scholarly journals Enhanced Cadaverine Production by Recombinant Corynebacterium Glutamicum with Response Regulator DR1558 at low pH Conditions

Author(s):  
Soong-bin Kang ◽  
Jong-Il Choi

Abstract Background: Corynebacterium glutamicum is used industrially to produce various bio-based organic acids. However, it is often cultivated under abiotic stress conditions, such as low pH, which can reduce both cell growth and the yield of the target compound. Here, a response regulator from Deinococcus radiodurans, DR1558, was introduced into a recombinant C. glutamicum strain expressing lysine decarboxylase (cadA) to enhance cadaverine production at acidic pHs.Results: During batch cultivation under acidic conditions, 6.4 g/L of cadaverine was produced by the recombinant C. glutamicum strain expressing cadA and dr1558; this yield was 1.7-fold higher than that produced by a recombinant C. glutamicum strain expressing only cadA. Transcriptional analysis revealed altered expression levels of stress defense- and cadaverine biosynthesis-related genes in the recombinant C. glutamicum strain expressing dr1558. During fed-batch cultivation, the recombinant C. glutamicum strain expressing cadA and dr1558 showed a 2.4-fold increase in cadaverine production compared to that produced by the recombinant C. glutamicum strain expressing only cadA. The cell growth of C. glutamicum expressing both cadA and dr1558 increased markedly during fed-batch cultivation at acidic pH.Conclusion: These results indicated that the response regulator dr1558 altered the expression of genes involved in metabolic pathways and stress defense mechanisms in C. glutamicum. Furthermore, C. glutamicum expressing the D. radiodurans dr1558 can be used to produce bio-based organic acids by fermentation in processes requiring acidic conditions.

Fermentation ◽  
2021 ◽  
Vol 7 (2) ◽  
pp. 62
Author(s):  
Konstantins Dubencovs ◽  
Janis Liepins ◽  
Arturs Suleiko ◽  
Anastasija Suleiko ◽  
Reinis Vangravs ◽  
...  

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.


2001 ◽  
Vol 44 (2) ◽  
pp. 125-128 ◽  
Author(s):  
Sandra A. Furlan ◽  
Heizir F. de Castro

Xylitol production by Candida parapsilosis was investigated under fed-batch cultivation, using single (xylose) or mixed (xylose and glucose) sugars as substrates. The presence of glucose in the medium induced the production of ethanol as secondary metabolite and improved specific rates of growth, xylitol formation and substrate consumption. Fractionated supply of the feed medium at constant sugar concentration did not promote any increase on the productivity compared to the single batch cultivation.


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