Raman-probes for monitoring metabolites and nutrient fate in Yarrowia lipolytica using deuterated glucose

2022 ◽  
Vol 39 ◽  
pp. 102241
Author(s):  
Gurkeerat Kukal ◽  
Andreas E. Vasdekis ◽  
Armando G. McDonald
Keyword(s):  
Planta Medica ◽  
2006 ◽  
Vol 72 (11) ◽  
Author(s):  
O Gortzi ◽  
S Papanikolaou ◽  
S Lalas ◽  
M Galiotou-Panayotou ◽  
P Mitliaga

LWT ◽  
2021 ◽  
pp. 111760
Author(s):  
Samantha Rossi ◽  
Luigi Parrotta ◽  
Stefano Del Duca ◽  
Marco Dalla Rosa ◽  
Francesca Patrignani ◽  
...  

Fermentation ◽  
2021 ◽  
Vol 7 (2) ◽  
pp. 88
Author(s):  
Paulina Snopek ◽  
Dorota Nowak ◽  
Bartłomiej Zieniuk ◽  
Agata Fabiszewska

Yarrowia lipolytica is one of the most studied non-conventional forms of yeast, exhibiting a high secretory capacity and producing many industrially important and valuable metabolites. The yeast conceals a great biotechnological potential to synthesize organic acids, sweeteners, microbial oil, or fragrances. The vast majority of bioprocesses are carried out in bioreactors, where suitable culture conditions are provided. In the current study, the effect of agitation speed (200–600 rpm) and air flow rate (0.0375–2.0 dm3/(dm3 × min)) on the biomass yield and lipase activity of Y. lipolytica KKP 379 is analyzed in a growth medium containing waste fish oil. The increase of aeration intensity limited the period of oxygen deficit in the medium. Simultaneously, an increase in lipolytic activity was observed from 2.09 U/cm3 to 14.21 U/cm3; however, an excessive agitation speed likely caused oxidative or shear stresses, and a reduction in lipolytic activity was observed. Moreover, it is confirmed that the synthesis of lipases is related to oxygen consumption, pH, and the yeast growth phase, and appropriate process selection may provide two advantages, namely, the maximum use of the waste carbon source and the production of lipolytic enzymes that are valuable in many industries.


2021 ◽  
pp. 124659
Author(s):  
Satish Kommoji ◽  
M. Gopinath ◽  
Polinati Satya Sagar ◽  
D. Yuvaraj ◽  
J. Iyyappan ◽  
...  

2009 ◽  
Vol 11 (5) ◽  
pp. 619-626 ◽  
Author(s):  
Guanglei Liu ◽  
Lixi Yue ◽  
Zhe Chi ◽  
Wengong Yu ◽  
Zhenming Chi ◽  
...  

2019 ◽  
Vol 12 (1) ◽  
Author(s):  
Pratik Prashant Pawar ◽  
Annamma Anil Odaneth ◽  
Rajeshkumar Natwarlal Vadgama ◽  
Arvind Mallinath Lali

Abstract Background Recent trends in bioprocessing have underlined the significance of lignocellulosic biomass conversions for biofuel production. These conversions demand at least 90% energy upgradation of cellulosic sugars to generate renewable drop-in biofuel precursors (Heff/C ~ 2). Chemical methods fail to achieve this without substantial loss of carbon; whereas, oleaginous biological systems propose a greener upgradation route by producing oil from sugars with 30% theoretical yields. However, these oleaginous systems cannot compete with the commercial volumes of vegetable oils in terms of overall oil yields and productivities. One of the significant challenges in the commercial exploitation of these microbial oils lies in the inefficient recovery of the produced oil. This issue has been addressed using highly selective oil capturing agents (OCA), which allow a concomitant microbial oil production and in situ oil recovery process. Results Adsorbent-based oil capturing agents were employed for simultaneous in situ oil recovery in the fermentative production broths. Yarrowia lipolytica, a model oleaginous yeast, was milked incessantly for oil production over 380 h in a media comprising of glucose as a sole carbon and nutrient source. This was achieved by continuous online capture of extracellular oil from the aqueous media and also the cell surface, by fluidizing the fermentation broth over an adsorbent bed of oil capturing agents (OCA). A consistent oil yield of 0.33 g per g of glucose consumed, corresponding to theoretical oil yield over glucose, was achieved using this approach. While the incorporation of the OCA increased the oil content up to 89% with complete substrate consumptions, it also caused an overall process integration. Conclusion The nondisruptive oil capture mediated by an OCA helped in accomplishing a trade-off between microbial oil production and its recovery. This strategy helped in realizing theoretically efficient sugar-to-oil bioconversions in a continuous production process. The process, therefore, endorses a sustainable production of molecular drop-in equivalents through oleaginous yeasts, representing as an absolute microbial oil factory.


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