Whey fermentation: on-line analysis of lactose and lactic acid by FTIR spectroscopy

Summary The batch fermentation of whey permeate by Lactobacillus helveticus 8652, was monitored on-line by Fourier transform infrared (FTIR) spectroscopy. Substrate (lactose) and product (lactic acid) levels were measured over a period of 47 h. A method for the quantitative analysis of the two components was first established. Fifteen standard solutions containing both lactose and lactic acid were used. The method developed was tested using validation samples of known composition. Mean errors of 1.1% and 0.9% were attained in the measurement of lactose and lactic acid respectively. Sample analysis is fast (approx. 3 min), simple and almost completely automated. The results obtained with FTIR spectroscopy compared favourably with samples analysed off-line using enzyme kits. Offprint requests to: P. Fairbrother     

A new bioreactor with a semi-fixed packing: investigation of degradation of phenol

A new bioreactor using a semi-fixed packing of frames with “sacks” made of a fabric of “Raschell” type stretched on them is proposed. The construction provides not only a large surface area of the biofilm carrier per unit volume of the apparatus, but also the possibility for an easy removal of the biomass after reaching a certain thickness of the biofilm increasing the gas velocity. Aerobic degradation of phenol in the new bioreactor, using microorganisms of the strain Pseudomonas putida, was studied. The experiments are carried out using water containing 0.7?g/l of phenol at a temperature of 27–30?°C. Different specific surface area of the packing (within 176 and 387?m²/m³) are studied. Degradation rates from 60 to 140?mg/(1?h) are attained. A retardation of the process at the end is observed, probably due to inhibition effect. This rate is 5–6 times higher than the rate observed when using free cells. At air velocity of 0.03–0.035?m/s (related to the total cross section of the bioreactor) the vibrations of the packing material lead to destruction and removal of the old biomass.     

Changes in lactic acid bacteria and components of Awa-bancha by anaerobic fermentation

ABSTRACT

Awa-bancha is a post-fermented tea produced in Naka and Kamikatsu, Tokushima, Japan. We investigated the lactic acid bacteria in each stage of production of Awa-bancha and evaluated the relationships with the components. Lactic acid bacteria were isolated from tea leaves cultured with de Man, Rogosa, and Sharpe (MRS) agar plates, and the species were identified by homology of the 16 S rRNA gene and multiplex polymerase chain reaction (PCR) of the recA gene to distinguish the Lactobacillus plantarum group. As a result, a variety of species were isolated from the raw tea leaves, and Lactobacillus pentosus was isolated most frequently after anaerobic fermentation. Regarding the tea leaf components, organic acids, such as lactic acid, increased, free amino acids decreased, and catechins changed owing to anaerobic fermentation. Our results suggest that the microbial flora mainly composed of L. pentosus is important in the anaerobic fermentation process for flavor formation of Awa-bancha.     

Direct lactic acid fermentation: Focus on simultaneous saccharification and lactic acid production

In the recent decades biotechnological production of lactic acid has gained a prime position in the industries as it is cost effective and eco-friendly. Lactic acid is a versatile chemical having a wide range of applications in food, pharmaceutical, leather and textile industries and as chemical feedstock for so many other chemicals. It also functions as the monomer for the biodegradable plastic. Biotechnological production is advantageous over chemical synthesis in that we can utilize cheap raw materials such as agro-industrial byproducts and can selectively produce the stereo isomers in an economic way. Simultaneous saccharification and fermentation can replace the classical double step fermentation by the saccharification of starchy or cellulosic biomass and conversion to lactic acid concurrently by adding inoculum along with the substrate degrading enzymes. It not only reduces the cost of production by avoiding high energy consuming biomass saccharification, but also provides the higher productivity than the single step conversion by the providing adequate sugar release.     

Uptake of lactose and continuous lactic acid fermentation by entrapped non-growing Lactobacillus helveticus in whey permeate

 Continuous production of lactic acid from lactose has been carried out in a stirred-tank reactor with non-growing Lactobacillus helveticus entrapped in calcium alginate beads. A considerably longer operation half-life was obtained in a continuously operated reactor than in a batch-operated reactor. It is possible to simulate the action of entrapped non-growing cells on the basis of information from diffusion and kinetic experiments with suspended free cells. The simulation fit the experimental data over a broad range of substrate concentrations if the specific lactic acid production rate, q _P, was used as a variable parameter in the model. The dynamic mathematical model used is divided into three parts: the reactor model, which describes the mass balance in a continuously operated stirred-tank reactor with immobilized biomass, the mass-transfer model including both external diffusion and internal mass transfer, and the kinetic model for uptake of substrate on the basis of a Michaelis-Menten-type mechanism. From kinetic data obtained for free biomass experiments it was found, with the use of non-linear parameter estimation techniques, that the conversion rate of lactose by L. helveticus followed a Michaelis-Menten-type mechanism with K _S at half-saturation=0.22±0.01 g/l. The maximum specific lactose uptake rate for growing cells, q _S,max, varied between 4.32±0.02 g lactose g cells^-1 h^-1 and 4.89 ±0.02 g lactose g cells^-1 h^-1. The initial specific lactose uptake rate for non-growing cells, q _S,0, was found to be approximately 40% of the maximum specific lactose uptake rate for growing cells. Received: 4 October 1995/Received last revision: 23 April 1996/Accepted: 29 April 1996     

Amylolytic bacterial lactic acid fermentation - a review

Lactic acid, an enigmatic chemical has wide applications in food, pharmaceutical, leather, textile industries and as chemical feed stock. Novel applications in synthesis of biodegradable plastics have increased the demand for lactic acid. Microbial fermentations are preferred over chemical synthesis of lactic acid due to various factors. Refined sugars, though costly, are the choice substrates for lactic acid production using Lactobacillus sps. Complex natural starchy raw materials used for production of lactic acid involve pretreatment by gelatinization and liquefaction followed by enzymatic saccharification to glucose and subsequent conversion of glucose to lactic acid by Lactobacillus fermentation. Direct conversion of starchy biomass to lactic acid by bacteria possessing both amylolytic and lactic acid producing character will eliminate the two step process to make it economical. Very few amylolytic lactic acid bacteria with high potential to produce lactic acid at high substrate concentrations are reported till date. In this view, a search has been made for various amylolytic LAB involved in production of lactic acid and utilization of cheaply available renewable agricultural starchy biomass. Lactobacillus amylophilus GV6 is an efficient and widely studied amylolytic lactic acid producing bacteria capable of utilizing inexpensive carbon and nitrogen substrates with high lactic acid production efficiency. This is the first review on amylolytic bacterial lactic acid fermentations till date.     

Genetics of lactose utilization in lactic acid bacteria

Abstract: Lactose utilization is the primary function of lactic acid bacteria used in industrial dairy fermentations. The mechanism by which lactose is transported determines largely the pathway for the hydrolysis of the internalized disaccharide and the fate of the glucose and galactose moieties. Biochemical and genetic studies have indicated that lactose can be transported via phosphotransferase systems, transport systems dependent on ATP binding cassette proteins, or secondary transport systems including proton symport and lactose-galactose antiport systems. The genetic determinants for the group translocation and secondary transport systems have been identified in lactic acid bacteria and are reviewed here. In many cases the lactose genes are organized into operons or operon-like structures with a modular organization, in which the genes encoding lactose transport are tightly linked to those for lactose hydrolysis. In addition, in some cases the genes involved in the galactose metabolism are linked to or co-transcribed with the lactose genes, suggesting a common evolutionary pathway. The lactose genes show characteristic configurations and very high sequence identity in some phylogenetically distant lactic acid bacteria such as Leuconostoc and Lactobacillus or Lactococcus and Lactobacillus . The significance of these results for the adaptation of lactic acid bacteria to the industrial milk environment in which lactose is the sole energy source is discussed.     

Simultaneous saccharification and fermentation of cellulose to lactic acid

Recent interest in the industrial manufacture of ethanol and other organic chemicals from biomass has led to the utilization of surplus grain and cane juice as a fermentation feedstock. Since those starting materials are also foods, they are expensive. As an alternative, cellulosic substances-the most abundant renewable resources on earth(1)-have long been considered for conversion to readily utilizable hydrolyzates.(2, 3)For the production of ethanol from cellulose, we have proposed the simultaneous saccharification and fermentation (SSF) process.(4) In SSF, enzymatic cellulose hydrolysis and glucose fermentation to ethanol by yeast proceed simultaneously within one vessel. The process advantages-reduced reactor volume and faster saccharification rates-have been confirmed by many researchers.(5-8) During SSF, the faster saccharification rates result because the glucose product is immediately removed, considerably diminishing its inhibitory effect on the cellulase system.(9)To effectively apply the SSF method to produce substances fermented from glucose, several conditions should be satisfied. One is coincident enzymatic hydrolysis and fermentation conditions, such as pH and temperature. The other is that cellulase inhibition by the final product is less than that by glucose and/or cellobiose. One of us has reported that acetic acid, citric acid, itaconic acid, alpha-ketoglutaric acid, lactic acid, and succinic acid scarcely inhibit cellulase.(10) This suggests that if the microorganisms which produce these organic acids were compatible with cellulase reaction conditions, the organic acids could be produced efficiently from cellulosic substrates by SSF.In this article, the successful application of SSF to lactic acid production from cellulose is reported. Though there have been several reports of direct cellulose conversion to organic acids by anaerobes such as Clostridium, only trace amounts of lactic acid were detected in the fermentation medium among the low-molecular-weight fatty acid components.(11-13) Lactic acid is one of the most important organic acids and has a wide range of food-related and industrial applications.     

Extractive fermentation for lactic acid production

Lactic acid extractive fermentation was demonstrated using Alamine 336 in oleyl alcohol at acidic pH. The use of an efficient extraction system was possible through employment of the cell immobilization procedure. Process modeling was performed to relate the various process parameters such as flow rate, concentration, and pH. In experiments with 15% Alamine 336/oleyl alcohol, the bioreactor operation resulted in a higher productivity (12 g/L gel h) compared to that of a control fermentation (7 g/L gel h). Strategies for optimizing the extractive fermentation process were proposed considering both productivity and product recovery.     

Direct fermentation of starch to lactic acid byLactobacillus amylovorus

Summary Fermentation production of lactic acid directly from starch was studied in a batch fermentor usingLactobacillus amylovorus. At an initial concentration of 120 g/L starch, 96.2 g/L of lactic acid was produced from liquefied starch in 20 hours while 92.5 g/L of lactate was produced from the raw starch in 39 hours. High initial glucose levels (100 g/L) in the medium inhibited the organism, unless it had been adapted by growing it in a low-glucose medium. The direct production of lactic acid from starch could reduce overall production costs significantly.     

Modeling and simulation of lactic acid fermentation with inhibition effects of lactic acid and glucose

An unstructured mathematical model for lactic acid fermentation was developed. This model was able to predict the inhibition effects of lactic acid and glucose and was confirmed to be valid with various initial concentrations of lactic acid and glucose. Simulation of energy production was made using this mathematical model, and the relationship between the kinetics of energy metabolism and lactic acid production was also analyzed.     

Coupled lactic acid fermentation and adsorption

Polyvinylpyridine (PVP) and activated carbon were evaluated for coupled lactic acid fermentation and adsorption, to prevent the product concentration from reaching inhibitory levels. The lactic acid production doubled as a result of periodical circulation of the fermentation broth through a PVP adsorption column. The adsorbent was then regenerated and the adsorbed lactate harvested, by passing 0.1 N NaOH through the column. However, each adsorption-regeneration cycle caused about 14% loss of the adsorption capacity, thus limiting the practical use of this rather expensive adsorbent. Activated carbon was found much more effective than PVP in lactic acid and lactate adsorption. The cells of Lactobacillus delbrueckii subsp. delbrueckii (LDD) also had strong tendency to adsorb on the carbon. A study was therefore conducted using an activated carbon column for simultaneous cell immobilization and lactate adsorption, in a semi-batch process with periodical medium replacement. The process produced lactate steadily at about 1.3 g l(-1)h(-1) when the replacement medium contained at least 2 g l(-1) of yeast extract. The production, however, stopped after switching to a medium without yeast extract. Active lactic acid production by LDD appeared to require yeast extract above a certain critical level (<2 g l(-1)).     

Extractive lactic acid fermentation with tri-n-decylamine as the extractant

In this study, the possibility of tri-n-decylamine (TDA) was investigated as the extractant in extractive lactic acid fermentation with a recombinant yeast being used. Extractive fermentation with TDA did not provide high l-lactic acid production relative to fermentation without extraction. Through determination of trace components of the TDA, it was found that the TDA contained a high concentration of 1-decylaldehyde, which was confirmed to be toxic to yeast and to have an inhibitory effect on cell growth even at low concentration (40 ppm). When 1-decylaldehyde in TDA was reduced from 700 ppm to 33 ppm, the productivity and total concentration of lactic acid increased by 1.8 times and 2.5 times, respectively.     

Using banana to generate lactic acid through batch process fermentation

We evaluated the usefulness of waste banana for generating lactic acid through batch fermentation, using Lactobacillus casei under three treatments. Two treatments consisted of substrates of diluted banana purée, one of which was enriched with salts and amino acids. The control treatment comprised a substrate suitable for L. casei growth. When fermentation was evaluated over time, significant differences (P<0.05) were found in the three treatments for each of five variables analyzed (generation and productivity of lactic acid, and consumption of glucose, fructose, and sucrose). Maximum productivity was (in g l^–1 h^–1) 0.13 for the regular banana treatment, 1.49 for the enriched banana, and 1.48 for the control, with no significant differences found between the latter two treatments. Glucose consumption curves showed that L. casei made greater use of the substrate in the enriched banana and control treatments than in the regular banana treatment. For fructose intake, the enriched banana treatment showed significantly better (P<0.05) results than the regular one. Sucrose consumption was insignificant (P<0.05), probably because fermentation time was too short. Even when enriched, diluted banana purée is an ineffective substrate for L. casei, probably because it lacks nutrients.     

Cream fermentation by immobilized lactic acid bacteria

Summary Mesophilic lactic acid bacteria were immobilized in calcium alginate gel and added to pasteurized 15% fat cream at a 1.6x10⁹ bacteria per ml inoculation level. A pH of 5.5 was obtained in only two hours while it took 4 hours under classical conditions. Once the immobilized cells were removed, the cream contained 6.1x10⁶ lactic bacteria per ml which was almost 400 times less than the bacterial population obtained at pH 5.5 under a classical fermentation. The fermented cream obtained from immobilized cells showed much less overacidification under subsequent refrigeration.     

Extractive lactic acid fermentation using ion-exchange resin

Lactic acid fermentation is an end-product-inhibited reaction. The restriction imposed by lactic acid on its fermentation can be avoided by extractive fermentation techniques. Studies were performed by attaching an ion-exchange resin packed column with a 2-L fermentor for separation of lactic acid. The fermentation, in a conventional batch mode, resulted in a lactic acid yield of 0.828 g . g(-1) and a lactic acid productivity of 0.313 g . L(-1) . h(-1). However, these could be further enhanced to 0.929 g . g(-1) and 1.665 g . L(-1) . h(-1) by extractive fermentation techniques. The effect of temperature on extractive fermentation was remarkable and has been included in this work.     

Utilization of renewables for lactic acid fermentation

Originally, lactic acid was produced from pure substrates like glucose. Increasingly, however, agricultural feedstocks such as grains and green biomass are also being used as raw materials for the biotechnological production of lactic acid. A high-productivity lactic acid bacterium strain was selected, process parameters were optimized for the batch fermentation on a laboratory scale, and its performance at cultivation on a barley hydrolysate medium together with different supplements was examined. The present results for the cultivation of the Lactobacillus paracasei on complex nutrient broth are in the same range as those for another strain of the same species with pure glucose, de Man, Rogosa and Sharpe medium (MRS) minerals, peptone and yeast extract. Under these conditions, this strain was able to accumulate more than 100 g lactate/L in the MRS medium. Medium optimization experiments showed that the main part of the nitrogen-containing nutrients in the medium (peptone, yeast extract) can be replaced by protein extracts from green biomass (lucerne green juice). The green juice after pressing fresh biomass contains a series of nitrogen-containing compounds and inorganic salts, which are essential for cell growth. Thus, on laboratory scale, we have demonstrated that it is possible to substitute synthetic nutrients by renewable resources like cereals and green biomass without any loss of productivity. This high biomass concentration together with the number of living cells could increase the productivity to higher levels compared to the well-adapted synthetic nutrients of MRS.     

Rice straw fermentation using lactic acid bacteria

To efficiently utilize rice straw and lessen its disposal problem on the environment, a lactic acid bacteria community, SFC-2 was developed from natural fermentation products of rice straw by continuous enrichment with the MRS-S broth (MRS broth with sucrose), and used to accelerate the fermentation of air-dried straws. The SFC-2 could rapidly lower the pH of the broth and produce high levels of lactic acid. Using a combination of plate isolation, denaturing gradient gel electrophoresis (DGGE) and 16S rDNA sequencing, the microbial composition of the SFC-2 was classified into Lactobacillus, mainly comprised of L. fermentum, L. plantarum and L. paracacei. An evaluation of the fermentation effect of SFC-2 on rice straw showed that it lowered the pH and significantly (P<0.05) increased lactic acid concentration in the straw. Further analysis with DGGE indicated that L. plantarum, L. fermentum and L. paracasei were the dominant species during fermentation.     

通气对乳酸发酵过程的影响

对拟干酪乳杆菌发酵产乳酸的过程进行研究,通过改变不同的通气量(不通气、0.1vvm、0.2 vvm、0.5 vvm)确定0.1vvm的通气量最有利于产生乳酸;再通过优化通气策略,在发酵0～15 h不通空气,15～50 h通0.1 vvm空气使得乳酸的产量比全程通0.1 vvm空气又提高了11.7%,同时乳酸产率也提高了16.2%。最后通过对胞内NAD~+、NADH、乳酸脱氢酶和NADH氧化酶活性、以及发酵过程氧化还原电位(Oxidation-reduction potential,ORP)变化进行分析,阐述了通气影响乳酸发酵过程的机理。