SCI和EI收录∣中国化工学会会刊

中国化学工程学报 ›› 2019, Vol. 27 ›› Issue (10): 2481-2490.DOI: 10.1016/j.cjche.2019.02.019

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Optimization and kinetic modeling of waste lard methanolysis in a continuous reciprocating plate reactor

Marija R. Miladinovi?1, Ivan J. Stojkovi?2, Ana V. Veli?kovi?1, Olivera S. Stamenkovi?1, Ivana B. Bankovi?-Ili?1, Vlada B. Veljkovi?1,3   

  1. 1 University of Niš, Faculty of Technology, Bulevar oslobođenja 124, Leskovac 16000, Serbia;
    2 University of Belgrade, Faculty of Technology and Metallurgy, Karnegijeva 4, Belgrade 11000, Serbia;
    3 Serbian Academy of Sciences and Arts(SASA), Knez Mihailova 35, Belgrade 11000, Serbia
  • 收稿日期:2018-06-30 修回日期:2019-01-28 出版日期:2019-10-28 发布日期:2020-01-17
  • 通讯作者: Vlada B. Veljković
  • 基金资助:
    Supported by the Ministry of Education, Science and Technological Development of the Republic of Serbia (Project III 45001), and the Project 0-14-18 of the SASA Branch in Niš, Serbia.

Optimization and kinetic modeling of waste lard methanolysis in a continuous reciprocating plate reactor

Marija R. Miladinovi?1, Ivan J. Stojkovi?2, Ana V. Veli?kovi?1, Olivera S. Stamenkovi?1, Ivana B. Bankovi?-Ili?1, Vlada B. Veljkovi?1,3   

  1. 1 University of Niš, Faculty of Technology, Bulevar oslobođenja 124, Leskovac 16000, Serbia;
    2 University of Belgrade, Faculty of Technology and Metallurgy, Karnegijeva 4, Belgrade 11000, Serbia;
    3 Serbian Academy of Sciences and Arts(SASA), Knez Mihailova 35, Belgrade 11000, Serbia
  • Received:2018-06-30 Revised:2019-01-28 Online:2019-10-28 Published:2020-01-17
  • Contact: Vlada B. Veljković
  • Supported by:
    Supported by the Ministry of Education, Science and Technological Development of the Republic of Serbia (Project III 45001), and the Project 0-14-18 of the SASA Branch in Niš, Serbia.

摘要: Continuous biodiesel production from a waste pig-roasting lard, methanol and KOH was carried out in a reciprocating plate reactor (RPR) using a factorial design containing three process factors, namely methanol/lard molar ratio, catalyst loading, and normalized height of the reactor. The main goals were to optimize the influential process factors with respect to biodiesel purity using the response surface methodology and to model the kinetics of the transesterification reaction in order to describe the change of triacylglycerols (TAG) and fatty acid methyl esters (FAME) concentrations along the RPR height. The first-order rate law was proved for both the reaction and the mass transfer. The model of the changing reaction mechanism and mass transfer of TAG was also applicable. Both kinetic models agreed with the experimental concentrations of TAG and FAME determined along the RPR height.

关键词: Biodiesel, Kinetics, Optimization, Reciprocating plate reactor, Waste lard

Abstract: Continuous biodiesel production from a waste pig-roasting lard, methanol and KOH was carried out in a reciprocating plate reactor (RPR) using a factorial design containing three process factors, namely methanol/lard molar ratio, catalyst loading, and normalized height of the reactor. The main goals were to optimize the influential process factors with respect to biodiesel purity using the response surface methodology and to model the kinetics of the transesterification reaction in order to describe the change of triacylglycerols (TAG) and fatty acid methyl esters (FAME) concentrations along the RPR height. The first-order rate law was proved for both the reaction and the mass transfer. The model of the changing reaction mechanism and mass transfer of TAG was also applicable. Both kinetic models agreed with the experimental concentrations of TAG and FAME determined along the RPR height.

Key words: Biodiesel, Kinetics, Optimization, Reciprocating plate reactor, Waste lard