Potential for using enriched cultures and thermotolerant bacterial isolates for production of biohydrogen from oil palm sap and microbial community analysis

A limited number of bacteria can convert oil palm (Elaeis guineensis) sap to hydrogen with satisfactory yield and productivity. In this study, a total of 18 fermentative enriched cultures and 36 newly isolated thermotolerant bacterial strains were compared for hydrogen production from oil palm (OP) sap. The new isolates were obtained from hot springs, palm oil mill effluent and oil palm sap. The test was conducted in three steps: (i) a test for hydrogen production from mixed substrates (cellulose, starch, xylose, and glucose) and OP sap; (ii) a test for substrate concentration tolerance; and (iii) a test for thermotolerance. Five enriched candidates for each of the hydrogen producers were selected according to the criteria defined for the screening test. The hydrogen production of these selected bacterial strains from hot springs were cultivated in batch fermentation of oil palm sap at room temperature (30 ± 2 °C). Five enriched cultures, namely 81RN1, OPS, 85RN5, 89SR3-2 and 112YL1 were found to give high cumulative hydrogen formation of 1085, 1009, 994, 983 and 778 mL H₂/L-OP sap, respectively, with the hydrogen content of 29.8, 29.4, 28.7, 27.1 and 27.5%, respectively. PCR–DGGE profiling showed that all these five enriched cultures consisted of species closely related to the genus Clostridium sp. based on the 16S rRNA gene. For pure cultures, the top five hydrogen producers were the isolates encoded as PS-3, PS-4, PS-5, PS-7 and PS-8 exhibiting the hydrogen production of 1973, 1774, 1335, 1170 and 1070 mL H₂/L-OP sap, respectively, with the hydrogen content of 33.7, 29.6, 32.5, 31.5 and 26.4%, respectively. Identification of these high hydrogen producers using 16S rRNA sequence matching showed that the isolates PS-3 and PS-8 belonged to Clostridium beijerinckii, while the isolate PS-7 belonged to Clostridium acetobutylicum and the isolates PS-4 and PS-5 belonged to Klebsiella sp. and Klebsiella pneumoniae, respectively. Therefore, the pure culture C. beijerinckii PS-3 exhibited 1.8 folds higher hydrogen production (1973 mL H₂/L-OP sap) than the enriched cultures of 81RN1 (1085 mL H₂/L-OP sap).     

Isolation and molecular characterization of hydrogenase gene from a high rate of hydrogen-producing bacterial strain Enterobacter cloacae IIT-BT 08

Degenerate PCR primers (forward as well as the reverse) were designed from the protein sequences of known structural genes encoding the catalytic subunits of Fe-hydrogenases obtained from NCBI Protein Sequence Database. Amino acid sequences were multiple aligned through CLUSTAL-W software and compared for conserved sequence motifs. Mole percent of G+C of the present strain is found to be 55% by thermal melting method. An amplified PCR product of 1 kb in size was obtained from the genomic DNA of Enterobacter cloacae IIT-BT 08 by using a set of (JM-1 and JM-12) degenerate primer. Gel purified PCR product was cloned in TOPO TA cloning vector (3.9 kb) and transformed into TOPOF’ cells. Initial experiment on Southern hybridization of the PCR product showed no homology with hydA gene of Clostridium acetobutylicum ATCC 824.     

Co-culture of Clostridium beijerinckii L9, Clostridium butyricum M1 and Bacillus thermoamylovorans B5 for converting yeast waste into hydrogen

In order to enhance anaerobic hydrogen production from yeast waste, a series of 120-mL batch co-cultures of Clostridium beijerinckii L9, Clostridium butyricum M1, and Bacillus thermoamylovorans B5 under mesophilic conditions were established according to full factorial design (FFD) and mixture design (MD). The experimental results were subjected to multivariate and response surface analyses to determine the relationships between bacteria converting yeast waste into hydrogen. The results indicated clearly that C. beijerinckii L9 and C. butyricum M1 had significant potential to convert yeast waste into hydrogen. There was no significant hydrogen generation when B. thermoamylovorancs B5 alone was cultured with yeast waste. However, B. thermoamylovorancs B5 could significantly shorten the co-culture’s hydrogen-producing lag phase. Response surface analyses demonstrate that B. thermoamylovorancs B5 can stimulate the specific hydrogen production rate of C. beijerinckii L9 and C. butyricum M1, greater in the case of the former than of the latter. An ultimate hydrogen yield of 46 mL H₂/g COD added yeast waste was obtained with an optimal volumetric ratio C. beijerinckii L9: C. butyricum M1: B. thermoamylovoranc B5 of 8.9:4.8:10.3. Highly reproducible co-culture results confirm that FFD and MD, via response surface analysis, are applicable to assess the roles of the individual microorganisms in the defined co-culture.     

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.     

Optimization of biohydrogen production by Clostridium butyricum EB6 from palm oil mill effluent using response surface methodology

Clostridium butyricum EB6 successfully produced hydrogen gas from palm oil mill effluent (POME). In this study, central composite design and response surface methodology were applied to determine the optimum conditions for hydrogen production (P_c) and maximum hydrogen production rate (R_max) from POME. Experimental results showed that the pH, temperature and chemical oxygen demand (COD) of POME affected both the hydrogen production and production rate, both individually and interactively. The optimum conditions for hydrogen production (P_c) were pH 5.69, 36 °C, and 92 g COD/l; with an estimated P_c value of 306 ml H₂/g carbohydrate. The optimum conditions for maximum hydrogen production rate (R_max) were pH 6.52, 41 °C and 60 g COD/l; with an estimated R_max value of 914 ml H₂/h. An overlay study was performed to obtain an overall model optimization. The optimized conditions for the overall model were pH 6.05, 36 °C and 94 g COD/l. The hydrogen content in the biogas produced ranged from 60% to 75%.     

Potential of hydrogen from oil palm biomass as a source of renewable energy worldwide

Various catastrophes related to extreme weather events such as floods, hurricanes, droughts and heat waves occurring on the Earth in the recent times are definitely a clear warning sign from nature questioning our ability to protect the environment and ultimately the Earth itself. Progressive release of greenhouse gases (GHG) such as CO₂ and CH₄ from development of various energy-intensive industries has ultimately caused human civilization to pay its debt. Realizing the urgency of reducing emissions and yet simultaneously catering to needs of industries, researches and scientists conclude that renewable energy is the perfect candidate to fulfill both parties requirement. Renewable energy provides an effective option for the provision of energy services from the technical point of view. In this context, biomass appears as one important renewable source of energy. Biomass has been a major source of energy in the world until before industrialization when fossil fuels become dominant and researches have proven from time to time its viability for large-scale production. Although there has been some successful industrial-scale production of renewable energy from biomass, generally this industry still faces a lot of challenges including the availability of economically viable technology, sophisticated and sustainable natural resources management, and proper market strategies under competitive energy markets. Amidst these challenges, the development and implementation of suitable policies by the local policy-makers is still the single and most important factor that can determine a successful utilization of renewable energy in a particular country. Ultimately, the race to the end line must begin with the proof of biomass ability to sustain in a long run as a sustainable and reliable source of renewable energy. Thus, the aim of this paper is to present the potential availability of oil palm biomass that can be converted to hydrogen (leading candidate positioned as the energy of the millennium) through gasification reaction in supercritical water, as a source of renewable energy to policy-makers. Oil palm topped the ranking as number 1 fruit crops in terms of production for the year 2007 with 36.90 million tonnes produced or 35.90% of the total edible oil in the world. Its potentiality is further enhanced by the fact that oil constitutes only about 10% of the palm production, while the rest 90% is biomass. With a world oil palm biomass production annually of about 184.6 million tons, the maximum theoretical yield of hydrogen potentially produced by oil palm biomass via this method is 2.16×10¹⁰ kg H₂ year⁻¹ with an energy content of 2.59 EJ year⁻¹, meeting almost 50% of the current worldwide hydrogen demand.     

A hydrogen-producing, hydrogenase-free mutant strain of Nostoc punctiforme ATCC 29133

The hupL gene, encoding the uptake hydrogenase large subunit, in Nostoc sp. strain ATCC 29133, a strain lacking a bidirectional hydrogenase, was inactivated by insertional mutagenesis. Recombinant strains were isolated and analysed, and one hupL⁻ strain, NHM5, was selected for further study. Cultures of NHM5 were grown under nitrogen-fixing conditions and H₂ evolution under air was observed using an H₂ electrode.     

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.     

Isolation and characterization of a new hydrogen-producing strain Bacillus sp. FS2011

A new fermentative hydrogen-producing strain FS2011 was isolated from an effluent of bio-hydrogen production reactor, and identified as Bacillus amyloliquefaciens on the basis of 16S rDNA gene sequence. The strain could utilize various carbon and nitrogen sources to produce hydrogen in a broad range of initial pH (5.29–7.38). Phosphate buffer concentration and fermentation temperature significantly affected hydrogen production and cell growth. The maximum hydrogen yield of 2.26 mol/mol was observed at glucose concentration of 10 g/l, beef extract concentration of 2 g/l, initial pH 6.98, phosphate buffer of 20 mmol/l, and 35 °C, indicating FS2011 was a high-efficiency hydrogen-producing bacterium.     

Fermentative hydrogen production in recombinant Escherichia coli harboring a [FeFe]-hydrogenase gene isolated from Clostridium butyricum

The [FeFe]-hydrogenase (hydA) from Clostridium butyricum TERI BH05-2 strain was isolated to elucidate its molecular characterization. A 1953 bp DNA fragment encompassing the ORF and the putative promoter region of hydA gene was PCR amplified and subcloned into pGEM^®-T-Easy cloning vector (pGEM^®-T-hydA). The hydA DNA sequence revealed the presence of a 1725 bp length ORF (including the stop codon) encoding 574 amino acids with a predicted isoelectric point and molecular mass of 6.8 and 63097.67 Da, respectively. The hydA ORF was PCR amplified from pGEM^®-T-hydA and inserted into a prokaryotic expression vector to create a recombinant plasmid (pGEX-5X-hydA) and transformed into Escherichia coli BL-21. The recombinant E. coli BL-21 was investigated for fermentative hydrogen production under anaerobic condition from glucose. Heterologous expression of the Clostridium butyricum hydA resulted in 1.9 fold increase in hydrogen productivity as compared to that from the wild type strain, C. butyricum TERI BH05-2. The hydrogen yield of the recombinant strain was 3.2 mol H₂/mol glucose, 1.68 fold higher than the wild type parent strain.     

Biohydrogen production from oil palm frond juice and sewage sludge by a metabolically engineered Escherichia coli strain

Biohydrogen is considered a promising and environmentally friendly energy source. Escherichia coli BW25113 hyaB hybC hycA fdoG frdc ldhA aceE has been previously engineered for elevated biohydrogen production from glucose. In this study, we show that this strain can also use biomass from oil palm frond (OPF) juice and sewage sludge as substrates. Substrate improvement was accomplished when hydrogen productivity increased 8-fold after enzymatic treatment of the sludge with a mixture of amylase and cellulase. The OPF juice with sewage sludge provided an optimum carbon/nitrogen ratio since the yield of biohydrogen increased to 1.5 from 1.3 mol H₂/mol glucose compared to our previous study. In this study, we also reveal that our engineered strain improved 200-fold biohydrogen productivity from biomass sources compared to the unmodified host. In conclusion, we determined that our engineered strain can use biomass as an alternative substrate for enhanced biohydrogen production.     

Photofermentive production of biohydrogen from oil palm waste hydrolysate

Oil palm empty fruit bunch (OPEFB) was hydrolyzed with dilute sulfuric acid (6% v/v; 8 mL acid per g dry OPEFB) at 120 °C for 15-min to release the fermentable sugars. The hydrolysate contained xylose (23.51 g/L), acetic acid (2.44 g/L) and glucose (1.80 g/L) as the major carbon components. This hydrolysate was used as the sole carbon source for photofermentive production of hydrogen using a newly identified photosynthetic bacterium Rhodobacter sphaeroides S10. A Plackett–Burman experimental design was used to examine the influence of the following on hydrogen production: yeast extract concentration, molybdenum concentration, magnesium concentration, EDTA concentration and iron concentration. These factors influenced hydrogen production in the following decreasing order: yeast extract concentration > molybdenum concentration > magnesium concentration > EDTA concentration > iron concentration. Under the conditions used (35 °C, 14.6 W/m² illumination, initial pH of 7.0), the optimal composition of the culture medium was (per L): mixed carbon in OPEFB hydrolysate 3.87 g, K₂HPO₄ 0.9 g, KH₂PO₄ 0.6 g, CaCl₂⋅2H₂O 75 mg, l-glutamic acid 795.6 mg, FeSO₄⋅7H₂O 11 mg, Na₂MoO₂⋅2H₂O 1.45 mg, MgSO₄⋅7H₂O 2.46 g, EDTA 0.02 g, yeast extract 0.3 g). With this medium, the lag period of hydrogen production was 7.65 h, the volumetric production rate was 22.4 mL H₂/L medium per hour and the specific hydrogen production rate was 7.0 mL H₂/g (xylose + glucose + acetic acid) per hour during a 90 h batch culture of the bacterium. Under optimal conditions the conversion efficiency of the mixed carbon substrate to hydrogen was nearly 29%.     

Biohydrogen production from pentose-rich oil palm empty fruit bunch molasses: A first trial

Oil palm empty fruit bunch (OPEFB) was pretreated by local plantation industry to increase the accessibility towards its fermentable sugars. This pretreatment process led to the formation of a dark sugar-rich molasses byproduct. The total carbohydrate content of the molasses was 9.7 g/L with 4.3 g/L xylose (C₅H₁₀O₅). This pentose-rich molasses was fed as substrate for biohydrogen production using locally isolated Clostridium butyricum KBH1. The effect of initial pH and substrate concentration on the yield and productivity of hydrogen production were investigated in this study. The best result for the fermentation performed in 70 mL working volume was obtained at the initial reaction condition of pH 9, 150 rpm, 37 °C and 5.9 g/L total carbohydrate. The maximum hydrogen yield was 1.24 mol H₂/mol pentose and the highest productivity rate achieved was 0.91 mmol H₂/L/h. The optimal pH at pH 9 was slightly unusual due to the presence of inhibitors, mainly furfural. The furfural content decreased proportionally as pH was increased. The optimal experiment condition was repeated and continued in fermentation volume of 200 mL. The maximum hydrogen yield found for this run was 1.21 mol H₂/mol pentose while the maximum productivity was 1.1 mmol H₂/L/h. The major soluble metabolites in the fermentation were n-butyric acid and acetic acid.     

Production of glucose from oil palm trunk and sawdust of rubberwood and mixed hardwood

Disposing of solid waste and demand of fossil fuel have become the great challenges in the 21st century. Malaysia as one of the top producers of palm oil and wooden furniture in the world is well positioned to take the challenge of the reuses of its enormous output of lignocellulosic biomass such as oil palm trunk, sawdust of rubberwood and sawdust of mixed hardwood generated from palm oil and furniture industries. Before these lignocellulosic biomasses can be used to produce fuel and major chemicals which are normally derived from petroleum, lignocellulosic materials have to be converted to glucose. Hence, it is a need to investigate the conversion efficiency and to determine the optimum conditions for the conversion of lignocellulosic materials to glucose. This present work is aimed to investigate the potential use of oil palm trunk, rubberwood sawdust and mixed hardwood sawdust as an alternative feedstock for lignocellulosic glucose production. This research also served to identify the optimum two-stage concentrated acid hydrolysis condition that can convert these three lignocellulosic biomasses to glucose efficiently. Two stages concentrated sulfuric acid hydrolysis process using different acid concentration and reaction time were performed on those lignocellulosic biomass samples. The optimum results for oil palm trunk, rubberwood and mixed hardwood sawdust were obtained by using 60% acid concentration reacted for 30 min during 1st stage hydrolysis and subsequently followed by another 60 min reaction time with 30% acid concentration during the 2nd stage hydrolysis. The results, showed that oil palm trunk has a higher glucose conversion yield than those of rubberwood sawdust and mixed hardwood sawdust.     

Phototrophic hydrogen production from glucose by pure and co-cultures of Clostridium butyricum and Rhodobacter sphaeroides

Phototrophic hydrogen production from glucose by pure and co-cultures of Clostridium butyricum and Rhodobacter sphaeroides was studied in batch experiments. Results showed that in all batches hydrogen was produced after a lag phase of about 10 h; pure culture of R. sphaeroides produced hydrogen at rates substantially lower than C. butyricum. In co-culture systems, R. sphaeroides even with cell populations 5.9 times higher still could not compete with C. butyricum for glucose. In co-culture systems, R. sphaeroides syntrophically interacted with C. butyricum, using the acetate and butyrate produced by the latter as substrate for hydrogen production. Hydrogen production was ceased in all batches when the pH was lowered to the level of pH 6.5, resulting from the accumulation of fatty acids. It was also demonstrated in this study that fluorescence in situ hybridization (FISH) was an effective means for the quantification of the relative abundance of individual bacteria in a co-culture system.     

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 syngas yield from residual branches of oil palm tree using steam gasification

Wastes produced during oil palm production from agro-industries have great potential as a source of renewable energy in agriculturally rich countries, such as Thailand and Malaysia. Clean chemical energy recovery from oil palm residual branches via steam gasification is investigated here. A semi-batch reactor was used to investigate the gasification of palm trunk wastes at different reactor temperatures in the range of 600 to 1000 °C. The steam flow rate was fixed at 3.10 g/min. Characteristics and overall yield of syngas properties are presented and discussed. Results show that gasification temperature slightly affects the overall syngas yield. However, the chemical composition of the syngas varied tremendously with the reactor temperature. Consequently, the syngas heating value and ratio of energy yield to energy consumed were found to be strongly dependent on the reactor temperature. Both the heating value and energy yield ratio increased with increase in reactor temperature. Gasification duration and the steam to solid fuel ratio indicate that reaction rate becomes progressively slower at reactor temperatures of less than 700 °C. The results reveal that steam gasification of oil palm residues should not be carried out at reactor temperatures lower than 700 °C, since a large amount of steam is consumed per unit mass of the sample in order to gasify the residual char.     

Purification and characterization of [Fe]-hydrogenase from high yielding hydrogen-producing strain, Enterobacter cloacae IIT-BT08 (MTCC 5373)

Fe-hydrogenase from Enterobacter cloacae IIT-BT08 was purified 1284 fold with specific activity of 335 μmol H₂/min/mg protein for hydrogen evolution using reduced methyl viologen as an electron-donor at 25 °C. The molecular weight of the monomeric enzyme was determined to be 51 kDa by MALDI-ToF mass spectrometry. The PI of the enzyme was 5.6 displaying its acidic nature. The optimal temperature and pH for hydrogen evolution was 37 °C and 7–7.2 respectively. The affinity constant, K_m for reduced methyl viologen was 0.57 ± 0.03 mM and that of reduced ferredoxin was 0.72 ± 0.04 μM. The enzyme contained 11.47 gm-atom Fe/mol of Fe-hydrogenase. Electron paramagnetic resonance analysis ascertained the existence of iron molecules as [4Fe–4S] clusters. The internal amino acid sequences of trypsin digested peptides of hydrogenase as determined by ESI MS/MS Q-ToF showed 80-87% identities with the respective sequences of Clostridium sp. and Trichomonas sp. hydrogenase.     

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.     

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.