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Kinetics of faecal biomass hydrothermal carbonisation for hydrochar production

journal contribution
posted on 07.06.2013 by Eric Danso-Boateng, Richard Holdich, G. Sharma, Andrew Wheatley, M. Sohail (Khan), Simon Martin
Decomposition kinetics of primary sewage sludge (PSS) and synthetic faeces (SF), of various moisture contents, were investigated over different reaction times and temperatures using a hydrothermal batch reactor. Solid decomposition of PSS and SF was first-order with activation energies of 70 and 78 kJ/mol, and pre-exponential factors of 4.0 106 and 1.5 107 min 1, respectively. Solid decomposition was significantly affected by reaction temperature more so than reaction time. Higher temperature resulted in higher solids conversion to hydrochar. Equilibrium solid hydrochar yields (relative to the original dry mass used) were 74%, 66%, 61% and 60% for PSS at 140, 170, 190 and 200 C respectively, and 85%, 49%, 48% and 47% for SF at 140, 160, 180 and 200 C respectively. Energy contents of the hydrochars from PSS carbonised at 140–200 C for 4 h ranged from 21.5 to 23.1 MJ/kg, and increased following carbonisation. Moisture content was found to affect the Hydrothermal Carbonisation (HTC) process; feedstocks with higher initial moisture content resulted in lower hydrochar yield and the extent of carbonisation was more evident in feedstock with lower moisture content. The results of this study provide information useful for the design and optimisation of HTC systems for waste treatment.

Funding

This research was part of Gates Foundation: "Reinventing the Toilet".

History

School

  • Architecture, Building and Civil Engineering

Research Unit

  • Water, Engineering and Development Centre (WEDC)

Citation

DANSO-BOATENG, E. ... et al., 2013. Kinetics of faecal biomass hydrothermal carbonisation for hydrochar production. Applied Energy, 111, pp. 351 - 357

Publisher

© Elsevier Ltd.

Version

VoR (Version of Record)

Publication date

2013

Notes

This article was published in the journal, Applied Energy [© Elsevier Ltd.] and the definitive version is available at:

Language

en

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