Feasibility study of SCFAs production from microalgae during hydrogen fermentation

https://doi.org/10.1016/j.ijhydene.2015.10.135Get rights and content

Highlights

  • Feasibility test of SCFAs production from microalgae during H2 fermentation.

  • The highest H2 yield of 36 mL H2/g dcw at 40 g dcw/L.

  • The highest 34% SCFAs conversion efficiency at 10 g dcw/L.

  • Description of H2 and SCFAs production rate by Andrew's Eq. and Monod Eq.

Abstract

In the present work, the feasibility of short-chain fatty acids (SCFAs) production from microalgae was investigated during hydrogen (H2) fermentation. The fermentation was conducted at various substrate concentrations ranging 2.5–100 g dry cell weight (dcw)/L by using anaerobic mixed cultures under mesophilic condition. It was found that H2 yield increased to 36 mL H2/g dcw as substrate concentration increased to 40 g dcw/L. However, a significant decrease in H2 yield was observed at substrate concentration of ≥60 g dcw/L. As substrate concentration increased, SCFAs concentration gradually increased, reaching 12,410 mg COD/L at 100 g dcw/L. However, in terms of SCFAs conversion efficiency, it increased from 17 to 34% (on chemical oxygen demand basis) with substrate concentration increase up to 10 g dcw/L. Acetate was the major product at 2.5 g dcw/L, but butyrate became dominant at substrate concentration of 5–60 g dcw/L. At 80 and 100 g dcw/L, lactate became the major product. H2 and SCFAs production rate were successfully described by kinetic models of Andrew's Eq. and Monod Eq., respectively. From the fermentation performance obtained, it can be concluded that microalgae could substitute the current attempt that acidifying sewage sludge to use as an external carbon source in denitrifier.

Introduction

The concerns on environmental pollution, climate change, and energy security have brought about a lot of research efforts on developing alternative production chains in transport and chemical sectors [1]. Biorefinery concept is considered the alternative and sustainable way to create value-added biofuels and products through a biomass-based industry [2]. Biomass is defined as the contemporary plant matter formed by photosynthetic capture of solar energy, splitting into terrestrial and aquatic one depending on its growth environment. Compared to terrestrial biomass, microalgae, one of the representing aquatic biomass, has a number of potential advantages: faster growth rate with higher biodegradability, lower need for land use, and no competition with edible agricultural crops [3]. In addition, microalgae can be converted into a wide range of metabolites and chemicals including proteins, carbohydrates and lipids, which can subsequently be transformed into biofuels and value-added products via thermochemical and fermentation processes [4].

Hydrogen (H2) has garnered huge interest as a promising alternative energy carrier in last years since it has high energy content and its combustion only produces water as byproduct [5]. From biomass by fermentation routes, H2 can be produced in two ways depending on the light dependency. The photo-driven process has an advantage of high H2 yield, but there is a limitation that requires big-sized fermenter caused by low H2 production rate (HPR) [6]. Meanwhile, dark fermentative H2 production, in short, H2 fermentation, proceeded in a fast manner and can directly use solid materials as feedstock [7]. In addition, short-chain fatty acids (SCFAs, C2–C5) can be obtained as byproducts, during H2 fermentation [8]. The produced SCFAs can be used as external carbon sources in biological nutrient removal process in wastewater treatment, and are highly suitable substrates for polyhydroxyalkanoate (PHA) production [9], [10].

There have been a few studies on SCFAs production by using pure culture, but a relevant literature on fermentation using mixed culture is scarce. The use of mixed cultures can offer several advantages compared to that of pure cultures in engineering point of view, such as simpler operation, better substrate utilization, and diverse metabolic capabilities [11], [12]. There are lots of factors that affect fermentation from microalgae using mixed cultures such as substrate concentration, pH, temperature, solids retention time (SRT), etc. Among these factors, substrate concentration has a significant effect on product distribution and yield, and it is a basic parameter judging the feasibility of invented process [13], [14].

This study aimed to investigate the feasibility of SCFAs production from microalgae during H2 fermentation. The batch tests at various substrate concentrations of microalgae (2.5–100 g dcw/L) were conducted by using anaerobic mixed cultures under mesophilic condition. The results obtained here might helpful to understand the mechanisms for SCFAs and H2 production from microalgae and beneficial for the sustainability of microalgae-based biorefinery.

Section snippets

Preparation of feedstock and inoculum

Chlorella vulgaris (carbohydrate 12.5%, protein 66.9%, lipid 13%, ash 6%, and others 1.6%) was utilized as a feedstock. The chemical oxygen demand (COD) concentration of C. vulgaris was 1.3 g COD/g dry cell weight (dcw). The inoculum used in this study was obtained from an anaerobic digester at a local wastewater treatment plant. The pH, alkalinity, and volatile suspended solid (VSS) concentration of the sludge were 7.2, 2.6 g CaCO3/L, and 42 g VSS/L, respectively. In order to inactivate the H2

H2 production

Fig. 1(a) shows the time courses of cumulative H2 production from microalgae at various substrate concentrations. The production curves were well fitted by the modified Gompertz Eq. (R2 > 0.96), and CH4 production was negligible during the entire experimental period.

The amount of H2 produced increased as substrate concentration increased up to 40 g dcw/L. In total, 177 ± 3 mL of H2 was produced at 40 g dcw/L, corresponding to 36 ± 1 mL H2/g dcw (Table 1). At ≥ 60 g dcw/L, H2 production

Conclusions

From the batch fermentation tests of microalgae at various substrate concentrations, following conclusions were drawn.

  • 1)

    The maximum H2 yield of 36 mL H2/g dcw was attained at 40 g dcw/L while the highest HPR was estimated to be 0.1109 L/L/h at 91 g dcw/L with the half saturation constant of 153.25 g dcw/L and inhibition constant of 69.02 g dcw/L, respectively.

  • 2)

    SCFAs yield was peaked to 439 mg COD/g dcw at 10 g dcw/L, corresponding to 34% conversion efficiency on COD basis. 50% of the maximum

Acknowledgment

This work was supported by the Energy Efficiency & Resources Core Technology Program of the Korea Institute of Energy Technology Evaluation and Planning (KETEP), granted financial resource from the Ministry of Trade, Industry & Energy, Republic of Korea (20132020000170), and by INHA UNIVERSITY Research Grant. (INHA-51356-1).

References (34)

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