ArticlePDF Available

Pyrogenic Carbon Capture & Storage (PyCCS)


Abstract and Figures

The growth of biomass is considered the most efficient method currently available to extract carbon dioxide from the atmosphere. However, biomass carbon is easily degraded by microorganisms releasing it in the form of greenhouse gases back to the atmosphere. If biomass is pyrolysed, the organic carbon is converted into solid (biochar), liquid (bio‐oil), and gaseous (permanent pyrogas) carbonaceous products. During the last decade, biochar, has been discussed as a promising option to improve soil fertility and sequester carbon, although, the carbon efficiency of the thermal conversion of biomass into biochar is in the range of 30 to 50% only. So far, the liquid and gaseous pyrolysis products were mainly considered for combustion, though they can equally be processed into recalcitrant forms suitable for carbon sequestration. In this review, we show that pyrolytic carbon capture and storage (PyCCS) can aspire for carbon sequestration efficiencies of >70%, which is shown to be an important threshold to allow PyCCS to become a relevant negative emission technology. Prolonged residence times of pyrogenic carbon can be generated (i) within the terrestrial biosphere including the agricultural use of biochar; (ii) within advanced bio‐based materials as long as they are not oxidized (biochar, bio‐oil); (iii) within suitable geological deposits (bio‐oil and CO2 from permanent pyrogas oxidation). While pathway (iii) would need major carbon taxes or similar governmental incentives to become a realistic option; pathways (i) and (ii) create added economic value and could at least partly be implemented without other financial incentives. Pyrolysis technology is already well established, biochar and bio‐oil sequestration in soils, respectively bio‐materials, do not present ecological hazards, and global scale‐up appears feasible within a timeframe of 10 to 30 years. Thus, PyCCS could evolve into a decisive tool for global carbon governance, serving climate change mitigation and the sustainable development goals simultaneously. This article is protected by copyright. All rights reserved.
This content is subject to copyright. Terms and conditions apply.
Pyrogenic carbon capture and storage
HansPeter Schmidt
Andrés AncaCouce
Nikolas Hagemann
Constanze Werner
Dieter Gerten
Wolfgang Lucht
Claudia Kammann
Ithaka Institute, Hamburg, Germany
Institute of Thermal Engineering, Graz
University of Technology, Graz, Austria
Environmental Analytics, Agroscope,
Zurich, Switzerland
Potsdam Institute for Climate Impact
Research (PIK), Research Domain I:
Earth System Analysis, Potsdam,
HumboldtUniversität zu Berlin,
Geography Department, Berlin, Germany
Department of Applied Ecology,
Hochschule Geisenheim University,
Geisenheim, Germany
HansPeter Schmidt, Ithaka Institute,
Hamburg, Germany.
Funding information
Bundesministerium für Bildung und
Forschung, Grant/Award Number:
01LS1620A, 01LS1620B
The growth of biomass is considered the most efficient method currently available
to extract carbon dioxide from the atmosphere. However, biomass carbon is easily
degraded by microorganisms releasing it in the form of greenhouse gases back to the
atmosphere. If biomass is pyrolyzed, the organic carbon is converted into solid (bio-
char), liquid (biooil), and gaseous (permanent pyrogas) carbonaceous products.
During the last decade, biochar has been discussed as a promising option to improve
soil fertility and sequester carbon, although the carbon efficiency of the thermal con-
version of biomass into biochar is in the range of 30%50% only. So far, the liquid
and gaseous pyrolysis products were mainly considered for combustion, though they
can equally be processed into recalcitrant forms suitable for carbon sequestration. In
this review, we show that pyrolytic carbon capture and storage (PyCCS) can aspire
for carbon sequestration efficiencies of >70%, which is shown to be an important
threshold to allow PyCCS to become a relevant negative emission technology. Pro-
longed residence times of pyrogenic carbon can be generated (a) within the terres-
trial biosphere including the agricultural use of biochar; (b) within advanced bio
based materials as long as they are not oxidized (biochar, biooil); and (c) within
suitable geological deposits (biooil and CO
from permanent pyrogas oxidation).
While pathway (c) would need major carbon taxes or similar governmental incen-
tives to become a realistic option, pathways (a) and (b) create added economic value
and could at least partly be implemented without other financial incentives. Pyroly-
sis technology is already well established, biochar sequestration and biooil seques-
tration in soils, respectively biomaterials, do not present ecological hazards, and
global scaleup appears feasible within a time frame of 1030 years. Thus, PyCCS
could evolve into a decisive tool for global carbon governance, serving climate
change mitigation and the sustainable development goals simultaneously.
biochar, biooil, carbon sequestration, climate mitigation, permanent pyrogas, pyrolysis, tCDR
To keep global warming in the range that has sustained
civilization during the past millennia, the carbon balance
between emissions to the atmosphere and carbon
accumulation in the terrestrial system has to return to an
equilibrium by 2050 at the latest (Obersteiner et al., 2018;
Rockström et al., 2016, 2009 ). To achieve this, greenhouse
gas (GHG) emissions need to be reduced by at least 90%
This is an open access article under the terms of the Creative Commons Attribution License, which permits use, distribution and reproduction in any medium, provided the
original work is properly cited.
© 2018 John Wiley & Sons Ltd
Received: 27 March 2018
Accepted: 4 August 2018
DOI: 10.1111/gcbb.12553
GCB Bioenergy. 2019;11:573591.
with the world economy becoming climate neutral by 2050
(Rogelj et al., 2015, Bertram et al., 2015; Sanderson,
ONeill, & Tebaldi, 2016; Schleussner et al., 2016). How-
ever, even if the most ambitious scenarios of global GHG
emission reductions were implemented within this time
frame, the additional need for largescale atmospheric car-
bon dioxide removal (CDR) to prevent overshooting the
1.5°C temperature threshold remains (Boysen, Lucht,
Schellnhuber, et al., 2016; Hansen et al., 2017; Smith
et al., 2015). Thus, most recent scenarios from integrated
assessment models (IAMs) include the largescale deploy-
ment of socalled negative emissions technologies (NETs)
to achieve CDR (Fuss et al., 2014; Hansen et al., 2017;
Riahi et al., 2015; Rogelj et al., 2015; Rogelj, McCollum,
Reisinger, Meinshausen, & Riahi, 2013; Van Vuuren et al.,
2013). Technical solutions to extract CO
from the atmo-
sphere like direct air capture (Kumar et al., 2015; Sanz
Pérez, Murdock, Didas, & Jones, 2016), enhanced weather-
ing (Koeve, Keller, & Oschlies, 2017; Moosdorf, Renforth,
& Hartmann, 2014), and artificial ocean alkalinization
(Montserrat et al., 2017) are promising geoengineering
approaches, although they are, to different degrees, either
not yet mature or available at the needed scale, or the risk
of largescale implementation may still be considered too
high (Hansen et al., 2017). An increase in terrestrial and
marine biomass production, combined where possible with
the sequestration of a significant part of its accumulated
carbon, is therefore considered a CDR strategy that may be
implemented most rapidly, and with the lowest risk of
other geological and ecological processes (Hansen et al.,
2017; Rockström et al., 2017; Smith et al., 2015).
Beside afforestation, bioenergy production with carbon
capture and storage (BECCS) is the only NET included in
the mitigation scenarios of the Intergovernmental Panel on
Climate Change's (IPCC) Fifth Assessment Report (Allen
et al., 2014). The BECCS scenario anticipates that biomass
combustion could become a major pathway for clean
energy production and that capturing the emitted CO
would become a complementary technology. Besides the
known and unknown risks of fossilizing CO
and its high
costs (>150 USD/t CO
(Klein et al., 2014; Smith et al.,
2015), BECCS is increasingly being recognized for poten-
tially harming ecosystem services and the integrity of the
biosphere with its extended implementation (Boysen,
Lucht, Gerten, & Heck, 2016; Burns & Nicholson, 2017;
Heck, Gerten, Lucht, & Popp, 2018).
Alternatively, CDR could be achieved through increased
net primary productivity (NPP) of the biosphere, combined
with the extension of the mean residence time (MRT) of the
biogenic carbon (i.e. net C sequestration) (Erb et al., 2017;
Smith et al., 2015). Increasing soil organic matter is one way
forward to extend MRTs (Lal, 2011; Minasny, Malone,
et al., 2017; Zomer, Bossio, Sommer, & Verchot, 2017).
However, the capacity of soils to accumulate organic carbon
is likely limited (Barré et al., 2017; Minasny, Arrouays,
et al., 2017) and requires large amounts of nitrogen (van
Groenigen et al., 2017). Maintaining increased soil organic
matter (SOM) stocks will depend on agronomic methods and
may further be hampered by the effects of climate change
(Sierra, Trumbore, Davidson, Vicca, & Janssens, 2015). The
MRT of SOM is 5080 years at maximum (Schmidt et al.,
2011; Wang & Chang, 2001). Thus, increasing SOM is
clearly an important CDR with extensive ecological cobene-
fits; however, its longterm potential may not be sufficient as
sole CDR technology (Boysen, Lucht, Schellnhuber, et al.,
2016; Smith et al., 2015; Soussana et al., 2017; van Groeni-
gen et al., 2017). Moreover, the conversion of plant residues
(shoots, roots, and rootderived C) into SOM has low Ceffi-
ciencies of 10%15% (Bolinder, Angers, Giroux, & Laver-
dière, 1999) not considering SOM saturation (Six & Jastrow,
2002). A complementary way forward to extend the MRT of
biogenic C in the terrestrial system and to increase Ceffi-
ciencies is the pyrolytic treatment of biomass with subse-
quent sequestration in the bio, geo, and anthroposphere.
In pyrolysis processes, shredded biomass is heated under
oxygendeficient atmospheres to temperatures between 350
and 900°C (EBC, 2012) converting the biomass into a solid
(biochar), a liquid (biooil), and a permanent pyrogas frac-
tion. In most current pyrolysis systems, the pyrolysis liquids
and gases are combusted for the production of thermal and
electric energy releasing the carbon as GHG back to the
atmosphere. While this is often considered as carbon neutral,
that is green energybecause it is made from biomass, it
can only sequester the biochar carbon but not the carbon
from the gaseous and liquid phases which is more than half
of the initial biomass carbon. To optimize the carbon
sequestration potential, the following review is focused on
the material use of all pyrogenic carbon species (i.e. solid,
liquid, gaseous), and to reduce the combustion of pyrolytic
products to a minimum. We specifically investigate the con-
ditions and capacity of pyrogenic carbon capture and storage
(PyCCS) as a complete negative emission system, quantify-
ing the Csequestration potential of all three pyrolysis prod-
ucts including their use as biobased materials and
agronomic amendments, but also for geologic carbon stor-
age. We review literature on biochar, biooil, and pyrolysis
systems for the required properties of pyrolytic products and
summarize production conditions optimized for material use
and C sequestration. We then compare PyCCS with BECCS
in terms of carbon and nutrient efficiency, costs, environ-
mental risks, and time frame for technology implementation.
Pyrolysis is the thermal conversion of carbonaceous materi-
als (e.g. biomass) in a low oxygen atmosphere. During
pyrolysis, biomass evolves into biochar (solid product) and
releases volatiles, the socalled pyrolytic gas or pyrogas.
Cooled to ambient temperature, pyrogases mostly condense
into a liquid, the biooil. The remaining gas is called per-
manent pyrogas referring to the volatiles of the pyrolysis
gas that do not condense at ambient temperature. The qual-
ity and properties of the three products and their yield frac-
tion depend on the feedstock and its properties (e.g. woody
vs. herbaceous biomass, softvs. hardwood, moisture con-
tent, particle size) and on the pyrolysis process conditions.
These include heating rate, highest treatment temperature
(HTT), residence time of the solid, residence time of the
volatiles as determined by the gas flow rate in the pyrolysis
reactor, direction of gas flow and pyrogas pressure, residual
oxygen contact, and for biochar also quenching/activation
procedures (Boateng, GarciaPerez, Masek, Brown, &
Campo, 2015; Hagemann et al., 2018; Weber & Quicker,
The solid pyrolysis product, biochar, is a highly porous
material consisting mainly of polyaromatic hydrocarbons
and inorganic species originally contained in the biomass.
Biooil is a dark brown, oillike liquid composed of water
and more than 100 oxygenated condensable hydrocarbon
species including acetic acid, methanol, aldehydes, ketones,
phenols, oligomeric sugars, and waterinsoluble lignin
derived compounds (Sanna, Li, Linforth, Smart, & a,
Andrésen JM, 2011). The remaining permanent pyrogas
includes CO, CO
, and C
; it is highly inflam-
mable. To date, a multitude of different pyrolysis technolo-
gies exists that are usually optimized for one of the
products, for example fast or flash pyrolysis for biooil,
slow pyrolysis for biochar, or gasification for pyrolytic
During the last decade, biochar was increasingly discussed
as a tool for carbon sequestration in soil (Fowles, 2007;
Laird, 2008; Lehmann, Gaunt, & Rondon, 2006; Matovic,
2011; Woolf, Amonette, StreetPerrott, Lehmann, &
Joseph, 2010; Woolf, Lehmann, & Lee, 2016). It is the
most resistant form of organic carbon in soils as well as in
lake and ocean sediments (Cotrufo et al., 2016; Lehmann
et al., 2015; Reisser, Purves, Schmidt, & Abiven, 2016;
Zimmerman & Gao, 2013). In the absence of very long
term (1,000 years) field experiments in various environ-
ments and climatic zones, the MRT can only be approxi-
mated by (a) shortterm (<10 years) experimental data,
combined with mathematical decay models and temperature
normalization (Kuzyakov, Bogomolova, & Glaser, 2014;
Lehmann et al., 2015), by (b) bottomup assessments of
fire frequencies and pyrogenic carbon (PyC) leftovers from
natural fires (Cheng, Lehmann, & Engelhard, 2008; Santín
et al., 2017), or by (c) archeological evidence (Braadbaart,
Poole, & Brussel, 2009; Criscuoli et al., 2014).
The MRT of biochar is strongly related to its H/C
ratio (which depends mainly on the pyrolysis temperature)
and to the environmental conditions of its storage (Braad-
baart et al., 2009; CampsArbestain, Amonette, Singh,
Wang, & Schmidt, 2015). In a metaanalysis of 111 experi-
ments on biochar persistence, Lehmann et al. (2015) esti-
mated that biochars with a H/C
ratio of <0.4 have, when
applied to soil, a MRT of >1,000 years, corresponding to
halflife (T
) times of ~700 years. Similar estimates were
obtained in a review by Zimmerman and Gao (2013).
Another metaanalysis by Wang, Xiong, and Kuzyakov
(2016) based on 24 studies with stable (
C) and radioac-
tive (
C) carbon isotopes found MRTs of 556 years inde-
pendent of the H/C
ratio. However, the soil environment
seems to play a dominant role in PyC persistence. While
the majority of field and laboratory studies reveal centen-
nial MRTs of >100 years (Lehmann et al., 2015; Rasse
et al., 2017), some studies show that under certain soil
(biota) conditions, biochar can be degraded biologically
with much shorter MRTs (de la Rosa, Miller, & Knicker,
2018; de la Rosa, Rosado, Paneque, Miller, & Knicker,
2018). In their recent assessment of the worldsstocks of
PyC, Reisser et al. (2016) found that soil PyC stocks aver-
age 13.7% (i.e. 200 Pg C globally) of the overall soil
organic carbon stocks down to 2 m depth. Soil clay content
and pH were the variables with the strongest predictive
value for high PyC contents in soils. However, native, fire
derived PyC in soils is chemically different to biochar pro-
duced from the same feedstock; the chemical characteristics
of biochar produced from the same material point toward
greater stability of the latter (Santín et al., 2017).
Once mixed into soil, PyC particles shatter into micro
and nanoparticles (Zimmerman & Gao, 2013). This is
mainly a physical process, that is the chemical structure
and the amount of carbon stored remain unchanged (Spo-
kas, et al., 2014). Fine particles can be transported verti-
cally to deeper soil horizons, groundwater, or horizontally
into adjacent soils or waterbodies where it may be pro-
tected against degradation. In fact, deep soil horizons are
the most important compartments for sequestration of soil
organic carbon on timescales of decades to centuries (Lor-
enz & Lal, 2014). Over longer timescales, groundwater and
sediments may be more relevant sequestration compart-
ments due to micronized biocharcarbon species being
even better preserved there from microbial and chemical
degradation (Zimmerman & Gao, 2013). Micronsized and
nanofractured PyC may ultimately reach the ocean (Foer-
eid, Lehmann, & Major, 2011; Hockaday, Grannas, Kim,
& Hatcher, 2007; Jaffe et al., 2013; Major, Lehmann, Ron-
don, & Goodale, 2010). In the ocean floor sediments, PyC
MRTs of >6,000 years were calculated (Coppola, Ziolk-
owski, Masiello, & Druffel, 2014). However, to the best of
our knowledge, no published study experimentally proved
and quantified the transfer of PyC from topsoil applications
to waterbodies and sediments (Maestrini et al., 2014).
Often, a proportion of an applied biochar are just missing
after several years without having left the soil system as
efflux (e.g. Major et al., 2010).
Based on the available data, it is hard to provide a
globally valid leakage rate of biochar applied to soil after
80 years. Biochars produced at pyrolysis temperatures
>400°C show MRTs, based on extrapolations from degra-
dation assessments of at least three years, that range from
201 years (Singh, Cowie, & Smernik, 2012) to 4,419 years
(Lehmann et al., 2015; Zimmerman & Gao, 2013), depend-
ing on the models, degradation methods, and biochar char-
acteristics. Under a conservative estimation and
considering a doubleexponential decay model (Lehmann
et al., 2015; Zimmerman & Gao, 2013), we assume aver-
age Cleakage rates for the first 100 years after soil appli-
cation (BC
) between 10% at molar H/C
ratios below
0.4% and 20% above. However, caution is recommended
as some soils, for example with low SOC and frequent
harvestresidue fires or frequent frostthaw cycles, may
turn out to be less suitable for biochar carbon sequestration
causing lower MRTs (Rosa, Rosado, et al., 2018). While
more research about mechanisms of PyC degradation and
the fate of the degradation products are clearly needed,
three metaanalyses and all studies on biochar persistence
in soil (based on >120 experiments) confirm that biochars
are much more recalcitrant than their precursor materials
and natural SOM and that MRTs exceed the centennial
Biochar can not only be used as soil amendment but also
in multiple ways for industrial products like construction
materials (Gupta & Kua, 2017), for wastewater treatment
(Mohan, Sarswat, Ok, & Pittman, 2014), and for electron-
ics (Gu et al., 2014). In all of these products, PyC can
serve as a Csink, as long as the product is not thermally
degraded and oxidized during use, recycling, or disposal.
When biochar is not used as a soil amendment but, for
example, as a composite building material or stored in a
longterm deep soil repositories, it can likely be protected
more efficiently from microbial and chemical degradation
to reach MRTs comparable to those of PyC in sediments
(Coppola & Druffel, 2016).
To date, biochar is mainly used as a soil amendment, as
animal feed ingredient, for manure treatment in agriculture
(Schmidt & Shackley, 2016) or as a compost or planting
substrate additive (Jaiswal, Elad, Cytryn, Graber, & Fren-
kel, 2018; Kern et al., 2017). When applied to soil, biochar
can, but does not always, improve parameters like soil
nutrient retention, water retention, soil pH, cation exchange
capacity, or microbial activity, with effects strongly
depending on both soil and biochar characteristics (Atkin-
son, Fitzgerald, & Hipps, 2010; Cornelissen et al., 2013;
Lehmann et al., 2011) and plant species grown on it (e.g.
Guereña et al., 2015; Schmidt, Pandit, Cornelissen, &
Kammann, 2017). In the longer term, for example with
repeated additions of biochar organic blends, biochar will
modify the original soil chemical and physical properties
and cause bulk density decreases, improved water infiltra-
tion, and increased stocks of water or plantavailable nutri-
ents. Such modifications are frequent in PyCrich
anthropogenic dark earth soils worldwide (Glaser & Birk,
2012; Solomon et al., 2016) or at old charcoalmaking
(kiln) places (Borchard et al., 2014; Criscuoli et al., 2014).
Biochar can have contrasting effects on nonpyrogenic
soil organic carbon stocks (Wang et al., 2016). As shown
in some studies, biochar soil application may enhance the
accumulation of plantderived carbon entering the soil (lit-
ter, root exudates) and thus increase the content of soil
organic carbon beyond the addition of biochar's PyC
(Amendola et al., 2017; Bruun, Petersen, Hansen, Holm, &
HauggaardNielsen, 2014; Ventura et al., 2014; Weng
et al., 2017). In some cases, however, decomposition of
already present nonpyrogenic soil organic carbon was
accelerated (Wardle, Nilsson, & Zackrisson, 2008; Whit-
man & Lehmann, 2015). Thus, biochar can have positive
or negative priming effects; particularly, the interaction
with plant roots is not well understood (Cross & Sohi,
2011; Wang et al., 2016). To trace C flows, C sources
must be traced by stable isotopes to three CO
C sources:
plantderived C, soil organic matterderived C, and bio-
charderived C. Due to the complexity of such experiments,
the number of published studies is still low.
Several metaanalyses of biochar field trials indicate
average yield increases of 10%20% following amendments
of more than 5 t/ha of pure, notnutrientenriched biochar
(CraneDroesch, Abiven, Jeffery, & Torn, 2013; Jeffery,
Abalos, Spokas, & Verheijen, 2015). While yield increases
(with pure biochar use) are low or absent in temperate
soils, biochar application increased yields in tropical and
subtropical soils by 25% on average, according to the latest
extensive metaanalysis (Jeffery et al., 2017). The increase
also enhances accumulated C from the atmosphere by the
same percentage; if the same practice is maintained over
decades, the sustained increase in NPP increases the terres-
trial carbon pool by the corresponding amount. Such a re-
turn of investmentof biochar use, that is the increase in
nonPyC SOC and NPP, may be as important for PyCCS
as the PyC sequestration by the biochar itself.
However, the use of large amounts of pure biochar may
not become the final pathway of soil application in the
future. Biochar may serve as raw material for different
agricultural (fertilizer) products rather than being a final
amendment product in itself. For example, biochar made
from invasive weed and harvest residues improved fertilizer
efficiencies and boosted yields in fertile soils in Nepal by
on average 100% when used as a nutrient carrier at low
dosages (<12 t/ha) (Schmidt et al., 2017). Moreover, bio-
char can be used as a tool to further reduce agronomic
GHG emissions (Kammann et al., 2017) as it has been
shown to reduce methane emissions in saturated soils, for
example in rice agriculture (Han et al., 2016; Jeffery, Ver-
heijen, Kammann, & Abalos, 2016), or N
O emissions
from fertilized soils by 40%50% on average (metastudies:
Cayuela et al., 2014; Schirrmann et al., 2017).
While biochar is well established as a means of carbon
sequestration (Brassard, Godbout, & Raghavan, 2016), bio
oil was not yet discussed as such. Biooil, also known
under the names pyrolysis liquids, pyroligneous acid, or
(more historically) wood vinegar, is a very complex liquid
mixture composed of hundreds of different oxygenated
hydrocarbons and water. It is an obligate byproduct of all
kinds of pyrolysis. When biooil is the main intended
pyrolysis product, optimal production parameters are fast
(<1 s) pyrolysis at 500°C (Xie, Xu, Fang, Luo, & Ma,
Fast pyrolysis, biooil is typically viscous but freeflow-
ing and dense (~1.2 kg/L), has usually a dark brown color,
is acidic (pH ~2.5), and has a low net calorific value (NCV
<20 MJ/kg) due to the high oxygen content and moisture
(Mohan, Pittman, & Steele, 2006; Oasmaa, Beld, Saari,
Elliott, & Solantausta, 2015). It is a microemulsion, in
which pyrolytic lignin and other waterinsoluble organic
compounds are dispersed. Pyrogenic organic compounds
dissolved in the aqueous phase serve as emulsifiers, though
it has a strong tendency for phase separation. A decanted
heavy oil phase at the bottom, rich in nonpolar compounds
(mainly pyrolytic lignin), can be distinguished from an
upper aqueous phase rich in polar compounds (light
organic compounds and heavy sugars) (Oasmaa, Fonts,
PelaezSamaniego, GarciaPerez, & GarciaPerez, 2016).
Additionally, a distinctive upper layer rich in extractives
(mainly waxes, fatty acids, phenolics) may form.
A typical composition of biooil made from woody bio-
mass by fast pyrolysis at 500°C includes, in mass percent-
age, 25% water, 20% pyrolytic lignin, 55% of organic
watersoluble compounds (around 30% of sugars produced
from cellulose and hemicellulose and 20% of carbonyls and
alcohols), and small amounts of solid particles including
char, ash, or sand (Bayerbach & Meier, 2009; Oasmaa
et al., 2016, 2015 ).
Biooil can be also obtained from slow pyrolysis pro-
cesses over the whole pyrolysis temperature range (350
900°C) and from all types of biomass feedstocks (Sanna
et al., 2011). Thus, pyrolysis optimized for biochar produc-
tion still yields biooil, though at considerably lower
amounts and with some distinct differences in composition.
At a given temperature, slow pyrolysis biooil has similar
elemental composition on a dry basis, although with the
following differences:
The water content is increased, which leads to enhanced
phase separation.
The sugar content is significantly reduced due to sec-
ondary reactions (AncaCouce, Mehrabian, Scharler, &
Obernberger, 2014; Branca, Giudicianni, & Blasi, 2003).
The pyrolytic lignin yield is reduced.
The production of benzene, toluene, and xylene isomers
(BTX) and polycyclic aromatic hydrocarbons (PAH) is
enhanced to significant values, which can be a concern
for some applications due to their toxicity (Fagernäs,
Kuoppala, & Simell, 2012; Milhé et al., 2013).
Biooil can be employed for heat and power generation in
gas turbines or furnaces and, after an upgrading, as biofuel
for internal combustion engines (Elliott, 2007; Fagernäs,
Kuoppala, Tiilikkala, & Oasmaa, 2012; Kauffman, Dumor-
tier, Hayes, Brown, & Laird, 2014). Here, however, we do
not consider the purpose of energetic use which is of
course possible but would release the carbon back to the
atmosphere. We rather consider applications and uses that
maintain the biooil's carbon sequestered. Instead of com-
busting the nonsolid byproducts of biomass pyrolysis as
suggested by Woolf et al. (2016), the biooil could be
either used in a biorefinery approach (Table 1) or seques-
tered in geological repositories as discussed below.
Before the advent of fossil fuel extraction in the early
20th century, main raw materials for the chemical industry
were produced by wood distillation, which is a historical
name for pyrolytic biooil production. Besides tar and pitch
for building ships and roads, basic chemicals like naph-
thalene, anthracene, aniline, phenol, benzene, methanol,
acidic acid, and acetone were produced with pyrolysis sys-
tems for the nascent chemical industry (Aftalion, 2001).
Until 1950, methanol was still mainly produced through
wood pyrolysis, though by then the much cheaper and
more homogeneous fossil oils replaced the biomass materi-
als as important resource for the chemical industry (Soltes
& Elder, 2017). Currently, 10% of annually produced fossil
oils are used as raw material by the chemical industry
(Keim, 2014). If humanity succeeds in limiting mean glo-
bal warming to 1.5°C or 2°C as specified in the Paris
Agreement (Schleussner et al., 2016, Rockström et al.,
2017), carbon emissions will have to be reduced by 90%
until 2050. Emission reduction of this order can only be
achieved with rapid and complete phasingout fossil fuels
within the next 30 years (Rogelj et al., 2015, Bertram
et al., 2015; Sanderson et al., 2016; Schleussner et al.,
2016). This, however, implicates that the 440 million tons
of fossil oil (OECD, 2018) that are currently extracted and
used as raw material for the chemical industry would have
to be replaced by biomassderived raw chemicals, that is
biooil, cellulose, starch, lactic acid monomers.
Most chemical products that are currently produced
from fossil fuels can as well be produced from biooils in a
biorefinery approach (see Table 1) though today (until CO
emissions are properly taxed) at higher costs.
The most pertinent industrial Cstoring use of biooil is
certainly its blending to asphalt binder for road construc-
tion. Raman, Hainin, Hassan, and Ani (2015) have shown
that the addition of 5%20% of biooil to the asphalt mix-
ture improves asphalt quality like stiffness and durability.
If 10% biooil by weight were added as binder additives
and/or aggregates to 1.8 billion tons of asphalt poured each
year, 180 million tons of carbonized material would be
entombed annually. With a carbon content of 55%, the
amount of sequestered C in asphalt could be 100 million
tons per year. Biooil could further be added to concrete
and other building materials (Czernik & Bridgwater, 2004;
Xie et al., 2013), which would also become longterm
carbon storage deposits, as those materials would end their
material life cycle in other construction works or landfills.
Those applications could be realized already within years,
that is short to mid term.
More challenging is the use of biooil as raw material
for bioplastics and other types of composite materials
(Crombie & Mašek, 2014), which will need advanced
chemical engineering. Depending on the life cycle of the
plastic materials, carbon fibers and carbon composites, the
persistence of the carbon in the terrestrial system would
vary between short, mid, and long term. With the increas-
ing public and political pressure on recycling plastic mate-
rials (instead of waste combustion and landfill dumping),
the carbon contained in the advanced biomaterials could be
stored for much longer timescales in the terrestrial system,
so that the material use and recycling would become a
longterm carbon sink.
Research and development in regard to biorefinery of
biooil is, although based on a long history, currently only
at the beginning though, from the theory, it is rather clear
that biooil could well become a decisive raw material for
the chemical industry once the production of fossil fuels
would be banned. Further possible fields of biooil applica-
tion include agronomy, animal husbandry, pharmaceutical
industry, or wood preservation (Table 1). However, those
latter applications would have a rather short carbon storage
As long as the chemicals or materials using biooil car-
bon are not combusted or otherwise oxidized, the carbon
remains sequestered, augmenting the terrestrial carbon pool.
With advanced endoflife product management, the carbon
of these biooil based products could be recycled or
sequestered in protected deposits at the end of its lifetime,
then still serving as a Csink.
Compared to fossil crude oil, biooil is characterized by a
higher moisture and oxygen content, lower viscosity, and
lower caloric value. However, both liquids are similar in
regard to pumping, transportation, and storage (Czernik &
Bridgwater, 2004; Gueudré et al., 2017; Staš, Chudoba,
Kubicka, Blazek, & Pospíšil, 2017). It can be assumed that
the environmental toxicity of fossil crude and biooil is
similar (Fermoso, Pizarro, Coronado, & Serrano, 2017;
Louwes et al., 2017; Varma & Mondal, 2017; Zhang,
Chang, Wang, & Xu, 2007) though direct comparisons and
ecotoxicological assessments were not yet done. It is clear
that both should not be applied to soil. However, biooil
carbon could, as crude oil was for millions of years, be
sequestered for the long term (>1,000 years) when pumped
into depleted fossil oil deposits (Werner, Schmidt, Gerten,
TABLE 1 Suggested and tested uses of biooilbased products
product and use References
Bioplastics Crombie and Mašek (2014)
Asphalt amendment Raman et al. (2015)
Amendment for
building materials
Czernik and Bridgwater (2004) and Xie
et al. (2013)
Wood preservative Czernik and Bridgwater (2004) and
Tiilikkala, Fagernäs, and Tiilikkala (2010)
Biocide and crop
Tiilikkala et al. (2010)
Feed additive Yamauchi, Ruttanavut, and Takenoyama
(2010), Cai, Jiang, and He (2011) and
Chu et al. (2013)
Plant growth
Ratanapisit, Apiraksakul, Rerngnarong,
Chungsiriporn, and Bunyakarn (2009),
Tiilikkala et al. (2010) and Hagner,
Penttinen, Tiilikkala, and Setälä (2013)
Lucht, & Kammann, 2018). Those deposits would have the
advantage that they are typically deeper than 1,000 m
below the surface, that is deep below the groundwater zone
(Philp, 1985). They would thus be protected from oxygen
and microbial degradation. Any risk of leaching would be
avoided. The biooil carbon could thus, in theory, be
sequestered without any apparent environmental risk while
being protected from decomposition. The geological integ-
rity of the sequestration deposits was demonstrated by the
ability to hold fossil oil for millions of years without leak-
age. Risks of volatilization to the atmosphere, except for
the transportation to the final geological deposit, could be
assumed to be minimal considering that biooil has a poor
volatility compared to fossil oil (Czernik & Bridgwater,
The carbon density of biooil (590750 kg C/m
(Neves, Thunman, Matos, Tarelho, & GómezBarea, 2011))
is slightly lower than that of fossil oil (800 kg C/m
nik & Bridgwater, 2004)) though more than three times
higher than that of liquefied CO
(135220 kg C/m
(IPCC, 2005)), which is proposed to be used for BECCS.
Geologic sequestration of biooil would therefore take less
volume than CO
CCS. Moreover, it would avoid most of
the known and unknown shortand longterm risks associ-
ated with geological storage of CO
leakage, alter-
ation of groundwater chemistry, seismic activity, etc.
(Vaughan & Gough, 2016; Burns & Nicholson, 2017)). In
Werner et al. (2018), the carbon leakage during transporta-
tion of the biooil to the final repository and the millennial
underground storage was assumed to be 2% over 80 years
for the geological biooil storage pathway.
Today, the geological storage of biooil can only be
considered a thought experiment. It certainly seems coun-
terintuitive to replenish fossil oil reservoirs with biooil,
when today's fossil oil extraction continues unabated at
4.4 Gt per year (OECD, 2018). However, it might become
one of the options of last resort when, as it appears today,
the phasing out of fossil fuels will be delayed by one or
more decades. To return atmospheric CO
to a save level, humanity might be soon forced (Rockström
et al., 2016) not only to stop fossil fuel extraction but also
to reverse the direction of liquidC movement to geological
stores using the same pipelines. In the meantime, biooil
may reduce the dependency on fossil fuels by being used
as energy carrier or raw material for the chemical industry.
The biooil can either be stored as one mixed liquid
substance or it can be stored in different fractions, which
are obtained either by phase separation or by fractional
condensation. Fractional condensation of biooil would be
controlled by a liquidvapor equilibrium separating the
heavy tars (polar and nonpolar, including pyrolytic lignin
and heavy sugars) which condense at higher temperatures
and an aqueous phase with light organic molecules which
condense at lower temperatures (Oasmaa et al., 2016). The
composition of each phase can be controlled by the temper-
ature in the fractional condensation when cooling down the
pyrolysis volatiles or by stepwise distillation of biomass
(i.e. recovering volatiles when heating the biomass at 250,
350, 400°C). It would thus be possible to recover first
those parts of the pyrolytic oil that are, already today, eco-
nomically valuable for biobased chemical materials (C
sequestration in economically valuable products) and to
sequester the remaining fractions in geological deposits.
While the aqueous phase of the oil is well pumpable
but has a low pH (<3), the heavy tar fraction is not well
pumpable but has a more neutral pH, which would facili-
tate the intermediate storage of that fraction. The following
biooil properties should further be considered when plan-
ning for transport and storage:
Biooils are incapable of sustaining combustion and can
be classified as nonflammable liquids (Oasmaa et al.,
Biooil is slightly corrosive, and toxicity increases from
fast to slow pyrolysis biooils, which is associated with
a higher concentration of PAHs (Blin, 2005).
Biooil has a high viscosity, commonly in the order of
tens of centistokes, and the viscosity increases during
storage (Mohan et al., 2006).
Shortterm storage should be conducted in the type of
containers recommended for fast pyrolysis oil (Oasmaa
et al., 2016), which are composed of corrosionresistant
steel and materials such as AISI 304, AISI 316, polyte-
trafluoroethylene (PTFE), highdensity polyethylene
(HDPE), and polyvinyl chloride (PVC).
It can be expected that dedicated research and engineer-
ing could solve the mentioned storage and displacement
issues. However, more research is clearly needed, espe-
cially for valuegenerating and cascading uses of biooil for
Csequestering and its environmentally safe longterm stor-
Depending on the process parameters, the carbon contained
in the permanent pyrogas accounts for 15%45% of the
total carbon of the initial biomass (Table 2). To ensure a
high Csequestration efficiency of PyCCS, the gaseous car-
bon should be included in the sequestration scenarios (Fig-
ure 1). Usually, the gas is combusted to produce thermal
energy to drive the pyrolytic process (Crombie & Mašek,
2014) or to produce electricity. However, in conventional
combustion where air is used as oxidizing agent, the flue
gas contains beside CO
and H
O more than 50% N
Separating the flue gas from the N
to obtain pure CO
CCS purposes would be a complex and expensive process
increasing the cost of CO
CCS heavily. It would therefore
only be economically viable in largescale industrial
devices (Reynolds, Ebner, & Ritter, 2006). As one impor-
tant advantage of PyCCS is the option for decentralized,
smallscale production units (e.g. one unit per farm or vil-
lage), this may exclude CO
CCS from gas combustion. A
recent alternative that could well be set up in smallscale
devices is chemicallooping combustion (CLC). In CLC, a
solid oxygen carrier is used for combustion instead of air
(Adanez, Abad, GarciaLabiano, Gayan, & Diego, 2012).
The oxygen carrier, most often based on nickel, iron, or
TABLE 2 Pyrolysis product properties for five PyCCS scenarios
Slow pyrolysis
Slow pyrolysis
Slow pyrolysis
Slow pyrolysis
Fast pyrolysis
Ash content % d.b. 1 1 1 1 1
Initial moisture % w.b. 25 25 25 25 5
Char yield % w.b. 26.1 22.4 17.9 14.4 20.0
C char % 74.6 79.8 83.8 85.4 78.6
H char % 3.4 2.5 1.6 1.0 2.5
O char % 19.1 14.4 10.4 8.4 14.1
Ash char % 2.9 3.3 4.2 5.2 4.8
H/C ratio 0.54 0.38 0.23 0.14 0.38
Liquids yield % w.b. 52.8 56.1 54.3 49.2 61.2
C liquids % d.b. 56.3 56.3 59.9 63.6 56.3
H liquids % d.b. 6.1 6.1 6.4 6.7 6.1
O liquids % d.b. 37.6 37.6 33.6 29.7 37.6
Moisture liquids % w.b. 66.4 62.4 64.5 71.2 28.9
Permanent gas
% w.b. 21.1 21.4 27.7 36.5 18.9
C gases % 37.1 35.1 38.6 44.0 37.5
H gases % 7.1 7.4 6.9 6.5 6.5
O gases % 55.8 57.5 54.5 49.5 56.0
LCV biomass MJ/kg
13.4 13.4 13.4 13.4 17.7
LCV char MJ/kg 27.2 28.7 29.7 29.8 28.3
LCV liquids MJ/kg
5.6 6.6 6.8 5.6 14.7
LCV gases MJ/kg 13.9 13.4 14.5 16.4 13.5
Cdensity of char kg/m
239 298 235
Cdensity of
672 590 734
C in char % 52.1 48.0 40.3 32.9 33.2
C in liquids % 26.8 31.9 31.0 24.1 51.9
C in gases % 21.0 20.2 28.7 43.0 15.0
Leakage BC
%20 10 10 10 10
CSE without CO
%70 74 67 53 81
CSE % 88 94 94 94 95
Note. BC+100: biochar carbon that remains after 100 years after soil amendment; CSE without CO
: CSE of the PyCCS pathway with biochar and biooil seques-
tration only; CSE: total carbon sequestration efficiency of the complete PyCCS pathway; d.b.: based on dry matter; LCV: low caloric value; w.b.: based on wet mat-
ter; PyCCS: pyrolytic carbon capture and storage.
Biomass feedstock for all considered scenarios is woody biomass. The correlations are derived from pyrolysis process parameters, and they are based on the assump-
tions and formula presented in the SI.
manganese oxides, is moved through the permanent pyro-
gas stream in a countercurrent process where the metal
bound oxygen reacts with the gas. Once the oxygen carri-
ers are reduced, they are conveyed out of the combustion
reactor into another reactor where they get reoxidized with
air before being reused. This chemical looping can be
repeated for countless cycles without losing its efficiency
(Adanez et al., 2012). The reaction products of permanent
pyrogas CLC are nearly pure CO
and water, which can
easily be separated by condensation. The CO
could by
then be treated as in conventional CO
CCS scenarios
(Zakkour, Kemper, & Dixon, 2014).
Alternatively, the gases could also be treated with a
chemicallooping reforming (CLR) process that results in
and H
as reaction products (Adanez et al., 2012; de
Diego et al., 2008). While the resulting H
will be a car-
bonneutral energy carrier, the pure CO
could be pro-
cessed for geological sequestration. As this process would
not generate the heat needed for pyrolysis, the required
energy input needs to be generated from renewable electric-
ity (i.e. Epyrolysis). This approach should be investigated
as a new option for power to gas.
CLC and CLR are considered as the most promising
alternative to reduce the costs of CO
capture (Kerr, 2005)
and are fitting technical opportunities to increase the C
transformation efficiency of the PyCCS technology. How-
ever, CLC and CLR in combination with pyrolysis are not
yet widely tested or mature technologies. Hence, they need
further development and upscaling before being imple-
mented at larger scales.
Following Kemper (2015) and Vaughan and Gough
(2016) and assuming that captured CO
is harder to contain
than biooil and biochar, we assume leakage rates of 5%
over 80 years for the geological CO
Biomass contains a wealth of elements beyond CHO.
Although present only in lower concentrations, they are of
high relevance due to their role as plant macroand
micronutrients. After harvest, essential nutrients bound in
biomass should be returned to biomassproducing agroe-
cosystems. Otherwise, soil fertility deteriorates over time
(Hänsch & Mendel, 2009; Ingerslev, Skov, Sevel, & Ped-
ersen, 2011). Already today, the mineral depletion of
agronomically used soils is a point of concern, affecting
global food security (Jones et al., 2013). This would be
further accelerated when biomass is extracted without
returning the minerals it contains to the soil. The latter is
the case in BECCS scenarios where biomass is combusted
to produce energy, and the resulting ashes cannot or can
only partially be returned back to soils due to heavy
metal, PAH, and dioxin contamination (Ingerslev et al.,
2011) or to toxic ash transformation reactions during com-
bustion (Boström et al., 2012). On the other hand, return-
ing the ashes and minerals to the soil with the biochar
will likely deliver a mineral weatheringCCS contribu-
tion to CDR, which would need to be further explored
and quantified.
FIGURE 1 General pyrolytic carbon capture and storage scheme for pyrolytic treatment of biomass, the pathways of solid, liquid, and
gaseous products, their use and sequestration scenarios, the respective Cleakage rates, and the circular effect on carbon farming systems and
sustainable biomass production
Nitrogen is an important nutrient of plants, and its avail-
ability is often limiting for plant growth. In biomass, it is
mainly present in the form of proteins. The main primary
pyrolysis product of proteins at temperatures around 500°C
is amides, which are present in the biooil. Nitrogen is fur-
ther retained to a lower extent in the biochar but also
released in small amounts as NH
and HCN with the gas
phase (Nussbaumer, 2003). At higher temperatures, tars
crack, reducing the Ncontent in the biooil and enhance
the production of NH
and HCN in the permanent pyrogas.
and HCN are precursors of nitrogen oxides (NO
which can form during combustion of the volatiles depend-
ing on the combustion technology employed (Vermeulen,
Block, & Vandecasteele, 2012). However, using a proper
combustion approach, harmful emissions can be minimized
(Nussbaumer, 2003) to near zero (i.e. N
release), in accor-
dance with the clean air regulations that are in place in
industrialized countries such as Germany.
Several elements such as Ca, Si, Mg, Al, Fe, or Ti are
almost entirely retained in the solid fraction due to their
nonvolatile nature. At pyrolysis temperatures of up to
700°C, alkali metals (K and Na) are mainly retained in the
char, but they are partially released to the gas phase above
700°C (van Lith, Jensen, Frandsen, & Glarborg, 2008).
Most of the chlorine and a considerable proportion of sul-
fur are released to the gas phase at temperatures above
400°C where it can be easily scrubbed off (Van Lith, Jen-
sen, Frandsen, & Glarborg, 2008). Cl and Sbearing
organic compounds are further present in the biooil. How-
ever, the sulfur and chlorine content of biooil made from
woody biomass are lower than 100 ppm (Oasmaa et al.,
2015), which is considerably lower than the sulfur content
in crude oil.
Thus, most of the biomass nutrients are retained in the
biochar when slow pyrolysis technology is used at tempera-
tures below 700°C. The biooil is mainly composed of car-
bon, hydrogen, and oxygen, with a minor content of
nitrogen, still smaller amounts of sulfur and chlorine, and
only traces (in the ppm range) of all other elements (Oas-
maa et al., 2015). The nutrient concentrations in biochar
and biooil mainly depend on the initial biomass composi-
tion with woody feedstock having lower and annual harvest
residues have much higher mineral contents, particularly
graminoid species (e.g. switchgrass, miscanthus, or crop
residue of rice, wheat, maize, or others) with their compa-
rably high silicon content.
The overarching aim of PyCCS is to enable lowcost high
Ctransformation rates (i.e. minimum losses of carbon to
the atmosphere) and products with a longterm Cstability.
As biochar is the pyrolytic carbon product that can be
sequestered at the lowest costs and with large cobenefits,
high biochar yields are targeted. As the sequestration of the
carbon from the permanent pyrogases is the most expensive
and technically challenging Csequestration pathway, the
gas production should be minimized. While pyrolysis is
often optimized for the production of one product and the
other two products are considered either a waste or a barely
valued coproduct, in PyCCS scenarios all three pyrolysis
products have to be used to optimize the transformation of
the biomass carbon into pyrogenic forms for longterm C
sequestration. Overall, an optimum between production
costs, robustness of the process, product distribution, qual-
ity and product value, sequestration potential (halflife in
the terrestrial system), and the recycling of biomass
extracted nutrients should be achieved (Appendix S1).
The distribution and characteristics of the solid, liquid,
and gaseous pyrolysis products depend mainly on the
pyrolysis temperature, particle size, residence time of the
pyrolysis volatiles in the kiln, pressure, and feedstock com-
position (AncaCouce, 2016). Slow pyrolysis at low tem-
peratures (350450°C) has the highest solid yield, though
the carbon stability of the biochar is rather low, as is the
quality of the biooil (CampsArbestain et al., 2015; Fager-
näs, Kuoppala, & Simell, 2012). At a given pyrolysis tem-
perature, the biochar yield can further be increased with
slow heating rates, higher residence time of the volatiles,
larger particle size of the feedstock, and higher pressure
(AncaCouce, 2016).
At higher pyrolysis temperatures (700850°C), the per-
manent pyrogas yield is significantly increased; conse-
quently, lower biochar and biooil yields will be obtained
(AncaCouce, Sommersacher, & Scharler, 2017; Sadaka &
Boateng, 2009; Tripathi, Sahu, & Ganesan, 2016). The
resulting biochar contains graphitelike carbon (instead of
amorphous carbon), which increases its recalcitrance, for
example in soil (Budai et al., 2014; Keiluweit, Nico, John-
son, & Kleber, 2010). At these high temperatures, the pyro-
lytic liquids show a higher carbon content and higher
aromaticity and contain a large spectrum of typical tertiary
tars (AncaCouce, 2016). Tertiary tars are molecules free of
oxygen, which can be stable at high temperatures having a
single aromatic ring (BTX) or several rings (PAH). Also,
hightemperature pyrolysis oils have a high content of phe-
nols. Therefore, high concentrations of BTX/PAH and phe-
nols might pose an environmental concern for certain bio
oil use scenarios (e.g. when used in asphalt or for plant
protection), but not when sequestered geologically.
Fast pyrolysis is less suited for the purpose of carbon
sequestration because the overall energy expenditure is
high due to the necessary drying and milling of the feed-
stock and very high heating rates (>500°C/s) (Lédé &
Authier, 2015). Moreover, the fast pyrolysis biochar yield
and quality are rather low (Brewer et al., 2012).
To provide an example for the selection of optimal
PyCCS parameters, we expose in Table 2 the results of an
exemplary calculation of carbon yields, distribution, and
composition for four slow and one fast pyrolysis scenarios
as a function of the pyrolysis temperature according to
Neves et al. (2011). Their comprehensive literature review
of pyrolysis experiments includes data from more than 60
biomass samples with different reactor configurations and
temperatures between 350 and 1,000°C.
Modifying pyrolysis conditions determine yield and
quality of biochar, biooil, and permanent pyrogas. Summa-
rizing the above considerations, we suggest the following
general guidelines to optimize the pyrolysis process condi-
tions for PyCCS scenarios:
Produce a low portion of permanent pyrogas and high
portion of biochar and biooil (avoid temperatures
Maximize the biochar yield compared to biooil, using
rather slow than fast pyrolysis, as it is easier and less
costintensive to sequester biochar, in soils or materials,
than biooil;
Achieve low H/C ratios of <0.4 and thus a high recalci-
trance of biochar by using pyrolysis temperatures not
lower than 450°C.
Based on these guidelines, we suggest using slow pyrol-
ysis with a highest treatment temperature between 500 and
650°C for PyCCSbased CDR. In this temperature range, a
compromise between high biochar yield and its recalci-
trance is achieved for a large spectrum of diverse biomass
feedstocks (Brassard et al., 2016; Weber & Quicker, 2018).
At these temperatures, the gas yield is low, and only few
minerals end up in the biooil. When the resulting biochar
is applied to soil, either directly or via cascading use in
animal husbandry or prior material use (Schmidt, 2012),
most of the minerals (but only reduced portions of nitro-
gen) can be recycled within the biosphere.
However, the suggested temperature range does not
exclude the application of higher or lower pyrolysis tem-
peratures in individual cases. Depending on the economic
scenarios and intended uses of the pyrolysis products, the
production parameters can and sometimes should be
adapted, for example, lower temperatures are recommended
to produce biochar for peat replacement (Kern et al., 2017)
or for soilless media to enhance plant growth and/or dis-
ease suppression (Jaiswal et al., 2018). Higher temperatures
are necessary to produce activated biochar for remediation
of contaminated soils or for electric capacitors (Frack-
owiak, 2007; Hagemann et al., 2018). The latter pyrolysis
conditions will increase the yield of gas, but if the CO
after the oxidation of these gases is captured and stored,
the overall carbon efficiency can still be high.
To pyrolyze biomass, the feedstock has to be harvested,
transported, chipped, or milled. All these processes are cur-
rently executed by fossil fueldriven machinery though it
could equally be powered by carbonneutral electricity.
Except for the proposed concept of Epyrolysis for CLR,
pyrolysis itself has low electric consumption and the neces-
sary thermal energy is provided by the permanent pyrogas
oxidation (Crombie & Mašek, 2014). The postpyrolysis
processing of the products like quenching and milling of
biochar or the pumping of biooil to geological storages
can be done electrically. The application of biochar to soil
necessitates land management machinery, although the car-
bon footprint of an estimated one liter of diesel per ton of
biochar is negligible and could in the near future be exe-
cuted by electric tractors (Lünenbürger, 2012; Tubiello
et al., 2013). Liquefaction and pumping of CO
after CLC
or CLR are equally a process that could be powered by
carbonneutral electricity (Kerr, 2005). The carbon footprint
for the production and maintenance of the machinery dedi-
cated to the preparation, pyrolysis, and postproduction pro-
cesses is compared to the amount of treated carbon
negligible, although detailed calculations are missing in the
literature. Based on these assumptions, we do not include
further Cexpenditures beside the Cleakages of the applied
PyCCS products as considered in the chapters above
(10%20%, 2%, and 5% over 80 years for soilapplied bio-
char, geological biooil storage, and geological CO
age, respectively).
Biochar is suggested as a material for longterm carbon
sequestration since the late 1990 s (Ogawa, 1991; Okimori,
Ogawa, & Takahashi, 2003). However, burning pyrolysis
liquids and gases and sequestering only the biochar result
in Csequestration efficiencies that are too low for making
it a competitive NET (Werner et al., 2018). This is espe-
cially the case when biochar is produced at higher tempera-
tures (>500°C), which is necessary to produce a
recalcitrant product well suited for most material uses.
In earlier studies, the potential of PyCCS was calculated
for harvest residues under the assumption that only the bio-
char is sequestered (Smith, 2016; Woolf et al., 2010, 2016
). Compared to the current practice of burning or decompo-
sition of these residues, pyrolysis would clearly be an
improvement, even if only 40% of the biomassC is eventu-
ally sequestered. However, the calculated NET potential of
0.7 Gt C
/year (Smith, 2016) would, even when doubled
under a complete PyCCSscenario, not be sufficient to ful-
fill current climate change mitigation targets (Fajardy &
Mac Dowell, 2017; Smith et al., 2015). Specific new and
complementary global biomass production would thus be
needed. When biomass production is undertaken for the
purpose of NET, the carbon sequestration efficiency is the
crucial factor that determines the size of the land area
needed for biomass production (Werner et al., 2018).
Increasing the carbon sequestration efficiency of a technol-
ogy will thus decrease the land requirements substantially
(Beringer, Lucht, & Schaphoff, 2011; Boysen, Lucht, Ger-
ten, et al., 2016).
The current benchmark for BECCSbased NETs is a C
sequestration efficiency (CSE) of 90% (Klein et al., 2014),
which can theoretically be attained, but only at high eco-
nomic costs and environmental risks (Fajardy & Mac Dow-
ell, 2017; Smith et al., 2015). PyCCS systems can equally
theoretically attain CSEs of ~90% when the sequestration
of CO
CCS is included and more realistically 70%80%
(Table 2) when only biochar and biooil are sequestered.
Using the latter pathway avoids the high costs, environ-
mental risks, and societal challenges of geological CO
storage. The technology for PyCCS is ready to be imple-
mented across smalltoindustrial scales: Networks of small
production units could be installed avoiding the constraints
of using massive industrial power plants only (Schmidt &
Shackley, 2016). Rather than establishing vast industrial
biomass plantations with their monoculture drawbacks,
their tradeoffs with food production, and other SDGs or
their environmental side effects (Boysen, Lucht, Schellnhu-
ber, et al., 2016), a network of smaller scale PyCCS sys-
tems would allow to establish biomass as a desired and
cultivated coproduct of agriculture, for example in agro-
forestry, silvopasture, and perennial coppicing types of
agricultures (i.e. carbon farming approaches, (Toensmeier,
2016)). However, the logistics of such farmbased PyCCS
systems producing biochar for local soil applications while
delivering the biooil to centralized processing facilities are
challenging especially in tropical and subtropical countries
with poor infrastructure and low degree of economic orga-
If PyCCS generates sustainable tCDR that are paid for
by society (i.e. negative carbon taxes), economic incentives
could be provided for farmers to optimize their land man-
agement with combined crop and biomass production.
Thanks to the plant growthenhancing properties of bio-
charbased fertilization, the same food and feed crop pro-
ductivity per cultivation area could be maintained, while
the focus on additional biomass production could increase
the NPP of agricultural land and thus the terrestrial carbon
accumulation. With biochar being applied back to agricul-
tural soils, preferentially nutrientloaded after cascading use
(Schmidt et al., 2017), most of the nutrients would be
recycled back to the soil, maintaining the soil fertility in
the long term. Thanks to the yield increasing value of bio-
char and the added value of biooil and biochar, once a
market can be established for its material use, the Cse-
questration costs of PyCCS may be expected to be signifi-
cantly lower than for BECCS. However, for the moment
this can only be assumed as it is not yet possible to pro-
vide a comprehensive costbenefit assessment based on
peerreviewed literature.
The expected 25% yield increases in tropical and sub-
tropical climates (Jeffery et al., 2017) following the amend-
ment of biochar to soil would lead to a higher production
of biomass and thus to more positive feedstock toward
PyCCS. Consequentially, the 70%80% Csequestration
efficiency of the biochar and biooil PyCCS pathway could
effectively rise to >90%. Moreover, biochar application
could reduce agricultural nonCO
GHG emissions (Kam-
mann et al., 2017) and most likely increase nonbiochar soil
organic matter (Tian et al., 2016; Weng et al., 2017). Con-
sidering all these secondary climate mitigation effects of
PyCCS, the high Csequestration efficiencies would trans-
late into an even higher climate mitigation potential.
Another major argument for pursuing PyCCS instead of
BECCS is the fact that the supposed massive switch from
fossil fuel energy production to bioenergy production
(170 EJ/year (Smith et al., 2015)) is economically unlikely
at a large scale. Solar and wind energy production costs
are expected to decrease to <0.03 USD/kWh (Kumar Sahu,
2015), whereas prices for bioelectricity production without
CCS range from 0.06 USD with waste materials as feed-
stock to >0.12 USD for lowcost feedstock and can go up
to 0.30 USD when pelletized biomass has to be purchased
(International Renewable Energy Agency, 2012). Although
the transformation of biomass into heat for, for example,
district heating systems in temperate climates may remain
economically viable at current prices of 0.020.04 USD/
kWh, the global need for heating is rather small compared
to the global electricity demand, particularly in tropical cli-
mates. Considering further that biomass will have to
become the principal source of chemicals for Cbased
materials when decarbonization (i.e. the reduction in
anthropogenic carbon emissions) eventually leads to phas-
ing out of fossil carbon (Honary & Singh, 2010), prices for
biomass feedstock and thus for bioenergy will increase
rather than decrease in the future. Hence, the longterm
economic viability of biomassbased electricity production
becomes increasingly unlikely, even if carbonoffset pay-
ments would finance the extra costs for CCS. If the pro-
duction of thermal energy from biomass remains an
important factor for the future energy mix, at least in tem-
perate climates, the biooil and permanent pyrogas of
PyCCS systems hold an interesting potential as flexible
energy carrier to produce heat on demand in the cold
season while it could be sequestered in the warm season or
when market prices for heat are low. Biomass pyrolysis
could also produce fuel, especially methane and hydrogen,
to replace fossil fuel though the carbon sequestration effi-
ciency of the system would be lowered.
Pyrolytic carbon capture and storage is mainly designed
to produce biomaterials that have multiple industrial and
agronomic uses besides sequestering carbon. This does,
however, not exclude that in some scenarios biofuels may
remain for a more or less long transitional period a valu-
able coproduct of PyCCS. While all pyrolytic products
already have an industrial value with a current market
price, the largescale adaptation of the technology will cer-
tainly depend on the price that the global community is
willing to pay per sequestered ton of carbon. The current
price paid by the market for biochar (300600 Eur/t (Sch-
midt & Shackley, 2016)) and biooil (150400 Eur/t (Ali-
baba, 2018)) exceeds by far its energetic value, which is
about 135 and 33 Eur, respectively (based on a caloric
value of 29 GJ/t = 8.1 MWh/t for biochar and 6.8 GJ/
t = 1.9 MWh/t for biooil; an average price of 60 Eur/
MWh electricity (Kost et al., 2013); the average energy
efficiency of 32% for coalfired power plants with CCS
(Goto, Yogo, & Higashii, 2013); and a 10% for investment
and operational costs). It is difficult to foresee how these
market prices for pyrolytic products may develop, once a
massive global expansion of the technology would occur,
although it can be assumed that a quickly increasing offer
would exert pricing pressure before new biocarbonbased
markets develop. The evolution of PyCCS pricing will
mainly depend on the timing of phasingout fossil fuels
where (pyrolytic) biomass carbon will have to replace fossil
carbon as a base material for the chemical industry. Sub-
stantial carbon taxes, paying for carbon sequestration,
would have at least to pay for the economic contingencies
and assure that the pyrogenic carbon is sequestered in the
long term without (for economic reasons) being oxidized to
atmospheric CO
This review demonstrates that PyCCS holds the prospect,
when mediated by a substantial increase in sustainable bio-
mass production, to mitigate global climate change and to
curb the concentration of atmospheric carbon. In contrast
to BECCS, PyCCS is expected to provide additional
ecosystem services, to recycle biomass nutrients within the
biosphere, to be ready for implementation within a shorter
time frame, to be scalable also at the village and farm
levels, to provide advanced products for the bioeconomy,
and to avoid the high costs and risks of liquid CO
tration. The Csequestering use of biooil and biochar as
raw materials for the chemical and construction industry
could increasingly replace fossil oil during the expected
phasing out of fossil fuels. Given the current economic and
political situation, it seems extremely unlikely that, anytime
soon, global governance may decide to set the incentives
to pump biooil into geological storages. However, it may
become an option of last resort if the combustion of fossil
fuels will not be reduced quickly enough within the next
30 years. In the meantime, a mix of PyCCS and BECCS,
where pyrogas is used for methane and hydrogen fuel pro-
duction, and where biochar is applied to soil or used in
biomaterials, could evolve into a way forward to early
adoption of scalable, SDGsupporting CDR technologies.
This study was conducted within the BMBFfunded project
BioCAPCCS, grants no. 01LS1620A and 01LS1620B.
HansPeter Schmidt
Adanez, J., Abad, A., GarciaLabiano, F., Gayan, P., & de Diego, L.
F. (2012). Progress in ChemicalLooping Combustion and
Reforming technologies. Progress in Energy and Combustion
Science,38, 215282.
Aftalion, F. (2001). A history of the international chemical industry.
Philadelphia, PA: Chemical H edn.
Alibaba,, (2018). Pyrolytic oil prices. Retrieved from
k9co [wwwdocument], (accessed, 20180203).
Allen, M. R., Barros, V. R., Broome, J., Cramer, W., Christ, R.,
Church, J. A., Edenhofer, O. (2014). IPCC fifth assessment syn-
thesis report Climate Change 2014 synthesis report. Retrieved
from [WWWDocument] (ac-
cessed 20180322).
Amendola, C., Montagnoli, A., Terzaghi, M., Trupiano, D., Oliva, F.,
Baronti, S., Scippa, G. S. (2017). Short term effects of bio-
char on grapevine fine root dynamics and arbuscular mycorrhizae
production. Agriculture, Ecosystems and Environment,239, 236
AncaCouce, A. (2016). Reaction mechanisms and multiscale mod-
elling of lignocellulosic biomass pyrolysis. Progress in Energy
and Combustion Science,53,4179.
AncaCouce, A., Mehrabian, R., Scharler, R., & Obernberger, I.
(2014). Kinetic scheme of biomass pyrolysis considering sec-
ondary charring reactions. Energy Conversion and Management,
87, 687696.
AncaCouce, A., Sommersacher, P., & Scharler, R. (2017). Online
experiments and modelling with a detailed reaction scheme of single
particle biomass pyrolysis. Journal of Analytical and Applied Pyrol-
ysis,127, 411425.
Atkinson, C. J., Fitzgerald, J. D., & Hipps, N. (2010). Potential mech-
anisms for achieving agricultural benefits from biochar application
to temperate soils: A review. Plant and Soil,337,118. https://d
Barré, P., Angers, D. A., BasileDoelsch, I., Bispo, A., Cécillon, L.,
Chenu, C., & Pellerin, S. (2017) Ideas and perspectives: Can we
use the soil carbon saturation deficit to quantitatively assess the
soil carbon storage potential, or should we explore other strate-
gies? Biogeosciences Discussions,395,112.
Bayerbach, R., & Meier, D. (2009). Characterization of the waterin-
soluble fraction from fast pyrolysis liquids (pyrolytic lignin). Part
IV: Structure elucidation of oligomeric molecules. Journal of Ana-
lytical and Applied Pyrolysis,85,98107.
Beringer, T., Lucht, W., & Schaphoff, S. (2011). Bioenergy produc-
tion potential of global biomass plantations under environmental
and agricultural constraints. GCB Bioenergy,3, 299312. https://d
Bertram, C., Johnson, N., Luderer, G., Riahi, K., Isaac, M., & Eom,
J. (2015). Carbon lock-in through capital stock inertia associated
with weak near-term climate policies. Technological Forecasting
and Social Change,90,6272.
Blin, J. (2005). An assessment of biooil toxicity for safe handling
and transportation. Montpellier, France: CIRADForet, UPR Bio-
masse Energie.
Boateng, A. A., GarciaPerez, M., Masek, O., Brown, R., & Campo, B.
(2015). Biochar production technology. In J. Lehmann & S. D.
Joseph (Eds.), Biochar for environmental management science and
technology, 2nd ed. (pp. 63109), New York, NY: Routledge edn.
Bolinder, M. A., Angers, D. A., Giroux, M., & Laverdière, M. R.
(1999). Estimating C inputs retained as soil organic matter from
corn (Zea Mays L.). Plant and Soil,215,8591.
Borchard, N., Ladd, B., Eschemann, S., Hegenberg, D., Möseler, B.
M., & Amelung, W. (2014). Black carbon and soil properties at
historical charcoal production sites in Germany. Geoderma,232
234, 236242.
Boström, D., Skoglund, N., Grimm, A., Boman, C., Öhman, M.,
Broström, M., & Backman, R. (2012). Ash transformation chem-
istry during combustion of biomass. Energyand Fuels,26,8593.
Boysen, L. R., Lucht, W., Gerten, D., & Heck, V. (2016). Impacts
devalue the potential of largescale terrestrial CO
through biomass plantations. Environmental Research Letters,11,
Boysen, L. R., Lucht, W., Schellnhuber, H. J., Gerten, D., Heck, V.,
& Lenton, T. M. (2016). The limits to globalwarming mitigation
by terrestrial carbon removal. Earths Future,5, 463474.
Braadbaart, F., Poole, I., & van Brussel, A. A. (2009). Preservation
potential of charcoal in alkaline environments: An experimental
approach and implications for the archaeological record. Journal
of Archaeological Science,36, 16721679.
Branca, C., Giudicianni, P., & Di lasi, C. (2003). GC/MS characteri-
zation of liquids generated from lowtemperature pyrolysis of
wood. Industrial and Engineering Chemistry Research,42, 3190
Brassard, P., Godbout, S., & Raghavan, V. (2016). Soil biochar
amendment as a climate change mitigation tool: Key parameters
and mechanisms involved. Journal of Environmental Manage-
ment,181, 484497.
Brewer, C. E., Hu, Y.Y., SchmidtRohr, K., Loynachan, T. E., Laird,
D. A., & Brown, R. C. (2012). Extent of Pyrolysis Impacts on
Fast Pyrolysis Biochar Properties. Journal of Environment Qual-
ity,41, 11151122.
Bruun, E. W., Petersen, C. T., Hansen, E., Holm, J. K., & Haug-
gaardNielsen, H. (2014). Biochar amendment to coarse sandy
subsoil improves root growth and increases water retention. Soil
Use and Management,30, 109118.
Budai, A., Wang, L., Gronli, M., Strand, L. T., Antal, M. J., Abiven,
S., Rasse, D. P. (2014). Surface properties and chemical com-
position of corncob and miscanthus biochars: Effects of produc-
tion temperature and method. Journal of Agricultural and Food
Chemistry,62, 37913799.
Burns, W., & Nicholson, S. (2017). Bioenergy and carbon capture
with storage (BECCS): The prospects and challenges of an emerg-
ing climate policy response. Journal of Environmental Studies and
Sciences,4, 527534.
Cai, K. Z., Jiang, S. T., & He, Y. J. (2011). Effects of bamboo char-
coal including vinegar liquid on growth performance and meat
quality in chinese indigenous breed during fattening. Journal of
Animal and Veterinary Advances,10, 24702473.
CampsArbestain, M., Amonette, J. E., Singh, B., Wang, T., & Sch-
midt, H.P. (2015). A biochar classification system and associated
test methods. In J. Lehmann, & S. Joseph (Eds.), Biochar for
environmental management, earthscan ed. (pp. 165194). London,
UK: Routledge.
Cayuela, M. L., van Zwieten, L., Singh, B. P., Jeffery, S., Roig, A.,
& Sánchez-Monedero, M. A. (2014). Biochars role in mitigating
soil nitrous oxide emissions: A review and meta-analysis. Agricul-
ture, Ecosystems & Environment,191,516.
Cheng, C.H., Lehmann, J., & Engelhard, M. H. (2008). Natural oxi-
dation of black carbon in soils: Changes in molecular form and
surface charge along a climosequence. Geochimica (Beijing)Et
Cosmochimica Acta,72, 15981610.
Chu, G. M., Jung, C. K., Kim, H. Y., Ha, J. H., Kim, J. H., Jung, M.
S., Song, Y. M. (2013). Effects of bamboo charcoal and bam-
boo vinegar as antibiotic alternatives on growth performance,
immune responses and fecal microflora population in fattening
pigs. Animal Science Journal = Nihon Chikusan Gakkaihō,84,
Coppola, A. I., & Druffel, E. R. M. (2016). Cycling of black carbon
in the ocean. Geophysical Research Letters,43, 44774482.
Coppola, A. I., Ziolkowski, L. A., Masiello, C. A., & Druffel, E. R.
M. (2014). Aged black carbon in marine sediments and sinking
particles. Geophysical Research Letters,41, 24272433. https://d
Cornelissen, G., Martinsen, V., Shitumbanuma, V., Alling, V., Breed-
veld, G., Rutherford, D., Mulder, J. (2013). Biochar effect on
maize yield and soil characteristics in five conservation farming
sites in Zambia. Agronomy,3, 256274.
Cotrufo, M. F., Boot, C., Abiven, S., Foster, E. J., Haddix, M., Reis-
ser, M., Schmidt, M. W. I. (2016). Quantification of pyrogenic
carbon in the environment: An integration of analytical
approaches. Organic Geochemistry,100,4250.
CraneDroesch, A., Abiven, S., Jeffery, S., & Torn, M. S. (2013).
Heterogeneous global crop yield response to biochar: A metare-
gression analysis. Environmental Research Letters,8, 44049.
Criscuoli, I., Alberti, G., Baronti, S., Favilli, F., Martinez, C., Cal-
zolari, C., Miglietta, F. (2014). Carbon sequestration and fer-
tility after centennial time scale incorporation of charcoal into
soil. PloS One,9, e91114.
Crombie, K., & Mašek, O. (2014). Investigating the potential for a
selfsustaining slow pyrolysis system under varying operating con-
ditions. Bioresource Technology,162, 148156.
Cross, A., & Sohi, S. P. (2011). The priming potential of biochar
products in relation to labile carbon contents and soil organic mat-
ter status. Soil Biology and Biochemistry,43, 21272134. https://d
Czernik, S., & Bridgwater, A. V. (2004). Overview of applications of
biomass fast pyrolysis oil. Energyand Fuels,18, 590598.
de Diego, L. F., Ortiz, M., Adánez, J., GarcíaLabiano, F., Abad, A.,
& Gayán, P. (2008). Synthesis gas generation by chemicallooping
reforming in a batch fluidized bed reactor using Nibased oxygen
carriers. Chemical Engineering Journal,144, 289298. https://doi.
de la Rosa, J. M., Miller, A. Z., & Knicker, H. (2018). Soilborne
fungi challenge the concept of longterm biochemical recalcitrance
of pyrochar. Scientific Reports,8, 2896.
de la Rosa, J. M., Rosado, M., Paneque, M., Miller, A. Z., &
Knicker, H. (2018). Effects of aging under field conditions on bio-
char structure and composition: Implications for biochar stability
in soils. Science of the Total Environment,613614, 969976.
EBC (2012). European biochar certificate Guidelines for a sustain-
able production of biochar. Version 7.1 of 22nd December 2015.
European Biochar Foundation. Retrieved from [WWWDocument] (accessed 20180305).
Elliott, D. C. (2007). Historical developments in hydroprocessing bio
oils. Energy and Fuels,21, 17921815.
Erb, K.H., Kastner, T., Plutzar, C., Bais, A. L. S., Carvalhais, N.,
Fetzel, T., Luyssaert, S. (2017). Unexpectedly large impact of
forest management and grazing on global vegetation biomass. Nat-
Fagernäs, L., Kuoppala, E., & Simell, P. (2012). Polycyclic aromatic
hydrocarbons in birch wood slow pyrolysis products. Energy &
Fuels,26, 69606970.
Fagernäs, L., Kuoppala, E., Tiilikkala, K., & Oasmaa, A. (2012).
Chemical composition of birch wood slow pyrolysis products.
Energyand Fuels,26, 12751283.
Fajardy, M., & Mac Dowell, N. (2017). Can BECCS deliver sustain-
able and resource efficient negative emissions? Energyand Envi-
ronmental Science,10, 13891426.
Fermoso, J., Pizarro, P., Coronado, J. M., & Serrano, D. P. (2017).
Advanced biofuels production by upgrading of pyrolysis biooil.
Wiley Interdisciplinary Reviews: Energy and Environment,6,1
Foereid, B., Lehmann, J., & Major, J. (2011). Modeling black carbon
degradation and movement in soil. Plant and Soil,345, 223236.
Fowles, M. (2007). Black carbon sequestration as an alternative to
bioenergy. Biomass and Bioenergy,31, 426432.
Frackowiak, E. (2007). Carbon materials for supercapacitor applica-
tion. Physical Chemistry Chemical Physics,9, 1774. https://doi.
Fuss, S., Canadell, G., Peters, G. P., Tavoni, M., Andrew, R. M.,
Ciais, P., Yamagata, Y. (2014). Betting on negative emissions.
Nature Climate Change,4, 850853.
Glaser, B., & Birk, J. (2012). State of the scientific knowledge on
properties and genesis of Anthropogenic Dark Earths in Central
Amazonia ( terra preta de Índio). Geochimica (Beijing)Et Cos-
mochimica Acta,82,3951.
Goto, K., Yogo, K., & Higashii, T. (2013). A review of efficiency
penalty in a coalfired power plant with postcombustion CO2
capture. Applied Energy,111, 710720.
Gu, X., Wang, Y., Lai, C., Qiu, J., Li, S., Hou, Y., Zhang, S.
(2014). Microporous bamboo biochar for lithiumsulfur batteries.
Nano Research,8, 129139.
Güereña, D. T., Lehmann, J., Thies, J. E., Enders, A., Karanja, N., &
Neufeldt, H. (2015). Partitioning the contributions of biochar
properties to enhanced biological nitrogen fixation in common
bean (Phaseolus vulgaris). Biology and Fertility of Soils,51, 479
Gueudré, L., Chapon, F., Mirodatos, C., Schuurman, Y., Vender-
bosch, R., Jordan, E., Gutierrez, R. M. (2017). Optimizing the
biogasoline quantity and quality in fluid catalytic cracking core-
fining. Fuel,192,6070.
Gupta, S., & Kua, H. W. (2017). Factors Determining the Potential of
Biochar As a Carbon Capturing and Sequestering Construction
Material: Critical Review. Journal of Materials in Civil Engineer-
ing,29, 4017086.
Hagemann, N., Spokas, K., Schmidt, H.P., Kägi, R., Böhler, M. A.,
& Bucheli, T. D. (2018). Activated carbon, biochar and charcoal:
Linkages and synergies across pyrogenic carbons ABCs. Water
(Switzerland),10, 182.
Hagner, M., Penttinen, O.P., Tiilikkala, K., & Setälä, H. (2013). The
effects of biochar, wood vinegar and plants on glyphosate leach-
ing and degradation. European Journal of Soil Biology,58,17.
Han, X., Sun, X., Wang, C., Wu, M., Dong, D., Zhong, T., Wu,
W. (2016). Mitigating methane emission from paddy soil with
ricestraw biochar amendment under projected climate change.
Scientific Reports,6, 24731.
Hänsch, R., & Mendel, R. R. (2009). Physiological functions of min-
eral micronutrients (Cu, Zn, Mn, Fe, Ni, Mo, B, Cl). Current
Opinion in Plant Biology,12, 259266.
Hansen, J., Sato, M., Kharecha, P., von Schuckmann, K., Beerling, D.
J., Cao, J., Ruedy, R. (2017). Young peoples burden:
Requirement of negative CO
emissions. Earth System Dynamics,
8, 577616.
Heck, V., Gerten, D., Lucht, W., & Popp, A. (2018). Biomassbased
negative emissions difficult to reconcile with planetary boundaries.
Nature Climate Change,8, 151155.
Hockaday, W. C., Grannas, A. M., Kim, S., & Hatcher, P. G. (2007).
The transformation and mobility of charcoal in a fireimpacted
watershed. Geochimica (Beijing)Et Cosmochimica Acta,71, 3432
Honary, L., & Singh, B. P. (2010). Industrial oil types and uses. In
B. P. Singh (Ed.), Industrial crops and uses (p. 157ff). Walling-
ford, UK: CABI.
Ingerslev, M., Skov, S., Sevel, L., & Pedersen, L. B. (2011). Element
budgets of forest biomass combustion and ash fertilisation A
Danish casestudy. Biomass and Bioenergy,35, 26972704.
International Renewable Energy Agency (2012). Renewable energy
technologies: Cost analysis series. International Renewable Energy
Agency (IRENA),1, 274.
IPCC (2005). IPCC special report on carbon dioxide capture and stor-
age. In B. Metz, O. Davidson, H. C. de Coninck, M. Loos, & L.
A. Meyer (Eds.), Prepared by Working Group III of the Intergov-
ernmental Panel on Climate. Cambridge: Cambridge University
Press, 442 pp.
Jaffe, R., Ding, Y., Niggemann, J., Vahatalo, A. V., Stubbins, A., Spen-
cer, R. G. M., Dittmar, T. (2013). Global charcoal mobilization
from soils via dissolution and riverine transport to the oceans.
Science,340, 345347.
Jaiswal, A. K., Elad, Y., Cytryn, E., Graber, E. R., & Frenkel, O.
(2018). Activating biochar by manipulating the bacterial and fun-
gal microbiome through preconditioning. New Phytologist,219
(1), 363377.
Jeffery, S., Abalos, D., Prodana, M., Bastos, A. C., van Groenigen, J.
W., Hungate, B. A., & Verheijen, F. (2017). Biochar boosts tropi-
cal but not temperate crop yields. Environmental Research Letters,
12, 53001.
Jeffery, S., Abalos, D., Spokas, K. A., & Verheijen, G. A. (2015).
Biochara effects on crop yield. In J. Lehmann, & S. Joseph
(Eds.), Biochar for environmental management, Routledge ed.
(pp. 301326). London, UK: Earthscan.
Jeffery, S., Verheijen, F. G. A., Kammann, C., & Abalos, D. (2016).
Biochar effects on methane emissions from soils: A metaanalysis.
Soil Biology and Biochemistry,101, 251258.
Jones, D. L., Cross, P., Withers, P. J. A., DeLuca, T. H., Robinson,
D. A., Quilliam, R. S., EdwardsJones, G. (2013). Review:
Nutrient stripping: The global disparity between food security and
soil nutrient stocks (ed Kardol P). Journal of Applied Ecology,50,
Kammann, C., Ippolito, J., Hagemann, N., Borchard, N., Cayuela, M.
L., Estavillo, J. M., WrageMönnig, N. (2017). Biochar as a
tool to reduce the agricultural greenhousegas burden knowns,
unknowns and future research needs. Journal of Environmental
Engineering and Landscape Management,25, 114139. https://d
Kauffman, N., Dumortier, J., Hayes, D. J., Brown, R. C., & Laird, D.
A. (2014). Producing energy while sequestering carbon? The rela-
tionship between biochar and agricultural productivity. Biomass
and Bioenergy,63, 167176.
Keiluweit, M., Nico, P. S., Johnson, M., & Kleber, M. (2010).
Dynamic molecular structure of plant biomassderived black car-
bon (biochar). Environmental Science and Technology,44, 1247
Keim, W. (2014). Fossil feedstockswhat comes after? In M. Bertau,
H. Offermanns, L. Plass, F. Schmidt, & H.-J. Wernicke (Eds.),
Methanol: The Basic Chemical and Energy Feedstock of the
Future (pp. 2337). Berlin: Springer.
Kemper, J. (2015). Biomass and carbon dioxide capture and storage:
A review. International Journal of Greenhouse Gas Control,40,
Kern, J., Tammeorg, P., Shanskiy, M., Sakrabani, R., Knicker, H.,
Kammann, C., Glaser, B. (2017). Synergistic use of peat and
charred material in growing media an option to reduce the pres-
sure on peatlands? Journal of Environmental Engineering and
Landscape Management,25, 160174.
Kerr, H. (2005). Capture and separation technology gaps and priority
research needs. In D. Thomas, & S. M. Benson (Eds.), Carbon diox-
ide capture for storage in deep geologic formationsresults from the
capture project (pp. 11131128). Oxford, UK: Elsevier.
Klein, D., Luderer, G., Kriegler, E., Strefler, J., Bauer, N., Leimbach,
M., Edenhofer, O. (2014). The value of bioenergy in low stabi-
lization scenarios: An assessment using REMINDMAgPIE. Cli-
matic Change,123, 705718.
Koeve, W., Keller, D. P., & Oschlies, A. (2017). Modelbased assess-
ment of the CO
sequestration potential of coastal ocean alkalin-
ization. Earths Future,5, 12521266.
Kost, C., Mayer, J. N., Thomsen, J., Hartmann, N., Senkpiel, C., Phi-
lipps, S., Schlelgl, T. (2013). Levelized cost of electricity. Renew-
able energy technologies. Freiburg, Germany: Fraunhofer ISE.
Kumar, A., Madden, D. G., Lusi, M., Chen, K.J., Daniels, E. A.,
Curtin, T., Zaworotko, M. J. (2015). Direct air capture of CO
by physisorbent Materials. Angewandte Chemie International Edi-
tion,54, 1437214377.
Kumar Sahu, B. (2015). A study on global solar PV energy develop-
ments and policies with special focus on the top ten solar PV
power producing countries. Renewable and Sustainable Energy
Reviews,43, 621634.
Kuzyakov, Y., Bogomolova, I., & Glaser, B. (2014). Biochar stability
in soil: Decomposition during eight years and transformation as
assessed by compoundspecific 14C analysis. Soil Biology and
Biochemistry,70, 229236.
Laird, D. A. (2008). The charcoal vision: A winwinwin scenario
for simultaneously producing bioenergy, permanently sequestering
carbon, while improving soil and water quality. Agronomy Jour-
nal,100, 178.
Lal, R. (2011). Sequestering carbon in soils of agroecosystems. Food
Policy,36, S33S39.
Lédé, J., & Authier, O. (2015). Temperature and heating rate of solid
particles undergoing a thermal decomposition. Which criteria for
characterizing fast pyrolysis? Journal of Analytical and Applied
Lehmann, J., Abiven, S., Kleber, M., Pan, G., Singh, B. P., Sohi, S.
P., & Zimmerman, A. R. (2015). Persistence of biochar in soil. In
J. Lehmann & S. D. Joseph (Eds.), Biochar for environmental
management (pp. 235282). New York, NY: Routledge ed.
Lehmann, J., Gaunt, J., & Rondon, M. (2006). Biochar sequestration
in terrestrial ecosystems a review. Mitigation and Adaptation
Strategies for Global Change,11, 395419.
Lehmann, J., Rillig, M. C., Thies, J., Masiello, C. A., Hockaday, W.
C., & Crowley, D. (2011). Biochar effects on soil biota A
review. Soil Biology and Biochemistry,43, 18121836. https://doi.
Lorenz, K., & Lal, R. (2014). Biochar application to soil for climate
change mitigation by soil organic carbon sequestration. Journal of
Plant Nutrition and Soil Science,177, 651670.
Louwes, A. C., Basile, L., Yukananto, R., Bhagwandas, J. C., Bramer,
E. A., & Brem, G. (2017). Torrefied biomass as feed for fast pyroly-
sis: An experimental study and chain analysis. Biomass and Bioen-
ergy,105, 116126.
Lünenbürger, B. (2012). Klimaschutz und Emissionshandel in der
Landwirtschaft. Umweltbundesamt. Retrieved from https://www. (Accessed: 20th July 2018).
Maestrini, B., Abiven, S., Singh, N., Bird, J., Torn, M. S., & Schmidt,
M. W. I. (2014). Carbon losses from pyrolysed and original wood
in a forest soil under natural and increased N deposition. Biogeo-
sciences,11, 51995213.
Major, J., Lehmann, J., Rondon, M., & Goodale, C. (2010). Fate of
soilapplied black carbon: Downward migration, leaching and soil
respiration. Global Change Biology,16, 13661379. https://doi.
Matovic, D. (2011). Biochar as a viable carbon sequestration option:
Global and Canadian perspective. Energy,36, 20112016.
Milhé, M., Van de Steene, L., Haube, M., Commandré, J. M., Fassi-
nou, W. F., & Flamant, G. (2013). Autothermal and allothermal
pyrolysis in a continuous fixed bed reactor. Journal of Analytical
and Applied Pyrolysis,103, 102111.
Minasny, B., Arrouays, D., McBratney, A. B., Angers, D. A., Cham-
bers, A., Chaplot, V., Winowiecki, L. (2017). Rejoinder to
comments on Minasny et al., 2017 soil carbon 4 per mille. Geo-
Minasny, B., Malone, B. P., McBratney, A. B., Angers, D. A.,
Arrouays, D., Chambers, A., Winowiecki, L. (2017). Soil car-
bon 4 per mille. Geoderma,292,5986.
Mohan, D., Pittman, C. U., & Steele, P. H. (2006). Pyrolysis of
wood/biomass for biooil: A critical review. Energy and Fuels,
20, 848889.
Mohan, D., Sarswat, A., Ok, Y. S., & Pittman, C. U. (2014). Organic
and inorganic contaminants removal from water with biochar, a
renewable, low cost and sustainable adsorbent A critical review.
Bioresource Technology,160, 191202.
Montserrat, F., Renforth, P., Hartmann, J., Leermakers, M., Knops,
P., & Meysman, F. J. R. (2017). Olivine dissolution in seawater:
Implications for CO
sequestration through enhanced weathering
in coastal environments. Environmental Science and Technology,
51, 39603972.
Moosdorf, N., Renforth, P., & Hartmann, J. (2014). Carbon dioxide
efficiency of terrestrial enhanced weathering. Environmental
Science and Technology,48, 48094816.
Neves, D., Thunman, H., Matos, A., Tarelho, L., & GómezBarea, A.
(2011). Characterization and prediction of biomass pyrolysis prod-
ucts. Progress in Energy and Combustion Science,37, 611630.
Nussbaumer, T. (2003). Combustion and cocombustion of biomass:
Fundamentals, technologies, and primary measures for emission
reduction.Energyand Fuels,17, 15101521.
Oasmaa, A., Fonts, I., PelaezSamaniego, M. R., GarciaPerez, M. E.,
& GarciaPerez, M. (2016). Pyrolysis oil multiphase behavior and
phase stability: A review. Energy and Fuels,30, 61796200.
Oasmaa, A., Källi, A., Lindfors, C., Elliott, D. C., Springer, D., Pea-
cocke, C., & Chiaramonti, D. (2012). Guidelines for transporta-
tion, handling, and use of fast pyrolysis biooil. 1. flammability
and toxicity. Energy and Fuels,26, 38643873.
Oasmaa, A., Vann De Beld, B., Saari, P., Elliott, D. C., & Solan-
tausta, Y. (2015). Norms, standards, and legislation for fast pyrol-
ysis biooils from lignocellulosic biomass. Energy and Fuels,29,
Obersteiner, M., Bednar, J., Wagner, F., Gasser, T., Ciais, P., Forsell,
N., SchmidtTraub, G. (2018). How to spend a dwindling
greenhouse gas budget. Nature Climate Change,8,710. https://d
OECD (2018). Crude oil production (indicator). (Accessed on, 13
June, 2018).
Ogawa, M. (1991). The earths green saved with charcoal. Tokyo,
Japan: Nihon Keizai Shimbun.
Okimori, Y., Ogawa, M., & Takahashi, F. (2003). Potential of Co
emission reductions by carbonizing biomass waste from industrial
tree plantation in South Sumatra, Indonesia. Mitigation and Adap-
tation Strategies for Global Change,8, 261280.
Philp, R. P. (1985). Petroleum Formation and Occurrence. Eos,
Transactions American Geophysical Union,66, 643. https://doi.
Raman, N. A. A., Hainin, M. R., Hassan, N. A., & Ani, F. N. (2015).
A review on the application of biooil as an additive for asphalt.
Jurnal Teknologi,72, 105110.
Rasse, D. P., Budai, A., OToole, A., Ma, X., Rumpel, C., & Abiven,
S. (2017). Persistence in soil of Miscanthus biochar in laboratory
and field condition. PLoS ONE,12,117.
Ratanapisit, J., Apiraksakul, S., Rerngnarong, A., Chungsiriporn, J., &
Bunyakarn, C. (2009). Preliminary evaluation of production and
characterization of wood vinegar from rubberwood. Songk-
lanakarin Journal of Science and Technology,31, 343349.
Reisser, M., Purves, R. S., Schmidt, M. W. I., & Abiven, S. (2016).
Pyrogenic carbon in soils: A literaturebased inventory and a glo-
bal estimation of its content in soil organic carbon and stocks.
Frontiers in Earth Science,4,114.
Reynolds, S. P., Ebner, A. D., & Ritter* JA,, (2006). Stripping PSA
cycles for CO
recovery from flue gas at high temperature using a
hydrotalcitelike adsorbent. Industrial and Engineering Chemistry
Research,45, 42784294.
Riahi, K., Kriegler, E., Johnson, N., Bertram, C., den Elzen, M.,
Eom, J., Edenhofer, O. (2015). Locked into Copenhagen
pledges Implications of shortterm emission targets for the cost