Fermentative hydrogen production by the newly isolated Clostridium beijerinckii Fanp3

A hydrogen producing strain newly isolated from anaerobic sludge in an anaerobic bioreactor, was identified as Clostridium beijerinckii Fanp3 by 16S rDNA gene sequence analysis and detection by BioMerieux Vitek. The strain could utilize various carbon and nitrogen sources to produce hydrogen, which indicates that it has the potential of converting renewable wastes into hydrogen. In batch cultivations, the optimal initial pH of the culture medium was between 6.47 and 6.98. Using 0.15 M phosphate as buffer could alleviate the medium acidification and improve the overall performance of C. beijerinckii Fanp3 in hydrogen production. Culture temperature of 35 °C was established to be the most favorable for maximum rate of hydrogen production. The distribution of soluble metabolic products (SMP) was also greatly affected by temperature. Considering glucose as a substrate, the activation energy (E_a) for hydrogen production was calculated as 81.01 kcal/mol and 21.4% of substrate energy was recovered in the form of hydrogen. The maximal hydrogen yield and the hydrogen production rate were obtained as 2.52 mol/mol-glucose and 39.0 ml/g-glucose h⁻¹, respectively. These results indicate that C. beijerinckii Fanp3 is an ideal candidate for the fermentative hydrogen production.     

Fermentative hydrogen production by Clostridium butyricum and Escherichia coli in pure and cocultures

The effect of coculture of Clostridium butyricum and Escherichia coli on hydrogen production was investigated. C. butyricum and E. coli were grown separately and together as batch cultures. Gas production, growth, volatile fatty acid production and glucose degradation were monitored. Whilst C. butyricum alone produced 2.09 mol-H₂/mol-glucose the coculture produced 1.65 mol-H₂/mol-glucose. However, the coculture utilized glucose more efficiently in the batch culture, i.e., it was able to produce more H₂ (5.85 mmol H₂) in the same cultivation setting than C. butyricum (4.62 mmol H₂), before the growth limiting pH was reached.     

Anthrahydroquinone-2,6-disulfonate increases the rate of hydrogen production during Clostridium beijerinckii fermentation with glucose,xylose, and cellobiose

Fermentative hydrogen production is considered a reasonable alternative for generating H₂ as an energy carrier for electricity production using hydrogen fuel cells. The kinetics of hydrogen production from glucose, xylose and cellobiose were investigated using pure culture Clostridium beijerinckii NCIMB 8052. Adding anthrahydroquinone-2,6-disulfonate (AH₂QDS) at concentrations ranging from 100 μM to 500 μM increased the hydrogen production rates from 0.80 to 1.35 mmol/L-hr to 1.20–2.70 mmol/L-hr with glucose, xylose, or cellobiose as the primary substrates. AH₂QDS amendment also increased the substrate utilization rate and biomass growth rate by at least two times. These findings suggest that adding hydroquinone reducing equivalents influence cellular metabolism with hydrogen production rate, substrate utilization rate, and growth rate being simultaneously affected. Resting cell suspensions were conducted to investigate the influence of AH₂QDS on the hydrogen production rate from glyceraldehyde 3-phosphate, which is a shared intermediate in both glycolysis and pentose phosphate pathway. Data demonstrated that hydrogen production rate increased by 1.5 times when glyceraldehyde 3-phosphate was the sole carbon source, suggesting that the hydroquinone may alter reactions starting with or after glyceraldehyde 3-phosphate in central metabolism. These data demonstrate that adding hydroquinones increased overall metabolic activity of C. beijerinckii. This will eventually increase the efficiency of industrial scale production once appropriate hydroquinone equivalents are identified that work well in large-scale operations, since fermentation rate is one of the two critical factors (production rate and yield) influencing efficiency and cost.     

Biohydrogen production from wastewater by Clostridium beijerinckii: Effect of pH and substrate concentration

An investigation of biological hydrogen production from glucose by Clostridium beijerinckii was conducted in a synthetic wastewater solution. A study examining the effect of initial pH (range 5.7–6.5) and substrate loading (range 1–3 g COD/L) on the specific conversion and hydrogen production rate has shown interaction behaviour between the two independent variables. Highest conversion of 10.3 mL H₂/(g COD/L) was achieved at pH of 6.1 and glucose concentration of 3 g COD/L, whereas the highest production rate of 71 mL H₂/(h L) was measured at pH 6.3 and substrate loading of 2.5 g COD/L. In general, there appears to be a strong trend of increasing hydrogen production rate with an increase in both substrate concentration and pH. Butyrate (14–63%), formate (10–45%) and ethanol (16–40%) were the main soluble products with other volatile fatty acids and alcohols present in smaller quantities.     

Fermentative hydrogen production by new marine Clostridium amygdalinum strain C9 isolated from offshore crude oil pipeline

The present study investigated hydrogen production potential of novel marine Clostridium amygdalinum strain C9 isolated from oil water mixtures. Batch fermentations were carried out to determine the optimal conditions for the maximum hydrogen production on xylan, xylose, arabinose and starch. Maximum hydrogen production was pH and substrate dependant. The strain C9 favored optimum pH 7.5 (40 mmol H₂/g xylan) from xylan, pH 7.5–8.5 from xylose (2.2–2.5 mol H₂/mol xylose), pH 8.5 from arabinose (1.78 mol H₂/mol arabinose) and pH 7.5 from starch (390 ml H₂/g starch). But the strain C9 exhibited mixed type fermentation was exhibited during xylose fermentation. NaCl is required for the growth and hydrogen production. Distribution of volatile fatty acids was initial pH dependant and substrate dependant. Optimum NaCl requirement for maximum hydrogen production is substrate dependant (10 g NaCl/L for xylose and arabinose, and 7.5 g NaCl/L for xylan and starch).     

Fermentative hydrogen production by Clostridium butyricum CGS5 using carbohydrate-rich microalgal biomass as feedstock

In this work, a carbohydrate-rich microalga, Chlorella vulgaris ESP6, was grown photoautotrophically to fix the CO₂. The resulting microalgal biomass was hydrolyzed by acid or alkaline/enzymatic treatment and was then used for biohydrogen production with Clostridium butyricum CGS5. The C. vulgaris biomass could be effectively hydrolyzed by acid pretreatment while similar hydrolysis efficiency was achieved by combination of alkaline pretreatment and enzymatic hydrolysis. The biomass of C. vulgaris ESP6 containing a carbohydrate content of 57% (dry weight basis) was efficiently hydrolyzed by acid treatment with 1.5% HCl, giving a reducing sugars (RS) yield of nearly 100%. C. butyricum CGS5 could utilize RS from C. vulgaris ESP6 biomass to produce hydrogen without any additional organic carbon sources. The optimal conditions for hydrogen production were 37 °C and a microalgal hydrolysate loading of 9 g RS/L with pH-controlled at 5.5. Under the optimal conditions, the cumulative H₂ production, H₂ production rate, and H₂ yield were 1476 ml/L, 246 ml/L/h, and 1.15 mol/mol RS, respectively. The results demonstrate that the C. vulgaris biomass has the potential to serve as effective feedstock for dark fermentative H₂ production.     

Performance and population analysis of hydrogen production from sugarcane juice by non-sterile continuous stirred tank reactor augmented with Clostridium butyricum

Non-sterile operation of continuous stirred tank reactor (CSTR) augmented with Clostridium butyricum and fed with sugarcane juice was studied at various hydraulic retention time (HRT). The maximum hydrogen production rate and yield of 3.38 mmol H₂/L/h and 1.0 mol H₂/mol hexose consumed, respectively, were achieved at HRT 4 h. The relationship of the augmented microorganism and normal flora in the fermentation system under non-sterile condition were analyzed by polymerase chain reaction-denaturing gradient gel electrophoresis (PCR-DGGE). Initially, at HRT 36 h, other species related to Lactobacillus harbinensis and Klebseilla pneumoniae were present as a major group in the reactor. When HRT was decreased to 12, 6 and 4 h, C. butyricum was present with a competition between L. harbinensis and K. pneumoniae. Results indicated that augmented C. butyricum could compete with contaminated microorganisms during non-sterile operation at low HRT (12-4 h) with the support of normal flora (K. pneumoniae).     

Isolation of Clostridium perfringens strain W11 and optimization of its biohydrogen production by genetic modification

Clostridium perfringens strain W11, which we previously identified as the major hydrogen producer in a hydrogen-producing microbial flora, was isolated in this study. The hydrogen yield from sucrose of this strain was 1.53 mol H₂/mol hexose. To exclude potential safety problems, the plc gene, encoding an alpha toxin protein, was permanently knocked out using the Targetron gene knockout system, creating strain W12. Strains W11 and W12 both produced lactate, acetate, and butyrate during hydrogen production. Furthermore, yields of these metabolites and hydrogen were near-identical by the two strains. When the ldh gene encoding lactate dehydrogenase in strain W12 was deleted, the hydrogen yield and acetate and butyrate concentrations in the resulting mutant, W13, increased by 51%, 26%, and 57%, respectively. Lactate production by strain W13 decreased almost to zero. The growth rates of the wild-type strain W11 and its mutant derivatives were similar.     

The effect of dilution and l-malic acid addition on bio-hydrogen production with Rhodopseudomonas palustris from effluent of an acidogenic anaerobic reactor

In this study, H₂ was produced from cheese whey wastewater in a two-stage biological process: i) first stage; thermophilic dark fermentation ii) second stage; the photo fermentation using Rhodopseudomonas palustris strain DSM 127 (R. palustris). The effect of both dilution and addition of l-malic acid on the hydrogen production was investigated. Among the dilution rates used, 1/5 dilution ratio was found to produce the best hydrogen production (349 ml H₂/g COD_fed). On the other hand, It was seen that the mixing the effluent with l-malic acid at increasing ratios had further positive effect and improved the hydrogen production significantly. It was concluded that dilution of the feeding helps to reduce the nitrogen content and the volatile fatty acid content that might be otherwise harmful to the photo-heterotrophic organisms. Overall hydrogen production yield (for dark + photo fermentation) was found to vary 2 and 10 mol H₂/mol lactose. Second conclusion is that cheese whey effluent should be mixed with a co-substrate containing l-malic acid such as apple juice processing effluents before fed into the photo fermentation reactor.     

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).     

Regulation of hydrogen production by Enterobacter aerogenes by external NADH and NAD

Experiments involving the addition of external nicotinamide adenine dinucleotide, reduced form (NADH) or nicotinamide adenine dinucleotide (NAD⁺) have been designed to examine how the hydrogen in Enterobacter aerogenes is liberated by NADH or NAD⁺. The addition of external NADH or NAD⁺ was found to regulate hydrogen production by E. aerogenes in resting cells, batch cultures, and chemostat cultures. Particularly in chemostat cultivation, with the external addition of NADH, hydrogen production via the NADH pathway was decreased, while that via the formate pathway was increased; in the end, the overall hydrogen p was decreased. The addition of NAD⁺, on the other hand, gave the opposite results. The membrane-bound hydrogenase was found to play a central role in regulating hydrogen production. The occurrence of NADH oxidation (NAD⁺ reduction) on the cell membrane resulted in an electron flow across the membrane; this changed the oxidation state and metabolic pattern of the cells, which eventually affected the hydrogen evolution.     

Comparison of metabolic pathway for hydrogen production in wild-type and mutant Clostridium tyrobutyricum strain based on metabolic flux analysis

There has been a great interest in fermentative hydrogen production during recent decades. However, the low H₂ yield associated with fermentative hydrogen production process continues to hinder its industrial application. It is delectable that a maximum 3.9 mol H₂ per mol glucose was obtained in fed-batch fermentation mode with a butyric acid over-producing Clostridium tyrobutyricum mutant, which to our knowledge is the highest H₂ yield ever got in the fermentation process with Clostridium sp. This study aimed to better understand the change of flux profile within the whole metabolic network and to conduct the metabolic flux analysis of fermentative hydrogen production. For the first time, we constructed a metabolic flux model for the anaerobic glucose metabolism of C. tyrobutyricum ATCC 25755, and revealed the internal mechanism responsible for the redistribution of the carbon flux in the mutant strain in comparison with the wide-type. The MFA methodology was used to study the fractional flux response to variations in operational pH, and revealed that pH was a significant operational parameter effecting on the fermentative hydrogen production process. Furthermore, the presence of NADH-ferredoxin oxidoreductase activity in this anaerobe was demonstrated. By measuring the activities of related enzymes in the biosynthesis pathway of hydrogen, we thus concluded that the increased specific activities of both NFOR and hydrogen-catalyzing enzyme (hydrogenase) would be attributed to the hydrogen over-producing.     

Metabolic flux analysis of hydrogen production network by Clostridium butyricum W5: Effect of pH and glucose concentrations

Fermentative hydrogen production by strict anaerobes has been widely reported. There is a lack of information related to metabolic flux distribution and its variation with respect to fermentation conditions in the metabolic production system. This study aimed to get a better understanding of the metabolic network and to conduct metabolic flux analysis (MFA) of fermentative hydrogen production by a recently isolated Clostridium butyricum strain W5. We chose the specific growth rate as the objective function and used specific H₂ production rate as the criterion to evaluate the experimental results with the in silico MFA. For the first time, we constructed an in silico metabolic flux model for the anaerobic glucose metabolism of C. butyricum W5 with assistance of a modeling program MetaFluxNet. The model was used to evaluate metabolic flux distribution in the fermentative hydrogen production network, and to study the fractional flux response to variations in initial glucose concentration and operational pH. The MFA results suggested that pH has a more significant effect on hydrogen production yield compared to the glucose concentration. The MFA is a useful tool to provide valuable information for optimization and design of the fermentative hydrogen production process.     

The effect of landfill leachate on hydrogen production in Chlamydomonas reinhardtii as monitored by PAM Fluorometry

This study investigated the effect of landfill leachate on biomass and biohydrogen production from Chlamydomonas reinhardtii. Maximum biomass and cell viability was recorded in 16% leachate medium with a corresponding growth rate of 927 μg/L chl a d⁻¹ as compared to the control of 688 μg/L chl a d⁻¹. Chlamydomonas cultured in leachate-supplemented medium was subsequently induced to produce 37% more biohydrogen compared to the control culture. The spurge in growth can be a consequence of abundant essential elements in the diluted leachate. Energy Dispersive X-ray analysis of cells in a 16% leachate medium had the highest accumulation of Cr, Mn, Fe, Co, Ni, Mo and Cd. The benefits of the leachate medium were further shown during the hydrogen production phase using Pulse Amplitude Modulated Fluorometry. This period was extended to 8 days in comparison to the control. Leachate therefore increases both the biomass and biohydrogen yield of Chlamydomonas.     

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.     

Bioproduction of hydrogen by simultaneous saccharification and fermentation of cassava starch with 2-deoxyglucose-resistant mutant strains of Clostridium tyrobutyricum

Laboratory mutagenesis of microorganisms offers the possibility of relating acquired mutations to improve the quality of microbial cultures. In the present study, a mutant strain, Clostridium tyrobutyricum ATCC 25755 DG-8, with significantly elevated α-amylase activity as well as resistant to the non-metabolizable and toxic glucose analog 2-deoxyglucose (2-DG) was obtained by implanting the low-energy nitrogen ion beam. DG-8 was further developed to produce hydrogen by simultaneous saccharification and fermentation (SSF) directly form cassava starch in batch fermentation mode, which to our knowledge is at the first attempt in genus Clostridium. Our results demonstrated that the increased activity of α-amylase would be attributed to the hydrogen over-producing. Higher hydrogen yield (3.2 mol/mol glucose) was achieved with the volumetric productivity of 0.41 L/h/L when the initial total sugar concentration of cassava starch rise up to 100 g/L. The present work will help to decrease the cost of hydrogen fermentation process and stimulate its industrial application in the near future.     

Evaluation of the influence of CO2 on hydrogen production by Caldicellulosiruptor saccharolyticus

Stripping gas is generally used to improve hydrogen yields in fermentations. Since CO₂ is relatively easy to separate from hydrogen it could be an interesting stripping gas. However, a higher partial CO₂ pressure is accompanied with an increased CO₂ uptake in the liquid, where it hydrolyses and induces an increased requirement of NaOH to maintain the pH. This enhances the osmotic pressure in the culture by 30%, which inhibited the growth of Caldicellulosiruptor saccharolyticus. Indications for this conclusion are: i) Inhibition could almost completely be circumvented by reducing the bicarbonate through decreasing the pH (from 6.5 to 5.5), ii) Growth rates were reduced by 60 ± 10% at an osmotic pressure of 0.218 ± 0.005 osm/kg H₂O independently of the stripping gas, iii) Increased extracellular DNA and protein concentrations were observed as a function of the osmotic pressure. In addition to growth inhibition, the increased sodium bicarbonate in the effluent will contribute to a negative environmental impact when applied at industrial scale.     

The effect of nutrient limitation on hydrogen production by batch cultures of Escherichia coli

In order to understand some limiting factors in microbial hydrogen fermentation we have examined hydrogen production by different strains of Escherichia coli grown in batch cultures under different limiting nutrient regimes. The effect of mutations in uptake hydrogenases, in lactate dehydrogenase (ldhA), and fhlA, coding for the regulator of formate hydrogen lyase (fhl) component synthesis, were studied. Each mutation contributed to a modest increase in hydrogen evolution and the effects were synergistic. Various elements were used as limiting nutrient. In batch experiments, limitation for sulfate was without great effect. There was some affect of limiting phosphate with yields approaching 1 mol per mol of glucose. However, strains showed the highest yield of hydrogen per glucose (∼2$\sim 2$) when cultured at limiting concentrations of either ammonia or glucose.