scholarly journals ß-galactosidase production by Kluyveromyces lactis in batch and continuous culture

2011 ◽  
Author(s):  
◽  
Elaine C. Ram

Kluyveromyces sp. have adapted to existence in milk due to the evolution of permeabilisation and hydrolytic systems that allow the utilisation of lactose, the sugar most abundant in milk. Lactose hydrolysis, to equimolar units of glucose and galactose, is facilitated by a glycoside hydrolase, i.e., β-galactosidase (EC 3.2.1.23). The versatility of this enzyme allows its application in numerous industrial processes, amongst the most significant of which, is its role in the alleviation of lactose intolerance, one of the most prevalent digestive ailments, globally. In this study, β-galactosidase production by Kluyveromyces lactis UOFS y-0939 was initially optimised in shake flask culture with lactose as the sole carbon source, and thereafter, production was scaled up to batch, fedbatch and continuous culture. Shake flask studies revealed optimum conditions of 30°C, pH 7 and a 10% inoculum ratio, to be most favourable for β-galactosidase synthesis, producing a maximum of 0.35 ± 0.05 U.ml-1 when cell lysates were prepared by ultrasonication with glass beads. Batch cultivation in 28.2 and 40 g.L-1 lactose revealed that elevated levels of the carbon source was not inhibitory to β-galactosidase production, as maximum enzyme activities of 1.58 and 4.08 U.ml-1, respectively, were achieved. Cell lysates prepared by ultrasonication and homogenisation were compared and homogenised cell lysates were more than 3.5 fold higher that those prepared by ultrasonication, proving homogenisation to be the superior method for cell disruption. The lactose feed rate of 4 g.L-1.h-1 in fed-batch culture operated at ± 20.4% DO, appeared to be inhibitory to biomass production, as indicated by the lower biomass productivity in fed-batch (0.82 g.L-1.h-1) than batch culture (1.27 g.L-1.h-1). Enzyme titres, however, were favoured by the low DO levels as a maximum of 8.7 U.ml-1, 5.5 fold more than that obtained in batch culture, was achieved, and would be expected to increase proportionally with the biomass. Continuous culture operated at a dilution rate of 0.2 h-1, under strictly aerobic conditions, revealed these conditions to be inhibitory to the lactose consumption rate, however, the non-limiting lactose and high DO environment was favourable for β-galactosidase synthesis, achieving an average of 8 ± 0.9 U.ml-1 in steady state.

1991 ◽  
Vol 72 (6) ◽  
pp. 457-460 ◽  
Author(s):  
Nobuyuki Uozumi ◽  
Katsuhito Kohketsu ◽  
Osamu Kondo ◽  
Hiroyuki Honda ◽  
Takeshi Kobayashi

1992 ◽  
Vol 38 (4) ◽  
pp. 296-302 ◽  
Author(s):  
Sharon Harris ◽  
Warwick Silvester

Frankia grown in batch culture was unable to maintain a high rate of nitrogenase activity and, once a peak level was reached, activity rapidly declined. Addition of 5 mM carbon source of cultures or transfer to fresh medium was followed by brief recovery of nitrogenase activity. The extent of recovery decreased as additions or transfers were made to progressively older cultures. Daily addition of fresh medium (dilution rate = 0.125 day−1) allowed Frankia to be maintained in continuous, derepressed culture with stable rates of growth and nitrogenase activity for more than 30 days. The proportion of active, mature vesicles also remained constant in continuous culture but decreased with time inbatch culture. Key words: Frankia, batch culture, continuous culture, nitrogenase activity.


Author(s):  
Rawia, F. Gamal ◽  
Hemmat, M. Abdel-hady ◽  
Shimaa, A. Amin ◽  
Shimaa, K. Ali

Aims: Production of gellan gum by Sphingomoas paucimobilis from whey was optimized by different fermentation techniques. Study Design: Study the growth behavior of Sphingomoas paucimobilis was cultivated on 40% sweet whey medium in the bioreactor as a batch, fed batch and continuous culture and effect of aeration and agitation speed on gellan production. Place and Duration of Study: Microbiology Dept., Fac. of Agriculture, Ain Shams Univ., Cairo, Egypt, 2016/ 2017. Methodology: Using Sphingomoas paucimobilis on sweet whey in the bioreactor as a batch, fed batch (pulsed & continuous) and continuous culture. Among the four levels of air saturation and four levels of agitation speeds. Results: Using the continuous feeding of sugar sweet whey at 1.53 gl-1h-1during 12 h was favorable than pulsed feeding for gellan production in fed-batch culture. In continuous culture addition of                             40% SW at 0.055 h-1 dilution rate (110 ml h-1), the values of gellan parameters recorded by Sphingomoas paucimobilis were 24.34%, 26.54% & 0.337 gl-1h-1 for gellan yield, conversion coefficient and gellan productivity during 24 h. At 28ºC. This technique increments the gellan production (gl-1h-1) by 3.3 &  2.2-2.5 and 1.5- 1.6 fold as compared to that produced by using batch & fed- batch pulsed and fed-batch continuous techniques respectively. The emulsifying capability of the partially purified gellan was 100% whereas it was 95% for xanthan gum, as well as its high flocculating activity than xanthan. A tough worm-like gel or firm gel were formed when 10% calcium chloride solution or 0.5 g sodium chloride were added to gellan solution. Conclusion: The maximum gellan yield and lower fermentation period were obtained with air saturation of 60% at 750 rpm agitation speed. The continuous feeding at 1.53 gl-1h-1 was favorable than pulsed feeding for gellan production in fed-batch culture, while the maximum gellan productivity was obtained by using a continuous culture technique at 0.055 h-1 dilution rate.


2021 ◽  
Vol 18 (22) ◽  
pp. 453
Author(s):  
Azila Adnan ◽  
Giridhar Nair ◽  
Mark Lay ◽  
Janis Swan

Bacterial cellulose (BC) is an abundant polysaccharide, which is secreted by several genera of bacteria. It has remarkable characteristics, which include high purity, high tensile strength, high biocompatibility and non-toxic. The main feature that differentiates BC and plant cellulose (PC) is the absence of contaminants such as lignin, hemicellulose and pectin. However, the main drawbacks in producing BC are low yield and expensive carbon source. Due to that, this study was carried out to enhance BC volumetric productivity in fed-batch operation mode using glycerol as a carbon source. BC was produced in fill-and-draw and pulse-feed fed-batch cultures of Gluconacetobacter xylinus DSM 46604 in a 3-L bench-top bioreactor. The fed-batch fermentation trials were conducted in agitated and aerobic conditions at 30 ºC. For fill-and-draw fed-batch culture, a total of 24.2 g/L of BC accumulated in the bioreactor after 9 days, which corresponded to a yield and productivity of 0.2 g/g and 2.69 g/L/day, respectively. Pulse-feed fed-batch fermentation resulted in a yield and volumetric productivity of 0.38 g/g and 2.71 g/L/day, respectively. The pulse-feed fed-batch culture proved to be a better fermentation system for utilizing glycerol, which is a low-cost and abundant carbon source. HIGHLIGHTS Komagataeibacter species, which were formerly known as Acetobacter or Gluconacetobacter is one of the Gram-negative BC producers that secretes a large quantity of BC microfibrils extracellularly One of the main challenges in bacterial cellulose (BC) production is low productivity and high processing cost As fed-batch fermentation is one of the operation modes in bioprocess that can control the microbial growth rate, this operation mode is conducted to enhance the yield of BC, substrate consumption and also volumetric productivity Fill-and-draw and pulse feed fed-batch culture were conducted to enhance yield and volumetric productivity. The pulse-feed fed-batch culture resulted to be a favorable operation mode for utilizing glycerol, which is a low-cost and abundant carbon source GRAPHICAL ABSTRACT


2001 ◽  
Vol 44 (2) ◽  
pp. 179-184 ◽  
Author(s):  
Oscar Soto-Cruz ◽  
Rafael Chávez-Rivera ◽  
Gerardo Saucedo-Castañeda

Continuous culture study of the ruminal bacterium Megasphaera elsdenii using lactate as carbon source is reported. Butyrate, the minor product in batch culture, was the main product in continuous culture. Under steady state conditions the biomass concentration was increased from 0.46 to 0.72 g l-1. Addition of Yea Sacc did not result an increased availability of carbon. The produced amounts of valerate and CO2 were calculated by using a combined carbon and degree of reduction balances. According to these results, the lactate catabolism of M. elsdenii was changed by the presence of yeast additive, yielding more butyrate and diminishing the production of valerate, while acetate and propionate production was not affected. Results reported in this work suggested that soluble compounds present in the yeast additive filtrate enhanced the anabolism of M. elsdenii and modified the carbon fluxes through its pathways by increasing butyrate and decreasing valerate production in continuous culture.


2020 ◽  
Vol 192 (4) ◽  
pp. 1163-1175
Author(s):  
Muhammad Shafiq ◽  
Liaqat Zeb ◽  
Guannan Cui ◽  
Muhammad Jawad ◽  
Zhanyou Chi

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