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  • V článku je analyzován třístavový fenomenologický model tzv. fotosyntetické továrny. Řasová fotosyntéza s uvažováním fotoinhibice je popsána pomocí tří obyčejných diferenciálních rovnic s bilineární strukturou. Další rovnicí modelu je algebraický vztah mezi průměrnou hodnotou aktivovaného stavu a velikostí specifické růstové rychlosti řasové biomasy. Pro intermitentní průběh intenzity ozáření (tzv. cykly světlo/tma) byla hodnota specifické růstové rychlosti v závislosti na parametrech cyklů světlo/tma (doba a úroveň osvětlení, doba temna) odvozena analyticky. Pro hodnoty konstant modelu nalezené v literatuře byl analytický vztah využit k simulování tzv. flashing light experimentů. Výsledky prokazují dobrou kvalitativní shodu s dříve publikovanými experimentálními výsledky. (cs)
  • Mathematical models make it possible to predict or simulate a system behaviour. In biotechnology, models are required for the design of new processes and devices, e.g. bioreactors (6), and for the analysis of existing processes. Biological processes are generally described either in terms of empirical equations or through the use of definite biological or chemical descriptions. In contrast to most of the physical processes the mmechanistic understanding of photosynthesis in microalgae is still small. Quantitative knowledge on photosynthesis and it relation to input ( control ) variables are mainly based on laboratory experiments, and only little information exists about real applications. A number of proposals of reaction kinetics has been presented in the biotechnological literature (2, 8). A common characteristic of most of them is that they are seen as mathematical equations that give a static picture of the dependence of the production rate on available substrate ( e.g. the static dependence of th
  • Mathematical models make it possible to predict or simulate a system behaviour. In biotechnology, models are required for the design of new processes and devices, e.g. bioreactors (6), and for the analysis of existing processes. Biological processes are generally described either in terms of empirical equations or through the use of definite biological or chemical descriptions. In contrast to most of the physical processes the mmechanistic understanding of photosynthesis in microalgae is still small. Quantitative knowledge on photosynthesis and it relation to input ( control ) variables are mainly based on laboratory experiments, and only little information exists about real applications. A number of proposals of reaction kinetics has been presented in the biotechnological literature (2, 8). A common characteristic of most of them is that they are seen as mathematical equations that give a static picture of the dependence of the production rate on available substrate ( e.g. the static dependence of th (en)
Title
  • Multiscale modelling in microalgal biotechnology
  • Multiscale modelling in microalgal biotechnology (en)
  • Mnohoškálové modelování v řasové biotechnologii (cs)
skos:prefLabel
  • Multiscale modelling in microalgal biotechnology
  • Multiscale modelling in microalgal biotechnology (en)
  • Mnohoškálové modelování v řasové biotechnologii (cs)
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  • RIV/60076658:12640/06:00006776!RIV07-MSM-12640___
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  • RIV/60076658:12640/06:00006776
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  • Multiscale modelling in microalgal biotechnology (en)
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  • [10FA22631268]
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  • Plzeň
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  • Modelování a měření nelineárních jevů v mechanice
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  • Štys, Dalibor
  • Papáček, Štěpán
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  • Vědeckotechnická společnost Škoda
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  • 80-02-01827-3
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  • 12640
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