Abstract

This study compares the H2 production from glucose, xylose, and acidic hydrolysates of Agave tequilana bagasse as substrates. The fermentation was performed in a granular sludge reactor operated in two phases: (1) model substrates (glucose and xylose) and (2) acidic hydrolysates at 35 °C, pH 4.5 and a hydraulic retention time of 5.5 h with glucose (10 g L-1) and xylose (12 g L-1). A sequencing batch reactor was used to acclimate the biomass between the glucose and xylose continuous fermentation (with a mixture of xylose-glucose) and acidic hydrolysates. During the discontinuous acclimating step, the xylose/glucose ratio increment negatively affected the H2 productivity. Although the continuous H2 production with xylose was negligible, the co-fermentation with glucose (88-12%) allowed H2 productivity of 2,889 ± 502 mL H2 L-1d-1. An acidic hydrolysate concentration of 3.3 gcarbohydrate L-1 showed a three-fold higher H2 productivity than with a concentration of 10 g L-1. The results indicated that xylose, as the only substrate, was challenging to metabolize by the inoculum, and its mixture with glucose improved the H2 productivity. Therefore, the low H2 productivity with hydrolysates could be related to the presence of xylose.

Highlights

  • The lignocellulosic biomass can be used for hydrogen production through dark fermentation (Kumar et al 2015)

  • The fermentation was performed in a granular sludge reactor operated in two phases: (1) model substrates and (2) acidic hydrolysates at 35 °C, pH 4.5 and a hydraulic retention time of 5.5 h with glucose (10 g LÀ1) and xylose (12 g LÀ1)

  • The results indicated that xylose, as the only substrate, was challenging to metabolize by the inoculum, and its mixture with glucose improved the H2 productivity

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Summary

Introduction

The lignocellulosic biomass can be used for hydrogen production through dark fermentation (Kumar et al 2015). This kind of biomass is composed mainly of 35–45% of cellulose, 25–40% of hemicellulose, and 20–30% of lignin, forming a matrix interlinked with several chemical bonds, making it difficult to be used by the microorganisms (Prakasham et al 2009a, 2009b). The diluted acidic pretreatment releases sugars from the biomass and other degradation products, negatively affecting the lignocellulosic fermentation (Chen et al 2017). The detoxification with activated carbon allowed improved H2 productivity from 58 mL H2 LÀ1 hÀ1 to 63 mL H2 LÀ1 hÀ1 in batch experiments (Valdez-Guzmán et al 2019)

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