Influence of Additives (Isoamyl Laurate or Isoamyl Nonanoate) in the Solid-Liquid Equilibrium of Fatty Acid Ethyl Esters

被引:4
|
作者
Branco Almeida Bessa, Larissa Castello [1 ]
Robustillo, Maria Dolores [1 ]
da Silva, Erica Gonna [1 ,2 ]
Tadini, Carmen Cecilia [1 ,2 ]
de Almeida Meirelles, Antonio Jose [3 ]
Pessoa Filho, Pedro de Alcantara [1 ,2 ]
机构
[1] Univ Sao Paulo, Engn Sch, Dept Chem Engn, BR-05424970 Sao Paulo, SP, Brazil
[2] Univ Sao Paulo, NAPAN Food Res Ctr, FoRC, BR-05508080 Sao Paulo, SP, Brazil
[3] Univ Campinas UNICAMP, Sch Food Engn FEA, Dept Food Engn DEA, BR-13083862 Campinas, SP, Brazil
来源
基金
巴西圣保罗研究基金会;
关键词
TERNARY MIXTURES; BINARY-MIXTURES; LOW-TEMPERATURE; PHASE-DIAGRAMS; CLOUD POINT; REPRESENTATIVE COMPOUNDS; METHYL-ESTERS; BIODIESEL; PALMITATE; SYSTEMS;
D O I
10.1021/acs.jced.8b01019
中图分类号
O414.1 [热力学];
学科分类号
摘要
Solid liquid equilibrium data of binary mixtures of fatty acid ethyl esters present in biodiesel, namely, ethyl laurate, ethyl palmitate, ethyl myristate, ethyl stearate, and ethyl oleate, and fatty esters of branched-chain alcohols used as additives (isoamyl laurate and isoamyl nonanoate) were obtained through differential scanning calorimetry. Most of these systems presented eutectic behavior, except for the system system ethyl laurate + isoamyl laurate, which presented peritectic transition. Equilibrium data were thermodynamically modeled either using two different liquid-phase activity coefficient models or considering that the liquid phase is an ideal mixture. Best correlations were observed for the Flory-Huggins equation, but good agreement between calculated and experimental data was also obtained when using both the ideal and UNIFAC-Dortmund models.
引用
收藏
页码:2062 / 2074
页数:13
相关论文
共 50 条
  • [41] Predicting Solid-Liquid Equilibrium of Fatty Acid Methyl Ester and Monoglyceride Mixtures as Biodiesel Model Fuels
    Yoshidomi, Shinichiro
    Sugami, Yuitsu
    Minami, Eiji
    Shisa, Noriko
    Hayashi, Hitoshi
    Saka, Shiro
    [J]. JOURNAL OF THE AMERICAN OIL CHEMISTS SOCIETY, 2017, 94 (08) : 1087 - 1094
  • [42] SYNTHESIS OF SULFUR-CONTAINING LUBRICANT ADDITIVES ON THE BASIS OF FATTY ACID ETHYL ESTERS
    Bodachivskyi, Iurii S.
    Pop, Grigoriy S.
    Golovchenko, Olexandr V.
    [J]. BULLETIN OF DNIPROPETROVSK UNIVERSITY-SERIES CHEMISTRY, 2016, 24 (02): : 62 - 72
  • [43] Solid-liquid equilibrium of terephthalic acid in aqueous acetic acid at elevated temperature
    Wang, Qin-Bo
    Xu, Hai-Bo
    Li, Xi
    [J]. Huaxue Gongcheng/Chemical Engineering (China), 2006, 34 (03): : 46 - 48
  • [44] THERMODYNAMIC MODELING AND EXPERIMENTAL VALIDATION OF FATTY ORGANIC SYSTEMS SOLID-LIQUID EQUILIBRIUM
    Mailhe, Clement
    Duquesne, Marie
    [J]. 4TH THERMAL AND FLUIDS ENGINEERING CONFERENCE, ASTFE 2019, 2019,
  • [45] Determination and measurement of solid-liquid equilibrium for binary fatty acid mixtures based on NRTL and UNIQUAC activity models
    Mirpoorian, Seyed Mohammadreza
    Vakili, MohammadHassan
    Baghban, Seyed Hossein Noie
    Roohi, Pejman
    [J]. JOURNAL OF THERMAL ANALYSIS AND CALORIMETRY, 2019, 137 (02) : 679 - 688
  • [46] Solid-Liquid Equilibrium for Binary and Ternary Phases of Saturated Fatty Acid-Urea-Alcohol in Urea Complexation
    Setyawardhani, Dwi Ardiana
    Sulistyo, Hary
    Sediawan, Wahyudi Budi
    Fahrurrozi, Mohammad
    Ariyanto, Teguh
    [J]. JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2019, 64 (12): : 5066 - 5078
  • [47] Purification of fatty acid ethyl esters by solid-phase extraction and high-performance liquid chromatography
    Bernhardt, TG
    Cannistraro, PA
    Bird, DA
    Doyle, KM
    Laposata, M
    [J]. JOURNAL OF CHROMATOGRAPHY B-BIOMEDICAL APPLICATIONS, 1996, 675 (02): : 189 - 196
  • [48] A UNIQUE CONFORMATIONAL EQUILIBRIUM OF POLYACRYLIC-ACID AT THE SOLID-LIQUID INTERFACE
    KUNJAPPU, JT
    SOMASUNDARAN, P
    SIVADASAN, K
    [J]. COLLOIDS AND SURFACES A-PHYSICOCHEMICAL AND ENGINEERING ASPECTS, 1995, 97 (02) : 101 - 107
  • [49] (Liquid plus liquid) equilibria of (water plus propionic acid plus methyl isoamyl ketone or diisobutyl ketone or ethyl isoarnyl keton) at T=298.2 K
    Ozmen, Dilek
    [J]. FLUID PHASE EQUILIBRIA, 2006, 250 (1-2) : 70 - 75
  • [50] Binodal curve of two liquid phases and solid-liquid equilibrium for water+fatty acid+ethanol systems and water+fatty acid+acetone systems
    Himeji Inst of Technology, Hyogo, Japan
    [J]. Fluid Phase Equilib, 1-2 (281-294):