Energy 35 (2010) 2059e2069
Contents lists available at ScienceDirect
Energy
journal homepage: www.elsevier.com/locate/energy
Theoretical efficiency limits for energy conversion devices
Jonathan M. Cullen*, Julian M. Allwood
Department of Engineering, University of Cambridge, Cambridge CB2 1PZ, UK
a r t i c l e i n f o
a b s t r a c t
Article history:
Received 14 July 2009
Received in revised form
6 January 2010
Accepted 19 January 2010
Available online 5 March 2010
Using energy more efficiently is a key strategy for reducing global carbon dioxide emissions. Due to
limitations on time and resources, actions must be focused on the efficiency measures which will deliver
the largest gains. Current surveys of energy efficiency measures assess only known technology options
developed in response to current economic and technical drivers. However, this ignores opportunities to
deliver long-term efficiency gains from yet to be discovered options. In response, this paper aims to
calculate the absolute potential for reducing energy demand by improving efficiency, by finding the efficiency limits for individual conversion devices and overlaying these onto the global network of energy
flow. The potential efficiency gains for each conversion device are found by contrasting current energy
demand with theoretical minimum energy requirements. Further insight is gained by categorising
conversion losses according to the underlying loss mechanisms. The result estimates the overall efficiency
of global energy conversion to be only 11 per cent; global demand for energy could be reduced by almost 90
per cent if all energy conversion devices were operated at their theoretical maximum efficiency.
Ó 2010 Elsevier Ltd. All rights reserved.
Keywords:
Energy efficiency
Sankey diagram
Prioritisation
Exergy analysis
Conversion loss
1. Introduction: the efficient use of energy
The reasons for using energy more efficiently are clear: to relieve
pressure on scarce energy resources, to reduce energy costs by
avoiding wastefulness, and perhaps most pressing, to reduce energy
related carbon dioxide (CO2) emissions which contribute to climate
change. The well-known Kaya identity [1] expresses the generation
of energy-based CO2 emissions as the product of four drivers: population, per capita wealth, energy intensity (energy per unit wealth)
and carbon intensity (CO2 per unit energy). The first two drivers are
socio-economic and are difficult to limit in practice. The third and
fourth drivers are technical options which require energy to be used
more efficiently (which lowers energy intensity) and the decarbonisation of energy supplies (which reduces carbon intensity).
To date, emission reduction strategies have focused primarily on
energy supply options: renewable energy technologies, nuclear
power, carbon capture and storage (CCS) and fuel switching. Yet, the
International Energy Agency (IEA) asserts that ‘energy efficiency
improvements . represent the largest and least costly savings’ [[2],
p. 4] available. There is further need to develop energy efficient
technologies and understand the scope of efficiency measures to
reduce CO2 emissions.
* Corresponding author. Tel.: þ44 1223 760360; fax: þ44 1223 332662.
E-mail address: jmc99@cam.ac.uk (J.M. Cullen).
URL: http://www.lcmp.eng.cam.ac.uk
0360-5442/$ e see front matter Ó 2010 Elsevier Ltd. All rights reserved.
doi:10.1016/j.energy.2010.01.024
In the 1975 conference Efficient use of energy, Ford et al. [3] stated
that the primary objective of any technical energy study is to define
a target ‘standard of performance’ against which current demand
for energy can be compared. Such a target may be chosen from
several options, for example, current best practice, the extrapolation
of an historical trend, or the projected gains from a specific design
innovation. The difference between today's energy demand and this
target provides a measure of the improvement potential, or possible
energy savings from energy efficiency measures.
Finding the global improvement potential from energy efficiency requires tracing the scale of energy flow through technical
devices in the energy network, and assessing the efficiency gains
available in each device. Equation (1) is used to calculate these
potential savings from efficiency, in conversion devices:
Target
Scale of
Potential for
¼
efficiency
savingenergy energyflow
Current
efficiency
(1)
where the energy terms are measured in joules (J) and the efficiency terms in percentages (%).
Assessing the scale of energy flow through the global energy
network is the subject of a previous article by Cullen and Allwood
[4]. Their research traces energy flow from fuel to final service,
including the technical steps of fuel transformation, electricity
generation, and end-use conversion, as shown in Fig. 1. The results
are presented visually in Sankey diagram form, permitting identification of the technical areas with the largest energy flows.
Particular attention is given to the technical components, rather
2060
J.M. Cullen, J.M. Allwood / Energy 35 (2010) 2059e2069
Fig. 2. Diagram of the potential gains from energy efficiency.
Fig. 1. The flow-path of energy.
than economic sectors, within each chain of energy. The same
technical categories are used in this paper to analyse potential
efficiency gains.
Cullen and Allwood make a novel distinction between ‘conversion devices’ (e.g. power stations, engines, and light bulbs) which
upgrade energy into more useful forms, and ‘passive systems’ (e.g.
houses, vehicles) where useful energy is finally ‘lost’ (referring to
a loss of energy quality, or usefulness) as low-grade heat to the
environment, in exchange for final services (e.g. transport, sustenance or thermal comfort). This becomes important when calculating efficiency targets, because in passive systems no conversion
of energy takes place and therefore no meaningful theoretical
efficiency target can be calculated. For example, a perfectly insulated building requires no heat input to maintain thermal comfort,
giving an infinite efficiency limit for the heated space, which is
nonsensical. Thus it is possible to set theoretical efficiency targets
for conversion devices but not passive systems. The efficiency limits
of passive systems depend instead on practical engineering design
constraints and will be examined in future work.
The current analysis aims to determine the efficiency terms
from Equation (1) for conversion devices, and to overlay these onto
the global map of energy flow. This will enable energy researchers
and policy makers to:
compare the efficiencies of energy conversion devices on an
equivalent basis;
determine which conversion devices have the greatest theoretical potential for reducing energy use and therefore CO2
emissions;
categorise avoidable losses according to the mechanisms
which lead to the loss of energy quality.
2. Previous work: the limits of energy efficiency
Estimates in the literature of possible energy savings from efficiency measures vary greatly depending on what target efficiency is
chosen. For example, if the target efficiency is constrained by
market forces an economic potential is defined, whereas a technical
potential takes into account practical efficiency limitations, and
a theoretical potential is based on thermodynamic efficiency limits.
Fig. 2 summarises these approaches for calculating possible energy
savings, and demonstrates with indicative values, how varied these
estimates can be (adapted from Dyer et al. [5], p. 4437).
Selecting a suitable target efficiency that is both objective and
technically defensible is essential if the full potential for efficiency
gains is to be gauged. Basing long-term targets on economic
potentialsdby tracking historic efficiency indicators or surveying
known technologiesdis risky because future economic drivers are
difficult to forecast over long time periods. Economic drivers can
vary and are in part pre-determined by governmental policies,
whereas the technical and theoretical efficiency limits of energy
devices do not change with time. To follow is a critical discussion of
the current models used for predicting future efficiency gains,
divided into three groups: top-down models, bottom-up models
and theoretical models.
Top-down models track historical trends in efficiency indicators
and extrapolate these into the future, to determine energy efficiency targets. For example, in the World Energy Outlook reference
scenario, the IEA predicts that the global average energy intensity
(a measure of global energy efficiency) will fall on average by 1.7%
per year from 2004 to 2030, based on the past 30 year trend [6].
However, there are two problems with such an approach. Firstly,
the extrapolated efficiency target may be unachievable because it
exceeds some theoretical or practical limit. An annual improvement in efficiency of 1.7% equates to a 35% saving by 2030 and an
impressive 55% by 2050. For many technical devices, such gains
may not be physically possible, leading to an exhaustion of the
innovation potential if alternative solutions cannot be found, as
discussed by Blok [7]. Secondly, these models assume that the
underlying structural components of energy demand are stable and
predictable over long periods, when in reality demand is affected
by disruptive events, discontinuities and non-rational human
behaviour. For example, Raupach et al. [8] show that the declining
trend in global energy intensity from 1980 to 2000, has in recent
years reversed, placing in doubt many predictions of future energy
demand and associated CO2 emissions. In practice, future predictions based on extrapolation of energy trends are rarely accurate,
prompting Vaclav Smil to comment that ‘long-range energy forecasts are no more than fairy tales’ [[9], p. 154].
Bottom-up models survey best practice efficiency technologies
and estimate their combined potential for reducing energy demand.
For example, a recent McKinsey Global Institute report found that
global energy demand could be reduced by more than 20% in 2020
by diffusing currently available technologies throughout the world
[10]. Efficiency options are typically ranked according to their
abatement potential and cost of implementation, enabling cumulative graphs of abatement potential to be created. Some wellknown examples of abatement curves include: the Global climate
abatement map by Vattenfall [11]; the IPCC bottom-up analysis for
sectoral mitigation in 2030 from Sims et al. [12]; the IEA marginal
abatement cost curves for sectors [2]. Such studies provide a useful
snapshot of current economic and technological drivers, and show
where efficient technologies can be immediately applied.
However, bottom-up models in their current form are incomplete
for two reasons. Firstly, these models aggregate potential efficiency
gains into broad economic sectors (e.g. transport, buildings,
industry), often ignoring the complex chains of technical conversion
devices and energy systems involved. Efficiency gains cannot simply
be added together, because a saving in one device often reduces the
potential for gain in a connected device. For example, a more efficient
electric motor requires less electricity for the same load, reducing the
demand for generation and therefore the absolute benefit of
J.M. Cullen, J.M. Allwood / Energy 35 (2010) 2059e2069
efficiency gains in that upstream generation. Secondly, bottom-up
models assess only known or emerging technologies that have
evolved under today's economic drivers and technical conditions.
Hence, surveys of current efficiency options identify mostly incremental gains to existing processes and tend to overlook opportunities from novel disruptive technologies or divergent development
pathways, which are beyond the influence of industry. Attempting to
assess all available technical options, including those that are yet to
be discovered, is problematic, so instead researchers have found
ways to calculate the theoretical improvement potential, independent from known efficiency measures.
Theoretical models define an absolute target by calculating an
upper efficiency limit based on thermodynamics. These models
avoid setting a theoretically impossible target and are not constrained by currently known technologies or industrial practice.
The thermodynamic property exergy (also known as availability)
shows how far a device is operating from its thermodynamic ideal,
allowing all energy conversion devices to be compared on an
equivalent basis. Detailed exergy models exist for many individual
conversion devices and include useful breakdowns of exergy losses.
Rosen et al. [13] stress that exergy analysis has an important role
to play in charting the increase of efficiency in society, because it
clearly identifies possible efficiency improvements and reductions
in thermodynamic loss. The first exergy analysis of an entire society
was published by Reistad [14] and estimated the overall efficiency
of the United States to be 21%. A review paper by Ertesvag [15]
summarises a further 15 societal exergy studies, including
coverage of numerous countries, regions, and one global study by
Nakicenovic et al. [16]. The analysis by Nakicenovic et al. estimates
the global efficiency of energy conversion in 1990 to be about 10% of
the theoretical limit, but the paper is highly technical and difficult
to comprehend for a non-expert reader. Although many exergy
analyses have been performed on individual conversion devices,
these are also technical in nature and appear only in specialist
thermodynamic journals. Attempts to aggregate exergy information for conversion devices into an accessible global form are rare,
and for this reason theoretical models are often overlooked when
determining research priorities and creating energy policy.
In this article, a theoretical model is used to assess energy
conversion devices providing an absolute basis for identifying and
ranking efficiency options. This requires comparing the current
efficiency of conversion devices with their theoretical maximum,
while considering the scale of energy flow through the technical
devices in the global energy network. Inevitably, using a purely
theoretical measure of efficiency promotes an ideal which may not
be practically achievable, either economically or technically.
However, such an approach provides a useful theoretical target
from which to set practical limits, and an absolute basis from which
to measure progress.
3. Constructing a map of global energy efficiency
Previous efforts to assess the potential savings from efficiency
measures are useful for identifying options and directing responses
in the short term. Yet their reliance upon recent economic trends
and known technical options makes them unlikely to be accurate
over the times scales being negotiated in climate change policy.
Using an absolute measure of efficiency, such an exergy analysis,
avoids the uncertainty which results from the extrapolation of
economic trends and captures the potential of yet to be discovered
efficient designs.
This paper aims to provide a visual map of global energy efficiency, which allows options to be identified and compared
according to an absolute basis, independent of benchmarks based
on economic or technical limitation. Three tasks must be completed
2061
to create such a map. The first is to determine the global scale of
energy flow through conversion devices, which can be found in the
previous analysis by Cullen and Allwood [4]. The second, requires
determining the theoretical efficiency limit for each type of
conversion device, and superimposing these onto the device energy
flows. Finally, it is important to present the results in a visually
accessible formatdsuch as a Sankey diagramdpermitting the
maximum savings from efficiency measures to be visualised.
3.1. Selecting a consistent measure of efficiency
To calculate the theoretical efficiency limit for each conversion
device an appropriate measure of energy efficiency is required.
Conventional energy efficiency, which is based on the first-law of
thermodynamics, is typically defined for a conversion device as:
h¼
energy output ðusefulÞ
energy input
(2)
A natural gas power plant operating at 40% efficiency, an electric
motor that is 95% efficient, and an air conditioner with a Coefficient
of Performance (COP) of 1.8, are all typical examples of reported
first-law efficiencies. However, this measure of efficiency is of
limited use when comparing different types of conversion devices,
because it is possible to have a maximum efficiency greater than
100%, and the quality of energy is not considered. For example, in
space heating applications, a typical “high-efficiency” gas burning
furnace has a first-law conversion efficiency of 95%, and an electric
heating system is 100% efficient. Based on these figures, it could be
assumed that space heating devices are already approaching their
maximum efficiency limits. However, a typical heat pump has
a COP of 3 (equivalent to an efficiency of 300%) and under ideal
conditions can approach 10 (or 1000%).
Such large variances in efficiency result from the failure of
conventional efficiency definitions to consider the quality of energyd
electricity and mechanical work are more valuable energy carriers
than low temperature heat. Conventional energy efficiency (based on
the first-law of thermodynamics) does not take into account this
difference in quality and hence is not an objective basis for evaluating
energy conversion devices.
In contrast, exergy efficiency (based on both the first and second
laws of thermodynamics, and similar in concept to effectiveness or
availability) provides a more equitable measure of conversion
efficiency. It uses mechanical work rather than energy as the basis
for comparing devices with each other and their thermodynamic
ideal. Exergy efficiency is defined for a device as:
e¼
exergy output
work output
¼
exergy input
maximum possible work output
(3)
By definition, the theoretical limit of exergy efficiency for an
individual device or a chain of multiple conversion devices, is
always unity.
Mechanical work is chosen as a basis for comparison because it is
a high quality, low entropy form of energy. Electricity, which can be
perfectly converted into mechanical work, is another high quality
form of energy. Thus for a device which converts one form of
mechanical energy to another (e.g. gearbox), or electrical energy to
mechanical energy (e.g. electric motor), exergy efficiency and energy
efficiency are almost the same. However, when the input or output of
the device is heat (e.g. space-heater) the energy value of the heat
must be downgraded into equivalent units of mechanical work.
The importance of using an absolute measure of efficiency is
explained using an example of lighting devices. It is sometimes
argued that replacing incandescent light bulbs with more efficient
compact fluorescent bulbs saves little energy, because the building's
2062
J.M. Cullen, J.M. Allwood / Energy 35 (2010) 2059e2069
space heating requirements are offset by the bulb's waste heat
production. Ignoring the fact that in many climates space heating is
not required in summer, and that waste heat from the bulb may
compete with air-conditioning systems, the argument is flawed
because it ignores the ‘quality’ of the energy. According to the firstlaw of thermodynamics, 100% of the electricity input to the bulb is
converted to either light or waste heat. Yet, from a second law
perspective the electricity is high quality energy (it can be converted
into work almost completely), whereas the bulb's waste heat is a low
quality form of energy (it is at low temperature, so is difficult to
convert to mechanical work). If a more efficient lighting device was
installed, the electricity saved could be used to run a high efficiency
device like a heat pump that could deliver 3 times more of the same
low quality heat than the light bulb (assuming a typical COP of 3).
Clearly, not all forms of energy are equal in quality or usefulness, and
therefore a consistent measure such as exergy is needed to equate
device efficiencies.
Exergy efficiency can be calculated directly, by finding the ratio of
the output to input exergy flows through the device, but in practice
this is complicated. Instead, if the conventional energy efficiency (h)
is known, then the exergy efficiency (e) can be estimated using:
e ¼ hn
Table 1
Energy and exergy efficiencies for upstream conversion devices.
Device
Description
h
n
e
%
%
%
Electricity generation from:
Oil
Crude oil and petroleum products
37a 94 35
Biomass
Combustible plant/animal products
25b 90 23
and municipal/industrial waste
Gas
Natural gas and gas works
40a 96 38
Coal
Hard coal, lignite and derived fuels
34a 94 32
(e.g. coke, blast furnace gas)
Nuclear
Nuclear fission (heat equivalent
33c 100 33
of electricity)
Renewable
Hydro, geothermal, solar, wind, tide,
80b 100 80
and wave energy
Fuel transformation In petroleum refineries, gas works,
93d 100 93
coal preparation, liquefaction,
distribution and own-use
CHP
Combined heat and power plants (all fuels) 56d 62 35
Heat
Utility heat plants (all fuels)
85d 24 20
Notes: h ¼ energy efficiency, n ¼ quality factor, e ¼ exergy efficiency.
a
IEA (p. 73) [25].
b
Estimated.
c
IEA (p. 138) [26].
d
Calculated from IEA [24].
(4)
where a dimensionless quality factor (n) is used to correct for the
loss of energy quality in the conversion process, resulting from two
sources. Firstly, the chemical exergy in a fuel is marginally higher
than the standard enthalpy of combustion, due to the additional
contribution of the post-combustion water vapour (lower heating
value) and the flue-gas components. Ertesvag and Mielnik [[17], p.
959] give values called ‘exergy factors’ which vary by between 4
and 11% across typical fuel sources. Secondly, where energy is
converted into heat, the heat output must be downgraded to be
measured as mechanical work, using the thermal efficiency for
a reversible Carnot engine (defined as j(T
T0)/Tj, where T is the
heat carrier and T0 is the ambient temperature, both in Kelvin).
Formal definitions of energy and exergy efficiency are found in
standard thermodynamic textbooks such as Çengel and Boles [18],
while more detailed explanations of the exergy method are
provided by Ahern [19], Hammond [20], Kotas [21], Szargut et al.
[22] and Szargut [23].
3.2. Calculating efficiency limits in conversion devices
Creating a map of global energy efficiency requires assigning
average efficiencies to each conversion device in the energy
network, including fuel transformation, different modes of electricity generation and end-use applications. It is important to select
efficiency values that are representative of the global device
average, calculated in a consistent way, and are from credible
sources. The input and output energy flows for the upstream conversionsdfuel transformation and electricity generation are well
defined in the energy literature, allowing efficiencies to be deduced.
However, global energy flow data is not available for end-use
conversion devices, and instead the efficiency values must be found
by a survey of literature.
The conversion efficiencies for fuel transformation and electricity generation are calculated from the 2005 Balance Table for the
World, produced by the IEA [24]. This table provides values for the
global energy supply broken down by fuel type, and the ‘final’ energy
delivered to consumers in the form of refined fuels and electricity.
Thus the average energy and exergy efficiencies for fuel transformation, electricity generation, and heat production, can be
inferred from these flows and other literature sources, as shown in
Table 1.
Some minor differences are found between energy and exergy
efficiency for combustion based electricity generation (n < 100%).
The input to these devices is increased when it is changed from
energy to chemical exergy, while the electricity output remains
unchanged. Thus the ratio of electricity output to chemical exergy
input is reduced, by the factor n, and the exergy efficiency is lower.
For Combined Heat and Power plants, and Heat plants, the difference between energy and exergy efficiency is larger because the
heat output of these devices must be downgraded to mechanical
work. In contrast, no difference is found for fuel transformation
(n ¼ 100%) because the inefficiency relates to material losses during
processing, nor for nuclear and renewable sources, for which the
device input remain unchanged.
Finding representative efficiency values for the global stock of
end-use conversion devices is difficult. Efficiencies cannot be
inferred from statistical studies of global energy flows, as this data is
not available for end-use devices. Instead published values for
energy and exergy efficiency must be used, but these vary considerably depending on the technology and vintage of the equipment
surveyed, the chosen system boundary for each device, and the
geographical scope of the study. Table 2 presents a review of 10
studies, covering the last 40 years, that list conversion device efficiencies. The review indicates whether the study uses energy efficiency or exergy efficiency (or equivalent second law measure), the
number of devices categories given, and describes the scope of the
study. The study by Nakicenovic et al. [16] is easily the most
comprehensive and consistent analysis of global energy and exergy
efficiency values. Unlike other studies, which use device case
studies to estimate best practice values, Nakicenovic et al. aggregate
data from 11 sub-regions, and across 6 fuels types, to create average
global values of energy efficiency (h) [in their Table 3.4] and exergyquality factors (n) [in their Table 3.5]. The analysis also allocates
global energy flows for 1990 to the selected devices, which helps to
verify the efficiency values. The list of end-use conversion devices
includes:
Residential/commercial sector cooking, washer/dishwasher,
space heating, hot tap water, space cooling, refrigeration,
mechanical energy, lighting, electronic data processing (EDP)/
television (TV), other household appliances.
2063
J.M. Cullen, J.M. Allwood / Energy 35 (2010) 2059e2069
Table 2
Survey of conversion device efficiencies.
Reference
Energy
Summers [[41], p.151]
U
Reistad [[14], p. 431]
Ford et al. [[3], p. 50]
O'Callaghan [[42], p. 108]
Culp [[43], p. 33]
Gilli et al. [[44], p. 11]
Nakicenovic et al. [[16], p. 228]
Hammond and Stapleton [[45], pp. 152e157]
U
USDOE [[27], p. 1]
Warr et al. [[46], pp. 34e35]
U
U
U
U
U
Exergy
No. of
devices
Scope
25
Chart of best available technology, by the type
of energy conversion
Table of US data, including electricity generation at 38%
Table, system boundary includes upstream electricity generation
Chart, system boundary includes upstream electricity generation
Chart of typical operational efficiencies
Chart of end-use devices, with range of efficiencies shown
Global values for energy and exergy efficiency, categorised by fuel
Charts and tables, by domestic, commercial, industrial
and transport applications
Table of US power generation and industrial equipment
Charts of UK devices
U
U
U
23
17
38
28
17
20
11
U
14
10
U
U
U
Industry process heat (low and medium temperature), high
temperature heat/electrolysis, mechanical energy, other industrial uses.
Transport bus/truck (Diesel), car/truck (Otto), airplanes,
internal navigation (by water), rail, other.
These minor adjustments made to the Nakicenovic et al. [16]
data result in the list of 14 end-use conversion devices, with efficiency values, shown in Table 3.
However, three adjustments are required to bring the efficiency
values reported by Nakicenovic et al. into a form which is suitable
for directing technical priorities today.
Firstly, some individual device efficiencies are updated to reflect
changes in system boundaries. The energy efficiencies for ‘mechanical energy’ devices (relating to electrical motors) are reported as 70%
in industry and 54% in residential, by Nakicenovic et al. However,
USDOE [27] calculate an average efficiency of 45% for the entire
motor driven system, including the pump or compressor. This lower
value more accurately describes the boundary system for an end-use
conversion device used in this paperdthe device output is measured
in its final useful form, in this case fluid motion. Ayres et al. [[28], p.
1117] provides a breakdown of industrial electricity use in the United
States, which is used to separate refrigeration (6% of total net
demand) from the broader category of ‘mechanical energy’ used by
Nakicenovic et al. The efficiency for internal navigation (by water) is
also applied to transport by international marine vessels, and biofuel
powered engines are assumed to have an efficiency of 10%.
Secondly, the reported efficiency values represent 1990 technology and are therefore outdated. Therefore the efficiencies are
scaled to match historical improvements in global energy intensity
using the IEA's reported sector improvements (cumulative from
1990 to 2004, updated for 2005): buildings 13.3%, industry 22.7%
and transport 8.2% [29]. Applying a uniform efficiency improvement
across the devices in each sector might lead to device efficiencies
greater than 100%. Instead the historical scale factors are applied
uniformly to the non-useful output of energy from each conversion
device, grouped by economic sectors.
Thirdly, the devices presented by Nakicenovic et al. are grouped
by economic sectors instead of individual technologies. For
example, the electrical motor could be listed as a distinct technology, but instead is included in four different categories:
‘mechanical energy’ (both industry and residential/commercial),
‘other household appliances’ and ‘other industrial uses’. The diesel
engine is hidden in these same four categories, and in four additional transport categories: ‘bus/truck’, ‘internal navigation’, ‘rail’
and ‘other’. The selected device categories also vary considerable
in scale of energy flow, from as low as 0.1% of global energy
demand for ‘washer/dishwashers’ to greater than 16% for ‘space
heating’. It is preferable to organise the efficiency data into technically discrete categories of conversion devices, of approximately
equal scale of energy flow.
For any real process (and thus energy conversions) there are
always thermodynamic irreversibilities present. To provide further
insight into how energy is degraded, and therefore what strategies
could make better use of energy, the calculated exergy losses from
each conversion device are aggregated into ten engineering loss
mechanisms, as described in Table 4.
There is no single study which provides a breakdown of global
exergy loss across the range of conversion devices considered.
Instead a number of exergy analyses of individual conversion
devices are consulted: Dunbar and Lior [30] and Prins and Ptasinski
[31] for generic combustion processes (applicable to engines,
heaters and fossil fuel based electricity generation); Dunbar et al.
3.3. Grouping losses by engineering mechanisms
Table 3
Energy and exergy efficiencies of end-use conversion devices.
End-use device
Description
h
n
e
%
%
%
Motion average
Diesel engine
Compression ignition diesel engine: truck,
car, ship, train, generator
Petrol engine
Spark ignition otto engine: car, generator,
garden machinery
Aircraft engine Turbofan, turboprop engine
Other engine
Steam or natural gas powered engine
Electric motor
AC/DC induction motor (excl. refrigeration)
26 90 24
22 95 21
28 99 27
47 53 25
60 93 56
Heat average
Oil burner
58 24 14
61 25 15
13 99 12
Oil combustion device: boiler,
petrochemical cracker, chemical reactor
Biomass burner Wood/biomass combustion device:
open fire/stove, boiler
Gas burner
Gas combustion device: open fire/stove, boiler,
chemical reactor
Coal burner
Coal combustion device: open fire/stove, boiler,
blast furnace, chemical reactor
Electric heater Electric resistance heater, electric arc furnace
Heat exchanger Direct heat application: district heat,
heat from CHP
Other average
Cooler
Light device
Electronic
All devices
Refrigeration, air con.: industry,
commercial, residential
Lighting: tungsten, fluorescent, halogen
Computers, televisions, portable devices
34 20
7
64 21 13
59 31 19
80 30 24
87 15 24
60 14
104 6
Notes: h ¼ energy efficiency, n ¼ quality factor, e ¼ exergy efficiency.
8
7
13 90 12
20 30 6
51 50 25
2064
J.M. Cullen, J.M. Allwood / Energy 35 (2010) 2059e2069
Table 4
Loss mechanisms.
Mechanism
Combustion
Internal heat
exchange
Description
Heat transfer between product molecules leaving
the reaction site (with kinetic and photon energy)
and neighbouring unreacted molecules, leads to
unrecoverable exergy loss. Internal heat exchange can
be avoided if the reactant and product streams are
separated.
Oxidation
Chemical interactions (intra-molecular, radiation,
thermo-mechanical) result from the reaction
of oxygen and fuel, producing irreversible changes
of energy. Conversion of chemical energy to a useful
form without combustion, for example in fuel cells,
can prevent some of this loss.
Mixing
Spontaneous mixing of reactants in the
pre-combustion stage, and products in the
post-combustion stage, cannot be reversed without
additional energy input. It is difficult to avoid mixing
in combustion processes.
Heat transfer
Heat exchange
Heat transfer through a finite temperature produces
irreversibilities (e.g. from combustion gases to steam).
Minimising the temperature difference reduces losses,
but increases the heat exchanger costs. Avoiding the
use of high temperature fuel combustion for low
quality applications (space and water heating),
and cascading heat can reduce losses.
Exhaust
Thermal and chemical potential of stack and tailpipe
emissions. Extracting heat from water vapour
(condensing boilers) and completely oxidising fuel
can prevent some loss.
Heat loss
Heat transfer from equipment to the environmental
reference state. Losses can be minimised using
insulation, preventing leaks of hot gas and liquids,
and ensuring reactants and products leave the system
at the surrounding temperature.
Other
Electrical resistance Resistivity (I2R), eddy currents and magnetic
hysteresis losses in devices (e.g. power distribution,
electric motor, light bulb, electronic). Can be
minimised by selecting superior materials/metals
for electrical components, and by reducing the length
of electrical wires through miniaturisation of
electronics and localisation of electricity supply.
Friction
Friction (sliding and fluid flow), inelastic deformation
and unrestrained compression/expansion leads to
non-recoverable exergy loss (e.g. in motors, turbine,
engine, pump and pipe). Losses are reduced by using
lubricants, reducing fluid flow velocities, and resisting
expanding gases.
Fission (nuclear)
Highly irreversible fission and heat transfer processes
result in losses. Can be partially reduced by using
fossil fuel fired superheat and reheat units in the
downstream steam system.
Fuel losses
Transformation, own-use, distribution
and transmission of primary fuels results in physical
losses (e.g. oil and gas leaks from pipelines).
These can be reduced with good design and
maintenance, or by using a more localised energy source.
[32] and Durmayaz and Yavuz [33] for electricity generation using
nuclear fission; Ertesvag and Mielnik [17] for hydroelectricity;
Rakopoulos and Giakoumis [34] for diesel engines; Ford et al. [3] for
petrol engines; Turgut et al. [35] for aircraft engines; Mecrow and
Jack [36] and USDOE [27] for electric motor drives; Kotas [21] for
refrigeration. The exergy breakdowns do not always correlate
directly with the conversion device categories used in this study; in
these cases scale factors, interpolation and estimation were used to
complete the data. The exergy efficiencies for these individual
studies were compared with the global averages presented by
Nakicenovic et al. [16] and found to be broadly consistent.
3.4. Results
The global map of conversion efficiency is presented in Fig. 3.
Energy flow is traced from primary energy sources (left), through fuel
transformation, electricity generation, and end-use device conversion, to useful energy (top-right). The vertical lines show where
energy is converted to a new form, with any non-useful energy
output (exergy loss) being separated from the main flow and collated
in the bottom-right corner. (The labels used to distinguish the energy
flows are defined in: Table 1 for energy sources, Table 3 for conversion devices, and Table 4 for loss mechanisms). The thickness of each
line represents the scale of energy flow, with the use of colour to help
distinguish different energy flows. Useful energy, in the form of heat,
motion, light, sound, and cooling, is collected in the top-right corner
and indicates the energy required if the current conversion devices
were all to operate at their theoretical maximum exergetic efficiency.
Energy values are reported in exajoules (EJ ¼ 1018 J) and direct CO2
emissions associated with fossil fuels are shown in the red circles in
billion tonnes of CO2 (GtCO2 ¼ 109 t CO2) (based on 2005 data from
the IEA Key World Energy Statistics [[37], p. 44]).
3.5. Data accuracy
Rigorous data for estimating conversion device efficiencies and
allocating losses, is not readily available. Energy allocation varies
considerably between countries and energy efficiency differs
between devices depending on the age, operation, and type of
device. Although some exergy loss breakdowns are available for
specific devices, the various methodologies employed make it
difficult to translate this data into a consistent global analysis. To
minimise the influence of these variables, data was selected from
only two sources with global coveragedIEA [24] for energy flow and
Nakicenovic et al. [16] for conversion device efficiencies. These
sources do not include a quantitative error analysis, and therefore
a formal assessment of the data accuracy cannot be made. However,
each data set has been prepared in a consistent manner, having been
collated from many smaller regional energy studies and surveys. All
energy values reported in this analysis are rounded to the nearest EJ.
One simplifying factor in this analysis is the allocation of energy
use directly to the physical devices which convert energy. There is
no need to embed the energy associated with upstream conversion
processes such as electricity generation, or non-direct energy
inputs such as transport and capital equipment. These energy
inputs are allocated directly to the conversion device. This avoids
the complex boundary issues associated with other energy analysis
methods, such as Life Cycle Assessment, where the allocation of
non-direct impacts is subject to truncation and double-counting
errors, as discussed by Cullen and Allwood [38].
Despite these known imperfections in data accuracy, the use of
best available energy data provides a much needed basis for prioritising action in the area of energy efficiency. It is anticipated that
over time new studies will provide more accurate efficiency data
for energy conversion devices, which can be used to build further
upon this research.
4. Discussion
Having mapped the theoretical efficiency limits for conversion
devices onto the global energy network, what can now be inferred
about the efficiency with which society uses energy? How do the
efficiencies of different conversion devices compare? How can we
2065
J.M. Cullen, J.M. Allwood / Energy 35 (2010) 2059e2069
Fig. 3. The global map of energy conversion efficiency.
interpret the map of energy efficiency, in order to direct priorities
for researchers, designers and engineers working in the field of
efficiency?
4.1. How efficient are current conversion devices?
Individual device efficiencies from different parts of the diagram
cannot be compared directly with each other. To state that an electric
motor is more efficient than a diesel engine, ignores the larger
upstream losses from electricity generation and distribution that are
linked with the electric motor. Instead, a compound efficiency (ec)
can be calculated for each energy chain, by multiplying consecutive
device efficiencies together along the entire chain length:
ec ¼ ef ee ed
(5)
The subscripts used to indicate the type of conversion device are
taken from the map of energy flow shown in Fig. 1: c ¼ compound
efficiency, f ¼ fuel transformation; e ¼ electricity generation and
distribution; d ¼ device conversion (end-use).
The resulting compound efficiencies for energy chains are shown
in Table 5, organised by the end-use conversion devices. These
indicate the theoretical efficiency limit for each chain, from fuel to
useful energy, irrespective of any particular combination of
conversion devices. Table 5 demonstrates that the conversion of
fuels to useful energy is typically inefficient, averaging only 11%
across all devices. The efficiency of conversion devices has improved
only marginally over the last 15 years, when compared with the 10%
calculated by Nakicenovic et al. [16]. This small absolute improvement in average device efficiency places into sharp contrast the
reported and acclaimed 15% relative improvement in global energy
efficiency between 1990 and 2005 IEA [25]. Furthermore, the
compound efficiencies (ec) for energy chains in 2005 range from 2 to
25% suggesting any device operating above an efficiency of 20% is
converting energy in an efficient manner.
Most of the inefficiency can be traced to the poor conversion of
energy in end-use conversion devices (ed), which average only 18%.
Looking specifically at this column, it can be seen that engines,
which deliver motion, typically operate with relatively high efficiencies (12e27%) due to intense development motivated by
economic drivers to reduce the weight of both fuel and the engine in
Table 5
Comparing the efficiency of conversion devices.
Energy chain
Conversion efficiencies
ef
ee
ed
ec
%
%
%
%
Aircraft engine
Diesel engine
Other engine
Electric motor
Petrol engine
Motion average
93
93
92
93
93
93
100
100
78
32
100
77
27
21
25
56
12
24
25
20
18
17
12
17
Coal burner
Oil burner
Gas burner
Electric heater
Biomass burner
Heat exchanger
Heat average
90
93
91
93
95
93
93
100
100
100
32
100
17
76
19
15
13
24
7
13
14
17
14
12
7
6
2
10
Light device
Cooler
Electronic
Other average
93
93
93
93
34
33
32
33
12
7
6
8
4
2
2
2
Overall Average
93
70
18
11
Notes: e ¼ exergy efficiency, with subscripts, f ¼ fuel transformation; e ¼ electricity
generation; d ¼ end-use device conversion; c ¼ compound efficiency.
2066
J.M. Cullen, J.M. Allwood / Energy 35 (2010) 2059e2069
transport vehicles. This is particularly the case for aircraft engines
where weight constraints have resulted in highly efficient designs.
Electric motors are even more efficient (56%), because the upstream
conversion losses from combustion are included in the intermediate
conversion step of electricity generation (ee). In contrast, devices
which combust fuels to provide heat operate at lower device efficiencies (7e19%), with the variance depending primarily on the
temperature at which heat is delivered. This explains why natural
gas, a high quality fuel used in many low-grade applications such as
space heating, is combusted at lower efficiencies than coal, which
has many higher temperature industrial applications such as steel
production. Cooling, lighting and electronic applications have low
efficiencies (6e12%), and additional losses result from the conversion of fuel to electricity, at an efficiency of 32%.
However, the efficiencies calculated in Table 5 are not in
themselves sufficient for ranking conversion devices. To be
consistent, the analysis needs to consider both the device efficiency
limit and the scale of energy flow. For example, it would be illogical
to focus efforts on improving the low efficiency of steam engines
(included under other engines), when this technology is no longer
in common use. The resulting efficiency gains would not translate
into significant reductions in energy use or CO2 emissions because
the application lacks scale.
4.2. Theoretical energy and CO2 savings
Theoretical energy savings can now be calculated for each
complete energy chain, from fuel to useful energy. Using Equation
(1), the target efficiency is set to unity and the current efficiency
equals the compound efficiency for each chain (ec), from Table 5.
The corresponding savings in CO2 emissions are calculated by
equating the fossil fuel energy inputs with their direct CO2 emissions, and are reported in Table 6. This allows alternative energy
chains to be compared and ranked, based on the potential for
reducing energy demand and CO2 emissions, and for responses to
be directed towards the conversion devices with the greatest
improvement potential.
Table 6 shows that 85% of conversion losses can be attributed to
the provision of heat and motion (10.4 and 9.6 EJ respectively, out of
a total 23.8 EJ). The top half of the table is dominated by heaters,
burners and engines, and efforts should be focused on improving
Table 6
Theoretical energy and CO2 savings.
ec Energy
Energy
CO2 emissions CO2 savings
demand EJ savings EJ GtCO2
GtCO2
Energy
Chain
1
%
Electric heater
Diesel engine
Electric motor
Biomass burner
Gas burner
Petrol engine
Cooler
Coal burner
Oil burner
Heat exchanger
Light device
Electronic
Other engine
Aircraft engine
93
80
83
94
88
88
98
83
86
98
96
98
82
75
58
58
55
49
47
41
33
31
28
20
18
16
10
11
54
47
46
45
41
36
33
26
24
20
17
15
8
8
3.4
4.1
3.2
0.0
2.6
2.9
1.9
2.7
1.9
1.2
1.0
0.9
0.7
0.7
3.1
3.3
2.6
0.0
2.3
2.5
1.9
2.2
1.7
1.2
1.0
0.9
0.6
0.5
Heat
Motion
Other
90
83
98
233
175
67
210
145
65
11.7
11.6
3.9
10.4
9.6
3.8
Total
89
475
420
27.2
23.8
Notes: ec ¼ compound exergy efficiency; potential for saving energy h conversion
losses.
the efficiency of these devices. Lighting devices, electronics and
aircraft engines together account for less than 10% of the potential
savings. Efforts aimed at promoting compact fluorescent light bulbs
(CFL) and reducing electronic standby losses, present easy gains due
to their relatively low efficiencies and help raise public awareness of
efficiency concerns, but will not make a significant impact on
demand for energy. The conversion efficiency of aircraft engines is
already high (27%), suggesting that improvement in engine efficiency will be difficult to achieve, and the available energy savings at
the global level are small. Thus few technical options remain to
improve the energy efficiency of flying, so a reduction in CO2
emissions from this sector would be more easily obtained by
a reduction in the number of flights.
4.3. Where are efficiency gains most likely?
The analysis has shown that conversion devices on average
operate at only 11% of their theoretical potential. Yet, given the
sizeable effort already in progress to improve device efficiency, it is
unlikely that this idealda factor 10 improvementdwill be
approached in the near future. Where should action and responses
be focused? Is it better to prioritise efforts on improving coal-fired
power stations or diesel engines? This is difficult to answer because
the theoretical saving in both energy and CO2 emissions depends
not only on the efficiency of the individual device, but also on the
upstream efficiencies of all devices in the energy chain. A solution to
this question can be found by performing a sensitivity analysis to
assess the energy savings that would be achieved from a small
independent change in efficiency for each type of conversion device.
Applying an absolute efficiency change (i.e. increasing each
value of e by 1%) to each device might be misleading, as achieving
an equivalent gain in an already efficient device is likely to be more
difficult than for a less efficient device. Instead, the conversion loss
(which equals the theoretical energy saving) for each device is
reduced by 1%, and a modified device efficiency is calculated using:
e0 ¼ e þ ð1
eÞ1% ¼ 0:99e þ 0:01
(6)
The efficiency of each device in turn was changed to the modified value (e0 ) and the resulting total global energy input required to
deliver the same useful energy was calculated. This leads to
a sensitivity analysis of energy savings for the same relative level of
improvement in each device, and provides a more equitable way to
compare and rank individual conversion devices, irrespective of the
location of the device in the energy network. This sensitivity
analysis is performed for individual conversion devices, as opposed
to energy chains, and the results are shown in Fig. 4. The chart
shows the reduction in energy and CO2 emissions resulting from
a 1% reduction in the loss from each conversion device.
Efforts to improve the efficiency of coal-fired power stations will
deliver the most savings in the upstream fuel conversion and
electricity generation processes, because coal dominates electricity
generation. However, greater energy savings are available from
focusing individually on: biomass burners, coolers, gas burners and
petrol engines. Collectively, prioritising efficiency measures for
end-use conversion devices over fuel transformation and electricity
generation delivers more than five times the potential gain (28 EJ
versus 5 EJ). This is a surprising result, given the emphasis placed
on improving the efficiency of electricity generation, for example in
the IEA report, Energy technology perspectives 2008 [2].
Biomass burners emerge as the single most important conversion device, where the largest energy savings can be achieved from
an incremental improvement in efficiency. These burners are
predominantly open fires, which burn wood, dung, crop waste, coal
2067
J.M. Cullen, J.M. Allwood / Energy 35 (2010) 2059e2069
Table 7
Loss mechanisms which cause energy to be degraded.
Loss mechanism EJ
Fuel
conversion
Electricity
generation
Device
conversiona
Internal heat exchangeb
Heat exchange
Exhaust
Electrical resistance
Heat loss
Oxidationb
Fuel loss
Friction
Fission
Mixingb
0
0
0
0
0
0
34
0
0
0
25
24
7
15
19
15
0
10
15
2
51
49
47
34
26
29
0
12
0
6
76
73
54
49
45
44
34
22
15
8
Heat transfer
Combustion
Otherc
0
0
34
50
42
40
122
86
46
172
128
120
Total
34
132
254
420
Total loss
Notes:
a
In end-use devices.
b
In combustion processes.
c
Includes friction, electrical, fission, fuel losses.
Fig. 4. The ranking of individual conversion devices by sensitivity to theoretical efficiency improvement.
and charcoal, to meet the energy needs of people living in the
developing world. The reason biomass burners top the sensitivity
list is due to the inefficiency of the burners, averaging only 7%, and
the scale of usedmore than a third of the world's population burn
biomass for cooking and heating, according to Warwick and Doig
(p. 1 [39]), and the IEA [[26], p. 115] report that solid biomass
accounts for 10% of global energy supply. In this analysis, biomass
burners do not contribute to CO2 emissions, because it is assumed
that the CO2 released during combustion is equivalent to the CO2
absorbed when growing the biomass. However, if the biomass is not
replaced, for example in areas where deforestation is a problem,
then net CO2 emissions to the atmosphere result.
Improving the efficiency of biomass burning stoves is technically very easy, and has the added benefit of reducing respiratory
illness from the inhalation of smoke, which is ‘the single biggest
killer of children under five years of age’ [[40], p. 24]. Options to
improve stove technology or use fuels with lower CO2 emissions are
held back by the lack of international political backing, limited
funding and the logistical problem of disseminating new technology, due to the enormous number of open fires in use.
4.4. Understanding how energy quality is degraded
The global map of energy conversion (Fig. 3) shows that only
a small fraction of the available energy supply is converted to useful
energy in conversion devices. This fraction represents the theoretical
minimum amount of energy that is required to provide the same
amount of final service (assuming the downstream passive system
does not change). During the conversion process the remaining
energy is degraded to low temperature heat and finally ‘lost’ to the
surrounding environment. In Table 7 this loss of energy quality (or
exergy) is divided into ten engineering loss mechanisms. Understanding the causes of energy degradation in conversion processes
helps to direct research priorities and future technical innovation.
Heat transfer processes are identified as the most significant
source of loss (at 172 EJ, more than 40%). This stems from the
irreversible nature of heat transfer across a finite temperature
difference, and reflects the ill-considered use of high quality energy
sources (fossil fuels and electricity) for low temperature applications. Combustion processes are a significant source of losses
(128 EJ, 30%), especially from internal heat exchange when cold
reactants mix with hot combusted products. The majority of
combustion losses cannot be avoided without separating the
reactant and product streams, suggesting that long-term technical
opportunities lie in devices which convert chemical energy directly
to electricity. Surprisingly, friction does not feature prominently in
the analysis indicating that the research activity in the fields of
lubrication and tribology, though important for preventing material wear and hence reducing equipment costs, have limited scope
for reducing energy use.
5. Conclusion
Developing more efficient energy conversion devices is essential
if efforts to reduce CO2 emissions are to be successful. The global
map of energy efficiency presented in this paper allows conversion
devices to be ranked according to their theoretical improvement
potential. The analysis makes three novel contributions to our
understanding of energy efficiency by:
determining the average global conversion efficiency of devices
along each individual energy chain, and presenting this analysis in a visually accessible format;
combining the scale of energy flow and the theoretical limits to
efficiency to identify key areas where technical innovation is
likely to deliver gains;
allocating, for the first time, the global loss of energy quality to
technical loss mechanisms, to direct future priorities.
2068
J.M. Cullen, J.M. Allwood / Energy 35 (2010) 2059e2069
Simple options for improving device efficiency include moving
the average global efficiency towards best practice and reducing
excess capacity from over-design. For example, the global average
efficiency of energy use in light devices is calculated to be 4%, still far
below advanced technologies such as CFL and light emitting diodes
(LED) with efficiencies above 20%. Similarly, electricity generation in
advanced gas-turbine plants is approaching efficiencies of 60%, yet
the global average is nearer to half this value. Many conversion
devices are also over-designed for excess capacity so operate well
away from their optimal efficiency point. This is the case with
vehicle engines, which at normal cruising conditions operate well
below their optimum efficiency, because of the requirement to have
reserve power for acceleration. Designs which avoid or smooth out
these peaks in power demand, such as hybrid power systems in
vehicles, deliver much higher conversion efficiencies.
How much of the theoretical efficiency improvement could be
realised in practice? Beyond the simple gains described above, it is
necessary to consider the technical and socio-economic barriers
preventing advances in energy efficiency and look for alternative
technology chains to deliver useful energy. There are many technical
factors that prevent designers from approaching theoretical efficiency limits. For example, combustion processes, because they
convert fuel into heat, are constrained by Carnot's Law and the
adiabatic flame temperature of the fuel. This means that the efficiency of power generation is unlikely to rise much above 65% and
current efforts to improve efficiencydfor example, increasing the
heat addition temperature by using novel materials, preheating
combustion reactants, extracting mechanical work from turbines
prior to steam productiondwill give only incremental gains. To
approach the thermodynamic limit would require avoiding
combustion altogether, by converting the chemical energy in fuels
directly into electricity (and then motion) in devices such as fuel cells.
Significant socio-economic barriers also limit the uptake of new
efficient designs. These include market imperfections (such as
a lack of adequate information and financing, higher perceived
costs, and differential benefits to the owner and user) and behavioural barriers (for example, consumer trends and habits, and the
rebound effect). It is important that theoretical measures of efficiency gain, such as the work presented in this article, are in turn
evaluated against such socio-economic considerations. Nevertheless, the overriding lesson from this analysis is to begin focusing
research initiatives and directing efficiency policy towards the
technical devices in which the greatest gains can be found. Only 11%
of primary energy is converted into useful energy, thus the theoretical gains available are substantial.
Further work is required to find the practical improvement
potential for conversion devices, subject to engineering and technical constraints. In addition, estimating the potential gains from
improving passive systems, for which there are no theoretical limits,
would allow the overall gains from fuel to final services to be found.
Nevertheless, a consistent framework for ranking energy efficiency
opportunities is now in place, and can be used for directing future
research and policy decisions in the field of energy efficiency.
Acknowledgements
The work of the first author is supported by the Overseas
Research Scheme and the Cambridge Commonwealth Trust.
References
[1] Kaya Y. Impact of carbon dioxide emission control on GNP growth: interpretation of proposed scenarios. Paris: IPCC Energy and Industry Subgroup.
Response Strategies Working Group; 1990.
[2] IEA. Energy technology perspectives 2008. Paris: International Energy Agency;
2008a.
[3] Efficient use of energy. In: Ford KW, Rochlin GI, Socolow RH, Hartley D,
Hardesty DR, Lapp M, Dooher J, Dryer F, Berman SM, Silverstein SD, editors.
Conference on the technical aspects of the more efficient use of energy,
Princeton, NJ, July 8eAugust 2, 1974. New York, United States: American
Institute of Physics; 1975.
[4] Cullen JM, Allwood JM. The efficient use of energy: tracing the global flow of
energy from fuel to service. Energy Policy 2010;38(1):75e81.
[5] Dyer CH, Hammond GP, Jones CI, McKenna RC. Enabling technologies for
industrial energy demand management. Energy Policy 2008;36(12):4434e43.
[6] IEA. World energy outlook 2006. Paris: International Energy Agency; 2006.
[7] Blok K. Improving energy efficiency by five percent and more per year?
Journal of Industrial Ecology 2004;8(4):87e99.
[8] Raupach MR, Marland G, Ciais P, Le Quere C, Canadell JG, Klepper G, et al.
Global and regional drivers of accelerating CO2 emissions. Proceedings of the
National Academy of Sciences of the United States of America 2007;104
(24):10288e93.
[9] Smil V. Long-range energy forecasts are no more than fairy tales. Nature
2008;453(7192):154.
[10] Bressand F, Farrell D, Hass P, Morin F, Nyquist S, Remes J, et al. Curbing global
energy demand growth: the energy productivity opportunity, Tech. Rep.
McKinsey Global Institute; 2007.
[11] Vattenfall. Global climate abatement map, Vattenfall, www.vattenfall.com;
2007 [accessed 20.02.07].
[12] Sims R, Schock R, Adegbululgbe A, Fenhann J, Konstantinaviciute I,
Moomaw W, et al. Energy supply. In: Metz B, Davidson OR, Bosch PR, Dave R,
Meyer LA, editors. Climate change 2007: mitigation. Contribution of Working
Group III to the Fourth Assessment Report of the Intergovernmental Panel on
Climate Change. Cambridge, United Kingdom and New York, NY, USA:
Cambridge University Press; 2007.
[13] Rosen M, Dincer I, Kanoglu M. Role of exergy in increasing efficiency and
sustainability and reducing environmental impact. Energy Policy 2008;36
(1):128e37.
[14] Reistad GM. Available energy-conversion and utilization in United-States.
Journal of Engineering for Power-Transactions of the ASME 1975;97(3):
429e34.
[15] Ertesvag I. Society exergy analysis: a comparison of different societies. Energy
2001;26(3):253e70.
[16] Nakicenovic N, Gilli PV, Kurz R. Regional and global exergy and energy efficiencies. Energy 1996;21(3):223e37.
[17] Ertesvag I, Mielnik M. Exergy analysis of the Norwegian society. Energy
2000;25(10):957e73.
[18] Çengel Y, Boles M. Thermodynamics: an engineering approach. 5th ed.
McGrawl Hill; 2006.
[19] Ahern JE. The exergy method of energy systems analysis. New York: John
Wiley & Sons; 1980.
[20] Hammond GP. Industrial energy analysis, thermodynamics and sustainability.
Applied Energy 2007;84(7e8):675e700.
[21] Kotas T. The exergy method of thermal plant analysis. London: Butterworths;
1985.
[22] Szargut J, Morris DR, Steward FR. Exergy analysis of thermal, chemical, and
metallurgical processes. New York: Hemisphere; 1998.
[23] Szargut J. Exergy method: technical and ecological applications. Great Britain:
WIT Press; 2005.
[24] IEA. 2005 balance table for the world. Paris: International Energy Agency,
www.iea.org; 2008b [accessed July 2008].
[25] IEA. Worldwide trends in energy efficiency. Paris: International Energy
Agency; 2008c.
[26] IEA. Energy statistics manual. Paris: International Energy Agency; 2005.
[27] USDOE. Energy use, loss and opportunities analysis. U.S. Manufacturing &
Mining, Industrial Technologies Program, U.S. Department of Energy; 2004.
[28] Ayres RU, Ayres LW, Pokrovsky V. On the efficiency of US electricity usage
since 1900. Energy 2005;30(7):1092e145.
[29] IEA. Energy use in the new millenium: trends in IEA countries. Paris: International Energy Agency; 2007a.
[30] Dunbar W, Lior N. Sources of combustion irreversibility. Combustion Science
and Technology 1994;103(1e6):41e61.
[31] Prins M, Ptasinski K. Energy and exergy analyses of the oxidation and gasification of carbon. Energy 2005;30(7):982e1002.
[32] Dunbar W, Moody S, Lior N. Exergy analysis of an operating boiling-waterreactor nuclear-power station. Energy Conversion and Management 1995;36
(3):149e59.
[33] Durmayaz A, Yavuz H. Exergy analysis of a pressurized-water reactor nuclearpower plant. Applied Energy 2001;69(1):39e57.
[34] Rakopoulos CD, Giakoumis EG. Comparative first- and second-law parametric
study of transient diesel engine operation. Energy 2006;31(12):1927e42.
[35] Turgut ET, Karakoc TH, Hepbasli A. Exergetic analysis of an aircraft turbofan
engine. International Journal of Energy Research 2007;31(14):1383e97.
[36] Mecrow B, Jack A. Efficiency trends in electric machines and drives. United
Kingdom: Foresight Programme, Office of Science and Innovation; 2006.
[37] IEA. Key world energy statistics 2007. Paris: International Energy Agency; 2007b.
[38] Cullen JM, Allwood JM. The role of washing machines in life cycle assessment
studies. Journal of Industrial Ecology 2009;13(1):27e37.
J.M. Cullen, J.M. Allwood / Energy 35 (2010) 2059e2069
[39] Warwick H, Doig A. Smoke e the killer in the kitchen: indoor pollution in
developing countries. London: ITDG Publishing; 2004.
[40] Gordon B, MacKay R, Rehfuess E. Inheriting the world: the atlas of children's health and the environment. Geneva: World Health Organization;
2004.
[41] Summers CM. The conversion of energy. Scientific American 1971;225(3):148e60.
[42] O'Callaghan P. Design and management for energy conservation. Oxford:
Pergamon Press; 1981.
[43] Culp A. Principles of energy conversion. 2nd ed. McGrawl Hill; 1991.
2069
[44] Gilli PV, Nakicenovic N, Kurz R. First- and second-law efficieincies of the global
and regional energy system. Austria: International Institute for Applied
Systems Analysis (IIASA); 1996.
[45] Hammond G, Stapleton A. Exergy analysis of the United Kingdom energy
system. Proceedings of the Institution of Mechanical Engineers Part A-Power
and Energy 2001;215(A2):141e62.
[46] Warr B, Schandl H, Ayres R. Long term trends in resource exergy consumption
and useful work supplies in the UK, 1900e2000. Canberra: CSIRO Sustainable
Ecosystems; 2007.