An Exploratory Study of Hydrochar as a Matrix for Biotechnological Applications.

This paper explores the potentialities of hydrochar in protein separation and enzyme immobilization for non-energy biorefinery applications of hydrothermal carbonization. An innovative experimental procedure monitors soluble protein-hydrochar interactions and enzymatic reactions in a continuously stirred tank reactor. The hydrochar comes from hydrothermal carbonization of silver fir (200 °C, 30 min, 1/7 solid/water ratio) and standard activation (KOH, oven, 600 °C).

Hydrothermal carbonization of waste biomass: An experimental comparison between process layouts.

This paper contributes to the knowledge on waste biomass conversion processes occurring in the presence of hot compressed water. The experimental procedure detailed herein assesses different process schemes based on the low-temperature reaction known as hydrothermal carbonization. The performances of two lab-scale reactor configurations, with and without a downstream flash expansion step, were evaluated and compared.

Hydrothermal conversions of waste biomass: Assessment of kinetic models using liquid-phase electrical conductivity measurements.

This experimental study proposes the systematic monitoring of liquid phase electrical conductivity as a new technique for evaluating kinetic models for hydrothermal conversion of biomass. The application to the hydrothermal carbonization of three different wooden materials is validated by batch experiments at 200 °C, up to 120 min of reaction time, and at a 7:1 water to solid ratio. Whatever the biomass, the time course of electrical conductivity follows a unique law, unquestionably corresponding to the evolution of solid-phase carbon content.

Hydrothermal carbonization of Biomass: New experimental procedures for improving the industrial Processes.

This study aims to introduce new experimental methods, not yet described in the literature, to be adopted in hydrothermal carbonization processes. Silver fir was selected as model biomass in batch experiments in the range 200-300°C, up to 120min of reaction time, and at a 7:1 water to solid ratio. Simple equations were proposed for modeling the evolution of the process variables during the reaction, particularly the electrical conductivity of the liquid phase, correctly described by a simple two-step first order mechanism, regardless of the reaction temperature.