Abstract
To systematically study multi-stage countercurrent process for Antarctic krill protein extracting and to optimize the multi-stage countercurrent technology, the solubility of Antarctic krill proteins after multi-step dissolution was explored firstly; multi-step extraction was investigated; and then multi-stage countercurrent system for protein extraction was carried out. In single step extraction, krill-to-water ratio and pH were chosen as 1:10 and 12.5 respectively, in order to extract more protein. In the multi-step dissolution process, the protein solubility of aqueous solution at pH 12.5 was 33.0 ± 0.8 mg/mL. Multi-step cross-flow processing testified the feasibility of multi-stage countercurrent assumption. Three-stage countercurrent method using krill-to-water ratio 1:10 extracted, 95.1 ± 0.6% protein from krill, where almost the same water as previous works. The total recovery yield of 67.9 ± 1.6% was achieved after precipitation at pH 4.5.
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Acknowledgements
This study was supported by the Key Research and Development Project of Shandong Province (No. 2015GSF115005), Huimin Special Fund of Qingdao Municipal achievement transformation plan (No.15-9-2-120-NSH), and the Natural Science Foundation of China project (No. 31101380).
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Qi, X., Liao, E., Zhao, K. et al. Multi-stage countercurrent process for extracting protein from Antarctic Krill (Euphausia superba). J Food Sci Technol 55, 4450–4457 (2018). https://doi.org/10.1007/s13197-018-3368-7
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DOI: https://doi.org/10.1007/s13197-018-3368-7