Recovery of Astaxanthin from Shrimp Cooking Wastewater: Optimization of Astaxanthin Extraction by Response Surface Methodology and Kinetic Studies
A protein and astaxanthin-concentrated fraction (Rf) can be recovered from shrimp cooking wastewater by ultrafiltration at 300 kDa, indicating that astaxanthin is somehow associated to membrane-retained proteins. Response surface analysis showed that astaxanthin can be extracted from Rfusing sunflow...
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Published in | Food and bioprocess technology Vol. 8; no. 2; pp. 371 - 381 |
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Main Authors | , , , |
Format | Journal Article |
Language | English |
Published |
Boston
Springer-Verlag
01.02.2015
Springer US Springer Nature B.V |
Subjects | |
Online Access | Get full text |
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Summary: | A protein and astaxanthin-concentrated fraction (Rf) can be recovered from shrimp cooking wastewater by ultrafiltration at 300 kDa, indicating that astaxanthin is somehow associated to membrane-retained proteins. Response surface analysis showed that astaxanthin can be extracted from Rfusing sunflower oil (3:1 v/v) under milder conditions (T < 40 °C) than directly from shrimp exoskeleton. Modeling astaxanthin extraction kinetics at 30 °C revealed that the process is a consequence of both mass transfer and hydrogen bonding between astaxanthin and oil. The freeze-dried concentrate (FR f) showed two-phase extraction profiles with a much faster pigment recovery observed at 30 °C compared to the liquid form (Rf). The best yields of astaxanthin extraction were not further improved after hydrolysis with alcalase at 45 °C for 30 min (HR f), although higher yields were obtained when both Rfand LR f were extracted in the presence of 200 mg/L butylated hydroxyanisole or ethoxyquin. Astaxanthin from this shrimp by-product has low thermal stability in oil at high temperatures (60 and 70 °C), suggesting the carotenoid is mainly free as a result of the cooking process and not bounded to proteins or lipids as it occurs in its natural form. |
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Bibliography: | http://dx.doi.org/10.1007/s11947-014-1403-x |
ISSN: | 1935-5130 1935-5149 |
DOI: | 10.1007/s11947-014-1403-x |