Abstract

An increasing number of industrial plants integrate the anaerobic digestion (AD) of the organic fraction of municipal solid waste (OFMSW) with a subsequent composting phase. To improve the plant productivity, a fraction of OFMSW digestate can be converted into a carbonaceous material, called hydrocar (HC), through Hydrothermal Carbonization (HTC), and then composted together with the OFMSW digestate itself, to produce “hydrochar co-compost”. The aim of this paper is to present the design and assembly of batch bioreactors, built in-house to investigate the co-composting process of OFMSW digestate and its HC, and to provide some preliminary results. The OFMSW digestate from an industrial plant was carbonized at 200 °C for 3 h in a 2 L HTC reactor, to produce wet HC after filtration. The ratio of OFMSW digestate and green waste (1:1) used as bulking medium was reproduced in four bioreactors with an increasing percentage of HC substituting the OFMSW digestate (0, 25, 50, 75%). The bioreactors managed to effectively compost the solid wet biomasses in a wet environment with temperature and oxygen control, while measuring online the oxygen consumption and thus the dynamic respirometric index (DRI). The DRI24,max measured with AIR-nl solid respirometer (standardized offline measurement) started from values above 800 mg O2 kgVS−1 h−1 before composting and dropped at the end of the process to values in the range 124–340 mg O2 kgVS−1 h−1 for the four mixes, well below the recommended limit of 500 mg O2 kgVS−1 h−1 for high-quality compost stability. These offline DRI values were confirmed by the online DRI measurements. This research is part of the international C2Land Project funded by the European Institute of Innovation and Technology Climate Knowledge and Innovation Community (EIT Climate-KIC), which is greatly acknowledged.

Highlights

  • The organic fraction of municipal solid waste (OFMSW) is commonly treated in Europe through anaerobic digestion (AD) and/or composting as best available techniques— BAT [1]

  • The C2Land project moves towards this direction: it aims to design an industrial scaling model producing a valuable co-compost from green wastes with OFMSW digestate and its hydrochar produced through Hydrothermal Carbonization (HTC)

  • Two operative parameters were adopted in order to overcome this risk: the air flow rate was kept continuously high to help oxygen diffusion, while the mechanical turning/mixing of the pile in the sector at the transition from thermophilic to mesophilic conditions allowed a reallocation of particles and air pathways, enabling the access of microorganisms to further sources of organic matter

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Summary

Introduction

The organic fraction of municipal solid waste (OFMSW) is commonly treated in Europe through anaerobic digestion (AD) and/or composting as best available techniques— BAT [1]. The case of Italy is emblematic, since the produced digestate cannot be directly applied on farmland, so post-composting is almost always applied after AD [3]. In actual integrated plants where OFMSW is digested and composted, this second phase can be a bottleneck for the management of the whole system, requiring new strategies to improve the plant productivity. The C2Land project (supported by EIT Climate-KIC, Call 2019) moves towards this direction: it aims to design an industrial scaling model producing a valuable co-compost from green wastes with OFMSW digestate and its hydrochar produced through Hydrothermal Carbonization (HTC). With HTC, any kind of biomass can be treated in the temperature range 180–250 ◦C in liquid water at saturation pressure, producing hydrochar (HC, solid phase), liquor (liquid phase) and a gaseous phase (consisting mainly of carbon dioxide) [5]. The main operative parameter governing the HTC process is the temperature, and directly connected to temperature is pressure since it should maintain water in the liquid phase; other important factors are residence time, solid load (or dry biomass to water ratio), pH, and feedstock composition, HTC heating rate and the possible use of catalysts [6,7,8]

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