scholarly journals Batch and Fed-Batch Production of β-carotene by Rhodotorula Toruloides KP324973 Using Corn Steep Liquor As Sole Carbon Source

Author(s):  
Alireza Habibi ◽  
Samira Fallahi ◽  
Saeed Abbasi ◽  
Rouhallah Sharifi

Abstract Application of agro-industrial waste in microbial fermentation is interesting in economic and environmental aspects. Carotenoids production by Rhodotorula toruloides KP324973 was investigated using corn steep liquor (CSL) as sole carbon source. Haldane model with constants µmax = 0.056 h-1, KS = 1.54 vv-1%, and KI = 58.58 vv-1% showed best describe of cell growth kinetics on CLS. A same maximum carotenoid production rate (Rp) about 2.23 μg gcell-1 h-1 was obtained at initial CSL concentration of 5 v/v% after 72 h and 21 h in batch cultivation in shaken flasks and bubble column reactor (BCR), respectively. Further improvement of carotenogenesis was followed by fed-batch cultivation in BCR where the optimal setting of factors at feed flow rate of 5 mL h-1, pH of 5.66, and temperature 14 ˚C gained a highest Rp = 8.686 μg gcell-1 h-1. Chromatographic analysis showed more than 94% of produced carotenes was β-carotene.

2012 ◽  
Vol 554-556 ◽  
pp. 1925-1928 ◽  
Author(s):  
Ji Wu Li ◽  
Xiao Hong Zhu ◽  
Jun Ya Pan

The stain of Fusarium sp. HJ01 used in 4-chlorophenol (4-CP) degradation was isolated in our laboratory. The effects of pH, temperature, 4-CP concentration, carbon source on 4-CP degradation rate were studied. It was concluded that Fusarium sp. HJ01 could grow with 4-CP as the sole carbon and energy source. 4-CP concentration of 100mg/L in the pH range of 4~10 and temperature range of 25°C~35°C could be degraded completely. The capacity of 4-CP degradation was effectively enhanced by the addiction of sucrose. The kinetics of 4-CP degradation could well accord with the Haldane model for 4-CP as the sole carbon source and with first order equation for added other sucrose.


2020 ◽  
Vol 7 (4) ◽  
pp. 138
Author(s):  
Spyridon Achinas ◽  
Sytse Jelmer Mulder ◽  
Gerrit Jan Willem Euverink

Syngas fermentation by methanogens is a novel process to purify biogas. Methanogens are able to ferment non-desirable CO2, H2, and CO to methane. However, to use methanogens on an industrial scale, more research has to be done. There are studies that discuss the growth of methanogens on syngas in combination with acetate. In this research, growth of methanogens on syngas as sole carbon source is discussed. Effluent of an anaerobic fed-batch was selectively cultivated with syngas in 400 mL Eppendorf© bioreactors. After a period of 7 days, fifteen 120 mL flasks were filled with three different liquid-to-gas ratios (1:1, 1:3, 1:5). Results showed that different liquid-to-gas ratios change the metabolic preference of the anaerobic microbial community. Moreover, complete conversion in a four-to-eight-day period, via the carboxidotrophic pathway, was observed in all three liquid-to-gas ratios.


2010 ◽  
Vol 16 (4) ◽  
pp. 319-327 ◽  
Author(s):  
M. Dilipkumar ◽  
M. Rajasimman ◽  
N. Rajamohan

Kluyveromyces marxianus var marxianus was found to secrete a large amount of extracellular inulinase in to the medium. The optimization of inulinase production using copra waste as carbon source was performed with statistical methodology based on experimental designs. The screening of eighteen nutrients for their influence on inulinase production was achieved using a Plackett-Burman design. Corn steep liquor, (NH4)2SO4, ZnSO4.7H2O, K2HPO4 and urea were selected based on their positive influence on inulinase production. The selected components were optimized using Response Surface Methodology (RSM). The optimum conditions are: corn steep liquor - 0.0560 (g/gds), (NH4)2SO4 - 0.0084 (g/gds), ZnSO4.7H2O - 0.0254 (g/gds), K2HPO4 - 0.0037 (g/gds) and urea - 0.02147 (g/gds). These conditions were validated experimentally which revealed an enhanced inulinase yield of 372 U/gds.


2020 ◽  
Vol 10 (3) ◽  
pp. 5348-5354

This work aim the carotenoid bioproduction by the yeast Phaffia rhodozyma Y-17268 in a fed-batch bioreactor with different low-cost agroindustrial substrates (crude glycerol, corn steep liquor, and rice parboiling water). The maximum concentration of total carotenoid and cell productivity were 4118 µg/L (835 µg/g) and 0.05 g/L. h, respectively, with a feed volume of 75 mL every 12 h. The medium were composed of 100 g/L crude glycerol, 100 g/L corn steep liquor, and 20 g/L rice parboiling water at 25ºC, pHinitial 4.0, agitation rate of 250 rpm, aeration rate of 1.5 vvm and 96 h of bioproduction. 0.188 h-1 of maximum specific growth speeds (μmax) was obtained for the major carotenoid - (all-E)-β-carotene (75.9%). Thus, the yeast P. rhodozyma produced in a fed-batch bioreactor demonstrated a great potential to produce the β-carotene.


2021 ◽  
Vol 20 (1) ◽  
Author(s):  
Pariya Shaigani ◽  
Dania Awad ◽  
Veronika Redai ◽  
Monika Fuchs ◽  
Martina Haack ◽  
...  

Abstract Background Oleaginous yeasts are promising microbial platforms for sustainable, bio-based production of biofuels and oleochemical building blocks. Bio-based residues provide sustainable and cost-effective carbon sources for fermentative yeast oil production without land-use change. Considering the regional abundancy of different waste streams, we chose complex biomass residue streams of marine origin; macroalgae hydrolysate, and terrestrial origin; wheat straw hydrolysate in the presence, and absence of corn steep liquor as a complex nitrogen source. We investigated the biomass and lipid yields of an array of well-described oleaginous yeasts; R. glutinis, T. asahii, R. mucilaginosa, R. toruloides, C. oleaginosus growing on these hydrolysates. Furthermore, their sugar utilization, fatty acid profile, and inhibitory effect of the hydrolysates on yeast growth were compared. For correlative reference, we initially performed comparative growth experiments for the strains on individual monomeric sugars separately. Each of these monomeric sugars was a dominant carbon source in the complex biomass hydrolysates evaluated in this study. In addition, we evaluated N-acetylglucosamine, the monomeric building block of chitin, as a low-cost nitrogen and carbon source in yeast fermentation. Results C. oleaginosus provided the highest biomass and lipid yields. In the wheat straw and brown algae hydrolysates, this yeast strain gained 7.5 g/L and 3.8 g/L lipids, respectively. Cultivation in algae hydrolysate resulted in a higher level of unsaturated fatty acids in the lipids accumulated by all yeast strains. R. toruloides and C. oleaginosus were able to effectively co-utilize mannitol, glucose, and xylose. Growth rates on wheat straw hydrolysate were enhanced in presence of corn steep liquor. Conclusions Among the yeast strains investigated in this study, C. oleaginosus proved to be the most versatile strain in terms of substrate utilization, productivity, and tolerance in the complex media. Various fatty acid profiles obtained on each substrate encourage the manipulation of culture conditions to achieve the desired fatty acid composition for each application. This could be accomplished by combining the element of carbon source with other formerly studied factors such as temperature and oxygen. Moreover, corn steep liquor showed promise for enhancement of growth in the oleaginous strains provided that carbon substrate is available.


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