromatography and thermogravimetric analysis.

The use of sulfated tin oxide as solid superacid catalyst for heterogeneous transesterification of Jatropha curcas oil

2010 ◽  
Vol 64 (6) ◽  
Author(s):  
Gerald Kafuku ◽  
Keat Lee ◽  
Makame Mbarawa
Keyword(s):  
Tin Oxide ◽  
Jatropha Curcas ◽  
Methyl Esters ◽  
Solid Catalyst ◽  
Reaction Conditions ◽  
Jatropha Curcas Oil ◽  
Biodiesel Standards ◽  
Superacid Catalyst ◽  
Astm D6751 ◽  
Central Composite

AbstractThis work presents the use of sulfated tin oxide enhanced with SiO2 (SO42−/SnO2-SiO2) as a superacid solid catalyst to produce methyl esters from Jatropha curcas oil. The study was conducted using the design of experiment (DoE), specifically a response surface methodology based on a threevariable central composite design (CCD) with α = 2. The reaction parameters in the parametric study were: reaction temperature (60°C to 180°C), reaction period (1 h to 3 h), and methanol to oil mole ratio (1: 6 to 1: 24). Production of the esters was conducted using an autoclave nitrogen pressurized reactor equipped with a thermocouple and a magnetic stirrer. The maximum methyl esters yield of 97 mass % was obtained at the reaction conditions: temperature of 180°C, reaction period of 2 h, and methanol to oil mole ratio of 1: 15. The catalyst amount and agitation speed were fixed to 3 mass % and 350–360 min−1, respectively. Properties of the methyl esters obtained fell within the recommended biodiesel standards such as ASTM D6751 (ASTM, 2003).

scholarly journals OPTIMIZATION OF THE PRODUCTION PROCESS OF BIODIESEL FROM JATROPHA CURCAS OIL

2019 ◽  
Vol 49 (4) ◽  
pp. 275-281
Author(s):  
María Fernanda Laborde ◽  
Laura Ivana Orifici ◽  
José Alberto Bandoni ◽  
Medardo Serna Gonzalez ◽  
José María Ponce Ortega ◽  
...  
Keyword(s):  
Jatropha Curcas ◽  
Net Present Value ◽  
Methyl Esters ◽  
Biodiesel Production ◽  
Molar Ratio ◽  
Esterification Reaction ◽  
Integrated Process ◽  
Energy Integration ◽  
Jatropha Curcas Oil ◽  
Utility Cost

In this paper was assessed the potential of biodiesel production from Jatropha curcas oil. The proposed process was simulated in the software Aspen Plus™ involving the stages of trans-esterification reaction, methanol recovering, purification of the obtained methyl esters, catalyst removing, purifying of glycerol and the energy integration through heat exchange networks (HEN). The biodiesel process was carried out through the catalytic reaction of transesterification of Jatropha oil with methanol using a molar ratio of methanol oil of 6:1, and with 1% w/w of NaOH (related to oil mass) as catalyst. Under these conditions, it is technologically feasible to carry out the production of biodiesel. With energy integration through the synthesis of HENs, reductions of 100% and 41.3% of hot and cold utilities were achieved. This way, the utility cost decreases 70.92%. The net present value (NPV) for the integrated process was 70.64% higher than the one corresponding to the non-integrated process under the same production conditions.

scholarly journals Methyl Esters Selectivity of Transesterification Reaction with Homogenous Alkaline Catalyst to Produce Biodiesel in Batch, Plug Flow, and Continuous Stirred Tank Reactors

2014 ◽  
Vol 2014 ◽  
pp. 1-13 ◽  
Author(s):  
N. F. Nasir ◽  
W. R. W. Daud ◽  
S. K. Kamarudin ◽  
Z. Yaakob
Keyword(s):  
Reaction Temperature ◽  
Rate Constants ◽  
Methyl Esters ◽  
Plug Flow ◽  
Operating Conditions ◽  
Transesterification Reaction ◽  
Molar Ratio ◽  
Base Case ◽  
Biodiesel Fuel ◽  
Alkaline Catalyst

Selectivity concept is essential in establishing the best operating conditions for attaining maximum production of the desired product. For complex reaction such as biodiesel fuel synthesis, kinetic studies of transesterification reaction have revealed the mechanism of the reaction and rate constants. The objectives of this research are to develop the kinetic parameters for determination of methyl esters and glycerol selectivity, evaluate the significance of the reverse reaction in transesterification reaction, and examine the influence of reaction characteristics (reaction temperature, methanol to oil molar ratio, and the amount of catalyst) on selectivity. For this study, published reaction rate constants of transesterification reaction were used to develop mathematical expressions for selectivities. In order to examine the base case and reversible transesterification, two calculation schemes (Case  1 and Case  2) were established. An enhanced selectivity was found in the base case of transesterification reaction. The selectivity was greatly improved at optimum reaction temperature (60°C), molar ratio (9 : 1), catalyst concentration (1.5 wt.%), and low free fatty acid feedstock. Further research might explore the application of selectivity for specifying reactor configurations.

scholarly journals Green Heterogeneous Base Catalyst from Ripe-Unripe Plantain Peels for the Transesterification of Waste Cooking Oil

2021 ◽  
Author(s):  
Olayomi Abiodun Falowo ◽  
Babatunde Oladipo ◽  
Abiola Ezekiel Taiwo ◽  
Tomiwa Ayomiposi Olaiya ◽  
Oluwaseun Oyekola ◽  
...  
Keyword(s):  
Reaction Time ◽  
Reaction Temperature ◽  
Waste Cooking Oil ◽  
Molar Ratio ◽  
Base Catalyst ◽  
Catalyst Amount ◽  
X Ray ◽  
Cooking Oil ◽  
Heterogeneous Base Catalyst ◽  
Heterogeneous Base

Abstract Economical feedstocks such as agricultural wastes, food wastes, and waste cooking oil were used for biodiesel production to expand their application. Thus, a solid base catalyst was synthesized from a mixture of ripe and unripe plantain peels at a calcination temperature of 500 oC for 4 h. The catalyst was characterized using Scanning Electron Microscope (SEM), X-ray Diffraction (XRD) analysis, Fourier Transform Infrared (FT-IR) spectroscopy, Energy dispersive X-ray (EDX) analysis, and Brunauer-Emmett-Teller (BET) method. The waste cooking oil (WCO) used in this study was first pretreated with 3% (v/v) of H2SO4 via esterification reaction due to its high acid value. The esterified WCO was converted to biodiesel via transesterification reaction, and the process was then modeled and optimized using Taguchi L9 orthogonal array design method considering reaction temperature, reaction time, catalyst amount, and methanol/WCO molar ratio as the input variables. Based on the results, the synthesized catalyst predominantly contained potassium phases with 45.16 wt.%. The morphology of the catalyst revealed a crystalline mesoporous nanocomposite. At the end of WCO esterification, the acidity of the oil decreased from 5 to 1 mg KOH/g. The optimal conditions established for the transesterification process were catalyst amount of 0.5 wt.%, methanol/WCO molar ratio of 6:1, reaction temperature of 45 oC, and reaction time of 45 min with a corresponding biodiesel yield of 97.96 wt.%. The quality of the biodiesel produced satisfied the specifications (ASTM D6751 and EN 14241) recommended for biodiesel fuels. Hence, a blend of ripe and unripe plantain peels could serve as an efficient heterogeneous base catalyst in producing biodiesel from WCO.

Jatropha curcas L.: A Non-food Oil Source for Optimized Biodiesel Production

2019 ◽  
Vol 41 (3) ◽  
pp. 458-458
Author(s):  
Tahir Mehmood Tahir Mehmood ◽  
Adeela Naseem Adeela Naseem ◽  
Farooq Anwar Farooq Anwar ◽  
Mudassir Iqbal and Muhammad Ashraf Shaheen Mudassir Iqbal and Muhammad Ashraf Shaheen
Keyword(s):  
Reaction Time ◽  
Jatropha Curcas ◽  
Positive Impact ◽  
Methyl Esters ◽  
Polynomial Equation ◽  
Biodiesel Production ◽  
Molar Ratio ◽  
Quadratic Term ◽  
Factors Affecting ◽  
Jatropha Curcas Oil

Response Surface Methodology (RSM) was applied based on central composite rotatable design (CCRD) to optimize transesterification reaction parameters for obtaining optimal biodiesel yield from Jatropha curcas oil. Transesterification variables such as: catalyst concentration (CC) (0.16-2%), reaction temperature (RT) (40-65and#176;C), molar ratio of oil and methanol (0.95-11.5), and reaction time (30-140 min) were optimized via RSM involving 24 full factorial CCRD design. The molar ratio of methanol to oil and RT were the most significant (pandlt; 0.5) factors affecting the yield of Jatropha curcas oil methyl esters (JOMEs). A linear relationship was recorded between the observed and predicted values (R2 = 0.766). Using multiple regression analysis, a quadratic polynomial equation was constructed to predict JOMEs yield. The quadratic term of molar ratio showed a significant impact on the JOMEs yield. The interaction terms of molar ratio and CC with reaction time exhibited positive impact on ester yield (pandlt; 0.05). The optimum reaction conditions including CH3OH to oil ratio of 6:1, 1.0 % CC, 60 and#176;C RT and 60 min reaction time offered the highest yield of JOMEs (99.90%). JOMEs were analytically characterized using GLC and FTIR. The fuel properties of produced JOMEs were in accordance to ASTM D6751 and EN 14214 standards.

Application of Response Surface Methodology for Optimization of Biodiesel Production from Microalgae Through Nanocatalytic Transesterification Process.

2021 ◽  
Author(s):  
Vaishali Mittal ◽  
Uttam Kumar Ghosh
Keyword(s):  
Response Surface Methodology ◽  
Reaction Time ◽  
Response Surface ◽  
Process Parameters ◽  
Reaction Temperature ◽  
Methyl Esters ◽  
Biodiesel Production ◽  
Molar Ratio ◽  
Impregnation Method ◽  
The Impact

Abstract Production of biodiesel from microalgae is gaining popularity since it does not compromise food security or the global economy. This article reports biodiesel production with Spirulina microalgae through nanocatalytic transesterification process. The nanocatalyst calcium methoxide Ca(OCH3)2 was synthesized using wet impregnation method and utilized to carry out the transesterification process. The nanocatalyst was characterized to evaluate its structural and spectral characteristics using different characterization techniques such as Thermogravimetric analysis (TGA), X-ray diffraction (XRD), Scanning electron microscopy (SEM), Fourier transform infrared spectroscopy (FT-IR), and Brunaeur-Emmett-Teller(BET) measurement for surface area. The result demonstrates that calcium methoxide Ca(OCH3)2 possesses a high catalytic activity compared to a heterogeneous catalyst such as calcium oxide (CaO). The impact of several process parameters such as reaction temperature, the molar ratio of methanol to oil, catalyst concentration, and reaction time used in the transesterification process was optimized by employing central composite design(CCD) based response surface methodology(RSM). The polynomial regression equation of second order was obtained for methyl esters. The model projected a 99% fatty acid methyl esters (FAME) yield for optimal process parameters of reaction time 3hrs,3 wt.% of Ca(OCH3)2 catalyst loading, 80°C reaction temperature, and 30:1 methanol to oil molar ratio.

Heterogeneous Catalyst for Transesterification of Biodiesel Synthesis

2012 ◽  
Vol 622-623 ◽  
pp. 1204-1208
Author(s):  
Amar P. Pandhare ◽  
Atul S. Padalkar
Keyword(s):  
Heterogeneous Catalyst ◽  
Reaction Temperature ◽  
Rural Economy ◽  
Heterogeneous Catalysts ◽  
Methyl Esters ◽  
Cetane Number ◽  
Molar Ratio ◽  
Catalyst Loading ◽  
Jatropha Oil ◽  
Biodiesel Synthesis

The awareness on biodiesel in developing countries in the recent times has been increased. Several activities have been picked up for its production especially with a view to boost the rural economy. In the present investigation biodiesel was prepared from jatropha curcas seed oil (non edible oil). Before exploiting any plant for industrial application, it is imperative to have complete information about its biology, chemistry, and all other applications so that the potential of plant could be utilized maximally. Biodiesel was prepared by transesterification process of jatropha oil with methanol in heterogeneous system, using heterogeneous catalyst. The heterogeneous catalysts are environment friendly and render the process simplified. Calcination process was followed by the dependence of the conversion of jatropha oil on the reaction variables such as the catalyst loading; the molar ratio of the methanol to oil, reaction temperature agitation speed and the reaction time was studied. The conversion was over 89% at a reaction temperature of 70oC and molar ratio 12:1. Finally, Jatropha oil methyl esters was characterized to test its properties as fuels in diesel engines, such as viscosity, flash point, cetane number. Results showed that biodiesel obtained under the optimum conditions is an excellent substitute for fossil fuels.

Application of Calcium Methoxide as Solid Base Catalyst for Biodiesel Production from Waste Cooking Oil

2016 ◽  
Vol 723 ◽  
pp. 594-598 ◽  
Author(s):  
Nichaonn Chumuang ◽  
Vittaya Punsuvon
Keyword(s):  
Reaction Temperature ◽  
Catalyst Concentration ◽  
Waste Cooking Oil ◽  
Transesterification Reaction ◽  
Biodiesel Production ◽  
Molar Ratio ◽  
Solid Base ◽  
Base Catalyst ◽  
Solid Base Catalyst ◽  
Cooking Oil

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.

Esterification of Menthol and Lactic Acid by Silicotungstic Acid Catalyst Supported on Bentonite

2013 ◽  
Vol 634-638 ◽  
pp. 647-650
Author(s):  
Jian Zhong Jin ◽  
Na Bo Sun
Keyword(s):  
Lactic Acid ◽  
Reaction Time ◽  
Reaction Temperature ◽  
Acid Catalyst ◽  
Molar Ratio ◽  
Main Reaction ◽  
Silicotungstic Acid ◽  
Optimum Conditions ◽  
Reaction Parameters ◽  
Acid Loading

The silicotungstic acid catalyst supported on bentonite was employed in the esterification of menthol and lactic acid. The main reaction parameters were silicotungstic acid loading on bentonite, the amounts of catalyst, molar ratio of reactants, reaction temperature and reaction time. The optimum conditions were determined as follows : silicotungstic acid loading on bentonite 50 wt %, catalyst 1.25 g , mole ratio of menthol to lactic acid 1:1.1, reaction temperature 130 °C and reaction time 3 h . The esterification yield of menthyl lactiate was about 83.97 %. The catalyst could be used repeatedly for many times without distinct loss in activity.

scholarly journals Comprehensive Comparison of Hetero-Homogeneous Catalysts for Fatty Acid Methyl Ester Production from Non-Edible Jatropha curcas Oil

Catalysts ◽  
2021 ◽  
Vol 11 (12) ◽  
pp. 1420
Author(s):  
Khawer Khan ◽  
Noaman Ul-Haq ◽  
Wajeeh Ur Rahman ◽  
Muzaffar Ali ◽  
Umer Rashid ◽  
...  
Keyword(s):  
Fatty Acid ◽  
Reaction Time ◽  
Jatropha Curcas ◽  
Low Cost ◽  
Methyl Esters ◽  
Maximum Yield ◽  
Acid Methyl Ester ◽  
Molar Ratio ◽  
Acid Methyl ◽  
Comprehensive Comparison

The synthesis of biodiesel from Jatropha curcas by transesterification is kinetically controlled. It depends on the molar ratio, reaction time, and temperature, as well as the catalyst nature and quantity. The aim of this study was to explore the transesterification of low-cost, inedible J. curcas seed oil utilizing both homogenous (potassium hydroxide; KOH) and heterogenous (calcium oxide; CaO) catalysis. In this effort, two steps were used. First, free fatty acids in J. curcas oil were reduced from 12.4 to less than 1 wt.% with sulfuric acid-catalyzed pretreatment. Transesterification subsequently converted the oil to biodiesel. The yield of fatty acid methyl esters was optimized by varying the reaction time, catalyst load, and methanol-to-oil molar ratio. A maximum yield of 96% was obtained from CaO nanoparticles at a reaction time of 5.5 h with 4 wt.% of the catalyst and an 18:1 methanol-to-oil molar ratio. The optimum conditions for KOH were a molar ratio of methanol to oil of 9:1, 5 wt.% of the catalyst, and a reaction time of 3.5 h, and this returned a yield of 92%. The fuel properties of the optimized biodiesel were within the limits specified in ASTM D6751, the American biodiesel standard. In addition, the 5% blends in petroleum diesel were within the ranges prescribed in ASTM D975, the American diesel fuel standard.

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