Lactic acid production from cheese whey by immobilized bacteria

The performance of immobilized Bifidobacterium longum in sodium alginate beads and on a spiral-sheet bioreactor for the production of lactic acid from cheese whey was evaluated. Lactose utilization and lactic acid yield of B. longum were compared with those of Lactobacillus helveticus. B. longum immobilized in sodium alginate beads showed better performance in lactose utilization and lactic acid yield than L. helveticus. In the spiral-sheet bioreactor, a lactose conversion ratio of 79% and lactic acid yield of 0.84 g of lactic acid/g of lactose utilized were obtained during the first run with the immobilized L. helveticus. A lactose conversion ratio of 69% and lactic acid yield of 0.51 g of lactic acid/g of lactose utilized were obtained during the first run with immobilized B. longum in the spiral-sheet bioreactor. In producing lactic acid L. helveticus performed better when using the Spiral Sheet Bioreactor and B. longum showed better performance with gel bead immobilization. Because B. longum is a very promising new bacterium for lactic acid production from cheese whey, its optimum fermentation conditions such as pH and metabolic pathway need to be studied further. The ultrafiltration tests have shown that 94% of the cell and cheese whey proteins were retained by membranes with a mol wt cutoff of 5 and 20 KDa.     

Biohydrogen Production Through Dark Fermentation by a Microbial Consortium Using Whey Permeate as Substrate

Nowadays, hydrogen produced globally has been synthesized from fossil fuel with limited source. Therefore, research has been developed in order to explore biological H₂ production by dark fermentation. The purpose of this work was to evaluate the effect of initial pH and ferrous sulfate and ammonium sulfate concentrations on the production of biohydrogen by dark fermentation. The process was carried out in batch mode under anaerobic conditions, in the absence of light, and at standard room temperature and pressure. A microbial consortium provided by the effluent treatment plant of a local dairy company was inoculated into a synthetic medium supplemented with cheese whey permeate (20 g/L of lactose) as a carbon source. The influence of three variables was analyzed by a central composite design 2⁽³⁾, and the optimum results of hydrogen yield (4.13 mol H₂/mol lactose) and productivity (86.31 mmol H₂/L/day) were achieved at initial pH 7.0 and FeSO₄ and (NH₄)₂SO₄ concentrations of 0.6 and 1.5 g/L, respectively. Under these conditions, the kinetic parameters of fermentation were investigated by analyzing the profile of H₂ yield and productivity, metabolite concentrations, pH, and concentration of dissolved iron. In the kinetic analysis, the modified Gompertz equation described adequately the fermentative hydrogen production from cheese whey permeate (R ²?=?0.98). The profile of ethanol and volatile organic acids showed that lactic acid and butyric acid were the main metabolites produced, and the sum of both by-products corresponded to about 58 % of the total metabolites.     

Succinic Acid Production from Cheese Whey using Actinobacillus succinogenes 130 Z

Actinobacillus succinogenes 130 Z was used to produce succinic acid from cheese whey in this study. At the presence of external CO₂ supply, the effects of initial cheese whey concentration, pH, and inoculum size on the succinic acid production were studied. The by-product formation during the fermentation process was also analyzed. The highest succinic acid yield of 0.57 was obtained at initial cheese whey concentration of 50 g/L, while the highest succinic acid productivity of 0.58 g h⁻¹ L⁻¹ was obtained at initial cheese whey concentration of 100 g/L. Increase in pH and inoculum size caused higher succinic acid yield and productivity. At the preferred fermentation condition of pH 6.8, inoculum size of 5% and initial cheese whey concentration of 50 g/L, succinic acid yield of 0.57, and productivity of 0.44 g h⁻¹ L⁻¹ were obtained. Acetic acid and formic acid were the main by-products throughout the fermentation run of 48 h. It is feasible to produce succinic acid using lactose from cheese whey as carbon resource by A. succinogenes 130 Z.     

Direct Conversion of Sugars and Organic Acids to Biobutanol by Non-growing Cells of Clostridium spp. Incubated in a Nitrogen-Free Medium

Several Clostridium spp. were incubated in a nitrogen-free medium (non-growth medium) containing only butyric acid as a sole precursor for performing butanol production by non-growing cells. Non-growing cells of Clostridium spp., especially Clostridium beijerinckii TISTR 1461, could convert butyric acid to butanol via their sole solventogenic activity. This activity was further enhanced in the presence of glucose as a co-substrate. In addition to glucose, other monosaccharides (i.e., galactose and xylose) and disaccharides (i.e., maltose, sucrose, and lactose) could also be used as a co-substrate with butyric acid. Among the organic acids tested (i.e., formic, acetic, propionic, and butyric acids), only butyric and acetic acids were converted to butanol. This study has shown that it is possible to use the non-growing cells of Clostridium spp. for direct conversion of sugars and organic acids to biobutanol. With this strategy, C. beijerinckii TISTR 1461 produced 12 g/L butanol from 15 g/L glucose and 10 g/L butyric acid with a high butanol yield of 0.68 C-mol/C-mol and a high butanol ratio of 88 %.     

Production of lactic acid from cheese whey by batch and repeated batch cultures of Lactobacillus sp. RKY2

The fermentative production of lactic acid from cheese whey and corn steep liquor (CSL) as cheap raw materials was investigated by using Lactobacillus sp. RKY2 in order to develop a cost-effective fermentation medium. Lactic acid yields based on consumed lactose were obtained at more than 0.98 g/g from the medium containing whey lactose. Lactic acid productivities and yields obtained from whey lactose medium were slightly higher than those obtained from pure lactose medium. The lactic acid productivity gradually decreased with increase in substrate concentration owing to substrate and product inhibitions. The fermentation efficiencies were improved by the addition of more CSL to the medium. Moreover, through the cell-recycle repeated batch fermentation, lactic acid productivity was maximized to 6.34 g/L/h, which was 6.2 times higher than that of the batch fermentation.     

Effect of nutrient supplements addition on ethanol production from cheese whey usingCandida pseudotropicalis under batch condition

Candida pseudotropicalis ATCC 8619 was selected among nine strains of lactose fermenting yeast for the production of ethanol from cheese whey. The effects of three nutrients (ammonium sulfate (NH₄)₂SO₄, dipotassium hydrogen phosphate K₂HPO₄, yeast extract, and a combination of them) on the ethanol yield from cheese whey were investigated. The results indicated that no addition of nutrient supplement is necessary to achieve complete lactose utilization during the cheese whey ethanol fermentation. However, addition of a small concentration (0.005% w/v) of these supplements reduced the lag period and the total fermentation time and increased the specific growth rate of the yeast. Higher concentrations (0.01 and 0.015% w/v) of ammonium sulfate and dipotassium hydrogen phosphate inhibited the cell growth and reduced lactose consumption. The highest ethanol (21.17 g/L) was achieved using yeast extract at a concentration of 0.01% w/v, given a conversion efficiency of 98.3%. No indication of alcohol inhibition was observed in this study.     

Functionalized Alginate as Immobilization Matrix in Enantioselective <Emphasis Type="SmallCaps">l</Emphasis> (+) Lactic Acid Production by <Emphasis Type="Italic">Lactobacillus delbrucekii</Emphasis>

The imperative role of functionalized natural alginate in immobilization of Lactobacillus delbrucekii (NCIM 2365) cells in production of optically pure L (+) lactic acid was studied. L. delbrucekii cells were immobilized in alginate, succinylated alginate and carrageenan to evaluate the bead stability and selectivity towards production of optically pure L (+) lactic acid. The scanning electron microscopic studies of free and immobilized cells show little morphological changes. The present study highlights the use of functionalized alginate-immobilized L. delbrucekii cells in production of L (+) lactic acid in higher yields (0.93 Yp/s in grams) with an improved enantioselectivity (99%). In addition, they further revealed decreased by-product formation (acetic and propionic acid) when compared to free and other immobilized cell fermentation.     

Utilization of Cheese Whey Using Synergistic Immobilization of β-Galactosidase and <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> Cells in Dual Matrices

Whey is a byproduct of the dairy industry, which has prospects of using as a source for production of various valuable compounds. The lactose present in whey is considered as an environmental pollutant and its utilization for enzyme and fuel production, may be effective for whey bioremediation. The dairy yeast Kluyveromyces marxianus have the ability to utilize lactose sharply as the major carbon source for the production of the enzyme. Five strains were tested for the production of the β-galactosidase using whey. The maximum β-galactosidase activity of 1.74 IU/mg dry weight was achieved in whey using K. marxianus MTCC 1389. The biocatalyst was further immobilized on chitosan macroparticles and exhibited excellent functional activity at 35 °C. Almost 89 % lactose hydrolysis was attained for concentrated whey (100 g/L) and retained 89 % catalytic activity after 15 cycles of reuse. Finally, β-galactosidase was immobilized on chitosan and Saccharomyces cerevisiae on calcium alginate, and both were used together for the production of ethanol from concentrated whey. Maximal ethanol titer of 28.9 g/L was achieved during fermentation at 35 °C. The conclusions generated by employing two different matrices will be beneficial for the future modeling using engineered S. cerevisiae in scale-up studies.     

Production of lactic acid from cheese whey by batch and repeated batch cultures of Lactobacillus sp. RKY2

The fermentative production of lactic acid from cheese whey and corn steep liquor (CSL) as cheap raw materials was investigated by using Lactobacillus sp. RKY2 in order to develop a cost-effective fermentation medium. Lactic acid yields based on consumed lactose were obtained at more than 0.98 g/g from the medium containing whey lactose. Lactic acid productivities and yields obtained from whey lactose medium were slightly higher than those obtained from pure lactose medium. The lactic acid productivity gradually decreased with increase in substrate concentration owing to substrate and product inhibitions. The fermentation efficiencies were improved by the addition of more CSL to the medium. Moreover, through the cell-recycle repeated batch fermentation, lactic acid productivity was maximized to 6.34 g/L/h, which was 6.2 times higher than that of the batch fermentation.     

Galacto-oligosaccharides Synthesis from Lactose and Whey by β-Galactosidase Immobilized in PVA

The synthesis of galacto-oligosaccharides (GOS) by ??-galactosidase immobilized in both polyvinyl alcohol (PVA) lenses and sol?Cgel carriers was studied and compared with the performance of the free enzyme. PVA-immobilized ??-galactosidase retained 95?% of the initial activity after seven repeated uses and retained 51?% of the initial activity after 3?months of storage, while sol?Cgel-immobilized ??-galactosidase only retained 39?% of the initial activity under storage. Lactose conversion takes place at a higher rate in the PVA-immobilized ??-galactosidase, while the lowest rate of lactose conversion was noticed with immobilized ??-galactosidase in sol?Cgel. Continuous production of GOS from either lactose or whey, with PVA-immobilized ??-galactosidase, was performed in a packed-bed reactor. A maximum GOS production of 30?% of total sugars was attained for a 40-% lactose feed solution with a feed rate of 10.8?ml/h, at pH 4.5 and 40?°C, corresponding to a productivity of 117?g/l?h. The maximum GOS productivity of 344?g/l?h was obtained at a flow rate of 28.7?ml/h. 3-OS and 4-OS were the major types of GOS formed. Conversion of whey in continuous mode resulted in GOS production of 15?% of total sugars and formation of 45?% 3-OS, 40?% 4-OS, and 15?% 5-OS.     

Production of ginseng saponin and polysaccharide by cell cultures ofPanax notoginseng andPanax ginseng

The effects of various combinations of the two kinds of phytohormones, auxin and cytokinin, on cell growth and production of ginseng saponin and polysaccharide were investigated in suspension cultures ofPanax notoginseng. It was found that a high concentration of kinetin (KT) (7 mg/L) seriously inhibited cell growth, but that of benzyl adenine (BA) did not. Under 0.7 mg/L of cytokinin (i.e., KT and BA), 2,4-dichlorophenoxy acetic acid (2,4-D) at 0.2 mg/L was better for the cell cultures than that at 2 or 20 mg/L; and for both naphthalene acetic acid (NAA) and indole acetic acid (IAA), 20 mg/L was their best level for the cell cultures. The highest cell concentration of 11.9 g/L (by dry wt) was obtained with the combination of 0.2 mg/L of 2,4-D and 0.7 mg/L of BA. The highest saponin content of 13.9% was achieved under 2.0 mg/L IAA and 0.07 mg/L KT; its highest production, i.e., 1.13 g/L, was obtained at 0.2 mg/L of 2,4-D and 0.7 mg/L of KT. Under 20 mg/L NAA and 0.7 mg/L KT, the highest polysaccharide content and production were reached, i.e., 16.4% and 1.86 g/L, respectively. In this work, the effects of phytohormones onP. ginseng cell cultures were also studied. A high saponin production of 1.78 g/L was observed at 10 mg/L of indole butyric acid and 0.1 mg/L of BA, and the highest production of polysaccharide (1.95 g/L) was reached with the combination of 10 mg/L NAA and 0.1 mg/L KT.     

Lactic acid bacteria production from whey

The main purpose of this work was to isolate and characterize lactic acid bacteria (LAB) strains to be used for biomass production using a whey-based medium supplemented with an ammonium salt and with very low levels of yeast extract (0.25 g/L). Five strains of LAB were isolated from naturally soured milk after enrichment in whey-based medium. One bacterial isolate, designated MNM2, exhibited a remarkable capability to utilize whey lactose and give a high biomass yield on lactose. This strain was identified as Lactobacillus casei by its 16S rDNA sequence. A kinetic study of cell growth, lactose consumption, and titratable acidity production of this bacterial strain was performed in a bioreactor. The biomass yield on lactose, the percentage of lactose consumption, and the maximum increase in cell mass obtained in the bioreactor were 0.165 g of biomass/g of lactose, 100%, and 2.0 g/L, respectively, which were 1.44, 1.11, and 2.35 times higher than those found in flask cultures. The results suggest that it is possible to produce LAB biomass from a whey-based medium supplemented with minimal amounts of yeast extract.     

Potential of various archae- and eubacterial strains as industrial polyhydroxyalkanoate producers from whey

Three different microbial wild-type strains are compared with respect to their potential as industrial scale polyhydroxyalkanoate (PHA) producers from the feed stock whey lactose. The halophilic archaeon Haloferax mediterranei as well as two eubacterial strains (Pseudomonas hydrogenovora and Hydrogenophaga pseudoflava) are investigated. H. mediterranei accumulated 50 wt.-% of poly-3-(hydroxybutyrate-co-8%-hydroxyvalerate) from hydrolyzed whey without addition of 3-hydroxyvalerate (3HV) precursors (specific productivity q(p): 9.1 mg x g(-1) x h(-1)). Using P. hydrogenovora, the final percentage of poly-3-hydroxybutyrate (PHB) amounted to 12 wt.-% (q(p): 2.9 mg x g(-1) x h(-1)). With H. pseudoflava, it was possible to reach 40 wt.-% P-3(HB-co-5%-HV) on non-hydrolyzed whey lactose plus addition of valeric acid as 3HV precursor (q(p): 12.5 mg x g(-1) x h(-1)). A detailed characterization of the isolated biopolyesters and an evaluation with regard to the economic feasibility completes the study.     

近平滑假丝酵母细胞催化乙酰基三甲基硅烷不对称还原反应

 采用近平滑假丝酵母细胞用于催化乙酰基三甲基硅烷不对称还原反应, 可高选择性地生成 (R)-1-三甲基硅乙醇. 结果表明, 固定化于海藻酸钙的细胞催化该反应的产物收率比游离细胞的高. 不同辅底物对该反应的影响显著, 以葡萄糖为辅底物时, 反应的初速率较快, 产物收率较高. 该反应的最适条件为: 辅底物 (葡萄糖) 浓度 110 mmol/L, 振荡速度 180 r/min, 缓冲液 pH 值 6.0, 反应温度 30 oC, 底物浓度 20 mmol/L. 在此反应条件下反应的初速率、产物收率和产物的 ee 值分别为 11.4 μmol/h, 96.5% 和 99.9%.     

High hydrostatic pressure increases the biosynthesis of γ-aminobutyric acid using bee pollen as a novel and eco-friendly catalyst

Gamma-amino butyric acid (GABA) has antihypertensive and anti-stress effects on human health. High hydrostatic pressure (HHP), a nonthermal treatment, has been documented as a novel approach to enhance the nutritional quality and functional components of plant-based food. In this study, a novel method to convert monosodium glutamate (MSG) to GABA using bee pollen as a natural catalyst was observed, and the GABA yield was improved by HHP treatment. Firstly, GABA production was confirmed by high performance liquid chromatography (HPLC) and tandem mass spectrometry (MS-MS), the highest GABA production was found in lotus bee pollen (LBP) when different varieties of bee pollen were used for the reaction. Secondly, the reaction conditions were utilized, and the optimal reaction condition of the GABA production was determined as described below: 250 mg/mL of bee pollen mixed with 590 mmol/L of MSG that prepared by 80 mmol/L of phosphate buffer (pH 5.8), and incubated at 40 °C for 6 h. For HHP treatment conditions, a treatment of 200 MPa for 10 min at 40 °C was found as the optimal. Under optimal conditions, GABA production reached 508.79 mmol/L (containing GABA from LBP) from 590 mmol/L of MSG. In conclusion, we found and optimized a novel method to convert monosodium glutamate (MSG) to GABA, and proposed the promotion of HHP on GABA bio-conversion.     

Semicontinuous production of lactic acid from cheese whey using integrated membrane reactor

Semicontinuous production of lactic acid from cheese whey using free cells of Bifidobacterium longum with and without nanofiltration was studied. For the semicontinuous fermentation without membrane separation, the lactic acid productivity of the second and third runs is much lower than the first run. The semicontinuous fermentation with nanoseparation was run semicontinuously for 72 h with lactic acid to be harvested every 24 h using a nanofiltration membrane unit. The cells and unutilized lactose were kept in the reactor and mixed with newly added cheese whey in the subsequent runs. Slight increase in the lactic acid productivity was observed in the second and third runs during the semicontinuous fermentation with nanofiltration. It can be concluded that nanoseparation could improve the lactic acid productivity of the semicontinuous fermentation process.     

Polyhydroxyalkanoate (PHA) Biosynthesis from Whey Lactose

Summary: The potential of three different microbial wild type strains as polyhydroxyalkanoate (PHA) producers from whey lactose is compared. Homopolyester and co-polyester biosynthesis was investigated by the archaeon Haloferax mediterranei and the eubacterial strains Pseudomonas hydrogenovora and Hydrogenophaga pseudoflava. H. mediterranei accumulated 50 wt.-% of poly-3-(hydroxybutyrate-co-6%-hydroxyvalerate) in cell dry mass from hydrolyzed whey without addition of 3-hydroxyvalerate (3HV) precursors (specific productivity q_p: 2.9 mg/g h). Using P. hydrogenovora, the final percentage of poly-3-hydroxybutyrate (PHB) amounted to 12 wt.-% (q_p: 0.03 g/g h); co-feeding of valeric acid resulted in the production of 12 wt.-%. P-3(HB-co-21%-HV) (q_p: 0.02 g/g h). With H. pseudoflava, it was possible to reach 40 wt.-% P-3 (HB-co-5%-HV) on not-hydrolyzed whey lactose plus valeric acid as 3HV precursor (q_p: 9.1 mg/g h); on hydrolyzed whey lactose without addition of valeric acid, the strain produced 30 wt.-% of PHB (q_p: 0.16 g/g h). The characterization of the isolated biopolyesters completes the study.     

基于果糖自氧化体系的抗氧化剂筛选方法

机体内果糖的自氧化过程中会产生多种自由基, 并最终转化为羟自由基, 苯甲酸钠可捕获羟自由基生成具有强荧光信号的羟基苯甲酸钠. 本文采用荧光光度法考察了影响果糖自氧化体系的各种因素, 建立了果糖自氧化产生羟自由基体系. 实验结果表明, 在果糖浓度为8.00 mmol/L, CuSO₄浓度为20.0 μmol/L, 苯甲酸钠浓度为24.0 mmol/L, pH=7.4, 温度为37℃及反应时间为24 h的条件下, 果糖自氧化体系最终可产生19.27 μmol/L的羟自由基. 抗氧化剂的存在可清除果糖自氧化过程中产生的自由基, 使最终生成的羟自由基的量减少, 从而导致生成的羟基苯甲酸钠减少, 荧光信号减弱, 由此建立了基于果糖自氧化体系的抗氧化剂筛选方法. 利用本评价体系考察了抗氧化剂盐酸小檗碱和阿魏酸的抗氧化能力, 实验结果表明, 中药标准品盐酸小檗碱和阿魏酸均能有效清除果糖自氧化体系产生的羟自由基, 其IC₅₀值分别为0.023和0.036 mmol/L.     

Enhanced Properties and Lactose Hydrolysis Efficiencies of Food-Grade β-Galactosidases Immobilized on Various Supports: a Comparative Approach

In this study, a fungal and two yeast β-galactosidases were immobilized using alginate and chitosan. The biochemical parameters and lactose hydrolysis abilities of immobilized enzymes were analyzed. The pH optima of immobilized fungal β-galactosidases shifted to more acidic pH compared to free enzyme. Remarkably, the optimal temperature of chitosan-entrapped yeast enzyme, Maxilact, increased to 60 °C, which is significantly higher than that of the free Maxilact (40 °C) and other immobilized forms. Chitosan-immobilized A. oryzae β-galactosidase showed improved lactose hydrolysis (95.7%) from milk, compared to the free enzyme (82.7%) in 12 h. Chitosan-immobilized Maxilact was the most efficient in lactose removal from milk (100% lactose hydrolysis in 2 h). The immobilized lactases displayed excellent reusability, and chitosan-immobilized Maxilact hydrolyzed >?95% lactose in milk after five reuses. Compared to free enzymes, the immobilized enzymes are more suitable for cost-effective industrial production of low-lactose milk due to improved thermal activity, lactose hydrolysis efficiencies, and reusability.

     

壳聚糖固定化乳酸脱氢酶的制备及酶学性质研究

以磁性壳聚糖作为载体,戊二醛作为交联剂,对乳酸脱氢酶(LDH)进行固定化.固定化的最适条件为:戊二醛浓度6%,pH值7.5,酶的偶联时间2 h.对游离及固定化LDH酶学性质的研究表明,酶促反应的最适pH值为9.2,最适温度分别为37℃和50℃,对乳酸的表观米氏常数分别为1.6 mmol/L和0.9 mmol/L.游离酶和固定化酶在40℃放置150 min后,其活力分别为最初的56.5%和76.1%.固定化酶在4℃贮存4周后,活力仍保留50%以上.固定化酶在室温下与底物重复反应6次后,活力仍保留60%以上,说明固定化酶具有较好的热稳定性、贮存稳定性和复用性.