Bio-hydrogen production from acid hydrolyzed waste ground wheat by dark fermentation

Waste ground wheat was subjected to acid hydrolysis (pH = 3.0) at 90 °C for 15 min using an autoclave. The sugar solution obtained from acid hydrolysis was subjected to dark fermentation for hydrogen gas production after neutralization. In the first set of experiments, initial total sugar concentration was varied between 3.9 and 27.5 g L⁻¹ at constant biomass (cell) concentration of 1.3 g L⁻¹. Biomass concentration was varied between 0.28 g L⁻¹ and 1.38 g L⁻¹ at initial total sugar concentration of 7.2 ± 0.2 g L⁻¹ in the second set of experiments. The highest hydrogen yield (1.46 mol H₂ mol⁻¹ glucose) and the specific formation rate (83.6 ml H₂ g⁻¹ cell h⁻¹) were obtained with 10 g L⁻¹ initial total sugar concentration. Biomass (cell) concentration affected the specific hydrogen production rate yielding the highest rate (1221 ml H₂ g⁻¹ cell h⁻¹) and the yield at the lowest (0.28 g L⁻¹) initial biomass concentration. The most suitable X_o/S_o ratio, maximizing the yield and specific rate of hydrogen gas formation was X_o/S_o = 0.037. Dark fermentation of acid hydrolyzed ground wheat was found to be more beneficial as compared to simultaneous bacterial hydrolysis and fermentation.     

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.     

Bio-hydrogen production by different operational modes of dark and photo-fermentation: An overview

This article overviews reported studies on bio-hydrogen production from different raw materials by dark and photo-fermentations operated with different modes. Sequential and combined dark and photo-fermentations operated in batch, continuous and fed-batch modes were compared. Operating conditions and modes resulting in the highest hydrogen yield and formation rate were revealed. Relative advantages of sequential and combined dark and photo-fermentations were discussed. Sequential fermentation was found to be preferable due to high H₂ yields and productivities. High cell density fed-batch culture with controlled feeding and simultaneous product removal was concluded to be the most suitable operation mode at the optimum environmental conditions.     

Bio-hydrogen production from ground wheat starch by continuous combined fermentation using annular-hybrid bioreactor

Continuous combined fermentation of ground wheat starch was realized in an annular-hybrid bioreactor (AHB) for hydrogen gas production. A mixture of pure cultures of Clostridium beijerinkii (DSMZ-791) and Rhodobacter sphaeroides-RV were used as seed cultures in combined fermentation. The feed contained 5 g L⁻¹ ground wheat with some nutrient supplementation. Effects of hydraulic residence time (HRT) on the rate and yield of hydrogen gas formation were investigated. Steady-state daily hydrogen production decreased but, hydrogen yield increased with increasing HRT. The highest hydrogen yield was 90 ml g⁻¹ starch at HRT of 6 days. Hydrolysis of starch and fermentation of glucose to volatile fatty acids (VFA) were readily realized at all HRTs. However, slow conversion of VFAs to H₂ and CO₂ by photo-fermentation caused accumulation of VFAs in the medium. Specific and volumetric rates of hydrogen formation also decreased with increasing HRT. High hydrogen yields obtained at high HRTs are due to partial fermentation of VFAs by Rhodobacter sp. The system should be operated at HRTs longer than 5 days for effective hydrogen gas formation by the dark and photo-fermentation bacteria.     

Hydrogen gas production from acid hydrolyzed wheat starch by combined dark and photo-fermentation with periodic feeding

Hydrogen gas production from acid hydrolyzed waste wheat starch by combined dark and photo-fermentation was investigated in continuous mode with periodic feeding and effluent removal. A mixture of heat treated anaerobic sludge and Rhodobacter sphaeroides (NRRL-B 1727) were used as the seed culture for dark and light fermentations, respectively with biomass ratio of Rhodobacter/sludge = 3. Hydraulic residence time (HRT) was changed between 1 and 8 days by adjusting the feeding periods. Ground waste wheat was acid hydrolyzed at pH = 3 and 121 °C for 30 min using an autoclave and the resulting sugar solution was used as the substrate for combined fermentation after pH adjustment and nutrient addition. The highest daily hydrogen gas production (41 ml d⁻¹), hydrogen yield (470 ml g⁻¹ total sugar = 3.4 mol H₂ mol⁻¹glucose), volumetric and specific hydrogen production rates were obtained at the HRT of 8 days. The highest biomass and the lowest total volatile fatty acids (TVFA) concentrations were also realized at HRT = 8 days indicating VFA fermentation by Rhodobacter sp. at high HRTs. The lowest total sugar loading rate of 0.625 g L⁻¹ d⁻¹ resulted in the highest hydrogen yield and formation rate. Hydrogen gas production by combined fermentation with periodic feeding was proven to be an effective method resulting in high hydrogen yields at long HRTs.     

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.     

Culture conditions affecting H2 production by phototrophic bacterium Rhodobacter sphaeroides KD131

The effect of culture conditions on photo-H₂ production was investigated using the photosynthetic bacterium Rhodobacter sphaeroides KD131. When the initial cell concentrations were either below or above a threshold of 0.56 g-dcw/L, the H₂ production decreased due to an imbalance between the biomass and the substrate. Malate- and succinate-fed cultures exhibited the highest substrate conversion to H₂ production, whereas more than 85% of the substrate was utilized for cell growth in acetate- and butyrate-fed cultures. Compared with (NH₄)₂SO₄, glutamate as a nitrogen source was more appropriate for the initial H₂ production, but inhibited H₂ evolution during extended cultivation due to released NH₄⁺ ion. Even though the KD131 strain grew well under slightly acidic conditions, the pH value should be maintained in a neutral range in order to enhance H₂ production. The highest H₂ yield of 3.65 mol-H₂/mol-succinate was achieved when the KD131 strain grew in the succinate–glutamate medium with an initial cell concentration of 0.56 g-dcw/L and the pH level controlled to 7.5.     

Bio-hydrogen production and the F0F1-ATPase activity of Rhodobacter sphaeroides: Effects of various heavy metal ions

Rhodobacter sphaeroides MDC 6521 isolated from Arzni mineral springs in Armenia is able to produce bio-hydrogen (H₂) in anaerobic conditions upon illumination in the presence of various metal ions. The significant aspect in regulation of H₂ production by these bacteria and its energetics is the requirement for F₀F₁-ATPase, the main membrane enzyme responsible for generation of proton motive force under anaerobic conditions. In order to determine the mediatory role of F₀F₁ in H₂ production, the effects of various metal ions (Mn²⁺, Mg²⁺, Fe²⁺, Ni²⁺, and Mo⁶⁺) on N,N′-dicyclohexylcarbodiimide inhibited ATPase activity of R. sphaeroides membrane vesicles were investigated. These ions in appropriate concentrations considerably enhanced H₂ production, which was not observed in the absence of Fe²⁺, indicate the requirement for Fe²⁺. The R. sphaeroides membrane vesicles demonstrated significant ATPase activity. In the absence of Fe²⁺ inhibition (∼80%) of ATPase activity was observed, which was increased by addition of metal ions. A higher ATPase activity was detected in the presence of Fe²⁺ (80 μM) and Mo⁶⁺ (16 μM). These results indicate a relationship between the F₀F₁-ATPase activity and H₂ production that might be a significant pathway to provide novel evidence of a requirement for F₀F₁-ATPase in H₂ production by R. sphaeroides.     

Dark fermentation of acid hydrolyzed ground wheat starch for bio-hydrogen production by periodic feeding and effluent removal

Dark fermentation of acid hydrolyzed ground wheat starch for bio-hydrogen production by periodic feeding and effluent removal was investigated at different feeding intervals. Ground wheat was acid hydrolyzed at pH = 3 and T = 121 °C for 30 min using an autoclave. The resulting sugar solution was subjected to dark fermentation with periodic feeding and effluent removal. The feed solution contained 9 ± 0.5 g L⁻¹ total sugar supplemented with some nutrients. Depending on the feeding intervals hydraulic residence time (HRT) was varied between 6 and 60 h. Steady-state daily hydrogen production increased with decreasing HRT. The highest daily hydrogen production (305 ml d⁻¹) and volumetric hydrogen production rate (1220 ml H₂ L⁻¹ d⁻¹) were obtained at HRT of 6 h. Hydrogen yield (130 ml H₂ g⁻¹ total sugar) reached the highest level at HRT = 24 h. Effluent total sugar concentration decreased, biomass concentration and yield increased with increasing HRT indicating more effective sugar fermentation at high HRTs. Dark fermentation end product profile shifted from acetic to butyric acid with increasing HRT. High acetic/butyric acid ratio obtained at low HRTs resulted in high hydrogen yields.     

Repeated-batch production of hydrogen using Rhodobacter sphaeroides S10

Photofermentation of acid hydrolyzed oil palm empty fruit bunch is reported for hydrogen production in repeated-batch fermentations using the bacterium Rhodobacter sphaeroides S10. Photofermentations were carried out at 35 °C at an incident light level of 10 klux. At specified times, different specified volumes of the culture broth were removed and replaced with an equal volume of the fresh medium. The initial mixed carbon (glucose, xylose, acetic acid) content in the medium of the repeated-batch reactors was adjusted to 20 mM. The kinetics of hydrogen production were evaluated in repeated-batch fermentations carried out in various ways: different volume exchange levels, different switch times from batch to repeated-batch operation, and different cycle times.     

Photo-fermentative hydrogen gas production from dark fermentation effluent of acid hydrolyzed wheat starch with periodic feeding

Hydrogen gas production by photo-fermentation of dark fermentation effluent of acid hydrolyzed wheat starch was investigated at different hydraulic residence times (HRT = 1-10 days). Pure Rhodobacter sphaeroides (NRRL B-1727) culture was used in continuous photo-fermentation by periodic feeding and effluent removal. The highest daily hydrogen gas production (85 ml d⁻¹) was obtained at HRT = 4 days (96 h) while the highest hydrogen yield (1200 ml H₂ g⁻¹ TVFA) was realized at HRT = 196 h. Specific and volumetric hydrogen formation rates were also the highest at HRT = 96 h. Steady-state biomass concentrations and biomass yields increased with increasing HRT. TVFA loading rates of 0.32 g L⁻¹ d⁻¹ and 0.51 g L⁻¹ d⁻¹ resulted in the highest hydrogen yield and formation rate, respectively. Hydrogen gas yield obtained in this study compares favorably with the relevant literature reports probably due to operation by periodic feeding and effluent removal.     

Comparison of bio-hydrogen production from hydrolyzed wheat starch by mesophilic and thermophilic dark fermentation

Hydrogen gas production potentials of acid-hydrolyzed and boiled ground wheat were compared in batch dark fermentations under mesophilic (37 °C) and thermophilic (55 °C) conditions. Heat-treated anaerobic sludge was used as the inoculum and the hydrolyzed ground wheat was supplemented by other nutrients. The highest cumulative hydrogen gas production (752 ml) was obtained from the acid-hydrolyzed ground wheat starch at 55 °C and the lowest (112 ml) was with the boiled wheat starch within 10 days. The highest rate of hydrogen gas formation (7.42 ml H₂ h⁻¹) was obtained with the acid-hydrolyzed and the lowest (1.12 ml H₂ h⁻¹) with the boiled wheat at 55 °C. The highest hydrogen gas yield (333 ml H₂ g⁻¹ total sugar or 2.40 mol H₂ mol⁻¹ glucose) and final total volatile fatty acid (TVFA) concentration (10.08 g L⁻¹) were also obtained with the acid-hydrolyzed wheat under thermophilic conditions (55 °C). Dark fermentation of acid-hydrolyzed ground wheat under thermophilic conditions (55 °C) was proven to be more beneficial as compared to mesophilic or thermophilic fermentation of boiled (partially hydrolyzed) wheat starch.     

Molecular hydrogen production by nitrogenase of Rhodobacter sphaeroides and by Fe-only hydrogenase of Rhodospirillum rubrum

The genes coding for two PII-like proteins, GlnB and GlnK, which play key roles in repressing the nitrogenase expression in the presence of ammonium ion, were interrupted from the chromosome of Rhodobacter sphaeroides. The glnB–glnK mutant exhibits the less ammonium ion-mediated repression for nitrogenase compared with its parental strain, which results in more H₂ accumulation by the mutant under the conditions. Rhodospirillum rubrum produces H₂ by both nitrogenase and hydrogenase. R. rubrum containing the recombinant pRK415 with an insert of hydC coding for its own Fe-only hydrogenase showed twofold higher accumulation of H₂ in the presence of pyruvate under photoheterotrophic conditions, which was not observed in the absence of pyruvate. The same was true with R. rubrum containing the recombinant pRK415 cloned with hydA coding for Fe-only hydrogenase of Clostridium acetobutylicum. Thus, Fe-only hydrogenase requires pyruvate as an electron donor for the production of H₂.     

Statistical optimization of biohydrogen production from sucrose by a co-culture of Clostridium acidisoli and Rhodobacter sphaeroides

Statistically based experimental designs were applied to optimize the fermentation process parameters for hydrogen (H₂) production by co-culture of Clostridium acidisoli and Rhodobacter sphaeroides with sucrose as substrate. An initial screening using the Plackett–Burman design identified three factors that significantly influenced H₂ yield: sucrose concentration, initial pH, and inoculum ratio. These factors were considered to have simultaneous and interdependent effects. A central composite design and response surface analysis were adopted to further investigate the mutual interactions among the factors and to identify the values that maximized H₂ production. The optimal substrate concentration, initial pH, and inoculum ratio of C. acidisoli to R. sphaeroides were 11.43 g/L sucrose, 7.13, and 0.83, respectively. Using these optimal culture conditions, substrate conversion efficiency was determined as 10.16 mol H₂/mol sucrose (5.08 mol H₂/mol hexose), which was near the expected value of 10.70 mol H₂/mol sucrose (5.35 mol H₂/mol hexose).     

Optimization of photosynthetic hydrogen production from acetate by Rhodobacter sphaeroides RV

In this study, hydrogen production by Rhodobacter sphaeroides RV from acetate was investigated. Ammonium sulphate and sodium glutamate were used to study the effects of nitrogen sources on photosynthetic hydrogen production. The results showed the optimal concentrations for ammonium sulphate and sodium glutamate were in the range of 0.4–0.8 g/L. Orthogonal array design was applied to optimize the hydrogen-producing conditions of the concentrations of yeast, FeSO₄ and NiCl₂. The theoretical optimal condition for hydrogen production was as follow: yeast 0.1 g/L, FeSO₄ 100 mg/L and NiCl₂ 20 mg/L.     

Thermophilic dark fermentation of acid hydrolyzed waste ground wheat for hydrogen gas production

Batch dark fermentation experiments were performed to investigate the effects of biomass and substrate concentration on bio-hydrogen production from acid hydrolyzed ground wheat at 55 °C. In the first set of experiments, the substrate concentration was constant at 20 g total sugar L⁻¹ and biomass concentration was varied between 0.52 and 2.58 g L⁻¹. Total sugar concentration was varied between 4.2 and 23.7 g L⁻¹ in the second set of experiments with a 1.5 g L⁻¹ constant biomass concentration. The highest cumulative hydrogen formation (582 mL, 30 °C, 1 atm), formation rate (5.43 mL h⁻¹) and final total volatile fatty acid (TVFA) concentration (6.54 g L⁻¹) were obtained with 1.32 g L⁻¹ biomass concentration. In variable substrate concentration experiments, the highest cumulative hydrogen (365 mL) and TVFA concentration (4.8 g L⁻¹) were obtained with 19.25 g L⁻¹ initial total sugar concentration while hydrogen gas formation rate (12.95 mL h⁻¹) and the yield (200 mL H₂ g⁻¹ total sugar) were the highest with 4.2 g L⁻¹ total sugar concentration.     

Dark fermentation of ground wheat starch for bio-hydrogen production by fed-batch operation

Ground wheat solution was used for bio-hydrogen production by dark fermentation using heat-treated anaerobic sludge in a completely mixed fermenter operating in fed-batch mode. The feed wheat powder (WP) solution was fed to the anaerobic fermenter with a constant flow rate of 8.33 mL h⁻¹ (200 mL d⁻¹). Cumulative hydrogen production, starch utilization and hydrogen yields were determined at three different WP loading rates corresponding to the feed WP concentrations of 10, 20 and 30 g L⁻¹. The residual starch (substrate) concentration in the fermenter decreased with operation time while starch consumption was increasing. The highest cumulative hydrogen production (3600 mL), hydrogen yield (465 mL H₂ g⁻¹ starch or 3.1 mol H₂ mol⁻¹ glucose) and hydrogen production rate (864 mL H₂ d⁻¹) were obtained after 4 days of fed-batch operation with the 20 g L⁻¹ feed WP concentration corresponding to a WP loading rate of 4 g WP d⁻¹. Low feed WP concentrations (10 g L⁻¹) resulted in low hydrogen yields and rates due to substrate limitations. High feed WP concentrations (30 g L⁻¹) resulted in the formation of volatile fatty acids (VFAs) in high concentrations causing inhibition on the rate and yield of hydrogen production.     

Function of glucose catabolic pathways in hydrogen production from glucose in Rhodobacter sphaeroides 6016

Purple non-sulfur (PNS) bacteria can convert volatile fatty acids into hydrogen with a high substrate conversion efficiency. However, when PNS bacteria utilize sugars as a carbon source, such as glucose and sucrose, the substrate conversion efficiency is relatively low. In order to investigate the contributions of the glucose catabolic pathways in Rhodobacter sphaeroides 6016 to its hydrogen production, the cfxA gene from the Embden–Meyerhof–Parnas (EMP) pathway, edd from the Entner–Doudoroff (ED) pathway, and kdg from the semi-phosphorylative ED bypass were knocked out to construct the mutant strains edd⁻, cfxA⁻, and kdg⁻, respectively. Additionally, two of these three genes were knocked out to construct the mutant strains kdg⁻edd⁻, kdg⁻cfxA⁻, and cfxA⁻edd⁻. Hydrogen productions by these mutant strains were compared to that of the wild type strain 6016 using 25 mM glucose as a carbon source. Compared to 6016, variations in hydrogen production and growth were detected in the edd mutant strains (kdg⁻edd⁻, cfxA⁻edd⁻, and edd⁻), while no obvious changes were detected in the others. Notably, the kdg⁻edd⁻ mutant did not produce hydrogen, and its maximum growth was 70% less than that of R. sphaeroides 6016. These results indicate that the ED pathway and semi-phosphorylative ED bypass have a governing impact on cell growth and hydrogen production from glucose in R. sphaeroides 6016. The potential synergistic function of the ED pathway and semi-phosphorylative ED bypass and the reasons for the low hydrogen yield from sugar carbon sources in R. sphaeroides 6016 are discussed.