Roadmap for Australian Electricity Generation

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    ESSAYRoadmap for Australian

    Electricity Generation

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    TABLE OF CONTENTS

    Table of contents I

    1. Introduction 1

    1.1. Australias energy profile 1

    2. Carbon capture and storage 3

    2.1. CO2 capture techniques 3

    2.1.1. Post combustion 3

    2.1.2. Pre combustion 42.1.3. Oxyfuel combustion 4

    2.2. CO2 storage 4

    2.2.1. Structural storage 5

    2.2.2. Residual storage 5

    2.2.3. Dissolution storage 5

    2.2.4. Mineral storage 5

    2.3. Geological sites 5

    2.3.1. Deep saline formations 5

    2.3.2. Coal seam 6

    2.3.3. Depleted oil and gas fields 6

    2.4.Projects underway 7

    3. Enhanced oil recovery (EOR) 7

    4. Trigeneration Systems 9

    4.1. Prime mover 9

    4.1.1. Gas powered prime mover 11

    4.2.Cooling technologies 13

    5. Conclusion 14

    6. References 15

    I

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    1. INTRODUCTION

    Australia as a nation relies heavily on coal to satisfy its energy needs. This

    reliance has led heavy CO2 emissions which are becoming a serious concern.

    There is a dire need for Australia to rethink its electricity generation plan for the

    future.

    This essay proposes a roadmap for the future of Australian electricity generation

    taking into consideration various options like renewable energy, carbon captureand storage and government policies. My proposal focuses initially on the process

    of carbon removal and then on trigeneration systems which have better

    efficiencies and lower emissions compare to conventional power plants.

    1.1.Australias energy profile

    The desire for higher life standards and comfort levels along with

    technological advancement and growing population in the last threedecades have led to a steep increase in the worldwide energy consumption.

    The total primary energy consumption has increased from 4948.66 MTOE

    in 1970 to 12476.63 MTOE in 2012. While Africa has the least share of 3.2%,

    Asia Pacific leads the energy consumption with 40.01% in 2012. Europe &

    Eurasia consumes 23.47% of the total primary energy closely followed by

    North America at 21.84% [1].

    Conventional fossil fuels are still the dominating source of fuel in 2012. Fig.

    2 represents the primary energy world consumption by fuel type and the

    reliance on fossil fuels is clear. Oil, natural gas and coal make up for 86.9%

    of the worlds fuel usage while nuclear contributes 4.49%, hydroelectricity

    6.6% and renewables make up just about 1.9% [2]. As per the Australian

    energy update by BREE, the energy consumption by renewables has fallen

    by 7.3% from 2010-11 to 2011-12 [3].

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    This heavy reliance on fossil fuels has lead to an increase in CO2 emissions.

    The global energy-related CO2 emissions increased by 1.9% to 34.47

    gigatonnes in 2012 compared to 2011 [1].

    Fig. 1. World Primary Energy Consumption by fuel types [4]

    30% of the total energy consumption is accounted for by the buildingsector. Energy used in buildings is mainly for electric power, heating and

    cooling/refrigeration needs [5]. It hence becomes important to reduce

    energy usage or increase efficiency. Most of the power buildings receive are

    from power plants employing fossil fuels; coal is predominantly used in

    Australia. These power plants are known to have high rates of energy losses

    mostly in the form of heat. Coal power plants convert 39% of the available

    heat to electrical power [6]. Additional losses during transmission along

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    with huge infrastructure costs mainly borne by the customers, emphasises

    on the need for more efficient and cost effective technologies.

    2. CARBON CAPTURE AND STORAGE

    Carbon Sequestration (CS), also termed as Carbon Capture and Storage (CCS) is a

    method of capturing carbon from industries such as energy or oil and gas

    industries, compressing it and then storing it in the earths crust at sufficient

    depth to make sure it remains there indefinitely.

    It involves various stages, first one being capture, in which the carbon dioxide is

    captured from flue gases and other sources using an appropriate process. Once

    the carbon is captured it needs to be transported to the required site for storage.

    For easier transport, the carbon dioxide is pressurised and liquefied. There

    already exists mature technology that is needed for this transport. The final stage

    involves injection of the captured carbon dioxide into the earths crust. There are

    various mechanisms by which this can be injected. The injected carbon dioxide

    can also be used to recover oil and gas that could not be reached during previous

    exploration from already exploited gas and oil fields.

    There are various natural ways as well to conduct carbon sequestration. Plants act

    as a reservoir for carbon dioxide. Increasing plantation can also help in reducing

    the carbon dioxide content from the atmosphere.

    2.1.CO2 capture techniques

    2.1.1. POST COMBUSTION

    Separation of Carbon dioxide from other flue gases after combustion

    is known as Post Combustion capture. This separation can be done

    by solvent absorption or by using membrane or adsorption

    technologies.

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    Post Combustion CO2capture using special chemicals called amines

    is the most commonly used process. The CO2 rich gas (power plant

    exhaust) is passed through an amine solution. The CO2 bonds with

    amines, while other gases pass through the solution. This solution

    hence has CO2 captured and is pumped into a stripper where the

    captured CO2 is extracted. The solution containing amines can be

    recycled [7].

    2.1.2. PRE COMBUSTION

    As is the case in Post Combustion capture, Pre Combustion capture

    also has various processes like solvent absorption, adsorption and

    membrane separation.

    Once coal is gasified, the produced syngas then enters an absorption

    column. In the absorption column, the gas comes in contact with the

    solvent, which absorbs the CO2. The CO2rich solvent is pumped into

    another column known as the stripping column while the other gases

    leave out of the absorption column. CO2 is released from the solvent

    by heating it to 120C. The CO2that emerges is cooled at the top of the

    tower so as to remove traces of water and solvent. The solvent is then

    used again for the absorption process [8].

    2.1.3. OXYFUEL COMBUSTION

    Also known as oxyfiring, it is the combustion of coal in pure oxygen

    instead of air, mostly used in conventional steam generator. The CO2

    in the exhaust is highly concentrated due to the fact that no other

    gases are introduced in the combustion chamber. This method is

    relatively easy in capturing and compressing CO2, though it is still in

    testing stages [9].

    2.2.CO2 storage

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    2.2.1. STRUCTURAL STORAGE

    When CO2 is pumped underground, as it is more buoyant than water, it

    will rise up through the porous rocks. As it rises, it will eventually reach

    a layer of impermeable layer of cap-rock under which it gets trapped.

    Plugs made of steel and cement can be used to seal the holes drilled to

    pump in the CO2 [10].

    2.2.2. RESIDUAL STORAGE

    Residual rocks behave much like a tight, rigid sponge. As we know that a

    sponge has to be squeezed several times before all the air in it can be

    replaced with water. Similarly when liquid CO2 is pumped into these

    rocks, they get stuck within the pore spaces of these rocks and do not

    move [10].

    2.2.3. DISSOLUTION STORAGE

    CO2 dissolves in salty water, which makes it heavier. This water that has

    CO2 dissolved in it and is heavier than the surrounding water, sinks to

    the bottom of the rock formation [10].

    2.2.4. MINERAL STORAGE

    The salt water that has CO2 dissolved in it is weakly acidic and can react

    with surrounding minerals forming new minerals. The new minerals

    that are formed form a coating on the rocks around it. The process caneither be quick or very slow and it binds the CO2 to the rocks [10].

    2.3.Geological sites

    2.3.1. DEEP SALINE FORMATIONS

    These are underground formations of permeable reservoir rock, such as

    sandstone. The formations are covered with impermeable cap rock and

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    contain very salty inside. Only at depths below 800m, CO2 formations in

    deep saline formations are expected.

    They are widely distributed and are frequently close to concentrated

    sources of man-made CO2 emissions in cities and industrial zones. There

    is a lot of potential capacity available in saline formations across the

    world. However, a great amount of assessment work is needed to prove

    their suitability for CO2 storage.

    2.3.2. COAL SEAM

    Coal steam storage involves another form of trapping in which the

    injected CO2 accumulates on the surface of in situ coal, thereby

    displacing other gases like methane.

    Coal seam storage is considered to be feasible when undertaken with

    enhanced coalbed methane recovery where in the production of the coal

    seam methane is assisted by the injected CO2. Permeability of the coalseam also impacts the effectiveness of the technique.

    2.3.3. DEPLETED OIL AND GAS FIELDS

    Depleted oil and gas fields are geologically well defined and well

    explored. These are known to have proven ability to store hydrocarbons

    over extended periods of time (millions of years). This process is

    discussed further in detail in the following sections.

    Australia completed in 2011 all elements of its CO2 injection and

    storage framework at the federal level for offshore storage. Three of its

    states have state-level legislation in place to regulate onshore storage

    (Victoria, South Australia and Queensland), and one state (Victoria) also

    has a legislative framework for offshore CO2 storage in its jurisdiction.

    In addition, The Barrow Island Act 2003 is project-specific legislation

    that was enacted solely to regulate the CCS activities associated with the

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    Gorgon project in Western Australia. The Western Australian

    government is now in the process of developing broader CCS regulation

    through amendments to the existing Petroleum and Geothermal Energy

    Resources Act 1967, building on knowledge gained from the application

    of the Barrow Island Act. [11]

    2.4.Projects underway

    List of projects underway in Australia [12]:

    Callide Oxyfuel Project, Queensland;

    CarbonNet Project, Victoria;

    South West Hub Project, Western Australia;

    The CO2CRC Otway Project, Victoria; and

    Gorgon Project, Western Australia

    3. ENHANCED OIL RECOVERY (EOR)

    Shell has joined a research project exploring CO2-driven enhanced oil recovery

    (CO2-EOR) in the North Sea.[13]

    We anticipate significant growth in CO2 supplies available to the EOR industry.

    Overall CO2 utilisation by CO2-EOR (including both industrial and natural CO2)

    will nearly double by 2020to 6.5 bcfd by 2020 from 3.5 bcfd in 2014 [14]

    Three phases of oil production exists: primary, secondary and tertiary. EOR is the

    tertiary approach, which increases the production from a well up to 75%. Three

    main categories of EOR have been found to be of successful application:

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    http://www.globalccsinstitute.com/projects/12416http://www.globalccsinstitute.com/projects/12651http://www.globalccsinstitute.com/phttp://www.globalccsinstitute.com/projects/12646http://www.callideoxyfuel.com/What/CallideOxyfuelProject.aspx
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    Thermal Recovery To lower the viscosity and improve the ability to flow, heat

    is introduced in to the well. The introduction of heat can be done through

    injection of steam. Over 40% of US EOR production is done using this method.

    Chemical Injection In order to increase the efficiency of water flooding or to

    boost the effectiveness of surfactants, which are cleansers that help lower

    surface tension that inhibits the flow of oil through the reservoir, long chained

    polymers are introduced into the reservoir. This technique is not commonly

    used as its effectiveness is unpredictable and high costs are involved.

    Gas Injection gases such as carbon dioxide, nitrogen or natural gas, which

    expand in the reservoir, are used. The compressed gas is pumped in and once it

    expands, it either pushes the additional oil out of the wellbore or it dissolves in

    the oil, subsequently decreasing its viscosity and increasing its flow rate. This

    method is widely used as CO2 is readily available and it is cost effective. Nearly

    60% of the US EOR production is done by this method.

    Fig 3. Schematic diagram of CO2-Enhanced Oil Recovery (Source: http://www.worldcoal.org/

    coal-the-environment/carbon-capture-use--storage/ccs-technologies/ccs-technologies-more/)

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    The gas injection method discussed above is used for two benefits at the same

    time. It helps in storing carbon dioxide while recovering the otherwise hard-to-

    recover oil. Once all the oil is recovered and the well is filled up with carbon

    dioxide, it can be sealed and it is sure to stay there for a significant period of time.

    4. TRIGENERATION SYSTEMS

    Trigeneration systems or CCHP (Combined Cooling, Heating and Power) systems

    are those which produce electricity, heating and cooling from a single source of

    fuel. These primarily consist of a prime mover running on a conventional fuel,

    electric generator, a heat recovery system and an absorption chiller for cooling

    needs.

    4.1. Prime mover

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    Power System Electricity

    Heat Recovery

    Thermally driven

    refrigeration

    Heating

    Cooling/

    refrigeration

    Fuel

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    A prime mover is what drives a trigeneration system. It converts fuels

    energy to useful mechanical work. Following is a comparison of various

    prime mover technologies available which are primarily divided into two

    categories, combustion based and electrochemical based. Some of the

    technologies like reciprocating engines and gas turbines are in a mature

    stage and widely available, while others are relatively new and in

    development stage.

    Table 1. Comparison of different trigeneration prime movers [15]

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    4.1.1. GAS POWERED PRIME MOVER

    Considering all the above criterions and feasibility, for our analysis

    gas powered prime mover is chosen. Though fuel cells have better

    part load efficiencies, higher lifetimes and low noise levels, gas

    turbines are a better option as they have higher capacities along with

    lower investment costs, lower footprints and comparable efficiency.

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    Also, the lack of maturity of fuel cell technology makes gas turbine

    an ideal choice.

    Table 2. Key performance parameters and cost estimates [16]

    A gas turbine CCHP consists usually of a generator, compressor and

    turbine connected by a shaft, combustion chamber, recuperator and

    an absorption chiller [17]. A heat recovery system is used to recover

    heat from the hot exhaust gas. For different commercial and

    industrial applications, various gas turbine systems ranging from

    several hundred kilowatts to several hundred megawatts are

    available. To serve small scale applications, recently, micro turbines

    have also been developed which put out 30 - 400 kW [18]. Systems,

    using regenerative Brayton cycle and high speed centrifugal turbo

    machines are considered as potential alternatives to the conventional

    ICE systems, especially for small scale applications [17]. Gas turbines

    are more compact and require less maintenance compared to ICE

    based systems. Hot gases released from gas turbines at 250C can

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    easily drive thermally activated cooling technologies like absorption

    chillers [19].

    4.2.Cooling technologies

    Of all the cooling technologies, absorption cooling is mature and well-

    established. It has been in use for many years now in numerous cooling and

    air conditioning applications. An absorber, generator, condenser and

    evaporator are the four main components that make up an absorption

    cycle. Absorption cycle uses the heat supplied to compress the refrigerant

    vapour while conventional systems would use a rotating device or

    compressor. Based on the number of times the heat is utilised within the

    system, absorption cooling systems are classified in to single effect, double

    effect and triple effect systems. Lithium bromide-water and water-

    ammonia are the most commonly used working fluids.

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    5. CONCLUSION

    The future of our electricity generation does not depend only on the above

    mentioned technologies. The technologies discussed above concentrate of

    removal of existing carbon dioxide and reduction of emissions immediately.

    Carbon capture and storage is of prime importance as we already have critical

    amounts of carbon dioxide in our atmosphere which needs to be removed in order

    to avert from the extreme consequences of global warming.

    Carbon capture and storage alone is not enough as we do not have long supplies of

    fossil fuels remaining. Focus also has to shift towards developing renewable

    technologies which will be the future. Wind, geothermal and solar energy is most

    abundant in Australia and it could hold the key to the future of our electricity

    needs if economical electricity transportation methods are developed.

    Nuclear energy is also a reliable option for a country like Australia. Australia

    possesses vast amounts of barren flat land which are calamity free and ideal for

    nuclear plants. The biggest advantage of nuclear energy is the fact that Australia

    has substantial Uranium resources, all of which it currently exports.

    In conclusion, the future lies in a balanced use of all the available technologies

    and also government policies.

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    6. REFERENCES

    1. Statistical Review of World Energy 2013. Available from: http://www.bp.com/content/dam/bp/excel/Energy-Economics/statistical_review_of_world_energy_2013_workbook.xlsx.

    2. Statistical Review of World Energy 2013. 2013; Available from: http://www.bp.com/content/dam/bp/pdf/statistical-review/statistical_review_of_world_energy_2013.pdf.

    3. 2013 Australian Energy Update - July 2013, BREE, Editor. 2013.

    4. Energy Charting Tool. [cited 2014; Available from: http://www.bp.com/en/global/corporate/about-bp/energy-economics/statistical-review-of-world-energy-2013/energy-charting-tool.html.

    5. Stephan, A. and R.H. Crawford, A multi-scale life-cycle energy and greenhouse-gasemissions analysis model for residential buildings. Architectural Science Review, 2013.57(1): p. 39-48.

    6. Power Generation from Coal - Measuring and Reporting Efficiency Performance and CO2Emissions. 2010; Available from: http://www.iea.org/publications/freepublications/publication/power_generation_from_coal.pdf.

    7. POST-COMBUSTION CAPTURE OF CARBON DIOXIDE. Available from: http://www.co2crc.com.au/dls/factsheets/Post_comb_Solvent.pdf.

    8. PRE-COMBUSTION CAPTURE OF CARBON DIOXIDE. Available from: http:// www.co2crc.com.au/dls/factsheets/Pre-comb_Solvent.pdf.

    9. About CCS. Available from: http://www.co2crc.com.au/aboutccs/capture.

    10. Carbon Capture & Storage Technologies. Available from: http://www.worldcoal.org/coal-the-environment/carbon-capture-use--storage/ccs-technologies/ccs-technologies-more/.

    11. Technology Roadmap Carbon capture and storage. Available from: http://www.iea.org/publications/freepublications/publication/TechnologyRoadmapCarbonCaptureandStorage.pdf.

    12. CCS in Australia. Available from: http://www.globalccsinstitute.com/location/australia.

    13. Shell joins carbon capture project. 2014.

    14. Oil and Gas journal. Available from: http://www.ogj.com/articles/print/volume-112/issue-5/drilling-production/co-sub-2-sub-eor-set-for-growth-as-new-co-sub-2-sub-supplies-emerge.html.

    15. Jradi, M. and S. Riffat, Tri-generation systems: Energy policies, prime movers, coolingtechnologies, configurations and operation strategies. Renewable and Sustainable EnergyReviews, 2014. 32(0): p. 396-415.

    16. Gas Market Report, October 2013. BREE.

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    17. Arteconi, A., C. Brandoni, and F. Polonara, Distributed generation and trigeneration: Energy

    saving opportunities in Italian supermarket sector. Applied Thermal Engineering, 2009.29(8-9): p. 1735-1743.

    18. Gu, Q., et al., Integrated assessment of combined cooling heating and power systems underdifferent design and management options for residential buildings in Shanghai. Energyand Buildings, 2012. 51: p. 143-152.

    19. Li, H., et al., Energy utilization evaluation of CCHP systems. Energy and Buildings, 2006.38(3): p. 253-257.

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