Oxalic acid production by Aspergillus niger

Oxalic acid is formed by Aspergillus niger at nearly neutral pH values. In this study the applicability of milk whey as a carbon source was investigated, both in shaking flask experiments and in a stirred tank reactor. The influence of pH on oxalic acid formation showed that the maximum production rate and higher concentration of the product are observed at pH 6. At pH 7 the same production rate was obtained although at a lower oxalic acid concentration. The process was shown to be inhibited by product from an oxalic acid concentration of about 10?kg/m³ and its behaviour was fitted by Luong's equation. In a 10-dm³ strirred tank ferment the stirrer speed was varied in a range from 100 to 600 rpm. At values between 200 and 400 rpm, maximum production rates of oxalic acid of 6.8?kg/m³·d and 6.5?kg/m³·d were reached, respec-tively. A final concentration of 41.4?kg oxalic acid/m³ was reached operating at 400 rpm.     

Optimization of medium constituents and fermentation conditions for the production of L-Glutamic acid by the coimmobilized whole cells of Micrococcus glutamicus and Pseudomonas reptilivora

Statistical experimental design was used to optimize medium constituents and the conditions of fermentation, viz., temperature, pH?and the time of fermentation. Higher yields of L-glutamic acid (37.1?kg/m³) was obtained after optimizing medium components and the conditions of fermentation. The optimal levels of medium components were: 61.5575?kg/m³ glucose, 7.3272?kg/m³ urea and 1.783?μg/dm³ biotin. The optimum productivity was achieved using optimized medium at the fermentation temperature of 33.7?°C, initial pH?7.74, and at the time of fermentation of 58.4?h.     

Comparison of startup and anaerobic wastewater treatment in UASB, hybrid and baffled reactor

An experimental study was carried out to compare the performance of selected anaerobic high rate reactors operated simultaneously at 37?°C. The three reactors, namely upflow anaerobic sludge bed reactor (UASB), hybrid of UASB reactor and anaerobic filter (anaerobic hybrid reactor – AHR) and anaerobic baffled reactor (ABR), were inoculated with the anaerobic digested sludge from municipal wastewater treatment plant and tested with synthetic wastewater. This wastewater contained sodium acetate and glucose with balanced nutrients and trace elements (COD 6000?mg?·?l^?1). Organic loading rate (B _v ) was increased gradually from an initial 0.5?kg?·?m^?3?·?d^?1 to 15?kg?·?m^?3?·?d^?1 in all the reactors. From the comparison of the reactors' performance, the lowest biomass wash-out resulted from ABR. In the UASB, significant biomass wash-out was observed at the B _v 6?kg?·?m^?3?·?d^?1, and in the AHR at the B _v 12?kg?·?m^?3?·?d^?1. The demand of sodium bicarbonate for pH maintenance in ABR was two times higher as for UASB and AHR. The efficiency of COD removal was comparable for all three reactors – 80–90%. A faster biomass granulation was observed in the ABR than in the other two reactors. This fact is explained by the kinetic selection of filamentous bacteria of the Methanotrix sp. under a high (over 1.5?g?·?l^?1) acetate concentration.     

Design of acidogenic reactors for the anaerobic treatment of the organic fraction of solid food waste

Volatile Fatty Acids (VFA) production by anaerobic fermentation of organic solid wastes was studied at laboratory scale. The influence of initial substrate concentration was evaluated on VFA production. Completely mixed reactors (0.9?l) were used at mesophilic temperature (35?°C). Food wastes had 43.8% Total Solids content. Three dilutions of substrate (1/25, 1/10 and 1/5) corresponding to 1.75%, 4.38% and 8.76% of Total Solids and five values of Organic Loading Rates: 2, 5, 10, 12.5 and 25?kg COD/m³?d were studied. It was found that substrate 1/10 led to 14?g VFA/l at a loading rate of 12.5?kg COD/m³?d and an hydraulic retention time of 3.7 d. The main VFA produced were especially acetate and butyrate. Substrate diluted 1/5 led to 26.1?g VFA/l at a loading of 5?kg COD/m³?d and an hydraulic retention time of 15.1 d, but biomass production was not optimal. In a second study, a cascade of three reactors was used. An effluent with 42?g VFA/l was obtained at steady-state conditions at a loading of 12.5?kg of COD/m³?d and an hydraulic retention time of 12.5?d. The distribution of VFA was the following: 36% of propionate, 34% of acetate and 22.5% of butyrate.     

Influence of milk whey, nitrogen and phosphorus concentration on oxalic acid production by Aspergillus niger

A factorial design at two levels was used to determine the effect of milk whey concentration and the addition of nitrogen (as NH₄NO₃) and phosphorus (as KH₂PO₄) on the oxalic acid production by Aspergillus niger. The results of the experiments indicated that milk whey contains enough nutrients for fungus growth, therefore medium supplementing with N and P is not necessary. The optimum milk whey concentration was 100 kg/m³ reaching a final oxalic acid concentration of 37 kg/m³ and a maximum production rate of 3.4 kg/m³ · d. The yield of oxalic acid was 0.4, a very high value compared to previous works.     

Evaluation of different expression systems for the heterologous expression of pyranose 2-oxidase from <Emphasis Type="Italic">Trametes multicolor</Emphasis> in <Emphasis Type="Italic">E. coli</Emphasis>

The heterologous production of the industrially relevant fungal enzyme pyranose 2-oxidase in the prokaryotic host E. coli was investigated using 3 different expression systems, i.e. the well-studied T7 RNA polymerase based pET21d⁺, the L-arabinose inducible pBAD and the pCOLD system. Preliminary experiments were done in shaking flasks at 25°C and optimized induction conditions to compare the productivity levels of the different expression systems. The pET21d⁺ and the pCOLD system gave 29 U/L·h and 14 U/L·h of active pyranose 2-oxidase, respectively, whereas the pBAD system only produced 6 U/L·h. Process conditions for batch fermentations were optimized for the pET21d⁺ and the pCOLD systems in order to reduce the formation of inactive inclusion bodies. The highest productivity rate with the pET21d⁺ expression system in batch fermentations was determined at 25°C with 32 U/L·h. The pCOLD system showed the highest productivity rate (19 U/L·h) at 25°C and induction from the start of the cultivation. Using the pCOLD system in a fed batch fermentation at 25°C with a specific growth rate of μ = 0.15 h^-1resulted in the highest productivity rate of active pyranose oxidase with 206 U/L·h.     

The effect of cultivation conditions on the penicillin production using a urethane foam-supported Penicillium chrysogenum

Urethane foam was applied to immobilize the fungus Penicillium chrysogenum in order to accelerate penicillin fermentation. Various operational conditions, such as cultivation temperature, initial pH value, composition of substrate and inoculum size of spores, which might influence penicillin fermentation significantly, were studied in a shaking flask culture system. The results are summarized as follows:

1. The maximum production amount of penicillin was achieved when cultivation temperature and initial pH were kept at 25±1°C and 4, respectively.
2. The maximum production yield of penicillin for substrate was obtainable when the concentration of lactose and that of cornsteep liquor in the basal medium were adjusted at 60 kg/m³ and 30 kg/m³, respectively.
3. It was found in this cultivation system that the optimum region concerning inoculum size was enlarged from 7.0·10⁵ to 1.0·10⁷ spores/dm³ while that of the traditional mehtod was very narrow around 1.0·10⁷ spores/dm³. Moreover, the production amount of penicillin produced by this new method was about twelve times as high as that produced by the traditional method.

     

Diacetyl fermentation coupled with pervaporation using oleyl alcohol supported liquid membrane

Pervaporation using oleyl alcohol supported liquid membrane was successfully applied to diacetyl fermentation by immobilized lactic acid bacteria. Diacetyl productivity was about 10 g·m⁻³·h⁻¹, while productivity during batch fermentation was about 6 g·m⁻³·h⁻¹. Diacetyl yield from consumed glucose was about 0.04 g·g⁻¹ which was 4 times as large as that of batch fermentation. The pervaporation functioned favorably on actual fermentation broth. The flux of the permeate and the diacetyl separation factor for the pervaporation were about 9 g·m⁻²·h⁻¹ and 36, respectively, and these values were maintained at almost constant levels during fermentation. Diacetyl concentration in the permeate was about 2 kg·m⁻³, which is sufficiently high for commercial use.     

Productivity of theEcklonia cava community in a bay of Izu Peninsula on the Pacific Coast of Japan

Net production of theEcklonia cava community was monitored on a monthly basis for a year, and annual net production was estimated. Growth rate of blades reached a maximum of about 13 g dry wt·m^?2·day^?1 in spring and a minimum of about 2 g dry wt·m^?2·day^?1 in late summer. Annual production of blades was calculated to be 2.84 kg dry wt·m^?2·year^?1. If the growth of stipes is taken into account, annual net production is estimated to be about 2.9 kg dry wt·m^?2·year^?1. Standing crop was monitored monthly for two and a half years, and a close negative correlation was found between seasonal change in standing crop and net production. Standing crop reached a maximum of about 3 kg dry wt·m^?2 in summer and a minimum of about 1 kg dry wt·m^?2 in winter. Low productivity in summer at a period of maximum biomass may be explained by the dense canopy and the large area of reproductive portion occupying a blade, which diminish net assimilation.     

Ammonium ion & citric acid supplementation in batch cultures ofAspergillus niger B 60

Summary The effect of a single pulse of ammonium sulphate or of citrate upon the progress and final outcome of a batch citric acid fermentation was studied. It was found that the optimum addition time for the supplemental N was in the range of 40 to 75 h. Final citric acid concentration achieved was significantly increased when the concentration of N source added was between 0.25 and 0.5 kg m^–3. The mechanism of the observed stimulation seemed to be an indirect one. Addition of exogenous citric acid to the broth, led to an increase in citrate production by the culture. The optimum time for citric acid addition was around 90 h.Nomenclature Y_p/s Yield of citric acid produced (kg) on sucrose consumed (kg) - P/t Overall citric acid productivity (kg m^–3 h^–1)     

Kinetics of ethanol production by baker's yeast in an integrated process of fermentation and microfiltration

The productivity of a fermentation is proportional to the biomass concentration. The productivity can therefore be increased by retention of the cells in the fermentor. In this study microfiltration was used for cell retention in a fermentation of glucose to ethanol by baker's yeast. Compared to a system without cell retention the productivity could be increased 12-fold to 55 kg/m³ h at a biomass concentration of 135 kg/m³. Maximal ethanol concentrations of 76 kg/m³ were obtained at conditions of growth. At zero growth conditions in the integrated system the ethanol concentration could be increased to about 115 kg/m³, and could be produced for at least 10 hours. The fermentation results in the integrated system could be described reasonably well with a mathematical model based on a different linear inhibition kinetics for growth and substrate consumption.     

Use of the upflow sludge blanket (USB) reactor concept for biological wastewater treatment,especially for anaerobic treatment

In recent years considerable effort has been made in the Netherlands toward the development of a more sophisticated anaerobic treatment process, suitable for treating low a strength wastes and for applications at liquid detention times of 3–4 hr. The efforts have resulted in new type of upflow anaerobic sludge blanket (UASB) process, which in recent 6 m³ pilot-plant experiments has shown to be capable of handling organic space loads of 15–40 kg chemical oxygen demand (COD)·m^?3/day at 3–8 hr liquid detention times. In the first 200 m³ full-scale plant of the UASB concept, organic space loadings of up to 16 kg COD·m^?3/day could be treated satisfactorily at a detention times of 4 hr, using sugar beet waste as feed. The main results obtained with the process in the laboratory as well as in 6 m³ pilot plant and 200 m³ full-scale experiments are presented and evaluated in this paper. Special attention is given to the main operating characteristics of the UASB reactor concept. Moreover, some preliminary results are presented of laboratory experiments concerning the use of the USB reactor concept for denitrification as well as for the acid formation step in anaerobic treatment. For both purposes the process looks feasible because very satisfactory results with respect to denitrification and acid formation can be achieved at very high hydraulic loads (12 day^?1) and high organic loading rates, i.e., 20 kg COD·m^?3/day in the denitrification and 60–80 kg COD·m^?3/day in the acid formation experiments.     

Effects of ethanol concentration on immobilized Zymomonas mobilis for continuous production of ethanol

The effects of ethanol concentration on the ethanol productivity and activity of immobilized Zymomonas mobilis cells during continuous fermentation of glucose has been studied at various ethanol concentrations. On changing the inlet ethanol concentration, Po, from 0.0 kg/m³ to any other level, 8 h were required to fully experience the effects of a change in Po, whereas 8 h to 2 days, depending on Po, were required to reach the steady state on switching back to the ethanol free medium. The volumetric ethanol productivity decreased from 92.5 to 0.0 kg/m³·h as the ethanol concentration in the bioreactor was changed from 46.3 to 126 kg/m³. The activity of the immobilized cells recovered up to 63% in 2 days even after exposing the cells to 126 kg/m³ of ethanol.     

Productivity and calcification on a coral reef: A survey using pH and oxygen electrode techniques

An instrument package carrying pH and oxygen electrodes and a thermistor was floated across a reef flat at different times of the day and night. The data collected were used to obtain profiles of primary production, respiration, and calcification or solution of reef rock across the transect area. Average rates for these processes across the transect area, and rates at particular points along the transect, were related to light intensity and light response curves were constructed for productivity and calcification. Productivity tended to saturate at high light intensities and the amplitude and shape of the response curve changed with distance from the reef crest. Calcification showed no such saturation. Rates of calcification, and the dependence of calcification on light intensity, increased with distance from the reef crest. Average reef flat gross productivity and net calcification, based on the light response curves were 8.8 g C · m ^?2 · day^?1 and 9.4 g CaCO₃ · m^?2 · day^?1 (3.5 kg · m^?2· yr^?1), and the production: consumption ratio was 1.16:1. These results were obtained in late summer, and are for a cloudless day. The results suggest that the degree of stability in the reef surface, and the amount of disturbance experienced by different reef flat communities, probably exert major controls on reef flat community metabolism.     

Enhanced solid‐state citric acid bio‐production using apple pomace waste through surface response methodology

Aims: To evaluate the potential of apple pomace (AP) supplemented with rice husk for hyper citric acid production through solid‐state fermentation by Aspergillus niger NRRL‐567. Optimization of two key parameters, such as moisture content and inducer (ethanol and methanol) concentration was carried out by response surface methodology. Methods and Results: In this study, the effect of two crucial process parameters for solid‐state citric acid fermentation by A. niger using AP waste supplemented with rice husk were thoroughly investigated in Erlenmeyer flasks through response surface methodology. Moisture and methanol had significant positive effect on citric acid production by A. niger grown on AP (P < 0·05). Higher values of citric acid on AP by A. niger (342·41 g kg^?1 and 248·42 g kg^?1 dry substrate) were obtained with 75% (v/w) moisture along with two inducers [3% (v/w) methanol and 3% (v/w) ethanol] with fermentation efficiency of 93·90% and 66·42%, respectively depending upon the total carbon utilized after 144 h of incubation period. With the same optimized parameters, conventional tray fermentation was conducted. The citric acid concentration of 187·96 g kg^?1 dry substrate with 3% (v/w) ethanol and 303·34 g kg^?1 dry substrate with 3% (v/w) methanol were achieved representing fermentation efficiency of 50·80% and 82·89% in tray fermentation depending upon carbon utilization after 120 h of incubation period. Conclusions: Apple pomace proved to be the promising substrate for the hyper production of citric acid through solid‐state tray fermentation, which is an economical technique and does not require any sophisticated instrumentation. Significance and Impact of the Study: The study established that the utilization of agro‐industrial wastes have positive repercussions on the economy and will help to meet the increasing demands of citric acid and moreover will help to alleviate the environmental problems resulting from the disposal of agro‐industrial wastes.     

Poly(β-hydroxybutyric acid) thermoplastic production by Alcaligenes latus: Behavior of fed-batch cultures

Fed-batch culture of Alcaligenes latus, ATCC 29713, was investigated for producing the intracellular bioplastic poly(β–hydroxybutyric acid), PHB. Constant rate feeding, exponentially increasing feeding rate, and pH-stat fed batch methods were evaluated. pH-stat fed batch culture reduced or delayed accumulation of the substrate in the broth and led to significantly enhanced PHB productivity relative to the other modes of feeding. Presence of excessive substrate appeared to inhibit PHB synthesis, but not the production of cells. In fed-batch culture, the maximum specific growth rate (0.265?h^?1) greatly exceeded the value (0.075?h^?1) previously observed in batch culture of the same strain. Similarly, the maximum PHB production rate (up to 1.15?g?·?l^?1?·?h^?1) was nearly 8-fold greater than values observed in batch operations. Fed-batch operation was clearly superior to batch fermentation for producing PHB. A low growth rate was not a prerequisite for PHB accumulation, but a reduced or delayed accumulation of substrate appeared to enhance PHB accumulation. Under the best conditions, PHB constituted up to 63% of dry cell mass after 12?h of culture. The average biomass yield coefficient on sucrose was about 0.35, or a little less than in batch fermentations. The highest PHB concentrations attained were about 18?g?·?l^?1.     

Propionic acid fermentation: improvement of performances by coupling continuous fermentation and ultrafiltration

The present paper presents a study of propionic acid production from whey by using Propionibacterium acidipropionici in batch and continuous fermentation with cell recycle. The experimental investigation is carried through with a biomass concentration (DW) of 112kg/m³. The highest propionic acid productivity is 2.14 kg/(m³ h). Biomass concentration is 9 times as high, propionic acid productivity 6 times as high as compared to batch results.     

Optimization of medium composition by response surface methodology for the production of tartaric acid by Gluconobacter suboxydans

The combined effect of sorbitol and yeast extract of the medium on tartaric acid production by Gluconobacter suboxydans, NCIM 2049, was studied in batch fermentation while keeping the temperature (30?°C) and pH (6.2) constant. Response surface methodology was used to obtain quadratic models for the production of tartaric acid. The multiple coefficients of regression between 0.8945 and 0.9820 was obtained during the process. The optimum medium composition comprising 20?kg/m³ sorbitol and 2?kg/m³ yeast extract was verified experimentally by observing the variation of cell mass and tartaric acid production with time.     

Hydroxyethylation of Comenic Acid

A small jar fermentor was developed in order to investigate the effect of oxygen supply on hydrocarbon fermentation. Several indices to oxygen transfer were examined with this small jar fermentor. Conditions for suitable oxygen supply were examined in l-glutamic acid fermentation from hydrocarbon by use of shaking flasks and these small jar fermentors. The data indicated that the rate of oxygen transfer ought to be more than 14.3 × 10^?7 mole/ml·min in order to obtain satisfactory results. The coefficient of oxygen transfer rate (K_La/H) decreased as the fermentation went on, so the supply of oxygen enriched gas mixture was effective to increase the production of l-glutamic acid.     

Analysis of copper corrosion in compacted bentonite clay as a function of clay density and growth conditions for sulfate‐reducing bacteria

Aims: To investigate the relationships between sulfate‐reducing bacteria (SRB), growth conditions, bentonite densities and copper sulfide generation under circumstances relevant to underground, high‐level radioactive waste repositories. Methods and Results: Experiments took place 450 m underground, connected under in situ pressure to groundwater containing SRB. The microbial reduction of sulfate to sulfide and subsequent corrosion of copper test plates buried in compacted bentonite were analysed using radioactive sulfur (³⁵SO₄^2?) as tracer. Mass distribution of copper sulfide on the plates indicated a diffusive process. The relationship between average diffusion coefficients (D_s) and tested density (ρ) was linear. D_s (m² s^?1) = ?0·004 × ρ (kg m^?3) + 8·2, decreasing by 0·2 D_s units per 50 kg m^?3 increase in density, from 1·2 × 10^?11 m² s^?1 at 1750 kg m^?3 to 0·2 × 10^?11 m² s^?1 at 2000 kg m^?3. Conclusions: It is possible that sulfide corrosion of waste canisters in future radioactive waste repositories depends mainly on sulfide concentration at the boundary between groundwater and the buffer, which in turn depends on SRB growth conditions (e.g., sulfate accessibility, carbon availability and electron donors) and geochemical parameters (e.g., presence of ferrous iron, which immobilizes sulfide). Maintaining high bentonite density is also important in mitigating canister corrosion. Significance and Impact of the Study: The sulfide diffusion coefficients can be used in safety calculations regarding waste canister corrosion. The work supports findings that microbial activity in compacted bentonite will be restricted. The study emphasizes the importance of growth conditions for sulfate reduction at the groundwater boundary of the bentonite buffer and linked sulfide production.