TY - JOUR
T1 - Advantages of MW-assisted water extraction, combined with steam explosion, of black alder bark in terms of isolating valuable compounds and energy efficiency
AU - Arshanitsa, Alexandr
AU - Ponomarenko, Jevgenija
AU - Lauberte, Līga
AU - Jurkjane, Vilhelmine
AU - Pals, Matiss
AU - Akishin, Yegor
AU - Lauberts, Maris
AU - Jashina, Lilija
AU - Bikovens, Oskars
AU - Telysheva, Galina
N1 - Publisher Copyright:
© 2022 Elsevier B.V.
PY - 2022/7
Y1 - 2022/7
N2 - “Green” extraction of black alder bark using deionized water as an alternative to organic solvents and microwave (MW) - induced heating instead of convective/conductive heating was studied. An extractor of original construction with the MW capacity of 2.4 kW, equipped with a pressurized extraction chamber (V = 1350 cm3) and a condenser section, was used. The MW-assisted heating of the suspension up to the desirable temperature was performed with a uniform high rate of ~ 30 ℃ min−1. The yield of the black alder bark water extracts obtained by MW-assisted extraction varied from 15.4% to 26.4% (on bark dry matter) increasing with increasing extraction temperature (70–150 ℃) and increasing duration of the isothermal step of extraction (0–30 min). The electricity consumption per dry weight of obtained products needed for MW-assisted heating of the substrate containing suspension varied from 6.2 to 32.0 kWh kg−1 being higher at higher extraction temperature and longer duration of isothermal heating step. UHPLC-ESI-MS/MS, GC-FID, Py-GS/MS/FID, UV spectroscopy methods revealed that the main constituents of the obtained black alder bark water extracts were diarylheptanoids, condensed tannins, carbohydrates, organic acids, flavonoids, lignin related phenols. The MW-induced depolymerization of alder bark cell wall constituents (hemicellulose, lignin) evidenced by Py-GC/MS/FID, GC-FID, wet chemistry analyses of extracts and bark residues after extraction, resulted in the disruption of the bark cell wall and isolation of metabolites bound within it by microwaves-assisted extraction (MAE). Therefore, the black alder bark water extracts, obtained by MAE at 70–110 ℃, compared to those isolated by advanced accelerated solvent extraction (ASE) at a given temperature, have higher diversity and higher contents of different groups of phenolic extractives, including a higher content of their major class in alders – diarylheptanoids. The increase of the extraction temperature above 110 ℃ and the duration of extraction up to 30 min led to an increase of the content of carbohydrates and noticeable decrease of phenolics content in extracts, including the dominating diarylheptanoid - oregonin. The content of oregonin, having a high antioxidant activity and valuable biological activities, was in focus of our research and practical interest. MAE with dynamic heating to 90 ℃ without keeping of isothermal heating is the most attractive for obtaining of oregonin-enriched extracts, containing up to 57% of oregonin, in contrast to ASE water extracts with the maximum oregonin content of 39%. In this regime, two-fold less energy consumption (7 vs 15 kWh kg−1) and two and a half times more productivity (1.5 vs 0.6)% min−1 was achieved in comparison to the case of the ASE method used as reference.
AB - “Green” extraction of black alder bark using deionized water as an alternative to organic solvents and microwave (MW) - induced heating instead of convective/conductive heating was studied. An extractor of original construction with the MW capacity of 2.4 kW, equipped with a pressurized extraction chamber (V = 1350 cm3) and a condenser section, was used. The MW-assisted heating of the suspension up to the desirable temperature was performed with a uniform high rate of ~ 30 ℃ min−1. The yield of the black alder bark water extracts obtained by MW-assisted extraction varied from 15.4% to 26.4% (on bark dry matter) increasing with increasing extraction temperature (70–150 ℃) and increasing duration of the isothermal step of extraction (0–30 min). The electricity consumption per dry weight of obtained products needed for MW-assisted heating of the substrate containing suspension varied from 6.2 to 32.0 kWh kg−1 being higher at higher extraction temperature and longer duration of isothermal heating step. UHPLC-ESI-MS/MS, GC-FID, Py-GS/MS/FID, UV spectroscopy methods revealed that the main constituents of the obtained black alder bark water extracts were diarylheptanoids, condensed tannins, carbohydrates, organic acids, flavonoids, lignin related phenols. The MW-induced depolymerization of alder bark cell wall constituents (hemicellulose, lignin) evidenced by Py-GC/MS/FID, GC-FID, wet chemistry analyses of extracts and bark residues after extraction, resulted in the disruption of the bark cell wall and isolation of metabolites bound within it by microwaves-assisted extraction (MAE). Therefore, the black alder bark water extracts, obtained by MAE at 70–110 ℃, compared to those isolated by advanced accelerated solvent extraction (ASE) at a given temperature, have higher diversity and higher contents of different groups of phenolic extractives, including a higher content of their major class in alders – diarylheptanoids. The increase of the extraction temperature above 110 ℃ and the duration of extraction up to 30 min led to an increase of the content of carbohydrates and noticeable decrease of phenolics content in extracts, including the dominating diarylheptanoid - oregonin. The content of oregonin, having a high antioxidant activity and valuable biological activities, was in focus of our research and practical interest. MAE with dynamic heating to 90 ℃ without keeping of isothermal heating is the most attractive for obtaining of oregonin-enriched extracts, containing up to 57% of oregonin, in contrast to ASE water extracts with the maximum oregonin content of 39%. In this regime, two-fold less energy consumption (7 vs 15 kWh kg−1) and two and a half times more productivity (1.5 vs 0.6)% min−1 was achieved in comparison to the case of the ASE method used as reference.
KW - Bark
KW - Black alder
KW - Extraction
KW - Microwaves
KW - Oregonin
UR - https://www.scopus.com/pages/publications/85126938218
U2 - 10.1016/j.indcrop.2022.114832
DO - 10.1016/j.indcrop.2022.114832
M3 - Article
AN - SCOPUS:85126938218
SN - 0926-6690
VL - 181
JO - Industrial Crops and Products
JF - Industrial Crops and Products
M1 - 114832
ER -