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Frontiers of Chemical Science and Engineering

ISSN 2095-0179

ISSN 2095-0187(Online)

CN 11-5981/TQ

邮发代号 80-969

2019 Impact Factor: 3.552

Frontiers of Chemical Science and Engineering  2012, Vol. 6 Issue (2): 210-215   https://doi.org/10.1007/s11705-012-1282-5
  RESEARCH ARTICLE 本期目录
Optimization of pretreatment of Jatropha oil with high free fatty acids for biodiesel production
Optimization of pretreatment of Jatropha oil with high free fatty acids for biodiesel production
Supriyono SUWITO1,2, Giuliano DRAGONE1(), Hary SULISTYO2, Bardi MURACHMAN2, Suryo PURWONO2, José TEIXEIRA1
1. Institute for Biotechnology and Bioengineering, Centre of Biological Engineering, University of Minho, Braga 4710-057, Portugal; 2. Chemical Engineering Department, Gadjah Mada University, Yogyakarta 55281, Indonesia
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Abstract

A central composite rotatable design and response surface methodology were used in order to investigate the individual and combined effects of the ethanol-to-oil ratio, H2SO4 concentration, temperature and time of reaction on the reduction of free fatty acid (FFA) in jatropha oil. A quadratic polynomial model relating the reaction variables with FFA reduction was developed, presenting a good coefficient of determination (R2= 0.893). For reducing FFA to less than 1%, the optimal combination was found to be 0.62 v·v-1 ethanol-to-oil ratio (14.9 v·v-1 ethanol-to-FFA ratio), 1.7% v·v-1 H2SO4 concentration, and 79 min reaction time at a reaction temperature of 54°C. These results are of great relevance to maximize methyl esters formation by transesterification using an alkaline catalyst.

Key wordsbiodiesel    biofuel    esterification    free fatty acids    jatropha curcas oil
收稿日期: 2011-11-20      出版日期: 2012-06-05
Corresponding Author(s): DRAGONE Giuliano,Email:gdragone@deb.uminho.pt   
 引用本文:   
. Optimization of pretreatment of Jatropha oil with high free fatty acids for biodiesel production[J]. Frontiers of Chemical Science and Engineering, 2012, 6(2): 210-215.
Supriyono SUWITO, Giuliano DRAGONE, Hary SULISTYO, Bardi MURACHMAN, Suryo PURWONO, José TEIXEIRA. Optimization of pretreatment of Jatropha oil with high free fatty acids for biodiesel production. Front Chem Sci Eng, 2012, 6(2): 210-215.
 链接本文:  
https://academic.hep.com.cn/fcse/CN/10.1007/s11705-012-1282-5
https://academic.hep.com.cn/fcse/CN/Y2012/V6/I2/210
Fatty Acid /%CaprylicCapricLauricMyristicPalmitoleicPalmiticMargaricOleicStearicLinoleicLinolenicEicosenoicEicosanoicEicosenoicEicosapentaenoicBehenicDocosatrienoicDecahexanoicTeracosanoicKinematic viscosity /(40°C, mm2/s)Water content /(vol-%)Specific gravity at 60/60°CFlash point PMcc /°FConradson carbon residue /(wt-%)Saponification value /(mg·g–1)Peroxide value0.040.060.020.090.8214.090.2375.827.930.090.040.150.330.090.080.030.010.04<0.00142.7650.20.91843741.0521820.61
Tab.1  
Independent variableSymbolLevels and range
-101
Ethanol-to-oil ratio /(v·v–1)EtO0.30.50.7
H2SO4 concentration /(vol-%)Ac123
Time /minTi507090
Temperature /°CTe455565
Tab.2  
RunH2SO4 /(vol- %)Ethanol: Oil /(v·v-1)Time /minTemperature /°CFFA reduction
ExperimentalPredicted
1710.570553.803.14
110.350452.562.29
210.350653.092.67
310.390452.932.58
410.390652.982.16
510.750453.353.13
610.750653.593.45
710.790453.553.05
810.790653.372.57
1920.370553.032.71
2120.550553.663.26
2320.570453.543.08
29 (C)20.570553.623.17
25 (C)20.570553.603.17
26 (C)20.570553.643.17
28 (C)20.570553.663.17
27 (C)20.570553.643.17
2420.570653.312.87
2220.590553.583.08
2020.770553.853.23
930.350452.602.49
1030.350652.892.55
1130.390453.693.01
1230.390652.932.27
1830.570553.433.18
1330.750453.383.11
1430.750653.423.11
1530.790453.483.27
1630.790653.252.47
Tab.3  
Variables and interactions a)Estimated effectsStandard errorst-valuep-value
Ac (L)-0.0190.075-0.2480.808
Ac (Q)-0.0240.192-0.1240.903
EtO (L)0.5040.0766.6760.000
EtO (Q)-0.3980.198-2.0050.065
Ti (L)0.1360.0761.8060.092
Ti (Q)-0.0420.198-0.2100.836
Te (L)-0.0270.076-0.3560.727
Te (Q)-0.4210.198-2.1210.052
Ac EtO-0.1090.080-1.3570.196
Ac Ti0.1020.0801.2700.225
Ac Te-0.1610.080-2.0050.065
EtO Ti-0.1860.080-2.3270.035
EtO Te-0.0290.080-0.3590.725
Ti Te-0.2790.080-3.4820.004
Tab.4  
Fig.1  
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