The effect of whey protein hydrolyzates on the lactic acid fermentation

Summary The batch fermentation of whey permeate to lactic acid was improved markedly by the addition of enzymehydrolyzed whey protein. Acid concentrations greater than 90 g/l were achieved at a productivity of 4.3 g/l per h and a 98% substrate use. Cell mass concentration reached 6 g/l. The acid productivity achieved is somewhat higher than that typical for fermentation of whole whey. The process economics, based on in-house hydrolyzate preparation, look promising. Presented in this paper are the experimental results showing the effects of hydrolyzate concentration on acid and cell mass production.     

光合菌群发酵玉米秸秆水解液产氢

以玉米秸秆水解液作为产氢底物,研究光合菌群产氢性能。考察了硫酸浓度、固液比、水解时间、水解温度等秸秆水解条件对产氢的影响,确定了最佳水解条件,并对不同脱毒方法进行了对比研究。结果表明,最佳的水解条件为硫酸浓度1%,固液比1:12,水解时间0.5 h,水解温度为110°C。采用Ca(OH)2脱毒方法的产氢效果要优于其他2种脱毒方法;NH4+在一定浓度范围内对该光合菌群产氢有促进作用。     

Polyhydroxyalkanoate production from whey by Pseudomonas hydrogenovora

Whey permeate from dairy industry was hydrolyzed enzymatically to cleave its main carbon source, lactose, to glucose and galactose. The hydrolysis products were chosen as carbon sources for the production of poly-3-hydroxybutyric acid (PHB) by Pseudomonas hydrogenovora. In shaking flask experiments, the utilization of whey permeate as a cheap substrate was compared to the utilization of pure glucose and galactose for bacterial growth under balanced conditions as well as for the production of PHB under nitrogen limitation. After determination of the inhibition constant Ki for sodium valerate on biomass production (Ki=1.84 g/l), the biosynthesis of PHA co-polyesters containing 3-hydroxybutyrate (3HB) and 3-hydroxyvalerate (3HV) units from hydrolyzed whey permeate and valerate was investigated. The application of hydrolyzed whey permeate turned out to be advantageous compared with the utilization of pure sugars. Therefore, fermentation under controlled conditions in a bioreactor was performed with hydrolyzed whey permeate to obtain detailed kinetic data (maximum specific growth rate, mu max=0.291/h, maximum polymer concentration, 1.27 g/l PHB), values for molecular mass distribution (weight average molecular weight Mw=353.5 kDa, polydispersity index PDI=3.8) and thermo analytical data. The fermentation was repeated with co-feeding of valerate (maximum specific growth rate, mu(max)=0.201/h, maximum polymer concentration, 1.44 g/l poly-(3HB-co-21%-3HV), weight average molecular weight M(w)=299.2 kDa, polydispersity index PDI=4.3).     

Fed-batch cultivation of <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> on lignocellulosic hydrolyzate

Saccharomyces cerevisiae grows very poorly in dilute acid lignocellulosic hydrolyzate during the anaerobic fermentation for fuel ethanol production. However, yeast cells grown aerobically on the hydrolyzate have increased tolerance for the hydrolyzate. Cultivation of yeast on part of the hydrolyzate has therefore the potential of enabling increased ethanol productivity in the fermentation of the hydrolyzate. To evaluate the ability of the yeast to grow in the hydrolyzate, fed-batch cultivations were run using the ethanol concentration as input variable to control the feed-rate. The yeast then grew in an undetoxified hydrolyzate with a specific growth rate of 0.19 h⁻¹ by controlling the ethanol concentration at a low level during the cultivation. However, the biomass yield was lower for the cultivation on hydrolyzate compared to synthetic media: with an ethanol set-point of 0.25 g/l the yield was 0.46 g/g on the hydrolyzate, compared to 0.52 g/g for synthetic media. The main reason for the difference was not the ethanol production per se, but a significant production of glycerol at a high specific growth rate. The glycerol production may be attributed to an insufficient respiratory capacity.     

Enhancement of growth and chitosan production by Rhizopus oryzae in whey medium by plant growth hormones

The effect of some plant growth hormones, viz., gibberellic acid, indole-3-acetic acid, indole-3-butyric acid, and kinetin on chitosan production by Rhizopus oryzae in deproteinized whey was studied. Hormones, at different concentrations, increase the mycelial growth by 19-32%. However, increase in chitosan content of the mycelia was relatively small (1.7-14.3%) over the control. Maximum enhancement was observed with gibberellic acid. Fifty percent more chitosan could be obtained from 1L of whey containing 0.1mg/L gibberellic acid. Hormones, at higher dose, instead of stimulation inhibited both growth and mycelial chitosan content. This study showed that hormones have no influence on degree of deacetylation of chitosan but increase the quality of the chitosan by increasing weight average molecular weight and decreasing polydispersity. All the hormones had been found to enhance chitin deacetylase activity of R. oryzae by 1.067-1.267-fold and may be one of the reasons for increased chitosan production.     

Casein as a necessary factor in the production of stimulatory material for associative growth of lactic streptococci

Strains of Streptococcus cremoris KH and HC produced material that was stimulatory for S. cremoris R₆ in milk and in the dialyzable fraction of milk, but not in the dialysate fraction of milk, lactic acid whey, or lactose broth. The addition of casein to these latter media permitted the production of this stimulatory material to occur. Tryptone, peptone, and yeast extract could not be substituted for casein in producing the stimulatory material or in initiating associative growth in the lactic acid whey. The minimum concentration of casein required appeared to be from 2.0 to 2.5%.     

Enzymatic Modification of Proteins in Foodstuffs

Peptic hydrolyzate of soy protein was submitted to the plastein reaction with α-chymotrypsin under the following condition: substrate concentration, 20%; enzyme-substrate ratio by weight, 1/100; reaction pH, 7.0; and reaction temperature, 37°C. The plastein yield resulting from the plastein reaction for 24 hr was found to depend on the degree of hydrolysis of the substrate (per cent ratio between nitrogen amount in 10% trichloroacetic acid soluble nitrogen and that in whole hydrolyzate); the optimum degree of hydrolysis for the highest plastein yield seemed to lie around 80%. A turbidity appeared in the process of the plastein reaction, whose intensity was correlative to the plastein yield. The peptic hydrolyzate of soy protein per se had bitterness and its magnitude decreased with increasing plastein yield.

As a result of the plastein reaction applied for 24 hr to the hydrolyzate whose degree of hydrolysis was 80%, the average molecular weight estimated by the change in amino nitrogen content increased by approximately three times. The molecular weight distribution pattern obtained by gel filtration supported the above result. The total amount of amino acids liberated from the plastein reaction product by its treatment with either leucine aminopeptidase or carboxypeptidase A was significantly less than that liberated from the original hydrolyzate by its similar treatment. This result also supports the formation of higher-molecular protein-like substances by the plastein reaction. Deuteration study followed by IR spectrometry showed the occurrence of peptide bond formation, i.e. decrease in ionized carboxyl group at 1575 cm^?1 and increase in deuterated amide at 1450 cm^?1, even at the earlier stages of the plastein reaction.     

Purification of kappa-casien glycomacropeptide from sweet whey with undetectable level of phenylalanine

Glycomacropeptide (GMP) found in sweet whey is a biologically active compound released from kappa-casein by the action of chymosin during cheese making. This study was undertaken to purify GMP from sweet whey as a research chemical on a laboratory scale. Glycomacropeptide was isolated from proteins and other non-GMP compounds by deproteinization with trichloroacetic acid and gel chromatography on Sephacryl S-200. The purified GMP accounted for 0.12% of dry sweet whey powder and contained 107.0, 50.9, 61.2 and 4.3 microg, respectively, of sialic acid, galactose, galactosamine and phosphorus per mg dry weight. The GMP was of high purity, with its amino acid composition showing undetectable levels of phenylalanine, tyrosine and arginine, the amino acids that do not occur in bovine GMP. On gel electrophoresis, the GMP showed a single broad band with an average mobility faster than that of carbonic anhydrase (molecular weight = 31 kDa). The purified GMP may be used as a standard glycopeptide in chromatography and electrophoresis and may also be used to test various known or unknown properties and biological activities of this compound.     

The Oligosaccharides Produced from Sucrose by Dematium pullulans

A tetrasaccharide produced from sucrose by Dematium pullulans was obtained in a crystalline state, and its properties and physical constants were studied. By elementary analysis, molecular weight, tetrazolium test, the Raybin test, aldose value, paper chromatographic examination of partial acid hydrolyzate and enzymic hydrolyzate, periodate oxidation, and molar optical rotation, the crystalline compound was identified as β-fructofuranosyl-1-kestose trihydrate.     

Poly(L-histidyl-L-alanyl-α-L-glutamic acid). I. Synthesis

Poly(L -histidyl-L -alanyl-α-L -glutamic acid) has been prepared in order to test the acid–base catalytic ability of a carboxyl-imidazole hydrogen-bonded system. Two different blocked histidyl-alanyl-glutamic acid monomers were used in the polymerization step. The imidazole ring was blocked with either a dinitrophenyl or a t-butyloxycarbonyl group. The γ-carboxyl of glutamic acid was protected as the benzyl ester. Both the coupling reactions and the polymerization step were via the N-hydroxysuccinimide active ester method. Thiolysis removed the dinitrophenyl group, while hydrogen bromide removed the t-butyloxycarbonyl and the benzyl groups. The water-soluble unblocked polymers obtained were fractionated on Sephadex G-50 or Bio-Gel P30. Fractions within a range of average molecular weights of 2,000 to 25,000 were isolated. Enzymatic oxidation of the acid hydrolyzate of the polymers revealed that no detectable racemization had occurred.     

The partial replacement of the serum growth factor requirement of SV3T3 cells by lactalbumin hydrolyzate.

Lactalbumin hydrolyzate (LH), a commercially prepared, enzymatic digest of a milk protein fraction, can partially replace the serum requirement of SV3T3 cells. In a low, but obligatory, background of calf serum (0.15% v/v), LH carses a large increase in the final cell density (5-10 x over the control) while modestly steimulating the actual growth rate. Lactalbumin hydrolyzate does not contain survival activity for SV3T3 cells and does not affect the growth of 3T3 cells. Since even prolonged exposure to pH 4 or 2 results in complete abolishment of the growth-rate stimulatory capability without affecting the capacity to increase the final cell density, it is possible that the LH growth activity may consist of two dissociable components. All of LH growth activity is water soluble, autoclavable, and resists proteolytic treatment. On Sephadex G15 growth activity appears as a single peak at the void volume but on G25 it is retained beyond the void volume as a broad, skewed peak. The relevant molecular weight range lies between 1,500 and 4,000. The putative low pH resistant material is strongly adsorbed to Dowex 1 x 2 and can be displaced from the column by a reduction in the pH. A comparison of the properties of the LH factors with those of known growth promoting agents isolated from serum and various enzymatic digests indicates that these new factors do not correspond to any of these agents.     

Fed-batch Cultivation of Mucor indicus in Dilute-acid Lignocellulosic Hydrolyzate for Ethanol Production

Mucor indicus fermented dilute-acid lignocellulosic hydrolyzates to ethanol in fed-batch cultivation with complete hexose utilization and partial uptake of xylose. The fungus was tolerant to the inhibitors present in the hydrolyzates. It grew in media containing furfural (1 g/l), hydroxymethylfurfural (1 g/l), vanillin (1 g/l), or acetic acid (7 g/l), but did not germinate directly in the hydrolyzate. However, with fed-batch methodology, after initial growth of M. indicus in 500 ml enzymatic wheat hydrolyzate, lignocellulosic hydrolyzate was fermented with feeding rates 55 and 100 ml/h. The fungus consumed more than 46% of the initial xylose, while less than half of this xylose was excreted in the form of xylitol. The ethanol yield was 0.43 g/g total consumed sugar, and reached the maximum concentration of 19.6 g ethanol/l at the end of feeding phase. Filamentous growth, which is regarded as the main obstacle to large-scale cultivation of M. indicus, was avoided in the fed-batch experiments.     

Lactic acid production by batch fermentation of whey permeate: A mathematical model

Summary The batch fermentation of whey permeate to lactic acid was improved by supplementing the broth with enzyme-hydrolyzed whey protein. A mathematical model based on laboratory results predicts to a 99% confidence limit the kinetics of this fermentation. Cell growth, acid production and protein and sugar use rates are defined in quantifiable terms related to the state of cell metabolism. The model shows that the constants of the Leudeking-Piret model are not true constants, but must vary with the medium composition, and especially the peptide average molecular weight. The kinetic mechanism on which the model is based also is presented.Nomenclature K _i lactic acid inhibition constant (g/l) - K _pr protein saturation constant during cell growth (g/l) - K _pr protein saturation constant during maintenance (g/l) - K _s lactose saturation constant (g/l) - [LA] lactic acid concentration (g/l) - [PR] protein concentration (g/l) - [S] lactose concentration (g/l) - t time (h) - [X] cell mass concentration (g/l) - , fermentation constants of Leudeking and Piret - specific growth rate (l/h) - Y _{g, LA/S} acid yield during cell growth (g acid/g sugar) - Y _{m, LA/S} acid yield during maintenance (g acid/g sugar) - Y _x/pr yield (g cells/g protein) - specific sugar use rate during cell growth (g sugar/h·g cell) - specific sugar use rate during maintenance (g sugar/h·cell)     

Batch and repeated batch production of l(+)-lactic acid by Enterococcus faecalis RKY1 using wood hydrolyzate and corn steep liquor

Lactic acid production was investigated for batch and repeated batch cultures of Enterococcus faecalis RKY1, using wood hydrolyzate and corn steep liquor. When wood hydrolyzate (equivalent to 50 g l⁻¹ glucose) supplemented with 15–60 g l⁻¹ corn steep liquor was used as a raw material for fermentation, up to 48.6 g l⁻¹ of lactic acid was produced with, volumetric productivities ranging between 0.8 and 1.4 g l⁻¹ h⁻¹. When a medium containing wood hydrolyzate and 15 g l⁻¹ corn steep liquor was supplemented with 1.5 g l⁻¹ yeast extract, we observed 1.9-fold and 1.6-fold increases in lactic acid productivity and cell growth, respectively. In this case, the nitrogen source cost for producing 1 kg lactic acid can be reduced to 23% of that for fermentation from wood hydrolyzate using 15 g l⁻¹ yeast extract as a single nitrogen source. In addition, lactic acid productivity could be maximized by conducting a cell-recycle repeated batch culture of E. faecalis RKY1. The maximum productivity for this process was determined to be 4.0 g l⁻¹ h⁻¹.     

Optimization and effect of dairy industrial waste as media components in the production of hyaluronic acid by Streptococcus thermophilus

Hyaluronic acid (HA) production using a dairy industrial waste is a more cost-efficient strategy than using an expensive synthetic medium. In this study, we investigated the production of HA using Streptococcus thermophilus under shake flask conditions using dairy industrial waste as nutritional supplements, namely whey permeate (WP) and whey protein hydrolysate (WPH). Preliminary screening using Plackett–Burman design exhibited WP, WPH, initial pH, and inoculum size as significant factors influencing HA titer. Response surface methodology design of four factors was formulated at three levels for enhanced production of HA. Shake flask HA fermentation by S. thermophilus was performed under global optimized process conditions and the optimal HA titer (342.93?mg?L^?1) corroborates with Box–Behnken design prediction. The molecular weight of HA was elucidated as 9.22–9.46?kDa. The ultralow-molecular weight HA reported in this study has a potential role in drug and gene delivery applications.     

Mouse whey acidic protein is a novel member of the family of 'four-disulfide core' proteins.

Unlike in other mammalian species, the major whey protein in mouse is not alpha-lactalbumin, but a cysteine rich, acidic protein with a molecular weight of 14.0 kDa. We have deduced the amino acid sequence of this mouse acidic of whey protein from the nucleotide sequence of cloned cDNA. The positions of the half cysteines suggest that mouse whey acidic protein (WAP) is a two domain protein, very similar in structure to the plant lectin wheat germ agglutinin and the hypothalamic carrier protein neurophysin.     

Bovine colostrum fraction as a serum substitute for the cultivation of mouse hybridomas

Summary Fractions of bovine colostrum were prepared and their ability to support the growth of mouse-mouse hybridomas in culture was tested. Whey was prepared from defatted colostrum by removal of casein using acid precipitation. An ultrafiltrate was obtained from cleared whey by filtration through membranes with a nominal molecular mass cut-off of 100 000 Da. Colostrum ultrafiltrate contained 1.16 g/l protein, 0.24 g/l immunoglobulin G (IgG) and less than 0.24 EU (endotoxin unit)/ml endotoxins. The effect of defatted colostrum, whey and ultrafiltrate as serum substitutes was examined by cultivation of hybridoma cells in minimal essential medium containing different concentrations of the supplements. Under optimal conditions in ultrafiltrate-supplemented medium, the maximal cell concentration was 35–40% of that obtained using 10% foetal bovine serum, and IgG production per cell was equal to that achieved using serum. In 1% defatted colostrum the maximum hybridoma concentration was about 30% of that in 10% serum, but at higher concentrations hybridoma growth was significantly reduced. The growth-promoting activity of whey was low. The results show that bovine colostrum ultrafiltrate provides a very attractive alternate to serum for production of monoclonal antibodies. Correspondence to: R. Pakkanen     

Nutrition and broth alterations in the lactic acid fermentation

In order to optimize the thermophilic lactic acid fermentation on saccharose as the sole carbon source and improve the effectiveness of the process, alternative nitrogen sources were tested and a minimal broth composition was found. Of the alternative nitrogen sources, whey protein hydrolyzate (WPH) was the best; the broth composition was reduced from seven down to three items. Application of ammonium as a neutralizing agent instead of sodium hydroxide brought an important positive change.     

Interactions among thermophilic lactobacilli during growth in cheese whey

The starters used in the Parmesan cheese technology are whey-cultured, mixed strain cultures of thermophilic rod lactic acid bacteria. In mixed strain cultures, interactions among different strains can result in both stimulatory or inhibitory effects on microbial growth rate and metabolic activity. These effects, studied by the use of conductance, were observed for individual strains of thermophilic lactobacilli, which were grown in whey and in the presence of cell-free supernatant fluids from whey cultures of other strains. The importance of whey as a growth medium on the microbial composition of the whey cultures is discussed.     

Involvement of SDS-stable higher M(r) forms of bovine normal milk alpha-lactalbumin in inducing intestinal IEC-6 cell death

Monomeric 14-kDa bovine alpha-lactalbumin was purified with a preparation of lower molecular weight whey protein concentrate from Holstein cow normal milk followed by size exclusion chromatography. The protein showed a stimulatory rather than an inhibitory effect on the proliferation of a cultured IEC-6 cell line from the rat small intestine. But incubation in 30% trifluoroethanol/acetate buffer (pH 5.5) at 37 degrees C for 5 d in a slowly rotating test tube rendered it highly cytotoxic with concomitant appearance of SDS-stable 20- and 30-kDa forms of alpha-lactalbumin on electrophoresis. Furthermore, alpha-lactalbumin obtained by a one-step purification procedure by affinity chromatography on an anti-alpha-lactalbumin antibody column from the lower molecular weight whey protein concentrate, which had been found to contain several SDS-stable higher M(r) forms of alpha-lactalbumin, exhibited potent inhibitory activity on IEC-6 cell growth. These results indicate the involvement of SDS-stable higher M(r) forms of bovine normal milk alpha-lactalbumin in inducing cell death on the intestinal IEC-6 cell line.