4.7 Article

Valorization of palm oil soap stock waste toward for biodiesel production: Process optimization under zero waste concept

Journal

BIOMASS & BIOENERGY
Volume 154, Issue -, Pages -

Publisher

PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.biombioe.2021.106231

Keywords

Palm oil soap stock; Acidification; Esterification; Biodiesel; Immobilized ALG-PVA lipase

Funding

  1. Royal Golden Jubilee (RGJ) PhD Programme, Bangkok, Thailand [PHD/0018/2557]
  2. Research Centre for Environmental and Hazardous Substance Management (EHSM), Faculty of Engineering, Khon Kaen University, Khon Kaen, Thailand
  3. Center of Excellence on Hazardous Substance Managememt (HSM), Bangkok, Patumwan, Thailand
  4. Newton Fund Institutional Links 2019/2020, British Council, London, UK

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The study recycled palm oil soap stock waste into bio-fuel, producing biodiesel through acidification and esterification reactions, achieving a zero waste production process.
Palm oil soap stock (POSS) was recycled from bio-waste to bio-fuel. Firstly, POSS was converted through acidification to be acidified POSS (APOSS) coupled with solvent extraction. APOSS with a high content of free fatty acids (FFAs) (90.94%) was obtained. Subsequently, the FFAs in APOSS were converted to biodiesel via esterification, catalyzed by immobilized alginate-polyvinyl alcohol (ALG-PVA) lipase. The key factors affecting the reaction, such as the temperature (30-50 degrees C), methanol to FFA molar ratio (2:1 to 4:1), and agitation rate (150-250 rpm) were optimized by statistical response surface methodology (RSM). The highest biodiesel yield was achieved with a reaction temperature of 40 degrees C, methanol/FFA molar ratio of 3:1, and 200 rpm agitation rate, as the optimal conditions. Furthermore, the biocatalyst can be reused up to 16 cycles. Interestingly, the alter-native biodiesel production process reported herein promotes zero waste from the palm oil refinery process.

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