Fermentative hydrogen production with xylose by Clostridium and Klebsiella species in anaerobic batch reactors

Hydrogen production was obtained from low concentrations of xylose metabolized by heat treated inoculum obtained from the slaughterhouse wastewater treatment UASB reactor installed in Brazil. The molecular biological analysis Clostridium and Klebsiella species, recognized as H₂ and volatile acid producers, in addition to Burkholderia species and uncultivated bacteria. The assays were carried out in batch reactors: (1) 630.0 mg xylose/L, (2) 1341.0 mg xylose/L, (3) 1848.0 mg xylose/L and (4) 3588.0 mg xylose/L. The following yields were obtained: 3% (0.2 mol H₂/mol xylose), 8% (0.5 mol H₂/mol xylose), 10% (0.6 mol H₂/mol xylose) and 14% (0.8 mol H₂/mol xylose), respectively. The end products obtained were acetic acid, butyric acid, methanol and ethanol in all of the anaerobic reactors. The concentrations of xylose did not inhibit microbial growth and hydrogen production. This suggested that low concentrations of xylose should be added to wastewater to produce hydrogen.     

Dark fermentative hydrogen production with crude glycerol from biodiesel industry using indigenous hydrogen-producing bacteria

Glycerol is an inevitable by-product from biodiesel synthesis process and could be a promising feedstock for fermentative hydrogen production. In this study, the feasibility of using crude glycerol from biodiesel industry for biohydrogen production was evaluated using seven isolated hydrogen-producing bacterial strains (Clostridium butyricum, Clostridium pasteurianum, and Klebsiella sp.). Among the strains examined, C. pasteurianum CH4 exhibited the best biohydrogen-producing performance under the optimal conditions of: temperature, 35 °C; initial pH, 7.0; agitation rate, 200 rpm; glycerol concentration, 10 g/l. When using pure glycerol as carbon source for continuous hydrogen fermentation, the average H₂ production rate and H₂ yield were 103.1 ± 8.1 ml/h/l and 0.50 ± 0.02 mol H₂/mol glycerol, respectively. In contrast, when using crude glycerol as the carbon source, the H₂ production rate and H₂ yield was improved to 166.0 ± 8.7 ml/h/l and 0.77 ± 0.05 mol H₂/mol glycerol, respectively. This work demonstrated the high potential of using biodiesel by-product, glycerol, for cost-effective biohydrogen production.     

Sugarcane vinasse as substrate for fermentative hydrogen production: The effects of temperature and substrate concentration

The present study aimed to evaluate the hydrogen production of a microbial consortium using different concentrations of sugarcane vinasse (2–12 g COD L⁻¹) at 37 °C and 55 °C. In mesophilic tests, the increase in vinasse concentration did not significantly impact the hydrogen yield (HY) (from 1.72 to 2.23 mmol H₂ g⁻¹ COD_influent) but had a positive effect on the hydrogen production potential (P) and hydrogen production rate (R_m). On the other hand, the increase in the substrate concentration caused a drop in HY from 2.31 to 0.44 mmol H₂ g⁻¹ COD_influent in the tests performed at 55 °C with vinasse concentrations from 2 to 12 g COD L⁻¹. The mesophilic community was composed of different species within the Clostridium genus, and the thermophilic community was dominated by organisms affiliated with the Thermoanaerobacter genus. Not all isolates affiliated with the Clostridium genus contributed to a high HY, as the homoacetogenic pathway can occur.     

Hydrogen production from soft-drink wastewater in an upflow anaerobic packed-bed reactor

The production of hydrogen from soft-drink wastewater in two upflow anaerobic packed-bed reactors was evaluated. The results show that soft-drink wastewater is a good source for hydrogen generation. Data from both reactors indicate that the reactor without medium containing macro- and micronutrients (R2) provided a higher hydrogen yield (3.5 mol H₂ mol⁻¹ of sucrose) as compared to the reactor (R1) with a nutrient-containing medium (3.3 mol H₂ mol⁻¹ of sucrose). Reactor R2 continuously produced hydrogen, whereas reactor R1 exhibited a short period of production and produced lower amounts of hydrogen. Better hydrogen production rates and percentages of biogas were also observed for reactor R2, which produced 0.4 L h⁻¹ L⁻¹ and 15.8% of H₂, compared to reactor R1, which produced 0.2 L h⁻¹ L⁻¹ and 2.6% of H₂. The difference in performance between the reactors was likely due to changes in the metabolic pathway for hydrogen production and decreases in bed porosity as a result of excessive biomass growth in reactor R1. Molecular biological analyses of samples from reactors R1 and R2 indicated the presence of several microorganisms, including Clostridium (91% similarity), Enterobacter (93% similarity) and Klebsiella (97% similarity).     

Microbial characterization of hydrogen-producing bacteria in fermented food waste at different pH values

An anaerobic fermentation of food waste was conducted in a 0.5 L bioreactor incubated at a thermophilic temperature of 55 °C to evaluate the effects of different controlled pH values (5.0, 5.5 and 6.0) on biohydrogen production. Effective biohydrogen production was found at controlled pH 5.5 and 6.0 corresponding to lower lactic acid production compared to pH 5.0. It was demonstrated that biohydrogen production from food waste was pH-dependent with hydrogen yields of 79, 76 and 23 mmol H₂/L-media/d for pH 5.5, 6.0 and 5.0, respectively. Specific microbial determination for Clostridium sp. and total bacteria quantification were carried out by the fluorescent in-situ hybridization (FISH) technique. The number of Clostridium sp. for acclimatized sludge, fermentation broth at pH 5.0, 5.5 and 6.0 were 2.9 × 10⁸, 3.6 × 10⁸, 7.8 × 10⁸ and 5.4 × 10⁸ cells/ml, respectively. The quantification analysis showed that 92% of the total bacteria belonged to Clostridium sp. from clusters I and XI from the sample at controlled pH 5.5. The denaturing gradient gel electrophoresis (DGGE) bands of the sample after heat-treatment, acclimatization and during fermentation indicated the presence of Bacteroidetes, Caloromator australicus sp. and Clostridium sp.     

Improvement of fermentative biohydrogen production by Clostridium butyricum CWBI1009 in sequenced-batch,horizontal fixed bed and biodisc-like anaerobic reactors with biomass retention

A horizontal tubular fixed bed bioreactor (HFBR) and an anaerobic biodisc-like reactor (AnBDR) were designed to both fix Clostridium biomass and enable rapid transfer of the hydrogen produced to gas phase in order to decrease the strong effect of H₂ partial pressure and H₂ supersaturation on the performances of Clostridium strains. The highest H₂ production rate (703 mL H₂/L h) and yield (302 mL/g glucose consumed i.e. 2.4 mol/mol) with the pure culture were recorded in the AnBDR with 300 mL culture medium (total volume 2.3 L) at pH 5.2 and a glucose loading rate of 2.87 g/L h. These results are about 2.3 and 1.3-fold higher than those achieved in the same bioreactor with 500 mL liquid medium and with the same glucose consumption rate. Therefore, our experimentations and a short review of the literature reported in this paper emphasize the relevance of performing bioreactors with high L/G transfer.     

Application of Clostridium-specific PCR primers on the analysis of dark fermentation hydrogen-producing bacterial community

Molecular method such as PCR-DGGE using well-accepted universal 16S rDNA PCR primer sets was often applied on the study of Clostridium bacterial community. However, unsatisfied results were often obtained due to the difficulty of distinguishing coexisting Clostridium and other anaerobic microorganisms. In this study, a specific PCR primer set (Chis150f–ClostIr), based on the available rRNA gene sequences from the database, targeting only the majority of Clusters I and II Clostridia was designed and tested on both the pure culture Clostridium and dark fermentation sludge. It was demonstrated that this new primer set could not only successfully distinguish the coexisted Clostridium species but also revealed the existence of some Clostridium species in the sludge which could not be detected by using the universal primer set. This method successfully provides a detailed view on the Clostridium community responsible for an effective hydrogen production in dark fermentation system.     

State estimation of a batch hydrogen production process using the photosynthetic bacteria Rhodobacter capsulatus

This paper addresses the problem of estimating the states of an anaerobic photosynthetic process used for biohydrogen production by the photosynthetic bacterium Rhodobacter capsulatus. The process is described by a non-linear, time-discrete model and the state estimation is solved using an observer based on the Moving-Horizon State Estimation Method (MHSE). This approach is based on the minimization of a criterion (a non-linear function), in this case, the difference between the estimated output and the measured output of the system over a considered time horizon, where the solution is computed by using a numerical interval method. The observer was successfully applied to hydrogen production by R. capsulatus strain B10 in a batch process.     

Changes in hydrogenase genetic diversity and proteomic patterns in mixed-culture dark fermentation of mono-, di- and tri-saccharides

Dark fermentation using mixed cultures is a promising biotechnology for producing hydrogen (H₂) from renewable organic waste at a low cost. The impact of the characteristics of carbohydrates was evaluated on H₂ production and the associated changes in clostridial populations. A series of H₂-producing batch experiments was performed from mono-, di- to tri-saccharides (i.e. fructose, glucose, sucrose, maltose, cellobiose, maltotriose). Both chain length and alpha- or beta-linkage of carbohydrates impacted H₂ production performance as well as the patterns of hydrogenases. The H₂ yield, ranging from 1.38 to 1.84 mol-H₂/mol-hexose, decreased with the increasing chain length of the carbohydrates, showing a negative effect of the hydrolysis step on H₂ production efficiency. Changes in H₂ yield were associated with a specialization of clostridial species, which used different metabolic routes. The rise in H₂ production was associated with butyrate and acetate increases while H₂ consumption was related to caproate formation. Both clostridial [FeFe]- and [NiFe]-hydrogenases were identified in cellobiose cultures by a proteomic approach. This is the first study that combines genetic and proteomic analyses focused on H₂-producing bacteria under various conditions and it opens very interesting perspectives to better understand and optimize H₂ production using mixed cultures.     

Biohydrogen production from cellobiose in phenol and cresol-containing medium using Clostridium sp. R1

Cellobiose fermentation in batch test using an isolated strain, Clostridium sp. R1, was investigated. The Clostridium sp. R1 achieved a maximum hydrogen yield of 3.5 mol H₂ mol⁻¹ cellobiose at pH 6 and 30 °C, higher than most yields reported in literature. This strain can generate hydrogen from a number of carbohydrates, including galactose, glucose, mannose, maltose, sucrose, and starch. This strain can also convert cellobiose to hydrogen in the presence of toxic phenol or cresol. The inhibition effects of phenolic compounds on strain R1 activity followed phenol > p-cresol > o-cresol > m-cresol. Co-culturing with another strain, Clostridium butyricum, can co-degrade some of the phenol as substrates. The new isolated strain can yield hydrogen from phenol-containing wastewaters.     

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.     

Alkali-treated sewage sludge as a seeding source for hydrogen fermentation of food waste leachate

In the present work, alkali-treated sewage sludge (SS) was used as a seeding source for H₂ fermentation of food waste leachate (FWL). The role of alkaline treatment of SS was to suppress the activity of non-H₂-producers in SS and also to enhance the solubility of SS. The effect of pretreatment pH and FWL:SS ratio on H₂ production was crucial, by changing the pH conditions and selecting the dominant species. High pretreatment pH and high SS content resulted in high initial pH conditions. The highest H₂ yield of 2.1 mol H₂/mol hexose_added was achieved at pretreatment pH 10 and a mixing ratio of FWL:SS = 3:5. At these conditions, the initial pH was 7.9, and cultivation pH was maintained within the reported optimum range of 5.5–6.5 during fermentation. It was found that pretreatment pH 9 was not strong enough to suppress the activity of non-H₂-producers in SS, in particular, lactic acid bacteria (LAB). Microbial analysis results confirmed that LAB such as Lactobacillus sp. and Enterococcus sp. were the dominant species at pretreatment pH 9 while Clostridium sp., the main anaerobic H₂-producers, were dominant at pretreatment pH 10.     

Expression of different types of [FeFe]-hydrogenase genes in bacteria isolated from a population of a bio-hydrogen pilot-scale plant

[FeFe]-hydrogenases are the enzymes responsible for high yield H₂ production during dark fermentation in bio-hydrogen production plants. The culturable bacterial population present in a pilot-scale plant efficiently producing H₂ from waste materials was isolated, classified and identified by means of 16S rDNA gene analysis. The culturable part of the mixed population consists of nine bacterial species that include non-hydrogen producers (Lactobacillus, Enterococcus and Staphylococcus) and several Clostridium that are directly responsible for H₂ production.     

Enhancement in hydrogen production by co-cultures of Bacillus and Enterobacter

Defined co-cultures of hydrogen (H₂) producers belonging to Citrobacter, Enterobacter, Klebsiella and Bacillus were used for enhancing the efficiency of biological H₂ production. Out of 11 co-cultures consisting of 2–4 strains, two co-cultures composed of Bacillus cereus EGU43, Enterobacter cloacae HPC123, and Klebsiella sp. HPC793 resulted in H₂ yield up to 3.0 mol mol⁻¹ of glucose. Up-scaling of the reactor by 16-fold resulted in a corresponding increase in H₂ production with an actual evolution of 7.44 L of H₂. It constituted 58.2% of the total biogas. Continuous culture evolution of H₂ by co-cultures (B. cereus EGU43 and E. cloacae HPC123) immobilized on ligno-cellulosic materials resulted in 6.4-fold improvement in H₂ yield compared to free floating bacteria. This synergistic influence of B. cereus and E. cloacae can offer a better strategy for H₂ production than undefined or mixed cultures.     

Ethanol production from enzymatic hydrolysis of sugarcane bagasse pretreated with lime and alkaline hydrogen peroxide

In this work we evaluated ethanol production from enzymatic hydrolysis of sugarcane bagasse. Two pretreatments agents, lime and alkaline hydrogen peroxide, were compared in their performance to improve the susceptibility of bagasse to enzymatic action. Mild conditions of temperature, pressure and absence of acids were chosen to diminish costs and to avoid sugars degradation and consequent inhibitors formation. The bagasse was used as it comes from the sugar/ethanol industries, without grinding or sieving, and hydrolysis was performed with low enzymes loading (3.50 FPU g⁻¹ dry pretreated biomass of cellulase and 1.00 CBU g⁻¹ dry pretreated biomass of ??-glucosidase). The pretreatment with alkaline hydrogen peroxide led to the higher glucose yield: 691 mg g⁻¹ of glucose for pretreated bagasse after hydrolysis of bagasse pretreated for 1 h at 25 °C with 7.35% (v/v) of peroxide. Fermentation of the hydrolyzates from the two pretreatments were carried out and compared with fermentation of a glucose solution. Ethanol yields from the hydrolyzates were similar to that obtained by fermentation of the glucose solution. Although the preliminary results obtained in this work are promising for both pretreatments considered, reflecting their potential for application, further studies, considering higher biomass concentrations and economic aspects should be performed before extending the conclusions to an industrial process.     

The effect of heat pretreatment temperature on fermentative hydrogen production using mixed cultures

The effect of heat treatment at different temperatures on two types of inocula, activated sludge and anaerobically digested sludge, was investigated in batch cultures. Heat treatments were conducted at 65, 80 and 95 °C for 30 min. The untreated inocula produced less amount of hydrogen than the pretreated inocula, with lactic acid as the main metabolite. The maximum yields of 2.3 and 1.6 mol H₂/mol glucose were achieved for the 65 °C pretreated anaerobically digested and activated sludges, respectively. Approximately a 15% decrease in yield was observed with increasing pretreatment temperature from 65 to 95 °C concomitant with an increase in butyrate/acetate ratio from 1.5 to 2.4 for anaerobically digested sludge. The increase of pretreatment temperature of activated sludge to 95 °C suppressed the hydrogen production by lactic acid fermentation. DNA analysis of the microbial community showed that the elevated pretreatment temperatures reduced the species diversity.     

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.     

Effect of changing temperature on anaerobic hydrogen production and microbial community composition in an open-mixed culture bioreactor

The temperature effect (37–65 °C) on H₂ production from glucose in an open-mixed culture bioreactor using an enrichment culture from a hot spring was studied. The dynamics of microbial communities was investigated by polymerase chain reaction-denaturing gradient gel electrophoresis (PCR-DGGE). At 45 and 60 °C the H₂ production was the highest i.e. 1.71 and 0.85 mol H₂/mol glucose, respectively. No H₂ was produced at temperatures 50 and 55 °C. At 37–45 °C, H₂ production was produced by butyrate type fermentation while fermentation mechanism changed to ethanol type at 60 °C. Clostridium species were dominant at 37–45 °C while at 50–55 °C and 60 °C the culture was dominated by Bacillus coagulans and Thermoanaerobacterium, respectively. In the presence of B. Coagulans the metabolism was directed to lactate production. The results show that the mixed culture had two optima for H₂ production and that the microbial communities and metabolic patterns promptly changed according to changing temperatures.     

Development and application of a functional CE-SSCP fingerprinting method based on [Fe–Fe]-hydrogenase genes for monitoring hydrogen-producing Clostridium in mixed cultures

A Capillary Electrophoresis Single Strand Conformation Polymorphism (CE-SSCP) method based on functional [Fe–Fe]-hydrogenase genes was developed for monitoring the hydrogen (H₂)-producing clostridial population in mixed-culture bioprocesses. New non-degenerated primers were designed and then validated on their specific PCR detection of a broad range of clostridial hydA genes. The hydA-based CE-SSCP method gave a specific and discriminating profile for each of the Clostridium strains tested. This method was validated using H₂-producing mixed cultures incubated at temperatures ranging from 25 °C to 45 °C. The hydA CE-SSCP profiles clearly differed between temperatures tested. Hence, they varied according to variations of the H₂ production performances. The HydA sequences amplified with the new primer set indicated that diverse Clostridium strains impacted the H₂ production yields. The highest performances were related to the dominance of Clostridium sporogenes-like hydA sequences. This CE-SSCP tool offers highly reliable and throughput analysis of the functional diversity and structure of the hydA genes for better understanding of the H₂-producing clostridial population dynamics in H₂ dark fermentation bioreactors.