Soybean soapstock (SS), a lipid rich by-product of soybean oil production is a promising feedstock for the production ofbiodiesel due to its availability and affordability. In the esterification and transesterification reactions involving soyabeansoapstock, sodium hydroxide, methanol and n-hexane were used as catalyst, solvent and co-solvent respectively. The physico-chemical properties of the biodiesel obtained were determinedusing the Association of Analytical Chemist (AOAC) and American Society of Testing Materials (ASTM) methods. The esterification and transesterification reactions were optimised using both response surface methodology (RSM) under design expert 7.0 platform and Particle swarm technique in ANFIS (ANFIS-PSO) using the MATLAB software. The optimized acid value from the esterification reaction using RSM and ANFIS-PSO were 4.956 and 1.488 while the yield obtained were 97.29% and 99.91%respectively with ANFIS-PSO proving to be the better optimization technique in both cases. Comparison plots made for both reactions shows the ANFIS-PSO curve mirroring the experimental and thus signifying a closer trend when compared to the RSM curve. The suitability of the ANFIS-PSO prediction was further highlighted by the error analysis carried out on both techniques. The Residual sum of squares (RSS), Mean absolute error (MAE), Root mean square error (RMSE), Correlation coefficient (R), Coefficient of determination (R2), Adjusted R2, Absolute average deviation (AAD) and Mean absolute percent error (MAPE) values for the ANFIS-PSO predictions in both reactions were better than the RSM predictions. It can thus be concluded that soybean soapstock is a viable feedstock for biodiesel production and ANFIS-PSO is a more efficient optimization technique when compared with RSM in esterification and transesterification of soybean soapstock.
Published in | Advances (Volume 5, Issue 2) |
DOI | 10.11648/j.advances.20240502.13 |
Page(s) | 49-63 |
Creative Commons |
This is an Open Access article, distributed under the terms of the Creative Commons Attribution 4.0 International License (http://creativecommons.org/licenses/by/4.0/), which permits unrestricted use, distribution and reproduction in any medium or format, provided the original work is properly cited. |
Copyright |
Copyright © The Author(s), 2024. Published by Science Publishing Group |
Biodiesel, Soyabean Soapstock, Response Surface Methodology (RSM), Adaptive Neuro-Fuzzy Inference System (ANFIS), Particle Swarm Optimization (PSO)
Variables/Unit | Symbols | Coded | levels | |||
---|---|---|---|---|---|---|
-2 | -1 | 0 | +1 | +2 | ||
Catalyst concentration (wt%) | A | 5 | 10 | 15 | 20 | 25 |
Methanol/FFA volume ratio | B | 2:1 | 4:1 | 6:1 | 8:1 | 10:1 |
Temperature (°C) | C | 55 | 60 | 65 | 70 | 75 |
Esterification time (min) | D | 60 | 70 | 80 | 90 | 100 |
Independent variables | Symbols | Coded | variables | Levels | ||
---|---|---|---|---|---|---|
-ɑ | -1 | 0 | +1 | +ɑ | ||
Temperature (°C) | X1 | 45 | 50 | 55 | 60 | 65 |
Reaction time (min) | X2 | 45 | 50 | 55 | 60 | 65 |
Catalyst concentration (wt %) | X3 | 0.50 | 1.00 | 1.50 | 2.00 | 2.50 |
Methanol/oil ratio (mol/mol) | X4 | 3:1 | 4:1 | 5:1 | 6:1 | 7:1 |
Stiring speed (rpm) | X5 | 200 | 300 | 400 | 500 | 600 |
Run | Catalyst. Concentration. (wt%) | Methanol/oil ratio (mol/mol) | Temperature | Time (min) | Acid Value | Rsm Prediction |
---|---|---|---|---|---|---|
1 | 1.5 | 2 | 70 | 90 | 5.67 | 5.76 |
2 | 1.5 | 2 | 65 | 80 | 6.03 | 5.25 |
3 | 2 | 1.5 | 65 | 80 | 5.18 | 6.6 |
4 | 1.5 | 1.5 | 65 | 70 | 5.04 | 5.49 |
5 | 1.5 | 2 | 65 | 80 | 6.54 | 5.86 |
6 | 1.5 | 2 | 60 | 90 | 4.99 | 5.98 |
7 | 1.5 | 2 | 60 | 70 | 5.98 | 5.32 |
8 | 2 | 2 | 65 | 70 | 6.06 | 5.97 |
9 | 2 | 2 | 70 | 80 | 5.76 | 6.78 |
10 | 2 | 2 | 60 | 80 | 5.25 | 6.15 |
11 | 1.5 | 2.5 | 65 | 90 | 5.35 | 6.68 |
12 | 1.5 | 2 | 70 | 70 | 6.12 | 5.69 |
13 | 1 | 2 | 65 | 90 | 7.01 | 4.83 |
14 | 1.5 | 1.5 | 70 | 80 | 5.25 | 5.25 |
15 | 2 | 2.5 | 65 | 80 | 5.26 | 5.09 |
16 | 1.5 | 1.5 | 65 | 90 | 5.3 | 5.76 |
17 | 1.5 | 2.5 | 70 | 80 | 5.87 | 6.28 |
18 | 1 | 1.5 | 65 | 80 | 5.8 | 5.3 |
19 | 1.5 | 1.5 | 60 | 80 | 4.96 | 6.5 |
20 | 1.5 | 2 | 65 | 80 | 5.24 | 5.86 |
21 | 1 | 2 | 60 | 80 | 6.32 | 5.09 |
22 | 1.5 | 2 | 65 | 80 | 5.23 | 6.33 |
23 | 2 | 2 | 65 | 90 | 6.22 | 5.51 |
24 | 1.5 | 2.5 | 60 | 80 | 5.33 | 5.36 |
25 | 1 | 2 | 70 | 80 | 6.48 | 5.91 |
26 | 1 | 2.5 | 65 | 80 | 6.48 | 5.91 |
27 | 1.5 | 2.5 | 65 | 70 | 6.48 | 5.91 |
28 | 1 | 2 | 65 | 70 | 6.48 | 5.91 |
29 | 1.5 | 2 | 65 | 80 | 6.48 | 5.91 |
Source | Sum of squares | Df | Mean square | F value | p-value Prob> F | |
---|---|---|---|---|---|---|
Model | 7.05 | 14 | 0.5 | 2.73 | 0.0014 | significant |
A-Catalyst Conc (wt%) | 1.97 | 1 | 1.97 | 10.67 | 0.0056 | |
B-Methanol/oil ratio (mol/mol) | 0.88 | 1 | 0.88 | 4.78 | 0.0463 | |
C-Temp (°C) | 0.45 | 1 | 0.45 | 2.45 | 0.0397 | |
D-Time (min) | 0.22 | 1 | 0.22 | 1.21 | 0.2894 | |
AB | 0.092 | 1 | 0.092 | 0.5 | 0.0011 | |
AC | 0.029 | 1 | 0.029 | 0.16 | 0.6968 | |
AD | 0.033 | 1 | 0.033 | 0.18 | 0.6801 | |
BC | 0.016 | 1 | 0.016 | 0.085 | 0.7755 | |
BD | 0.49 | 1 | 0.49 | 2.64 | 0.0023 | |
CD | 0.072 | 1 | 0.072 | 0.39 | 0.543 | |
A^2 | 0.62 | 1 | 0.62 | 3.36 | 0.008 | |
B^2 | 1.26 | 1 | 1.26 | 6.84 | 0.0204 | |
C^2 | 0.35 | 1 | 0.35 | 1.89 | 0.191 | |
D^2 | 0.077 | 1 | 0.077 | 0.42 | 0.5288 | |
Residual | 2.59 | 14 | 0.18 | |||
Lack of Fit | 0.93 | 10 | 0.093 | 0.22 | 0.9747 | not significant |
Pure Error | 1.66 | 4 | 0.41 | |||
Cor Total | 9.64 | 28 |
Std. Dev. | 5.43 | R-Squared | 0.9316 |
---|---|---|---|
Mean | 5.8 | Adj R-Squared | 0.9131 |
C.V. % | 7.41 | Pred R-Squared | 0.8752 |
PRESS | 117.95 | Adeq Precision | 6.296 |
Run | Time (min) | Temperature (°C) | Catalyst concentration (wt%) | Methanol/oil ratio (mol/mol) | Stirring speed (rpm) | Yield (%) | Rsm Prediction (%) |
---|---|---|---|---|---|---|---|
1 | 50 | 50 | 2 | 5 | 400 | 90.9 | 93.98 |
2 | 50 | 50 | 2 | 7 | 400 | 90.48 | 87.98 |
3 | 50 | 50 | 3 | 5 | 400 | 91.88 | 86.48 |
4 | 50 | 50 | 2 | 5 | 400 | 92.98 | 87.78 |
5 | 65 | 45 | 2.5 | 4 | 500 | 77.88 | 74.88 |
6 | 50 | 45 | 2.5 | 4 | 300 | 93.08 | 97.58 |
7 | 65 | 55 | 2.5 | 6 | 500 | 77.48 | 75.08 |
8 | 50 | 45 | 2.5 | 6 | 500 | 93.18 | 95.38 |
9 | 50 | 45 | 1.5 | 6 | 300 | 79.38 | 77.48 |
10 | 50 | 55 | 2.5 | 6 | 300 | 79.38 | 89.48 |
11 | 50 | 50 | 2 | 5 | 400 | 93.78 | 97.48 |
12 | 50 | 50 | 2 | 5 | 400 | 91.28 | 95.18 |
13 | 65 | 55 | 2.5 | 4 | 300 | 93.98 | 93.08 |
14 | 45 | 50 | 2 | 5 | 400 | 78.88 | 79.38 |
15 | 65 | 55 | 1.5 | 4 | 500 | 95.08 | 97.38 |
16 | 50 | 50 | 2 | 5 | 400 | 95.48 | 93.48 |
17 | 50 | 50 | 2 | 5 | 600 | 95.38 | 97.48 |
18 | 50 | 50 | 2 | 5 | 400 | 95.18 | 97.48 |
19 | 50 | 50 | 1 | 5 | 400 | 79.48 | 85.08 |
20 | 50 | 55 | 1.5 | 4 | 300 | 96.8 | 95.88 |
21 | 65 | 45 | 2.5 | 6 | 300 | 77.98 | 79.9 |
22 | 50 | 55 | 1.5 | 6 | 500 | 78.48 | 81.28 |
23 | 65 | 45 | 1.5 | 6 | 500 | 77.58 | 73.58 |
24 | 50 | 60 | 2 | 5 | 400 | 78.48 | 75.78 |
25 | 50 | 50 | 2 | 5 | 200 | 93.98 | 94.98 |
26 | 50 | 55 | 2.5 | 4 | 500 | 93.58 | 93.98 |
27 | 50 | 45 | 1.5 | 4 | 300 | 79.48 | 83.18 |
28 | 50 | 50 | 2 | 3 | 400 | 93.08 | 95.88 |
29 | 65 | 55 | 1.5 | 6 | 300 | 76.48 | 79.48 |
30 | 50 | 55 | 1.5 | 5 | 400 | 77.78 | 78.88 |
31 | 50 | 45 | 2 | 5 | 400 | 94.98 | 92.98 |
32 | 55 | 45 | 2.5 | 4 | 500 | 78.88 | 86.8 |
Source | Sum of Squares | Df | Mean Square | F Value | p-value Prob> F | |
---|---|---|---|---|---|---|
Model | 1627.63 | 20 | 81.38 | 3.49 | 0.0086 | significant |
A-Rxn Time (min) | 144.16 | 1 | 144.16 | 6.19 | 0.0302 | |
B-Rxn Temp (°C) | 94.17 | 1 | 94.17 | 4.04 | 0.0695 | |
C-Cat Conc.(wt%) | 128.23 | 1 | 128.23 | 5.5 | 0.0088 | |
D-Methanol/oil mol ratio (mol/mol) | 381.23 | 1 | 381.23 | 16.36 | 0.0019 | |
E-Stirring speed (rpm) | 0.014 | 1 | 0.014 | 6.19E-04 | 0.9806 | |
AB | 8.95 | 1 | 8.95 | 0.38 | 0.548 | |
AC | 58.55 | 1 | 58.55 | 2.51 | 0.0012 | |
AD | 29.9 | 1 | 29.9 | 1.28 | 0.0013 | |
AE | 0.69 | 1 | 0.69 | 0.029 | 0.8668 | |
BC | 16.62 | 1 | 16.62 | 0.71 | 0.4163 | |
BD | 241.37 | 1 | 241.37 | 10.36 | 0.0082 | |
BE | 10.16 | 1 | 10.16 | 0.44 | 0.0025 | |
CD | 6.27 | 1 | 6.27 | 0.27 | 0.6143 | |
CE | 0.48 | 1 | 0.48 | 0.021 | 0.8881 | |
DE | 79.74 | 1 | 79.74 | 3.42 | 0.0913 | |
A^2 | 146.35 | 1 | 146.35 | 6.28 | 0.0022 | |
B^2 | 243.35 | 1 | 243.35 | 10.45 | 0.008 | |
C^2 | 142.4 | 1 | 142.4 | 6.11 | 0.0015 | |
D^2 | 9.18 | 1 | 9.18 | 0.39 | 0.5431 | |
E^2 | 0.53 | 1 | 0.53 | 0.023 | 0.8823 | |
Residual | 256.28 | 11 | 23.3 | |||
Lack of Fit | 237.83 | 6 | 39.64 | 8.74 | 3.099 | Not- significant |
Pure Error | 18.45 | 5 | 3.69 | |||
Cor Total | 1883.91 | 31 |
Std. Dev. | 4.83 | R-Squared | 0.964 |
---|---|---|---|
Mean | 86.96 | AdjR-Squared | 0.9466 |
C.V. % | 5.55 | Pred R-Squared | 0.9004 |
PRESS | 420.9 | Adeq Precision | 5.474 |
Runs | Catalyst concentration (wt%) | Methanol/oil ratio (mol/mol) | Temperature (°C) | Time (min) | Acid Value | ANFIS prediction |
---|---|---|---|---|---|---|
1 | 1.5 | 2 | 70 | 90 | 5.67 | 5.67 |
2 | 1.5 | 2 | 65 | 80 | 6.03 | 5.904 |
3 | 2 | 1.5 | 65 | 80 | 5.18 | 5.18 |
4 | 1.5 | 1.5 | 65 | 70 | 5.04 | 5.04 |
5 | 1.5 | 2 | 65 | 80 | 6.54 | 5.904 |
6 | 1.5 | 2 | 60 | 90 | 4.99 | 4.99 |
7 | 1.5 | 2 | 60 | 70 | 5.98 | 5.98 |
8 | 2 | 2 | 65 | 70 | 6.06 | 6.06 |
9 | 2 | 2 | 70 | 80 | 5.76 | 5.76 |
10 | 2 | 2 | 60 | 80 | 5.25 | 5.25 |
11 | 1.5 | 2.5 | 65 | 90 | 5.35 | 5.35 |
12 | 1.5 | 2 | 70 | 70 | 6.12 | 6.12 |
13 | 1 | 2 | 65 | 90 | 7.01 | 7.01 |
14 | 1.5 | 1.5 | 70 | 80 | 5.25 | 5.25 |
15 | 2 | 2.5 | 65 | 80 | 5.26 | 5.26 |
16 | 1.5 | 1.5 | 65 | 90 | 5.3 | 5.3 |
17 | 1.5 | 2.5 | 70 | 80 | 5.87 | 5.87 |
18 | 1 | 1.5 | 65 | 80 | 5.8 | 5.8 |
19 | 1.5 | 1.5 | 60 | 80 | 4.96 | 4.96 |
20 | 1.5 | 2 | 65 | 80 | 5.24 | 5.904 |
21 | 1 | 2 | 60 | 80 | 6.32 | 6.32 |
22 | 1.5 | 2 | 65 | 80 | 5.23 | 5.904 |
23 | 2 | 2 | 65 | 90 | 6.22 | 6.22 |
24 | 1.5 | 2.5 | 60 | 80 | 5.33 | 5.33 |
25 | 1 | 2 | 70 | 80 | 6.48 | 6.48 |
26 | 1 | 2.5 | 65 | 80 | 6.48 | 6.48 |
27 | 1.5 | 2.5 | 65 | 70 | 6.48 | 6.48 |
28 | 1 | 2 | 65 | 70 | 6.48 | 6.48 |
29 | 1.5 | 2 | 65 | 80 | 6.48 | 5.904 |
Run | Reaction Time (min) | Temperature (°C) | Catalyst Concentration (wt%) | Methanol/Oil ratio (mol/mol) | Stirring speed (rpm) | Yield | ANFIS prediction |
---|---|---|---|---|---|---|---|
1 | 50 | 50 | 2 | 5 | 400 | 90.9 | 93.27 |
2 | 50 | 50 | 2 | 7 | 400 | 90.48 | 90.48 |
3 | 50 | 50 | 3 | 5 | 400 | 91.88 | 91.88 |
4 | 50 | 50 | 2 | 5 | 400 | 92.98 | 93.27 |
5 | 65 | 45 | 2.5 | 4 | 500 | 77.88 | 77.88 |
6 | 50 | 45 | 2.5 | 4 | 300 | 93.08 | 93.08 |
7 | 65 | 55 | 2.5 | 6 | 500 | 77.48 | 77.48 |
8 | 50 | 45 | 2.5 | 6 | 500 | 93.18 | 93.18 |
9 | 50 | 45 | 1.5 | 6 | 300 | 79.38 | 79.38 |
10 | 50 | 55 | 2.5 | 6 | 300 | 79.38 | 79.38 |
11 | 50 | 50 | 2 | 5 | 400 | 93.78 | 93.27 |
12 | 50 | 50 | 2 | 5 | 400 | 91.28 | 93.27 |
13 | 65 | 55 | 2.5 | 4 | 300 | 93.98 | 93.98 |
14 | 45 | 50 | 2 | 5 | 400 | 78.88 | 78.88 |
15 | 65 | 55 | 1.5 | 4 | 500 | 95.08 | 95.08 |
16 | 50 | 50 | 2 | 5 | 400 | 95.48 | 93.27 |
17 | 50 | 50 | 2 | 5 | 600 | 95.38 | 95.38 |
18 | 50 | 50 | 2 | 5 | 400 | 95.18 | 93.27 |
19 | 50 | 50 | 1 | 5 | 400 | 79.48 | 79.48 |
20 | 50 | 55 | 1.5 | 4 | 300 | 96.8 | 96.8 |
21 | 65 | 45 | 2.5 | 6 | 300 | 77.98 | 77.98 |
22 | 50 | 55 | 1.5 | 6 | 500 | 78.48 | 78.48 |
23 | 65 | 45 | 1.5 | 6 | 500 | 77.58 | 77.58 |
24 | 50 | 60 | 2 | 5 | 400 | 78.48 | 78.48 |
25 | 50 | 50 | 2 | 5 | 200 | 93.98 | 93.98 |
26 | 50 | 55 | 2.5 | 4 | 500 | 93.58 | 93.58 |
27 | 50 | 45 | 1.5 | 4 | 300 | 79.48 | 79.48 |
28 | 50 | 50 | 2 | 3 | 400 | 93.08 | 93.08 |
29 | 65 | 55 | 1.5 | 6 | 300 | 76.48 | 76.48 |
30 | 50 | 55 | 1.5 | 5 | 400 | 77.78 | 77.78 |
31 | 50 | 45 | 2 | 5 | 400 | 94.98 | 94.98 |
32 | 55 | 45 | 2.5 | 4 | 500 | 78.88 | 78.88 |
Parameter | RSM | ANFIS |
---|---|---|
Temperature | 61.63 | 60 |
Time | 74.01 | 73 |
Catalyst concentration | 1.77 | 1.5 |
Methanol/oil ratio | 1.52 | 1.5 |
Acid value | 4.956 | 1.488 |
Parameter | RSM | ANFIS |
---|---|---|
Temperature | 50.68 | 54 |
Time | 53.36 | 42 |
Catalyst concentration | 1.77 | 1.5 |
Methanol/Oil ratio | 4.36 | 4 |
Speed | 407.6 | 300 |
Yield | 97.29 | 99.91 |
Erroranalysismethod | Esterification of soya soapstock | Transesterification of soya soapstock | ||
---|---|---|---|---|
ANFIS | RSM | ANFIS | RSM | |
RSS | 1.647 | 21.545 | 18.453 | 433 |
MAE | 0.092 | 0.711 | 0.29 | 3.057 |
RSME | 0.238 | 0.862 | 0.759 | 3.678 |
R | 0.909 | 0.298 | 0.995 | 0.899 |
R2 | 0.828 | 0.089 | 0.99 | 0.81 |
ADJ R2 | 0.821 | 0.044 | 0.989 | 0.804 |
AAD | 6.13E-17 | 0.0027 | 0.00045 | -1 |
MAPE | 1.595 | 12.355 | 0.312 | 3.596 |
RSM | Response Surface Methodology |
ANFIS | Adaptive Neuro-Fuzzy Inference System |
RSS | Residual Sum of Squares |
MAE | Mean Absolute Error |
RMSE | Root Mean Square Error |
R | Coerrelation Coefficient |
R2 | Coefficient of Determination |
AAD | Absolute Average Deviation |
MAPE | Mean Absolute Percent Error |
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APA Style
Mbah, C. G., Nwafulugo, F. U., Ezetoha, N. O. (2024). Comparism of Response Surface Methodology (RSM) and Adaptive Neuro-Fuzzy Inference Systems (ANFIS) in Optimisation of Soybean Soapstock Biodiesel Production. Advances, 5(2), 49-63. https://doi.org/10.11648/j.advances.20240502.13
ACS Style
Mbah, C. G.; Nwafulugo, F. U.; Ezetoha, N. O. Comparism of Response Surface Methodology (RSM) and Adaptive Neuro-Fuzzy Inference Systems (ANFIS) in Optimisation of Soybean Soapstock Biodiesel Production. Advances. 2024, 5(2), 49-63. doi: 10.11648/j.advances.20240502.13
AMA Style
Mbah CG, Nwafulugo FU, Ezetoha NO. Comparism of Response Surface Methodology (RSM) and Adaptive Neuro-Fuzzy Inference Systems (ANFIS) in Optimisation of Soybean Soapstock Biodiesel Production. Advances. 2024;5(2):49-63. doi: 10.11648/j.advances.20240502.13
@article{10.11648/j.advances.20240502.13, author = {Chinedu Gabriel Mbah and Francisca Unoma Nwafulugo and Njideka Ophelia Ezetoha}, title = {Comparism of Response Surface Methodology (RSM) and Adaptive Neuro-Fuzzy Inference Systems (ANFIS) in Optimisation of Soybean Soapstock Biodiesel Production }, journal = {Advances}, volume = {5}, number = {2}, pages = {49-63}, doi = {10.11648/j.advances.20240502.13}, url = {https://doi.org/10.11648/j.advances.20240502.13}, eprint = {https://article.sciencepublishinggroup.com/pdf/10.11648.j.advances.20240502.13}, abstract = {Soybean soapstock (SS), a lipid rich by-product of soybean oil production is a promising feedstock for the production ofbiodiesel due to its availability and affordability. In the esterification and transesterification reactions involving soyabeansoapstock, sodium hydroxide, methanol and n-hexane were used as catalyst, solvent and co-solvent respectively. The physico-chemical properties of the biodiesel obtained were determinedusing the Association of Analytical Chemist (AOAC) and American Society of Testing Materials (ASTM) methods. The esterification and transesterification reactions were optimised using both response surface methodology (RSM) under design expert 7.0 platform and Particle swarm technique in ANFIS (ANFIS-PSO) using the MATLAB software. The optimized acid value from the esterification reaction using RSM and ANFIS-PSO were 4.956 and 1.488 while the yield obtained were 97.29% and 99.91%respectively with ANFIS-PSO proving to be the better optimization technique in both cases. Comparison plots made for both reactions shows the ANFIS-PSO curve mirroring the experimental and thus signifying a closer trend when compared to the RSM curve. The suitability of the ANFIS-PSO prediction was further highlighted by the error analysis carried out on both techniques. The Residual sum of squares (RSS), Mean absolute error (MAE), Root mean square error (RMSE), Correlation coefficient (R), Coefficient of determination (R2), Adjusted R2, Absolute average deviation (AAD) and Mean absolute percent error (MAPE) values for the ANFIS-PSO predictions in both reactions were better than the RSM predictions. It can thus be concluded that soybean soapstock is a viable feedstock for biodiesel production and ANFIS-PSO is a more efficient optimization technique when compared with RSM in esterification and transesterification of soybean soapstock. }, year = {2024} }
TY - JOUR T1 - Comparism of Response Surface Methodology (RSM) and Adaptive Neuro-Fuzzy Inference Systems (ANFIS) in Optimisation of Soybean Soapstock Biodiesel Production AU - Chinedu Gabriel Mbah AU - Francisca Unoma Nwafulugo AU - Njideka Ophelia Ezetoha Y1 - 2024/07/08 PY - 2024 N1 - https://doi.org/10.11648/j.advances.20240502.13 DO - 10.11648/j.advances.20240502.13 T2 - Advances JF - Advances JO - Advances SP - 49 EP - 63 PB - Science Publishing Group SN - 2994-7200 UR - https://doi.org/10.11648/j.advances.20240502.13 AB - Soybean soapstock (SS), a lipid rich by-product of soybean oil production is a promising feedstock for the production ofbiodiesel due to its availability and affordability. In the esterification and transesterification reactions involving soyabeansoapstock, sodium hydroxide, methanol and n-hexane were used as catalyst, solvent and co-solvent respectively. The physico-chemical properties of the biodiesel obtained were determinedusing the Association of Analytical Chemist (AOAC) and American Society of Testing Materials (ASTM) methods. The esterification and transesterification reactions were optimised using both response surface methodology (RSM) under design expert 7.0 platform and Particle swarm technique in ANFIS (ANFIS-PSO) using the MATLAB software. The optimized acid value from the esterification reaction using RSM and ANFIS-PSO were 4.956 and 1.488 while the yield obtained were 97.29% and 99.91%respectively with ANFIS-PSO proving to be the better optimization technique in both cases. Comparison plots made for both reactions shows the ANFIS-PSO curve mirroring the experimental and thus signifying a closer trend when compared to the RSM curve. The suitability of the ANFIS-PSO prediction was further highlighted by the error analysis carried out on both techniques. The Residual sum of squares (RSS), Mean absolute error (MAE), Root mean square error (RMSE), Correlation coefficient (R), Coefficient of determination (R2), Adjusted R2, Absolute average deviation (AAD) and Mean absolute percent error (MAPE) values for the ANFIS-PSO predictions in both reactions were better than the RSM predictions. It can thus be concluded that soybean soapstock is a viable feedstock for biodiesel production and ANFIS-PSO is a more efficient optimization technique when compared with RSM in esterification and transesterification of soybean soapstock. VL - 5 IS - 2 ER -