Investigating the effects of iron and nickel nanoparticles on dark hydrogen fermentation from starch using central composite design

https://doi.org/10.1016/j.ijhydene.2015.08.004Get rights and content

Highlights

  • Dark hydrogen fermentation from starch was performed using mesophilic sludge.

  • Effects of iron and nickel nanoparticles on biohydrogen production were studied.

  • Response surface method was used to design the experiments and analyse the results.

  • Yield of 149.6 mL H2/g-VS was obtained by adding 37.5 mg/L of each nanoparticle.

Abstract

The effects of Fe0 and Ni0 nanoparticles on mesophilic dark hydrogen fermentation from starch were investigated using heat-shock pretreated anaerobic sludge in batch reactors. Starch concentration in the range of 0–20 g/L was used in the presence of 0–50 mg/L of each Fe0 and Ni0 nanoparticles while the initial pH of all experiments was adjusted to 7. The hydrogen production was optimized using response surface methodology (RSM) in a central composite design (CCD) mode. The results showed the significance of the linear effect of starch and Fe0 concentrations, the interactive effect between Fe0 and Ni0 concentrations, and the squared effect of starch concentration on the biohydrogen production. The maximum yield of hydrogen production 149.8 mL/g-VS was obtained at starch, Fe0 and Ni0 concentrations of 5.37 g/L, 37.5 mg/L, and 37.5 mg/L, respectively. This was nearly 200% higher than those in the corresponding control test. Moreover, the analysis of metabolites indicated the hydrogen production through acetic acid pathway.

Introduction

Global warming, greenhouse gas emission, and environmental pollution caused by fossil fuel consumption, along with the depletion of fossil fuel sources and the rise of their prices, have increasingly directed the attentions towards energy production from clean and renewable energy sources [1], [2]. Hydrogen, with the highest energy density among other known fuels (142 MJ/kg), has become a promising energy carrier for the future as it is carbon-free and its combustion produces only energy and water. It could also be efficiently produced via biological methods under ambient conditions [3], [4].

Dark hydrogen fermentation is considered more practical in comparison with the other biological hydrogen production methods [5], [6]. It is technically simpler and more flexible. It can deal with a wide variety of biomass wastes including wastewaters and solid wastes. Solid wastes such as agricultural and domestic wastes have a high starch content which could be efficiently hydrolyzed into glucose and maltose by enzymes involved in the dark fermentation process [6], [7], [8], [9].

Hydrogenases play a key role in the dark fermentation process by catalyzing the simplest chemical reaction, 2H+ + 2e ↔ H2. The released electrons from substrate oxidation, together with protons (electron acceptor), are converted to hydrogen in the presence of hydrogenases under anoxic conditions [10]. Two types of hydrogenases are known to be evolved in the dark fermentation process: [Ni–Fe]-hydrogenases and [Fe–Fe]-hydrogenases (Fig. 1). [Ni–Fe]-hydrogenases are usually expressed by a wide variety of bacteria while a few bacteria have the potential to express [Fe–Fe]-hydrogenases [11]. Moreover, substrate affinity of [Ni–Fe]-hydrogenases is higher than that of [Fe–Fe]-hydrogenases. The chemical structures related to the active sites for [Ni–Fe]-hydrogenase and [Fe–Fe]-hydrogenase are shown in Fig. 1[12].

The catalytic activity of hydrogenase usually depends on metal cofactors (Fe and Ni) in the active sites of their polypeptide structure. Therefore, iron and nickel are expected to influence the activity of hydrogenases and therefore can enhance the efficiency of the dark fermentation process. However, at higher concentrations, iron and nickel may inhibit the process [11]. Alshiyab et al. (2008) investigated the impact of Fe2+ ions concentration (0–1000 mg/L) on the batch hydrogen fermentation from glucose using Clostridium acetobutylicum, and reported that the hydrogen yield was enhanced from 391 to 408 mL/g-VS at Fe2+ ions concentration of 25 mg/L, while the higher concentrations of Fe2+ ions negatively affected the yield [13]. Wang and Wan (2008) investigated the impact of Ni2+ ions on the batch hydrogen fermentation using mixed culture and reported that Ni2+ ions concentrations below 0.1 mg/L could increase the hydrogen yield. Addition of 0.1 mg/L Ni2+ ions to the system led to the maximum hydrogen yield of 296.1 mL/g-VS, while further increase in Ni2+ ions concentration reduced the hydrogen yield [11].

When Fe0 nanoparticles (NPs) are exposed to oxygen in an aqueous phase, they are oxidized to Fe2+ by the following reaction [14]:2 Fe0 + O2 + 2H2O → 2 Fe2+ + 4 OH, ΔE0 = 1.67 V

This reaction (in the presence of nano-size iron powder) is completed in less than 1 min. After the consumption of the available oxygen, Fe0 NPs is oxidized by the water, which has a lower oxidation potential than oxygen, and then hydrogen is produced as the sole product of the reaction:Fe0 + 2H2O → Fe2+ + 2 OH + H2

Since the redox potential of the Fe0∖Fe2+ couple is low (−0.44 V), the above equation occurs readily at the ambient temperature and pressure. It must be noted that the reduction of iron particle sizes from micro to nano-scale can increase the rate of the above reactions by 10,000 times [14], [15]. Therefore, the addition of iron NPs to the anaerobic fermentation medium could decrease the availability of undesired oxygen in the system like the oxygen consumption by the facultative anaerobic bacteria, thereby leading to a better performance of the oxygen-sensitive hydrogenases. Moreover, after the depletion of oxygen, it produces hydrogen gas and Fe2+ ions required for hydrogenases. Mullai et al. (2013) investigated the impact of glucose concentration (10–30 g/L), the initial pH (5–6) and Ni0 NPs concentration (0–30 mg/L) on the dark hydrogen fermentation. They obtained the maximum yield of 316.1 mL/g-VS at glucose concentration of 14.01 g/L, initial pH 5.61, and Ni0 NPs concentration of 5.67 mg/L [16]. Mohanraj et al. [17] compared the impacts of iron oxide NPs and iron sulfate on the efficiency of dark hydrogen fermentation from glucose using Enterobacter cloacae. They observed that the supplementation of iron oxide NPs, at the concentration of 125 mg/L, led to the maximum hydrogen yield of 257.6 mL/g-VS, while supplementation of iron sulfate at their optimum concentration (25 mg/L) led to the hydrogen yield of 211.6 mL/g-VS. To the best of our knowledge, no study has ever investigated the effect of nickel and iron NPs on the efficiency of the dark fermentation of starch for biohydrogen production.

The aim of this work was to investigate the impacts of starch, Fe0 NPs, and Ni0 NPs concentrations on the yield of the dark hydrogen fermentation using the mesophilic mixed culture. The response surface methodology (RSM) in a central composite design (CCD) mode was applied for the optimization.

Section snippets

Seed sludge and reagents

The used inoculum was prepared from a 7000 m3 anaerobic digester located in Northern Isfahan Sewage Treatment Plant (Isfahan, Iran). The total solids (TS), volatile solids (VS), and pH of the inoculum were 7.39%, 3.53%, and 7, respectively. It was filtered through a 1 mm strainer to eliminate its sands and large particles and then subjected to anaerobic heat-shocking at 90 °C for 45 min. This was followed by immersion in cold water (15 °C) until its temperature reached near 37 °C, and then kept

Results and discussion

The influences of concentrations of starch, Fe0 NPs and Ni0 NPs on the dark hydrogen fermentation were investigated in batch experiments under mesophilic condition. After 7 days, no considerable gas was detected almost for all samples. Therefore, the experiments were stopped and the samples were subjected to volatile fatty acids (VFA) analysis. Moreover, their final pH was measured and reported.

Conclusions

In this study, Starch and Fe0 NPs concentrations were found to be the most important factors affecting the hydrogen production from starch via mesophilic dark fermentation. There was some interaction between Fe0 NPs and Ni0 NPs concentrations. The maximum experimental hydrogen yield of 147.3 mL/g-VS was obtained at starch concentration of 5 g/L, and Fe0 and Ni0 NPs concentrations of 37.5 mg/L.

Acknowledgement

Authors would like to thank Mrs. Freshteh Shams for her contribution throughout this study.

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