Diffusivity optimization of supercritical carbon dioxide extraction with co-solvent-ethanol from peanut skin

Authors

  • Nicky Rahmana Putra Faculty of Chemical and Energy Engineering, Universiti Teknologi Malayia, 81310 Johor Bahru,Malaysia b Centre of Lipid Engineering and Advanced Research (CLEAR), Ibnu Sina Institute for Scientific and Industrial Research, Universiti Teknologi Malaysia, 81310, UTM Johor Bahru, Malaysia
  • Ahmad Hazim Abdul Aziz Faculty of Chemical and Energy Engineering, Universiti Teknologi Malayia, 81310 Johor Bahru,Malaysia Centre of Lipid Engineering and Advanced Research (CLEAR), Ibnu Sina Institute for Scientific and Industrial Research, Universiti Teknologi Malaysia, 81310, UTM Johor Bahru, Malaysia
  • Zuhaili Idham Centre of Lipid Engineering and Advanced Research (CLEAR), Ibnu Sina Institute for Scientific and Industrial Research, Universiti Teknologi Malaysia, 81310, UTM Johor Bahru, Malaysia
  • Muhammad Syafiq Hazwan Ruslan Department of Chemical Engineering, Universiti Teknologi Petronas, 32610 Bandar Seri Iskandar, Perak, Malaysia
  • Mohd Azizi Che Yunus Centre of Lipid Engineering and Advanced Research (CLEAR), Ibnu Sina Institute for Scientific and Industrial Research, Universiti Teknologi Malaysia, 81310, UTM Johor Bahru, Malaysia

DOI:

https://doi.org/10.11113/mjfas.v14n1.726

Keywords:

Peanut skin, CO2 supercritical fluid extraction, yield, diffusivity coefficient

Abstract

Peanut skin is a waste of industrial peanut butter that contains bioactive compound, which is used as antioxidant, anti-diabetic, anti-cancer, and anti-inflammatory. Supercritical carbon dioxide (SC-CO2) extraction as green technology is applied to extract peanut skin oil. The aim of this study is to optimize the operational conditions of pressure, temperature, and percentage of co-solvent to obtain oil yield and diffusivity coefficient. Determination of diffusivity coefficient was needed to evaluate the mass transfer between solvent and solute. The operational conditions of SC-CO2 studied were different pressure (10, 20, 30 MPa), different temperature (40, 55, 70 °C and different co-solvent percentage (2.5, 5, and 7.5 % (Vethanol/Vsolvent)). The extraction time was 3 hours respectively. The optimum condition were 29.95 MPa, 40 °C and 6.49 % (Vethanol/Vsolvent) with 14.95 % yield and 8.47E-12 m2/s diffusivity coefficient. 

Author Biography

Nicky Rahmana Putra, Faculty of Chemical and Energy Engineering, Universiti Teknologi Malayia, 81310 Johor Bahru,Malaysia b Centre of Lipid Engineering and Advanced Research (CLEAR), Ibnu Sina Institute for Scientific and Industrial Research, Universiti Teknologi Malaysia, 81310, UTM Johor Bahru, Malaysia

Master Student Of Chemical Engineering Department Universiti Malaysia

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Published

08-03-2018