# Optimization of Conversion of High Free Fatty AcidJatropha curcas Oil to Biodiesel Using Response Surface Methodology

Authors: Prerna Goyal; M. P. Sharma; Siddharth Jain
Journal: ISRN Chemical Engineering
 (2012)

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## Abstract

A five-level-four-factor central composite design (CCD) with 54 assays was employed to study the effect of catalyst concentration (NaOH), reaction temperature, reaction time, and methanol/oil molar ratio on the methyl esters yield fromJatropha curcas oil (JCO) during its transesterification. Using response surface methodology (RSM), a quadratic polynomial equation was obtained for Jatropha curcas biodiesel (JCB) yield by regression analysis. Verification experiments confirmed the validity of the predicted model. The high free fatty acids (FFAs) (14.6%) of JCO could be reduced to 0.34% by acid-catalyzed esterification and a JCB yield of 98.3% was obtained with methanol/oil ratio (11 : 1) using NaOH as catalyst (1% w/w) in 110 min time at 55°C temperature. The predicted value of JCB yield is found to be in good agreement with the experimental value at the optimum level of input parameters. The properties of the biodiesel, thus, produced conform to the ASTM and IS specifications, making it an ideal alternative fuel for diesel engines. The model can be effectively used in oil industry to maximize the biodiesel yield from given oil.


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## Body

## 1. Introduction

The rapid increase in energy demand and fast depletion of fossil fuel resources has led to the search for alternative energy sources. Biodiesel, a renewable and biodegradable fuel, has generated considerable interest as a substitute to petrodiesel in recent years. Presently, the main focus is being placed to explore the nonedible oil resources likeJatropha, Pongamia, Mahua, and Neem as a potential source for biodiesel. Jatropha curcas L. oil (JCO) has been assigned top priority by the Government of India as feedstock for biodiesel production, and accordingly, Jatropha curcas plantations are cultivated on about 400,000 ha of land under National Biodiesel Mission of the Government of India, and the oil is expected to be available for biodiesel production in the coming years. The oil can be converted to biodiesel using transesterification, but the type of transesterification to be adopted depends on the free fatty acid (FFA) content of the oil. For the conversion of high FFA JCO, two-step acid-base catalyzed method has been-developed [1] which consists of acid-catalyzed pretreatment/esterification step to reduce the FFA to less than 1% using H2SO4 as acid catalyst and transesterification of pretreated oil to biodiesel using alkali catalyst. Its basic objective is to maximize the yield of biodiesel and to achieve higher conversion efficiency of biodiesel production. Different oils are found to contain varying amount of FFAs with ageing and the same holds true for JCO which emphasizes the need for optimization of biodiesel production from JCO in order to maximize the JCB yield. The literature revealed that only few papers are available on the use of response surface methodology (RSM) for the optimization of process variables to maximize the biodiesel yield. Boonmee et al. [2] have studied the effect of three process variables, namely, methanol-to-oil molar ratio, catalyst concentration, and reaction time on the methyl esters yield of JCO using a central composite design (CCD) of 20 experiments and achieved 99.87% biodiesel yield. Similarly, Tiwari et al. [3] have optimized only two variables, namely, methanol quantity and reaction time using RSM based on five-level-two-factor central composite rotatable design (CCRD) of 21 experiments and obtained biodiesel yield of 99%. The effect of catalyst concentration, reaction temperature, reaction time, and methanol-to-oil ratio on the fatty acid methyl ester (FAME) yield of palm oil was studied by Chin et al. [4] using CCRD. In all, 30 experiments were conducted and a quadratic polynomial equation was obtained for evaluating biodiesel yield by multiple regression analysis. Biodiesel yield of 72% was achieved. Jeong and Park [5] further investigated the effect of three variables, namely, reaction temperature, oil-to-methanol molar ratio, and catalyst quantity (KOH) on biodiesel yield from castor oil using CCRD in 20 experimental runs and obtained about 92% yield. The effect of above the three variables on the biodiesel yield from animal fat (Lard) was studied by Jeong et al. [6], using CCRD in 20 experiments and achieved 97.8% yield. The study on the effect of four variables, namely, catalyst concentration, reaction temperature, time and methanol/oil ratio on biodiesel yield from high FFA waste rapeseed oil was examined by Yuan et al. [7] using CCD in 30 experimental runs and reported that the catalyst concentration and reaction time were the limiting conditions and obtained 83% yield. RSM-based CCRD was used to optimize four process variables: methanol/oil molar ratio, catalyst (NaOCH3) concentration, reaction temperature, and reaction time to produce rice bran oil methyl ester in 30 experimental assays by Rashid et al. [8], who obtained 83.3% biodiesel yield. In view of the above, it can be seen that most of the authors have optimized biodiesel yield using three process variables while few concentrated on four variables using the same optimization technique. No work is reported on optimization of biodiesel yield from JCO using four variables. The present paper, therefore, reports the results of the optimization of four process variables, namely, catalyst (NaOH) concentration (0–2% w/w), reaction temperature (35°–55°C), reaction time (30–180 min), and methanol/oil ratio (w/w) (6 : 1–12 : 1) for transesterification of high FFA JCO using RSM-based CCD to maximize the JCB yield with the help of Design Expert 8.0.6 software. A model to predict the response (JCB yield (%)) was formulated and validated by analysis of variance (ANOVA). A total of 54 experiments were conducted to get the response experimentally. The experimental results were found in good agreement with the predicted response, thereby proving the credibility of the model.


## 2. Materials and Methods

JCO was procured from Jatropha Vikas Sansthan, New Delhi India. All chemicals like H2SO4, KOH, methanol, ethanol, Na2SO4, and NaOH were of analytical reagent grade and 99% pure. NaOH in pellet form was used as a base catalyst.


### 2.1. Pretreatment of High FFA JCO

Raw JCO was filtered to remove all insoluble impurities followed by heating at 100°C for 10 min to remove all the moisture. JCO had high FFA (14.60%), far above the 1% limit suitable for base catalyzed transesterification reaction. FFAs were, therefore, first converted to esters in a pretreatment process developed by the authors in their laboratory for the production of JCB [1]. The reaction was carried out at a temperature of 50°C for 125 min using conc. H2SO4 (1.5% v/v) as acid catalyst and methanol as a solvent with methanol/oil ratio of 6.5 : 1, and high FFAs were first reduced to 0.34% through esterification and the resulting reaction mixture was finally subjected to base catalyzed transesterification process for biodiesel production.


### 2.2. Base Catalyzed Transesterification of JCO

Pretreated JCO was transesterified by using methanol and NaOH as base catalyst for the production of JCB [1]. The methyl ester layer was separated, washed with water, heated to remove moisture, and dried over anhydrous Na2SO4. The transesterification of JCO has been optimized using RSM for the maximization of JCB yield which was calculated using the following:
(1)YieldofJCB(%)=TotalweightofmethylestersTotalweightofoilinthesample*100%.


### 2.3. Analysis of JCB

The JCB was prepared in the laboratory under the operating conditions optimized by RSM-based CCD. The JCB was analyzed for fatty acid composition using gas chromatograph (Model: Netal). The process is already described by Jain and Sharma [1].


### 2.4.1H-NMR Spectroscopy of JCB

1H-NMR spectrometer (Model: Bruker DRX-600) available at Institute Instrumentation Centre (IIC) operating at 500 MHz and using deuterated chloroform (CDCl3) as a solvent was used to analyze the purity of JCB.


### 2.5. Physiochemical Properties of JCB

The physical and chemical properties of JCB produced under optimum conditions were determined by using standard methods [9].


### 2.6. Experimental Design Based on RSM

A five-level, four-factor CCD was applied for carrying out the optimization studies to maximize the JCB yield. Catalyst concentration (A) (%), reaction temperature (B) (°C), reaction time (min) (C), and methanol-to-oil molar ratio (w/w) (D) were the independent variables selected to optimize the yield of JCB. The coded and uncoded levels of the independent variables are given in Table 1.Table 1
Independent variables and levels used for CCD in transesterification process.
Serial number
Variables
Symbols
Levels
−1
−0.5
0
0.5
1
1
Catalystconcentration (% w/w)
A
0
0.5
1.0
1.5
2.0
2
Temperature (°C)
B
35
40
45
50
55
3
Time (min)
C
30
67.5
105
142.5
180
4
Methanol-to-oil ratio (w/w)
D
6
7.5
9
10.5
12


### 2.7. Statistical Analysis

The Design Expert 8.0.6 software was used for the regression and graphical analysis of the data. The maximum values of JCB yield were taken as the response of the design experiment. The experimental data obtained by the above procedure was analyzed by the response surface regression using the following second-order polynomial:(2)y=βo+∑i=1kβixi+∑i=1kβiixi2+∑ii>jk∑jkβijxixj,
where y is the response (JCB %), i and j are the linear and quadratic coefficients, respectively, βo is the regression co-efficient, and k is the number of factors studied and optimized in the experiment. Statistical analysis of the model was carried out to evaluate the ANOVA. Confirmatory experiments were also carried out to validate the equation.


## 2.1. Pretreatment of High FFA JCO

Raw JCO was filtered to remove all insoluble impurities followed by heating at 100°C for 10 min to remove all the moisture. JCO had high FFA (14.60%), far above the 1% limit suitable for base catalyzed transesterification reaction. FFAs were, therefore, first converted to esters in a pretreatment process developed by the authors in their laboratory for the production of JCB [1]. The reaction was carried out at a temperature of 50°C for 125 min using conc. H2SO4 (1.5% v/v) as acid catalyst and methanol as a solvent with methanol/oil ratio of 6.5 : 1, and high FFAs were first reduced to 0.34% through esterification and the resulting reaction mixture was finally subjected to base catalyzed transesterification process for biodiesel production.


## 2.2. Base Catalyzed Transesterification of JCO

Pretreated JCO was transesterified by using methanol and NaOH as base catalyst for the production of JCB [1]. The methyl ester layer was separated, washed with water, heated to remove moisture, and dried over anhydrous Na2SO4. The transesterification of JCO has been optimized using RSM for the maximization of JCB yield which was calculated using the following:
(1)YieldofJCB(%)=TotalweightofmethylestersTotalweightofoilinthesample*100%.


## 2.3. Analysis of JCB

The JCB was prepared in the laboratory under the operating conditions optimized by RSM-based CCD. The JCB was analyzed for fatty acid composition using gas chromatograph (Model: Netal). The process is already described by Jain and Sharma [1].


## 2.4.1H-NMR Spectroscopy of JCB

1H-NMR spectrometer (Model: Bruker DRX-600) available at Institute Instrumentation Centre (IIC) operating at 500 MHz and using deuterated chloroform (CDCl3) as a solvent was used to analyze the purity of JCB.


## 2.5. Physiochemical Properties of JCB

The physical and chemical properties of JCB produced under optimum conditions were determined by using standard methods [9].


## 2.6. Experimental Design Based on RSM

A five-level, four-factor CCD was applied for carrying out the optimization studies to maximize the JCB yield. Catalyst concentration (A) (%), reaction temperature (B) (°C), reaction time (min) (C), and methanol-to-oil molar ratio (w/w) (D) were the independent variables selected to optimize the yield of JCB. The coded and uncoded levels of the independent variables are given in Table 1.Table 1
Independent variables and levels used for CCD in transesterification process.
Serial number
Variables
Symbols
Levels
−1
−0.5
0
0.5
1
1
Catalystconcentration (% w/w)
A
0
0.5
1.0
1.5
2.0
2
Temperature (°C)
B
35
40
45
50
55
3
Time (min)
C
30
67.5
105
142.5
180
4
Methanol-to-oil ratio (w/w)
D
6
7.5
9
10.5
12


## 2.7. Statistical Analysis

The Design Expert 8.0.6 software was used for the regression and graphical analysis of the data. The maximum values of JCB yield were taken as the response of the design experiment. The experimental data obtained by the above procedure was analyzed by the response surface regression using the following second-order polynomial:(2)y=βo+∑i=1kβixi+∑i=1kβiixi2+∑ii>jk∑jkβijxixj,
where y is the response (JCB %), i and j are the linear and quadratic coefficients, respectively, βo is the regression co-efficient, and k is the number of factors studied and optimized in the experiment. Statistical analysis of the model was carried out to evaluate the ANOVA. Confirmatory experiments were also carried out to validate the equation.


## 3. Results and Discussions

A total of 54 experiments were performed to get the experimental values of JCB yield. Experimental and predicted values for JCB yield responses at the design points and all the four variables in uncoded form are given in Table2. The summary of ANOVA is provided in Table 3. The associated probability (P) value for the model is lower than 0.05 (i.e., α=0.05 or 95% confidence) implying the significance of the model. The value of regression coefficient R2 for the model is 0.945, indicating the good fitness of the model. A high value of predicted R2 (0.890) is an indication of precision of fitted model. The more the value of R2 approaches unity, the better the model fits the experimental data. The value of the adjusted coefficient of determination (RAdj2: 0.923) is also high, thus indicating the significance of the model. The value of coefficient of variation (CV) is low (2.09%), thereby indicating the reliability of the results of the fitted model [8].Table 2
CCD arrangement and responses for JCB yield.
Run
Parameter 1
Parameter 2
Parameter 3
Parameter 4
Experimental response
Predicted response
A: catalyst concentration (%)
B: temperature (°C)
C: time (min)
D: methanol/oil ratio
JCB yield(%)
JCB yield(%)
1
1
45
105
9
82.6
82.84
2
0
45
105
9
89.5
89.81
3
0.5
40
67.5
10.5
78.2
80.37
4
1.5
40
142.5
10.5
88.6
87.84
5
0.5
40
67.5
10.5
77.8
80.37
6
0.5
50
67.5
7.5
87.1
86.76
7
1.5
50
67.5
10.5
73.9
76.50
8
0.5
40
142.5
7.5
91
89.83
9
1
45
105
9
82.9
82.84
10
0.5
40
67.5
7.5
86.1
87.33
11
1
45
105
9
83.1
82.84
12
1
45
105
12
85.5
84.97
13
1
45
105
9
82.1
82.84
14
1
45
180
9
93.4
92.65
15
0.5
50
142.5
10.5
97.8
99.99
16
1
45
30
9
78.2
79.56
17
1.5
50
142.5
10.5
88.3
87.10
18
0.5
50
67.5
10.5
90
87.17
19
0.5
40
142.5
10.5
91.8
91.86
20
1.5
40
67.5
7.5
85.7
84.18
21
0.5
50
142.5
7.5
90
90.98
22
1
35
105
9
92.4
91.00
23
1.5
40
142.5
7.5
81.6
84.05
24
1.5
40
142.5
10.5
83.8
87.84
25
1
45
105
12
85.9
84.97
26
0.5
50
67.5
10.5
90.4
87.17
27
1.5
40
67.5
10.5
80
78.97
28
2
45
105
9
73
73.37
29
1
55
105
9
88.2
89.69
30
1.5
50
142.5
7.5
77
75.94
31
1.5
40
67.5
7.5
85.2
84.18
32
1
45
105
9
82.4
82.84
33
1
55
105
9
87.9
89.69
34
1.5
50
67.5
10.5
74.1
76.50
35
1.5
50
67.5
7.5
74.8
74.34
36
1.5
50
142.5
7.5
77.3
75.94
37
1.5
40
67.5
10.5
80.2
78.97
38
1
45
105
9
82.8
82.84
39
0.5
50
67.5
7.5
87.5
86.76
40
2
45
105
9
73.2
73.37
41
1
45
105
6
79.5
80.76
42
1.5
50
67.5
7.5
74.5
74.34
43
0
45
105
9
89.9
89.81
44
1.5
40
142.5
7.5
81.2
84.05
45
0.5
50
142.5
7.5
90.4
90.98
46
0.5
50
142.5
10.5
98.2
99.98
47
1
35
105
9
92.1
91.00
48
1
45
105
6
79.8
80.76
49
0.5
40
67.5
7.5
86.5
87.33
50
0.5
40
142.5
10.5
92.1
91.86
51
1
45
30
9
78.5
79.56
52
0.5
40
142.5
7.5
91.4
89.83
53
1.5
50
142.5
10.5
88.7
87.10
54
1
45
180
9
93.7
92.65Table 3
ANOVA for response surface quadratic model.
Source
Sum of squares
Degree of freedom (df)
Mean square
F value
P value prob > F
Model
2078.70
14
148.48
47.43
<0.0001
A: catalyst concentration
815.10
1
815.10
260.35
<0.0001
B: temperature
6.75
1
6.75
2.16
0.1500
C: time
520.08
1
520.08
166.12
<0.0001
D: methanol/oil molar ratio
53.76
1
53.76
17.17
0.0002
A
B
172.05
1
172.05
54.95
<0.0001
A
C
13.78
1
13.78
4.40
0.0424
A
D
6.13
1
6.13
1.96
0.1698
B
C
5.78
1
5.78
1.85
0.1820
B
D
108.78
1
108.78
34.75
<0.0001
C
D
162.90
1
162.90
52.03
<0.0001
A
2
4.19
1
4.19
1.34
0.2541
B
2
149.83
1
149.83
47.86
<0.0001
C
2
28.97
1
28.97
9.25
0.0042
D
2
0.0001157
1
0.0001157
0.00003697
0.9848
Residual
122.10
39
3.13
CV: 2.09%,Rmodel2: 0.945,  RAdj.2: 0.923, and predicted Rmodel2: 0.890.P values < 0.05 indicate that the model terms are significant [10]. In this case, A (catalyst concentration), C (time), D (ratio of methanol/oil), interaction effect of AB (catalyst concentration with reaction temperture), AC (catalyst concentration with reaction time), BD (reaction temperature with methanol/oil ratio), CD (time with ratio of methanol/oil), B2 (quadratic effect of temparature), C2 (quadratic effect of time) have significant effect on the JCB yield. The regression equation (3) for the determination of predicted values of output parameter (i.e., JCB in this study) is given as follows:
(3)JCB(%)=343.90+34.43A-8.34B-0.46C-15.19D-0.93AB-0.035AC+0.58AD+0.0023BC+0.25BD+0.04CD-1.25A2+0.075B2+0.0006C2+0.0023D2.The graph between the predicted and actual JCB yield (%) given in Figure1 shows that the predicted values are quite close to the experimental values, thereby validating the reliability of the model developed for establishing a correlation between the process variables and the JCB yield.Figure 1
Predicted versus actual JCB (%) yield values.


### 3.1. Effect of Process Parameters on JCB Yield

Figure2 shows the effect of catalyst concentration (NaOH), reaction temperature, reaction time, and molar ratio of methanol/oil on JCB yield. It can be seen from the figure that the JCB yield decreases significantly with an increase in catalyst concentration. This may be due to the fact that addition of excessive catalyst causes more triglyceride to react with the alkali catalyst leading to the formation of soap, which decreases the biodiesel yield [11]. JCB yield decreases with an increase in temperature till the middle point is reached, after that it increases. The increase in biodiesel yield at higher temperature is due to the fact that viscosity of oils decreases at high temperature and results in an increased reaction rate and shortened reaction time, thereby, increasing the biodiesel yield [11]. Reaction time has a positive effect on the JCB yield, as it increases with increase in time. This can be supported by the work of Freedman et al. [12] who found that the conversion rate of fatty acid esters increases with reaction time. At the beginning, the reaction is slow due to the mixing and dispersion of alcohol into the oil. After a while, the reaction proceeds very fast, thereby increasing the biodiesel yield. Yield of JCB is found to increase with the increase in methanol/oil ratio; since the transesterification reaction is reversible in nature, so excess alcohol is added to ensure the total conversion of triglycerides [11]. Thus, the yield of biodiesel increases with an increase in methanol quantity.Figure 2
Effect of catalyst concentration, temperature, time, and methanol/oil ratio on JCB (%) yield.3D response surfaces, which are the representation of the relationship between the responses and process parameters, are shown in Figures3(a)–3(f). Figure 3(a) shows the influence of catalyst concentration (NaOH) and temperature on the JCB yield. It can be seen that JCB yield increases with an an increase in reaction temperature at low amount of catalyst. Being an equilibrium reaction, the equilibrium constant is influenced by temperature; therefore, as the temperature increase, JCB yield also increases. However, JCB yield decreases at high temperature for high catalyst concentration. This may be due to the diffusion resistance between different phases of oil-methanol-catalyst at high amounts of catalyst. These results are similar to the findings of Chin et al. [4]. The influence of catalyst concentration and time on the JCB yield is shown in Figure 3(b) which indicates that the JCB yield increases with increase in reaction time at low catalyst concentration while it decreases at high catalyst concentration and high temperature and is supported by the work of Rashid et al. [8]. Figure 3(c) gives the effect of catalyst concentration and ratio of methanol/oil on the JCB yield. The contours do not have any significant effect on the JCB yield. Figure 3(d) establishes the interaction of temperature and reaction time on the JCB yield and shows that the interaction effect of reaction temperature and time has a favorable effect on increasing the JCB yield and is similar to the finding of Rashid et al. [8]. The effect of temperature and quantity of methanol given in Figure 3(e) indicates that the JCB yield increases at higher temperature and high methanol/oil ratio. This may be due to the fact that excess methanol can promote the transesterification reaction forward and increase the biodiesel yield. Figure 3(f) shows the influence of reaction time and quantity of methanol on the JCB yield. The biodiesel yield increases at higher time and high methanol/oil ratio because the conversion rate of triglycerides increases with time and excess methanol favors the complete conversion to biodiesel.(a) Response surface of JCB: effect of catalyst concentration and temperature. (b) Response surface of JCB: effect of catalyst concentration and time. (c) Response surface of JCB: effect of catalyst concentration and methanol/oil ratio.  (d) Response surface of JCB: Effect of temperature and time.  (e) Response surface of JCB: effect of temperature and methanol/oil ratio.  (f) Response surface of JCB: effect of time and methanol/oil ratio.
(a)
(b)
(c)
(d)
(e)
(f)


### 3.2. Optimization of Response Parameters

Optimization of individual responses was performed separately to achieve the desired maximization of JCB yield based on the developed mathematical model (i.e., (3)). The “Design Expert 8.0.6” software was used to optimize the response, and the value of the response (JCB yield) was set at maximum. The optimal value of input process parameters is given in Table 4. An experiment was carried out at the optimal parametric settings for JCB yield to obtain the targeted value of response parameter. The table shows the predicted value of JCB yield derived from the regression equation as well as the experimental result obtained by the optimal setting of the parameters. Predicted response is found to be in good agreement with the experimental results with an error of <±1%.Table 4
Optimized input process parameters and optimum value of JCB yield.
Response
Optimized value of input process
Modified value of input process
Predictedvalue
Experimentalvalue
Error%
parameters
parameters
A
B
C
D
A
B
C
D
JCB yield (%)
0.80
54.42
109.32
11.07
1.0
55
110
11
98.89
98.3
0.6


### 3.3. Analysis of JCB

The fatty acid (FA) composition of JCB prepared under the above optimum parameters and determined by gas chromatography (GC) is given in Table5 which shows that JCB mainly contained oleic and linoleic acids. The FA composition is in good agreement with the composition reported by Jain and Sharma [9]. 1H-NMR spectra of JCB showed a singlet in δ 3.68 ppm which is characteristic of methyl ester protons, and multiplet in δ 4.12–4.24 and δ 5.30–5.34 is attributed to oxymethylic hydrogen that is characteristic of triglycerides from Jatropha oil and is comparable with  1H-NMR spectral value of JCB reported in the literature [13], thereby indicating the purity of biodiesel prepared. From the NMR data, it was verified that Jatropha oil conversion into biodiesel was quite complete. The physio-chemical properties of JCB are reported in Table 6. The properties of JCB are in good accord with ASTM and IS specifications.Table 5
Fatty acid composition of JCB.
Serial number
Fatty acid
Formula
% Composition
1
Palmitic acid
C16H32O2
16.2
CH3(CH2)14COOH
2
Stearic acid
C18H36O2
8.2
CH3(CH2)16COOH
3
Oleic acid
C18H34O2
38.4
CH3(CH2)7–CH=CH–(CH2)7COOH
4
Linoleic acid
C18H32O2
36.8
CH3(CH2)4CH=CH–CH2–CH=CH– (CH2)7COOH
5
Linolenic acid
C18H30O2
0.4
CH3(CH2)4CH=CH–CH2–CH=CH–CH2–CH=CH–(CH2)4COOHTable 6
Physicochemical properties of JCB.
Serial number
Property (unit)
ASTM D6751
IS 15607
JCB prepared under optimum parameters
JCB [9]
ASTM D6751 limits
IS 15607 limits
1
Viscosity (cSt; 40°C)
ASTM D445
IS 1448
4.9
4.38
1.9–6.0
2.5–6.0
2
Density (g/c·c at 15°C)
ASTM D4052
IS 1448
0.862
—
—
0.860–0.900
3
Flash point (°C)
ASTM D93
IS 1448
174
172
Minimum  of 130
—
4
Water and sediment (Vol %)
D2709
D2709
0.05
0.05
Maximum of 0.05
Maximum of 0.05
5
Free glycerin (% mass)
D6584
D6584
0.01
0.01
Maximum of 0.02
D6584
6
Oxidative stability of JCB (h)
EN14112
—
3.3
3.27
3
—
7
Free glycerol
D6584
D6584
0.015
0.01
Maximum of 0.02
Maximum of 0.02
8
Total glycerol
D6584
D6584
0.14
0.12
Maximum of 0.25
Maximum of 0.25
9
Ester content (%)
—
EN 14103
98.3
98.5
—
Minimum of 96.5


## 3.1. Effect of Process Parameters on JCB Yield

Figure2 shows the effect of catalyst concentration (NaOH), reaction temperature, reaction time, and molar ratio of methanol/oil on JCB yield. It can be seen from the figure that the JCB yield decreases significantly with an increase in catalyst concentration. This may be due to the fact that addition of excessive catalyst causes more triglyceride to react with the alkali catalyst leading to the formation of soap, which decreases the biodiesel yield [11]. JCB yield decreases with an increase in temperature till the middle point is reached, after that it increases. The increase in biodiesel yield at higher temperature is due to the fact that viscosity of oils decreases at high temperature and results in an increased reaction rate and shortened reaction time, thereby, increasing the biodiesel yield [11]. Reaction time has a positive effect on the JCB yield, as it increases with increase in time. This can be supported by the work of Freedman et al. [12] who found that the conversion rate of fatty acid esters increases with reaction time. At the beginning, the reaction is slow due to the mixing and dispersion of alcohol into the oil. After a while, the reaction proceeds very fast, thereby increasing the biodiesel yield. Yield of JCB is found to increase with the increase in methanol/oil ratio; since the transesterification reaction is reversible in nature, so excess alcohol is added to ensure the total conversion of triglycerides [11]. Thus, the yield of biodiesel increases with an increase in methanol quantity.Figure 2
Effect of catalyst concentration, temperature, time, and methanol/oil ratio on JCB (%) yield.3D response surfaces, which are the representation of the relationship between the responses and process parameters, are shown in Figures3(a)–3(f). Figure 3(a) shows the influence of catalyst concentration (NaOH) and temperature on the JCB yield. It can be seen that JCB yield increases with an an increase in reaction temperature at low amount of catalyst. Being an equilibrium reaction, the equilibrium constant is influenced by temperature; therefore, as the temperature increase, JCB yield also increases. However, JCB yield decreases at high temperature for high catalyst concentration. This may be due to the diffusion resistance between different phases of oil-methanol-catalyst at high amounts of catalyst. These results are similar to the findings of Chin et al. [4]. The influence of catalyst concentration and time on the JCB yield is shown in Figure 3(b) which indicates that the JCB yield increases with increase in reaction time at low catalyst concentration while it decreases at high catalyst concentration and high temperature and is supported by the work of Rashid et al. [8]. Figure 3(c) gives the effect of catalyst concentration and ratio of methanol/oil on the JCB yield. The contours do not have any significant effect on the JCB yield. Figure 3(d) establishes the interaction of temperature and reaction time on the JCB yield and shows that the interaction effect of reaction temperature and time has a favorable effect on increasing the JCB yield and is similar to the finding of Rashid et al. [8]. The effect of temperature and quantity of methanol given in Figure 3(e) indicates that the JCB yield increases at higher temperature and high methanol/oil ratio. This may be due to the fact that excess methanol can promote the transesterification reaction forward and increase the biodiesel yield. Figure 3(f) shows the influence of reaction time and quantity of methanol on the JCB yield. The biodiesel yield increases at higher time and high methanol/oil ratio because the conversion rate of triglycerides increases with time and excess methanol favors the complete conversion to biodiesel.(a) Response surface of JCB: effect of catalyst concentration and temperature. (b) Response surface of JCB: effect of catalyst concentration and time. (c) Response surface of JCB: effect of catalyst concentration and methanol/oil ratio.  (d) Response surface of JCB: Effect of temperature and time.  (e) Response surface of JCB: effect of temperature and methanol/oil ratio.  (f) Response surface of JCB: effect of time and methanol/oil ratio.
(a)
(b)
(c)
(d)
(e)
(f)


## 3.2. Optimization of Response Parameters

Optimization of individual responses was performed separately to achieve the desired maximization of JCB yield based on the developed mathematical model (i.e., (3)). The “Design Expert 8.0.6” software was used to optimize the response, and the value of the response (JCB yield) was set at maximum. The optimal value of input process parameters is given in Table 4. An experiment was carried out at the optimal parametric settings for JCB yield to obtain the targeted value of response parameter. The table shows the predicted value of JCB yield derived from the regression equation as well as the experimental result obtained by the optimal setting of the parameters. Predicted response is found to be in good agreement with the experimental results with an error of <±1%.Table 4
Optimized input process parameters and optimum value of JCB yield.
Response
Optimized value of input process
Modified value of input process
Predictedvalue
Experimentalvalue
Error%
parameters
parameters
A
B
C
D
A
B
C
D
JCB yield (%)
0.80
54.42
109.32
11.07
1.0
55
110
11
98.89
98.3
0.6


## 3.3. Analysis of JCB

The fatty acid (FA) composition of JCB prepared under the above optimum parameters and determined by gas chromatography (GC) is given in Table5 which shows that JCB mainly contained oleic and linoleic acids. The FA composition is in good agreement with the composition reported by Jain and Sharma [9]. 1H-NMR spectra of JCB showed a singlet in δ 3.68 ppm which is characteristic of methyl ester protons, and multiplet in δ 4.12–4.24 and δ 5.30–5.34 is attributed to oxymethylic hydrogen that is characteristic of triglycerides from Jatropha oil and is comparable with  1H-NMR spectral value of JCB reported in the literature [13], thereby indicating the purity of biodiesel prepared. From the NMR data, it was verified that Jatropha oil conversion into biodiesel was quite complete. The physio-chemical properties of JCB are reported in Table 6. The properties of JCB are in good accord with ASTM and IS specifications.Table 5
Fatty acid composition of JCB.
Serial number
Fatty acid
Formula
% Composition
1
Palmitic acid
C16H32O2
16.2
CH3(CH2)14COOH
2
Stearic acid
C18H36O2
8.2
CH3(CH2)16COOH
3
Oleic acid
C18H34O2
38.4
CH3(CH2)7–CH=CH–(CH2)7COOH
4
Linoleic acid
C18H32O2
36.8
CH3(CH2)4CH=CH–CH2–CH=CH– (CH2)7COOH
5
Linolenic acid
C18H30O2
0.4
CH3(CH2)4CH=CH–CH2–CH=CH–CH2–CH=CH–(CH2)4COOHTable 6
Physicochemical properties of JCB.
Serial number
Property (unit)
ASTM D6751
IS 15607
JCB prepared under optimum parameters
JCB [9]
ASTM D6751 limits
IS 15607 limits
1
Viscosity (cSt; 40°C)
ASTM D445
IS 1448
4.9
4.38
1.9–6.0
2.5–6.0
2
Density (g/c·c at 15°C)
ASTM D4052
IS 1448
0.862
—
—
0.860–0.900
3
Flash point (°C)
ASTM D93
IS 1448
174
172
Minimum  of 130
—
4
Water and sediment (Vol %)
D2709
D2709
0.05
0.05
Maximum of 0.05
Maximum of 0.05
5
Free glycerin (% mass)
D6584
D6584
0.01
0.01
Maximum of 0.02
D6584
6
Oxidative stability of JCB (h)
EN14112
—
3.3
3.27
3
—
7
Free glycerol
D6584
D6584
0.015
0.01
Maximum of 0.02
Maximum of 0.02
8
Total glycerol
D6584
D6584
0.14
0.12
Maximum of 0.25
Maximum of 0.25
9
Ester content (%)
—
EN 14103
98.3
98.5
—
Minimum of 96.5


## 4. Conclusions

The high FFAs (14.6%) of JCO were reduced to 0.34% by its acid catalyzed pretreatment. Optimization of transesterification process of JCO was achieved by four-factorial CCD using RSM. A second-order model was obtained to predict the JCB yield as a function of process variables. The model can be successfully employed in the biodiesel industry to maximize the yield of methyl esters. On the basis of ANOVA, the catalyst concentration, reaction time, and methanol/oil molar ratio had a significant effect on JCB yield. A biodiesel yield of 98.3% was achieved with methanol/oil molar ratio (11 : 1) using NaOH as catalyst (1% w/w) in 110 min time at 55°C temperature. The prepared JCB conformed to the ASTM and IS standards specifications.



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*Source: 327049-2012-12-05.xml*