Enrichment of β-carotene in palm oil through deacidification using supercritical carbon dioxide

Supercritical carbon dioxide (SCCO 2 ) is a suitable medium for separating phytochemical compounds from various materials. Here, it was employed for crude palm oil (CPO) deacidification to concentrate the β -carotene component. In the semibatch process, SCCO 2 was introduced to CPO feed material at various operating temperatures (40−60 °C) and pressures (15−25 MPa) with a CO 2 flow rate of 3 mL min −1 for 120 min. The results indicate that the extraction yield was significantly affected by varying the operating temperature and/or pressure, and the highest extraction yield was 4.59 % (40 °C, 25 MPa). Under the same operating conditions, the addition of an ethanol entrainer improved the extraction yield to 9.31 %. However, due to the β -carotene enrichment in the raffinate product, the presence of an ethanol solvent in this process introduced challenges.

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Publication Details

Journal
Case Studies in Chemical and Environmental Engineering
Published
2025-03-18
DOI
https://doi.org/10.1016/j.cscee.2025.101191
Citations
1
Primary Topic
Food Chemistry and Fat Analysis
Type
article
Field-Weighted Citation Impact
1.16

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article

Enrichment of β-carotene in palm oil through deacidification using supercritical carbon dioxide

Tadafumi Adschiri, Siti Machmudah, Wahyu Diono, Masaru Watanabe et al.
1 citations
Case Studies in Chemical and Environmental Engineering
Food Chemistry and Fat Analysis
1.16
article

Enrichment of β-carotene in palm oil through deacidification using supercritical carbon dioxide

Tadafumi Adschiri, Siti Machmudah, Wahyu Diono, Masaru Watanabe, Motonobu Goto, D Annisa, Pramudya Riandana Bhayu Gautama, Rais Rahmat Rafsanjani
article en
1 citations

Abstract

Supercritical carbon dioxide (SCCO 2 ) is a suitable medium for separating phytochemical compounds from various materials. Here, it was employed for crude palm oil (CPO) deacidification to concentrate the β -carotene component. In the semibatch process, SCCO 2 was introduced to CPO feed material at various operating temperatures (40−60 °C) and pressures (15−25 MPa) with a CO 2 flow rate of 3 mL min −1 for 120 min. The results indicate that the extraction yield was significantly affected by varying the operating temperature and/or pressure, and the highest extraction yield was 4.59 % (40 °C, 25 MPa). Under the same operating conditions, the addition of an ethanol entrainer improved the extraction yield to 9.31 %. However, due to the β -carotene enrichment in the raffinate product, the presence of an ethanol solvent in this process introduced challenges.

Case Studies in Chemical and Environmental EngineeringVol. 11
Sepuluh Nopember Institute of Technology (ID), Tohoku University (JP), Nagoya University (JP)
Kementerian Pendidikan, Kebudayaan, Riset, dan Teknologi
Zero hunger
Openalex Percentile: Top 24%
Food Chemistry and Fat Analysis
1.16
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