Production of <Emphasis Type="SmallCaps">l</Emphasis>-lactic acid from a mixture of xylose and glucose by co-cultivation of lactic acid bacteria

The production of optically pure lactic acid in a high yield from xylose or a mixture of xylose and glucose, which is a model hydrolysate of lignocellulose, is described. In a single cultivation, Enterococcus casseliflavus produced 38 g/l of lactic acid with an optical purity of 96% enantiomeric excess (ee) and 6.4 g/l of acetic acid from 50 g/l of xylose when MRS medium was used. When a mixture of 50 g/l of xylose and 100 g/l of glucose was used as the carbon source in a cultivation of E. casseliflavus alone, glucose was converted to lactic acid in the early phase of the cultivation but xylose was hardly consumed. In a co-cultivation where E. casseliflavus and Lactobacillus casei specific for glucose were simultaneously inoculated, little or no lactic acid was produced after the glucose was almost consumed. A co-cultivation with two-stage inoculation (in which E. casseliflavus was added at a cultivation time of 40 h after L. casei cells were inoculated) resulted in complete consumption of 50 g/l of xylose and 100 g/l of glucose. In the co-cultivation, 95 g/l of lactic acid with a high optical purity of 96% ee was obtained at 192 h. Such a co-cultivation using two microorganisms specific for each sugar is considered to be one promising cultivation technique for the efficient production of lactic acid from a sugar mixture derived from lignocellulose.     

Lactic acid production from agricultural resources as cheap raw materials

Agricultural resources such as barley, wheat, and corn were hydrolyzed by commercial amylolytic enzymes and fermented into lactic acid by Enterococcus faecalis RKY1. Although no additional nutrients were supplemented to those resources, lactic acid productivities were obtained at >0.8 g/l h from barley and wheat. When 200 g/l of whole wheat flour was hydrolyzed by amylolytic enzymes after the pre-treatment with 0.3% (v/v) sulfuric acid and sterilized by filtration, E. faecalis RKY1 efficiently produced lactic acid with 2.6 g/l h of lactic acid productivity and 5.90 g/l of maximal dry cell weight without additional nutrients. Lactic acid productivity and cell growth could be enhanced to 31% and 12% higher values than those of non-adapted RKY1, by adaptation of E. faecalis RKY1 to CSL-based medium. When the medium contained 200 g/l of whole wheat flour hydrolyzate, 15 g/l of corn steep liquor, and 1.5 g/l of yeast extract, lactic acid productivity and maximal dry cell weight were obtained at 5.36 g/l h and 14.08 g/l, respectively. This result represented an improvement of up to 106% of lactic acid productivity and 138% of maximal dry cell weight in comparison to the fermentation from whole wheat flour hydrolyzate only.     

Effect of temperature and various nitrogen sources on L(+)-lactic acid production by Lactobacillus casei

 Two homofermentative strains, Lactobacillus casei NRRL B-441 and Lactobacillus casei subsp. rhamnosus NRRL B-445 were selected for further study from 17 lactic acid bacterial strains screened for lactic acid production. The effect of temperature on lactic acid production with the selected strains was investigated by adapting both strains to four different temperatures. The production of L(+)-lactic acid by both strains was most efficient at 37°C, although with L. casei the highest lactic acid concentration was obtained at 41°C. The maximal volumetric productivity with L. casei was 4.1 g l^-1 h^-1 and with L. casei subsp. rhamnosus 3.5 g l^-1 h^-1. The composition of the medium was studied in order to replace the costly yeast extract with less expensive sources of nitrogen and amino acids. From 11 different nitrogen sources investigated at 37°C, barley malt sprouts (88 g l^-1 lactic acid in 66 h) and grass extract (74 g l^-1 lactic acid in 73 h) were the best economic alternatives. The effect of different combinations of yeast extract, peptone and malt sprouts was further studied by using statistical experimental design, and an empirical second-order polynomial model was constructed on the basis of the results. With the right combination most of the yeast extract could be substituted by barley malt sprouts for efficient lactic acid production. A method for extraction of nutrients and growth factors from malt sprouts is also described. Received: 25 September 1995/Accepted: 24 October 1995     

Display of α-Amylase on the Surface of Lactobacillus casei Cells by Use of the PgsA Anchor Protein, and Production of Lactic Acid from Starch

We developed a new cell surface engineering system based on the PgsA anchor protein from Bacillus subtilis. In this system, the N terminus of the target protein was fused to the PgsA protein and the resulting fusion protein was expressed on the cell surface. Using this new system, we constructed a novel starch-degrading strain of Lactobacillus casei by genetically displaying α-amylase from the Streptococcus bovis strain 148 with a FLAG peptide tag (AmyAF). Localization of the PgsA-AmyA-FLAG fusion protein on the cell surface was confirmed by immunofluorescence microscopy and flow cytometric analysis. The lactic acid bacteria which displayed AmyAF showed significantly elevated hydrolytic activity toward soluble starch. By fermentation using AmyAF-displaying L. casei cells, 50 g/liter of soluble starch was reduced to 13.7 g/liter, and 21.8 g/liter of lactic acid was produced within about 24 h. The yield in terms of grams of lactic acid produced per gram of carbohydrate utilized was 0.60 g per g of carbohydrate consumed at 24 h. Since AmyA was immobilized on the cells, cells were recovered after fermentation and used repeatedly. During repeated utilization of cells, the lactic acid yield was improved to 0.81 g per g of carbohydrate consumed at 72 h. These results indicate that efficient simultaneous saccharification and fermentation from soluble starch to lactic acid were carried out by recombinant L. casei cells with cell surface display of AmyA.     

Direct fermentation of various pure and crude starchy substrates to L(+) lactic acid using Lactobacillus amylophilus GV6

Lactobacillus amylophilus GV6 fermented a variety of pure and natural starches directly to L(+) lactic acid. Starch to lactic acid conversion efficiency was more than 90% by strain GV6 at low substrate concentrations with all starches. The strain GV6 produced high yields of lactic acid per g of substrate utilized with pure starches such as soluble starch, corn starch, and potato starch, yielding 92–96% at low substrate concentrations in 2 days and 78–89% at high substrate (10%) concentrations in 4–6 days. Strain GV6 also produced high yields of lactic acid per g of substrate utilized with crude starchy substrates such as wheat flour, sorghum flour, cassava flour, rice flour and barley flour yielding 90–93% at low substrate concentrations in 2 days and 80% or more at high substrate concentrations in 6–7 days. Lactic acid yields by L. amylophilus GV6 with pure starches were comparable when low cost crude starchy substrates were used. Lactic acid productivity by strain GV6 is higher than for any other previously reported strains of L. amylophilus.     

Enhancement of lactic acid production with ram horn peptone by Lactobacillus casei

Ram horns are a waste material from the meat industry. The use of ram horn peptone (RHP) as a supplement for lactic acid production was investigated using Lactobacillus casei. For this purpose, first, RHP was produced. Ram horns were hydrolysed by treating with acids (3 M H₂SO₄ and 6 M HCl) and neutralizing the solutions to yield ram horn hydrolysate (RHH). The RHH was evaporated to yield RHP. The amounts of protein, nitrogen, ash, some minerals, total sugars, total lipids and amino acids of the RHP were determined and compared with a bacto-tryptone from casein. When the concentrations (1–6% w/v) of the RHP were used in bacterial growth medium as a supplement, 2% RHP (ram horn peptone medium) had a maximum influence on the production of lactic acid by L. casei. The content of lactic acid in the culture broth containing 2% RHP (43 g l^–1) grown for 24 h was 30% higher than that of the control culture broth (33 g l^–1) and 10% higher than that of 2% bacto-tryptone (39 g l^–1). RHP was demonstrated to be a suitable supplement for production of lactic acid. This RHP may prove to be a valuable supplement in fermentation technology.     

Sugar-cane pressmud as a novel and inexpensive substrate for production of lactic acid in a solid-state fermentation system

Lactobacillus casei subsp. casei CFTRI 2022 produced a higher concentration of lactic acid (5.27 g/100 g dry sugar-cane pressmud) in a solid-state fermentation (SSF) system as compared to L. helveticus CFTRI 2026 and Streptococcus thermophilus CFTRI 2034. The lactic acid production by L. casei subsp. casei CFTRI 2022 was found to be significantly influenced by the initial moisture content, initial pH and initial sugar concentration of the medium. Studies on four inert materials to reduce the initial sugar concentration in the medium showed the high potential of microcrystalline cellulose whereas the use of diatomaceous earth, acid-washed river sand and washed pith bagasse posed problems. The data indicate the potential of lactic acid production from sugar-cane pressmud in an SSF system.     

Repeated-batch fermentation in biofilm reactors with plastic-composite supports for lactic acid production

Novel plastic supports consisting of polypropylene blended with oat hulls/soybean flour or oat hulls/zein were evaluated as supports for mixed- and pure-culture, repeated-batch, lactic acid fermentations in biofilm reactors. Streptomyces viridosporus T7A (ATCC 39115) was used to form a biofilm for mixed-culture fermentations, and Lactobacillus casei subsp. rhamnosus (ATCC 11443) was used for L-lactic acid production. The pure- and mixed-culture biofilm reactors were operated as repeated-batch fermentors with pH controlled at 5 for more than 2 months in which each reactor's medium was changed every 3 days for 24 batches. The plastic-composite supports performed better than polypropylene-alone supports. Significantly (P<0.05) higher concentrations of lactic acid were produced by the mixed- and pure-culture biofilm bioreactors with corresponding plastic-composite supports (55 g/l and 60 g/l respectively) than with polypropylene-alone supports (48 g/l for both mixed and pure culture). However, the percentage yields, maximum productivity, glucose consumption rates, and growth rates (based on the mass of suspended cells only) were not significantly different between reactors. Maximum lactic acid concentration was consistently greater for the plastic-composite support biofilm reactors. In the suspension culture at pH 5 without plastic supports, maximum lactic acid concentration at days 3 and 5 was 48 g/l and 60 g/l, respectively. These results confirm that the use of plastic-composite supports is recommended for pure-culture lactic acid production in long-term repeated-batch fermentation, and that cell immobilization was occurring.Journal Paper No. J-15813 of the Iowa Agriculture and Home Economics Experiment Station, Ames, Iowa, Projects No. 3253 and 0178     

Lactate from cultures of Lactobacillus casei recovered in a fluidized bed column using ion exchange resin

Summary Lactic acid produced by continuous culture of L.casei in an upflow packed bed reactor, was recovered with Amberlite IRA 400 in a fluidized bed column. Bed expansions of 1.25 and 2.25 were applied. Reutilization did not alter the capability of net recovery of 0.048 ± 0.01 g lactic acid/g resin. When 2200 cm/h of ascensional velocity was used, (bed expansion of 2.25), the resin adsorbed 39.3% of the initial lactic acid and 63.5% was eluted. This resin supported the highest exchange capacity of 0.126 g lactic acid/g resin. Applying high flow rates, the process has potential industrial applications due to the short time employed.     

Evaluation of biofilm reactor solid support for mixed-culture lactic acid production

A combination of lactobacilli and biofilm-forming bacteria were evaluated in continuous fermentations for lactic acid production using various supports. Twelve different bacteria, including species of Bacillus, Pseudomonas, Streptomyces, Thermoactinomyces, and Thermomonospora were tested for biofilm-forming capabilities. Solid supports that were evaluated in either batch or continuous fermentations were pea gravels, 3M-macrolite ceramic spheres, and polypropylene mixed with 25% of various agricultural materials (e.g. corn starch, oat hulls) and extruded to form chips (pp-composite). Biofilm formation was evaluated by the extent of clumping of solid supports, weight gain and (in some instances) Gram stains of the supports after drying overnight at 70° C. The supports consistently producing the best biofilm were pp-composite chips followed by 3M-Macrolite spheres then by pea gravels. The best biofilm formation was observed with P. fragi (ATCC 4973), S. viridosporus T7A (ATCC 39115), and Thermoactinomyces vulgaris (NRRL B-5790), grown optimally at 25, 37, and 45° C, respectively, on various pp-composite chips. Lactic acid bacteria used in the fermentations were Lactobacillus amylophilus (NRRL B-4437), L. casei (ATCC 11443), and L. delbrueckii mutant DP3; these grow optimally at 25, 37 and 45° C, respectively. Lactic acid and biofilm bacteria with compatible temperature optima were inoculated into 50-ml reactors (void volume 25 ml) containing sterile pp-composite supports. Lactic acid production and glucose consumption were determined by HPLC at various flow rates from 0.06 to 1.92 ml/min. Generally, mixed-culture biofilm reactors produced higher levels of lactic acid than lactic acid bacteria alone. S. viridosporus T7A and L. casei on pp-composite chips were the best combination of those tested, and produced 13.0 g/l lactic acid in the reactors without pH control. L. casei produced 10.3 g/l lactic acid under similar conditions.Journal paper no. J-14840 of the Iowa Agriculture and Home Economics Experiment Station, Ames Iowa. Project nos. 2889 and 0178 Correspondence to: A. L. Pometto     

Production of lactic acid and fungal biomass by Rhizopus fungi from food processing waste streams

This study proposed a novel waste utilization bioprocess for production of lactic acid and fungal biomass from waste streams by fungal species of Rhizopus arrhizus 36017 and R. oryzae 2062. The lactic acid and fungal biomass were produced in a single-stage simultaneous saccharification and fermentation process using potato, corn, wheat and pineapple waste streams as production media. R. arrhizus 36017 gave a high lactic acid yield up to 0.94–0.97 g/g of starch or sugars associated with 4–5 g/l of fungal biomass produced, while 17–19 g/l fungal biomass with a lactic acid yield of 0.65–0.76 g/g was produced by the R. oryzae 2062 in 36–48 h fermentation. Supplementation of 2 g/l of ammonium sulfate, yeast extract and peptone stimulated an increase in 8–15% lactic acid yield and 10–20% fungal biomass.

     

Production of lactic acid from paper sludge using acid-tolerant, thermophilic Bacillus coagulan strains

Production of lactic acid from paper sludge was studied using thermophilic Bacillus coagulan strains 36D1 and P4-102B. More than 80% of lactic acid yield and more than 87% of cellulose conversion were achieved using both strains without any pH control due to the buffering effect of CaCO₃ in paper sludge. The addition of CaCO₃ as the buffering reagent in rich medium increased lactic acid yield but had little effect on cellulose conversion; when lean medium was utilized, the addition of CaCO₃ had little effect on either cellulose conversion or lactic acid yield. Lowering the fermentation temperature lowered lactic acid yield but increased cellulose conversion. Semi-continuous simultaneous saccharification and co-fermentation (SSCF) using medium containing 100 g/L cellulose equivalent paper sludge without pH control was carried out in serum bottles for up to 1000 h. When rich medium was utilized, the average lactic acid concentrations in steady state for strains 36D1 and P4-102B were 92 g/L and 91.7 g/L, respectively, and lactic acid yields were 77% and 78%. The average lactic acid concentrations produced using semi-continuous SSCF with lean medium were 77.5 g/L and 77.0 g/L for strains 36D1 and P4-102B, respectively, and lactic acid yields were 72% and 75%. The productivities at steady state were 0.96 g/L/h and 0.82 g/L/h for both strains in rich medium and lean medium, respectively. Our data support that B. coagulan strains 36D1 and P4-102B are promising for converting paper sludge to lactic acid via SSCF.     

The effect of soy protein hydrolyzates on fermentation by Lactobacillus amylovorus

After hydrolysis, soy protein was utilized by the lactic acid bacterium Lactobacillus amylovorus. With the addition of 0.5 and 1% of HT-Proteolytic enzyme for hydrolysis, the molecular weight of soy peptide decreased to 700 Da in 6 h and 1 h, respectively. When the soy protein hydrolyzates were used as a nitrogen source, the molecular weight of soy peptide had a significant influence on the production of lactic acid by Lactobacillus amylovorus and the optimum value was determined to be ∼700 Da. The production rate was also dependent upon the concentration of soy peptide and, with the 3% addition of 700-Da soy peptide, the concentration of lactic acid reached 51 g/litre in a medium with 5% enzyme-thinned starch.     

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.     

<Emphasis Type="SmallCaps">L</Emphasis>(+)-Lactic Acid Production Using <Emphasis Type="Italic">Lactobacillus Casei</Emphasis> in Solid-State Fermentation

Lactobacillus casei was grown at 37 °C on sugarcane bagasse (5 g) soaked with cassava starch hydrolysate (final moistening volume 34 ml) containing 3 g reducing sugar in a solid-state condition. The maximum yield of l-lactic acid after various process optimisations was 2.9 g/5 g initial substrate corresponding to 97% conversion of sugar to lactic acid with initial substrate moisture of 72%.     

Optimization of L(+)-lactic acid production employing statistical experimental design

Summary An orthogonal 2³-factorial experimental design was used to optimize L(+)-lactic acid production byLactobacillus casei. With a 22 % (v/v) inoculum the optimum concentration of yeast extract for maximum lactic acid concentration and yield was about 2 % (w/v) and that of the initial glucose 9 to 11 %.     

Utilization of cyanobacterial biomass from water bloom for bioproduction of lactic acid

Cyanobacterial biomass obtained from water blooms was successfully utilized as a material for lactic acid production. The starch contained in the biomass could be converted to D- and L-lactic acid with 80–90% yield by Lactobacillus amylovorus, in a manner similar to that contained in laboratory-cultured cyanobacterial biomass. The starch was also available for L-lactic acid production with similar high yields by L. agilis and L. ruminis that specifically produce L-lactic acid. The lactic acid production from the cyanobacterial biomass did not require any supplements such as yeast extract which are essential for lactic acid production from reagent soluble starch, indicating that nutrients contained in the cyanobacterial biomass might be effectively used for the production instead of the supplements. The starch content of the fresh cyanobacterial biomass from water bloom was increased from 10 to 19 and 24% by cultivation in 1 and 5% CO₂ in air, respectively. Using such starch-rich biomass, the concentration of lactic acid produced was successfully increased without changes in the conversion yield. These results indicate that wastewater bloom cyanobacteria could be utilized for the production of a useful compound, lactic acid.     

Production of lactic acid from hemicellulose extracts by <Emphasis Type="Italic">Bacillus coagulans</Emphasis> MXL-9

Bacillus coagulans MXL-9 was found capable of growing on pre-pulping hemicellulose extracts, utilizing all of the principle monosugars found in woody biomass. This organism is a moderate thermophile isolated from compost for its pentose-utilizing capabilities. It was found to have high tolerance for inhibitors such as acetic acid and sodium, which are present in pre-pulping hemicellulose extracts. Fermentation of 20 g/l xylose in the presence of 30 g/l acetic acid required a longer lag phase but overall lactic acid yield was not diminished. Similarly, fermentation of xylose in the presence of 20 g/l sodium increased the lag time but did not affect overall product yield, though 30 g/l sodium proved completely inhibitory. Fermentation of hot water-extracted Siberian larch containing 45 g/l total monosaccharides, mainly galactose and arabinose, produced 33 g/l lactic acid in 60 h and completely consumed all sugars. Small amounts of co-products were formed, including acetic acid, formic acid, and ethanol. Hemicellulose extract formed during autohydrolysis of mixed hardwoods contained mainly xylose and was converted into lactic acid with a 94% yield. Green liquor-extracted hardwood hemicellulose containing 10 g/l acetic acid and 6 g/l sodium was also completely converted into lactic acid at a 72% yield. The Bacillus coagulans MXL-9 strain was found to be well suited to production of lactic acid from lignocellulosic biomass due to its compatibility with conditions favorable to industrial enzymes and its ability to withstand inhibitors while rapidly consuming all pentose and hexose sugars of interest at high product yields.     

Lactic acid fermentation by Lactobacillus casei in free cell form and immobilised on gluten pellets

A comparative study of the fermentation of a range of carbohydrate substrates, at various temperatures, was carried out using a commercial Lactobacillus casei strain in a free cell form and immobilised on gluten pellets. This strain required yeast extract, l-cysteine HCl and Mn²⁺ at 5, 0.5 and 0.1 g l^–1, respectively, for maximum growth and lactic acid production. Sugar fermentation using free cells showed preference in the order glucose, sucrose, fructose while lactose was poorly utilised. Optimum temperature for growth and lactic acid production over (18–30 h) was 43 °C. L. casei was successfully immobilised on gluten pellets and fermented glucose and sucrose in a shorter time (18 h) with increased lactic acid production (42 and 41 g l^–1 on glucose and sucrose, respectively).     

Exopolysaccharide production by Lactobacillus casei under controlled pH

Summary The exopolysaccharide (EPS) production and growth characteristics of Lactobacillus casei CRL 87 under pH control were studied. Maximum polymer synthesis (488 mg/l) and cell viability (2.4×10¹⁰ cfu/ml) occurred when L. casei was cultured at a constant pH of 6.0 and 30°C for 24 h. However, the optimum specific EPS production (3.9×10^-5 g EPS/g cell dry weigt) and EPS yield (4.3%) were found at a pH of 4.0.