Optimization of Astaxanthin Recovery in the Downstream Process of <i>Haematococcus pluvialis</i>

Astaxanthin derived from <i>Haematococcus pluvialis</i> is a valuable metabolite applied in a wide range of products. Its extraction depends on a sophisticated series of downstream process steps, including harvesting, disruption, drying, and extraction, of which some are dependent on eac...

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Main Authors: Inga K. Koopmann, Simone Möller, Clemens Elle, Stefan Hindersin, Annemarie Kramer, Antje Labes
Format: Article
Language:English
Published: MDPI AG 2022-05-01
Series:Foods
Subjects:
Online Access:https://www.mdpi.com/2304-8158/11/9/1352
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author Inga K. Koopmann
Simone Möller
Clemens Elle
Stefan Hindersin
Annemarie Kramer
Antje Labes
author_facet Inga K. Koopmann
Simone Möller
Clemens Elle
Stefan Hindersin
Annemarie Kramer
Antje Labes
author_sort Inga K. Koopmann
collection DOAJ
description Astaxanthin derived from <i>Haematococcus pluvialis</i> is a valuable metabolite applied in a wide range of products. Its extraction depends on a sophisticated series of downstream process steps, including harvesting, disruption, drying, and extraction, of which some are dependent on each other. To determine the processes that yield maximum astaxanthin recovery, bead milling, high-pressure homogenization, and no disruption of <i>H. pluvialis</i> biomass were coupled with spray-drying, vacuum-drying, and freeze-drying in all possible combinations. Eventually, astaxanthin was extracted using supercritical CO<sub>2</sub>. Optimal conditions for spray-drying were evaluated through the design of experiments and standard least squares regression (feed rate: 5.8 mL/min, spray gas flow: 400 NL/h, inlet temperature: 180 °C). Maximal astaxanthin recoveries were yielded using high-pressure homogenization and lyophilization (85.4%). All combinations of milling or high-pressure homogenization and lyophilization or spray-drying resulted in similar recoveries. Bead milling and spray-drying repeated with a larger spray-dryer resulted in similar astaxanthin recoveries compared with the laboratory scale. Smaller astaxanthin recoveries after the extraction of vacuum-dried biomass were mainly attributed to textural changes. Evaluation of these results in an economic context led to a recommendation for bead milling and spray-drying prior to supercritical CO<sub>2</sub> extraction to achieve the maximum astaxanthin recoveries.
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spelling doaj.art-45ae89188d93447bb32ac797152dbd082023-11-23T08:14:16ZengMDPI AGFoods2304-81582022-05-01119135210.3390/foods11091352Optimization of Astaxanthin Recovery in the Downstream Process of <i>Haematococcus pluvialis</i>Inga K. Koopmann0Simone Möller1Clemens Elle2Stefan Hindersin3Annemarie Kramer4Antje Labes5ZAiT, Bio and Food Technology, Faculty Energy and Biotechnology, Flensburg University of Applied Sciences, 24943 Flensburg, GermanyZAiT, Bio and Food Technology, Faculty Energy and Biotechnology, Flensburg University of Applied Sciences, 24943 Flensburg, GermanySea & Sun Technology GmbH, 24610 Trappenkamp, GermanySea & Sun Technology GmbH, 24610 Trappenkamp, GermanyZAiT, Bio and Food Technology, Faculty Energy and Biotechnology, Flensburg University of Applied Sciences, 24943 Flensburg, GermanyZAiT, Bio and Food Technology, Faculty Energy and Biotechnology, Flensburg University of Applied Sciences, 24943 Flensburg, GermanyAstaxanthin derived from <i>Haematococcus pluvialis</i> is a valuable metabolite applied in a wide range of products. Its extraction depends on a sophisticated series of downstream process steps, including harvesting, disruption, drying, and extraction, of which some are dependent on each other. To determine the processes that yield maximum astaxanthin recovery, bead milling, high-pressure homogenization, and no disruption of <i>H. pluvialis</i> biomass were coupled with spray-drying, vacuum-drying, and freeze-drying in all possible combinations. Eventually, astaxanthin was extracted using supercritical CO<sub>2</sub>. Optimal conditions for spray-drying were evaluated through the design of experiments and standard least squares regression (feed rate: 5.8 mL/min, spray gas flow: 400 NL/h, inlet temperature: 180 °C). Maximal astaxanthin recoveries were yielded using high-pressure homogenization and lyophilization (85.4%). All combinations of milling or high-pressure homogenization and lyophilization or spray-drying resulted in similar recoveries. Bead milling and spray-drying repeated with a larger spray-dryer resulted in similar astaxanthin recoveries compared with the laboratory scale. Smaller astaxanthin recoveries after the extraction of vacuum-dried biomass were mainly attributed to textural changes. Evaluation of these results in an economic context led to a recommendation for bead milling and spray-drying prior to supercritical CO<sub>2</sub> extraction to achieve the maximum astaxanthin recoveries.https://www.mdpi.com/2304-8158/11/9/1352isomerizationUHPLC-PDA-MSmicroalgaecarotenoidsdisruptiondrying
spellingShingle Inga K. Koopmann
Simone Möller
Clemens Elle
Stefan Hindersin
Annemarie Kramer
Antje Labes
Optimization of Astaxanthin Recovery in the Downstream Process of <i>Haematococcus pluvialis</i>
Foods
isomerization
UHPLC-PDA-MS
microalgae
carotenoids
disruption
drying
title Optimization of Astaxanthin Recovery in the Downstream Process of <i>Haematococcus pluvialis</i>
title_full Optimization of Astaxanthin Recovery in the Downstream Process of <i>Haematococcus pluvialis</i>
title_fullStr Optimization of Astaxanthin Recovery in the Downstream Process of <i>Haematococcus pluvialis</i>
title_full_unstemmed Optimization of Astaxanthin Recovery in the Downstream Process of <i>Haematococcus pluvialis</i>
title_short Optimization of Astaxanthin Recovery in the Downstream Process of <i>Haematococcus pluvialis</i>
title_sort optimization of astaxanthin recovery in the downstream process of i haematococcus pluvialis i
topic isomerization
UHPLC-PDA-MS
microalgae
carotenoids
disruption
drying
url https://www.mdpi.com/2304-8158/11/9/1352
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