Simultaneous hydrolysis of cheese whey and lactulose production catalyzed by β-galactosidase from Kluyveromyces lactis NRRL Y1564

Bioprocess and Biosystems Engineering - β-Galactosidase was produced by the yeast Kluyveromyces lactis NRRL Y1564 in cheese whey supplemented with yeast extract under the optimal temperature...     

Production of β-galactosidase by Kluyveromyces marxianus MTCC 1388 using whey and effect of four different methods of enzyme extraction on β-galactosidase activity

Whey containing 4.4% (w/v) lactose was inoculated with Kluyveromyces marxianus MTCC 1389 for carrying out studies related to β-galactosidase production. β-galactosidase activity was found to be maximum after 30 h and further incubation resulted in decline in activity. The maximum cell biomass of 2.54 mg mL⁻¹ was observed after 36 h of incubation. Lactose concentration dropped drastically to 0.04 % from 4.40% after 36 h of incubation. Out of the four methods tested for extraction of enzyme, SDS — Chlorofom method was found to be best followed by Toluene — Acetone, sonication and homogenization with glass beads in that order. It could be concluded through this study that SDS — Chloroform is cheap and simple method for enzyme extraction from Kluyveromyces cells, which resulted in higher enzyme activity as compared to the activity observed using the remaining extraction methods. The study could also establish that whey could effectively be utilized for β-galactosidase production thus alleviating water pollution problems caused due to its disposal into the water streams.     

Kinetics of improved productivity of β-galactosidase by a cycloheximide-resistant mutant of Kluyveromyces marxianus

The maximum volumetric productivity of beta-galactosidase by a Kluyveromyces marxianus mutant, grown on lactose/corn steep liquor medium for 3 d, was 150 IU l(-1) h(-1) which is twice that of the parent organism. During product formation, mutated cells provided more resistance against thermal inactivation.     

Formulation of a lactose-free, low-cost culture medium for the production of β- D-galactosidase by Kluyveromyces marxianus

A lactose-free, low-cost culture medium for the production of -d-galactosidase by Kluyveromyces marxianus was formulated. At high aeration rates (2.2 vvm) and concentrations of 100 g sugar cane molasses l^–1 as carbon source and 100 g corn steep liquor l^–1 as vitamin and nitrogen source an enzyme production of 708 U l^–1 h was achieved. This was 20% higher than using a medium that contained lactose which is considered the primary inductor of -d-galactosidase synthesis.     

Influence of oxygen transfer rate on β-galactosidase production fromKluyveromyces marxianus

Summary -Galactosidase specific production fromK. marxianus was shown to be related with k a at low rates. A power type curve fitted very well when specific activity was plotted vs. k a. Significant difference in total activity yields among the k a treatments were not found, as every increase in specific activity was compensated by a decrease in biomass concentration.     

Improvement of intracellular β-galactosidase production in fed-batch culture of Kluyveromyces fragilis

Four fed-batch control strategies were evaluated to improve the specific lactase activity of Kluyveromyces fragilis. Control strategies tested included DO-stat control, exponential feeding, exponential feeding with manual feedback control and corrected feed-forward control. Each was implemented with standard sensors (i.e., temperature, dissolved oxygen and pH sensors) commonly installed in fermenters. The highest specific activity was obtained using the corrected feed-forward control strategy, a strategy incorporating a novel method for on-line estimation of specific growth rate. The control strategy was able to operate effectively to a final cell density of 69 g dry wt l^–1 with a specific lactase activity of 2 U mg^–1 cell dry wt.     

Lactose hydrolysis in aqueous two-phase system by whole-cellβ-galactosidase of Kluyveromyces marxianus

Semicontinuous and continuous hydrolysis of lactose in aqueous two-phase systems (polyethylene glycol 20000/dextran 40) with whole-cell-galactosidase ofK. marxianus were studied. Both phase polymers had no effect on-galactosidase activity confined in cells. Good operational stability of the biocatalyst during 55 cycles of semicontinuous process was observed without appreciable decrease in product concentration. Continuous hydrolysis of lactose was performed in the stirred bioreactor, connected with the phase separator. The satisfactory degree of hydrolysis (between 82–88%) and volumetric productivity (21.6 g/l/h) were reached during 72 hours of continuous hydrolysis of 5% (w/w) lactose.     

Selection of potentially probiotic Kluyveromyces lactis for the fermentation of cheese whey–based beverage

This work aimed to assess the probiotic potential of different Kluyveromyces lactis strains isolated from Canastra cheese and to produce a fermented cheese whey beverage added to beetroot juice using the selected strain. Kluyveromyces lactis strains were tested for their resistance to the passage through the simulated gastrointestinal tract, adhesion properties, and functional effects such as inhibition of enteric pathogens, short-chain fatty acids (SCFA) production, and β-galactosidase activity. The selected strain was used to produce a fermented cheese whey beverage added to beetroot juice in different proportions. The produced beverages were characterized using HPLC for sugars, Folin-Ciocalteu for total phenolic content, DPPH for antioxidant activity, and GC-MS for volatiles compounds. Except B51, all strains showed viability above 75% after exposure to the simulated gastric and duodenal juices. The aggregation rates were above 84% in 24 h. Only B9 and C16 strains presented hydrophobicity above 60%. The highest B9 β-galactosidase activities were 2.17 U/g and 2.21 U/g for pH 7 and 9, respectively. The B9 SCFA profile was similar to that found for Saccharomyces bourllardi. The fermented cheese whey beverages presented phenolic content ranging from 102.75 to 291.61 μg EAG/mL and inhibition of DPPH ranging from 38.69 to 81.02% after 21 days of storage, besides being lactose free. Esters and acetates were the most abundant compounds. Kluyveromyces lactis B9 presented interesting results as a potential probiotic yeast. The produced beverages allowed the delivery of K. lactis B9 through innovative product with functional properties.     

Effects of cultivation conditions on the production of heterologous α-galactosidase by Kluyveromyces lactis

Growth conditions relevant for the large-scale production of heterologous proteins with yeasts were studied on a laboratory scale. A strain of Kluyveromyces lactis, containing 15 copies of an expression cassette encoding guar -galactosidase integrated into its ribosomal DNA, was used as a model. By using urea as a nitrogen source, it was possible to produce active extracellular -galactosidase in shake-flask cultures grown on a defined mineral medium. Inclusion of urea instead of ammonium sulphate prevented unwanted acidification of cultures. With urea-containing mineral medium, enzyme production in shake flasks was comparable to that in complex media containing peptone. In contrast, the presence of peptone was required to achieve high productivity in chemostat cultures. The low productivity in chemostat cultures growing on mineral media was not due to loss oft the expression cassette, since addition of peptone to such cultures resulted in an immediate high rate of -galactosidase production. The discrepancy between the behaviour of shake-flask and chemostat cultures during growth on mineral medium illustrates the necessity of physiological studies for the scalling-up of heterologous protein production from laboratory to production scale.     

Oxygen transfer on β- D-galactosidase production by Kluyveromyces marxianus using sugar cane molasses as carbon source

The optimal initial volumetric oxygen transfer coefficient (K_La) was 60 h^–1 for the production of -d-galactosidase from Kluyveromyces marxianus CDB 002, using sugar cane molasses as carbon source. At this K_La applying an agitation/aeration relationship of 700 rpm/0.66 vvm resulted in 812 U l^–1 h^–1 for -d-galactosidase production. This was about 50% better than a relationship of 500 rpm/2 vvm at the same K_La.     

Production of a thermostable extracellular lipase by Kluyveromyces marxianus

Kluyveromyces marxianus was grown in submerged culture in a complex medium with several potential inducers of lipolytic activity (triacylglycerols, fatty acids). The highest extracellular lipolytic enzyme production (about 80 U ml^–1 in 3 d) was obtained when the medium was supplemented with 2 g urea l^–1 plus 5 g tributyrin l^–1. Addition of surfactants (1 g l^–1) did not improve production. The lipase had a high thermal stability in aqueous solution (73% residual activity after 9 d at 50 °C, 16 min half-life time at 100 °C). It was also stable at acidic pH and showed good tolerance to organic solvents (70% residual activity after 2 d in n-hexane of cyclohexane).     

A new bioprocess for the production of prebiotic lactosucrose by an immobilized β-galactosidase

A new bioprocess for the synthesis of lactosucrose was studied using a covalently immobilized β-galactosidase on macrospheres of chitosan. The effects of temperature and pH on the production of lactosucrose and other oligosaccharides were evaluated. At 30 °C and pH 7.0, the maximum concentration of lactosucrose reached to 79 g L⁻¹. The change of the reaction conditions allowed to modify the qualitative profile of the final products without quantitative change in the total of oligosaccharides produced. At pH 7 and 30 °C, products profile was 79 g L⁻¹ of lactosucrose, 37 g L⁻¹ of galactooligosaccharides and 250 g L⁻¹ of total oligosaccharides, while at pH 5 and 64 °C the concentrations for the same compounds were 40, 62 and 250 g L⁻¹, respectively. The immobilization increased the thermal stability up to 260-fold. Using 300 g L⁻¹ of sucrose and 300 g L⁻¹ of lactose, and 8.5 mg of chitosan mL⁻¹, 30 cycles of reuse were performed and the biocatalyst kept the maximal lactosucrose synthesis. These results fulfill some important aspects for the enzyme immobilization and oligosaccharides synthesis: the simplicity of the protocols, the high operational stability of the enzyme and the possibility of driving the final products.     

Causes of the production of multiple forms of β-galactosidase by Bacillus circulans

The presence of multiple types of β-galactosidases in a commercial enzyme preparation from Bacillus circulans ATCC 31382 and differences in their transgalactosylation activity were investigated. Four β-galactosidases, β-Gal-A, β-Gal-B, β-Gal-C, and β-Gal-D, which were immunologically homologous, were isolated and characterized. The N-terminal amino acid sequences of all of the enzymes were identical and biochemical characteristics were similar, except for galactooligosaccharide production. β-Gal-B, β-Gal-C, and β-Gal-D produced mainly tri- and tetra saccharides at maximum yields of 20-30 and 9-12%, while β-Gal-A produced trisaccharide with 7% with 5% lactose as substrate. The Lineweaver-Burk plots for all of the enzymes, except for β-Gal-A, showed biphasic behavior. β-Gal-A was truncated to yield multiple β-galactosidases by treatment with protease isolated from the culture broth of B. circulans. Treatment of β-Gal-A with trypsin yielded an active 91-kDa protein composed of 21-kDa and 70-kDa proteins with characteristics similar to those for β-Gal-D.     

Heterologous Kluyveromyces lactis β-galactosidase secretion by Saccharomyces cerevisiae super-secreting mutants

Several Saccharomyces cerevisiae strains with a super-secreting phenotype have been transformed using a secretion plasmid containing the LAC4 gene and have proven to be effective in the secretion of Kluyveromyces lactis -galactosidase. The strain CGY1585 (ssc1-1) showed the highest secretion (1.7 EU ml^–1) in the culture medium. As far as we know, Kluyveromyces lactis -galactosidase is the largest sized protein and the only intracellular one among those secreted by these mutants hitherto. The recombinant strains all grew in lactose media.     

Comparison of various permeabilization treatments on Kluyveromyces by determining in situ β-galactosidase activity

Permeabilization treatments using organic solvents or physical methods were applied to Kluyveromyces bulgaricus and compared by measuring the β-galactosidase activity of whole cells. The minimum solvent concentrations to be used for obtaining a good permeabilization were: 10% n-butanol; 20% propanol; 30% isopropanol, tert-butanol; 40% ethanol, acetone and 70% dimethylsulphoxide. Toluene/ethanol (1 : 4) at 10% was less effective. The addition of the surfactant Brij 35 to lower alkanol concentrations did not bring about a significant permeabilization but the treatment of cells with Brij 35 with a small amount of toluene in ethanol (4 : 96) resulted in a high enzymatic activity. Yeast pellet, but not yeast suspension, submitted to five cycles of freezing and thawing displayed an enzymatic activity similar to those obtained by organic solvents.     

Structural basis of specificity in tetrameric Kluyveromyces lactis β-galactosidase

β-Galactosidase or lactase is a very important enzyme in the food industry, being that from the yeast Kluyveromyces lactis the most widely used. Here we report its three-dimensional structure both in the free state and complexed with the product galactose. The monomer folds into five domains in a pattern conserved with the prokaryote enzymes of the GH2 family, although two long insertions in domains 2 and 3 are unique and related to oligomerization and specificity. The tetrameric enzyme is a dimer of dimers, with higher dissociation energy for the dimers than for its assembly. Two active centers are located at the interface within each dimer in a narrow channel. The insertion at domain 3 protrudes into this channel and makes putative links with the aglycone moiety of docked lactose. In spite of common structural features related to function, the determinants of the reaction mechanism proposed for Escherichia coli β-galactosidase are not found in the active site of the K. lactis enzyme. This is the first X-ray crystal structure for a β-galactosidase used in food processing.     

Differential induction of β-galactosidase and phospho-β-galactosidase activities in the fermentation of whey permeate by Clostridium acetobutylicum

Summary Strains of Clostridium acetobutylicum were tested for the presence of -galactosidase and phospho--galactosidase activities when grown on lactose. All strains, except C. acetobutylicum ATCC 824, showed both enzyme activities. Only phospho--galactosidase activity was detected with C. acetobutylicum ATCC 824. C. acetobutylicum strains P262 and ATCC 824 showed no detectable -galactosidase or phospho--galactosidase activities when grown on glucose. In the fermentation of whey permeate C. acetobutylicum P262 showed an early induction of phospho--galactosidase associated with the acidogenic phase. The -galactosidase activity peaked at a later stage of the fermentation (22 h) coinciding with the solvent production phase. Similar induction of phospho--galactosidase at the early stages (13 h) of fermentation of whey permeate by C. acetobutylicum ATCC 824 was also shown. No -galactosidase activity was detected during the entire course of fermentation by strain ATCC 824.     

Ethanol production from deproteinized whey byβ-galactosidase coimmobilized cells ofSaccharomyces cerevisiae

Summary The performance of -galactosidase coimmobilized cells ofSaccharomyces cerevisiae was evaluated during shake flask fermentation of deproteinized cheese whey lactose to ethanol. The performance of the coimmobilized enzyme treatment was compared to that of a treatment using acid prehydrolyzed whey lactose (a readily available substrate). Enzyme coimmobilization resulted in a slower rate and a lower extent of substrate utilization, thus giving a lower maximum ethanol concentration (13.5 versus 16.7 g/l). It did result, however, in a better ethanol yield (95% vs. 89% theoretical). It appears that, compared to acid prehydrolysis of whey lactose, through -galactosidase coimmobilization we could succeed in obtaining substantial process simplifications, thus saving in equipment and operating cost, while gaining in ethanol yield at the cost of some reasonable loss in the rate and the extent of lactose utilization.