Fed-batch cultivation of Spirulina (Arthrospira) platensis in tubular reactor using ammonium nitrate as nitrogen source

2010 ◽  
Vol 150 ◽  
pp. 394-394 ◽  
Author(s):  
L.C.C. Martinez ◽  
C. Knysak ◽  
L. Capurro Guimarães ◽  
E.D.G. Danesi ◽  
S. Sato ◽  
...  
Keyword(s):  
Ammonium Nitrate ◽  
Nitrogen Source ◽  
Tubular Reactor ◽  
Arthrospira Platensis ◽  
Batch Cultivation ◽  
Fed Batch ◽  
Fed Batch Cultivation

Fed-Batch Cultivation of Arthrospira platensis Using Carbon Dioxide from Alcoholic Fermentation and Urea as Carbon and Nitrogen Sources

2013 ◽  
Vol 6 (3) ◽  
pp. 1118-1125 ◽  
Author(s):  
Raquel Pedrosa Bezerra ◽  
Marcelo Chuei Matsudo ◽  
Sunao Sato ◽  
Attilio Converti ◽  
João Carlos Monteiro de Carvalho
Keyword(s):  
Carbon Dioxide ◽  
Alcoholic Fermentation ◽  
Nitrogen Sources ◽  
Arthrospira Platensis ◽  
Batch Cultivation ◽  
Fed Batch ◽  
Carbon And Nitrogen Sources ◽  
Carbon And Nitrogen ◽  
Fed Batch Cultivation

Continuous and pulse feedings of urea as a nitrogen source in fed-batch cultivation of Spirulina platensis

2004 ◽  
Vol 31 (3-4) ◽  
pp. 237-245 ◽  
Author(s):  
Luis D Sánchez-Luna ◽  
Attilio Converti ◽  
Gabriela C Tonini ◽  
Sunao Sato ◽  
João C.M de Carvalho
Keyword(s):  
Nitrogen Source ◽  
Spirulina Platensis ◽  
Batch Cultivation ◽  
Fed Batch ◽  
Fed Batch Cultivation

Repeated fed-batch cultivation of Arthrospira (Spirulina) platensis using urea as nitrogen source

2009 ◽  
Vol 43 (1) ◽  
pp. 52-57 ◽  
Author(s):  
Marcelo C. Matsudo ◽  
Raquel P. Bezerra ◽  
Sunao Sato ◽  
Patrizia Perego ◽  
Attilio Converti ◽  
...  
Keyword(s):  
Nitrogen Source ◽  
Spirulina Platensis ◽  
Batch Cultivation ◽  
Fed Batch ◽  
Fed Batch Cultivation

Effects of photobioreactor configuration, nitrogen source and light intensity on the fed-batch cultivation of Arthrospira (Spirulina) platensis. Bioenergetic aspects

2012 ◽  
Vol 37 ◽  
pp. 309-317 ◽  
Author(s):  
Raquel Pedrosa Bezerra ◽  
Marcelo Chuei Matsudo ◽  
Sunao Sato ◽  
Patrizia Perego ◽  
Attilio Converti ◽  
...  
Keyword(s):  
Light Intensity ◽  
Nitrogen Source ◽  
Spirulina Platensis ◽  
Batch Cultivation ◽  
Fed Batch ◽  
Fed Batch Cultivation

scholarly journals Optimization of Synthetic Media Composition for Kluyveromyces marxianus Fed-Batch Cultivation

Fermentation ◽  
2021 ◽  
Vol 7 (2) ◽  
pp. 62
Author(s):  
Konstantins Dubencovs ◽  
Janis Liepins ◽  
Arturs Suleiko ◽  
Anastasija Suleiko ◽  
Reinis Vangravs ◽  
...  
Keyword(s):  
Kluyveromyces Marxianus ◽  
Reaction Medium ◽  
Value Added ◽  
Batch Cultivation ◽  
Batch Processes ◽  
Biomass Growth ◽  
High Cell ◽  
Media Composition ◽  
Fed Batch ◽  
Fed Batch Cultivation

The Kluyveromyces marxianus yeast recently has gained considerable attention due to its applicability in high-value-added product manufacturing. In order to intensify the biosynthesis rate of a target product, reaching high biomass concentrations in the reaction medium is mandatory. Fed-batch processes are an attractive and efficient way how to achieve high cell densities. However, depending on the physiology of the particular microbial strain, an optimal media composition should be used to avoid by-product synthesis and, subsequently, a decrease in overall process effi-ciency. Thus, the aim of the present study was to optimise the synthetic growth medium and feeding solution compositions (in terms of carbon, nitrogen, phosphorous, magnesium, and calcium concentrations) for high cell density K. marxianus fed‑batch cultivations. Additionally, the biomass yields from the vitamin mixture and other macro/microelements were identified. A model predictive control algorithm was successfully applied for a fed-batch cultivation control. Biomass growth and substrate consumption kinetics were compared with the mathematical model predictions. Finally, 2‑phenylethanol biosynthesis was induced and its productivity was estimated. The determined optimal macronutrient ratio for K. marxianus biomass growth was identified as C:N:P = 1:0.07:0.011. The maximal attained yeast biomass concentration was close to 70 g·L-1 and the 2-PE biosynthesis rate was 0.372 g·L−1·h−1, with a yield of 74% from 2-phenylalanine.

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