Photofermentative hydrogen production from volatile fatty acids present in dark fermentation effluents

In the present study, the growth and hydrogen production of Rhodobacter sphaeroides O.U. 001, was investigated in media containing five different volatile fatty acids (VFA) individually (malate, acetate, propionate, butyrate and lactate) and in media containing mixtures of these acids that reflect the composition of dark fermentation effluents. The highest hydrogen production rate was obtained in malate (24 ml_hydrogen/l_reactor h) and the highest biomass concentration was obtained in acetate containing media (1.65 g/l). The substrate conversion efficiencies for different volatile fatty acids were found to vary between 14 and 50%. The malate and butyrate consumption rates were first order with consumption rate constants of 0.026 h⁻¹ and 0.015 h⁻¹, respectively. In the case of substrate mixtures, it was observed that the bacteria consumed acetate first, followed by propionate and then butyrate. It was also found that the consumption rate of the main substrate significantly increased when the minor substrates were depleted.     

Bio-hydrogen production from acid hydrolyzed wheat starch by photo-fermentation using different Rhodobacter sp

Hydrogen gas production from sugar solution derived from acid hydrolysis of ground wheat starch by photo-fermentation was investigated. Three different pure strains of Rhodobacter sphaeroides (RV, NRLL and DSZM) were used in batch experiments to select the most suitable strain. The ground wheat was hydrolyzed in acid solution at pH = 3 and 90 °C in an autoclave for 15 min. The resulting sugar solution was used for hydrogen production by photo-fermentation after neutralization and nutrient addition. R. sphaeroides RV resulted in the highest cumulative hydrogen gas formation (178 ml), hydrogen yield (1.23 mol H₂ mol⁻¹ glucose) and specific hydrogen production rate (46 ml H₂ g⁻¹ biomass h⁻¹) at 5 g l⁻¹ initial total sugar concentration among the other pure cultures. Effects of initial sugar concentration on photo-fermentation performance were investigated by varying sugar concentration between 2.2 and 13 g l⁻¹ using the pure culture of R. sphaeroides RV. Cumulative hydrogen volume increased from 30 to 232 ml when total sugar concentration was increased from 2.2 to 8.5 g l⁻¹. Further increases in initial sugar concentration resulted in decreases in cumulative hydrogen formation. The highest hydrogen formation rate (3.69 ml h⁻¹) and yield (1.23 mol H₂ mol⁻¹ glucose) were obtained at a sugar concentration of 5 g l⁻¹.     

Remarkable enhancement on hydrogen production performance of Rhodobacter sphaeroides by disrupting spbA and hupSL genes

The redox balance and bacteriochlorophyll (Bchl) synthesis are both significant to hydrogen generation in photosynthetic bacteria. In this study, spbA and hupSL genes were knocked out from the genome of Rhodobacter sphaeroides HY01. The UV–vis spectra showed that the Bchl contents of spbA mutants were enhanced under photosynthetic conditions. The hydrogen yields of WH04 (hupSL⁻) and WSH10 (spbA⁻, hupSL⁻) mutants increased by 19.4%, 21.8%, and the maximum hydrogen evolution rates increased by 29.9% and 55.0% respectively using glutamate as sole nitrogen source. The maximum hydrogen production rate of WSH10 was up to 141.9 mL/(L·h). The nifH expression levels of the mutants and the wild type supported the correlation between hydrogen production and nitrogenase activity. The results demonstrate that disruption of spbA in R. sphaeroides can partially derepress the ammonium inhibition in nitrogenase activity, and indicate that spbA is a negative regulator in nitrogenase synthesis in the presence of ammonium.     

Enhancement of phototrophic hydrogen production by Rhodobacter sphaeroides ZX-5 using a novel strategy — shaking and extra-light supplementation approach

Biohydrogen has gained attention due to its potential as a sustainable alternative to conventional methods for hydrogen production. In this study, the effect of light intensity as well as cultivation method (standing- and shaking-culture) on the cell growth and hydrogen production of Rhodobacter sphaeroides ZX-5 were investigated in 38-ml anaerobic photobioreactor with RCVBN medium. Thus, a novel shaking and extra-light supplementation (SELS) approach was developed to enhance the phototrophic H₂ production by R. sphaeroides ZX-5 using malate as the sole carbon source. The optimum illumination condition for shaking-culture by strain ZX-5 increased to 7000–8000 lux, markedly higher than that for standing-culture (4000–5000 lux). Under shaking and elevated illumination (7000–8000 lux), the culture was effective in promoting photo-H₂ production, resulting in a 59% and 56% increase of the maximum and average hydrogen production rate, respectively, in comparison with the culture under standing and 4000–5000 lux conditions. The highest hydrogen-producing rate of 165.9 ml H₂/l h was observed under the application of SELS approach. To our knowledge, this record is currently the highest hydrogen production rate of non-immobilized purple non-sulphur (PNS) bacteria. This optimal performance of photo-H₂ production using SELS approach is a favorable choice of sustainable and economically feasible strategy to improve phototrophic H₂ production efficiency.     

Hydrogen gas production by combined systems of Rhodobacter sphaeroides O.U.001 and Halobacterium salinarum in a photobioreactor

Rhodobacter sphaeroides O.U.001 is a photosynthetic non-sulfur bacterium which produces hydrogen from organic compounds under anaerobic conditions. Halobacterium salinarum is an archaeon and lives under extremely halophilic conditions (4 M NaCl). H. salinarum contains a retinal protein bacteriorhodopsin in its purple membrane which acts as a light-driven proton pump. In this study the Rhodobacter sphaeroides O.U.001 culture was combined with different amounts of packed cells of H. salinarum S9 or isolated purple membrane fragments in order to increase the photofermentative hydrogen gas production. The packed cells of H. salinarum have the ability to pump protons upon illumination due to the presence of bacteriorhodopsin. The proton gradient produced may be used for the formation of ATP or protons may be used for H₂ production by R. sphaeroides. Similar to intact cells purple membrane fragments may also form vesicles around certain ions and may act like closed systems.     

New tolerant strains of purple nonsulfur bacteria for hydrogen production in a two-stage integrated system

In this study we described the isolation of eight new strains of purple non-sulfur bacteria resistant to salinity ≥30 g L⁻¹ and high concentration of VFAs (200 mM). These strains were characterized by their general physiological properties and the occurrence of hupSL genes. Some correlation was observed between the rate of H₂ photoproduction, the absence of hupSL genes and hydrogenase activity. Two fast-growing strains without hupSL genes showed high nitrogenase activity and hydrogen accumulation during growth on Ormerod medium. These strains were capable of H₂ photoproduction using non-treated dark culture (75% in water) after dark fermentation of starch at 30 g L⁻¹, unlike control strains, Rhodobacter capsulatus B10 and Rb. sphaeroides GL. New N7 and 13 strains identified as Rb. sphaeroides can be recommended for application in a two-stage H₂ production system.     

Control strategies for hydrogen production through co-culture of Ethanoligenens harbinense B49 and immobilized Rhodopseudomonas faecalis RLD-53

This study evaluated hydrogen production by co-culture of Ethanoligenens harbinense B49 and immobilized Rhodopseudomonas faecalis RLD-53 with different control strategies. To enhance cooperation of dark and photo-fermentation bacteria during hydrogen production process, the glucose concentration, phosphate buffer concentration and initial pH were controlled at 6 g/l, 50 mmol/l and 7.5, respectively. The maximum yield and rate of hydrogen production were 3.10 mol H₂/mol glucose and 17.2 mmol H₂/l/h, respectively. Ethanol from E. harbinense B49 in acetate medium can enhance hydrogen production by R. faecalis RLD-53 except the ratio of ethanol to acetate (R_E/A) among 0.8 to 1.0. Control of the proper phosphate buffer concentration (50 mmol/l) not only increased acetic acid production by E. harbinense B49, but also maintained stable pH of co-culture system. Therefore, the results showed that co-culture of E. harbinense B49 and immobilized R. faecalis RLD-53 was a promising way of converting glucose into hydrogen.     

Light fermentation of dark fermentation effluent for bio-hydrogen production by different Rhodobacter species at different initial volatile fatty acid (VFA) concentrations

Three different Rhodobacter sphaeroides (RS) strains (RS–NRRL, RS–DSMZ and RS–RV) and their combinations were used for light fermentation of dark fermentation effluent of ground wheat containing volatile fatty acids (VFA). In terms of cumulative hydrogen formation, RS–NRRL performed better than the other two strains producing 48 ml H₂ in 180 h. However, RS–RV resulted in the highest hydrogen yield of 250 ml H₂ g⁻¹ TVFA. Specific hydrogen production rate (SHPR) with the RS–NRRL was also better in comparison to the others (13.8 ml H₂ g⁻¹ biomass h⁻¹). When combinations of those three strains were used, RS–RV + RS–DSMZ resulted in the highest cumulative hydrogen formation (90 ml H₂ in 330 h). However, hydrogen yield (693 ml H₂ g⁻¹ TVFA) and SHPR (12.1 ml H₂ g⁻¹ biomass h⁻¹) were higher with the combination of the three different strains. On the basis of Gompertz equation coefficients mixed culture of the three different strains gave the highest cumulative hydrogen and formation rate probably due to synergistic interaction among the strains. The effects of initial TVFA and NH₄–N concentrations on hydrogen formation were investigated for the mixed culture of the three strains. The optimum TVFA and NH₄–N concentrations maximizing the hydrogen formation were determined as 2350 and 47 mg L⁻¹, respectively.     

The effect of Ni,Fe and Mg concentration on photo-hydrogen production by Rhodopseudomonas faecalis RLD-53

In the present study, the effect of Ni²⁺ (0–10 μmol/l), Fe²⁺ (0–200 μmol/l) and Mg²⁺ (0–15 mmol/l) concentration on photo-hydrogen production from acetate was investigated by batch culture. Results showed that under a proper concentration range, Ni²⁺ was able to enhance the hydrogen production rate and the hydrogen yield; Fe²⁺ was able to increase the hydrogen yield, and hydrogen production rate was enhanced only when the culturing time was 24–72 h. Ni²⁺ and Fe²⁺ at a higher concentration inhibited cell growth. When Ni²⁺ and Fe²⁺ concentrations were 4 μmol/l and 80 μmol/l, respectively, maximal hydrogen yield of 2.87 and 2.78 mol H₂/mol acetate was obtained when batch culturing at 35 °C with initial pH 7.0. Mg²⁺ did not significantly affect hydrogen production and hydrogen yield which maintained at about 2.45 mol H₂/mol acetate, but it was favorable to cell growth.     

Investigation of the combined effects of acetate and photobioreactor illuminated fraction in the induction of anoxia for hydrogen production by Chlamydomonas reinhardtii

In the context of hydrogen production by microalgae, the growth of Chlamydomonas reinhardtii was characterized under autotrophic and mixotrophic conditions in a fully controlled photobioreactor (PBR). The combined effect of light transfer conditions, as represented by the illuminated fraction γ, with acetate consumption was observed upon establishment of anoxia. Anoxia was reached in batch cultures when γ was close to 1 (almost fully illuminated culture) in mixotrophic conditions while a value of γ ≈ 0.46 in autotrophic conditions was not sufficient. Based on these results, continuous hydrogen production was established in a cylindrical PBR operated in luminostat with constant illumination and in mixotrophic conditions. Maximum hydrogen gas production was equal to 1.4 ± 0.1 ml_H2 l⁻¹ h⁻¹ for photon flux density of 110 μmol m⁻² s⁻¹ and reactor illuminated fraction of γ = 0.5. Carbon mass balance was realized, emphasizing the necessity to work in strictly autotrophic conditions for hydrogen production with no concomitant CO₂ release.     

Hydrogen production and end-product synthesis patterns by Clostridium termitidis strain CT1112 in batch fermentation cultures with cellobiose or α-cellulose

Hydrogen (H₂) production and end-product synthesis were characterized in a novel, mesophilic, cellulolytic, anaerobic bacterium, Clostridium termitidis strain CT1112, isolated from the gut of the termite, Nasutitermes lujae. Growth curves, pH patterns, protein content, organic acid synthesis, and H₂ production were determined. When grown on 2 g l⁻¹ cellobiose and 2 g l⁻¹ α-cellulose, C. termitidis displayed a cell generation time of 6.5 h and 18.9 h, respectively. The major end-products synthesized on cellobiose included acetate, hydrogen, CO₂, lactate, formate and ethanol, where as on cellulose, the major end-products included hydrogen, acetate, CO₂ and ethanol. The concentrations of acetate were greater than ethanol, formate and lactate on both cellobiose and α-cellulose throughout the entire growth phase. Maximum yields of acetate, ethanol, hydrogen and formate on cellobiose were 5.9, 3.7, 4.6 and 4.2 mmol l⁻¹ culture, respectively, where as on cellulose, the yields were 7.2, 3.1, 7.7 and 2.9 mmol l⁻¹ culture, respectively. Hydrogen and ethanol production rates were slightly higher in C. termitidis cultured on cellobiose when compared to α-cellulose. Although, the generation time on α-cellulose was longer than on cellobiose, H₂ production was favored corresponding to acetate synthesis, thereby restricting the carbon flowing to ethanol. During log phase, H₂, CO₂ and ethanol were produced at specific rates of 4.28, 5.32, and 2.99 mmol h⁻¹ g dry weight⁻¹ of cells on cellobiose and 2.79, 2.59, and 1.1 mmol h⁻¹ g dry weight⁻¹ of cells on α-cellulose, respectively.     

Batch and continuous biohydrogen production from starch hydrolysate by Clostridium species

In this study, hydrogen gas was produced from starch feedstock via combination of enzymatic hydrolysis of starch and dark hydrogen fermentation. Starch hydrolysis was conducted using batch culture of Caldimonas taiwanensis On1 able to hydrolyze starch completely under the optimal condition of 55 °C and pH 7.5, giving a yield of 0.46–0.53 g reducing sugar/g starch. Five H₂-producing pure strains and a mixed culture were used for hydrogen production from raw and hydrolyzed starch. All the cultures could produce H₂ from hydrolyzed starch, whereas only two pure strains (i.e., Clostridium butyricum CGS2 and CGS5) and the mixed culture were able to ferment raw starch. Nevertheless, all the cultures displayed higher hydrogen production efficiencies while using the starch hydrolysate, leading to a maximum specific H₂ production rate of 116 and 118 ml/g VSS/h, for Cl. butyricumCGS2 and Cl. pasteurianum CH5, respectively. Meanwhile, the H₂ yield obtained from strain CGS2 and strain CH5 was 1.23 and 1.28 mol H₂/mol glucose, respectively. The best starch-fermenting strain Cl. butyricum CGS2 was further used for continuous H₂ production using hydrolyzed starch as the carbon source under different hydraulic retention time (HRT). When the HRT was gradually shortened from 12 to 2 h, the specific H₂ production rate increased from 250 to 534 ml/g  VSS/h, whereas the H₂ yield decreased from 2.03 to 1.50  mol H₂/mol glucose. While operating at 2 h HRT, the volumetric H₂ production rate reached a high level of 1.5 l/h/l.     

Growth characteristics and hydrogen production by Rhodobacter sphaeroides using various amino acids as nitrogen sources and their combinations with carbon sources

Some amino acids (alanine, asparagine, glutamate, glycine, proline, and tyrosine) were used as nitrogen sources in combination with carbon sources (succinate and malate) to study growth properties and H₂ production by purple non-sulfur bacterium Rhodobacter sphaeroides strains A-10 and D-3. Both strains produced H₂ in succinate–glutamate and malate–glutamate media. Succinate was a better carbon source than malate. In comparison with strain D-3, strain A-10 was able to utilize proline, alanine or tyrosine as nitrogen sources in succinate medium and to produce H₂. Both strains were unable to produce H₂ in the presence of asparagine or glycine as nitrogen sources. N,N′-dicyclohexylcarbodiimide, the F₀F₁-ATPase inhibitor, led to marked inhibition of H₂ production activity of R. sphaeroides. The results suggest that the R. sphaeroides cells growth can be achieved by the use of a large diversity of substrates but only some of them can increase the H₂ production rate.     

Effect of carbon sources on the photobiological production of hydrogen using Rhodobacter sphaeroides RV

Rhodobacter sphaeroides RV was employed to produce hydrogen for the photo-fermentation of sole (acetate, propionate, butyrate, lactate, malate, succinate, ethanol, glucose, citrate and sodium carbonate) and compound carbon sources (malate and succinate, lactate and succinate). The concentrations of sole carbon sources on hydrogen production were investigated in batch assays at 0.8 g/L sodium glutamate and the maximum hydrogen yield was 424 mmol H₂/mol-substrate obtained at 0.8 g/L sodium propionate. The maximum hydrogen yield reached 794 mmol H₂/mol-substrate for 2.02 g lactate and 2.0 g succinate as the compound carbon source. The results showed hydrogen production for the compound carbon source was better than the sole carbon source.     

Bio-hydrogen production by photo-fermentation of dark fermentation effluent with intermittent feeding and effluent removal

Pure culture of Rhodobacter sphaeroides (NRRL- B1727) was used for continuous photo-fermentation of volatile fatty acids (VFA) present in the dark fermentation effluent of ground wheat starch. The feed contained 1950 ± 50 mg L⁻¹ total VFA with some nutrient supplementation. Hydraulic residence time (HRT) was varied between 24 and 120 hours. The highest steady-state daily hydrogen production (55 ml d⁻¹) and hydrogen yield (185 ml H₂ g⁻¹ VFA) were obtained at HRT = 72 hours (3 days). Biomass concentration increased with increasing HRT. Volumetric and specific hydrogen formation rates were also maximum at HRT = 72 h. High extent of TVFA fermentation at HRT = 72 h resulted in high hydrogen gas production.     

Enhanced hydrogen production by means of sulfur-deprived Chlamydomonas reinhardtii cultures grown in pretreated olive mill wastewater

Under sulfur-deprived conditions, the metabolism of Chlamydomonas reinhardtii switches to the photoproduction of hydrogen. This process is sustained by both photosystem II-driven water splitting and by the fermentation of stored carbohydrates. We investigated the possibility of using diluted pretreated olive mill wastewaters (OMW), which contain organic acids and sugars, as a substrate on which to grow Chlamydomonas, in order to obtain suitable biomass to produce hydrogen. The cells grown on a mixture of pretreated OMW and TAP (tris-acetate-phosphate) (50% dilution) were found to be richer in carbohydrates and exhibited a greater production of hydrogen (150 ml H₂ l⁻¹ culture), compared to the control cells (100 ml H₂ l⁻¹ culture). In these cultures, the hydrogen production process was characterized by a shorter aerobic phase and a longer hydrogen-production period. The results offer a useful perspective for the utilization of olive mill wastewaters, which constitute an environmental problem, particularly in Mediterranean areas, and for increasing the output for hydrogen production with Chlamydomonas.     

Biohydrogen and 5-aminolevulinic acid production from waste barley by Rhodobacter sphaeroides O.U.001 in a biorefinery concept

The production of biohydrogen and 5-aminolevulinic acid (5-ALA) by Rhodobacter sphaeroides O.U.001 was investigated in a biorefinery concept. Waste barley was used as a substrate after acid hydrolysis. The hydrolysate was analyzed in terms of its total simple sugar, organic acid, ammonium, element and total phenol contents. Four different growth media having 5 g/L, 7 g/L, 9 g/L and 11 g/L sugar content were prepared using the waste barley hydrolysate to produce biohydrogen and 5-ALA. The increased sugar concentrations resulted in higher cell density and hydrogen accumulation. Accordingly, the highest cell density (OD₆₆₀: 1.78) and hydrogen production (0.4 L H₂/L culture) were observed in the 11 g/L sugar-containing medium. A 67.4 μM 5-ALA was produced upon vitamin B₁₂ and levulinic acid additions. These results showed that waste barley can be used as a substrate for R. sphaeroides for biohydrogen and 5-ALA production within a biorefinery concept.     

Production of biohydrogen from sugars and lignocellulosic biomass using Thermoanaerobacter GHL15

The effect of culture parameters on hydrogen production using strain GHL₁₅ in batch culture was investigated. The strain belongs to the genus Thermoanaerobacter with 98.9% similarity to Thermoanaerobacter yonseiensis and 98.5% to Thermoanaerobacter keratinophilus with a temperature optimum of 65–70 °C and a pH optimum of 6–7. The strain metabolizes various pentoses, hexoses, and disaccharides to acetate, ethanol, hydrogen, and carbon dioxide. However substrate inhibition was observed above 10 mM glucose concentration. Maximum hydrogen yields on glucose were 3.1 mol H₂ mol⁻¹ glucose at very low partial pressure of hydrogen. Hydrogen production from various lignocellulosic biomass hydrolysates was investigated in batch culture. Various pretreatment methods were examined including acid, base, and enzymatic (Celluclast^® and Novozyme 188) hydrolysis. Maximum hydrogen production (5.8–6.0 mmol H₂ g⁻¹ dw) was observed from Whatman paper (cellulose) hydrolysates although less hydrogen was produced by hydrolysates from other examined lignocellulosic materials (maximally 4.83 mmol H₂ g⁻¹ dw of grass hydrolysate). The hydrogen yields from all lignocellulosic hydrolysates were improved by acid and alkaline pretreatments, with maximum yields on grass, 7.6 mmol H₂ g⁻¹ dw.     

Brewery wastewaters in photobiological hydrogen generation in presence of Rhodobacter sphaeroides O.U. 001

Rhodobacter sphaeroides O.U. 001 (concentration of inoculum-0.36 g dry wt/l) and brewery wastewaters were applied in photobiogeneration of hydrogen under illumination of 116 W/m². The best results were obtained with filtered wastewaters sterilized at 120 °C for 20 min and maximal concentration of waste in medium equal 10% v/v. The main product in generated biogas was hydrogen (90%). After sterilization the amount of generated hydrogen was tripled (from 0.76 to 2.2 l H₂/l medium), whereas waste concentration of 10% v/v resulted in the best substrate yield (0.22 l H₂/l of waste). Under these conditions the amount of generated hydrogen was 2.24 l H₂/l medium and light conversion efficiency reached value of 1.7%. The modified Gompertz equations served in modeling of the kinetics of the studied process.