In-depth study of the transesterification reaction of Pongamia pinnata oil for biodiesel production using catalyst-free supercritical methanol process

被引:41
|
作者
Ortiz-Martinez, V. M. [1 ]
Salar-Garcia, M. J. [1 ]
Palacios-Nereo, F. J. [2 ]
Olivares-Carrillo, P. [2 ]
Quesada-Medina, J. [2 ]
Rios, A. P. de los [2 ]
Hernandez-Fernandez, F. J. [1 ]
机构
[1] Polytech Univ Cartagena, Chem & Environm Engn Dept, Campus Muralla del Mar,C Doctor Fleming S-N, E-30202 Murcia, Spain
[2] Univ Murcia, Dept Chem Engn, Campus Espinardo, E-30071 Murcia, Spain
来源
关键词
Pongamia pinnata oil; Transesterification reaction; Biodiesel production; Supercritical methanolysis; Thermal decomposition analysis; KARANJA BIODIESEL; VEGETABLE-OILS; METHYL-ESTERS; JATROPHA; PERFORMANCE; EMISSIONS; OPTIMIZATION; ENGINE; FUEL; FEEDSTOCK;
D O I
10.1016/j.supflu.2016.03.009
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Non-edible vegetable oils are promising substitutes for traditional edible food crops used in the synthesis of biodiesel. Among them, Pongamia pinnata oil, also known as Karanja oil, is considered as a good candidate with potential availability of more than 135 Mtpa. The present work offers an in-depth study of the transesterification reaction of Karanja oil in supercritical methanol in one-step catalyst-free process. Triglyceride (TG) conversion and the yield of fatty acid methyl esters (FAMEs) are analyzed in the temperature and reaction time ranges of 250-350 degrees C (12-43 MPa) and 15-90 min, respectively, at an alcohol-to-oil molar ratio of 43:1. This study also covers the evolution of intermediate products such as monoglycerides (MG) and diglycerides (DG) and the thermal decomposition of fatty acid chains for the stated reaction conditions. Optimal reactions conditions were found at 300 degrees C and 90 min reaction with almost complete triglyceride conversion. Significant thermal decomposition was observed from 325 degrees C, mainly caused by the degradation of polyunsaturated fatty acid methyl esters. Maximum degree of thermal decomposition of 38% was determined at 350 degrees C after 90 min reaction time. (C) 2016 Elsevier B.V. All rights reserved.
引用
收藏
页码:23 / 30
页数:8
相关论文
共 50 条
  • [41] Optimization of non-catalytic transesterification of tobacco (Nicotiana tabacum) seed oil using supercritical methanol to biodiesel production
    Garcia-Martinez, Nuria
    Andreo-Martinez, Pedro
    Quesada-Medina, Joaquin
    Perez de los Rios, Antonia
    Chica, Antonio
    Beneito-Ruiz, Ruben
    Carratala-Abril, Juan
    [J]. ENERGY CONVERSION AND MANAGEMENT, 2017, 131 : 99 - 108
  • [42] Production of biodiesel from microalgae oil (Chlorella protothecoides) by non-catalytic transesterification in supercritical methanol and ethanol: Process optimization
    Nan, Yue
    Liu, Jiuxu
    Lin, Ronghong
    Tavlarides, Lawrence L.
    [J]. JOURNAL OF SUPERCRITICAL FLUIDS, 2015, 97 : 174 - 182
  • [43] Pongamia pinnata biodiesel production using cobalt doped ZnO nanoparticles-An analytical study
    Pandya, Hiral Narendrakumar
    Banka, Samidha
    Parikh, Sachin Prakashbhai
    [J]. ENVIRONMENTAL PROGRESS & SUSTAINABLE ENERGY, 2022, 41 (04)
  • [44] A Kinetics Study of the Non-catalytic Supercritical Transesterification Reaction for Biodiesel Production
    Tan, K. T.
    Lee, K. T.
    Mohamed, A. R.
    [J]. ENERGY SOURCES PART A-RECOVERY UTILIZATION AND ENVIRONMENTAL EFFECTS, 2015, 37 (07) : 705 - 713
  • [45] Biodiesel Production via Transesterification of Soybean Oil Using Acid Catalyst in CO2 Expanded Methanol Liquids
    Ma, Zhen
    Shang, Zi-Yang
    Wang, En-Jun
    Xu, Jun-Chen
    Xu, Qin-Qin
    Yin, Jian-Zhong
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2012, 51 (38) : 12199 - 12204
  • [46] Ionic liquids in supercritical methanol greatly enhance transesterification reaction for high-yield biodiesel production
    Ortiz-Martinez, V. M.
    Salar-Garcia, M. J.
    Hernandez-Fernandez, F. J.
    Olivares-Carrillo, P.
    de los Rios, A. P.
    Quesada-Medina, J.
    [J]. AICHE JOURNAL, 2016, 62 (11) : 3842 - 3846
  • [47] Process design, kinetics, simulation, and techno-economic analysis of biodiesel production from Pongamia pinnata seed oil using a magnetically recyclable acidic ionic liquid catalyst
    Sangeetha, Baskaran
    Baskar, Gurunathan
    [J]. ENERGY CONVERSION AND MANAGEMENT, 2024, 301
  • [48] Synthesis of Linseed oil Biodiesel using a Non-Catalytic Supercritical Transesterification Process
    Gupta, Dileep Kumar
    Sharma, Abhishek
    Pathak, Varun
    Kumar, Naveen
    [J]. SAE INTERNATIONAL JOURNAL OF FUELS AND LUBRICANTS, 2014, 7 (01) : 317 - 322
  • [49] New approach of catalyst-free biodiesel production from canola oil in supercritical tert-butyl methyl ether (MTBE)
    Farobie, Obie
    Yanagida, Takashi
    Matsumura, Yukihiko
    [J]. FUEL, 2014, 135 : 172 - 181
  • [50] Production Biodiesel from Coconut Oil Using Microwave: Effect of Some Parameters on Transesterification Reaction by NaOH Catalyst
    Suryanto, A.
    Suprapto, S.
    Mahfud, M.
    [J]. BULLETIN OF CHEMICAL REACTION ENGINEERING AND CATALYSIS, 2015, 10 (02): : 162 - 168