Experimental investigation on biodiesel production through simultaneous esterification and transesterification using mixed rare earth catalysts

被引:5
|
作者
Kingkam, Wilasinee [1 ]
Issarapanacheewin, Sudarat [2 ]
Nuchdang, Sasikarn [1 ]
Pakawanit, Phakkhananan [3 ]
Puripunyavanich, Vichai [1 ]
Rattanaphra, Dussadee [1 ]
机构
[1] Thailand Inst Nucl Technol Publ Org, Nucl Technol Res & Dev Ctr, Bangkok 26120, Nakhon Nayok, Thailand
[2] Thailand Inst Nucl Technol Publ Org, Radioact Waste Management Ctr, Bangkok 26120, Nakhon Nayok, Thailand
[3] Synchrotron Light Res Inst Publ Org, 111 Univ Ave, Nakhon Ratchasima 30000, Thailand
关键词
Biodiesel; Esterification and transesterification; Mixed rare earth catalyst; Heterogeneous catalysts; OIL; TEMPERATURE; STABILITY; METHANOL; LA2O3; PH;
D O I
10.1016/j.egyr.2022.10.169
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
In this study, biodiesel production through simultaneous esterification and transesterification of palm oil with 10 wt% of oleic acid using the mixed rare earth catalyst was investigated. The mixed rare earth catalysts were prepared via the co-precipitation method. The effects of the precipitating parameters such as temperature, stirring speed and pH on the physicochemical and morphology of the catalysts were studied. All catalysts were thoroughly characterized using X-ray diffraction (XRD), scanning electron microscopy-energy dispersive spectrometer (SEM-EDS), fourier transform-infrared spectroscopy (STIR), N2 adsorption/desorption, CO2 temperature programmed desorption (CO2-TPD) and NH3 temperature programmed desorption. (NH3-TPD). The results indicated that the mixed rare earth catalyst prepared under the precipitation conditions: at pH 9, a stirring of 400 rpm and temperature of 30 degrees C showed the highest catalytic of 90% FAME content. High surface area of the catalyst, a significant larger amount of Ce and La contents in the catalyst and an appropriate amount of acid and basic sites on the catalyst led to the high catalytic activity. The catalyst could also accelerate the initial reaction rate to achieve the high FAME content of 50% within 30 min. (C) 2022 The Author(s). Published by Elsevier Ltd.
引用
收藏
页码:857 / 870
页数:14
相关论文
共 50 条
  • [31] Performance of Waste Cooking Oil Esterification for Biodiesel Production Using Various Catalysts
    Herman, Indah Thuraya
    Isa, Khairuddin Md
    Ibrahim, Naimah
    Saad, Saiful Azhar
    Abdullah, Tuan Amran Tuan
    Aziz, Mohd Aizudin Abd
    Hairunnaja, Muhammad Auni
    PERTANIKA JOURNAL OF SCIENCE AND TECHNOLOGY, 2024, 32 (02): : 669 - 684
  • [32] Production of Biodiesel Through Esterification Reaction Using Choline Exchanging Polytungstoboronic Acids as Temperature-Responsive Catalysts
    Siqi Yan
    Tong Tong
    Yue Li
    Shifa Ullah Khan
    Jing Zhao
    Shengtian Wang
    Xiaohong Wang
    Catalysis Surveys from Asia, 2017, 21 : 151 - 159
  • [33] Production of Biodiesel Through Esterification Reaction Using Choline Exchanging Polytungstoboronic Acids as Temperature-Responsive Catalysts
    Yan, Siqi
    Tong, Tong
    Li, Yue
    Khan, Shifa Ullah
    Zhao, Jing
    Wang, Shengtian
    Wang, Xiaohong
    CATALYSIS SURVEYS FROM ASIA, 2017, 21 (04) : 151 - 159
  • [34] Applying green chemistry principles in an investigation of alternative transesterification catalysts and wash methods in biodiesel production
    Ackley, Brandon
    Brush, Edward J.
    ABSTRACTS OF PAPERS OF THE AMERICAN CHEMICAL SOCIETY, 2014, 247
  • [35] Biodiesel production via simultaneous esterification and transesterification of chicken fat oil by mesoporous sulfated Ce supported activated carbon
    Shobhana-Gnanaserkhar
    Asikin-Mijan, N.
    AbdulKareem-Alsultan, G.
    Sivasangar-Seenivasagam
    Izham, Saiman Mohd
    Taufiq-Yap, Y. H.
    BIOMASS & BIOENERGY, 2020, 141
  • [36] Experimental investigation of biodiesel production from Madhuca longifolia seed through in situ transesterification and its kinetics and thermodynamic studies
    Yuvarani Mani
    Thiruselvi Devaraj
    Kubendran Devaraj
    Salma Aathika AbdurRawoof
    Sivanesan Subramanian
    Environmental Science and Pollution Research, 2020, 27 : 36450 - 36462
  • [37] Evaluation of Life Cycle Assessment of Jatropha Biodiesel Processed by Esterification of Thai Domestic Rare Earth Oxide Catalysts
    Rattanaphra, Dussadee
    Tawkaew, Sittinun
    Chuichulcherm, Sinsupha
    Kingkam, Wilasinee
    Nuchdang, Sasikarn
    Kitpakornsanti, Kittiwan
    Suwanmanee, Unchalee
    SUSTAINABILITY, 2024, 16 (01)
  • [38] Optimization of Biodiesel Production Process from Waste Cooking Oil Using Homogeneous and Heterogeneous Catalysts Through Transesterification Process
    Shende, Kiran
    Sonage, Sachin
    Dange, Pratik
    Tandale, Madhukar
    TECHNO-SOCIETAL 2018: PROCEEDINGS OF THE 2ND INTERNATIONAL CONFERENCE ON ADVANCED TECHNOLOGIES FOR SOCIETAL APPLICATIONS - VOL 1, 2020, : 531 - 542
  • [39] Optimization of acid catalyzed esterification and mixed metal oxide catalyzed transesterification for biodiesel production from Moringa oleifera oil
    Niju, S.
    Raj, Fernando Russell
    Anushya, C.
    Balajii, M.
    GREEN PROCESSING AND SYNTHESIS, 2019, 8 (01) : 756 - 775
  • [40] Optimization of experimental conditions for composite biodiesel production from transesterification of mixed oils of Jatropha and Pongamia
    Yogish, H.
    Chandrashekara, K.
    Kumar, M. R. Pramod
    HEAT AND MASS TRANSFER, 2012, 48 (11) : 1955 - 1960