Heat-assisted extraction of phenolic-rich bioactive antioxidants from Enantia chlorantha stem bark: multi-objective optimization, integrated process techno-economics and profitability risk assessment

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作者
Oladayo Adeyi
Abiola J. Adeyi
Emmanuel O. Oke
Bernard I. Okolo
Olusegun A. Olalere
Abiola E. Taiwo
Oluwole S. Aremu
Tozama Qwebani-Ogunleye
Yvonne Maphosa
Akinola D. Ogunsola
机构
[1] Michael Okpara University of Agriculture,Department of Chemical Engineering
[2] Ladoke Akintola University of Technology,Department of Mechanical Engineering
[3] Forest Research Institute of Nigeria,Analytical Biochemistry Research Centre (ABrC)
[4] Universiti Sains Malaysia (USM),Faculty of Engineering
[5] Mangosuthu University of Technology,Faculty of Applied and Computer Sciences, Institute of Traditional Knowledge and Traditional Medicine
[6] Vaal University of Technology,Department of Food Science and Technology
[7] Southern Guateng Science and Technology Park,undefined
[8] Cape Peninsula University of Technology,undefined
来源
SN Applied Sciences | 2023年 / 5卷
关键词
Heat-assisted extraction; Integrated process; Economic analyses; stem bark; Process risk analysis;
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摘要
This present study investigates the heat-assisted extraction (HAE) of bioactive antioxidants from Enantia chlorantha stem bark (ECSB). The effects of process parameters of operating temperature (OT: 35–55 °C), extraction time (ET: 100–200 min) and solid: liquid ratio (S/L: 1:20–1:50 g/mL) are determined on the total polyphenol content (TPC), antioxidant activity (AA) and extract yield (EY) using the D-Optimal design. Multi-criteria optimization is also conducted to determine the HAE optimum conditions. The integrated process for E. chlorantha stem bark extracts (ECBEs) production is thereafter designed with the optimum HAE conditions and techno-economically analysed. Three industrial ECBEs production setups (5, 100 and 1000 L extractor capacities) are analysed for probable scale-up and the risk & sensitivity analyses are conducted via Monte Carlo simulation. The HAE parameters affect the extraction process significantly. The OT, ET and S/L that maximize the TPC, AA and EY simultaneously are: OT = 54.10 °C, ET = 120.16 min and S/L = 1:50 g/mL. The 1000 L plant extractor setup is the most economical capacity having the least unit production cost (UPC) of 763.52 US$/kg ECBEs. The certainty of achieving 763.52 US$/kg ECBEs for the 1000 L capacity is 55.43% and the only variable with negative contribution (− 37.9%) on ECBEs UPC is the extract recovery variable.
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