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Transcript of Production pathways for renewable jet fuel - Spiral@Imperial ...
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Production pathways for renewable jet fuel: a review of commercialisation status and future prospects Rebecca Mawhood1*, Evangelos Gazis1, Sierk de Jong2, Ric Hoefnagels2, Raphael Slade1
1. Centre for Environmental Policy, Imperial College London
2. Copernicus Institute of Sustainable Development, Utrecht University
1 Abstract Aviation is responsible for an increasing share of anthropogenic CO2 emissions.
Decarbonisation to 2050 is expected to rely on renewable jet fuel (RJF) derived from
biomass, but this represents a radical departure from the existing regime of petroleum-
based fuels. Increased market deployment will require significant cost reductions, alongside
adaptation of existing supply chains and infrastructure.
This article maps development and manufacturing efforts for six RJF production pathways
expected to reach commercialisation in the next 5-10 years. A Rapid Evidence Assessment
was conducted to evaluate the technological and commercial maturity of each pathway and
progress towards international certification, using the Commercial Aviation Alternative Fuels
Initiative’s Fuel Readiness Level (FRL) framework. Planned and operational facilities have
been catalogued alongside partnerships with the aviation industry. Policy and economic
factors likely to affect future development and deployment are considered.
Hydroprocessed Esters and Fatty Acids (FRL 9) is the most developed pathway. It is ASTM
certified, has fuelled the majority of RJF flights to date, and is produced at three
commercial-scale facilities. Fischer-Tropsch derived fuels are moving towards the start-up of
first commercial facilities (FRL 7-8), although widespread deployment seems unlikely under
current market conditions. The Direct Sugars to Hydrocarbons conversion pathway (FRL 5-7)
is being championed by Amyris and Total in Brazil, but has yet to be demonstrated at scale.
Other pathways are in the demonstration and pilot phases (FRL 4-6).
Despite growing interest in RJF, demand and production volumes remain negligible.
Development of supportive policy is likely to be critical to future deployment.
*Corresponding author.
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2 Introduction Aviation is currently responsible for 2% of global anthropogenic carbon emissions.1
As
demand grows a rapid increase in annual emissions from 705 Mt of CO2 in 2013 to between
1,000 and 3,100 Mt by 2050 is anticipated.2 If the aviation sector is to contribute to
international policy ambitions to mitigate climate change, specific CO2 emissions per
passenger kilometre will need to be greatly reduced. Near-term options to decarbonise air
travel, however, are limited. Modern aircraft are already highly fuel-efficient, and
technological improvements tend to be incremental. Moreover, the diffusion of
improvements across the active global fleet is expected to be slow because commercial
aircraft have a service lifetime of 25 years.2 Advances in air traffic management and engine
efficiency have the potential to reduce aviation emissions by an estimated 0.8% per annum
over the period to 2050, equivalent to an aggregate reduction of around 15% from 2015,
but these reductions are expected to be insufficient to offset increases in passenger
numbers.2,3 The majority of emission reductions will therefore need to come from the
uptake of low carbon liquid fuels and particularly biofuels.
Within the aviation sector there is optimism that kerosene-like fuels produced from biomass
(hereafter referred to as renewable jet fuel (RJF)) could offer a viable means to reduce
emissions under the right policy circumstances. Recent years have witnessed increasing
activity in terms of research, development and deployment, test flights, fuel off-take
agreements and certification, with major commercial and military aircraft operators playing
a leading role.4,5 Yet to date almost all flights powered by RJF have used fuels derived from
vegetable oils and fats.6 Although production from these materials is straightforward, the
potential to scale-up RJF volumes is severely restricted by the lack of low cost and
sustainable feedstocks. Indeed, in many cases unprocessed vegetable oils are already more
costly than fossil jet fuel. The search is on, therefore, for alternative conversion pathways
and feedstocks that can offer the prospect of cost-effective and large-scale production.
Options being investigated include a diverse range of technologies with the potential to
upgrade sugars, alcohols and vegetable oils, to convert lignocellulosic feedstocks, and to
make effective use of low cost sources of biomass. Comparison of the commercialisation
status of these alternative pathways is often hindered by the absence of a common
technology terminology and a lack of transparency around competing claims by companies
seeking to promote their own proprietary technology.
The primary aim of this paper is therefore to provide an overview of the status quo in RJF
production pathways expected to be commercially available within the next 5-10 years. It
presents the results of a Rapid Evidence Assessment (REA) conducted to evaluate the
maturity of alternative conversion pathways using the Commercial Aviation Alternative
Fuels Initiative’s (CAAFI) Fuel Readiness Level (FRL) framework. It also provides a brief
assessment of policy and economic factors likely to affect the future development and
deployment of RJF. This analysis provides a detailed snapshot of the current status of RJF
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production options, and thus a basis to identify research needs, facilitate policy decisions
and inform investment strategies. This paper does not, however, seek to provide a detailed
review of the technical characteristics of biomass feedstocks, nor feedstock cost trends,
since these are generic across the bioenergy arena and well covered elsewhere. The reader
is referred to Chum et al. (2011) and Cazzola et al. (2013) and for discussion of these
issues.7,8
3 Methods A Rapid Evidence Assessment (REA) methodology was employed to obtain a comprehensive
overview of planned and operational RJF production facilities and to identify economic and
policy factors affecting future deployment of RJF. REA is an approach to collating and
synthesising evidence that draws on best practice systematic review methods for evidence
based policy; it entails rigorous searching of the literature to tackle a well-defined research
question.9,10 Advantages of this approach include minimising bias when selecting papers; a
disadvantage is that publications may be missed if these fall outside the search criteria.
One of the most important milestones for commercial acceptance of a new fuel is technical
certification by the American Society for Testing and Materials (ASTM)†, a mandatory
prerequisite for the fuel to be used in commercial aviation. The certification process has to
date taken between one and six years. Given this study’s focus on pathways expected to be
commercially available in the short term, the REA’s scope was limited to pathways which
have already been certified by the ASTM or which have a formal ASTM task force working
towards certification. Twelve such task forces exist, representing six families of conversion
technologies‡: hydroprocessed esters and fatty acids (HEFA) (which is considered to include
the catalytic hydrothermolysis (CT) and co-processing task forces for the purpose of this
report), Fischer-Tropsch (FT), direct sugars to hydrocarbons (DSHC), hydrotreated
depolymerised cellulosic jet (HDCJ), alcohol to jet (ATJ), and aqueous phase reforming
(APR).4,11 Figure 1 summarises the feedstocks and key processes for each of these. A number
of other RJF pathways exist but have been excluded since the ASTM task forces around
these have not yet been formed. The lignin to jet conversion pathway being developed by
the Italian company BioChemtex is one such example.12
† The ASTM International standard ASTM D7566 (established 2009) specifies technical requirements for synthetic jet fuels, including biofuels and blends with petroleum kerosene.160 Fuels meeting the standard are considered to be equivalent to conventional jet fuel and can be mixed in aircraft and supply infrastructure without the need for separate tracking or approval. A further standard, ASTM D4054, provides guidance on the testing requirements and property targets necessary for the evaluation of a candidate synthetic jet fuel. ‡ Task forces have been clustered with regards to process design, feedstock and product output. For this analysis no explicit distinction was made between synthetic paraffinic kerosene (SPK) and synthetic kerosene with aromatic (SKA) task forces.
4
Figure 1 RJF conversion pathways: feedstocks and processes.
Data regarding the commercialisation status of these pathways were collected from
academic, grey and industry literature. The Primo Central Index and Google Scholar were
interrogated for English language reports published between 2009 and 2014 using the
search terms: alternative fuels OR biofuels AND aviation. Key industry reports
recommended by the RENJET consortium members were also included, and the
bibliographies of relevant articles were reviewed for related citations. Publications were
excluded if: i) they did not specifically consider aviation fuels; ii) they considered the
development of only one aspect of the conversion processes; iii) they solely focussed on the
combustion characteristics of these fuels. This search strategy identified 18,396 titles, of
which 175 were deemed to fit the inclusion criteria. It also revealed the paucity of peer-
reviewed literature addressing the commercialisation activities of RJF developers, with only
32 such studies being identified. The lack of existing academic literature can be explained in
part by the commercial sensitivity of the topic of study: private companies are the leading
players promoting commercial-scale application of RJF production, typically using
proprietary technologies, and public reporting is accordingly minimal in many cases. The
findings presented in the current paper are therefore largely reliant on grey literature and
the aviation industry reports that were deemed to be of higher quality. Additional searches,
including media reports, were conducted to verify the current status of the biofuel
developers and facilities.
The data gathered were used to assess the commercialisation status of the conversion
pathways in accordance with the Commercial Aviation Alternative Fuels Initiative’s (CAAFI)
Fuel Readiness Level (FRL) methodology. The FRL approach is based on NASA’s ‘Technology
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Readiness Level’ (TRL) framework and is intended to provide a descriptive hierarchy
indicating the progress of a technology towards commercialisation via a series of “toll gates”
(Table 1).13,14 Unlike the TRL framework, the FRL method is specifically designed to reflect
the range of risks affecting the development of fuels (as opposed to equipment), in
particular a fuel’s chemistry and compatibility with fuelling infrastructure and aircraft.14,15
The FRL was preferred over the TRL since it is accepted as the best-practice communication
tool of fuel technology maturity within the aviation industry.14,15
Cost data were excluded from the review as very few cost estimates available in the
literature provide sufficient detail to allow comparison of alternative RJF pathways on an
equal footing. The reader is referred to De Jong et al. (2015) for an analysis of RJF
production costs.16
4 Results
Hydroprocessed esters and fatty acids (HEFA): FRL 6-8
Hydroprocessed esters and fatty acids (HEFA) technology combines hydrotreatment and
isomerisation to convert triglycerides to (iso)paraffinic hydrocarbons in the jet range. Efforts
are also underway to develop RJF using blends with HEFA-diesel.§
HEFA-jet is the most highly developed and widely utilised RJF technology at the time of
writing, with several commercial facilities operational and under development (Table 2). It
was ASTM certified in 2011 for use in blends of up to 50% with fossil jet fuel, and has fuelled
the majority of RJF demonstration flights (since 2008).4,6,17 It has also been used in
commercial flights since 2011.6 Most of these have used fuel derived from vegetable oils,
used cooking oil (UCO) and animal fats, although oil from non-edible crops such as jatropha,
camelina and algae-derived oils have also been used.
The most widely deployed HEFA technologies are those developed by Honeywell UOP/Eni
(EcofiningTM and the UOP Renewable Jet ProcessTM) and Neste (NexBTL) (Table 2), all of
which are deployed commercially. The processes differ in both process design and the
flexibility to alter the RJF/diesel ratio in the product slate.16 UOP’s Renewable Jet process
includes selective cracking alongside isomerization and hydrotreatment, thereby maximizing
RJF output, but also producing more light components.16,18 Both UOP processes were
designed such that they can be used to repurpose existing refineries and target the
production of RJF19,20 In contrast, Neste’s current facilities have been optimised for diesel
production; it is technically possible to produce RJF, but it requires significant adjustment to
the process conditions.
§ Jet and diesel fuel produced via HEFA are commonly referred to as hydrotreated renewable jet (HRJ) and hydrotreated renewable diesel (HRD). To avoid confusion they are simply called HEFA-jet and HEFA-diesel for the purpose of this paper.
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The UOP technologies are being used by Eni and Altair Fuels to repurpose two mothballed
refineries to decrease capital investments; according to Eni this strategy has led to a capital
expenditure of 100M€ compared to 600 M€ for a greenfield project.19 The two biorefineries
are respectively located in Venice, Italy (operational since 2014, with plans to produce RJF
alongside the primary diesel product) and Paramount, USA (under construction, expected to
be the world’s first continuous RJF production facility).19,21–23 Six additional facilities
targeting commercial RJF production using the UOP processes are being developed by Altair
Fuels, Petrixo and SG Preston, with planned start-dates from 2016 to 2020.24–26 Neste has
three operational commercial refineries which can be configured to produce batches of
HEFA-jet.27 Other active HEFA-jet developers include Sinopec and Pertamina.28,29
Several fuel testing, flight demonstration and fuel offtake partnerships exist between
producers and the aviation sector. RJF produced via EcofiningTM has been used by 16
aviation operators for commercial flights, as well as test and demonstration flights by the US
and Dutch militaries.23 Notably, it was used by GOL for 200 scheduled flights during the 2014
FIFA World Cup and by Aeroméxico for 52 flights between Mexico City & Costa Rica in
2011.23 AltAir Fuels has an offtake agreement for 15 million gallons of EcofiningTM RJF to fuel
United Airlines’ flights from Los Angeles International Airport over 2014-2017.24 Neste’s RJF
was used by Lufthansa for 1,187 scheduled domestic flights (Hamburg-Frankfurt) in 2011,
and one scheduled transatlantic flight (Frankfurt-Washington DC) in 2012.27 Neste plans to
produce 1.4 million litres of RJF over 2015-2016 for the EU ITAKA project,30 some of which is
being mixed with conventional jet fuel at fuel in Oslo Airport’s hydrant supply system; this is
the first non-segregated airport supply of RJF in the world.31 The company also supplies RJF
to the Finnish Air Force, and is working with KLM and Schiphol Airport (amongst others) to
scale-up RJF production at its Rotterdam facility.27,30,32 Hainan Airlines and Boeing partnered
with Sinopec for China’s first commercial RJF flight in late 2015.28
Most existing HEFA capacity, however, is optimised to produce diesel for use in road
transport (HEFA-diesel). Jet requires tuning of the process conditions and selective
hydrocracking to increase the yield of light components at the expense of the overall
distillate yield.18 The reconfiguration of some diesel capacity for commercial RJF production
is expected under existing collaborations with the aviation sector. Boeing has been exploring
the potential to blend HEFA-diesel in low concentrations with fossil jet since 2014. The
company successfully conducted the first test flight with a 15% HEFA-diesel blend supplied
by Neste in 2015, and anticipates that ASTM certification will be achieved in 2016.33 Boeing
claims that RJF produced using HEFA-diesel blends could be cheaper than HEFA-jet due to
increased economies of scale and diversity of supply locations,34 with the potential to unlock
sufficient refining capacity to provide 1% of global jet fuel uptake.33
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An additional complication is the availability of triglyceride feedstocks. World supply of
major vegetable oils is expected to exceed 178 million tonnes in 2015/16, 35 but the aviation
industry is reluctant to pursue large-scale conversion of these to RJF, due to perceived
competition with food production and concerns about environmentally-unsustainable
plantations.36 Many producers are instead to looking to waste oils to mitigate these
concerns in the short-term. The most widely used waste oil for RJF flights to date is used
cooking oil (UCO),17 however supplies are much smaller than the potential vegetable oil
resource. Regional estimates for the collectable volume include 542,000 t/yr in the USA (of
which 50% is used for biodiesel), 3 million t/yr in China, 646,800 t/yr in Indonesia and
22,099 t/yr in Argentina.37 In the EU-27 it is estimated that 972,000 t/yr could be collected
from commercial kitchens, but 90% of this is already utilised for biodiesel production - and
the 2015 amendment (EU)/2015/1513 to the EU Renewable Energy Directive is expected to
increase demand for road transport fuels further.37 **
HEFA technology is mature and already deployed at commercial scale (FRL 9). Use of HEFA-
diesel for aviation is novel, but certification and redirection of road transport streams could
rapidly push it to FRL 9. Despite this advanced status, however, HEFA technology should not
be considered a silver bullet for aviation as market penetration is capped by limited
availability and the high price of sustainable feedstock. In the current market environment it
may also be difficult for aviation to secure large-scale HEFA-diesel production capacity given
the existence of incentives for road transport biodiesel and the comparatively low price of
kerosene.
4.1.1 Co-processing and catalytic hydrothermolysis (CH) – FRL 6
Co-processing and catalytic hydrothermolysis technologies are also being explored as
potential production pathways for RJF from triglycerides, with each being promoted by an
ASTM task force. The co-processing ASTM task force, led by BP, Chevron and Phillips 66, is
investigating the feasibility of co-processing vegetable oil alongside middle distillates in
existing refineries.38 This approach leverages existing hydrotreating and hydrocracking
capacity and thus reduces the capital investment.39 The catalytic hydrothermolysis
pathway, developed jointly by ARA and Blue Sun Energy, uses water to reduce hydrogen
consumption and produces aromatic, cycloparaffinic, and isoparaffinic hydrocarbons.40 The
resulting product is suitable for use as a 100% drop-in fuel. ARA and Blue Sun Energy have
been contracted to produce RJF for US Navy, with deliveries due in 2015 and 2016.41
** The amendment retains the requirement for 10% of Member States’ transport energy consumption to come from renewable technologies by 2020, but caps the proportion that can be produced from food-based energy crops at 7% - whilst allowing fuels produced from UCO (amongst other feedstocks) to be double-counted towards the blending target.161
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Both co-processing and catalytic hydrothermolysis are yet to be commercialized and ASTM
certified. As such they have been categorised as FRL 6.
Fischer-Tropsch (FT) – FRL 7-8
Fischer-Tropsch (FT) pathways combine biomass gasification (or co-gasification with coal)
with Fischer-Tropsch synthesis and catalytic cracking to produce synthetic paraffinic
kerosene (SPK). SPK is a high quality liquid fuel that can substitute directly for conventional
kerosene jet fuel.
Fischer-Tropsch (FT) synthesis has been applied to coal and natural gas feedstocks in
industry for several decades. It is fully commercial although research and development is
still ongoing to improve catalyst performance. Coal-derived FT jet fuel has been used in
blends of up to 50% with conventional jet fuel for commercial flights since 1999, and as a
neat (pure/unblended) fuel since 2010, with no significant technical problems reported.42,43
Natural gas-derived FT jet fuel has been commercially produced since 2012 and is routinely
used in blends of up to 25% by Shell.42 Application of the process to biomass, however, is
considered to require considerable further development, particularly regarding the handling
of biomass feedstocks and syngas cleaning.42,44 Moreover, this capital-intensive process is
only cost effective at large scale, putting pressure on feedstock logistics and increasing
investment risk. The production of small amounts of biomass-SPK in test facilities has
enabled this fuel to be ASTM certified for commercial use (in blends of up to 50% with
petroleum jet fuel) since September 2009,4 but production volumes remain low and only a
handful of demonstration flights have been completed.
In the 2000s it was widely anticipated that FT would develop rapidly, but progress has been
slower than expected.13 Operations have ceased at pilot plants previously operated by the
companies CHOREN and NSE Biofuels, Forest BtL has frozen plans for a demonstration plant,
and the Solena/British Airways GreenSky project – targeting 50,000 tonnes/year of RJF - has
been cancelled.42,45–47 Despite these setbacks a small number of demonstration and
commercial facilities are being developed, with projected completion dates ranging from
2017 to 2020.
The largest, BioTfueL, aims to produce 200,000 tonnes of RJF and diesel per annum from co-
gasified biomass, crude oil and coal.48 Fulcrum Bioenergy and Red Rock Biofuels are
targeting 10-12 million litres of fuel per year, respectively from municipal solid waste, and
forestry and sawmill residues.49,50 Fulcrum Bioenergy has secured an offtake agreement
with Cathay Pacific Airways for five production plants, and a US $30 million investment from
United Airlines.51,52 Red Rock has supply agreements with Southwest Airlines and FedEx
Express.53
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On the FRL scale the FT pathway can be categorised as FRL 7 (corresponding with ASTM
certification) with evidence of progress towards FRL 8. Whether further progress to FRL 9
will occur, however, is difficult to judge. The quality of the fuel is not in question but the
difficulty of constructing operational production plant remains a challenge. The existence of
collaborations with airlines for demonstration projects is a positive indication that these
companies have faith in the technology. But a history or false starts and abandoned flagship
projects suggests that caution is required. Most recently, the subsidiary of the Solena Group
with which British Airways held a contract filed for bankruptcy in November 2015. The
remainder of the Solena group remains committed to waste to biofuels projects, but activity
in the aviation biofuels space remains uncertain.47
Direct sugars to hydrocarbons (DSHC) – FRL 5-7
The direct sugars to hydrocarbons (DSHC) pathway describes technologies that produce
alkane-type fuels from sugars via anaerobic fermentation, without an alcohol intermediate.
This technology has the potential to use sugars derived from lignocellulosic biomass as
feedstock, but most current research is focussed on simple hexose sugars derived from
sugarcane, sweet sorghum, and maize, which are easier to ferment.54–57
DSHC development is being led by a joint venture between the companies Amyris and Total
(Table 4). Their proprietary Biofene® technology uses sugarcane-derived glucose to produce
the isoprenoid farnesene. This can then be used as the basis for a range of petroleum
replacement products. The first commercial plant in Brota, Brazil, has been operational
since December 2012 and has the capacity to produce up to 50 million litres of farnesene
per annum.42,48 Looking forwards, Amyris has identified the potential for significant
production cost reductions if a yeast strain capable of fermenting C5 sugars alongside C6
sugars can be developed.58 The company is working with the US National Advanced Biofuels
Consortium to extend its fermentation process to use complex lignocellulosic sugar
streams.59 It is anticipated that Amyris will transition from sugar crops to cellulosic wastes
and residues once this process becomes economically viable.60
Biofene® jet fuel has been certified for blends of up to 10% with petroleum-derived jet since
June 2014 (Annex A3 of ASTM D7566).61 Air France committed to use a 10% blend of the
fuel for a weekly scheduled flight between Paris and Toulouse between October 2014 and
September 2015.62,63 Amyris also has a memorandum of understanding to develop
renewable jet fuel with the airline GOL Linhas Aéreas Inteligentes, which has aimed to use
up to 10% RJF blends in its Boeing 737 fleet since July 2014.64,65
The company LS9 has had an operational DSHC pilot plant since 2008 and was formerly
targeting the production of RJF. However since being bought out by REG Life Sciences in
2014 its focus has shifted from biofuels to biochemicals.66,67 Similarly, Amyris is currently
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focusing on cosmetics, flavours , fragrances and performance materials rather than biofuels,
as their product generates more value in these market segments.68
Amyris’ Biofene® jet fuel is considered to have a FRL of 7 moving towards 8. It has achieved
ASTM certification, a fuel purchase memorandum of understanding has been signed with an
airline, and a first commercial plant capable of producing jet fuel is operational. The
publically available literature on DSHC fuels produced by other companies is insufficient to
assess their FRLs, but since none are pursuing ASTM certification FRL 5 is assumed as a
maximum.
Alcohol to jet (ATJ) – FRL 4-6
The alcohol to jet (ATJ) pathway covers a wide range of technologies producing jet fuel from
biomass via alcohol intermediates. The alcohols are converted to hydrocarbon fuel via a
process of dehydration, oligomerisation and hydrogenation. The individual technical
processes employed in the ATJ pathway are considered to be mature, being widely used in
commercial petrochemical applications.69 However complete feedstock-to-fuel process
chains for ATJ are at the pilot and demonstration stages of development. In general, the
technologies to synthesise alcohol intermediates are better developed than those to
convert the intermediates to jet fuel. The most advanced RJF ATJ research efforts are
targeting ethanol and butanol as intermediates.69–71
4.4.1 Alcohol synthesis
Bioethanol derived from sugar and starch is a fully mature technology that serves a large
commodity market: some 93 billion litres of bioethanol were produced globally in 2014.69,72
Conversion of lignocellulosic biomass to ethanol, however, is still in the process of becoming
established. Commercial-scale facilities are operational in the Europe, Brazil and the USA.
with the largest, POET’s ‘Project Liberty’ (commissioned 2014) targeting production of 25
million gallons per annum.73 Abengoa’s Hugoton facility had the same nameplate capacity as
Project Liberty, but was closed in late 2015, one year after being opened.74 Beta
Renewable’s Crescentino facility (the world’s first commercial-scale plant, opened 2013) is
operating without reported faults.75,76
Commercial production of biobutanol by the ‘acetone-butanol-ethanol’ (ABE) fermentation
process was widespread until the 1950s, when it was replaced by a cheaper process using
petroleum feedstocks.77 Interest in biobutanol has re-emerged in recent years due in part to
the superiority of its fuel characteristics compared with ethanol.69 Around eleven ABE
facilities were operational in China in 200978 and several companies are developing
alternative production methods, including retrofit solutions for existing ethanol facilities.13
The companies Butamax and Gevo have operational demonstration plants producing
butanol and isobutanol from sugar and starch feedstocks.79,80 Cobalt Technologies had been
planning to retrofit lignocellulosic butanol facilities at an ethanol refinery in Michigan and a
11
sugar mill in Brazil, but went into administration in 2015.81,82 Efforts to scale-up biobutanol
over the last five years have also been slower than industry expectations in the mid-2000s.13
Lignocellulosic butanol is expected to progress slowly until technologies for first-generation
butanol and lignocellulosic ethanol become more advanced.
Direct conversion of syngas (from lignocellulosic biomass or industrial gases) to alcohols is at
the demonstration stage of development.13,69 Three companies – LanzaTech, INEOS Bio and
Enerkem – have operational demonstration plants respectively producing alcohols from
steel mill waste gases, mixed organic materials and municipal solid waste (MSW).83–85 The
LanzaTech and INEOS Bio plants employ fermentation processes, whilst Enerkem produces
alcohols via catalytic synthesis.84,86,87 INEOS Bio’s plant is reported to have encountered
considerable teething problems, with production volumes falling far short of
expectations.88,89 Nevertheless, LanzaTech and Enerkem are developing plans for
commercial-scale facilities.74,88,90
4.4.2 Conversion to jet fuel
A key strength of the ATJ pathway is its flexibility to process alcohols synthesised by a wide
range of methods and from diverse feedstocks. Partnerships targeting the production of jet
fuel exist between companies that produce alcohols and those that convert alcohols to fuels
(Table 5), notably BioChemtex/Gevo, LanzaTech/Swedish Biofuels and, formerly, Cobalt
Technologies/Albemarle Corporation/NREL.91–93 In most cases, the jet fuel conversion
processes are at the laboratory and pilot stages of development. LanzaTech and Swedish
Biofuels are also evaluating possible locations for a demonstration plant capable of
producing 57 million litres of synthetic jet fuel per annum from industrial waste gases –
although not a biofuel this plant could produce enough to fuel Virgin’s Shanghai-London
route.94,95
Partnerships also exist between fuel developers and aviation operators (Table 5). LanzaTech
and Swedish Biofuels have fuel development agreements with Virgin Atlantic, the US
Ministry of Defence and the Swedish Defence Material Administration.93 Gevo is being
supported by Lufthansa and the US Air Force for fuel tests, while Alaska Airlines intends to
use 1,000 gallons of Gevo’s RJF for a demonstration flight in 2016.96–98 Byogy Renewables
and Avianca Brazil are working in partnership to accelerate ASTM approval of Byogy’s ATJ
fuel, which is hoped to be suitable as a 100% replacement for petroleum kerosene.99
ATJ synthetic paraffinic kerosene produced from starch and sugar feedstocks is currently
undergoing ASTM evaluation.4,100 Certification is expected during 2016, although opinion is
divided as to whether the fuel will be certified for use as a blended (<50%) or neat drop-in
fuel.55,69,101 A second fuel, synthetic kerosene with aromatics (again produced from starch
and sugar feedstocks), is expected to take longer to achieve certification, but may be
12
suitable for use in blends of up to 100%.55 The RJF developed by Cobalt Technologies had
passed the early stages of the US Navy’s fuel certification scheme.101
Overall ATJ approaches are considered to have FRLs ranging from 4 to 6. The lower end of
this represents fuels which are still undergoing laboratory-scale technical evaluation (e.g.
Zeachem), whilst the upper end corresponds to those which are being scaled-up to
demonstration stage and tested for certification purposes (e.g. Gevo, Swedish Biofuels).
Hydrotreated depolymerised cellulosic jet (HDCJ) – FRL 6
The hydrotreated depolymerised cellulosic jet (HDCJ) pathway represents a diverse range of
fuel conversion technologies including conversion routes based on pyrolysis, hydrothermal
liquefaction and hybrid processes. For liquefaction-based HDCJ, wet lignocellulosic biomass
is converted to a bio-oil with a low oxygen content, whilst for pyrolysis-based HDCJ, dry
lignocellulosic biomass is converted to a bio-oil with a high oxygen content. In both cases
this conversion is achieved via hydrothermal catalysis and the bio-oil is subsequently
upgraded using hydrogen.
Biomass pyrolysis has been deployed at pilot scale since the 1970s and at demonstration
scale since the 1990s, but interest in upgrading the bio-oils generated for transport fuel only
developed in the late 1990s.102–104 Considerable R&D efforts are underway to lower the cost
of the upgrading processes, both through improvements to hydrodeoxygenation methods
and the development of novel upgrading techniques.103–109 These new approaches are
mostly in the laboratory or pilot stages of development.
Recent years have seen the closure of several biomass fast pyrolysis pilot plants across
Europe and the cancellation of proposed projects due to weak market conditions.103,110
Organisations with operational pilot plants include Air Liquide, Metso and the Biomass
Technology Group (BTG).111–113 Both the Air Liquide and Metso plants are producing bio-oil
for use as a gasification feedstock, whilst the BTG plants are not aiming to produce
upgraded products at present. None of these companies are currently targeting jet fuel.
The company Licella is the leading the development of HDCJ RJF (Table 6). It has one pilot
and two demonstration-scale facilities operating its proprietary ‘catalytic hydrothermal
reactor’ (Cat-HTR) technology, and is developing plans for a commercial scale
facility.106,114,115 The fuel is undergoing testing against ASTM specifications.116 Licella has
memoranda of understanding to develop aviation fuels with Virgin Australia and Air New
Zealand, and Renewable Oil Corporation has a memorandum with Virgin Australia.114,117
Envergent Technologies, a joint venture between Honeywell UOP and Ensyn, has partnered
with Chevron to evaluate the production of transportation fuels by co-processing
Envergent’s bio-oil in existing refineries.118 KiOR (catalytic fast pyrolysis/fluid catalytic
cracking) was playing an important role until recently, operating a pilot plant and having
13
advanced its RJF to ASTM assessment, however the company was declared bankrupt in early
2015.119
Licella’s Cat-HTR RJF can be categorized as at FRL 6: it has been scaled from laboratory to
pilot stages, a demonstration plant is being developed, and ASTM testing is underway. The
publically available literature on HDCJ fuels being developed by other companies is
insufficient to assess their FRLs.
Aqueous phase reforming (APR) – FRL 6
Aqueous phase reforming (APR) is a catalytic process that converts soluble plant sugars into
a mixture of water, hydrogen and chemical intermediates (such as alcohols, ketones, acids,
furans, paraffins and other oxygenated hydrocarbons). These can in turn be converted to
fuels and high value chemicals.104,120,121
APR technologies to produce biofuels in general are considered to be at the R&D and pilot
stages of development.13,69 Virent is the sole organisation identified that has reached an
advanced stage of jet fuel development. The company has two demonstration facilities
(Table 7) with a combined annual production capacity of almost 60,000 litres of fuels and
chemicals.101,122 Its fuel is being tested against ASTM specifications.122
Virent’s APR fuel is considered to be at FRL level 6 since demonstration facilities have been
established and ASTM testing is underway.
5 Discussion and conclusions
FRL assessment
It is clear from the Fuel Readiness Level assessment that RJF technologies pursuing
international certification vary considerably in terms of their technological maturity and
development status (Figure 2). Three pathways have already been certified by the ASTM:
HEFA-jet, FT and DHSC. Of these the most highly developed is HEFA, which can be split
between two major RJF fuel products: HEFA-jet and HEFA-diesel. HEFA-jet is ASTM certified,
and has fuelled the majority of test and demonstration RJF flights conducted to date. It is
produced on a batch-basis by several commercial-scale facilities worldwide, and the first
commercial facility for continuous production is expected to become operational in 2016
(FRL 9). HEFA-diesel is currently undergoing ASTM evaluation for aviation (FRL 6), but
globally there are already numerous facilities producing HEFA-diesel for road transport on a
commercial basis. FT is moving towards early deployment of first commercial facilities (FRL
7-8), although widespread commercialisation seems unlikely in the current market
environment. DHSC (FRL 5-7) from sugarcane is being championed by Amyris and Total in
Brazil. Other fuel conversion pathways are in the demonstration and pilot phases (4-6), with
some being pursued by only one or two developers and thus more vulnerable to individual
companies experiencing difficulties.
14
Figure 2 Current fuel readiness levels of RJF conversion technologies.
The CAAFI FRL scale is valuable as a standardised measure for comparing and
communicating the current status of aviation fuels produced by alternative technologies.123
However it has some clear limitations: completion of the penultimate level (FRL 8 –
corresponding to certification) may be achieved without large volumes of fuel being
produced; the final level may be achieved with the operation of only one commercial-scale
plant; and no consideration is given to potential integration with existing fuel supply chains.
The FRL measure therefore provides a better indication of the quality of an aviation fuel
than it does an assessment of whether commercial production is viable or ongoing.
The scale also provides only limited insight regarding the potential rate of progress for RJFs
along the FRL scale. Arup URS and E4Tech13 have observed that biofuels in general have
taken between three and five years to progress by one technology readiness level whilst
R&D is ongoing. But progress for an individual technology will depend on the level of
investment and effort, not simply elapsed time. Three pathways (FT, HEFA, DSHC) have
achieved ASTM certification (FRL 7), taking between one to three years to complete the
process; others (ATJ, HDCJ, APR) have been working towards this for up to five years at the
time of writing.14,100 Commercial deployment (FRLs 8-9 and beyond) is heavily dependent on
the ease of securing investment, itself determined by market demand, the policy
environment, technology risk (partially measured by the FRL) and economic outlook. This is
exemplified by the contrast in uptake of the HEFA and FT pathways. Whilst FT-RJF from
lignocellulosic feedstocks completed ASTM certification (FRL 8) in 2009, it has yet to be
15
demonstrated commercially. HEFA-jet was not certified until 2011 but has overtaken FT-RJF
with several commercial facilities currently in operation (FRL 9).
Factors affecting future RJF deployment
The majority of RJF produced to date has been from vegetable oil feedstocks (HEFA
conversion pathway). Lignocellulosic feedstocks, however, are considered to have greater
potential for production of sustainable and financially competitive RJF in regions such as the
EU. Here developers are focussing on low-cost residues and waste streams. The
compositional complexity and variability of these resources, however, remains a significant
challenge, and robust and reliable waste-to-fuel conversion technologies have yet to be
demonstrated at scale. Bulky feedstocks are also expensive to collect and transport, limiting
the size (and potential scale economies) of centralised conversion facilities. Competition
within the waste management sector can also make it difficult to acquire these resources.
Despite the demonstrable (and growing) interest in RJF, both demand and production
volumes remain negligible compared to conventional fossil jet fuel. Production facilities
involve significant capital investment, with cost estimates for commercial-scale plants
starting in the region of US $100 million.16,124 Estimated levelised costs are typically more
than twice the selling-price of conventional petroleum kerosene, and in some cases (notably
for vegetable oils), the price of the raw feedstock is already greater than that of the
kerosene produced.16,124 The extent to which novel conversion technologies and
decentralised processing strategies can drive down costs remains to be seen, but the
economics of RJF production are likely to remain challenging. An additional deterrent is the
comparatively high market value of alternative bioproducts such as gasoline, diesel and
chemicals – with which RJF must compete for production capacity. Further, ASTM
certification itself requires investments to cover the expenses of lab, engine and aircraft
testing, as well as the production of significant amounts of test fuel. Whilst initial product
testing might require as little as 0.5 litre, extensive engine testing towards the end of the
certification process can require up to 650 tonnes (225,00 US gallons) of fuel.125 Ongoing
research†† for the RENJET project highlights the difficulties this fuel requirement presents
for RJF developers.126 The need to secure investment for production scale-up and to
achieve ASTM certification in parallel creates a ‘Catch 22’ situation: certification is required
to assure investors of the value of larger-scale production facilities, but scaled production is
also necessary to conduct ASTM certification tests.126
These issues are exacerbated by the uneven renewable energy policy landscape in regions
such as the USA and the EU, with only limited support being available to aviation biofuels.
Aviation stakeholders perceive the lack of international market-pull policy to hinder the
establishment of stable market demand, in turn discouraging investors and preventing RJF
†† The study combines empirical evidence from stakeholder interviews with innovation systems approaches.126
16
developers from scaling-up RJF production.126 Furthermore, it is not currently possible to
incentivise the consumption of RJF through tax derogations since petroleum jet fuel is not
taxed – unlike road transport fuels. There are numerous examples of partnerships between
biofuel developers and airlines, with over twenty commercial, demonstration and pilot
facilities to produce RJF are operational or under development worldwide. Given the high
cost of both RJF production (compared to petroleum kerosene) and ASTM certification, it is
unlikely that the industry will bear the risks of developing new fuels for commercial aviation
or large-scale RJF facilities independently. Development of a supportive policy environment
is likely to be critical to the successful development and deployment of RJF
technologies.42,126–129
6 Acknowledgements This research has been conducted as a first-stage assessment of opportunities to develop
sustainable European RJF supply chains in the context of the Fuel Supply Chain Development
and Flight Operations (RENJET) project‡‡, funded by the EIT Climate-KIC. The project aims to
lay the basis for a self-sustaining network of regional renewable jet fuel supply chains based
on sustainable European feedstock sources.
We gratefully acknowledge the support of the RENJET consortium members: Imperial
College London, University of Utrecht, SkyNRG, KLM and Schiphol Airport.
7 Bibiographies
Rebecca Mawhood
Becky Mawhood is a Research Associate at the Centre for
Environmental Policy, Imperial College London. Her research
focuses on bioenergy system transitions, with case studies on
aviation biofuels and energy crops. She is also involved with
projects looking at rural energy services in Sub-Saharan
Africa. Becky has an MSc in Environmental Technology from
Imperial College London.
‡‡ http://www.climate-kic.org/projects/renewable-jet-fuel-supply-chain-development-and-flight-operations/
17
Evangelos Gazis
Dr Evangelos Gazis is a researcher at the Centre for
Environmental Policy, Imperial College London. He is an
electrical engineer with a background on socio-economic
analysis and life-cycle assessment of sustainable energy
technologies. His current research focuses on innovation
dynamics within the aviation biofuels sector
Sierk de Jong
Sierk de Jong is a Junior Researcher assigned to the RENJET
project at the Copernicus Institute (Utrecht University) and a
Business Analyst at SkyNRG. His research focuses on
assessing the current and future techno-economic and
environmental performance of biojet fuel supply chains. He
holds an MSc from Utrecht University in Energy Science.
Ric Hoefnagels
Dr Ric Hoefnagels is a researcher at the Copernicus Institute,
Utrecht University. He is involved in many projects related to
bioenergy, biomass trade and logistics. Furthermore, he has
experience with greenhouse gas balances of biofuels,
technological learning and CO2 capture and storage.
Raphael Slade
Dr Raphael Slade is Lecturer in Environmental Sustainability
at Imperial College London. His research focusses on the
techno-economic evaluation of low carbon energy systems,
resource availability and bioenergy.
18
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24
Available at: http://www.prnewswire.com/news-releases/avianca-brasil-and-byogy-renewables-forge-initiative-to-drive-the-global-approval-of-alcohol-to-jet-atj-renewable-jet-fuel-256265611.html(2014) [April 20 2015].
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121. Tompsett GA, Li N and Huber GW, Catalytic Conversion of Sugars to Fuels. [Online]. Available at: http://dx.doi.org/10.1002/9781119990840.ch8Thermochemical Processing of Biomass [Internet] John Wiley & Sons, Ltd p. 232–279(2011).
122. Virent, VIRENT DELIVERS PLANT-BASED JET FUEL TO U.S. AIR FORCE RESEARCH LABORATORY FOR TESTING. [Online]. Available at: http://www.virent.com/news/virent-delivers-plant-based-jet-fuel-to-u-s-air-force-research-laboratory-for-testing/(2013).
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Commercialization of Aviation Biofuels in Europe. Int J Sustain Transp 9(8):542–550 (2015).
129. IATA, . 1st ed., Sustainable Aviation Fuel Roadmap. International Air Transport Association, Montreal, Canada & Geneva, Switzerland (2015).
130. ARA, ARA and Blue Sun Partner to Commercialize 100% Drop-in Renewable Jet and Diesel Fuel. (2013).
131. Sherbacow B, Paramount, CA GreenJet Refinery. [Online]. Available at: http://www.smgov.net/uploadedFiles/Departments/Airport/Sustainability/20150126_AltAir_Presentation.pdf (2015).
26
132. Biofuels Digest, UOP’s Ecofining tech linked to massive renewable diesel project in Ohio. (2014).
133. Clark D, Fossil fuel subsidies: a tour of the data. [Online]. Available at: http://www.guardian.co.uk/environment/datablog/2012/jan/18/fossil-fuel-subsidyEnviron Energy | Guard [Internet] Guardian News and Media Limited or its affiliated companies. All rights reserved. (Journal Article) (2012).
134. Sinopec, SINOPEC Bio-jet Fuel Technology. (2012). 135. Sinopec, 2013 Corporate social responsibility report. (2014). 136. Viguie J, Ullrich N, Porot P, Bournay L, Hecquet M and Rousseau J, BioTfueL Project:
Targeting the Development of Second-Generation Biodiesel and Biojet Fuels. Oil Gas Sci Technol 68(5):935–946 (2013).
137. Culverwell W, Lakeview’s $200M biofuel project gets a public airing, 24 February 2015. [Online]. Available at: http://www.bizjournals.com/portland/blog/sbo/2015/02/lakeviews-200m-biofuel-project-gets-a-public.htmlPortland Business Journal. (2015) [May 28 2015].
138. Southwest Airlines, Southwest Airlines Announces Purchase Agreement With Red Rock Biofuels, 24 September 2014. [Online]. Available at: http://www.swamedia.com/releases/southwest-airlines-announces-purchase-agreement-with-red-rock-biofuels?l=en-US(2014) [May 28 2015].
139. Biofuels Digest, That was then, this is now: 10 Signature biofuels projects for 2015-16, and where they are, 18 October 2015. [Online]. Available at: http://www.biofuelsdigest.com/bdigest/2015/10/18/that-was-then-this-is-now-10-signature-biofuels-projects-for-2015-16-and-where-they-are/(2015) [December 17 2015].
140. Amyris, Amyris Ships First Truckload of Biofene From Its New Plant in Brazil, 1 February 2013. [Online]. Available at: https://amyris.com/amyris-ships-first-truckload-of-biofene-from-its-new-plant-in-brazil/(2013) [May 28 2015].
141. Amyris, Amyris Secures Additional Financing and Announces Start of Biofene® Production at Its Paraiso Facility in Brazil - 27 December 2012. [Online]. Available at: https://amyris.com/amyris-secures-additional-financing-and-announces-start-of-biofene-production-at-its-paraiso-facility-in-brazil/(2012) [May 28 2015].
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143. GreenAir Online, Brazil’s Avianca to back Byogy’s alcohol conversion technology as a future source of renewable jet fuel, 14 October 2013. [Online]. Available at: http://www.greenaironline.com/news.php?viewStory=1767(2013) [May 28 2015].
144. Byogy Renewables, Executive Summary, April 2013. (2013). 145. Werner D, Fly clean now with biofuels. Aerospace America (October) (2014). 146. Lane I, Gevo announces shrinking net loss for Q4 2014, 30 March 2015. [Online].
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147. Gevo, Gevo Sells Renewable Jet Fuel to NASA, 9 March 2015. [Online]. Available at: http://ir.gevo.com/mobile.view?c=238618&v=203&d=1&id=2023808(2015) [May 28 2015].
148. Craig H, Jennifer Holmgren explains the LanzaTech biofuel breakthrough. [Online]. Available at: http://www.virgin.com/unite/business-innovation/jennifer-holmgren-
27
explains-lanzatech-biofuel-breakthroughVirgin.com. (2015) [May 28 2015]. 149. Garthwaite J, Second Try: LanzaTech Graps Failed Biofuel Refinery in Georgia Pine, 20
January 2012. [Online]. Available at: http://news.nationalgeographic.com/news/energy/2012/01/12019-range-lanzatech-cellulosic-biofuel-ethanol/National Geographic. (2012) [May 28 2015].
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151. Environmental Leader, Virgin, LanzaTech Low-Carbon Jet Fuel Earns Sustainability Certification, 20 November 2013. [Online]. Available at: http://www.environmentalleader.com/2013/11/20/virgin-lanzatech-low-carbon-jet-fuel-earns-sustainability-certification/Environmental Leader. (2013) [May 28 2015].
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153. NordicGreen, Swedish Biofuels awarded bio jet fuel contract by the Swedish defence, 20 April 2011. [Online]. Available at: http://www.nordicgreen.net/startups/article/swedish-biofuels-awarded-bio-jet-fuel-contract-swedish-defence(2011) [May 28 2015].
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28
9 Tables Table 1 The CAAFI Fuel Readiness Level (FRL) scale and toll gates.14
LEVEL FRL DESCRIPTION FRL ‘TOLL GATE’ TECH
NO
LOG
ICA
L R&
D
1 Basic principles Feedstock & process basic principles
identified
2 Technology concept
formulated
Feedstock & complete process identified
3 Proof of concept Lab scale fuel sample produced from
realistic feedstock.
Energy balance analysis conducted for
initial environmental assessment.
Basic fuel properties validated
4 Preliminary technical
evaluation
System performance and integration
studies
Specification properties evaluated
5 Process validation Scaling from laboratory to pilot plant CER
TIFICA
TION
PR
OC
ESSES
6 Full-scale technical
evaluation
ASTM certification tests conducted: fit-for-
purpose properties evaluated, turbine hot
section testing, components and testing
7 Certification / fuel
approval
Fuel listed in international standards
CO
MM
ERC
IAL D
EPLO
YM
ENT
8 Commercialisation Business model validated for production
Airline purchase agreements secured
Plant-specific independent greenhouse gas
assessment conducted in line with
internationally-accepted methodology.
9 Production
capability
established
Full scale plant operational
29
Table 2: Planned and operational HEFA production facilities.8
COMPANY,
PROJECT &
REFERENCES
PROJECT TYPE,
LOCATION, RJF
TECHNOLOGY
BIOFUEL
CAPACITY
RJF
CAPACITY
FEEDSTOCK START-UP
DATE /
STATUS
AIRLINE INVOLVEMENT NOTES
ARA & BLUE SUN
ENERGY
HTTP://WWW.GO
BLUESUN.COM/ 22,40,41,130
Demonstration
St. Joseph, USA
Catalytic
hydrothermolysis
4,200
gal/day
(15,900
l/day)
Has RJF
capacity
Waste oils
and fats
Start-up
2014.
First fuel
deliveries
to US Navy
in 2015.
Contract signed with US Defense
Logistics Agency Energy to produce
100% drop-in diesel & RJF for US Navy.
Modification of existing
plant.
HONEYWELL UOP
HTTP://WWW.UO
P.COM/ 22,23
Demonstration
Texas, USA
HEFA-jet
250 barrels
per stream
day
(40,000
litres per
stream
day)
Has RJF
capacity
2008 Honeywell UOP’s Green Jet FuelTM has
fuelled 200 GOL commercial flights
during the 2014 FIFA world cup and 52
scheduled flights between Mexico City &
Costa Rica by Aeroméxico in 2011. Other
airlines to have used the fuel
commercially include LATAM Airlines
Group, NASA, Porter Airlines, United
Airlines, Air China, Iberia, Interjet,
Boeing, Honeywell USA TAM, KLM,
Japan Airlines, Continental Airlines, Air
New Zealand.
US Air Force, US Navy & Royal
Netherlands Air Force have used Green
Jet FuelTM for test & demonstration
flights.
8 The following currency conversion rates have been applied throughout this paper: 1 GBP = 1.67255 USD; 1 EUR = 1.38105 USD; 1 AUS = 0.903157 USD; 1 SEK = 0.117501 USD.
30
COMPANY,
PROJECT &
REFERENCES
PROJECT TYPE,
LOCATION, RJF
TECHNOLOGY
BIOFUEL
CAPACITY
RJF
CAPACITY
FEEDSTOCK START-UP
DATE /
STATUS
AIRLINE INVOLVEMENT NOTES
HONEYWELL UOP
& ALTAIR FUELS
HTTP://ALTAIRFUE
LS.COM/ 24,131
Commercial
Paramount,
California, USA
HEFA-jet
40 M
gal/yr (151
M l/yr)
initially,
with
potential
increase to
72 M
gal/yr (273
M l/yr)
Has RJF
capacity.
Inedible
natural oils,
agricultural
waste oils
Expected
2016
Offtake signed with United Airlines (15
M gal over 3 years for flights departing
LAX) & World Fuel Services
Received US $5 M grant
from California Energy
Commission.
HONEYWELL UOP
& ENI
THE ENI VENICE
BIOREFINERY
HTTP://WWW.ENI.
COM/ 19–21
Commercial
Venice, Italy
HEFA-jet
300,000
t/yr diesel
initially,
with
potential
to increase
to 500,000
t/yr
Interest in
producing
RJF
Initially palm
oil, moving
towards
waste oils &
fats
2014 Modification of existing
hydrotreatment plant.
HONEYWELL UOP
& PETRIXO
HTTP://WWW.PET
RIXO.COM/ 25,34
Commercial
Fujairah, United
Arab Emirates
HEFA-jet
150 M
gal/yr (568
M l/yr) jet
& diesel
Interest in
producing
RJF
500,000 t/yr In design Biorefinery to have
total capacity of 1 M
t/yr provided by UOP &
a second company (to
be confirmed). Petrixo
to invest US $800 M.
HONEYWELL UOP
& SG PRESTON
HTTP://SGPRESTO
N.COM/ 26,34,132
Commercial
South Point,
Lawrence County,
Ohio, USA
HEFA-jet
120 M
gal/yr (454
M l/yr)
diesel & jet
Interest in
producing
RJF
Waste fats,
oils and
greases;
distiller’s
corn oil
Expected
2017
Investment $400 M
31
COMPANY,
PROJECT &
REFERENCES
PROJECT TYPE,
LOCATION, RJF
TECHNOLOGY
BIOFUEL
CAPACITY
RJF
CAPACITY
FEEDSTOCK START-UP
DATE /
STATUS
AIRLINE INVOLVEMENT NOTES
Commercial
Van Wert, Ohio,
USA
HEFA-jet
120 M
gal/yr (454
M l/yr)
diesel & jet
Interest in
producing
RJF
Waste fats,
oils and
greases;
distiller’s
corn oil
Expected
by 2020
Commercial
Logansport,
Indiana, USA
HEFA-jet
120 M
gal/yr (454
M l/yr)
diesel & jet
Interest in
producing
RJF
Commercial
Michigan, Canada
HEFA-jet
120 M
gal/yr (454
M l/yr)
diesel & jet
Interest in
producing
RJF
Commercial
Ontario, Canada
HEFA-jet
120 M
gal/yr (454
M l/yr)
diesel & jet
Interest in
producing
RJF
NESTE
WWW.NESTE.COM 27,30–32,42,133
Commercial
Rotterdam, The
Netherlands
HEFA-jet
800,000
t/yr diesel
Interest in
producing
RJF
Crude palm
oil, waste
oils and fats
2011 Joined BioPort Holland for Aviation
Biofuel initiative in 2013, partnering with
Dutch government, KLM, Schiphol
Airport, SkyNRG & Port of Rotterdam to
scale up RJF production at Rotterdam
refinery.
Partner in EU ITAKA project since 2012.
Intention to produce 1.4 M litres of RJF
for project over 2015-16. Provides fuel
for world’s first mixed supply of RJF and
petroleum kerosene in conventional
hydrant system at Oslo Airport.
Commercial
Singapore
800,000
t/yr diesel
Has RJF
capacity.
2010
Commercial
Porvoo, Finland
HEFA-jet
380,000
t/yr jet &
diesel
15,000 t/yr
2007
32
COMPANY,
PROJECT &
REFERENCES
PROJECT TYPE,
LOCATION, RJF
TECHNOLOGY
BIOFUEL
CAPACITY
RJF
CAPACITY
FEEDSTOCK START-UP
DATE /
STATUS
AIRLINE INVOLVEMENT NOTES
RJF used by Lufthansa for 1,187
scheduled flights in 2011 (Hamburg-
Frankfurt) & one transatlantic flight
(Frankfurt-Washington DC) in 2012.
Supplies RJF to Finnish Air Force.
HEFA-diesel tested by Boeing in 2014.
Boeing and Nest working towards ASTM
approval of high-freeze point fuel.
PERTAMINA
HTTP://WWW.PER
TAMINA.COM/ 29
Commercial
Indonesia
Interest in
producing
RJF
<26 M l/yr Palm oil Expected
2018
Expected feasibility
study completion early
2016. Estimated plant
cost US$450-480 M.
SINOPEC
SINOPEC ZHENHAI
REFINING &
CHEMICAL
COMPANY
HTTP://WWW.SIN
OPECGROUP.COM/ 34,134,135
Demonstration
Zhenhai, China
18,000 t/yr
jet
Has RJF
capacity.
Palm oil,
used
cooking oil
2011 Partnered with Hainan Airlines and
Boeing for China’s first commercial RJF
flight from Beijing to Shanghai in 2015.
33
Table 3: Planned and operational FT production facilities.
COMPANY,
PROJECT &
REFERENCES
PROJECT TYPE
& LOCATION
BIOFUEL
CAPACITY
RJF
CAPACITY
FEEDSTOCK START-UP
DATE /
STATUS
AIRLINE INVOLVEMENT NOTES
BIOTFUEL
PROJECT
http://www.t
otal.com 42,46,48,136
Pretreatment
(torrefaction):
Demonstration
Sofiprotéol,
Venette,
France.
Gasification,
purification &
synthesis
Demonstration
Total refinery,
Dunkirk, France.
200,000
t/yr by
2020
diesel and
jet
Interest in
producing
RJF
Torrefied
biomass,
coal, crude
oil
Test phase
planned
2017,
commercial
production
2020
Partnership between : Axens, CEA, IFP
Energies Nouvelles, Sofiprotéol,
ThyssenKrupp Industrial Solutions and
Total.
Estimated cost €180 M (US $249 M). €33 M
(US $44 M) subsidy from French
government.
FULCRUM
BIOENERGY,
SIERRA
BIOFUELS
PLANT
http://fulcru
m-
bioenergy.co
m/ 9,51,52,137
Commercial
McCarran,
Nevada, USA
10 M
gal/yr (38
M l/yr) jet
& diesel
Interest in
producing
RJF
MSW
(200,000
t/yr)
Expected
2017
Offtake agreement for
Fulcrum’s first 5 biofuel
plants signed with Cathay
Pacific Airways.
United bought a US $30
million stake in Fulcrum
Energy in 2015 and agreed
to contemplate the joint
development of five plant.
.
Estimated cost US $266 M.
US $70 million grant from US Department
of Defense (2014) and US $105 M loan
guarantee backed by US Department of
Agriculture (2015).
Plans for 5 more plants across North
America under development.
Large zero-cost MSW supply secured.
Gasification technology provided by
Thermochem Recovery International.
34
COMPANY,
PROJECT &
REFERENCES
PROJECT TYPE
& LOCATION
BIOFUEL
CAPACITY
RJF
CAPACITY
FEEDSTOCK START-UP
DATE /
STATUS
AIRLINE INVOLVEMENT NOTES
RED ROCK
BIOFUELS
http://www.r
edrockbio.co
m/ 50,53,137–139
Demonstration
Lakeville,
Oregon, USA
12 M
gal/yr (45
M l/yr) jet,
diesel &
naphtha
Interest in
producing
RJF
Forestry and
sawmill
residues
(140,000
t/yr)
Expected
2017
Supply agreements with:
US Navy; Southwest
Airlines, 3 M gal/yr (11 M
L/yr); FedEx Express, 3 M
gal/yr (11 M l/yr) from
2017 to 2024.
Estimated cost US $182 M.
Received US $70 M grant from US
Departments of Agriculture and Energy &
US Navy in 2014.
35
Table 4: Planned and operational Direct Sugars to Hydrocarbons (DSHC) production facilities.
COMPANY, PROJECT &
REFERENCES
PROJECT TYPE
& LOCATION
BIOFUEL
CAPACITY
RJF
CAPACITY
FEEDSTOCK START-UP DATE /
STATUS
AIRLINE
INVOLVEMENT
NOTES
AMYRIS & TOTAL
HTTPS://AMYRIS.COM/ 104,140–142
Commercial
Brotas, São
Paulo, Brazil
40,000 t/yr
biofuels
Has RJF
capacity
Sugarcane,
molasses.
First commercial
shipment of farnesene
– Feb 2013.
Partnerships with
Airbus, Safran and Air
France.
Facility certified by the
Roundtable on
Sustainable
Biomaterials.
36
Table 5: Planned and operational alcohol to jet (ATJ) facilities.
COMPANY, PROJECT &
REFERENCES
PROJECT TYPE,
LOCATION &
INTERMEDIATE
BIOFUEL
CAPACITY
RJF
CAPACITY
FEEDSTOCK START-UP
DATE /
STATUS
AIRLINE INVOLVEMENT NOTES
BYOGY
HTTP://WWW.BYOGY.C
OM/ 99,143–145
Pilot
Bryan, Texas,
USA
Ethanol
Has RJF
capacity
Agave,
sugarcane,
corn, sweet
sorghum,
cassava,
sugar beet.
Operation
al
Partnership with BA through
CLEEN programme.
Agreement signed with Avianca
Brazil to accelerate ASTM
certification.
Offtake agreement with Qatar
Airways.
Partnerships with the FAA,
Rolls Royce, BA and Pratt &
Whitney through the
CLEEN programme. Testing
programme has supported
ASTM assessment.
GEVO
HTTP://WWW.GEVO.CO
M/ 4,6,69,76,79,96,97,101,146,147
Alcohol
synthesis:
Commercial
Luverne,
Minnesota, USA
Biorefinery:
Demonstration
Silsbee, Texas
Isobutanol
83.28 M l/yr
bioethanol;
68.14 M l/yr
isobutanol
Has RJF
capacity
Sugary
feedstocks
(maize,
grains, sugar
cane)
Co-
production
of ethanol
&
isobutanol
began
June 2014.
Some jet
fuel has
been
produced.
Supply agreements signed with
Alaska Airlines and United
Airlines. Alaska Airlines plans to
fly first commercial ATJ flight in
2016.
Fuel testing agreement with
Lufthansa, supported by EC.
US Air Force has completed test
flights with 50% blend.
US Navy completed first
supersonic ATJ flight using fuel
in Dec 2014.
Coproduction
ethanol/isobutanol plant
developed as retrofit to
existing ethanol plant.
LANZATECH / BEIJING
SHOUGANG,
LANZATECH NEW
ENERGY TECHNOLOGY
COMPANY
WWW.LANZATECH.COM
Demonstration
Shougang Steel
Mill, Beijing,
China
Ethanol
300 t/yr
ethanol
Has RJF
capacity
Steel flue
gas
2013 Partnership signed in 2011 with
Virgin Atlantic, Boeing and
Swedish Biofuels to produce 15
M gallons/yr (57 M l/yr) of RJF,
sufficient to fuel Virgin’s
Shanghai-London route. HSBC
Beijing Shougang plant is
first RJF production facility
to be certified by the
Roundtable on Sustainable
Biomaterials.
37
COMPANY, PROJECT &
REFERENCES
PROJECT TYPE,
LOCATION &
INTERMEDIATE
BIOFUEL
CAPACITY
RJF
CAPACITY
FEEDSTOCK START-UP
DATE /
STATUS
AIRLINE INVOLVEMENT NOTES
46,85,86,94,95,101,148–152 and GE are also partners in this
venture.
Lanzatech has plans for 2
commercial plants to start-
up in 2016 producing 10-30
million gallons/yr (38-113
M l/yr) ethanol.
LANZATECH, BLUE
SCOPE STEEL MILL
WWW.LANZATECH.COM 46,85,86,94,95,101,148–152
Pilot
Blue Scope Steel
Mill, Glenbrook,
New Zealand
15,000
gal/yr
(57,000 l/yr)
ethanol
Steel flue
gas
2008
LANZATECH BAOSTEEL
NEW ENERGY COMPANY
WWW.LANZATECH.COM 46,85,86,94,95,101,148–152
Demonstration
Baosteel Steel
Mill, Shanghai,
China
300 t/yr
(ethanol)
Steel flue
gas
2013
LANZATECH / WBT
WWW.LANZATECH.COM 46,85,86,94,95,101,148–152
Demonstration
Taiwan
0.1 t/day
ethanol
Steel flue
gas
2014
LANZATECH, FREEDOM
PINES BIOREFINERY
WWW.LANZATECH.COM 46,85,86,94,95,101,148–152
Pilot
Soperton,
Georgia USA
250 l/day
ethanol &
chemicals
Wood
residues
(125 ton/day
dry wood)
2014
SWEDISH BIOFUELS,
‘PRODUCTION OF FULLY
SYNTHETIC PARAFFINIC
JET FUEL FROM WOOD
AND OTHER BIOMASS’
HTTP://WWW.SWEDISH
BIOFUELS.SE/ 4,46,69,93,153,154
Demonstration
Ethanol
<10,000 t/yr
jet, diesel &
gasoline
5,000 t/yr MSW,
biogas, grain
crops,
agricultural
& forestry
residues
Project
completio
n expected
2019
Lufthansa is a project partner.
EC FP7 project with
Abengoa Bioenergy,
Lufthansa, SkyNRG, SCA
Energy E4Tech, Remeski
Keskus, Institute for
European Studies.
Total cost €56M (US $74
38
COMPANY, PROJECT &
REFERENCES
PROJECT TYPE,
LOCATION &
INTERMEDIATE
BIOFUEL
CAPACITY
RJF
CAPACITY
FEEDSTOCK START-UP
DATE /
STATUS
AIRLINE INVOLVEMENT NOTES
M), with €28 M (US $37 M)
from EU FP7.
SWEDISH BIOFUELS
HTTP://WWW.SWEDISH
BIOFUELS.SE/ 4,46,69,93,153,154
Pilot
Stockholm,
Sweden
10 t/yr jet,
gasoline &
diesel
4.8t/yr Started
2013
Supply agreement with Swedish
Defence Materiel
Administration for fighter jet
fuel.
39
Table 6: Planned and operational HDCJ production facilities.
COMPANY,
PROJECT &
REFERENCES
PROJECT TYPE
& LOCATION
BIOFUEL
CAPACITY
RJF
CAPACITY
FEEDSTOCK START-
UP DATE
/ STATUS
AIRLINE
INVOLVEMENT
NOTES
LICELLA
HTTP://WW
W.LICELLA.C
OM.AU/ 101,114,155–157
Pilot
Somersby, New
South Wales,
Australia
2008 Memoranda of
understanding
with Virgin
Airlines & Air
New Zealand to
develop RJF.
Interested in conversion of pulp & paper plants. Plant are being designed at a scale to process similar quantities of feedstock as paper mills. Partnership with Norske Skog, which operates two paper mills in Australia.
Demonstration cost: AU$10 M (US $9 M), with AU$4.6 M (US $4.2 M) from Australian Government.
Pre-commercial estimated cost AU$114 M (US $103 M). AU$5.4 M (US $4.9 M) grant from Australian Government for feasibility study (2013).
Demonstration
Somersby, New
South Wales,
Australia
350 t/yr
bio-oil
Radiata pine sawdust,
lignocellulosic bioenergy
crops, banna grass, algae
(Initially 1,000 oven dry
tonne/yr, expanded to
10,000 oven dry
tonne/yr)
2011
Demonstration 20 M l/yr
bio-crude
50,000 oven dry tonne
/yr
In design
40
Table 7: Planned and operational APR production facilities.
COMPANY,
PROJECT &
REFERENCES
PROJECT TYPE &
LOCATION
BIOFUEL
CAPACITY
RJF
CAPACITY
FEEDSTOCK START-
UP DATE
/ STATUS
AIRLINE
INVOLVEMENT
NOTES
VIRENT
HTTP://WW
W.VIRENT.C
OM/ 79,101,122,158,159
Demonstration
Madison,
Wisconsin, USA
5,000 gal/yr
(19,000 l/yr)
jet & diesel
Has RJF
capacity
Various
cellulosic and
starch/sugar
feedstocks incl.
corn stover
Jan 2013 Corporate partners include Royal Dutch Shell, Coca-
Cola, Cargill, Honda, Renmatix.
Project to convert corn stover to jet fuel funded by
US $1.5M grant from FAA and US Dept. of Transport
in 2011.