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ORIGINAL RESEARCH
published: 14 February 2020
doi: 10.3389/fenrg.2020.00015
Frontiers in Energy Resear ch | www .fr ontiersin.org 1 February 2020 | V olume 8 | Article 15
Edited by:
Camille Petit,
Imperial College London,
United Kingdom
Reviewed by:
Hannu-Petteri Mattila,
Independent Researcher ,
Parainen, Finland
Rosa Marisa Cuellar -Franca,
University of Manchester ,
United Kingdom
*Correspondence:
André Bardow
[email protected]
Specialty section:
This article was submitted to
Carbon Capture, Storage, and
Utilization,
a section of the journal
Frontiers in Energy Research
Received: 18 October 2019
Accepted: 23 January 2020
Published: 14 February 2020
Citation:
Müller LJ, Kätelhön A, Bachmann M,
Zimmermann A, Sternberg A and
Bardow A (2020) A Guideline for Life
Cycle Assessment of Carbon Capture
and Utilization.
Front. Energy Res. 8:15.
doi: 10.3389/fenrg.2020.00015
A Guideline for Life Cycle
Assessment of Carbon Captur e and
Utilization
Leonard Jan Müller 1 , Arne Kätelhön 1 , Marvin Bachmann 1 , Arno Zimmerm ann 2 ,
André Sternberg 3 and André Bardow 1, 4 *
1 Institute for T echnical Thermodynamics, RWTH Aachen University , Aachen, Germany , 2 Department of T echnical Chemistr y ,
T echnische Universität Berlin, Berlin, Germany , 3 Fraunhofer Institute for Solar Energy Systems (ISE), Freiburg, Germany ,
4 Institute of Energy and Climate Research - Energy Systems Engineering (IEK-10), Forschungszentrum Jülich GmbH, Jülich,
Germany
Carbon Capture and Utilization (CCU) is an emerging field pr oposed for emissions
mitigation and even negative emissions. These potential benefits need to be assessed
by the holistic method of Life Cycle Assessment (LCA) that accounts for multiple
envir onmental impact categories over the entire life cycle of pr oducts or services.
However , even though LCA is a standardized method, curr ent LCA practice differs widely
in methodological choices. The resulting LCA studies show large variability which limits
their value for decision support. Applying LCA to CCU technologies leads to further
specific methodological issues, e.g., due to the double role of CO 2 as emission and
feedstock. In this work, we therefor e present a compr ehensive guideline for LCA of CCU
technologies. The guideline has been development in a collaborative process involving
over 40 experts and builds upon existing LCA standar ds and guidelines. The presented
guidelines should improve comparability of LCA studies thr ough clear methodological
guidance and pr edefined assumptions on feedstock and utilities. T ransparency is
incr eased through interpr etation and r eporting guidance. Improved comparability should
help to strengthen knowledge-based decision-making. Consequently , r esearch funds
and time can be allocated more ef ficiently for the development of technologies for climate
change mitigation and negative emissions.
Keywords: CO 2 utilization, CCU, carbon captur e and use, life cycle assessment, LCA, standardization, carbon
capture and utilization, guideline
INTRODUCTION
Carbon capture and utilization (C CU) involves the capture of the greenhouse gas CO 2 from point
sources or ambient air and its subsequent conversion into valua ble products ( Baena-Moreno et al.,
2019 ). By converting CO 2 into valuable products, CCU aims to improve economic benefits while
also reducing environmental impacts such as the impact on climate change or fossil resour ce
depletion ( Al-Mamoori et al., 2017 ). However , the reduction of environmental impacts cannot
be taken for granted: high energetic co-react ants such as hydrogen ( Sternberg and Bardow,
2016 ) or epoxide are often needed to activate th e chemically inert CO 2 ( von der Assen and
Bardow, 2014 ). The production of these hig h energetic co-reactants, however , is associated with
high environmental impacts. Thus, whet her CCU technologies reduce environmental impacts
can only be concluded from a detailed environment al assessment. A method for environmental

Müller et al. Guideline for LCA of CCU
assessment with broad acceptance among academic and
industrial practitioners is Life Cycle A ssessment (LCA).
E ven though, LCA has been standardized in ISO 14040/14044
( European Committee for Standardis ation, 2009, 2018 ), the
standard leaves methodological choices, e.g., for selecting the
functional unit, system boundaries, background processes,
or environmental impact assessment methods ( European
Commission, 2018 ). As a resu lt, LCA studies on CCU
technologies are often not comparable, e.g., because of differences
in functional units, i.e., the relative basis for which environmental
impacts are assessed, or system boundaries. E ven if functional
units and system boundaries are comparable, LCA re sults often
show significant variation for identical technologies, because
different processes are selected for the production of feedstocks
or utilities. In particular , the supply of electricity or hydrogen has
been shown to vary largely between various LCA studie s such
that conclusions even change qualitatively ( Artz et al., 2018 ). For
example, for CO 2 -based methanol, LCA studies in the literature
reported cradle-to-gate carbon footprints between − 1.7 and
+ 9.7 kg of CO 2,eq per kg of met hanol. The conclusions of these
studies are thus qualitatively very different: CO 2 -b ased methanol
could either even be a carbon sink over its life cycle or emits much
more CO 2 than fossil-based methanol. However , harmonization
of assumptions regarding supply of electricity and CO 2 reduced
the variation such that all carbon footprints had the s ame sign
and could be clearly distinguished from fossil-based methanol.
The current lack of a consistent basis for LCA hampers proper
decision making of stakeholders involved in CCU te chnologies
and, in fact, may also lead sub-optimal decisions. As a result,
both the academic literature ( Cuéllar-Franca and Azapagic, 2015;
N aims et al., 2015 ) and the S cientific Advice Mechanism (SAM)
of the European Commission ( European Commission, 2018 ) call
for specific guidelines for LCA on CCU technologies.
Specific LCA guidelines have been developed in several areas
such as e.g., photovoltaic electricity ( Frischknecht et al., 2016 ),
buildings ( M almqvist et al., 2011 ), aggregates for construction
( Blengini et al., 2012 ), bio-based product ( European Commission
- Joint Research Center, 2011b, 2018 ), or industrial symbiosis
( Mattila et al., 2012 ). These specific LCA guidelines ha ve
also been developed based on t he ISO standard and further
refined based on main research questions in the specific area.
By providing a consistent framework to address these main
research que stions, specific LCA guidelines have been important
in advancing the adoption of environmental assessment in the
respective fields.
We therefore developed t he first guideline for standardized
LCA of CCU technologies ( Zimmerman et al., 2018 ). The
guideline aims to enhance transparency, comparability and
reliability of LCA studies for CCU technologies. In particular , the
guideline identifies pitfalls causing ambiguity when assessing the
environmental impact reduction potential of CCU te chnologies
and offers guidance on how to a void these pitfalls based on
existing standards and guidelines. The guideline was developed
in a 1-year project in cooperation with TU Berlin, University of
Sheffield and the Institute for Advanced Sustainability Studies in
Potsdam. A guideline for Techno-economic Assessment (TEA)
was developed in parallel ( Zimmerman et al., 2018 ).
In this paper , we present the content of t he guideline tailored
for a broad scientific audience. For t his purpose, we give an
over view of the de velopment process of the guidelines in
section Approach. In section General Introduction to Life Cycle
As sessment, we present the content of the guideline. Here, we
provide a short introduction to LCA followed by the identified
pitfalls sorted according to the four phases of LCA. For the
first phase of LCA, the goal and scope definition, we provide
examples for goal definitions for studies on CCU technologies,
unified functional units and system boundaries with respect to
the goal of the study and a hierarchy of methods to solve multi-
functionality. For the second phase, the life cycle inventory, we
present general requirements for the selection of inventory sets
and reference processes and methods to bridge data gaps. For
the third phase, the life cycle impact assessment, we provide
guidance for the selection of impact assessment methods with
respect to regions and on how to account for temporary storage
of CO 2 . In the fourth and last phase of LCA, the life cycle
interpretation, we specify requirements for uncert ainty and
sensitivity analysis, provide guidance on how to interpret neutral
and negative environmental impacts.
APPROACH
The basis for the guideline was literature on LCA methodology
covering the following standards ( European Committee for
Standardisation, 2009, 2017, 2018; BSI, 2 011; AFNOR, 2016 ),
guidelines ( World Resour ces Institute and World Business
Council for Sustainable Development ; European Commission -
Joint Research Center, 2011a, 2012 ), textbooks ( Baumann and
Tillman, 2004; Guinée, 2006; Curran, 2012 ), and scientific peer -
reviewed publications on LCA methodology and LCA studies on
CCU ( Artz et al., 2018 ). Building upon t his analysis, a first draft
document was created and discussed with six external experts (1
industry, 2 academia, 3 policy; 5 countries; 60% women) during
the first of two in-person discussion workshops. The discussions
of workshop 1 provided the basis further de velopment of
guidelines, which was then discussed with a large group of 39
external participants (26% industry, 46% academia, 28% policy;
11 countries, 28% women) during the second workshop. After
the second workshop, the guideline was re vised and then finally
reviewed by three academic researchers and an official of the
German Federal Environmental Agency (UB A) (“peer-review”).
After final revision, the guideline document were published in
Deep Blue Data, t he repository of the University of Michigan.
In this paper , we present the methodological core of t he
LCA guidelines, in particular shall, should and may rules. Sh all
rules are the minimum requirements that are re commended to
achieve a standardized TEA/LCA for CCU. Every LCA produced
using this guideline must cover these basic rules. All rules
in this category have to be addressed. S hould rules cover a
recommended level of analysis and should be applied to produce
LCA of greater depth. U se of may rules produces the gre atest
detail of LCA. These rules may not be applicable in all studies
and should be applied as determined by the practitioner. Note
that this work leaves out ma jor parts of LCA basics contained in
the full guideline.
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Müller et al. Guideline for LCA of CCU
GENERAL INTRODUCTION TO LIFE
CYCLE ASSESSMENT
Life cycle assessment is a methodology to account for the
environmental impacts of a product or ser vice throughout
its entire life cycle ( Figure 1 ). The entire life cycle spans
FIGURE 1 | The holistic approach of life cycle assessment accounts for
environmental impacts associated over the entir e life cycle with all stages of
product’ s life cycle (circle in the middle).
from cradle-to-gra ve: from raw material extraction through
production, packaging, use, end-of-life treatment and recycling
to final disposal. Through e ach stage, the product ’ s life cycle
interacts with the environment by consuming natural resources
and emitting pollutants. Life cycle assessment is a quantitative
method to describe these interactions and t heir potential
environmental impacts 1 . Due to its holistic approach, LCA
a voids problem shifting between both environmental impact
categories and life cycle stages. Therefore, LCA is a valuable
tool in various fields, e.g., product or process design, decision
making in industry and policy as well as marketing. The LCA
methodology was standardized in t he 1990s by the international
standardization organization (ISO) in ISO 14040 and 14044
and is still updated and extended regularly (most recently in
May 2018).
A c cording to the ISO standard, a LCA study is sub-divided in
four phases ( Figure 2 ):
1. Goal and Scope definition
2. Life cycle inventory analysis
3. Life cycle impact assessment
4. Interpretation.
All phases are interdependent, e.g., the gathered life cycle
inventories ha ve to fit to the goal and scope with respe ct to
time and space. In practice, this interdependence renders LCA an
iterative approach, as data availa bility is often not fully known at
the beginning of an LCA study. Furthermore, the entire life cycle
assessment framework is influenced and by its supposed direct
applications and the other way around ( Figure 2 ).
1 In this paper , the term “environmental impacts ” is used instead of “potential
environmental impacts ” to improve re adability. However , LCA is not able to as sess
actual environmental impacts.
FIGURE 2 | General framework for life cycle assessment ( European Committee for Standardisat ion, 2009 ).
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Müller et al. Guideline for LCA of CCU
GOAL DEFINITION
E very LCA study starts with the goal definition by
unambiguously stating “the intended applica tion of the
study, the reasons for carrying out t he study, the intended
audience of the study and whether the results are to be used in
comparative assertions disclosed to public ( European Committee
for Standardisation, 2018 ).” In ot her words, the central question
of the study is defined. However , many questions may be
answered by LCA. To get an over view, we here st art by
identifying typical goal definitions for CCU from literature. Most
CCU technologies are in stages of early de velopment and aim
to reduce environmental impacts. Therefore, most LCA studies
on CCU aim at quantifying the potenti al environmental impact
reductions of CCU processes or products in comparison to
existing processes ( Aresta and Galatola, 1999; Aresta et al., 2002;
Kim et al., 2011; Anicic et al., 2014; Souza et al., 2014; van der
Giesen et al., 2014; von der As sen and Bardow, 2014; Luu et al.,
2015; Al-Kalbani et al., 2016; Gar cia-Herrero et al., 2016; Hoppe
et al., 2016, 2017; Matzen and Demirel, 2016; Schakel et al.,
2016; Sternberg and Bardow, 2016; P arra et al., 2017; Sternberg
et al., 2017; Uusitalo et al., 2017; Zhang et al., 2017 ). Most
studies also include a contribution analysis of environmental
impacts to identify opportunities for improvement ( Aresta
and Galatola, 1999; Aresta et al., 2002; Kim et al., 2011; van
der Giesen et al., 2014; von der As sen and Bardow, 2014; Luu
et al., 2015; Garcia-Herrero et al., 2016; M atzen and Demirel,
2016; Schakel et al., 2016; Parra et al., 2017; Uusitalo et al.,
2017 ). One study, however , focused identifying the CCU
technology most efficiently using surplus energy ( Sternberg
and Bardow, 2015 ). Once CO 2 -based products are deployed
in the markets, LCA can be used for environmental product
declaration ( Car bonCure ; Carbon Recycling International ; Audi,
2017 ).
From this short literature review, the most common rese arc h
questions are derived:
1. What is the environmental impact reduction of a C CU-based
product or ser vice compared to the s ame product or ser vice
derived from fossil carbon sources?
2. What are the contributions to the environmental impacts of
a CCU product/process over the life cycle and where are hot
spots to reduce environmental impacts?
3. What CCU technology to make efficient use of
renewable energy?
4. What are the environmental footprints of products or ser vices
used as basis for customer decisions (product de claration)?
All of these research questions imply a comparison between
alternatives (explicit or implicit) and thus, intend to support
decision making, e.g., which process to use, how to improve
the technology or which product to buy (refers to product
declaration). In most cases, C CU technologies aim to produce
products that are already offered in t he market. For this
reason, this guideline focusses on comparative assessments, or
assessments that are to be used in comparative assertions. Goal
definition should use the research questions listed a bove to derive
the specific research question of the study. In addition, the
requirements of the ISO 14044 shall be fulfilled as listed in the
beginning of this section.
For CCU technologies in stages of early de velopment (low
technology readiness level, TRL), studies can end up in apple
vs. oranges comparisons, since most reference technologies are
mature and have been optimized over decades. In contrast, low
TRL processes usually ha ve hig her energy demand or solvent
consumption because of not yet established heat integration
and/or process optimization. At the same time, low TRL
processes lack auxiliary proces ses such as product purification
steps after reaction. Thus, LCA studies on lab-scale processes
can both under- or over -estimate environmental impacts. These
aspects should always be considered in comparative studies if
a high TRL technology is compared to a low TRL technology.
In early development st ages, LCA is most useful to identify hot
spots for environmental improvement via contribution followed
by a sensitivity analysis. However , a comparison between a low
TRL CCU technology and a high TRL reference te chnology can
still reveal valuable insights to guide research. Furthermore, ex-
ante assessments may be applied to compare the current low TRL
technology at a future industrial scale-up TRL with the future
reference process or the technology development ( Pehnt, 2006;
Gavankar et al., 2015b; Kaetelhoen et al., 2015, 2016; Ar vidsson
et al., 2017; V illares et al., 2017; Cucurachi et al., 2018 ). However ,
the prediction of future developments introduces another source
of uncertainty.
SCOPE DEFINITION
The scope definition shall describe under which conditions
and assumptions the results of the study are valid. Therefore,
every aspect of t he scope definition is closely related to and
has to be in line with the study’ s goal ( European Committee
for Standardisation, 200 9, 2018; European Commission - Joint
Research Center, 2010 ).
Defining Functional Units for CCU
T echnologies
Life cycle assessment quantifies the environmental impacts of
a product or process system on a relative basis with respect
to its function, e.g., global warming impact per kg of product
( European Committee for Standardisat ion, 2009 ). This relative
basis is called functional unit, which quantifies the per formance
of a product system or ser vice. As most LCA studies on
CCU aim at comparing CCU technologies to a benchmark or
results are used for comparisons, the functional unit should
ensure the sound comparison of the assessed technologies.
However , different LCA studies on identical technologies may
apply different functional units, which complicates comparisons
between studies or even makes them incomparable ( Artz et al.,
2018 ). To increase comparability among studies, we derive
functional units for each class of CCU technologies from current
LCA practice and derived a decision tree to define a suitable
functional unit.
For products with identical chemical structure and
composition to their conventional counterparts, in general,
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Müller et al. Guideline for LCA of CCU
mass shall be used as a basis for comparison since this is
the most common trading unit for chemicals, materials and
minerals ( Figure 3 ). Other bases for comparison, e.g., amount
of species, volume or exergy, could also be applied. However , as
enhanced comparability is a ma jor objective of this guideline, we
recommend using mass for comparisons, since mass is the most
common measure of trading.
In case of fuels with identical chemical structure and
composition, energy content (based on the lower heating value,
LHV) shall be used, since the value of fuels is measured by their
energy content. The lower heating value is recommended since in
most energy ser vices the condensation ent halpy of formed water
is not accessible due to exhaust temperatures above 100 ◦ C, e.g.,
power plants, internal combustion engines and most boilers.
For CO 2 -based products with different chemical structure
and composition to their conventional counterparts, a generic
functional unit cannot be defined. Instead, the functional unit
shall be defined so that the technical performance in t he defined
application of the products becomes comparable, e.g., compare
detergents based on the washing performance and not based
on mass.
The functional unit of CO 2 -based fuels with different chemical
structure and composition shall be defined with respect to
the purpose of the fuel, i.e., energy ser vices provided. Energy
FIGURE 3 | Illustration of a comparison of environmental impacts for pr oducts
with identical chemical structure and composition over the entir e life cycle.
Impacts shown as bars on the x-axis only differ during the phases raw material
acquisition and production and thus, comparative studies only have to
consider these phases.
ser vices are for example the supply of ele ctricity or heat or
the transportation of persons or goods. The functional unit
has to quantify either the precise energy ser vi ce (e.g., 1 MJ of
electricity from a gas turbine of a certain type) or the distance
for freight or person transport (e.g., one person km driven in a
specified vehicle/ship/aircra ft), since combustion properties may
be different and thus, comparability based on energy content is
not guaranteed ( Deutz et al., 2018 ).
Energy storage delays the use of energy to a later time than
when it is was generated and thus, decouples supply and demand
of energy ( The European P arliament the council of the European
Union, 2019 ). Through decoupling demand and supply, energy
storage offer additional degrees of freedom to operate the energy
generation in a more efficient way and thus, can lea d to lower
environmental impacts. However , potential impact reductions
strongly depend on the dynamics of demand and supply throug h
the energy system in which the energy storage operates and
the energy storage characteristics, e.g., char ging and discharging
rated output, the power ramping capability, and the storage
duration between charging and dischar ging. Due to the dynamic
nature of energy system with or without energy storages, the
functional unit may not be defined as an amount of energy.
Instead, the functional unit should be defined as the satisfaction
of energy demand over a period of time, e.g., as a time-series of
the power demand with a temporal re solution of 1 h covering
1 year.
To compare energy storage with different storage
characteristics, the energy system without any storage system
shall be compared to systems with the energy storage alternatives.
In a second step, the difference of environment al impacts
reductions of the energy storage alternatives can be compared.
To find a suitable functional unit, we developed the de cision
tree shown in Figure 4 leading to functional unit by answering
a maximum of three questions: (1) Is the subject of th e study
a CCU product or an energy storage? (2) If the subject of
the study is CCU product, is it fuels or not? (3) Is the
subject of the study chemically identical to the conventional
product or not?
Defining System Boundaries for CCU
T echnologies
The system boundary defines which processes and life cycle stages
are needed to fulfill the function as defined by the functional
unit and thus, are part of the analy zed product system. In
general, the system boundary should cover the entire life cycle
from cradle-to-gra ve ( European Committee for Stand ardisation,
2009 ). However , in si tuations where technical performance
and, thus, downstream emissions are identical, a cradle-to-gate
approach, in particular for comparative studies, is sufficient
where the system boundaries only cover the product system
from raw materials acquisition to the factory gate ( Figure 3 ;
Guinée, 2006 ). In fact, in some situations, it is practically
infeasible to cover the entire life cycle, e.g., if a product has
numerous but unknown potential applications. In the following,
we derive a decision tree ( Figure 5 ) with a set of system
boundaries for CCU technologies, which are in line with the
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Müller et al. Guideline for LCA of CCU
FIGURE 4 | Decision tree for the selection of a suitable functional unit.
FIGURE 5 | Decision tree for the selection of system boundaries.
functional units derived in section Defining Functional Units for
CCU Technologies.
For products and fuels with identical chemical structure and
composition to their conventional counterparts, a cradle-to-gate
approach is sufficient since the products cannot be differentiated
and thus, downstream life cycle phases are identical and so are
their environmental impacts ( Figure 3 ).
System boundaries for products with different chemical
structure and composition to their conventional counterparts,
such as CO 2 -based materials (e.g., consumer products) shall
cover the entire life cycle from cradle-to-grave. A cradle-to-
gate approach is only applicable if differences in technical
performance and end-of-life treatment not differ significantly. In
all other cases, materials perform differently and environment al
impacts from downstream processes will not be identical.
Therefore, LCA studies sh all cover the entire life cycle to
a void problem shifting from one life cycle phase to the
other ( Figure 5 ).
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Müller et al. Guideline for LCA of CCU
FIGURE 6 | Schematic life cycle of CCU technologies span from the CO 2 source, supply other feedstocks and energy to the end of life tr eatment. In all life cycle
stages, environmental impacts should be consider ed. Adopted from von der Assen et al. (2013) .
For fuels with different chemical structure and composition t o
their conventional counterparts, a cradle-to-grave approach
shall cover the raw material acquisition, production,
and transport as well as use and end-of-life, which
often occur simultaneously during combustion. Omitting
combustion can lead to qualitati vely incorrect results,
if fuels change engine efficiencies and tailpipe emissions
( Deutz et al., 2018 ).
However , if t he study aims to compare fuels with identical
chemical structure and composition to their conventional
counterparts, both fuels will behave identically in all potential
applications and thus, a cradle-to-gate approach is justified. In
other cases, omitting the combustion might still be ne cessary
if the potential application is unknown, e.g., in early stages
of development.
For the comparison of energy storage, the system
boundaries shall cover the entire energy system from
gate-to-gate, i.e., all environmental impacts arising from
the operation of the energy system, and the entire life
cycle of the energy storage, i.e., construction, operation,
and decommissioning.
Upstr eam Environme ntal Impact From CO 2
Captur e
CO 2 emitted to the environment is an elementary fl ow. Thus,
captured CO 2 is often treated intuitively as a consumed
emission  GW CO 2 = − 1 kg CO 2 e
kg CO 2  . However , c aptured CO 2 is
a product of human transformation. Consequently, CO 2 is a
technical flow, and a chemical feedstock for CO 2 utilization.
Thus, treating CO 2 as negative emission is usually incorrect
and captured CO 2 has to be treated like any other feedstock
( Heijungs and Frischknecht, 1998 ). CO 2 sources shall be
included in system boundaries as environmental impacts
occur due to the CO 2 supply. Assessments s hall comprise
all process steps leading to environmental impacts including
CO 2 source , CO 2 -purification and transport as shown in
Figure 6 .
Life Cycle Inventory Modeling Framework
and Solving Multi-Functionality
The life cycle inventory modeling framework defines how
data is gathered and processed during the life cycle inventory
stage of LCA ( European Commission - Joint Researc h Center,
2010 ). The framework defines how interactions with other
product systems are handled, in particular , how to solve multi-
functionality problems.
Data Inventory for CCU Pr ocesses
The system boundaries for LCA studies on CCU technologies
start with the acquisition of raw materials and eit her end at the
factory gate or at the end of the products life cycle.
During an LCA study, some process data will not be a vailable
from direct measurements. A company can usually only me asure
data within its factory gates. Oth er companies or LCA databases
can supply missing upstream and downstream data in t he life
cycle inventories. If the specific supplier of up-/downstre am
ser vices is known or the production process of an input can
be identified, inventory data specific to the process should be
used. In other cases, this information might not be availa ble,
because products are purchased from a market, e.g., electricity
traded at the stock market. In these cases, a spe cific technology is
not availa ble, and a market mix shall be used instead ( European
Commission - Joint Researc h Center, 2010 ).
The use of market mixes can be assumed until the additional
demand or supply of the CCU te chnology triggers large-scale,
structural changes 2 . An example for a large-scale, structural
change could be the installation of additional electrical power
2 Following the ILCD handbook ( European Commission - Joint Researc h Center,
2010 ) this shall be assumed as long as the additional supply or demand of the
production system under study does not exceed a threshold value of 5% of the
annual market size of a supplied or demanded product. The threshold value
of 5% refers to an estimated share of pro duction capacity which is annually
decommissioned, i.e., production plants in the end of their life time ( European
Commission - Joint Research Center, 2010 ). If the additional supply or demand
of the production under study exceeds 5% production capacity, plants are
decommissioned that would otherwise still produce and thus, large scale, structural
changes apply. This might be the case if CCU technologies are deployed on a global
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Müller et al. Guideline for LCA of CCU
capacities in response to an excessive electricity demand by
a CCU technology, which could also affect production and
consumption patterns in wide parts of the e conomy through
changes in electricity prices. Such large-scale effects may
occur for a large-scale market introduction of CCU products.
Nevertheless, accessing large-scale effects is typically beyond t he
scope of conventional LCA studies. The development of methods
for this purpose by integration of complex market models is topic
of current research ( Y ang and Heijungs, 2018 ). In this guideline,
we focus on the scope of conventional LCA studies.
Therefore, first, proces s-specific inventory dat a shall be used,
if this information is availa ble. Only otherwise, averaged market
mixes shall be used for the regarding input.
Solving Multi-Functionality
Most CCU systems are multi-functional, because CO 2 sources
often provide a main product and CO 2 ( Figure 8 ; von der A ssen
et al., 2014 ). For example, ammonia is produced by reacting
hydrogen with nitrogen. Hydrogen can be co-produced with
CO 2 in the steam-methane-reforming process. As poison to the
catalyst for ammonia production, CO 2 has to be separated prior
the formation of ammonia and subsequently, a pure CO 2 stream
is released. If CO 2 is now captured from ammonia synth esis, the
main-product ammonia and the co-product CO 2 are produced
simultaneously. If the environment al impacts for the produced
CO 2 stream are required, the total emissions of the s ystem need
to be split between the main and the co-product.
This problem is called multi-functionality. Other co-products
or functions may occur throughout t he life cycle of CCU
products. In general, the problem of multi-functionality is
no CCU-specific problem. The problem can be addressed
using established LCA methodologies. However , a number
of methodological choices have to be made. Therefore , we
first demonstrate how the methods can be applied to a CO 2
source since the multi-functionality problem at the CO 2 source
is at the core of most CCU processes. Subsequently, we
present a hierarchy of methods to solve multi-functionality
which is valid according to ISO 14044 and other guidelines
and standards ( World Resources Institute and World Busines s
Council for Sustainable Development ; European Commission -
Joint Research Center, 2010; BSI, 2011; AFNOR, 2016; European
Committee for Standardisation, 2018 ).
In the following, the alternative methods to solve multi-
functionality are described and applied to account for t he supply
of CO 2 . Sub-division solves the problem of multi-functionality by
separating an aggregated (black box) unit process with multiple
functions into smaller unit processes and gathering input and
output data of these smaller unit processes, e.g., a factory with
multiple products that are produced in independent processes
can be sub-divided into individual production lines ( European
Committee for Standardisation, 2009 ).
Cases where sub-division is applicable are not a problem of
multi-functionality in a strict sense, but a problem of missing
data. If this missing dat a can be gathered, multi-functionality can
scale and thus, C CU technologies trigger large-scale changes. The ILCD handbook
refers to this as the distinction between goal situation A and B.
be fully resolved and thus, sub-division shall always be applied
first. Sub-division shall even be applied if multi-functional
unit processes remain, as this leads to smaller and simpler
product systems.
Application to CO 2 -source: Sub-division is not applicable
to CO 2 -source since CO 2 is always produced jointly with the
main product.
System expansion expands the functional unit to include
other functions of the product systems t han originally stated
in goal and scope definition. If this expanded function is
still meaningful, the multi-functionality problem i s resolved
( European Committee for Standardisa tion, 2009 ).
CCU processes are often multi-functional, e.g., when the
CO 2 source co-produces another product such as electricity.
As discussed a bove, CCU processes are often compared to
conventional processes. To compare both product systems, each
product system needs to fulfill the same functional unit and
therefore, the system boundaries and the functional unit are
changed for the product systems. For the comparison of the C CU
process with two products (product of CO 2 source and product
of CO 2 -process) to a conventional system ( Figure 7A ), the main
product of the CO 2 source is added to the functional unit and the
conventional system is expanded with the CO 2 source without
capture ( Figure 7 ).
Note that a process used for system expansion (not in case
of CO 2 -sources) can be multi-functional as well and subsequent
system expansion may be needed. In theory, one could end up
modeling the entire global te chnosphere. However , this e ndless
chain of system expansion is usually interrupted by the definition
of cut-off criteria for small contributions to the LCA results.
Substitution does not include additional functions in the
functional unit. Instead, a credit is given for the production of
the co-product. The credit represents the environmental burdens
a voided by the substitution of the conventional production
system which would ha ve been used otherwise. The functional
unit remains as stated in the goal and s cope definition, but
the system boundary is altered for the product system where
substitution is applied. In comparative assessments, the system
boundary and functional unit of the conventional product
system(s) remains unchanged ( European Commission - Joint
Research Center, 2010 ).
Similar to the approach presented in section Dat a Inventory
for CCU Processes, first, a specific process to be substituted shall
be identified and used. In all other cases, a market-averaged
process mix shall be assumed ( European Commission - Joint
Research Center, 2010 ).
For CO 2 sources, the substituted proces s is usually the s ame
source but without capture ( Figure 7B ). This as sumption is
meaningful as long as not all CO 2 from t his source is already
fully utilized.
Both approaches, system expansion and system expansion
via substitution, are mathematically equivalent in comparative
LCA; however , results, meaning and interpret ation of results
are not, because system boundaries and functional unit are
altered. System expansion via substitution can lead to negative
environmental impacts (e.g., negative CO 2 emissions), because
by-products are credited. These negative environmental impacts
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Müller et al. Guideline for LCA of CCU
FIGURE 7 | (A) Comparison of a CCU production and a r eference pr oduction: CCU system produces a main pr oduct besides CO 2 -based product, i.e., the CCU
system has additional function (dashed red line) besides functional unit (dashed green line). Thus, the conventional and CCU system ar e not comparable due to
differ ent functions. System expansion enables the comparison of the CCU production and the refer ence production by including the main product of CO 2 -sour ce in
functional unit. For a sound comparison the refer ence production system is expanded with the conventional product ion of the main product without carbon captur e.
(B) Substitution: The production of the main pr oduct without carbon capture is avoided and thus, the CCU system is cr edited f or the otherwise emitted CO 2 , but has
to carry the burdens of purification, compr ession and transport. (C) Allocation sub-divides the CO 2 -sources into two pr ocesses and distributes the environmental
burdens of the CO 2 sour ce between the main product and the feedstock CO 2 pr oduction using underlying physical relationship or other r elationship. The CCU
production system becomes a mono-functional pr oduction system and can be compared to the refer ence production since functional units are identical .
can be misunderstood in a way that producing more of
the product could offer infinite benefits to the environment.
However , t hese negative environmental impacts are limited to
the market capacity of the by-products and thus, do not offer
infinite benefits. Furthermore, these negative environmental
impacts do not indicate that greenhouse gas emissions are
taken up by the production system from the atmosphere nor
that natural resources are generated ( T anzer and Ramíre z,
2019 ). The negative environmental impacts simply indicate
that the production system has lower environmental impacts
than the conventional production of all products and by-
product trough the conventional production. Howe ver , as
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Müller et al. Guideline for LCA of CCU
a conceptual advantage, substitution conserves t he causal
interaction between processes by accounting for impacts in other
life cycles.
Allocation partitions the in- and outputs of the multi-
functional process among the products or functions reflecting
an underlying physical causal, e conomic, or other non-caus al
physical relationship ( Figure 7C ).
A c cording to ISO 14044, an underlying physical caus al
relationship shall be applied first, by quantifying how input and
outputs physically relate to a function of system. For example,
the chlorination of benzene delivers mono-chlorobenzene , ortho-
, and para-dichlorobenzene and hydrochloric acid. The amount
of chlorine consumed by the process is directly physically related
to the amount of the chlorine incorporated in the products.
Therefore, the amount of chlorine in each product is the physical
criterion to distribute the chlorine flow between the products
of benzene chlorination. Another way to establish a physical
causality is to quantit atively change the functions and obser ve
how the inputs and outputs are affected. The distribution of the
inputs and outputs should than reflect this quantit ative change of
inputs and outputs 3 . Note that more than one relationship can be
applicable within one process.
In case of CO 2 sources, a physical causality can be found
by quantitatively changing the amount of main product and
the product CO 2 produced and obser ving h ow the inputs and
outputs are affected. Setting the amount of main product to zero,
leads to a process without inputs, outputs, and product CO 2 .
Therefore, the amount of main product affects the inputs and
outputs of the process. V arying the amount of product CO 2
changes the amount of CO 2 emitted, since CO 2 is no longer
emitted and the inputs and outputs related to the c apture process.
In consequence, 1 kg of CO 2 provided by the CO 2 -source leads to
an emission reduction of 1 kgCO 2 e and an increase of emissions
related to the capture process. The result is identical to the
substitution approach.
If a physical causal relationship cannot be applied, other
underlying relationships shall be used. For this purpose, the
multi-functional process is sub-divided into mono-functional
processes and the environmental burdens of the multi-functional
process are distributed among the mono-functional processes
according to attributes of the product or functions. The most
commonly applied attribute is economic value of products
or functions. Since the multi-functional process is artificially
sub-divided, the physical causality between processes is lost,
i.e., the independent production of former jointly produced
products. In addition, the selection of t he attribute is to some
extent arbitrary.
The selection of a suitable product attribute to distribute the
emissions of the CO 2 -source among the main product and the
CO 2 -source can be difficult. M ass can be applied to all processes
except power plants, since electricity has no mass and thus,
all emissions would be distributed to CO 2 . Energy is not a
suitable attribute since CO 2 does not contain any energy, or more
precisely: its lower heating value is zero. The economic value of
CO 2 is uncertain, since the ca pture process is related to costs,
3 The ILCD handbook refers to this as “virtual sub-division.”
the price of CO 2 might be positive and t hus, economic allocation
would attribute CO 2 would with positive emissions. However , it
can be argued that CO 2 has a negative economic value since it
is a waste stream, which needs a waste treatment. In this case,
the CO 2 source has only one function, i.e., producing the main
product and has a technical waste flow, i.e., the concentrated CO 2
stream. The CO 2 -utilizing step would then be multi-functional
in the sense that a CCU product is produced and the CO 2
waste stream is treated. As waste stream per se cannot carry
any environmental burdens, the environment al impacts of the
CCU utilizing step would be allocated between the C CU product
and the waste treatment ( European Commission - Joint Research
Center, 2010 ).
As each applied criterion would significantly alter the
environmental impact attributed to CO 2 and an objective
selection of one allocation criterion is not possible, a sensitivity
analysis is always needed.
Hierar chy of Methods for Solving Cases of
Multi-Functionality
Existing standards ( BSI, 2011; AFNOR, 2016; European
Committee for Standardisation, 2017, 2018 ) and guidelines
( European Commission - Joint Research Center, 2010, 2012;
World Resources Institute and World Business Council for
Sustainable Development, 2011 ) rank methods for solving
multi-functionality in a hierarchy whic h should be consistent
with stated goal definition. In the following, we present the
hierarc hy of methods for solving multifunctionality complying
with the hierarchy of ISO standards and guidelines.
First, check if multi-functionality can be solved by gathering
individual process data and apply sub-division.
If subdivision cannot solve the multi-functionality problem,
apply system expansion. Note that results obtained via system
expansion are joint impacts due to the production of more than
one product and thus, are not specific to a single product of
the CCU te chnology. This might be in conflict with the initial
research que stion and a modification of t he question might
be needed.
If product-specific assessments are needed to answer the initial
research que stion the following hierarchy of allocation method
shall be applied. Please note that results obtained via system
expansion shall always be computed to asses s the overall effect
of introducing the CCU te chnology.
For product-specific assessments, first, substitution shall be
applied. If substitution is not possible, e.g., because there is no
process a vailable to be substituted, apply allocation: First, using
an underlying physical relationship and then an underlying ot her
relationship, e.g., economic value.
Special Requir ements for Comparative
Studies
Any study intended for external communication shall be
reviewed. For comparative studies or studies to be used in
comparative assertions disclosed to public, a critical re view shall
be conducted by an independent and qualified review panel.
More information about the review process can be found in
the ILCD handbook, the ISO standard and the PEF guideline
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Müller et al. Guideline for LCA of CCU
( European Committee for Standardis ation, 2009, 2018; European
Commission - Joint Researc h Center, 2010, 2012; International
Organization for Standardization, 2014 ).
Note that external review also allows to le ave out confidential
information in the public report and thus, can protect
intellectual property.
LIFE CYCLE INVENTOR Y (LCI)
In the life cycle inventory phase, the actual data is gathered,
and the product system is modeled according to goal and
scope definition.
Estimation Methods to Bridge Data Gaps
During LCA studies, practitioners are often confronted with
limited data availability. To bridge data gaps, estimation methods
ha ve been developed. In the following, commonly applied
estimation methods are presented, and further readings are
provided. These methods may be used to bridge data gaps, but
the generated data should be replaced by measured values as soon
as possible.
Second-Law Analysis
W ith thermodynamic analysis, a second-law analysis ca n be
conducted based on stoichiometric reaction schemes, mass-,
energy-, exer gy-, and entropy balances. By assuming second-law
efficiency of 100%, an absolute best-case scenario is obtained. If
this best-case scenario does not offer environmental benefits, t he
considered process will never offer any environmental benefits.
In particular for low TRL technologies, the second-law analysis is
an useful tool to sort out technologies. Therefore, the second-law
analysis shall be used to establish a best-case scenario.
Gate-to-Gate Inventory Estimation
In cases, where specific information of chemical processes is
missing, e.g., for feedstocks, Ecoinvent uses a yield of 95%
based on a stoichiometric mass balance and a product avera ged
energy demand and other auxiliaries can be assumed as a rough
estimation ( Weidema et al., 2013; ecoinvent, 2017; Gendorf
Chemiepark, 2017 ).
Jiménez-Gonzáles et al. and Kim et al. provide a design-based
method to estimate gate-to-gate inventory information when
direct data is not available ( Jiménez-González et al., 2000; Kim
and Overcash, 2003 ). The provided method defines transparent
rules for data collection and provides rules of thumbs, e.g., for
the estimation of mass balance, energy requirements, and energy
recovery rates. Based on t his method, Kim et al. show for 86
chemicals that the gate-to-gate process energy ranges for h alf of
the organic chemicals from 0 to 4 MJ per kg and for half of the
inorganic chemicals from − 1 to 3 MJ per kg.
A method to estimate gate-to-gate process energy
consumption when no process engineering is availa ble, is
provided by Bumann et al. (2010) which correlates the process
energy demand with the energy index provided by Sugiyama
et al. (2008) . The proposed method is based on a simplified
process model consisting of a reactor and separation unit
and information of the chemical reaction, e.g., react ants,
products, co-products, and by-products, reaction conditions
and thermodynamic data. From this data, an energy index
is computed and used for the estimation of gate-to-gate
energy consumption. The a verage deviation of this met hod is
around 30%.
Artificial Neural Networks
Environmental impacts of processes ha ve been estimated from
molecular descriptors of the desired product using neural
networks ( Wernet et al., 2008, 2009 ). The resulting software
tool Finechem can be helpful if no process information is
a vailable. The neural network was trained with industrial data
and thus, the method mig ht be limited to predict molecules
comparable to those in the training set. In addition, the molecular
descriptors limit the range of application, as isomeric compounds
and polymers cannot be differentiated. Furthermore, as this
method uses solely the molecular des criptors of the product as an
input, alternative production pathways cannot be asses sed by this
method. This is in particular a shortcoming for CCU technologies
which aim to substitute identical products, fuels, or materials.
Selection of Refer ence Pr ocesses
The selection of a reference process has significant impact
on the reduction potential of the assessed CCU technology.
Therefore, the reference process has to be carefully selected. In
general, reference processes shall be those processes that the CCU
production system competes with in the market, i.e., t he marginal
process. However , the identific ation of the marginal process
may introduce complex market interactions, in particular if the
process has more than one function. Therefore, the reference
process shall be modeled as the a verage market mix if further
information is missing and if no large-scale, structural changes
occur (section Dat a Inventory for CCU Processes).
However , C CU technologies—in particular in stages of
early development—do not compete wit h current technologies,
since their market launch lies in the future. Instead, these
CCU processes compete with the te chnologies established in
the future. Thus, comparing CCU te chnologies in stages of
early development to currently used processes does not reflect
reality. Therefore, the time dimension is crucial for assessing
ecological benefits of C CU. For this purpose, future development
techniques, e.g., learning cur ves, may be appli ed to both the CCU
technology and the reference process, as both processes underlie
development ( Cucurachi et al., 2018 ). Methods to apply learning
cur ves are described by Gavankar et al. (2015b) and Cespi
et al. (2015) . Note that forecasting te chniques shall not exceed
physical limitations, e.g., th e second law of thermodynamics. In
addition, changes in the background system shall be accounted
for , e.g., the changes in the energy supply due to higher shares
from renewables.
However , predicting future te chnologies is potentially beyond
the scope and experience of many LCA practitioner and thus,
if no reliable predictions on future developments are availa ble,
the current best availa ble technology should be used as the
reference technology.
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Müller et al. Guideline for LCA of CCU
LIFE CYCLE IMP ACT ASSESSMENT
Key driver for CCU is to lower GHG emissions and our
dependence on fossil resour ces. Not surprisingly, global warming
and fossil resour ce depletion (or fossil-based cumulative energy
demand) are usually selected as impact categories in LCA
studies on CCU ( Artz et al., 2018 ). The introduction of C CU
technologies may further affect a variety of environmental
impacts and the holistic LCA approach aims to a void
problem shifting from one impact category to another.
Therefore, impact categories shall not be omitted from
LCA studies to a void misleading decision-making if impact
categories are:
- Relevant, i.e., accounted elementary fl ows contribute in these
categories and
- As sessable, i.e., impact asses sment methods exist and these
methods are reliable.
However , t he selection of impact categories and methods is
not straightforward: Numerous impact categories exist and
sometimes even multiple methods for one impact cate gory exist.
Furthermore, the uncertainty of impact assessment models varies
as more or less complex cause-effect chains are involved and
methods are more or less advanced. In consequence, different
impact assessment models are used in practice leading to
differences in LCA results.
Impact assessment s hould use the CML (Institute of
Environmental S ciences, University of Leiden) impact
assessment methodology in its most recent version as the
“International Environmental Product Declaration (EPD)
System” uses CML as a default for product category rules.
To the best of the authors ’ knowledge ( July 2018), the most
recent version of CML is 2016. Additionally, a second set
of methodology should be applied if this methodology
is geographically more appropriate than CML 4 , 5 . In this
way, comparability and geographical representativeness are
guaranteed at the same time.
For Europe, the Joint Research Center provide s a selection
of impact categories and methods which were defined in a
stakeholder’ s dialogue involving LCIA model developers and
LCA practitioners and thus, the JRC recommendation should
be followed for Europe ( European Commission - Joint Research
Center, 2011a ). For the United States, the EP A developed TRACI
2.1 as impact assessment methodology and thus, TRA CI in its
most recent version should be used for studies in the U.S.
( Bare, 2002 ).
Note that life cycle impact assessment s hould be limited to
midpoint indicators, because the le vel of uncertainty increases
with endpoint indicators or single point indicators. Also note that
a detailed knowledge of impact assessment method is necessary
4 CML-IA Characterisation Fa ctors. A vailable online at: https://
www.universiteitleiden.nl/en/researc h/research- output/science/cml- ia-
characterisation- factors#features (accessed May 17, 2018).
5 The International R
 System - Environmental Product Declarations. A vailable
online at: https://www.environdec.com/ (accessed May 17, 2018).
to interpret and report results properly, e.g., human toxicity
assessments ha ve high uncertainty and thus, results differing by
2–3 orders of magnitude might still be interpreted correctly as
“identically toxic” ( H auschild and Huijbregts, 2015 ).
T emporary Storage of CO 2
CCU products offer temporary carbon storage. Due to temporary
carbon storage, CO 2 emissions can be delayed and thus, do
not contribute to climate change during the time of storage.
Therefore, temporary storage is no independent or additional
benefit from the impact on climate change.
The relevance of temporary storage depends on the class of
CO 2 -based product or fuel considered:
For CO 2 -based products and fuels with identical chemical
structure and composition to their conventional counterparts,
carbon storage does not offer any additional benefits since
the product life is identical after leaving the factory gate for
both products and the amount of c arbon chemically bonded is
identical ( Kätelhön et al., 2019 ). Therefore, the time between
production and end-of-life treatment and the amount of CO 2
released during end-of-life treatment is identical. Thus, t he
emission time profile is identical after factory gate (blue and
green line in Figure 8 ) and there is no additional effect
storing CO 2 .
For CO 2 -based products different in chemical structure
and composition to their conventional counterparts, emission
time profiles are not identical (red line in Figure 8 ) and thus,
temporary storage may offer climate benefits ( Figure 9 ).
However , note t hat temporary storage offers a benefit
only once. Once all counterparts have been substituted , the
composition remains constant and thus, emission time profiles
are identical again.
For CO 2 -based fuels different in chemical structure and
composition to their conventional counterparts, temporary
storage is usually not significant, since the storage duration is
short compared to climate change dynamics.
To decide whether or not temporary storage may offer
any climate benefit, we developed t he decision tree shown
in Figure 9 by answering a maximum of three questions: (1)
Is the subject of the study a CCU product or an energy
storage? (2) If the subject of the study is CCU product, is it
chemically identical to the conventional product or not? (3) If
the chemical structure differs, is the subject of the study a fuel
or not?
The effect of temporary CO 2 storage is known from bio-based
products and methods to account for temporary storage exist
( Levasseur et al., 2010, 2012; Brandao et al., 2013 ). H owever ,
classic LCA does not account for temporary storage or emission
timings, “as LCA per se is not discounting emissions over time ”
(ILCD handbook, p. 226), since LCA models are usually static
and do not account for dynamic effects such as discounting
emissions over time ( Brander, 2016 ).
To follow the established LCA principles, delayed emission
shall not be discounted over time. Instead, emission time profiles,
the amount and duration of carbon stored may be reported as a
separate item.
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Müller et al. Guideline for LCA of CCU
FIGURE 8 | Emissions time profiles for differ ent products. CO 2 -based products with identical chemical structur e and composition to their conventional counterparts
have identical emissions timing profiles after pr oduction. CO 2 -based products dif ferent in chemical structur e and composition can have differ ent emissions during
use-phase and end-of-life treatment and dif ferent life spans and thus, the emissions timing profile can be dif ferent.
FIGURE 9 | Decision tree for determining if temporary storage is significant for LCA study .
Note that for permanent storage 6 , a discounting method is not
needed because end-of-life emission never oc cur and thus, are
zero. If end-of-life emissions are zero, the effect of storage is thus
already considered.
LIFE CYCLE INTERPRET A TION
During life cycle interpretation, the feedback loop of t he
iterative steps of LCA studies is closed, e.g., through evaluating
the gathered life cycle inventory in t he light of the goal
6 Permanent storage can be assumed if CO 2 is sequestered for 100,000 years.
definition. Furthermore, the results are evaluated to derive robust
conclusions and potential recommendations at the end of a
LCA study.
Uncertainty and Sensitivity Analysis
In the following, methods to quantify the impact of uncert ainties
are described and two levels of re commendation are provided.
This section is based on Igos et a l. (2018) . First, a basic level
is described using sensitivity analysis and s cenario analysis and
second, an intermediate level using uncert ainty analysis. The
basic level shall be applied and the intermediate le vel should be
applied if possible.
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Müller et al. Guideline for LCA of CCU
Please note that uncertainty assessment in general is already
covered sufficiently by standards and guidelines. However , the
following section describes how methods can be applied to
CCU technologies.
Basic Level
In the basic approach, input variables shall be identified that
ha ve uncertainties with hig h impacts on the uncertainty of the
model output. For this purpose, a sensitivity analysis shall be
carried out. Sensitivity analysis is a systemati c procedure to
estimate the effects that alternative choices for methods and
data have on the outcome of a study ( European Committee for
Standardisation, 2018 ). The most b asic approach to carry out a
sensitivity analysis is the one-at-a-time approach. For the one-at-
a-time approach, input variables s hall be varied separately one
after the other to quantify the sensitivity of the model results
toward the considered input variable. For this purpose, the input
variables sh all be varied within re alistic ranges. The results of the
sensitivity analysis may be sorted to identify key variables with
the highest influence on the overall output uncert ainty. If the
variation of the input variables reveals weak points of the study
that are not in line with the L CA study’ s goal and s cope, the goal
and scope definition shall either be refined or dat a quality and
modeling approach shall be reviewed until significance of results
according to goal definition is achieved.
Once the key variables are identified, either a scenario analysis,
i.e., the evaluation of a lternative choices, or the calculation of
threshold values for key variables shall be carried out.
For a scenario analysis, a number of s cenarios exploring key
variables sh all be defined. These scenarios shall be analyzed in
relation to the model results of the baseline scenario. Typi cally,
best- and worst-case scenarios should be defined to quantify the
range of the model results.
CCU technologies often make use of energy or high energetic
reactants, e.g., hydrogen to activate CO 2 . The production of
those high energetic reactants or t he supply of energy can lead
to high environmental impacts. In consequence, assumptions
on environmental impacts of these inputs have been identified
as the major sour ce of varying results in LCA studies on CCU
technologies. Thus, the environmental impacts related to t he high
energetic reactants are often the key variables in studies on CCU
technologies ( Artz et al., 2018 ). Furthermore, CCU technologies
are emerging technologies and thus, the derived scenarios shall
consider the transition of the background system. For t his
purpose, practitioners sh all define a scenario representing t he
status-quo, a fully decarbonized future and a transition s cenario.
An example for electricity generation is presented in T able 1 .
The status-quo is taken from t he Energy Technology Perspectives
report published by the International Energy A gency (2017) .
In fully decarbonized industry, th e greenhouse gas emissions
of the energy supply will be fairly close to zero, while in a
transition scenario the emissions will lie somewhere in between
the status-quo and a fully de carbonized industry (e.g., 50% of
the current emissions). These scenarios are derived in a very
simply way and the scenarios will perform ba dly at forecasting.
However , valuable insights from a s cenario analysis like this
can be gained, e.g., the dependence on clean energy supply
T ABLE 1 | Exemplary scenarios.
Input Unit Status-quo T ransition Full decarbonized
Electricity kg CO 2 -eq /MJ 0.091 a 0.046 0
a Calculated from International Energy Agency (2017) .
can be shown. Since the generation of scenarios can be ti me-
and resource-demanding, we derived scenarios for the supply of
electricity, hydrogen, CO 2 , heat and natural gas (as met hane) for
the European context is provided in the annex of t his document
(see Supplementary Material ). These scenarios should be used
per default in the European context to allow harmonization of
LCA studies.
However , note t hat scenario analysis can suffer from
ambiguity because the definition of s cenarios relies on the LCA
practitioner and can hardly become an automated part of LCA
calculations ( Jung et al., 2014 ).
As an alternative to scenario analysis, threshold values
for key variables can be calculated. A threshold value is
the smallest (or highest) value of an input variable that is
sufficient to achieve environmental benefits compared to t he
benchmark process. For example, water electrolysis consumes
50 kWh electricity per kilogram hydrogen. To emit les s
greenhouse gas emissions than steam reforming of methane
(10.7 kg CO 2 -eq per kilogram hydrogen, GaBi Software-
System v8.5.0.,79 and Dat abase for Life Cycle Engineering
SP 35, 1992–2018 ), the greenhouse gas emissions of electricity
supply for the water electrolysis would need to be 0.214
kgCO 2 -eq per kWh electricity or lower. In this case, the
threshold value of electricity supply for hydrogen from
water electrolysis compared to the benchmark process steam
methane reforming of methane would be 0.214 kg CO 2 -
eq per kWh electricity. For a sound interpret ation, the
calculated threshold values should lie within physical and
thermodynamic limits.
Intermediate Appr oach
Based on the b asic approach, the LCA practitioner should carry
out an intermediate approach to quantify the uncertainty of
the model output using uncertainty analysis. According to the
ISO 14044, uncertainty analysis is a “systematic procedure to
quantify the uncertainty introduced in t he results of a life
cycle inventory analysis due to the cumulative effec ts of model
imprecision, input uncertainty and d ata variability” ( European
Committee for Standardisation, 2018 ). Therefore, uncertainty
analysis is a measurement of the reliability of the model
output toward the underlying decision process. Uncertainty
analysis is usually carried out using stochastic methods, e.g.,
Monte Carlo simulation ( Sonnemann et al., 2003; S chenker
et al., 2009; W illiams et al., 2009; Sills et al., 20 13 ), or
perturbation theory, e.g., analytic al uncertainty propagation
( Huijbregts et al., 2001; Lloyd and Ries, 2007; Heijungs,
2010; Groen et al., 2014; Jung et al., 2014; Pfingsten et al.,
2017 ).
In the intermediate approach, the Monte Carlo simulation
is recommended since it is the most common method to ca rry
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Müller et al. Guideline for LCA of CCU
out an uncertainty analysis and it is i ntegrated in current LCA
software, e.g., SimaPro, OpenLCA, and GaBi. In a Monte Carlo
method, all input variables are varied randomly within their
defined ranges for a fixed number of model simulations. In
consequence, the range of the model results is a value for the
probability distribution and thus, a value for the overall model
uncertainty. The Monte C arlo method requires a high number
of simulations in order to obtain representative results and
therefore, high computational power or hig h calculation time.
U sually, 10,000 Monte C arlo sets are generated, but Wei et al.
(2016) showed that 1 million might be necessary to achieve
sufficient accuracy of results. In general, convergence cannot be
guaranteed ( Igos et al., 2018 ). Therefore, the number of Monte
Carlo sets should be as high as possible but at least 10,000 ( Igos
et al., 2018 ).
In comparative studies, Monte Carlo analysis shall not
be carried out independently for each alternative, since the
comparison of probability distribution can lead to wrong
interpretations, i.e., a large overlap of two probability
distributions might be misinterpreted as an indistinctive
decision. L arge overlaps can be a result of identical sensitivity of
both system toward one parameter ( Henriksson et al., 2015 ). For
example, if two hydrogen electrolysis with different efficiencies
A and B are compared. The environmental impacts of B and
A are both highly sensitive to the environment al impacts
of the electricity supply, but are impacted in t he same way.
However , if done independently, overlaps c an occur because
a Monte Carlo set of B with low impact electricity supply
is compared to a Monte Carlo set of A with a hig h impact
electricity supply ( Figure 10A ). Here, the interpretation that
both system perform equally good is wrong and can be avoided
by a joint Monte Carlo simulation of the difference of both
alternatives. A joint Monte Carlo a nalysis can show that the
environmental impacts of alternative B are always hig her than A
in each Monte Carlo set and thus, t hat A is clearly advantageous
( Figure 10B ).
Therefore, a comparison of different technologies shall be
carried out in a joint Monte Carlo simulation. Furt hermore,
a comparison between different technologies in a joint
Monte Carlo simulation step shall always be related to the
same background system to ensure consistent results. For
instance, the conventional synthesis of methanol requires
high amounts of carbon monoxide and hydrogen whereas
the CO 2 -based production pathways require hig h amounts of
carbon dioxide and hydrogen. To ensure a fair comparison
between both technologies and thus, a consistent result of the
uncertainty analysis, the b ackground production system of
hydrogen has to be the same for each individual Monte C arlo
simulation step. For this reason, using aggregated processes
in Monte Carlo analysis can be misleading and thus, should
be a voided.
Uncertainty and sensitivity analysis are important for
comparative studies to identify whether calculated differences
of environmental impacts are significant or not. Note t hat
significant difference may not be reve aled by sensitivity analysis.
This does not mean that no difference exists, but t hat the study
could not prove any. Furthermore, note that ignorance, as an
FIGURE 10 | (A) Results of an independent Monte Carlo analysis for
alternatives A and B. (B) Results of Monte Carlo analysis for the d iffer ence
of technologies.
additional source of uncertainty, can neither be assessed by
uncertainty nor by sensitivity analysis “but may be re vealed by
qualified peer review” ( European Commission - Joint Research
Center, 2010 ).
Communication of Uncertainty Assessment Results
The communication of uncertainty assessment results is
important to avoid misleading interpretations and to ensure the
credibility of the assessment ( Ga vankar et al., 2015a ). Therefore,
the communication of the results of the b asic approach shall
include parameters with high sensitivity and their effe cts to the
overall model results. The results of the scenario analysis and
calculated threshold values shall be reported separately to the
results of the sensitivity analysis. The intermediate uncerta inty
assessment approac h should furthermore include the results of
the uncertainty analysis. The results of the uncert ainty analysis
should be interpreted with regards to their effect on t he reliability
of the LCA results.
Carbon-Neutral Pr oducts and Negative
Emissions
CCU technologies consume CO 2 to produce value-added
products. Thus, intuitively CCU technologies may be thought
of as technologies with potentially zero emissions or net-
negative emissions.
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Müller et al. Guideline for LCA of CCU
FIGURE 11 | (a) Carbon neutral CO 2 -uptake: CO 2 is taken from the atmospher e and is re-emitted after the pr oduct life cycle. (b) Carbon-neutral CO 2 sequestration:
Fossil carbon is taken from undergr ound reservoirs and CO 2 is sequester ed after product life cycle. (a,b) ar e only carbon neutral if no emissions occur during the
product life cycle. (c) Negative emissions: CO 2 is taken fr om the atmosphere and sequester ed after the product life cycle. (c) will only have negative emissions if
emissions over the entire lifecycle ar e < 1 kg CO 2 -eq. per kg CO 2 up taken.
FIGURE 12 | Carbon reducing: CCU technologies can offer lower CO 2
emissions than the status quo and thus, may be considered as
carbon-reducing technologies.
CO 2 is usually considered to be captured from fossil or
biogenic point sources or directly from the atmosphere via
direct air capture. Fossil point sources release carbon previously
stored in underground departments, while biogenic point sour ces
releases carbon previously consumed from the atmosphere. CCU
technologies can theoretically be carbon neutral over the entire
life cycle if CO 2 is captured from the atmosphere (via biogenic
point sources or direct air capture) and the CO 2 is released at the
end-of-life ( Figure 11a ) or if CO 2 is captured from fossil point
sources and CO 2 is sequestered or permanently stored in the
product ( Figure 11b ) and if all other GHG emissions are zero
over the life cycle. C CU technologies ha ve potentially negative
emissions ( Figure 11c ) if CO 2 is captured from the atmosphere
(via biogenic point sources or direct air capture) and if CO 2 is
sequestered or permanently stored in the product and if overall
life cycle GHG emissions are lower than the amount of CO 2
fixated. If the amount of atmospheric CO 2 capture and fixation
is equal to other fossil emissions over the life cycle, the process is
carbon neutral.
In all other cases, CCU technologies have positive CO 2
emissions over the life cycle. Still, emissions can be lower than
for competing conventional processes ( Fig ure 12 ). In this c ase,
the CCU process also contributes to climate change mitigation
through substitution, and hence is carbon reducing. E ven though
such processes lower CO 2 emis sions compared to the st atus
quo, they are not carbon negative. In particular , thi s also holds
for carbon-reducing processes with negative CO 2 emissions
obtained from substitution. Through a pplying substitution
(section Solving Multi-Functionality) or cradle-to-gate analysis,
negative LCA results can be computed. However , the negative
LCA results does only reflect a comparison. In particular , negative
LCA results do not necessarily imply that the C CU product is
carbon neutral or e ven has negative emissions over its life cycle.
Therefore, negative CO 2 emissions obtained from substitution
shall be clearly stated as environmental benefit compared to
the benchmark technology and not as negative CO 2 emissions
over the life cycle. In addition, avoided CO 2 emissions and
other environmental impact from substitution shall be reported
separately ( T anzer and R amírez, 2019 ).
REPOR TING
The final step of an LCA study is a report. A ccording to
ISO 14044, “The results and conclusions of the LCA shall
be completely and accurately reported without bias to the
intended audience.” As sumptions made on data and met hods
should be transparently reported and enable the reader to
understand limitations of the results. Presented results should
enable readers to under stand the complexity and trade-offs of
the LCA study. Results and interpretation presented should
be in line with the goals of the study. The reports may be
reduced if sensitive or confidential information and data may not
be published.
The report shall include an executive summary and a technical
summary table to provide easy access to the data used in the
assessment. The main report sh all report all assumptions, data
for calculation, methods, results and limitations as transparently
and detailed as possible. This is also important to guarantee
reproducibility and full traceability by the reader. The assessment
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Müller et al. Guideline for LCA of CCU
results shall be clearly reported to the audience in order to avoid
ambiguity and misinterpretation.
The supporting information provides a checklist for an
executive summary, a technical summary t able and main report.
This checklist is derived from the ISO 14044 and the ILCD
handbook and additionally includes CCU-specific items.
DISCUSSION
Building upon established LCA standards and guidelines, our
work is tailored to the needs of LCA practitioners assessing
CCU technologies by identifying and resolving CCU-spe cific
pitfalls. The resulting guidelines substantially reduce th e space
for methodical choices in LCA with the goal to foster
comparable and transparent studies on the environmental
impacts of CCU.
E ven though our guideline alre ady defines a broad framework
for the environmental comparison of C CU technologies, some
aspects specific to C CU technologies are still unaddressed.
First, the guideline is not an ISO standard or document,
even thoug h reviewed by around 50 international experts from
industry, academia and policy in two workshops. Introducing
an ISO standard or document report could strongly enhance
the adoption of the guidelines. Howe ver , the process of
standardization is driven by industry and th us, can only be
initiated by us.
Second, the LCA guideline was developed in parallel to a
guideline for techno-economic assessment (TEA). Both TEA
and LCA are sub-divided into identical phases and both build
upon mass and energy balances and thus, share the same data
foundation. However , currently, the goal and scope of both
assessments are different: while LCA studies aim to quantify
the overall environmental impacts, TEA studies usually aim
to compare production costs, prices or analyze the market
situation. Therefore, both assessments are currently not aligned
and thus, TEA and LCA studies can be done at the same d ata
basis, but goal and scope may not ne cessarily be aligned. In
consequence, results of TEA and LCA ha ve to be interpreted
separately and combined indicators such as abatement costs ha ve
to be interpreted with caution. Therefore, a stronger alignment
between both guidelines would be beneficial, in particular ,
for the identification of trade-offs between environmental and
economic indicators.
Third, in many cases, CCU technologies promise to reduce
environmental impacts and achieve costs competitiveness. The
promises can, however , not be proven wit h high certainty
for technologies with early maturity, bec ause data availability
is low at these stages. For this reason, furt her methods
are needed to assess the potential of technologies with
low maturity.
Fourth, the last unsolved issue is that LCA reports are
usually of high complexity and long including trade-offs and
if-then conclusions. Decision-makers, such as policy makers,
often lack time and technological expertise to derive policies
from these highly complex LCA reports. Therefore, guidance
is missing for policy makers on how to commission and
understand LCA results. LCA practitioner s should develop
methods on how to write effective LCA reports for a
target audience.
CONCLUSION
This publication summarizes our guideline for standardized
life-cycle assessment of technologies for carbon capture and
utilization. This guideline aims to reduce the ambiguity in
methodological choices and enhances the transparency of
LCA studies. These goals ha ve been achieved by substantially
restricting the methodological choices currently left open by
LCA standards. To reduce methodological choices, we identified
typical goal definitions for LCA studies on CCU and provided
suitable scope definitions in line with these goal definitions. We
further predefined functional units and system boundaries with
respect to a CCU classification and provided a hierarc hy for
methods to solve multi-functionality with a focus on system-
wide assessments. For the life cycle inventory phase, we defined
rules to select data in line wit h major guideline s. Furthermore,
we recommended impact assessment methods with respect
to regional differences, in order to reduce the variation of
results. As CCU technologies are often set in a utopian future,
we define scenarios for the uncerta inty assessment for the
most common inputs in order to show the dependency of
clean feedstock. The presented guidelines should hopefully help
to strengthen the de velopment of environmentally beneficial
CCU technologies.
DA T A A V AILABILITY ST A TEMENT
The datasets for harmonized scenario analysis is provided in t he
electronic supporting information.
AUTHOR CONTRIBUTIONS
LM worked on the conception of this work, literature c ollection,
analysis, and drafted the article. MB contributed by drafting
section Uncertainty and Sensitivity analysis. AK, AS, AZ, and
AB contributed through to the conception of the work and
revising it critically for import ant intellectual content. All
authors contributed by giving final approval of the version to
be published.
FUNDING
Funding for this work from the Europe an Institute of Technology
(EIT) Climate-KIC grant number 180409 and by The Global CO 2
Initiative is thankfully acknowledged.
ACKNOWLEDGMENTS
The authors would like to thank Benedikt W inter (RWTH
Aac hen) for his support in the s cenario modeling as well as
Frontiers in Energy Resear ch | www .frontiersin.org 17 February 2020 | V olume 8 | Article 15

Müller et al. Guideline for LCA of CCU
Issam Dairanieh (formerly The Global CO 2 Initiative), Sira
Saccani (EIT Climate-KIC) and Ted Grozier (formerly EIT
Climate-KIC) as well as all participants of the co-collaboration
workshops and reviewers for their fruitful dis cussions
and feedback.
SUPPLEMENT AR Y MA TERIAL
The Supplementary Material for this article can be found
online at: https://www.frontiersin.org/articles/10.3389/fenr g.
2020.00015/full#supplementary-material
REFERENCES
AFNOR (2016). BP X30-323-0 General Principles for an Environmental
Communica tion on M ass M arket Products: Part 0: General Principles and
Methodological Fr amework . Paris: AFNOR
Al-Kalbani, H., Xuan, J., Garcia, S., and Wang, H. (2016). Comparative energetic
assessment of methanol production from CO 2 : chemical versus electrochemical
process. A ppl. Energy 165, 1–13. doi: 10.1016 /j.apenergy.2015.12.027
Al-Mamoori, A., Krishnamurthy, A., Rownaghi, A. A., and Rezaei, F. (2017).
Carbon capture and utilization update. Energy Technol. 5, 834–849.
doi: 10.1002/ente.201600747
Anicic, B., Trop, P., and Goricanec, D. (2014). Comparison between two
methods of methanol production from carbon dioxide. Energy 77, 279–289.
doi: 10.1016/j.energy.2014.09.069
Aresta, M., Caroppo, A., Dibenedetto, A., and Narracci, M. (2002). “Life Cycle
Asses sment (LCA) applied to the synthesis of methanol. Comparison of the
use of syngas with the use of CO 2 and dihydrogen produced from renewables, ”
in Environmental Challenges and Greenhouse Gas Control for Fossil Fuel
U tilization in the 21s t Century, Boston, MA: Publisher Name Springer , 331–347.
Aresta, M., and Galatola, M. (1999). Life cycle analysis applied to t he
assessment of the environmental impact of alternative synthetic
processes. The dimethylcarbonate case: part 1. J. Clean. Prod. 7, 181–193.
doi: 10.1016/S0959-6526(98)00074-2
Artz, J., Müller , T. E., Thenert, K., Kleinekorte, J., Meys, R., Sternber g,
A., et al. (2018). Sustainable conversion of carbon dioxide: an integrated
review of catalysis and life cycle assessment. Chem. Rev. 118, 434–504.
doi: 10.1021/acs.chemrev.7b00435
Ar vidsson, R., Tillman, A. M., Sandén, B. A., J anssen, M., Nordelöf,
A., Kushnir , D., et al. (2017). Environmental assessment of emerging
technologies: recommendations for prospective LCA. J. Ind. Ecol. 80:40.
doi: 10.1111/jiec.12690
Audi AG (2017). Audi g-Tron Models W ith Aud i e-Gas: The Energy Revolution in
the T ank . A vailable online at: https://www.audi- mediacenter.com/en/techday-
on- combustion- engine- technology- 8738/audi- g- tron- models- with- audi- e-
gas- the- energy- revolution- in- the- t ank- 8749 (accessed Marc h 27, 2018).
Baena-Moreno, F. M., Rodríguez-Galán, M., Vega, F., Alonso-Fariñas, B., V ilches
Arenas, L. F., and N avarrete, B. (2019). Carbon capture and utilization
technologies: a literature review and recent advances. Energy Sourc. A 41,
1403–1433. doi: 10.1080/15567036.2018.1548518
Bare, J. C. (2002). TRAC I 2.0: the tool for the reduction and assessment
of chemical and other environmental impacts 2.0. J. Ind. Ecol. 6, 49–78.
doi: 10.1162/108819802766269539
Baumann, H., and Tillman, A.-M. (2004). The H itch H ikers ’ s Guide to LCA:
An Orientat ion in Life Cycle A ssessment Me thodology and A pplication .
Lund: Studentlitteratur.
Blengini, G. A., Garbarino, E., Šolar , S., Shields, D. J., H ámor , T., V inai, R.,
et al. (2012). Life Cycle Assessment guidelines for the sustainable production
and recycling of aggregates: the Sustainable Aggregates Resource M anagement
project (SARMa). J. Clean. Prod. 27, 177–181. doi: 10.1016/j.jclepro.2012.01.020
Brandao, M., Levasseur , A., Kirschbaum, M. U. F., Weidema, B. P., Cowie,
A. L., Jorgensen, S. V., et al. (2013). Key issues and options in
accounting for carbon sequestration and temporary storage in life cycle
assessment and carbon footprinting. Int. J. Life Cycle As sess. 18, 230–240.
doi: 10.1007/s11367-012-0451-6
Brander , M. (2016). Transposing lessons between different forms of consequential
greenhouse gas accounting: lessons for consequential life cycle assessment,
project-level accounting, and policy-le vel accounting. J. Clean. Prod. 112,
4247–4256. doi: 10.1016/j.jclepro.2015.05.101
BSI (2011). P A S 2050 - Specifica tion for the Asse ssment of the L ife Cycle Greenhouse
Gas Emissions of Goods and Serv ices 13.310; 91.190 . London: BSI.
Bumann, A. A., P apadokonstantakis, S., Sugiyama, H., Fischer , U., and
Hungerbühler , K. (2010). Eva luation and analysis of a proxy indicator for
the estimation of gate-to-gate energy consumption in the early process
design phases: the case of organic solvent production. Energy 35, 2407–2418.
doi: 10.1016/j.energy.2010.02.023
Carbon Recycling International (201 9). Vulcanol . A vailable online at: http://
carbonrecycling.is/projects- 1/ (accessed Mar ch 27, 2018).
CarbonCure (2019). Contr ibution to LEED . A vailable online at: http://carboncure.
com/sustainability/contribution- to- leed/ (accessed Marc h 27, 2018)
Cespi, D., Beach, E. S., Swarr , T. E., Passarini, F., V assura, I., Dunn, P. J.,
et al. (2015). Life cycle inventory improvement in the pharmaceutical sector:
assessment of the sustainability combining PMI and LCA tools. Green Chem.
17, 3390–3400. doi: 10.1039/C5GC00424A
Cucurachi, S., van der Giesen, C., and Guinée, J. (2018). Ex-ante LCA of
emerging technologies. Proc. CIRP 69, 463–468. doi: 10.1016/j.procir.2017.
11.005
Cuéllar -Franca, R. M., and Azapagic, A. (2015). Carbon capture, storage and
utilisation technologies: a critical analysis and comparison of their life cycle
environmental impacts. J. CO 2 U til. 9, 82–102. doi: 10.1016/j.j cou.2014.12.001
Curran, M. A. (2012). Life Cycle A ssessment H andbook: A Guide for
Environmentally Susta inable Products . Beverly, MA: W iley-S crivener.
Deutz, S., Bongartz, D., Heuser , B., K ätelhön, A., Schulze L angenhorst, L.,
Omari, A., et al. (2018). Cleaner production of cle aner fuels: W ind-to-wheel
– environmental assessment of CO 2 -based oxymethylene ether as a drop-in
fuel. Energy Environ. Sci. 55:7296. doi: 10.1039 /C7EE01657C
ecoinvent (2017). Data on t he Production of Chemicals Crea ted for the EU Product
Environmental Footprint (PEF) Pilot Phase Implementa tion. Zürich: ecoinvent
Associatio n. A vailable online at: www.ecoinvent.org
European Commission - Joint Research Center (2010). ILCD H andbook -
General Guide for L ife Cycle Assessment - De tailed Guidance . Luxembour g:
Publications Office.
European Commission - Joint Research Center (2011a). ILCD H andbook:
Recommenda tions for Life Cycle Impact A ssessment in t he European Context .
Luxembourg: Publications Office.
European Commission - Joint Research Center (2011b). Supporting
Environmentally Sound Decisions for Bio-Was te Mana gement: A practical
guide to Life Cycle Th inking (LCT) and L ife Cycle Assessment (L CA) . Ispra:
European Commission - Joint Research Center
European Commission - Joint Research Center (2012). Product Environmental
Footprint (PEF) Guide . Ispra: European Commission - Joint Research Center.
European Commission - Joint Research Center (2018). B iomass Production,
Supply, U ses and Flows in the European Union: F irst Results From an Inte gra ted
Asse ssment . Ispra: European Commission - Joint Research Center.
European Commission (2018). Scientific Advice Mechanism (SAM): Novel Carbon
Capture and U tilisation Tec hnologies . Luxembourg: European Commission.
European Committee for Standardis ation (2009). ISO 14040- Environmental
M anagement – L ife Cycle Asse ssment – Principles and Fr amework 13.020.10 .
Berlin: Beuth Verlag GmbH.
European Committee for Standardisation (2017). ISO 14067 Greenhouse G ases –
Carbon Footprint of Products – Requirements and Gui delines for Quantifica tion
and Communica tion 13.020.4 0. Berlin: Beuth Verlag GmbH.
European Committee for Standardisation (20 18). ISO 14044 - Environmental
M anagement – L ife Cycle Asse ssment – Principles and Fr amework 13.020.10 .
Berlin: Beuth Verlag GmbH.
Frischknecht, R., Heath, G., R augei, M., Sinha, P., and de W ild-S cholten, M. (2016).
Methodology Guideline s on Life Cycle As sessment of Photovolt aic Electricity
3rd: EA PVPS T ask 1 . International Energy A gency Photovoltaic Power
Systems Programme.
GaBi Software-System v8.5.0.,79 and Database for Life Cycle Engineering SP 35
(1992–2018). Leinfeld-Ech terdingen: Thinkstep.
Frontiers in Energy Resear ch | www .frontiersin.org 18 February 2020 | V olume 8 | Article 15

Müller et al. Guideline for LCA of CCU
Garcia-Herrero, I., Cuellar -Franca, R. M., Enriquez- Gutierrez, V. M., Alvarez-
Guerra, M., Irabien, A., and Azapagic, A. (2016). Environmental assessment
of dimethyl carbonate production: comparison of a novel electrosynthesis
route utilizing CO 2 with a commercial oxidative carbonylation process. A CS
Susta inable Chem. Eng. 4, 2088–2097. doi: 10.1021/acssuschemeng.5b01515
Gavankar , S., Anderson, S., and Keller , A. A. (2015a). Critical components of
uncertainty communication in life cycle assessments of emerging technologies.
J. Ind. Ecol. 19, 468–479. doi: 10.1111/jiec.12183
Gavankar , S., Suh, S., and Keller , A. A. (2015b). The role of scale and technology
maturity in life cycle assessment of emerging technologies: a case study on
carbon nanotubes. J. Ind. Ecol. 19, 51–60. doi: 10.1111/jiec.12175
Gendorf Chemiepark (2017). Umwelterklärung 2017 . Gendorf:
Gendorf Chemiepark
Groen, E. A., Heijungs, R., Bokkers, E. A. M., and de Boer , I. J. M. (2014). Methods
for uncertainty propagation in life cycle assessment. Environ. Model. Softw. 62,
316–325. doi: 10.1016/j.envsoft.2014.10.006
Guinée, J. B. (2006). H andbook on L ife Cycle Asses sment: Opera tional Guide to the
ISO Standards . Dordrecht: Kluwer A cademic Publishers.
H auschild, M., and Huijbregts, M. A. J. (eds.). (2015). Life Cycle Impact Asse ssment .
Dordrecht: Springer.
Heijungs, R. (2010). Sensitivity coefficients for matrix-based LCA. Int. J. Life Cycle
Asse ss. 15, 511–520. doi: 10.1007/s11367-010-0158-5
Heijungs, R., and Frischknecht, R. (1998). A special view on the nature of the
allocation problem. Int. J. LCA 3, 321–332. doi: 10.1007/BF02979343
Henriksson, P. J. G., Heijungs, R., Dao, H. M., Phan, L. T., Snoo, G.
R. de, and Guinée, J. B. (2015). Product carbon footprints and their
uncertainties in comparative decision contexts. PLoS ONE. 10:e0121221.
doi: 10.1371/journal.pone.0121221
Hoppe, W., Bringezu, S., and Thonemann, N. (2016). Comparison of global
warming potential between conventionally produced and CO2-based natural
gas used in transport versus chemical production. J. Clean. Prod. 121, 231–237.
doi: 10.1016/j.jclepro.2016.02.042
Hoppe, W., Thonemann, N., and Bringezu, S. (2017). Life cycle assessment
of carbon dioxide-based production of methane and methanol and derived
polymers. J. Ind. Ecol. 7:181. doi: 10.1111/jiec.12583
Huijbregts, M. A. J., Norris, G., Bretz, R., Ciroth, A., Maurice , B., Bahr , B., et al.
(2001). Framework for modelling data uncertainty in life cycle inventories. Int.
J. Life Cycle A ssess. 6, 127–132. doi: 10.1007/BF02978728
Igos, E., Benetto, E., Meyer , R., Baustert, P., and Othoniel, B. (2018). How to treat
uncertainties in life cycle assessment studies? Int. J. Life Cycle As sess. 176:359.
doi: 10.1007/s11367-018-1477-1
International Energy Agency (2017). Energy Tec hnology Pers pectives 2017:
Cat alysing Energy Tec hnology Transforma tions . Paris: OECD.
International Organization for Standardization (2014). ISO 14071 - Environmental
M anagement - L ife Cycle Assessment - Critic al Rev iew Processe s and Rev iewer
Competencies: Add itional Requirements and Guidelines to ISO 14044:2006 .
Berlin: International Organization for Standardization.
Jiménez-González, C., Kim, S., and Overcash, M. R. (2000). Methodology for
developing gate-to-gate Life cycle inventory information. Int. J. Life Cycle
Asse ss. 5, 153–159. doi: 10.1007/BF02978615
Jung, J., von der Assen, N., and Bardow, A. (2014). Sensitivity coefficient-based
uncertainty analysis for multi-functionality in LCA. Int. J. Life Cycle As sess. 19,
661–676. doi: 10.1007/s11367-013-0655-4
Kaetelhoen, A., Bardow, A., and Suh, S. (2016). Stochastic technology choice model
for consequential life cycle assessment. Environ. Sci. Technol. 50, 12575–12583.
doi: 10.1021/acs.est.6b04270
Kaetelhoen, A., von der Assen, N., Suh, S., Jung, J., and Bardow, A. (2015).
Industry-cost-cur ve approach for modeling the environmental impact of
introducing new technologies in life cycle assessment. Environ. Sci. Technol.
49, 7543–7551. doi: 10.1021/es5056512
Kätelhön, A., Meys, R., Deutz, S., Suh, S., and Bardow, A. (2019). Climate
change mitigation potential of carbon capture and utilization in the chemical
industry. Proc. N atl. Ac ad. Sci. U.S.A. 116, 11187–11194. doi: 10.1073/pnas.1821
029116
Kim, J., Henao, C. A., Johnson, T. A., Dedrick, D. E., Miller , J. E., Stechel, E. B., et al.
(2011). Methanol production from CO 2 using solar-thermal energy: proce ss
development and techno-economic analysis. Energy Env iron. Sci. 4, 3122–3132.
doi: 10.1039/c1ee01311d
Kim, S., and Overcash, M. (2003). Energy in chemical manufacturing processes:
gate-to-gate information for life cycle assessment. J. Chem. Tec hnol. Biotechnol.
78, 995–1005. doi: 10.1002/jctb.821
Levasseur , A., Lesage, P., M argni, M., Brandao, M., and Samson, R. (2012).
Asses sing temporary carbon sequestration and storage projects throug h
land use, land-use change and forestry: comparison of dynamic life
cycle assessment with ton-year approaches. Clim. Change 115, 759–776.
doi: 10.1007/s10584-012-0473-x
Levasseur , A., Lesage, P., M argni, M., Deschênes, L., and Samson, R.
(2010). Considering time in LCA: dynamic LCA and its application to
global warming impact assessments. Environ. Sci. Technol. 44, 3169–3174.
doi: 10.1021/es9030003
Lloyd, S. M., and Ries, R. (2007). Characterizing, propagating, and analyzing
uncertainty in life-cycle assessment - a sur vey of quantitative approaches. J. Ind.
Ecol. 11, 161–179. doi: 10.1162/jiec.2007.1136
Luu, M. T., Milani, D., Ba hadori, A., and A bbas, A. (2015). A comparative
study of CO 2 utilization in methanol synthesis with various syngas production
technologies. J. CO 2 U til. 12, 62–76. doi: 10.1016/j.jcou.2015 .07.001
Malmqvist, T., Glaumann, M., Scarpellini, S., Z abalza, I., Aranda, A., Llera,
E., et al. (2011). Life cycle assessment in buildings: the ENSLIC simplified
method and guidelines. Energy. 36, 1900–1907. doi: 10.1016/j.energy.2010.
03.026
Mattila, T., Lehtoranta, S., Sokka, L., Melanen, M., and Nissinen, A.
(2012). Methodological Aspects of Applying Life Cycle Assessment
to Industrial Symbioses. Journal of Industrial Ecology 16, 51–60.
doi: 10.1111/j.1530-9290.2011.00443.x
Matzen, M., and Demirel, Y. (2016). Methanol and dimethyl ether from
renewable hydrogen and carbon dioxide: Alternative fuels production and life-
cycle assessment. J. Clean. Prod. 139, 1068–1077. doi: 10.1016/j.jclepro.2016.
08.163
N aims, H., Olfe-Kräutlein, B., Lorente Lafuente, A. M., and Bruhn, T. (2015).
CO 2 Recycling – An Option for Policymaking and Socie ty? Twelve Theses on
the Societ al and Political S ignificance of Carbon Capture and U tilisat ion (CCU)
Technologies . Institute for Advanced Sustainability Studies (IA SS).
Pa rra, D., Zhang, X., Bauer , C., and Patel, M. K. (2017). An integrated techno-
economic and life cycle environmental assessment of power-to-gas systems.
A ppl. Energy 193, 440–454. doi: 10.1016/j.apenergy.2017.02.063
Pehnt, M. (2006). Dynamic life cycle assessment (LCA) of renewable ener gy
technologies. Renew. Energy 31, 55–71. doi: 10.1016/j.renene.2005.03.002
Pfingsten, S. von, Broll, D. O., von der Assen, N., and Bardow, A. (2017). Second-
order analytical uncertainty analysis in life cycle assessment. Environ. Sci.
Technol. 51, 13199–13204. doi: 10.1021/acs.est.7b01406
Schakel, W., Oreggioni, G., Sing h, B., Stromman, A., and R amirez, A. (2016).
Asses sing the techno-environmental performance of CO2 utilization via dry
reforming of methane for the production of dimethyl ether. J. CO 2 U til. 16,
138–149. doi: 10.1016/j.jcou.2016.06.005
Schenker , U., Scheringer , M., Sohn, M. D., Maddalena, R. L., M cKone, T. E.,
and Hungerbühler , K. (2009). U sing information on uncertainty to improve
environmental fate modeling: a case study on DDT. Environ. Sci. Technol. 43,
128–134. doi: 10.1021/es801161x
Sills, D. L., Pa ramita, V., Franke, M. J., Johnson, M. C., Akabas, T. M.,
Greene, C. H., et al. (2013). Quantitative uncertainty analysis of Life Cycle
Asses sment for algal biofuel production. Env iron. Sci. Technol. 47, 687–694.
doi: 10.1021/es3029236
Sonnemann, G. W., Schuhmacher , M., and Castells, F. (2003). Uncert ainty
assessment by a Monte Carlo simulation in a life cycle inventory of
electricity produced by a waste incinerator. J. Clean. Prod. 11, 279–292.
doi: 10.1016/S0959-6526(02)00028-8
Souza, L. F. S., Ferreira, P. R. R., Medeiros, J. L. de, Alves, R. M. B., and Araújo,
O. Q. F. (2014). Production of DMC from CO 2 via indirect route: technical–
economical–environmental assessment and analysis. A CS Susta in. Chem. Eng.
2, 62–69. doi: 10.1021/sc400279n
Sternberg, A., and Bardow, A. (2015). Power-to-What? - Environmental
assessment of energy stora ge systems. Energy Environ . Sci. 8, 389–400.
doi: 10.1039/c4ee03051f
Sternberg, A., and Bardow, A. (2016). Life cycle assessment of power-
to-gas: syngas vs methane. A CS Sustain. Chem. Eng. 4, 4156–4165.
doi: 10.1021/acssuschemeng.6b00644
Frontiers in Energy Resear ch | www .frontiersin.org 19 February 2020 | V olume 8 | Article 15

Müller et al. Guideline for LCA of CCU
Sternberg, A., Jens, C. M., and Bardow, A. (2017). Life cycle assessment of CO 2
-based C1-chemicals. Green Chem. 19, 2244–2259. doi: 10.1039/C6GC02852G
Sugiyama, H., Fischer , U., Hungerbühler , K., and Hirao, M. (2008). Decision
framework for chemical process design including different stages of
environmental, health, and s afety assessment. AIChE J. 54, 1037–1053.
doi: 10.1002/aic.11430
T anzer , S. E., and R amírez, A. (2019). When are ne gative emissions negative
emissions? Energy Environ. Sci. 12, 1210–1218. doi: 10.1039/C8EE03338B
The European Parliament and the council of the European Union (2019). Directive
(EU) 2019/944. Brussels: The European Parliament and the council of the
European Union.
Uusitalo, V., V aisanen, S., Inkeri, E., and Soukka, R. (2017). Potential for
greenhouse gas emission reductions using surplus electricity in hydrogen,
methane and methanol production via electrolysis. Energ. Convers. M anag. 134,
125–134. doi: 10.1016/j.enconman.2016.12.031
van der Giesen, C., Kleijn, R., and Kramer , G. J. (2014). Energy and climate impacts
of producing synthetic hydrocarbon fuels from CO 2 . Env iron. Sci. Technol. 48,
7111–7121. doi: 10.1021/es500191g
V illares, M., I¸ sildar , A., van der Giesen, C., and Guinée, J. (2017). Does ex ante
application enhance the usefulness of LCA? A case study on an emerging
technology for metal recovery from e-waste . Int. J. Life Cycle As sess. 22,
1618–1633. doi: 10.1007/s11367-017-1270-6
von der Assen, N., and Bardow, A. (2014). Life cycle assessment of polyols for
polyurethane production using CO2 as feedstock: insights from an industrial
case study. Green Chem. 16, 3272–3280. doi: 10.1039/c4gc00513a
von der Assen, N., Jung, J., and Bardow, A. (2013). Life-cycle assessment of carbon
dioxide capture and utilization: avoiding the pitfalls. Energy Environ. Sci. 6,
2721–2734. doi: 10.1039/c3ee41151f
von der Assen, N., Voll, P., Peters, M., and Bardow, A. (2014). Life cycle assessment
of CO 2 capture and utilization: a tutorial review. Chem. Soc. Rev. 43, 7982–79 94.
doi: 10.1039/c3cs60373c
Wei, W., Larrey-L assalle, P., Faure , T., Dumoulin, N., Roux, P., and Mathias, J.-
D. (2016). U sing the reliability theory for assessing the decision confidence
probability for comparative life cycle assessments. Environ. Sci. Technol. 50,
2272–2280. doi: 10.1021/acs.est.5b03683
Weidema, B., Bauer , C., Hischier , R., Mutel, C., Neme cek, T., Reinhard, J., et al.
(2013). Over view and Methodology. Dat a Quality Guideline for the Ecoinvent
Dat abase Ver sion 3 . St. Gallen. A vailable online at: https://www.ecoinvent.org/
files/dataqualityguideline_ecoinvent_3_20130506.pdf
Wernet, G., Hellweg, S., Fischer , U., Papadokonstantakis, S., and Hungerbühler , K.
(2008). Molecular-structure-based models of chemical inventories using neural
networks. Environ. Sci. Technol. 42, 6717–6722. doi: 10.1021/es7022362
Wernet, G., Papadokonstantakis, S., Hellweg, S., and Hungerbühler , K. (2009).
Bridging data gaps in environmental assessments: Modeling impacts of
fine and basic chemical production. Green Chem. 11:1826. doi: 10.1039/b9
05558d
W illiams, E. D., Weber , C. L., and Hawkins, T. R. (2009). Hybrid framework
for managing uncertainty in life cycle inventories. J. Ind. Ecol. 13, 928–944.
doi: 10.1111/j.1530-9290.2009.00170.x
World Resources Institute and World Busines s Council for Sustainable
Development (2011). Greenhouse Gas Protocol: Produc t Life Cycle Account ing
and Reporting Standard . Was hington, D C; Geneva: World Resources Institute;
World Business Council for Sustainable Development.
Y ang, Y., and Heijungs, R. (2018). On t he use of different models for
consequential life cycle assessment. Int. J. Life Cycle As sess. 23, 751–758.
doi: 10.1007/s11367-017-1337-4
Zhang, X., Bauer , C., Mutel, C. L., and Volkart, K. (2017). Life cycle assessment
of power-to-g as: approaches, system variations and their environmental
implications. A ppl. Energy 190, 326–338. doi: 10.1016/j.apenergy.2016.12.098
Zimmerman, A., Müller , L. J., M ar xen, A., Armstrong, K., Buchner , G.,
Wunderlich, J., et al. (2018). Techno-Economic Asse ssment and L ife-Cycle
Asse ssment Guidelines for CO 2 U tilization . Ann Arbor , MI.
Conflict of Interest: The authors declare that the research was conducted in the
absence of any commer cial or financial relationships that could be construed as a
potential conflict of interest.
Copyright © 2020 Müller , Kä telhön, Bachmann, Zimmermann, Sternberg and
Bardow. This is an open-acce ss article distributed under the terms of the Cre at ive
Commons A ttr ibution L icense (CC BY). The use, distribution or reproduction in
other forums is permitted, provided the orig inal author(s) and the copyright owner(s)
are credited and th at t he orig inal publica tion in th is journal is cited, in accordance
with accepted academic pr ac tice. No use, distribution or reproduction is permitted
whic h does not comply with t hese terms.
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Why organizations use Identific for document trust, entry 82

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