TY - JOUR
T1 - Microencapsulated anthocyanins powder production from Hibiscus sabdariffa L. calyx
T2 - Process synthesis and economic analysis
AU - Adeyi, Oladayo
AU - Oke, Emmanuel Olusola
AU - Adeyi, Abiola John
AU - Okolo, Bernard Iberzim
AU - Olalere, Abayomi Olusegun
AU - Otolorin, John Adebayo
AU - Aremu, Oluwole Samuel
AU - Qwebani-Ogunleye, Tozama
PY - 2022/3/31
Y1 - 2022/3/31
N2 - In this work, we synthesized and economically analyzed a sustainable process of industrial production of microencapsulated anthocyanins powder (MAP) from Hibiscus sabdafiffa L. calyx (HSC) with the assistance of SuperPro Designer software. Open literature data were used in the synthesis of flowsheet and minimum selling price (MSP) of MAP was the only economic parameter used to assess the profitability of MAP production plant. Scale-up studies in the range of 0.127–130.393 × 103 kg/y MAP were conducted to identify the most economically feasible production capacity of MAP. Sensitivity and uncertainty analyses were further conducted on the most economically feasible capacity to determine technical and cost variables of significance. Material and energy demands and cost parameters increased with pant capacity. A power law relationship (R2 = 0.9081) was obtained between the MSP and selected range of plant capacities. The plant capacity of 108.551 × 103 kg/y MAP had the least MSP of 4013 US$/kg MAP and was selected as the most economically feasible capacity. Regarding the economics of plant capacity of 108.551 × 103 kg/y MAP, Packed Bed Adsorption (PBA) chromatography column was required in multiples and its cost contributed approximately 59% to the total equipment purchased cost (EPC). Consumables cost was the highest contributor to total operating cost (TOpC) and MSP showed a linear dependence (R2 = 0.9935) on the discount rate. Sensitivity and uncertainty analyses showed that resin binding capacity, PBA resins purchase cost and Hibiscus sabdafiffa L. calyx anthocyanins (HSCAs) recovery had most contributions to uncertainties in MSP.
AB - In this work, we synthesized and economically analyzed a sustainable process of industrial production of microencapsulated anthocyanins powder (MAP) from Hibiscus sabdafiffa L. calyx (HSC) with the assistance of SuperPro Designer software. Open literature data were used in the synthesis of flowsheet and minimum selling price (MSP) of MAP was the only economic parameter used to assess the profitability of MAP production plant. Scale-up studies in the range of 0.127–130.393 × 103 kg/y MAP were conducted to identify the most economically feasible production capacity of MAP. Sensitivity and uncertainty analyses were further conducted on the most economically feasible capacity to determine technical and cost variables of significance. Material and energy demands and cost parameters increased with pant capacity. A power law relationship (R2 = 0.9081) was obtained between the MSP and selected range of plant capacities. The plant capacity of 108.551 × 103 kg/y MAP had the least MSP of 4013 US$/kg MAP and was selected as the most economically feasible capacity. Regarding the economics of plant capacity of 108.551 × 103 kg/y MAP, Packed Bed Adsorption (PBA) chromatography column was required in multiples and its cost contributed approximately 59% to the total equipment purchased cost (EPC). Consumables cost was the highest contributor to total operating cost (TOpC) and MSP showed a linear dependence (R2 = 0.9935) on the discount rate. Sensitivity and uncertainty analyses showed that resin binding capacity, PBA resins purchase cost and Hibiscus sabdafiffa L. calyx anthocyanins (HSCAs) recovery had most contributions to uncertainties in MSP.
KW - Economic analysis
KW - Hibiscus sabdariffa L. calyx
KW - Microencapsulated anthocyanins powder
KW - Minimum selling price
KW - Process synthesis
UR - http://www.scopus.com/inward/record.url?scp=85124696201&partnerID=8YFLogxK
U2 - 10.1016/j.rineng.2022.100371
DO - 10.1016/j.rineng.2022.100371
M3 - Article
AN - SCOPUS:85124696201
SN - 2590-1230
VL - 13
JO - Results in Engineering
JF - Results in Engineering
M1 - 100371
ER -