Vol.:(0123456789) 1 3
Waste Biomass Valor
DOI 10.1007/s12649-017-9914-0
ORIGINAL PAPER
Process Water from the Hydrothermal Carbonization of Biomass:
A Waste or a Valuable Product?
Harpreet Singh Kambo
1
· Jamie Minaret
1
· Animesh Dutta
2
Received: 2 July 2015 / Accepted: 25 March 2017
© Springer Science+Business Media Dordrecht 2017
run). Most importantly, the HHV of hydrochars increased
from 18.9 (raw biomass) to 26.6 MJ/kg (maximal value)
during recirculation of process water. As a result, the recir-
culation of process water can increase the overall system’s
efciency and reduce both the operating costs and environ-
mental impact of a commercial HTC plant.
Keywords Hydrothermal carbonization · Organic acids ·
Recirculation · Process water
Introduction
The abundant amount of biomass on earth plays a sub-
stantial role in global energy production as it has been
widely consumed as an alternative to fossil fuels for the
purpose of generating heat and power. Lignocellulosic
biomass wastes (agricultural and forest residues) and pur-
pose grown energy crops (miscanthus, switchgrass, etc.)
are favored over frst generation biomass because of their
nonedible characteristics; hence they do not compete
with food shortage when the waste-biomasses are con-
sumed for producing energy [1]. Therefore, the consump-
tion of lignocellulosic biomass wastes as a resource of
fuel has gained remarkable attention in the development
of a clean, green renewable energy society. However,
lignocellulosic biomass has inferior physicochemical
properties when compared to coal, which include poor
homogeneous nature, high moisture content and hydro-
philic nature, poor grindability, low bulk energy density,
and high alkali and alkaline earth metal content. There-
fore the utilization of raw lignocellulosic biomass can be
highly inefcient and expensive [2]. Treatment processes
can be applied to biomass to overcome the aforemen-
tioned limitations [3]. Torrefaction, a thermal treatment
Abstract Hydrothermal carbonization (HTC) is a prom-
ising method for the production of energy dense coal-like
material from low quality lignocellulosic biomass. The pro-
cess takes place in the presence of water and therefore is
unafected by feedstocks containing a high moisture con-
tent. However, the substantial water requirement and dis-
posal concerns for a large scale HTC plant may outweigh
its advantages from an economical and environmental point
of view. The work presented in this study proposes a solu-
tion to the aforementioned problem. Miscanthus feedstock
was treated hydrothermally at three diferent reaction tem-
peratures (190, 225, and 260 °C) for 5 min with a solid load
ratio of 1:6. The liquid by-product from each experiment
was characterized for chemical composition. The results
show that the HTC process water was rich in organic acids
(acetic, formic, levulinic, and glycolic acid), Hydroxy-
methyl-furfural (HMF), and total organic carbon (TOC).
The acidity and the concentration of intermediate products
in the HTC process water increased with an increase in
reaction temperature. The HTC process water produced at
260 °C was examined for the recirculation of process water.
The results show that, during successive recirculation of
HTC process water, the mass yield of the hydrochar sam-
ples increases by 5–10% and the energy yield of the hydro-
char samples increased up to 15% compared to the HTC-
reference sample (hydrochar sample produced at initial
* Animesh Dutta
adutta@uoguelph.ca
1
School of Engineering, University of Guelph,
Guelph N1G 2W1, Canada
2
Mechanical Engineering Program, School of Engineering,
University of Guelph, Room No RICH 3509, 50 Stone Road
East, Guelph, ON N1G 2W1, Canada