TY - JOUR
T1 - Production and characterization of a new quality pyrolysis oil, char and syngas from digestate – Introducing the thermo-catalytic reforming process
AU - Neumann, Johannes
AU - Binder, Samir
AU - Apfelbacher, Andreas
AU - Gasson, James Richard
AU - Ramírez García, Paula
AU - Hornung, Andreas
PY - 2014/12
Y1 - 2014/12
N2 - A 2 kg/h laboratory scale thermo-catalytic reforming (TCR®) unit was designed and commissioned at Fraunhofer UMSICHT to convert digestate into enhanced pyrolysis products. The TCR® reactor is an intermediate pyrolysis screw reactor connected to a reformer. In the experimental series reported, digestate pellets were used as feedstock. The aim herein was to test and characterize the TCR® reactor for the feedstock digestate and its products for syngas applications and decentralized power production. Prior to the pyrolysis experiments thermal gravimetric analysis was used to analyze the weight loss over temperature. The digestate was pyrolyzed at a constant temperature of 400 °C, whereas the reformer temperature was varied between 500 and 750 °C. Following the cooling and condensation of pyrolysis vapors, these separated into bio-oil, an aqueous phase and permanent gases. Hydrogen concentration increased together with increased reforming temperatures and reached a maximum of 35 vol% at 750 °C. The bio-oil generated at 750 °C had a higher heating value of 33.9 MJ/kg, 1.7 wt% water content and a total acid number of 4.9 mg KOH/g. It was possible to convert over 91% of the energy content of the biomass into usable products. These results are analyzed together with the extensive feedstock and product characterization and the experimental parameters and discussed.
AB - A 2 kg/h laboratory scale thermo-catalytic reforming (TCR®) unit was designed and commissioned at Fraunhofer UMSICHT to convert digestate into enhanced pyrolysis products. The TCR® reactor is an intermediate pyrolysis screw reactor connected to a reformer. In the experimental series reported, digestate pellets were used as feedstock. The aim herein was to test and characterize the TCR® reactor for the feedstock digestate and its products for syngas applications and decentralized power production. Prior to the pyrolysis experiments thermal gravimetric analysis was used to analyze the weight loss over temperature. The digestate was pyrolyzed at a constant temperature of 400 °C, whereas the reformer temperature was varied between 500 and 750 °C. Following the cooling and condensation of pyrolysis vapors, these separated into bio-oil, an aqueous phase and permanent gases. Hydrogen concentration increased together with increased reforming temperatures and reached a maximum of 35 vol% at 750 °C. The bio-oil generated at 750 °C had a higher heating value of 33.9 MJ/kg, 1.7 wt% water content and a total acid number of 4.9 mg KOH/g. It was possible to convert over 91% of the energy content of the biomass into usable products. These results are analyzed together with the extensive feedstock and product characterization and the experimental parameters and discussed.
KW - Thermo-catalytic reforming
KW - Intermediate pyrolysis
KW - Digestate
KW - Oil
KW - Syngas
KW - Char
U2 - 10.1016/j.jaap.2014.11.022
DO - 10.1016/j.jaap.2014.11.022
M3 - Article
SN - 0165-2370
JO - Journal of Analytical & Applied Pyrolysis
JF - Journal of Analytical & Applied Pyrolysis
ER -