Photoheterotrophic growth of purple non-sulfur bacteria on Tris Acetate Phosphate Yeast extract (TAPY) medium and its hydrogen productivity in light under nitrogen deprivation

In this study, an active photoheterotrophic growth of purple non-sulfur bacteria (PNSB) on Tris Acetate Phosphate Yeast extract (TAPY) medium is reported. TAPY medium is a modified TAP medium supplemented with filter sterilized yeast extract (0.3 g L⁻¹) and vitamin B12. Heterotrophic growth of PNSB on nitrogen replete TAPY medium in dark could be obtained but much slower than that in light where cells could grow but without formation of pigments. The medium showed high potency for hydrogen production under nitrogen deprivation in light by Rhodobacter sphaeroides DSM 5864. Through using TAPY medium, 1 mole of acetate provided as glacial acetic acid produced 0.819 mole of hydrogen gas by R. sphaeroides on nitrogen deprived TAPY medium (initial pH 7 adjusted by HCl) with a maximum H₂ production rate of (0.669 mmol H₂ h⁻¹ L⁻¹) obtained at 42 h after start of fermentation. Repeated-batch hydrogen production could be achieved with high efficiency for three cycles by supplementing the nitrogen deprived culture with filter sterilized sodium acetate at the end of the log hydrogen production phase of each cycle. The medium was also applicable for photoheterotrophic growth in light and heterotrophic growth in dark of other PNSB namely Rhodobacter capsulatus JCM-21090 and Rhodospirillum rubrum DSM 467. Although R. rubrum could actively grow on TAPY medium under nitrogen deprivation in light, it was the lowest in hydrogen production compared to R. sphaeroides and R. capsulatus. The active growth of R. rubrum on nitrogen deprived TAPY medium suggests its possible use for producing biodegradable plastic polymers better than hydrogen. The results suggest that it's possible to use TAPY medium for growth and producing variable bioproducts by PNSB in future studies and applications. The repeated-batch hydrogen production by R. sphaeroides on nitrogen deprived TAPY medium is promising for large-scale applications of hydrogen production industry by only sequential supply with sodium acetate to the culture for three rounds of batch fermentation. This is the first report in using TAPY medium for growth and hydrogen production by PNSB.     

Modelling of hydrogen production in batch cultures of the photosynthetic bacterium Rhodobacter capsulatus

The photosynthetic bacterium, Rhodobacter capsulatus, produces hydrogen under nitrogen-limited, anaerobic, photosynthetic culture conditions, using various carbon substrates. In the present study, the relationship between light intensity and hydrogen production has been modelled in order to predict both the rate of hydrogen production and the amount of hydrogen produced at a given time during batch cultures of R. capsulatus. The experimental data were obtained by investigating the effect of different light intensities (6000–50,000 lux) on hydrogen-producing cultures of R. capsulatus grown in a batch photobioreactor, using lactate as carbon and hydrogen source. The rate of hydrogen production increased with increasing light intensity in a manner that was described by a static Baly model, modified to include the square of the light intensity. In agreement with previous studies, the kinetics of substrate utilization and growth of R. capsulatus was represented by the classical Monod or Michaelis–Menten model. When combined with a dynamic Leudekong–Piret model, the amount of hydrogen produced as a function of time was effectively predicted. These results will be useful for the automatization and control of bioprocesses for the photoproduction of hydrogen.     

Kinetic analysis of photosynthetic growth,hydrogen production and dual substrate utilization by Rhodobacter capsulatus

Rhodobacter capsulatus is purple non-sulfur (PNS) bacterium which can produce hydrogen and CO₂ by utilizing volatile organic acids in presence of light under anaerobic conditions. Photofermentation by PNS bacteria is strongly affected by temperature and light intensity. In the present study we present the kinetic analysis of growth, hydrogen production, and dual consumption of acetic acid and lactic acid at different temperatures (20, 30 and 38 °C) and light intensities (1500, 2000, 3000, 4000 and 5000 lux). The cell growth data fitted well to the logistic model and the cumulative hydrogen production data fitted well to the Modified Gompertz Model. The model parameters were affected by temperature and light intensity. Lactic acid was found to be consumed by first order kinetics. Rate of consumption of acetic acid was zero order until most of the lactic acid was consumed, and then it shifted to first order. The results revealed that the optimum light intensities for maximum hydrogen production were 5000 lux for 20 °C and 3000 lux for 30 °C and 38 °C.     

Fermentative hydrogen production from acetate using Rhodobacter sphaeroides RV

The study of photosynthetic hydrogen production by using Rhodobacter sphaeroides RV from acetate was described. We investigated the effects of light source (fluorescent, halogen and tungsten lamps), light intensity (1200–6000 lux), inoculum quantity (OD₆₆₀ 0.212–OD₆₆₀ 1.082) and initial pH (4.0–10.0) on biohydrogen production. The results indicated that the hydrogen production for halogen and tungsten lamps was better than it for fluorescent lamp as light source. The best light intensity of hydrogen production was 3600 lux for tungsten lamp as light source. Inoculum quantity experiments indicated that the higher hydrogen production volume and hydrogen conversion rate were obtained at initial OD₆₆₀ of 0.931. The effect of initial pH on hydrogen production indicated that the maximum hydrogen yield reached to 653.2 mmol H₂/mol acetate at initial pH 7.0.     

Photofermentative hydrogen production using dark fermentation effluent of sugar beet thick juice in outdoor conditions

In the present study, photofermentative hydrogen production on thermophilic dark fermentation effluent (DFE) of sugar beet thick juice was investigated in a solar fed-batch panel photobioreactor (PBR) using Rhodobacter capsulatus YO3 (hup⁻) during summer 2009 in Ankara, Turkey. The DFE was obtained by continuous dark fermentation of sugar beet thick juice by extreme thermophile Caldicellulosiruptor saccharolyticus and it contains acetate (125 mM) and NH₄⁺ (7.7 mM) as the main carbon and nitrogen sources, respectively. The photofermentation process was done in a 4 L plexiglas panel PBR which was daily fed at a rate of 10% of the PBR volume. The DFE was diluted 3 times to adjust the acetate concentration to approximately 40 mM and supplemented with potassium phosphate buffer, Fe and Mo. In order to control the temperature, cooling was provided by recirculating chilled water through a tubing inside the reactor. Hydrogen productivity of 1.12 mmol/L_c/h and molar yield of 77% of theoretical maximum over consumed substrate were attained over 15 days of operation. The results indicated that Rb. capsulatus YO3 could effectively utilize the DFE of sugar beet thick juice for growth and hydrogen production, therefore facilitating the integration of the dark and photo-fermentation processes for sustainable biohydrogen production.     

“Effect of light intensity and the light: dark cycles on the long term hydrogen production of Chlamydomonas reinhardtii by batch cultures”

The photomixotrophic hydrogen production was investigated in sulfur deprived Chlamydomonas reinhardtii cultures. The cultures were exposed to continuous illumination of various light intensities in 27-day batches. Light intensity of 70 × 2 ??E m⁻² s⁻¹ was selected for hydrogen production. Subsequent experiments involving 27-day long light:dark cycles were conducted at the selected light intensity. The cycles consisted of hour divisions (h:h; 18:6, 14:10, 12:12) or minute divisions (min:min; 45:15, 35:25, 30:30). The results showed an adverse effect of the light:dark cycles on hydrogen production. All experiments, irrespective of the type of illumination indicated that cultures needed a lag phase for production and the highest hydrogen production was obtained during first 7-10 days of production reaching a peak in the first 5 days.     

Optimization of temperature and light intensity for improved photofermentative hydrogen production using Rhodobacter capsulatus DSM 1710

Photofermentative hydrogen production is influenced by several parameters, including feed composition, pH levels, temperature and light intensity. In this study, experimental results obtained from batch cultures of Rhodobacter capsulatus DSM 1710 were analyzed to locate the maximum levels for the rate and yield of hydrogen production with respect to temperature and light intensity. For this purpose, a 3^k general full factorial design was employed, using temperatures of 20, 30 and 38 °C and light intensities of 100, 200 and 340 W/m². ANOVA results confirmed that these two parameters significantly affect hydrogen production. Surface and contour plots of the regression models revealed a maximum hydrogen production rate of 0.566 mmol H₂/L/h at 27.5 °C and 287 W/m² and a maximum hydrogen yield of 0.326 mol H₂/mol substrate at 26.8 °C and 285 W/m². Validation experiments at the calculated optima supported these findings.     

Improved photo – Hydrogen production by transposon mutant of Rhodobacter capsulatus with reduced pigment

The light shielding effect of photosynthetic bacteria in photo fermentation process, which is caused by high content of pigment, hinders their hydrogen production rates under intense light irradiation. In order to mitigate this effect and improve hydrogen production efficiency, it is necessary to screen mutants that hold less pigment content. In this study, a mini-Tn5 transposon encoded plasmid pRL27 was employed for transposon mutagenesis of Rhodobacter capsulatus SB1003. A mutant named MC1417 showed significant lower light absorbance from 330 nm to 900 nm compared to its parental strain by UV–visible spectra, and its bacteriochlorophyll a content was reduced by 38%. The results showed that its photo fermentative hydrogen production was improved by 50.5% on the basis of BChl a content using acetate and butyrate as carbon source under intense light irradiation, indicating that it is effective on improving hydrogen production by repressing the pigment biosynthesis. DNA sequencing and BLAST in NCBI Genebank showed that the mutation occurred within its pucDE gene.     

Hydrogen production from glucose by co-culture of Clostridium Butyricum and immobilized Rhodopseudomonas faecalis RLD-53

In this work, the effects of different parameters on co-culture hydrogen production using Clostridium Butyricum and immobilized Rhodopseudomonas faecalis RLD-53 were investigated. The maximum hydrogen yield of 4.134 mol H₂/mol glucose was obtained using 6 g/l glucose, 50 mmol/l phosphate buffer, initial pH of 7.5, the ratio of dark to photo bacteria of 1:10 and light intensity of 8000 lux. The maximum hydrogen production rate was 33.85 ml H₂/l/h. Phosphate buffer concentration was the most important parameter influencing hydrogen production in this co-culture. The ratio of acetate to butyrate increased from 0.74 to 1.82 in the soluble metabolites from C. butyricum with phosphate buffer concentration of 10–50 mmol/l. Experimental results could be of great significance for further pilot studies of co-culture hydrogen production.     

Photo-fermentative hydrogen production performance of a newly isolated Rubrivivax gelatinosus YP03 strain with acid tolerance

Screening and excavating new photosynthetic bacteria with excellent hydrogen production performance is extremely important for improving the photo-fermentative hydrogen production. A new photosynthetic bacterium YP03 was isolated and identified to be Rubrivivax gelatinosus by morphological characterization and phylogenetic analysis. The effects of several key factors on hydrogen production performance were carried out. The results indicated that YP03 strain showed a preference for the carbon sources, and 5375 ± 398 mL/L of maximum hydrogen yield was obtained using butyrate medium. Meanwhile, YP03 strain could use several nitrogen sources to produce hydrogen, and glutamic acid was the optimum nitrogen source for hydrogen produced. Furthermore, YP03 exhibited better hydrogen production performance at initial pH 7.0, reaction temperature 33 °C and light intensity 5000 lux, and the maximum hydrogen production rate was 108.3 ± 12.4 mL/(Lh), which was relatively high compared with the previous reports by R. gelatinosus. Especially, the proper pH for hydrogen production by YP03 ranged from weak acid to neutral (6.5–7.0) and it still could produce hydrogen at pH 5.5 showing the characteristic of acid tolerance. It suggested that YP03 is a potential candidate for the integration of dark- and photo-fermentative hydrogen production. These findings contribute to our understanding of YP03 strain and provide a prospective photosynthetic bacterium for efficient hydrogen production in future research.     

Effect of light intensity and initial pH during hydrogen production by an integrated dark and photofermentation process

Photofermentation was carried out with the spent fermentation broth obtained from the anaerobic dark fermentation in a two-stage process. For the first stage, i.e. dark fermentation Enterobacter cloacae DM 11 was used as hydrogen producing microorganism. For photofermentation Rhodobacter sphaeroides O.U. 001, a photo-heterotrophic purple non-sulfur bacterium, was used. pH study revealed that cumulative hydrogen production was maximum at initial medium pH of 7.0 ± 0.2. Biomass yield was also high at the vicinity of pH 7.0 and it decreased as the pH increased from 7.0 to 8.0. Increased light intensity resulted in an increase in the total volume of hydrogen evolved and also hydrogen production rate. However, light conversion efficiency decreased by increasing light intensity. A four-fold increase in light intensity resulted in a three-fold decrease in light conversion efficiency although the cumulative volume of hydrogen gas production increased. It was observed that only a maximum of 0.51% light conversion efficiency could be achieved but at the expense of very low light intensity of 2500 lux (3.75 W m⁻²).     

Amelioration of photofermentative hydrogen production from molasses dark fermenter effluent by zeolite-based removal of ammonium ion

One of the challenges in the development of integrated dark and photofermentative biological hydrogen production systems is the presence of ammonium ions in dark fermentation effluent (DFE). Ammonium strongly inhibits the sequential photofermentation process, and so its removal is required for successful process integration. In this study, the removal of ammonium ions from molasses DFE using a natural zeolite (clinoptilolite) was investigated. The samples were treated with batch suspensions of Na-form clinoptilolite. The ammonium ion concentration could be reduced from 7.60 mM to 1.60 mM and from 12.30 mM to 2.40 mM for two different samples. Photofermentative hydrogen production on treated and untreated molasses DFE samples were investigated in batch photobioreactors by an uptake hydrogenase deleted (hup⁻) mutant strain of Rhodobacter capsulatus. Maximum hydrogen productivities of 1.11 mmol H₂/L_c·h and 1.16 mmol H₂/L_c·h and molar yields of 79% and 90% were attained in the treated DFE samples, while the untreated samples resulted in no hydrogen production. The results showed that ammonium ions in molasses DFE could be effectively removed using clinoptilolite by applying a cost-effective, simple batch process.     

Genetically engineered deletion in the N-terminal region of nifA1 in R. capsulatus to enhance hydrogen production

NifA is the primary activator of nitrogenase, and the N-terminal domain of nifA is sensitive to ammonium concentration. In this work, a mutant Rhodobacter capsulatus ZX01 with a genetically engineered deletion in the N-terminal region of nifA1 was constructed by employing overlap extension PCR to mitigate the inhibition of ammonium on nitrogenase expression in photosynthetic bacteria. The effects of different ammonium ion concentrations on the growth and photo-fermentative hydrogen production performance of wild-type strain R. capsulatus SB1003 and mutant ZX01 with glucose and volatile fatty acids as the carbon sources were studied, respectively. When the ratio of NH₄⁺-N was 20% and 30%, the hydrogen yield of the mutant ZX01 was enhanced by 14.8% and 20.9% compared with that of R. capsulatus SB1003 using 25 mM acetic acid and 34 mM butyric acid as the carbon source, respectively. In comparison, using 30 mM glucose as the carbon source, the hydrogen yield of ZX01 was increased by 17.7% and 22.2% compared with that of R. capsulatus SB1003 when the ratio of NH₄⁺-N was 20% and 30%, and the nitrogenase activity of ZX01 was also enhanced by 38.0% and 47.6%, respectively. When using 10 mM NH₄⁺ as a single nitrogen source, ZX01 showed a 2.6-fold increase in H₂ production. These results indicated that ZX01 demonstrated higher ammonium tolerance and better hydrogen production performance than the wild-type. The deletion in the N-terminal region of nifA1 could partially de-repress the nitrogenase activity inhibited by ammonium.     

Bioproduction of hydrogen by Rhodobacter capsulatus KU002 isolated from leather industry effluents

A preliminary study on photoproduction of hydrogen by Rhodobacter capsulatus KU002 isolated from leather industry effluents under different cultural conditions with various carbon and nitrogen sources was investigated. Hydrogen production was measured using a Gas chromatograph. Lactate promoted more amounts of hydrogen production under anaerobic light conditions and aerobic light conditions. Cumulative hydrogen production by the organism was recorded at various time intervals. Incubation period of 120 h was optimum for production of hydrogen. pH 7.0 ± 0.2 was optimum for production of hydrogen by growing cells, while pH 7.5 ± 0.26 for resting cells. l-cystine was a good nitrogen source for production of hydrogen. Growing cells produced more amount of hydrogen than resting cells. Glutamine was a poor nitrogen source for hydrogen production by Rb. capsulatus. Significance of the above results in the presence of existing literature is discussed.     

Hydrogen production by photo-fermentative bacteria immobilized on fluidized bio-carrier

In this work, a novel bio-carrier was used to immobilize photo-fermentative bacteria for hydrogen production. The results showed that the bacterial immobilization and hydrogen production were strongly affected by particle size, amount of bio-carrier and light intensity. Controlling the proper size of bio-carrier not only prevented light shading effect from each other, but also made solid carriers better fluidized during operation. The scanning electronic microscopy revealed that the biofilm formed by photo-fermentative bacteria on the surface of bio-carrier enhanced hydrogen production. Because of bio-carrier fluidization, each immobilized bacterium could receive light energy and produce hydrogen. With the optimal particle size (2 × 2 mm), amount (3% weight to volume ratio) and light intensity (6000 lux), the maximum hydrogen yield of 3.24 mol H₂/mol acetate and production rate of 36.06 ml/l/h were obtained in continuous operation stage. Bio-carrier was an effective solid carrier to immobilize photo-fermentative bacteria for improving hydrogen production.     

Effect of physico-chemical parameters on biohydrogen production and growth characteristics by batch culture of Rhodobacter sphaeroides CIP 60.6

In this paper, Rhodobacter sphaeroides CIP 60.6 strain was newly used for the biohydrogen production in a perfectly shaken column photobioreactor, grown in batch culture under anaerobic and illumination conditions, to investigate the effects of some physico-chemical parameters in microbial hydrogen photofermentation. Luedeking–Piret model was considered for the data fitting to find out the mode of hydrogen generation and the relationship between the cell growth and hydrogen production. The results show that, both growth cells and resting cells can produce hydrogen at light intensities greater or equal to 2500 lux, however, at the weak intensities hydrogen is a metabolite associated to growth. Growth rate and hydrogen production rate increase with the increasing of light intensity. Moreover, hydrogen production rate become higher in stationary phase than that in logarithmic phase, with the enhancement of light intensity. Maximum hydrogen production rate obtained was 39.88 ± 0.14 ml/l/h, at the optimal conditions (4500–8500 lux). Modified Gompertz equation was applied for the data fitting to verify the accuracy and the agreement of the model with experimental results. It is revealed that, in the modified Gompertz equation, the lag time represents time for which hydrogen production becomes maximal, not the beginning time of hydrogen production. The stop of stirring reduced hydrogen production rate and created unstable hydrogen production in reactor. The pH ranges of 7.5 ± 0.1 were the favorable pH for hydrogen production.     

Enhanced hydrogen production performance of Rubrivivax gelatinosus M002 using mixed carbon sources

A new isolated photosynthetic bacterium, Rubrivivax gelatinosus M002, can produce hydrogen with glucose or lactate as sole carbon source, and grow on butyrate and acetate without hydrogen evolution. Experiments on studying its hydrogen production performance from glucose mixed with acetate, butyrate or lactate were carried out. The results showed that the hydrogen yield increased significantly and the pH value of the photo-fermentations could retain around 7 in these mixed carbon sources cultures. A hydrogen yield of 9.9 mol H₂/mol-glucose was observed when 20 mM acetate and 15 mM glucose was co-fed as substrate. The maximum hydrogen production rate was 44 mL/(L·h), which was 37.5% higher than the highest rate obtained with glucose as sole carbon source. The results suggest an alternative way for high-yield hydrogen production with mixed carbon source in one-step process instead of two-step fermentation process.     

Long-term stable hydrogen production from acetate using immobilized Rhodobacter capsulatus in a panel photobioreactor

Biological hydrogen production is attractive since renewable resources are utilized for hydrogen production. In this study, a novel panel photobioreactor (1.4 L) was constructed from Plexiglas with a network of nylon fabric support for agar immobilized bacteria complex. Two strains of Rhodobacter capsulatus DSM 1710 wild-type strain and Rhodobacter capsulatus YO3 (hup⁻, uptake hydrogenase deleted mutant) with cell concentrations of 2.5 and 5.0 mg dcw/mL agar, respectively were entrapped by 4% (w/v) of agar. The system was operated for 72–82 days in a sequential batch mode utilizing acetate as substrate at 30 °C under continuous illumination. Immobilization increased the stability of the photobioreactors by reducing the fluctuations in pH. The pH remained between 6.7 and 8.0 during the process. Both hydrogen yield and productivity were higher in immobilized photobioreactors compared to suspended culture. The highest hydrogen productivities of 0.75 mmol H₂/L/h and 1.3 mmol H₂/L/h were obtained by R. capsulatus DSM1710 and R. capsulatus YO3 respectively.     

Isolation,characterization and optimization of photo-hydrogen production conditions by newly isolated Rhodobacter sphaeroides KKU-PS5

A purple non-sulfur (PNS) photosynthetic bacterium was isolated from an upflow anaerobic sludge blanket (UASB) bioreactor for methane production and was identified as Rhodobacter sphaeroides KKU-PS5 (GenBank Accession no. KC481702) by 16s rRNA gene sequence analysis. Strain KKU-PS5 could utilize glucose, xylose, fructose, arabinose, malate, succinate, acetate, butyrate, lactate and D-mannitol for growth and hydrogen production. Malate was a preferred carbon source while glutamate and Aji-L (waste from the process of crystallizing monosodium glutamate) were the preferred nitrogen sources. The ability to utilize Aji-L as a low-cost nitrogen supplement for photo-biohydrogen production by the strain KKU-PS5 is considered as its desirable characteristic. The threshold substrate concentration of malate was 30 mmol/L. The optimum conditions for hydrogen production from malate were an initial pH of 7.0, FeSO₄ concentration of 4 mg/L, temperature of 30 °C and light intensity of 6 klux. Under the optimum conditions, the maximum hydrogen production, the hydrogen yield (HY) and the hydrogen production rate (HPR) of 1330 mL-H₂/L, 3.80 mol-H₂/mol-malate, and 11.08 mL-H₂/L h, respectively, were achieved. Hydrogen production under a dark/light cycle led to a decreased HY and HPR in comparison to continuous illumination.