Abstract

The cultivation of toxic lignocellulosic hydrolyzates has become a challengingresearch topic in recent decades. Although several cultivation methods have been proposed,numerous questions have arisen regarding their industrial applications. The current workdeals with a solution to this problem which has a good potential application on anindustrial scale. A toxic dilute-acid hydrolyzate was continuously cultivated using a high-cell-density flocculating yeast in a single and serial bioreactor which was equipped with asettler to recycle the cells back to the bioreactors. No prior detoxification was necessary tocultivate the hydrolyzates, as the flocks were able to detoxify it in situ. The experimentswere successfully carried out at dilution rates up to 0.52 h-1. The cell concentration insidethe bioreactors was between 23 and 35 g-DW/L, while the concentration in the effluent ofthe settlers was 0.32 ± 0.05 g-DW/L. An ethanol yield of 0.42-0.46 g/g-consumed sugarwas achieved, and the residual sugar concentration was less than 6% of the initialfermentable sugar (glucose, galactose and mannose) of 35.2 g/L.

Highlights

  • Ethanol is nowadays one of the most important renewable fuels on the market [1]

  • All component concentrations were determined from the refractive index (RI) detector except furfural and hydroxymethyl furfural (HMF), which were determined from the ultraviolet absorbance (UV) chromatogram at 210 nm wavelength

  • The flocculating yeast (FY) S. cerevisiae CCUG 53310 was quite fast to flocculate and settled down and quickly, which is a clear advantage to be used in cultivation with cell-recycling systems

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Summary

Introduction

Ethanol is nowadays one of the most important renewable fuels on the market [1]. Its market has been triggered especially by the depletion of fossil fuel sources, as well as by its increasing demand. Ethanol is predominantly produced from sugar sources such as sugar cane juice and starch sources such as corn and wheat grains [4,5,6,7,8,9]. Since these materials are food for humans and/or animals, the limitations of stock and price may hinder these materials from being widely used in the future as feedstock for ethanol production. Even though the commercial production of ethanol from lignocellulosic materials is still in development, it has been predicted that these materials will supply more than 50% of ethanol in the future [1]. Fast and efficient overall processes are desirable to reduce investment and operating cost, making ethanol competitive with gasoline

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