Cell growth and hydrogen production on the mixture of xylose and glucose using a novel strain of Clostridium sp. HR-1 isolated from cow dung compost

A novel mesophilic hydrogen-producing bacterium was isolated from cow dung compost and designated as Clostridium sp. HR-1 by 16S rRNA gene sequence. The optimum condition for hydrogen production by strain HR-1 was pH of 6.5, temperature of 37 °C and yeast extract as nitrogen sources. The strain HR-1 has the ability to utilize kinds of hexose and pentose as carbon sources for growth and H₂ production. Cell growth and hydrogen productivity were investigated for batch fermentation on media containing different ratios of xylose and glucose. Glucose was the preferred substrate in the glucose and xylose mixtures. The high glucose fraction had higher cell biomass production rate. The rate of glucose consumption was higher than xylose consumption, and remained essentially constant independent of xylose content of the mixture. The rate of xylose utilization was decreased with increasing of the glucose fraction. The average H₂ yield and specific H₂ production rates with xylose and glucose are 1.63 mol-H₂/mol xylose and 11.14-H₂ mmol/h g-cdw, and 2.02 mol-H₂/mol-glucose and 9.37 mmol-H₂/h g-cdw, respectively. Using the same initial substrate concentration, the maximum average H₂ yield and specific H₂ production rates with the mixtures of 9 g/l xylose and 3 g/l glucose was 2.01 mol-H₂/mol-mixed sugar and 12.56 mmol-H₂/h g-cdw, respectively. During the fermentation, the main soluble microbial products were ethanol and acetate which showed trends with the different ratios of xylose and glucose.     

Thermophilic hydrogen fermentation using Thermotoga neapolitana DSM 4359 by fed-batch culture

Biohydrogen fermentation by the hyperthermophile Thermotoga neapolitana was conducted in a continuously stirred anaerobic bioreactor (CSABR). The production level of H₂ from fermentation in a batch culture with pH control was much higher than without pH control from pentose (xylose) and hexose (glucose and sucrose) substrates. The respective H₂ yield in the batch culture with pH control from xylose and glucose was 2.22 ± 0.11 mol-H₂ mol⁻¹ xylose_consumed and 3.2 ± 0.16 mol-H₂ mol⁻¹ glucose_consumed, which was nearly 1.2-fold greater for xylose and 1.6-fold greater for glucose than without pH control. In the case of sucrose, the H₂ yield from fermentation increased by 40.63%, compared with fermentation in batch cultures without pH control, from 3.52 ± 0.171 to 4.95 ± 0.25 mol-H₂ mol⁻¹ sucrose_consumed. The effects of stirring speed and different pH levels on growth and H₂ production were studied in the CSABR for highly efficient H₂ production. Growth and H₂ production of this bacterial strain in a batch culture with pH control or without pH control using a 3 L bioreactor was limited within 24 h due to substrate exhaustion and a decrease in the culture’s pH. The pH-controlled fed-batch culture with a xylose substrate added in doses was studied for the prevention of substrate-associated growth inhibition by controlling the nutrient supply. The highest H₂ production rates were approximately 4.6, 4.1, 3.9, and 4.3 mmol-H₂ L⁻¹ h⁻¹ at 32, 52, 67, and 86 h, respectively.     

Phototrophic hydrogen production from acetate and butyrate in wastewater

Phototrophic hydrogen production was conducted using individual substrates, acetate and butyrate, which are the main products of dark fermentation. Effects of initial pH (ranging 5.0–10.0) and individual substrate concentrations (acetate ranging from 800 to 4100 mg/l, and butyrate ranging from 1000 to 5100 mg/l) on phototrophic hydrogen production were evaluated. The maximum hydrogen yields were 2.5 mol-H₂/mol-acetate at an initial pH of 8.0 treating 800 mg/l of acetate, 3.7 mol-H₂/mol-butyrate at an initial pH of 9.0 treating 1000 mg/l of butyrate. Analyses of DGGE (denaturing gradient gel electrophoresis) profiles of 16S rDNA fragments and FISH (fluorescent in situ hybridization) images show that both phototrophic hydrogen-producing sludges comprised only one predominant species resembling Rhodobacter capsulatus with over 80% relative abundance.     

Fermentative hydrogen production from different sugars by Citrobacter sp. CMC-1 in batch culture

In this study, production of hydrogen (H₂) from glucose, xylose, galactose, mannose, arabinose and rhamnose by a strain isolated from activated sludge was investigated. The strain, named as Citrobacter sp. CMC-1, was enriched in cellobiose amended minimal media. Based on 16S rRNA sequence, the CMC-1 strain is a close relative of Citrobacter amalonaticus strain SA01 (99%). Optimal cultivation parameters for H₂ production and growth such as pH and temperature were investigated. H₂ yields from glucose at optimal conditions (pH 6.0 and 34 °C) were 1.82 ± 0.02 mol-H₂/mol-glucose. Strain CMC-1 fermented galactose, mannose, xylose, arabinose and rhamnose. After 48 h incubation, the strain CMC-1 completely fermented all sugars tested, except arabinose. Increase in fermentation period lowered residual formate level in the media and improved H₂ production for galactose, mannose and xylose (1.68 ± 0.24, 1.93 ± 0.14 and 1.63 ± 0.07 mol-H₂/mol-substrate respectively).     

Effect of pH on glucose and starch fermentation in batch and sequenced-batch mode with a recently isolated strain of hydrogen-producing Clostridium butyricum CWBI1009

This paper reports investigations carried out to determine the optimum culture conditions for the production of hydrogen with a recently isolated strain Clostridium butyricum CWBI1009. The production rates and yields were investigated at 30 °C in a 2.3 L bioreactor operated in batch and sequenced-batch mode using glucose and starch as substrates. In order to study the precise effect of a stable pH on hydrogen production, and the metabolite pathway involved, cultures were conducted with pH controlled at different levels ranging from 4.7 to 7.3 (maximum range of 0.15 pH unit around the pH level). For glucose the maximum yield (1.7 mol H₂ mol⁻¹ glucose) was measured when the pH was maintained at 5.2. The acetate and butyrate yields were 0.35 mol acetate mol⁻¹ glucose and 0.6 mol butyrate mol⁻¹ glucose. For starch a maximum yield of 2.0 mol H₂ mol⁻¹ hexose, and a maximum production rate of 15 mol H₂ mol⁻¹ hexose h⁻¹ were obtained at pH 5.6 when the acetate and butyrate yields were 0.47 mol acetate mol⁻¹ hexose and 0.67 mol butyrate mol⁻¹ hexose.     

Hydrogen and ethanol fermentation of various carbon sources by immobilized Escherichia coli (XL1-Blue)

In this study, hydrogen and ethanol production by a facultative anaerobic bacterium Escherichia coli XL1-Blue immobilized in calcium-alginate beads have been investigated. Batch fermentations were carried out at mesophilic temperature (35 °C) and an initial cultivation pH of 6.5. Firstly, the influence of biomass concentration in terms of dry cell weight (expressed in g DCW/L, range 0.2–1.0) was investigated using fructose (5 g/L) as a carbon source. The peak hydrogen yield (HY) of 1.17 mol-H₂/mol-fructose_utilized was obtained at an initial cell concentration of 0.4 g DCW/L. The hydrogen production potential of other simple carbon sources (glucose and xylose) was evaluated at this optimized cell concentration and peak HY values were attained as 0.96 mol-H₂/mol-glucose_utilized and 0.69 mol-H₂/mol-xylose_utilized, respectively. In addition, utilization of the beverage wastewater (BWW) showed the peak cumulative hydrogen production and ethanol concentration of 120 mL and 5.65 g/L, attained at the substrate concentration of 20 g_{(glucose equivalent)}/L. However, peak HY (1.65 mol-H₂/mol-_{glucose eqivalent utilized}) was observed at low substrate concentration of 5 g_{(glucose equivalent)}/L. The percentage of sugar utilization of BWW was ranged between 80 and 96.     

Behavior of single chambered mediatorless microbial fuel cell (MFC) at acidophilic, neutral and alkaline microenvironments during chemical wastewater treatment

Single chamber mediatorless microbial fuel cell (MFC; non-catalyzed graphite electrodes; open air cathode) behaviour was evaluated under different pH microenvironments [acidophilic (pH 6), neutral (pH 7) and alkaline (pH 8)] during chemical wastewater treatment employing anaerobic mixed consortia as anodic biocatalyst at room temperature (29 ± 2 °C). The performance was found to depend on the feed pH used. Higher current density was observed at acidophilic conditions [pH 6; 186.34 mA/m²; 100 Ω] compared to neutral [pH 7; 146.00 mA/m²; 100 Ω] and alkaline [pH 8; 135.23 mA/m²; 100 Ω]. On the contrary, substrate degradation was found to be effective at neutral pH conditions (ξ_COD – 58.98%; SDR – 0.67 kg COD/m³-day) followed by alkaline (ξ_COD – 55.76%; SDR – 0.62 kg COD/m³-day) and acidophilic (ξ_COD of 47.80%; SDR 0.58 kg COD/m³-day) conditions studied. However, relatively higher specific power yield was observed at acidophilic microenvironment (46 mW/kg COD_R) compared to neutral (35 mW/kg COD_R) and alkaline (34 mW/kg COD_R) conditions. The behaviour of the MFC was also evaluated employing electron discharge, cyclic voltammetry, cell potentials, Coulombic efficiency and sustainable power analysis. Acidophilic operation showed higher Coulombic efficiency and effective electron discharge at relatively higher resistance compared to neutral and alkaline conditions studied.     

Hydrogen production from rice winery wastewater in an upflow anaerobic reactor by using mixed anaerobic cultures

Continuous production of hydrogen from the anaerobic acidogenesis of a high-strength rice winery wastewater by a mixed bacterial flora was demonstrated. The experiment was conducted in a 3.0-l upflow reactor to investigate individual effects of hydraulic retention time (HRT) (2–24 h), chemical oxygen demand (COD) concentration in wastewater (14–36 g COD/l), pH (4.5–6.0) and temperature (20–55°C) on bio-hydrogen production from the wastewater. The biogas produced under all test conditions was composed of mostly hydrogen (53–61%) and carbon dioxide (37–45%), but contained no detectable methane. Specific hydrogen production rate increased with wastewater concentration and temperature, but with a decrease in HRT. An optimum hydrogen production rate of 9.33 lH₂/gVSSd was achieved at an HRT of 2 h, COD of 34 g/l, pH 5.5 and 55°C. The hydrogen yield was in the range of 1.37–2.14 mol/mol-hexose. In addition to acetate, propionate and butyrate, ethanol was also present in the effluent as an aqueous product. The distribution of these compounds in the effluent was more sensitive to wastewater concentration, pH and temperature, but was less sensitive to HRT. This upflow reactor was shown to be a promising biosystem for hydrogen production from high-strength wastewaters by mixed anaerobic cultures.     

Xylose fermentation to biofuels (hydrogen and ethanol) by extreme thermophilic (70 °C) mixed culture

Combined biohydrogen and bioethanol (CHE) production from xylose was achieved by an extreme thermophilic (70 °C) mixed culture. Effect of initial pH, xylose, peptone, FeSO₄, NaHCO₃, yeast extract, trace mineral salts, vitamins, and phosphate buffer concentrations on bioethanol and biohydrogen yield was investigated in batch experiments. Results obtained showed that initial pH, concentration of xylose, peptone, and FeSO₄ significantly affected biohydrogen and bioethanol production, while the concentration of NaHCO₃ was only significant for bioethanol production. By changing cultivation conditions the culture could be directed to mainly produce ethanol with maximum ethanol yield of 1.60 mol ethanol/mol-xylose corresponding to 95.8% of the theoretical ethanol yield based on degradation of xylose through ethanologenic pathway, or mainly hydrogen with maximum hydrogen yield of 1.84 mol H₂/mol-xylose corresponding to 55% of the theoretical hydrogen yield based on acetate metabolic pathway. An empirical model was established to reveal the quantitative effect of factors significant for biohydrogen (quadratic model) production and for bioethanol (linear model) production. Changes in hydrogen/ethanol yields observed were due to the shift of the metabolic pathway between ethanol or hydrogen production, rather than changes in bacterial community composition at genus level. Thermoanaerobacter related bacteria were found to be the dominant hydrogen/ethanol producers.     

Selective inhibition of methanogens for the improvement of biohydrogen production in microbial electrolysis cells

The microbial electrolysis cell (MEC) is a promising technology for producing biohydrogen at greater yield than with conventional technology. However, during a run of an acetate-fed MEC at an applied voltage of 0.5 V, substantial amounts of substrate are consumed in undesirable methanogenesis. Therefore, in order to suppress the methanogens specifically without adversely affecting exoelectrogens, this study examined the effects of sudden changes in pH, temperature and air-exposure, as well as chemical inhibitors, such as 2-bromoethanesulfonate (BES) and lumazine on methanogenesis. An abrupt decrease in temperature and pH from 30 to 20 °C and 7 to 4.9, respectively, had no effect on methanogenesis. Exposing the anode biofilm to air was also ineffective in inhibiting specific methanogens because both methanogens and exoelectrogens were damaged by oxygen. However, an injection of BES (286 μM) reduced the methanogenic electron losses substantially from 36.4 ± 4.4 (= 145.8 ± 17.4 μmol-CH₄) to 2.5 ± 0.3% (= 10.2 ± 1.2 μmol-CH₄), which in turn improved the overall hydrogen efficiency (acetate to H₂) from 56.1 ± 5.7 to 80.1 ± 6.5% (= 3.2 mol-H₂/mol-acetate). Once after inhibited, the inhibitory influence was retained even after 10 batch cycles in the absence of further BES addition. In contrast to BES, methanogenesis was unaffected by lumazine, even at much higher concentrations. The installation of a Nafion membrane resulted in the production of high purity hydrogen at the cathode but hindered proton migration, which caused a serious pH imbalance between the anode and cathode compartments.     

Enhancement of fermentative hydrogen/ethanol production from cellulose using mixed anaerobic cultures

Batch tests were conducted to evaluate the enhancement of hydrogen/ethanol (EtOH) productivity using cow dung microflora to ferment α-cellulose and saccharification products (glucose and xylose). Hydrogen/ethanol production was evaluated based on hydrogen/ethanol yields (HY/EY) under 55 °C at various initial pH conditions (5.5–9.0). Our test results indicate that cow dung sludge is a good mixed natural-microflora seed source for producing biohydrogen/ethanol from cellulose and xylose. The heat-pretreatment, commonly used to produce hydrogen more efficiently from hexose, applied to mixed anaerobic cultures did not help cow dung culture convert cellulose and xylose into hydrogen/ethanol. Instead of heat-pretreatment, the mixed culture received enrichments cultivated at 55 °C for 4 days. Positive results were observed: hydrogen/ethanol production from fermenting cellulose and xylose was effectively enhanced at increases of 4.8 (ethanol) to 8 (hydrogen) and 2.4 (ethanol) to 15.6 (hydrogen) folds, respectively. In which, the ethanol concentration produced from xylose reached 4–4.4 g/L, an output comparable to that of using heat-treated sewage sludge and better than that (1.25–3 g/L) using pure cultures. Our test results show that for the enriched cultures the initial cultivation pH can affect hydrogen/ethanol production including HY, EY and liquid fermentation product concentration and distribution. These results were also concurred using a denaturing gradient gel electrophoresis analysis saying that both cultivation pH and substrate can affect the enriched cow dung culture microbial communities. The enriched cow dung culture had an optimal initial cultivation pH range of 7.6–8.0 with peak HY/EY values of 2.8 mmol-H₂/g-cellulose, 5.8 mmol-EtOH/g-cellulose, 0.3 mol-H₂/mol-xylose and 1 mol-EtOH/mol-xylose. However, a pH change of 0.5 units from the optimal values reduced hydrogen/ethanol production efficiency by 20%. Strategies based on the experimental results for optimal hydrogen/ethanol production from cellulose and xylose using cow dung microflora are proposed.     

Biohydrogen production from mixed xylose/arabinose at thermophilic temperature by anaerobic mixed cultures in elephant dung

Biohydrogen production by batch fermentation of mixed xylose/arabinose at thermophilic temperature using anaerobic mixed cultures in elephant dung as the seed inoculums was investigated. Elephant dung was heat-treated in boiling water for 2 h before used as the seed inoculum in order to inhibit methanogenic activity. Biohydrogen was successfully produced from mixed xylose/arabinose. The optimum conditions for hydrogen production were the initial concentration of mixed xylose/arabinose 5 g/L each, initial cultivation pH 5.5 and temperature 55 °C. Under the optimum conditions, a maximum hydrogen yield of 2.49 mol-H₂/mol-sugar consumed was obtained. The optimum conditions were then used to produce hydrogen from sugar derived from acid-hydrolysed sugarcane bagasse (SCB) at a reducing sugar concentration of 10 g/L in which a lower hydrogen yield of 1.48 mol-H₂/mol-sugar consumed was achieved. Main soluble product was acetate suggesting the hydrogen fermentation from mixed xylose/arabinose is the acetate type. The dominant hydrogen producers found in both fermentation broth were Thermoanaerobacterium thermosaccharolyticum and Clostridium sp. Lower hydrogen yield in the SCB hydrolysate fermentation broth may be due to the present of Clostridium ragsdalei and microorganisms in the class Bacilli viz. Lactococus lactis subsp., Lactobacillus delbrueckii, and Sporolactobacillus sp. as well as the inhibitors (acetic acid and furfural) contained in the SCB hydrolysate.     

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.     

Comparative kinetic modeling of growth and molecular hydrogen overproduction by engineered strains of Thermotoga maritima

Thermotoga maritima is an anaerobic hyperthermophilic bacterium known for its high amounts of hydrogen (H₂) production. In the current study, the kinetic modeling was applied on the engineered strains of T. maritima that surpassed the natural H₂ production limit. The study generated a kinetic model explaining H₂ overproduction and predicted a continuous fermentation system. A Leudking-Piret equation-based model predicted that H₂ production by Tma200 (0.217 mol-H₂ g⁻¹-biomass) and Tma100 (0.147 mol-H₂ g⁻¹-biomass) were higher than wild type (0.096 mol-H₂ g⁻¹ -biomass) with reduced rates of maltose utilization. Sensitivity analysis confirmed satisfactory fitting of the experimental data. The slow growth rates of Tma200 (0.550 h⁻¹) and Tma100 (0.495 h⁻¹) are compared with the wild type (0.663 h⁻¹). A higher maintenance energy along with growth and non-growth H₂ coefficients corroborate the higher H₂ productivity of the engineered strains. The modeled data established a continuous fermentation system for the sustainable H₂ production.     

Characterization of Pr1−xSrxCo0.8Fe0.2O3−δ (0.2 ≤ x ≤ 0.6) cathode materials for intermediate-temperature solid oxide fuel cells

Cathode materials consisting of Pr_1−xSr_xCo_0.8Fe_0.2O_3−δ (x = 0.2–0.6) were prepared by the sol–gel process for intermediate-temperature solid oxide fuel cells (IT-SOFCs). The samples had an orthorhombic perovskite structure. The electrical conductivities were all higher than 279 S cm⁻¹. The highest conductivity, 1040 S cm⁻¹, was found at 300 °C for the composition x = 0.4. Symmetrical cathodes made of Pr_0.6Sr_0.4Co_0.8Fe_0.2O_3−δ (PSCF)–Ce_0.85Gd_0.15O_1.925 (50:50 by weight) composite powders were screen-printed on GDC electrolyte pellets. The area specific resistance value for the PSCF–GDC cathode was as low as 0.046 Ω cm² at 800 °C. The maximum power densities of a cell using the PSCF–GDC cathode were 520 mW cm⁻², 435 mW cm⁻² and 303 mW cm⁻² at 800 °C, 750 °C and 700 °C, respectively.     

High-yield biohydrogen production from biodiesel manufacturing waste by Thermotoga neapolitana

Efficient conversion of glycerol waste from biodiesel manufacturing processes into biohydrogen by the hyperthermophilic eubacterium Thermotoga neapolitana DSM 4359 was investigated. Biohydrogen production by T. neapolitana was examined using the batch cultivation mode in culture medium containing pure glycerol or glycerol waste as the sole substrate. Pre-treated glycerol waste showed higher hydrogen (H₂) production than untreated waste. Nitrogen (N₂) sparging and pH control were successfully implemented to maintain the culture pH and to reduce H₂ partial pressure in the headspace for optimal growth rate and to enhance hydrogen production from the glycerol waste. It was found that hydrogen production increased from 1.24 ± 0.06 to 1.98 ± 0.1 mol-H₂ mol⁻¹ glycerol_consumed by optimising N₂ sparging and pH control. We observed that in medium containing 0.05 M HEPES, with three cycles of N₂ sparging, the H₂ yield increased to 2.73 ± 0.14 mol-H₂ mol⁻¹ glycerol_consumed, which was 2.22-fold higher than the non-N₂ sparged H₂ yield (1.23 ± 0.06 mol-H₂ mol⁻¹ glycerol_consumed).     

Hydrogen production from the monomeric sugars hydrolyzed from hemicellulose by Enterobacter aerogenes

Relatively large percentages of xylose with glucose, arabinose, mannose, galactose and rhamnose constitute the hydrolysis products of hemicellulose. In this paper, hydrogen production performance of facultative anaerobe (Enterobacter aerogenes) has been investigated from these different monomeric sugars except glucose. It was shown that the stereoisomers of mannose and galactose were more effective for hydrogen production than those of xylose and arabinose. The substrate of 5 g/l xylose resulted in a relative high level of hydrogen yield (73.8 mmol/l), hydrogen production efficiency (2.2 mol/mol) and a maximum hydrogen production rate (249 ml/l/h). The hydrogen yield, hydrogen production efficiency and the maximum hydrogen production rate reached 104 mmol/l, 2.35 mol/mol and 290 ml/l/h, respectively, on a substrate of 10 g/l galactose. The hydrogen yields and the maximum hydrogen production rates increased with an increase of mannose concentrations and reached 119 mmol/l and 518 ml/l/h on the culture of 25 g/l mannose. However, rhamnose was a relative poor carbon resource for E. aerogenes to produce hydrogen, from which the hydrogen yield and hydrogen production efficiency were about one half of that from the mannose substrate. E. aerogenes was found to be a promising strain for hydrogen production from hydrolysis products of hemicellulose.     

Biohydrogen production from xylose by Thermoanaerobacterium thermosaccharolyticum KKU19 isolated from hot spring sediment

A thermophilic hydrogen producer was isolated from hot spring sediment and identified as Thermoanaerobacterium thermosaccharolyticum KKU19 by biochemical tests and 16S rRNA gene sequence analysis. The strain KKU19 showed the ability to utilize various kinds of carbon sources. Xylose was the preferred carbon source while peptone was the preferred organic nitrogen source. The optimum conditions for hydrogen production and cell growth on xylose were an initial pH of 6.50, temperature of 60 °C, a carbon to nitrogen ratio of 20:1, and a xylose concentration of 10.00 g/L. This resulted in a maximum cumulative hydrogen production, hydrogen production rate and hydrogen yield of 3020 ± 210 mL H₂/L, 3.95 ± 0.20 mmol H₂/L h and 2.09 ± 0.02 mol H₂/mol xylose consumed, respectively. Acetic and butyric acids were the main soluble metabolite products suggesting acetate and butyrate type fermentation.     

Thermophilic hydrogen production from cellulose with rumen fluid enrichment cultures: Effects of different heat treatments

Elevated temperatures (52, 60 and 65 °C) were used to enrich hydrogen producers on cellulose from cow rumen fluid. Methanogens were inhibited with two different heat treatments. Hydrogen production was considerable at 60 °C with the highest H₂ yield of 0.44 mol-H₂ mol-hexose⁻¹ (1.93 mol-H₂ mol-hexose-degraded⁻¹) as obtained without heat treatment and with acetate and ethanol as the main fermentation products. H₂ production rates and yields were controlled by cellulose degradation that was at the highest 21%. The optimum temperature and pH for H₂ production of the rumen fluid enrichment culture were 62 °C and 7.3, respectively. The enrichments at 52 and 60 °C contained mainly bacteria from Clostridia family. At 52 °C, the bacterial diversity was larger and was not affected by heat treatments. Bacterial diversity at 60 °C remained similar between heat treatments, but decreased during enrichment. At 60 °C, the dominant microorganism was Clostridium stercorarium subsp. leptospartum.     

La0.84Sr0.16MnO3−δ cathodes impregnated with Bi1.4Er0.6O3 for intermediate-temperature solid oxide fuel cells

La_0.84Sr_0.16MnO_3−δ–Bi_1.4Er_0.6O₃ (LSM–ESB) composite cathodes are fabricated by impregnating LSM electronic conducting matrix with the ion-conducting ESB for intermediate-temperature solid oxide fuel cells (IT-SOFCs). The performance of LSM–ESB cathodes is investigated at temperatures below 750 °C by AC impedance spectroscopy. The ion-impregnation of ESB significantly enhances the electrocatalytic activity of the LSM electrodes for the oxygen reduction reactions, and the ion-impregnated LSM–ESB composite cathodes show excellent performance. At 750 °C, the value of the cathode polarization resistance (R_p) is only 0.11 Ω cm² for an ion-impregnated LSM–ESB cathode, which also shows high stability during a period of 200 h. For the performance testing of single cells, the maximum power density is 0.74 W cm⁻² at 700 °C for a cell with the LSM–ESB cathode. The results demonstrate the ion-impregnated LSM–ESB is one of the promising cathode materials for intermediate-temperature solid oxide fuel cells.