Abstract

The purification and concentration of volatile fatty acids (VFAs) after acidogenic fermentation represent the key steps for their industrial use. In this study, different batch adsorption tests were performed on single VFAs using powdered activated carbon (PAC), Lewatit VP OC 1065, Amberlyst A21, and VFA mixtures using Lewatit and Amberlyst. Adsorption yields of approximately 70% for PAC and 86–96% for Lewatit and Amberlyst were achieved on the single VFA tests at an initial concentration of 5 g/L. The VFA mixture tests at 25 g/L showed lower yields: 40 and 27% for Lewatit and Amberlyst, respectively. Batch desorption tests were performed adopting two desorbents, ethanol, and water at various NaOH concentrations (1, 0.1, and 0.01 M) and at decreasing volumes (5, 3, and 2 mL). The optimization of the adsorption and desorption operations allowed the final VFA concentrations of 85–90 g/L to be reached. The best adsorbent, Lewatit, and the best desorption conditions were applied on a real fermentate with an initial VFA concentration of approximately 18 g/L, obtaining a final VFA content three times higher than in the original solution.

Highlights

  • Volatile fatty acids (VFAs) are short-chain carboxylic acids that are commonly used as biological precursors in the pharmaceutical, cosmetic, food, and plastic industries as well as in biofuel production.[1,2] VFAs are high-demand chemicals, with values ranging from 800 €/ton for acetic acid to 1650 and 2500 €/ton for butyric and propionic acids, respectively.[3]

  • Single VFAs, NaOH, ethanol, and all chemicals used for soluble chemical oxygen demand determination were purchased from Merck

  • This trend can be explained considering the solubility of the VFAs, which decrease with the number of C atoms in the chain

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Summary

Introduction

Volatile fatty acids (VFAs) are short-chain carboxylic acids that are commonly used as biological precursors in the pharmaceutical, cosmetic, food, and plastic industries as well as in biofuel production.[1,2] VFAs are high-demand chemicals, with values ranging from 800 €/ton for acetic acid to 1650 and 2500 €/ton for butyric and propionic acids, respectively.[3]. The best operative conditions for acidogenic fermentation are as follows: neutral pH range (6.0−7.0), hydraulic retention time (HRT) lower than 10 days, organic loading rate of 10 kgVS/m3 d, mineral acid addition (0.5− 3.0%), and thermal pretreatment (140−170 °C). Under these conditions, VFAs can reach a final concentration of 25−30 g/ L.5

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