Preprint Article Version 1 Preserved in Portico This version is not peer-reviewed

Effect of Process Conditions on Hydro-Char Characteristics and Chemical Composition of Aqueous and Gaseous Products by Hydrothermal Processing of Corn Stover with Hot Compressed H2O: Structural Evolution of Hydro-Char and Kinetics of Corn Stover Decomposition

Version 1 : Received: 18 November 2022 / Approved: 22 November 2022 / Online: 22 November 2022 (03:13:44 CET)

A peer-reviewed article of this Preprint also exists.

Teribele, T.; Costa, M.E.G.; Sales da Silva, C.M.; Pereira, L.M.; Bernar, L.P.; de Castro, D.A.R.; da Costa Assunção, F.P.; Santos, M.C.; de Sousa Brandão, I.W.; Fonseca, C.J.N.; Shultze, M.; Hofmann, T.; Bremer, S.J.; Machado, N.T. Hydrothermal Carbonization of Corn Stover: Structural Evolution of Hydro-Char and Degradation Kinetics. Energies 2023, 16, 3217. Teribele, T.; Costa, M.E.G.; Sales da Silva, C.M.; Pereira, L.M.; Bernar, L.P.; de Castro, D.A.R.; da Costa Assunção, F.P.; Santos, M.C.; de Sousa Brandão, I.W.; Fonseca, C.J.N.; Shultze, M.; Hofmann, T.; Bremer, S.J.; Machado, N.T. Hydrothermal Carbonization of Corn Stover: Structural Evolution of Hydro-Char and Degradation Kinetics. Energies 2023, 16, 3217.

Abstract

In this work, the effect of reaction time and biomass-to-H2O ratio on the structural evolution of hydro-char and kinetic of by hydrothermal processing of corn Stover with hot compressed H2O, have been systematically investigated. The experiments were carried out at 250 °C, heating rate of 2.0 °C/min, biomass-to-H2O ratio of 1:10, and reaction times of 60, 120, and 240 minutes, and at 250 °C, 240 minutes, heating rate of 2.0 °C/min, and biomass-to-H2O water ratio of 1:10, 1:15, and 1:20, using a pilot scale stirred tank reactor of 5 gallon. The characterization of solid phase products performed by thermo-gravimetric analysis, scanning electron microscope, energy dispersive X-ray spectroscopy, X-ray diffraction, and elemental analysis (C, N, H, S). The physical-chemistry properties of solid phase analyzed in terms of dry matter (DM), total organic content (TOC), and ash. The yields of solid and gas phases decrease linearly with decreasing biomass-to-H2O ratio, while that of liquid phases increases linearly. For constant biomass-to-H2O ratio, the yields of solid, liquid, and gaseous reaction products varied between 52.97 and 35.82% (wt.), 44.84 and 54.59% (wt.), and 2.19 and 9.58% (wt.), respectively. The yield of solids decreases exponentially by decreasing the reaction time, while the yields of liquid and gas phases increase exponentially. For constant biomass-to-H2O ratio, TG/DTG curves shows that reaction time of 60 minutes was not enough to carbonize corn Stover. For constant reaction time, TG/DTG curves shows that increasing the H2O-to-biomass ratio worse the carbonization of corn Stover. For constant biomass-to-H2O ratio, the SEM images show the main morphological structure of the corn Stover remains practically unchanged, while for constant reaction time, SEM images show that plant microstructure retains part of its original morphology, demonstrating that a decrease on biomass-to-H2O ratio worse the carbonization of corn Stover. For constant biomass-to-H2O ratio, the EDX analysis shows that the carbon content in hydro-char increases with reaction time, while for constant reaction time, the carbon content decreases with increasing biomass-to-H2O ratio. The kinetic of corn Stover degradation was correlated with a pseudo-first order exponential model, exhibiting a root-mean-square error (r2) of 1.000, demonstrating that degradation kinetics of corn Stover with hot compressed H2O, expressed as hydro-char formation, is well described by an exponential decay kinetics.

Keywords

Corn Stover; Hydrothermal carbonization; Hydro-char characterization; Kinetics of major compounds; Structural evolution.

Subject

Engineering, Energy and Fuel Technology

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