Transesterification of sunflower oil in a sub- and supercritical dimethyl carbonate medium

被引:0
作者
Tiguntceva, Nadezhda P. [1 ,2 ]
Fomina, Elena S. [1 ,2 ]
Evstaf'ev, Sergej N. [3 ]
机构
[1] Irkutsk Natl Res Tech Univ, Chem, 83 Lermontov St, Irkutsk 664074, Russia
[2] Irkutsk Natl Res Tech Univ, 83 Lermontov St, Irkutsk 664074, Russia
[3] Irkutsk Natl Res Tech Univ, Chem & Food Technol Dept, 83 Lermontov St, Irkutsk 664074, Russia
来源
IZVESTIYA VUZOV-PRIKLADNAYA KHIMIYA I BIOTEKHNOLOGIYA | 2019年 / 9卷 / 04期
关键词
dimethyl carbonate; sub- and supercritical conditions; transesterification; sunflower oil; methyl esters of carboxylic acids; biodiesel; FREE FATTY-ACIDS; BIODIESEL PRODUCTION; RAPESEED OIL; SOYBEAN OIL; METHANOL; PRODUCT;
D O I
10.21285/2227-2925-2019-9-4-773-778
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
At present, the development of environmentally friendly methods for producing biodiesel and the development of new renewable energy sources appears to be an urgent task. The present article reports on a study aimed at assessing the effect of the duration and temperature of sunflower oil processing in sub- and supercritical dimethyl carbonate media on the yield and composition of methyl esters of carboxylic acids. The experiment was carried out using a batch type autoclave in the temperature range of 150-325 degrees C and an oil: dimethyl carbonate molar ratio equal to 1 : 9. The chemical composition of transesterification products was studied using the GC-MS method. Under subcritical conditions in the range of 150-225 degrees C, no transesterification of oils practically is detected. An increase in the yield of methyl esters is observed at temperatures above 225 degrees C with a maximum value of 90.6 % mass identified in the supercritical region at 280 degrees C. When processed under subcritical conditions for 9 min, the yield of methyl esters does not exceed 80 % of the mass. Along with methyl esters, transesterification products were represented by mono- and diglycerides of fatty acids, methanol, glycerine and the products of glycerine transformations. The content of these products decreased under an increase in temperature. The transesterification product of oil under supercritical conditions is represented by the composition of methyl esters of carboxylic acids. The content of impurities is not more than 1 %. The effect of the treatment duration on the yield of methyl esters is shown to be most pronounced in the subcritical conditions of the process. Under supercritical conditions, more than 80 % of the oil triglycerides are converted to carboxylic acid methyl esters within 3-5 minutes of treatment. Based on the conducted studies, the choice of temperature conditions for the transesterification of oil in dimethyl carbonate medium was substantiated and additional information on the composition of the products was obtained.
引用
收藏
页码:773 / 778
页数:6
相关论文
共 50 条
  • [1] Palm oil transesterification in sub- and supercritical methanol with heterogeneous base catalyst
    Asri, Nyoman Puspa
    Machmudah, Siti
    Wahyudiono
    Suprapto
    Budikarjono, Kusno
    Roesyadi, Achmad
    Goto, Motonobu
    CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2013, 72 : 63 - 67
  • [2] Transesterification of Sunflower Oil in Microreactors
    Bhoi, Rohidas
    Sen, Nirvik
    Singh, K. K.
    Mahajani, Sanjay M.
    Shenoy, K. T.
    Rao, Hanmanth
    Ghosh, S. K.
    INTERNATIONAL JOURNAL OF CHEMICAL REACTOR ENGINEERING, 2014, 12 (01) : 47 - 62
  • [3] Optimization of supercritical dimethyl carbonate method for biodiesel production
    Ilham, Zul
    Saka, Shiro
    FUEL, 2012, 97 : 670 - 677
  • [4] Transesterification of sunflower oil over MoO3 supported on alumina
    Sankaranarayanan, T. M.
    Pandurangan, A.
    Banu, M.
    Sivasanker, S.
    APPLIED CATALYSIS A-GENERAL, 2011, 409 : 239 - 247
  • [5] Enzyme catalyzed transesterification of waste cooking oil with dimethyl carbonate
    Gharat, Nikhil
    Rathod, Virendra K.
    JOURNAL OF MOLECULAR CATALYSIS B-ENZYMATIC, 2013, 88 : 36 - 40
  • [6] Transesterification of camelina sativa oil with supercritical alcohol mixtures
    Sun, Yingqiang
    Ponnusamy, Sundaravadivelnathan
    Muppaneni, Tapaswy
    Reddy, Harvind K.
    Wang, Jun
    Zeng, Zheling
    Deng, Shuguang
    ENERGY CONVERSION AND MANAGEMENT, 2015, 101 : 402 - 409
  • [7] Transesterification of sunflower oil in a countercurrent trickle-bed reactor packed with a CaO catalyst
    Son, Sung Mo
    Kusakabe, Katsuki
    CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2011, 50 (07) : 650 - 654
  • [8] Kinetics of transesterification of palm oil and dimethyl carbonate for biodiesel production at the catalysis of heterogeneous base catalyst
    Zhang, Liping
    Sheng, Boyang
    Xin, Zhong
    Liu, Qun
    Sun, Shuzhen
    BIORESOURCE TECHNOLOGY, 2010, 101 (21) : 8144 - 8150
  • [9] Modified Nanostructure MgO Superbasicity with CaO in Heterogeneous Transesterification of Sunflower Oil
    Qasim, Maimoonah Khalid
    EGYPTIAN JOURNAL OF CHEMISTRY, 2019, 62 (03): : 475 - 485
  • [10] Characterization of KNO3/NaX catalyst for sunflower oil transesterification
    Pena, Rosaura
    Romero, Rubi
    Luz Martinez, Sandra
    Natividad, Reyna
    Ramirez, Armando
    FUEL, 2013, 110 : 63 - 69