Hong, S.T., Kim, J.-W., Jang, W.-H., Lim, J.S., Park, H.S., Yoo, K.-P., Apfel, C. and Arlt, W. (2009) Transesterification of Palm Oil Using Supercritical Methanol with Co-Solvent HCFC-141b. Research on Chemical Intermediates, 35, 197-207.
http://dx.doi.org/10.1007/s11164-008-0018-0

has been cited by the following article:

• TITLE: Extending Functionality of Microalgae and Transesterification under Supercritical Fluid Conditions

  AUTHORS: Chamil A. Biktach, Rustem A. Usmanov, Farid M. Gumerov, Zufar I. Zaripov, Farizan R. Gabitov, Vener F. Khayrutdinov, Ilmutdin M. Abdulagatov

  KEYWORDS: Supercritical Methanol, Transesterification, Biodiesel, Microalgae, Supercritical Fluid, Supercritical Carbon Dioxide

  JOURNAL NAME: American Journal of Analytical Chemistry, Vol.5 No.16, November 25, 2014

  ABSTRACT: The experimental data on supercritical CO2 extraction of microalgae are presented. It is confirmed that microalgae contains omega-3 fatty acid components. Phase equilibria data are presented for the triolein-methanol (T = 413 K, P = 5.8 - 11.9 MPa) and ethyl eicosapentaenoate-carbon dioxide (T = 313 - 333 K, P = 10 - 21 MPa) binary systems. The scheme of the batch-type experimental setup for supercritical transesterification of oils is presented. Temperature and molar ratio dependences of non-refined palm oil yield to fatty acid methyl esters (FAME) are presented for T = 563 - 693 K, methanol to palm oil molar ratio 39:1. Experiments on ultrasonic emulsification of rapeseed oil-ethanol mixture (molar ratios 150:1 - 7:1) were conducted. Research data on ultrasonic emulsion stability are presented for the time range of 0 - 40 minutes after ultrasonication completion. Correlation is defined between FAME yield of emulsified reaction mixtures and the emulsion grain size. FAME yields are compared for emulsified and non-emulsified reaction mixtures.