Abstract

Acetic acid bacteria (AAB) can selectively oxidize diols into their corresponding hydroxyacids. Notably, they can convert 1,3-propanediol (1,3-PDO) into 3-hydroxypropionic acid (3-HP), which is a promising building-block. Until now, 3-HP production with AAB is carried out in batch and using resting cells at high cell densities (up to 10 g L−1 of cell dry weight). This approach is likely limited by detrimental accumulation of the intermediate 3-hydroxypropanal (3-HPA). Herein, we investigate an alternative implementation that allows highly efficient 3-HP production with lower cell densities of growing cells and that prevents 3-HPA accumulation. First, growth and 3-HP production of Acetobacter sp. CIP 58.66 were characterized with 1,3-PDO or glycerol as growth substrate. The strain was then implemented in a bioreactor, during a sequential process where it was first cultivated on glycerol, then the precursor 1,3-PDO was continuously supplied at a varying rate, easily controlled by the pH control. Different pH set points were tested (5.0, 4.5, and 4.0). This approach used the natural resistance of acetic acid bacteria to acidic conditions. Surprisingly, when pH was controlled at 5.0, the performances achieved in terms of titer (69.76 g3-HP L−1), mean productivity (2.80 g3-HP L−1 h−1), and molar yield (1.02 mol3-HP mol−11,3-PDO) were comparable to results obtained with genetically improved strains at neutral pH. The present results were obtained with comparatively lower cell densities (from 0.88 to 2.08 g L−1) than previously reported. This feeding strategy could be well-suited for future scale-up, since lower cell densities imply lower process costs and energy needs.

Highlights

  • Future petroleum shortage as well as environmental concerns have become major issues for the chemical industry to face in the upcoming decades

  • For 10 and 20 g ­L−1 initial 1,3-PDO, final 3-hydroxypropionic acid (3-HP) yields were lower: this was attributed to higher HPA accumulation. These results show that Acetic acid bacteria (AAB) growth and 3-HP production is best achieved with a 5 g L­ −1 initial 1,3-PDO

  • Prevention of detrimental 3‐HPA accumulation Shake flask cultures on 1,3-PDO showed a drop in 3-HP yield for initial substrate concentrations higher than 10 g ­L−1 (Table 1), with 3-HPA accumulation being responsible for the lower 3-HP yield

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Summary

Introduction

Future petroleum shortage as well as environmental concerns have become major issues for the chemical industry to face in the upcoming decades. In order to ensure that these challenges are addressed and that companies remain competitive, public policies are pushing towards more bio-based processes. In 2015, bio-based chemicals represented only 6.8% of the overall manufacture of chemicals in the European Union (Piotrowski et al 2018). The European Union has set itself ambitious objectives through its Bio-based Industries Consortium (BIC). 30% of the production of chemicals in the European Union should become bio-based by 2030 (BIC 2012). In order to meet these objectives, new products and processes still need to be imagined de Fouchécour et al AMB Expr (2021) 11:130 or further optimized, so that they reach industrial scale and financial viability. Top value-added chemicals from biomass were listed by the US Department of Energy in order to focus research efforts on the most promising candidates (Bozell and Petersen 2010; Werpy and Petersen 2004). Some technical hurdles remain and bio-based 3-HP is not yet commercialized

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