Production of Thermostable α-Amylase, Pullulanase, and α-Glucosidase in Continuous Culture by a New Clostridium Isolate

The production of α-amylase, pullulanase, and α-glucosidase and the formation of fermentation products by the newly isolated thermophilic Clostridium sp. strain EM1 were investigated in continuous culture with a defined medium and an incubation temperature of 60°C. Enzyme production and excretion were greatly influenced by the dilution rate and the pH of the medium. The optimal values for the formation of starch-hydrolyzing enzymes were a pH of 5.9 and a dilution rate of 0.075 to 0.10 per h. Increase of the dilution rate from 0.1 to 0.3 per h caused a drastic drop in enzyme production. The ethanol concentration and optical density of the culture, however, remained almost constant. Growth limitation in the chemostat with 1% (wt/vol) starch was found optimal for enzyme production. Under these conditions 2,800 U of pullulanase per liter and 1,450 U of α-amylase per liter were produced; the amounts excreted were 70 and 55%, respectively.     

Effect of culture conditions on astaxanthin production by a mutant of Phaffia rhodozyma in batch and chemostat culture

Temperature and pH had only a slight effect on the astaxanthin content of a Phaffia rhodozyma mutant, but influenced the maximum specific growth rate and cell yield profoundly. The optimum conditions for astaxanthin production were 22°C at pH 5.0 with a low concentration of carbon source. Astaxanthin production was growth-associated, and the volumetric astaxanthin concentration gradually decreased after depletion of the carbon source. The biomass concentration decreased rapidly during the stationary growth phase with a concomitant increase in the cellular content of astaxanthin. Sucrose hydrolysis exceeded the assimilation rates of D-glucose and D-fructose and these sugars accumulated during batch cultivation. D-Glucose initially delayed D-fructose uptake, but D-fructose utilization commenced before glucose depletion. In continuous culture, the highest astaxanthin content was obtained at the lowest dilution rate of 0.043 h^–1. The cell yield reached a maximum of 0.48 g cells·g^–1 glucose utilized between dilution rates of 0.05 h^–1 and 0.07 h^–1 and decreased markedly at higher dilution rates. Correspondence to: J. C. Du Preez     

Optimization of extracellular xylanase production by Dictyoglomus sp. B1 in continuous culture

The thermophilic, xylanolytic, anaerobic organism, Dictyoglomus sp. B1, was cultivated in batch and continuous cultures in media containing insoluble beech-wood xylan. The extracellular xylanase activity levels obtained for the two cultivation methods were compared. Experiments were performed separately to determine the optimum substrate concentration, dilution rate, pH and temperature for xylanase production. Maximum xylanase activity was found at a substrate concentration of 1.5 g xylan/l, a dilution rate of 0.112 h^–1, pH 8.0 and at 7°C. Different combinations of these optimum values were used in a 2³ factorial experiment to investigate whether an increase in the xylanase production/activity could be achieved. A maximum xylanase activity of 2312 U/l was found when fermentors were operated at 73°C with a substrate concentration of 1.5 g xylan/l, pH 8.0, and a dilution rate of 0.112 h^–1. Thus, the optimum xylanase activity in the factorial experiment was obtained when the conditions that gave the maximum xylanase activities in the individual experiments were combined. Optimum xylanase activity obtained in the 2³ factorial experiment was 6.2 times higher than the activity found in the initial batch culture (373 U/l) and 3.0 times higher than the activity of a batch culture (783 U/l) grown at the same optimum conditions as the factorial experiment. The higher specific xylanase activity (217 U/mg protein) found in the 2³ factorial experiment was 4.1 times higher than the specific activity in the initial batch culture (53 U/mg protein).     

High nisin Z production by Lactococcus lactis UL719 in whey permeate with aeration

The influence of controlled pH (5.0–6.5) and initial dissolved oxygen level (0–90% air saturation) on nisin Z production in a yeast extract/Tween 80-supplemented whey permeate (SWP) was examined during batch fermentations with citrate positive Lactococcus lactis subsp. lactis UL719. The total activity corresponding to the sum of soluble and cell-bound activities, as measured by a critical dilution method, was more than 50% lower at pH 5.0 than in the range 5.5–6.5, although the specific production decreased as pH increased. A maximum nisin Z activity of 8200 AU/ml (4100IU/ml) was observed in the supernatant after 8h of culture for pH ranging from 5.5 to 6.5. Prolonging the culture beyond 12h decreased this activity at pH 6.0 and 6.5 but not at pH 5.5 or 5.0. A corresponding increase in cell-bound activity was probably due to adsorption of soluble bacteriocin to the cell wall. Aeration increased cell-bound and total activity to maximum values of 32800 and 41000 AU/ml (16400 and 20500IU/ml), respectively, with an initial level of 60% air saturation after 24h of incubation at pH 6.0. The specific production at 60% or 90% initial air saturation was eight-fold higher than at 0%.     

The influence of H2, CO2 and dilution rate on the continuous fermentation of acetone-butanol

Summary The effect of product gases, H₂ and CO₂, on solvent production was studied using a continuous culture of alginate-immobilized Clostridium acetobutylicum. Initially, in order to find the optimum dilution rate for aceton--butanol production in this system, fermentations were carried out at various dilution rates. With 10% H₂ and 10% CO₂ in the sparging gas, a dilution rate of 0.07 h^–1 was found to maximize volumetric productivity (0.58 g·l^–1·h^–1), while the maximum specific productivity of 0.27 g^–·h^–1 occured at 0.12 h^–1. Continuous cultures with vigorous sparging of N₂ produced only acids. It was concluded that in the case of continuous fermentation H₂ is essential for good solvent production, although good solvent production is possible in an H₂-absent environment in the case of batch fermentations. When the fermentation was carried out at atmospheric pressure under H₂-enriched conditions, the presence of CO₂ in the sparging gas did not slow down glucose metabolism; rather it changed the direction of the phosphoroclastic reaction and as a result increased the butanol/acetone ratio.     

Production of Thermostable alpha-Amylase, Pullulanase, and alpha-Glucosidase in Continuous Culture by a New Clostridium Isolate

The production of alpha-amylase, pullulanase, and alpha-glucosidase and the formation of fermentation products by the newly isolated thermophilic Clostridium sp. strain EM1 were investigated in continuous culture with a defined medium and an incubation temperature of 60 degrees C. Enzyme production and excretion were greatly influenced by the dilution rate and the pH of the medium. The optimal values for the formation of starch-hydrolyzing enzymes were a pH of 5.9 and a dilution rate of 0.075 to 0.10 per h. Increase of the dilution rate from 0.1 to 0.3 per h caused a drastic drop in enzyme production. The ethanol concentration and optical density of the culture, however, remained almost constant. Growth limitation in the chemostat with 1% (wt/vol) starch was found optimal for enzyme production. Under these conditions 2,800 U of pullulanase per liter and 1,450 U of alpha-amylase per liter were produced; the amounts excreted were 70 and 55%, respectively.     

A novel alkaline, thermostable, protease-free lipase from Pseudomonas sp.

An extracellular, alkali-tolerant, thermostable lipase was from a Pseudomonas sp. It had optimal activity at 65 °C and retained 75% of its activity at 65 °C for 90 min. The pH optimum was 9.6 and it retained more than 70% activity between pH 5 and 9 for 2 h. The culture broth was free of protease and, at 30 °C, the culture filtrate retained all the activity for at least 7 days, without any stabilizer. In shake flask culture, addition of groundnut oil (3 g l^–1) towards the end of growth phase increased the activity from 4 U ml^–1 to 8 ml^–1.     

Continuous culture of Humicola lutea 120-5 for acid proteinase production

Acid proteinase production by the fungus Humicola lutea 120-5 in continuous culture was studied. The maximum activity of the culture broth reached 2200 U/ml at a dilution rate (D) of 0.05/h. The continuous process was carried out for 1 month without any bacterial contamination, due to low pH (3.0–3.5) during the cultivation.     

The isolation and characterisation of a salicylate-hydroxylase-producing strain of Pseudomonas putida

Summary A salicylate-hydroxylase-producing strain of Pseudomonas putida with an unusual capability to grow at toxic levels of salicylate up to 10 g l^–1 has been isolated. It grew well under continuous culture conditions, with optimum growth at pH 6.5 and a temperature of 25° C. The use of an ammonium salt as a nitrogen source, instead of nitrate, resulted in a 30–40% increase in its biomass yield coefficient. Optimum growth under continuous culture conditions was achieved using 4 g l^–1 salicylate at 25° C, pH 6.5 and 0.2 h^–1 dilution rate. High salicylate hydroxylase enzyme activity [236 units (U) l^–1] and productivity (424.8 U h^–1) were obtained at a dilution rate of 0.45 h^–1 using a mineral medium containing 4 g l^–1 of salicylate. Operating under continuous culture conditions with oxygen limitation and a slight accumulation of residual salicylate (0.2 g l^–1) resulted in a decrease in culture performance and enzyme productivity. Correspondence to: R. Marchant     

Mass cultivation of the nitrogen-fixing cyanobacteriumGloeotrichia natans,indigenous to rice-fields

Gloeotrichia natans, a nitrogen fixing cyanobacterium common in rice fields in the Philippines, was used for studies to establish key features of its physiology and potential production in outdoor cultures. Under optimal growth conditions (38 °C, pH 8.0, no carbon enrichment) the specific growth rate of rice-field isolate was 0.076 h^–1. The pH of the medium (between 6.5 and 9.0) did not influence the growth rate, but it did affect phycobiliprotein content, as reflected by a change in colour. At pH 7.0 the culture was green-brown, with phycobiliproteins constituting up to 10% of the total protein, while at pH 9.0 the culture was brownish-black and the pigment content was as high as 28% of the total protein. In outdoor cultures the specific growth rate was related directly to cell density in the range of 0.7–1.5 g dry weight 1^–1 at a rate of stirring of 30 rpm, and inversely related to cell density at half this rate. At a stirring of 30 rpm, daily production of outdoor cultures harvested to maintain cell densities of 0.7, 1.15 andw 1.5 g 1^–1 were 14.7, 17.1 and 18.1 g m^–2 d^t, respectively. This rate of production was maintained for more than 45 days. Phycobiliprotein content in the culture kept at a density of 1.5 g 1^–1 reached 14% of the total biomass.     

Metabolic and kinetic studies of hybridomas in exponentially fed-batch cultures using T-flasks

Exponentially fed-batch cultures (EFBC) of a murine hybridoma in T-flasks were explored as a simple alternative experimental tool to chemostats for the study of metabolism, growth and monoclonal antibody (MAb) production kinetics. EFBC were operated in the variable volume mode using an exponentially increasing and predetermined stepwise feeding profile of fresh complete medium. The dynamic and steady-state behaviors of the EFBC coincided with those reported for chemostats at dilution rates below the maximum growth rate. In particular, steady-state for growth rate and concentration of viable cells, glucose, and lactate was attained at different dilution rates between 0.005 and 0.05 h^–1. For such a range, the glucose and lactate metabolic quotients and the steady-state glucose concentration increased, whereas total MAb, volumetric, and specific MAb production rates decreased 65-, 6-, and 3-fold, respectively, with increasing dilution rates. The lactate from glucose yield remained relatively constant for dilution rates up to 0.03 h^–1, where it started to decrease. In contrast, viability remained above 80% at high dilution rates but rapidly decreased at dilution rates below 0.02 h^–1. No true washout occurred during operation above the maximum growth, as concluded from the constant viable cell number. However, growth rate decreased to as low as 0.01 h^–1, suggesting the requirement of a minimum cell density, and concomitant autocrine growth factors, for growth. Chemostat operation drawbacks were avoided by EFBC in T-flasks. Namely, simple and stable operation was obtained at dilution rates ranging from very low to above the maximum growth rate. Furthermore, simultaneous operation of multiple experiments in reduced size was possible, minimizing start-up time, media and equipment costs.Abbreviations EFBC exponentially-fed batch culture - CSC continuous suspended culture - MAb monoclonal antibody - D dilution rate - q _i metabolic quotient or specific rate of consumption or production of i     

The use of extraction methods for the quantification of extracellular polymer production byKlebsiella aerogenes under varying cultural conditions

Summary A combination of ultrasonication at 18 W for 10 min and centrifugation at 33,000 g for 60 min was found to achieve the highest recovery of extracellular polymer fromKlebsiella aerogenes, NCTC 8172, allowing both soluble and colloidal phases to be separated. Estimates of the total polymer present, made by gravimetry and by acid hydrolysis, indicated that polymer production was greater in continuous culture than in batch culture, and increased in continuous culture as the dilution rate decreased from 0.5 h^–1 to 0.01 h^–1. Extraction of polymer from these cultures varied in efficiency; up to 73% of the total polymer was extracted at low dilution rates where the colloidal form of polymer was predominant, but only 22% was extracted at high dilution rates where the majority of the polymer was in the soluble phase. Consequently, this extraction method was considered to be unsuitable as a quantitative measure of polymer production.     

Two-stage continuous fermentation of Clostridium acetobutylicum: effects of pH and dilution rate

Summary The kinetics of a two-stage continuous fermentation of Clostridium acetobutylicum have been studied. The pH and the dilution rate have been shown to be two essential factors for process optimization. An increase in pH or dilution rate in the first stage decreased solvent production in the second fermentor. To achieve optimal solvent production, the pH had to be maintained at 4.5 in the first stage and between 4.5 and 5.0 in the second stage. Dilution rates of 0.08 h^–1 and 0.04 h^–1,respectively, in the first and second fermentors allowed a high solvent concentration. When the pH was maintained at 4.5 in each stage and when the dilution rates were 0.08 h^–1 and 0.04 h^–1 in the first and second fermentors respectively, 21 g/l solvent concentration was achieved. A conversion yield of 0.36 g solvents/g glucose consumed was obtained with total consumption of glucose. Biomass was only produced in the first stage together with 40% of the solvents, indicating that solvent production had to be induced in the first fermentor. Offprint requests to: J. M. Engasser     

Chondrus crispus (Gigartinaceae,Rhodophyta) tank cultivation: optimizing carbon input by a fixed pH and use of a salt water well

The injection of exogenous carbon into intensively cultivated algal tanks is necessary to insure a maximum growth rate by stabilizing the dissolved inorganic carbon (DIC) pool, but represents the major part of the cultivation cost (ca. 73%). This study was conducted in paddle-wheel tanks ranging in size from 260 m² to 1000 m². Additional carbon was provided by carbon dioxide mixed into the incoming sea water through a tubular reactor. Production vs pH was analysed on 120 growth measurements covering two years of continuous cultivation. Whereas production peaked at pH 8.0–8.2, the economic optimum for pH regulation was in the range 8.4–8.5, where CO₂ injection was greatly reduced (–29%) for only a slight decrease in production (–4%). Expressed as a function of pH level, the specific carbon injection (g c gdw^–1 of Chondrus produced) showed an inverse exponential relationship, whereas gross photoconversion ratio (gdw mol photons^–1) varied according to a second degree equation with a low amplitude. The photoconversion ratio was not improved when the culture was maintained at a DIC concentration higher than the natural equilibrium (0.64 ± 0.11 gdw mol photons^–1 at 2.35 mM and 0.65 ± 0.15 gdw mol photons^–1 at 3.19 MM).A complementary source of carbon was found in underground salt water with a high and stable DIC concentration (10.15 ± 0.25 mmole Cl^–1). The mixing of the well water with natural sea water allowed another economy of CO₂ (–20% at pH 8.5) and nutrients (–12%), the total unitary cost of production being cut by about 17%.     

Development of a Pseudomonas sp. for aerobic chromate reduction

Summary Shake flask cultures using a chromate resistant isolate identified as Pseudomonas sp. in defined medium containing 60 mg Cr(VI)/1 gave maximum chromate reduction of 87% at 40°C and pH 9 in 72 h with urea as nitrogen source. Continuous culture at 30 C, pH 7.2–7.6 and dilution rate of 0.014/h in a 2-1 chemostat with the same isolate showed 81% chromate reduction with feed containing 124 mg Cr(VI)/1.     

Conversion of fat into yeast biomass in protein-containing waste-water

Summary Candida tropicalis S001 was grown on the lipid fraction of a protein-containing waste-water in order to (i) remove fat from the water, and (ii) produre yeast biomass for feed. The yeast cells were separated from the waste-water by sedimentation. Defatted waste-water was used for methane production and gave a yield of a 0.3 m³ methane/kg reduced chemical oxygen demand. The maximum specific growth rate (µ_max) of C. tropicalis growing on waste-water fat at pH 4.0 was 0.35 h^–1; the fat content was decreased from 8 g/l to about 0.1 g/l within 24 h. In continous culture a corresponding reduction was maintained at dilution rates up to 0.36 h^–1. The effect on growth of pH, temperature and CO₂ concentration was studied with triolein as the major carbon source. The µ_max was nearly constant (0.16 h^–1) in the pH and temperature range of 3.2–4.0 and 30°–38° C, respectively; 10% CO₂ was optimal for growth. Growth on triolein resulted in a biomass yield of 0.70 g dry weight/g fat. Offprint requests to: S. Rydin     

Productivity analysis of outdoor chemostat culture in tubular air-lift photobioreactors

Net productivity and biomass night losses in outdoor chemostat cultures ofPhaeodactylum tricornutum were analyzed in two tubular airlift photobioreactors at different dilution rates, photobioreactor surface/volume ratios and incident solar irradiance. In addition, an approximate model for the estimation of light profile and average irradiance inside outdoor tubular photobioreactors was proposed. In both photobioreactors, biomass productivity increased with dilution rate and daily incident solar radiation except at the highest incident solar irradiances and dilution rates, when photoinhibition effect was observed in the middle of the day. Variation of estimated average irradiance vs mean incident irradiance showed two effects: first, the outdoor cultures are adapted to average irradiance, and second, simultaneous photolimitation and photoinhibition took place at all assayed culture conditions, the extent of this phenomena being a function of the (incident)¹ irradiance and light regime inside the culture. Productivity ranged between 0.50 and 2.04 g L^–1 d^–1 in the tubular photobioreactor with the lower surface/volume ratio (S/V = 77.5 m^–1) and between 1.08 and 2.76 g L^–1 d^–1 in the other (S/V = 122.0 m^–1). The optimum dilution rate was 0.040 h^–1 in both reactors. Night-time biomass losses were a function of the average irradiance inside the culture, being lower in TPB0.03 than TPB0.06, due to a better light regime in the first. In both photobioreactors, biomass night losses strongly decreased when the photoinhibition effect was pronounced. However, net biomass productivity also decreased due to lower biomass generation during the day. Thus, optimum culture conditions were obtained when photolimitation and photoinhibition were balanced.     

Factors affecting lysine degradation by ruminal fusobacteria

Fusobacterium necrophorum can readily be enriched from the rumen with lysine, and its deamination rate is very rapid. The addition of F. necrophorum JB2 to mixed ruminal bacteria significantly increased lysine degradation, but only if the ratio of ruminal fluid to basal medium was less than 25%. If more ruminal fluid (pH 6.1) was added, ammonia production decreased by as much as 80%. Clarified, autoclaved ruminal fluid was also inhibitory. When F. necrophorum JB2 was grown in a lysine-limited continuous culture (0.1 h(-1) dilution rate) and pH was decreased using HCl, optical density decreased linearly, and the culture washed out at pH 5.6. Batch cultures of F. necrophorum JB2 deaminated as much lysine at pH 6.1 as at pH 6.6, but only if fermentation acids were not present. Sodium acetate (100 mM) had little effect at pH 6.6, but the same concentration inhibited ammonia production by 80% at pH 6.1. The idea that fermentation acids could prevent the enrichment of fusobacteria in vivo was supported by the observation that dietary lysine supplementation did not enhance the lysine deamination rate of the mixed ruminal bacteria.     

Optimization of lipid production in the oleaginous yeastApiotrichum curvatum in wheypermeate

Summary Lipid production of the oleaginous yeastApiotrichum curvatum was studied in wheypermeate to determine optimum operation conditions in this medium. Studies on the influence of the carbon to nitrogen ratio (C/N-ratio) of the growth medium on lipid production in continuous cultures demonstrated that cellular lipid content in wheypermeate remained constant at 22% of the cell dry weight up to a C/N-ratio of about 25. The maximal dilution rate at which all lactose is consumed in wheypermeate with excess nitrogen was found to be 0.073 h^-1. At C/N-ratios higher than 25–30 lipid content gradually increased to nearly 50% at C/N=70 and the maximal obtainable dilution rate decreased to 0.02 h^-1 at C/N=70. From these studies it could be derived that maximal lipid production rates can be obtained at C/N-ratios of 30–35 in wheypermeate. Since the C/N-ratio of wheypermeate normally has a value between 70 and 101, some additional nitrogen is required to optimize the lipid production rate. Lipid production rates ofA. curvatum in wheypermeate were compared in four different culture modes: batch, fed-batch, continuous and partial recycling cultures. Highest lipid production rates were achieved in culture modes with high cell densities. A lipid production rate of nearly 1 g/l/h was reached in a partial recycling culture. It was calculated that by using this cultivation technique lipid production rates of even 2.9 g/l/h may be reached when the supply of oxygen can be optimized.Nomenclature C/N-ratio carbon to nitrogen ratio of the growth medium (g/g) - C/N_crit C/N-ratio at which there is just enough nitrogen to allow all carbon source to be converted to biomass - D dilution rate=volume of incoming medium per unit time/volume of medium in the culture vessel (h^-1) - D_max maximum dilution rate (h^-1) - DW cell dry weight - L lipid yield (g storage lipid/g carbon source) - specific growth rate (h^-1) - _max maximum specific growth rate (h^-1) - Q_L lipid production rate (g/l/h) - Y_i molecular fraction of carbon substrate that is converted to storage carbohydrate (C-mol/C-mol) - Y_ls maximal amount of storage lipid that can be produced per mol carbon source (C-mol/C-mol)     

Production of laccase byBotrytis cinerea and fermentation studies with strain F226

After induction, seven strains ofBotrytis cinerea released into the culture broth considerable amounts of laccase in a brief production time. The set-up of a suitable production process was studied with a selected strain in a 10-L fermenter. The optimum fermentation conditions were a 3% inoculum with a high degree of sporulation, a simple medium containing 20 g L^–1 of glucose and 2 g L^–1 of yeast extract at pH 3.5, 2 g L^–1 gallic acid as inducer, added after 2 days of growth, an agitation speed of 300 rpm, an aeration rate of 1.2 vvm and a temperature of 24°C. By optimizing the culture conditions, the enzyme activity reached 28 U ml^–1 in 5 days with a specific activity of 560 U mg^–1 protein. The best procedure to obtain a suitable crude enzyme preparation was concentration of the supernatant medium to 10% of the initial volume by ultrafiltration, followed by a fractional precipitation with ethanol. The optimum pH and temperature for laccase activity were 5.5 and 40°C, respectively, with syringaldazine as the substrate.