Feasibility of biohydrogen production from industrial wastes using defined microbial co-culture
- Peng Chen†1Email author,
- Yuxia Wang†3,
- Lei Yan4,
- Yiqing Wang5,
- Suyue Li2,
- Xiaojuan Yan2,
- Ningbo Wang2,
- Ning Liang2 and
- Hongyu Li1Email author
© Chen et al.; licensee BioMed Central. 2015
Received: 26 June 2014
Accepted: 28 April 2015
Published: 6 May 2015
The development of clean or novel alternative energy has become a global trend that will shape the future of energy. In the present study, 3 microbial strains with different oxygen requirements, including Clostridium acetobutylicum ATCC 824, Enterobacter cloacae ATCC 13047 and Kluyveromyces marxianus 15D, were used to construct a hydrogen production system that was composed of a mixed aerobic-facultative anaerobic-anaerobic consortium. The effects of metal ions, organic acids and carbohydrate substrates on this system were analyzed and compared using electrochemical and kinetic assays. It was then tested using small-scale experiments to evaluate its ability to convert starch in 5 L of organic wastewater into hydrogen. For the one-step biohydrogen production experiment, H1 medium (nutrient broth and potato dextrose broth) was mixed directly with GAM broth to generate H2 medium (H1 medium and GAM broth). Finally, Clostridium acetobutylicum ATCC 824, Enterobacter cloacae ATCC 13047 and Kluyveromyces marxianus 15D of three species microbial co-culture to produce hydrogen under anaerobic conditions. For the two-step biohydrogen production experiment, the H1 medium, after cultured the microbial strains Enterobacter cloacae ATCC 13047 and Kluyveromyces marxianus 15D, was centrifuged to remove the microbial cells and then mixed with GAM broth (H2 medium). Afterward, the bacterial strain Clostridium acetobutylicum ATCC 824 was inoculated into the H2 medium to produce hydrogen by anaerobic fermentation.
The experimental results demonstrated that the optimum conditions for the small-scale fermentative hydrogen production system were at pH 7.0, 35°C, a mixed medium, including H1 medium and H2 medium with 0.50 mol/L ferrous chloride, 0.50 mol/L magnesium sulfate, 0.50 mol/L potassium chloride, 1% w/v citric acid, 5% w/v fructose and 5% w/v glucose. The overall hydrogen production efficiency in the shake flask fermentation group was 33.7 mL/h-1.L-1, and those the two-step and the one-step processes of the small-scale fermentative hydrogen production system were 41.2 mL/h-1.L-1 and 35.1 mL/h-1.L-1, respectively.
Therefore, the results indicate that the hydrogen production efficiency of the two-step process is higher than that of the one-step process.
KeywordsRenewable Energy Biohydrogen Microbial consortium Hydrogen
The research and development of hydrogen energy has attracted worldwide attention and become an important strategy for the production of clean energy [1,2]. Among the various technologies that have been developed for hydrogen production, the utilization of hydrogen-producing microbes is one of the most effective. Currently, microbial fermentative hydrogen production is achieved mainly through 2 routes: one utilizes pure microbial strains and the other employs a mixed microbial consortium [3-6]. Researchers have performed a large number of studies on fermentative hydrogen production using pure microbial strains and its disadvantages, including short test cycles, low hydrogen yields and poor applicability in the presence of complex substrates. To take better advantage of low-cost organic substrates for hydrogen production, recycle wastes and improve the environment, in recent years, many researchers have focused on hydrogen production by microbial fermentation using a mixed microbial consortium, in which various microbial strains exert synergistic effects [7,8]. In a favorable living environment that fully supports metabolic activities, the hydrogen production capacity and hydrogen yield from the mixed microbial consortium were enhanced compared with those of the pure microbial strains. Recent studies have confirmed that the hydrogen production efficiency of mixed microbial consortia are significantly higher than that of individual pure strains [9,10]. Therefore, the production of hydrogen by fermentation using low-cost agricultural waste by a mixed microbial consortium is a novel development for the hydrogen energy industry .
Our previous work was to observe the hydrogen production yield of 16 different pure strains and mixed culture, which contains hydrogen-producing strains and non-hydrogen-producing strains. The experimental results compared the hydrogen production yield of these pure strains. Based on these results and on the comparative hydrogen-production efficiencies of the microbial strains, Enterobacter cloacae (E. cloacae) ATCC 13047, Kluyveromyces marxianus (K. marxianus) 15D and Clostridium acetobutylicum (C. acetobutylicum) ATCC 824 were identified as suitable for use in hydrogen-producing mixed microfloras. In the present study, by the application of combinatorially optimized culture media, 3 microbial strains with different oxygen requirements, including C. acetobutylicum ATCC 824, E. cloacae ATCC 13047 and K. marxianus 15D, were combined to construct a hydrogen production system that was composed of a mixed aerobic-facultative anaerobic-anaerobic consortium.
The metal ions, organic acids and carbohydrate substrates are the most common material in industrial wastes environment. The ability of microorganism to produce hydrogen in the presence of industrial wastes sources (metal ions, organic acids and carbohydrate substrates) is worthy of study. The fundamental knowledge derived from this study should provide a valuable platform for further investigation into the behavior of microorganism involved in hydrogen production system and has potential biotechnological applications in waste resources reused. Therefore, the effects of metal ions, organic acids and carbohydrate substrates on the system were analyzed by assaying the electrochemical and kinetic parameters, along with the optimization and quality control of hydrogen production process. Based on the identification of the factors affecting the hydrogen production process, a small-scale biohydrogen production system (5 L) using starchy organic wastewater was constructed with the intent of providing preliminary data for further pilot-scale biohydrogen production.
Results and discussion
Effects of metal ions on hydrogen production system composed of mixed microbial consortium
The effects of different metal ions on the hydrogen production systems
Metal ions (0.50 mol/L)
H1 medium (mL/h -1 .L -1 )
H2 medium (mL/h -1 .L -1 )
Overall hydrogen production (%)
17.80 ± 1.51
15.90 ± 0.66
BaCl2 · 2H2O
3.74 ± 1.04
2.07 ± 0.36
6.23 ± 0.25
4.29 ± 1.03
CoCl2 · 6H2O
2.14 ± 0.99
1.113 ± 1.04
FeCl2 · 4H2O
21.54 ± 1.02
13.67 ± 0.76
FeCl3 · 4H2O
14.06 ± 1.09
18.44 ± 0.58
CuSO4 · 5H2O
14.77 ± 1.17
10.65 ± 1.97
18.69 ± 0.23
15.90 ± 1.54
MnSO4 · H2O
13.53 ± 0.76
10.02 ± 0.15
MgSO4 · 7H2O
21.18 ± 0.16
20.19 ± 0.83
12.64 ± 1.88
10.81 ± 1.96
ZnSO4 · 7H2O
16.20 ± 1.09
12.08 ± 1.03
Static fermentation experiments using 20 hydrogen-producing bacterial strains have shown that the addition of ferrum to culture media causes a shift from butyric acid to ethanol fermentation. In the 2 main pathways of fermentative hydrogen production from organic materials, ferrum is one of the essential components that participate in and promote various enzymatic reactions. Under similar culture conditions, both Fe3+ and Fe2+ stimulate the conversion of bacterial metabolism to ethanol-type fermentation, and Fe3+ exhibits stronger effects than Fe2+. Furthermore, Fe2+ enhances the fermentative hydrogen production capacities of bacteria .
In addition, Mg2+ and K+ ions also exhibit stimulatory effects on hydrogen production systems. Mg2+ is an important influential factor. Of the 10 types of cytoplasmic enzymes that are required for glycolysis, a vast majority are activated by Mg2+, and its deficiency affects the growth and anabolism of hydrogen-producing bacteria, thereby affecting the ability of the bacteria to produce hydrogen. The addition of Mg2+ to culture media has been shown to promote the growth of ethanol-based hydrogen-producing fermentative bacteria and thus enhance their hydrogen production capacities . In contrast, other metal ions, such as Ba2+, Ca2+, Co2+, Cu2+, Mn2+ and Zn2+, appear to exert inhibitory effects on hydrogen production systems by hindering microbial growth and hydrogenase activities.
Effects of organic acids on hydrogen production systems composed of mixed microbial consortium
The effects of various organic acids on the hydrogen production efficiencies
Organic acids (1% w/v)
H1 medium (mL/h -1 .L -1 )
H2 medium (mL/h -1 .L -1 )
Overall hydrogen production (%)
17.80 ± 1.51
15.90 ± 0.66
6.20 ± 2.70
7.60 ± 1.60
18.0 ± 1.10
20.3 ± 1.02
8.10 ± 3.12
8.0 ± 2.15
19.0 ± 2.03
10.1 ± 1.02
12.0 ± 3.98
12 ± 1.25
Effects of carbohydrate substrates on hydrogen production systems composed of mixed microbial consortium
To determine the effects of various carbohydrate substrates on H1 medium- and H2 medium-based hydrogen production systems, a two-step system that was composed of the 3 microbial strains was studied. As shown in Table 2, both fructose and glucose all exert significant stimulatory effects on the system, whereas the other carbohydrate substrates used in this study exhibited strong inhibition.
Small-scale biohydrogen production experiments based on starchy organic wastewater
Construction of mixed microbial consortium for biohydrogen production and synergistic effects between microbial strains
Effects of 2 types of biohydrogen production processes on electrochemical properties of hydrogen production systems
The electrochemical parameters of the two-step and one-step hydrogen production systems were compared (Figure 2). In hydrogen-production systems composed of pure microbial strains, when all other conditions are constant, the electrical conductance of the biohydrogen-producing solution is determined by the number of ions, their electric charges, and their mobility. The electrical conductance of the biohydrogen-producing solution is the sum of the electrical conductances of the various ions in the solution. Therefore, in the biological hydrogen-production process, the electrical conductance and conductivity can be utilised to determine the concentrations of the components in a hydrogen-production system and to optimise hydrogen-production conditions.
The results showed the following: (1) in the one-step hydrogen production system, a gradual declining trend in pH was observed, whereas in the two-step system, an opposite trend was observed; (2) in the one-step hydrogen production system, the redox potential showed a gradual rising trend, increasing from 25 mV to 89 mV. In contrast, the redox potential of the two-step system decreased gradually within a small range; (3) the electrical conductance and conductivity of the one-step hydrogen production system were higher than those of the two-step system.
Effects of 2 types of biohydrogen production processes on hydrogen production efficiency
As shown in Figure 3, the overall hydrogen production efficiency in the shake flask fermentation group was 33.7 mL/h-1.L-1, and those the two-step and the one-step processes were 41.2 mL/h-1.L-1 and 35.1 mL/h-1.L-1, respectively, which were higher than that of the shake flask fermentation group. Therefore, the performance of the small-scale fermentative hydrogen production system was superior to the shake flask fermentation method. In addition, the overall hydrogen production efficiency of the two-step process was higher than that of the one-step process. The differences in the overall hydrogen production efficiencies were related to the removal of the centrifugation step.
Microscopic analysis of mixed microbial consortium
The mixed microbial consortium was constructed by a two-step process using 3 microbial strains, including C. acetobutylicum ATCC 824, E. cloacae ATCC 13047 and K. marxianus 15D, and exhibited a high hydrogen production efficiency. Analyses of the effects of various metal ions, organic acids and carbohydrate substrates on the hydrogen production systems showed that the Fe2+/Fe3+ ions were crucial for the systems. Mg2+ and K+ also exerted stimulatory effects. Citric acid significantly enhanced hydrogen production efficiency. Additionally, fructose and glucose exhibited significant stimulatory effects. The hydrogen production efficiency of the two-step process is higher than that of the one-step process.
The microbial strains, used in the present study, were C. acetobutylicum ATCC 824, E. cloacae ATCC 13047 and K. marxianus 15D. All the three strains were preserved in our laboratory.
The composition of the nutrient broth was as follows
10.0 g of peptone, 3.0 g of beef extract, 5.0 g of NaCl, 20.0 g of agar and 1.0 L of distilled water. The medium was adjusted to pH 7.0 with 5 mol/L sodium hydroxide (approximately 0.2 mL) and autoclaved at 1.05Kg/cm2 for 20 min.
The composition of the potato dextrose broth was as follows: 200.0 g of potato, 20.0 g of dextrose, 1.0 L of distilled water, pH 7.0. The potatoes were washed, peeled and sliced. The potato dextrose agar (PDA) medium was prepared from 200 g washed and sliced potatoes, boiled in 500 ml filtered and strained through gauze. 20.0 g Agar was melted in the solution, and 0.5 L water and 20.0 g glucose were added before the medium was aliquoted and autoclaved at 1.05Kg/cm2 for 20 min .
The aerobic-facultative anaerobic culture medium (abbreviation: H1 medium) was prepared as follows
The nutrient broth and potato dextrose agar were prepared separately as described above and mixed evenly. The medium was utilized for the routine culture of the microbial strains E. cloacae ATCC 13047 and K. marxianus 15D.
The composition of the modified Gifu anaerobic medium (GAM) broth was as follows: 15.0 g of proteose peptone, 10.0 g of pancreatic casein peptone, 5.0 g of yeast extract, 2.0 g of beef powder, 13.5 g of digestive serum powder, 1.2 g of bovine liver extract powder, 3.0 g of glucose, 2.5 g of potassium dihydrogen phosphate, 3.0 g of sodium chloride, 0.3 g of soluble starch, 0.3 g of L-cysteine and 0.15 g of sodium thioglycolate. The medium was prepared by adding 1.0 L of distilled water to 74.0 g of modified GAM broth and autoclaved at 1.05Kg/cm2 for 20 min.
The mixed culture medium (abbreviated: H2 medium) was prepared as follows
The microbial strains E. cloacae ATCC 13047 and K. marxianus 15D were inoculated into the H1 medium. After an incubation time of 30 h, the microbial cultures were centrifuged at 10, 000 r/min for 10 min, and the liquid medium were collected. The H2 medium was obtained by adding 74.0 g of modified GAM broth to 1.0 L of liquid medium, which was then autoclaved at 1.05Kg/cm2 for 20 min. The H2 medium was used to culture the bacterial strain C. acetobutylicum ATCC 824
Culture medium for the small-scale biohydrogen production system was prepared as follows
To produce biohydrogen, the microbial strains were cultured in H1 medium or H2 medium. The H1 medium contained additional components that were not present in the H1 medium, including 0.50 mol/L ferrous chloride, 0.50 mol/L magnesium sulfate, 0.50 mol/L potassium chloride, 1% w/v citric acid, 5% w/v fructose and 5% w/v glucose.
The reagents that were used in the present study included peptone (OXIDE), beef extract (BBI), agar (BBI), GAM broth (Qingdao Hi-tech Industrial Park Haibo Biotechnology Co., Ltd.), potatoes, corn flour (commercially available), starch (made in our laboratory from fresh potatoes), lactose, maltose, fructose, glucose and sucrose (all of the above carbohydrates were biochemical reagent grade). All other reagents were analytical grade. An anaerobic gas mixture that was composed of 5% (v/v) CO2, 10% (v/v) H2 and 85% (v/v) N2 was used as carrier gas. The N2 had a purity level of 99.999% (v/v). The content of impurities in N2 was as follows: H2, ppm (v/v) ≤ 1.0, O2, ppm (v/v) ≤ 3.0 and H2O, ppm (v/v) ≤ 5.0.
Effects of various factors on hydrogen production systems
The effects of various carbohydrate substrates on the hydrogen production efficiencies
Carbohydrate substrates (5% w/v)
H1 medium (mL/h -1 .L -1 )
H2 medium (mL/h -1 .L -1 )
Overall hydrogen production (%)
17.80 ± 1.51
15.90 ± 0.66
23.3 ± 1.022
13.3 ± 1.94
19 ± 1.22
16.1 ± 1.07
16.4 ± 2.11
14.3 ± 1.04
15.7 ± 2.01
15.5 ± 2.64
14.9 ± 2.56
16.7 ± 1.43
13.8 ± 2.44
17.3 ± 2.39
Small-scale biohydrogen production experiments using starchy organic wastewater
Construction of a two-step biohydrogen production system
In order to obtain an aerobic-facultative anaerobic-anaerobic hydrogen production system in a stepwise manner, the microbial strains E. cloacae ATCC 13047 and K. marxianus 15D were inoculated into the H1 medium. Samples were collected periodically during the incubation period to determine the electrochemical parameters. The H2 medium was constructed from the H1 medium that was harvested from the cultures of E. cloacae ATCC 13047 and K. marxianus 15D. The bacterial strain C. acetobutylicum ATCC 824 was then inoculated into the H2 medium and incubated anaerobically. Samples were collected periodically during the incubation period, and the electrochemical parameters were analyzed. Uninoculated H1 and H2 media served as controls, and the relevant parameters were determined.
For the two-step biohydrogen production experiment, the H1 medium, after cultured the microbial strains E. cloacae ATCC 13047 and K. marxianus 15D, was centrifuged to remove the microbial cells and then mixed with GAM broth (H2 medium). Afterward, the bacterial strain C. acetobutylicum ATCC 824 was inoculated into the H2 medium to produce hydrogen by anaerobic fermentation.
For the one-step biohydrogen production experiment, the centrifugation step in the two-step hydrogen production process was omitted to ensure the operability of this pilot-scale experiment. The H1 medium was mixed directly with GAM broth to generate H2 medium. The bacterial strain C. acetobutylicum ATCC 824 was inoculated into the H2 medium. Finally, three species microbial co-culture to produce hydrogen under anaerobic conditions.
Small-scale biohydrogen production experiments
The small-scale experiments were conducted in a 5 L fermentor. The experimental conditions were as follows: liquid volume of 3 L, fermentation temperature of 30°C, rotation speed of 200 r/min, ventilation rate of 0.5 L/min, inoculum volume of 10% and vessel pressure of 0.1 MPa. Samples were collected periodically. The yields of hydrogen were determined using the GC-9A gas chromatograph with a thermal conductivity detector (Shimadzu, Japan) with N2 as the carrier gas. The injection volume was 1 mL. Hydrogen concentrations were calculated using the external standard method.
The electrochemical parameters were measured using an FJA-3 electrochemical ion analyzer (Nanjing Zhuan-Di Instrument & Equipment Co., Ltd.). The fermentation broth was collected periodically, and the temperature, pH, Eh, electrical conductance and conductivity were detected. The measurements were repeated 5 times, and the averages were used for the data analysis. Using the uninoculated liquid medium as a reference, the absorbances of the microbial cultures at the 600 nm wavelength were measured using a UV-1800PC spectrophotometer (Beijing Purkinje General Instrument Co., Ltd.).
The microbial strains E. cloacae ATCC 13047 and K. marxianus 15D were inoculated into the H1 medium. Following the appropriate incubation period, the microbial cells were harvested by centrifugation, stained with methylene blue and imaged using the Canon Powershot A3300/S Digital Camera (Japan). The microscopes used in this study were the OPTON universal microscope (West Germany) and XSM-20 biological microscope (Ningbo Sunny Instruments Co., Ltd.).
The hydrogen content was determined using a GC-9A gas chromatograph with a thermal conductivity detector (Shimadzu, Japan). The carrier gas was N2, and the injection volume was 1 mL. The hydrogen content was calculated using the external-standard method. Electrochemical parameters were measured using an FJA-3 electrochemical ion analyser (Nanjing Chuan-Di Instrument & Equipment Co., Ltd.). The fermentation broth was collected periodically, and the pH/Eh and electrical conductance/conductivity were determined. The measurements were repeated 5 times, and the average values were used for data analysis.
This work was supported by Gansu Province Science Foundation for Distinguished Young Scholars (Grant No. 1308RJDA014), Longyuan Support Project for Young Creative Talents (Grant No. GANZUTONGZI  no.4), Technology Program of Gansu Province (Grant No. 1205TCYA034), Technology Program of Lanzhou City (Grant No. 2013-4-115), and the National Natural Science Foundation of China (Grant No. 81200469).
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