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TakedownIf you consider content in White Rose Research Online to be in breach of UK law, please notify us by emailing eprints@whiterose.ac.uk including the URL of the record and the reason for the withdrawal request. Thermal hydrolysis and hydrothermal processing have shown promise for converting biomass 10 into higher energy density fuels. Both approaches can facilitate the extraction of inorganics in 11 to the aqueous process waters. This study compares the behaviour of microalgae, digestate, 12 swine and chicken manure by thermal hydrolysis and hydrothermal processing at increasing 13 process severity. Thermal hydrolysis was performed at 170 °C, hydrothermal carbonization 14 (HTC) was performed at 250 °C, hydrothermal liquefaction (HTL) was performed at 350 °C 15 and supercritical water gasification (SCWG) was performed at 500 °C in a batch reactor. The 16 level of nitrogen, phosphorus and potassium in the product streams was measured for each 17 feedstock. Nitrogen is present in the aqueous phase as organic-N and NH3-N. The proportion 18 of organic N increases the lower the temperature. The extraction of phosphorus is strongly 19 linked to the presence of inorganics such as Ca, Mg and Fe in the starting feedstock. 20
A comparison of product yields and inorganic content in process streamsMicroalgae and chicken manure release phosphorus more easily than the other feedstocks. 21Keywords: hydrothermal processing, NPK, manure, microalgae, digestate 22 23
Introduction 24Hydrothermal processing of biomass can be utilised as either a pre-treatment or for energy 25 densification. Thermal hydrolysis is often used prior to anaerobic digestion at temperatures in 26 the range 160-170 o C resulting in enhanced biogas yields (Mendez et al., 2015). 27Hydrothermal carbonisation (HTC) is operated at 180-250 °C and pressure between 2-10 28MPa, and produces a carbon-rich bio-coal (Mumme et al., 2011). Hydrothermal liquefaction 29 (HTL) is operated at 280-370 °C and pressures ranging from 10-25 MPa and produces a 30 synthetic bio-crude (Biller et al., 2012). Supercritical water gasification (SCWG) is operated 1 at temperatures above 450 °C and pressure above the critical point of water (22 MPa) 2 producing a syngas containing H2, CO2 and CH4 (Toor et al., 2011). There is a growing 3 interest in the recovery of nutrients from wet wastes such as manures and bio-solids and 4 hydrothermal processing has been proposed to facilitate...