DOCSLIB.ORG

'Retrofitting CCS to Coal: Enhancing Australia's Energy

Total Page：16

File Type：pdf, Size：1020Kb

Download full-text PDF Read full-text
'Retrofitting CCS to Coal: Enhancing Australia's Energy RETROFITTING CCS TO COAL: ENHANCING AUSTRALIA’S ENERGY SECURITY RETROFITTING CCS TO COAL: ENHANCING AUSTRALIA’S ENERGY SECURITY any representation about the content and suitability Disclaimer of this information for any particular purpose. The document is not intended to comprise advice, and is This report was completed on 2 March 2017 and provided “as is” without express or implied therefore the Report does not take into account warranty. Readers should form their own conclusion events or circumstances arising after that time. The as to its applicability and suitability. The authors Report’s authors take no responsibility to update the reserve the right to alter or amend this document Report. without prior notice. The Report’s modelling considers only a single set of Authors: Geoff Bongers, Gamma Energy Technology input assumptions which should not be considered Stephanie Byrom, Gamma Energy Technology entirely exhaustive. Modelling inherently requires Tania Constable, CO2CRC Limited assumptions about future behaviours and market interactions, which may result in forecasts that deviate from actual events. There will usually be About CO2CRC Limited: differences between estimated and actual results, CO2CRC Limited is Australia’s leading CCS research because events and circumstances frequently do not organisation, having invested $100m in CCS research occur as expected, and those differences may be over the past decade. CO2CRC is the first organisation material. The authors of the Report take no in Australia to have demonstrated CCS end-to-end, responsibility for the modelling presented to be and has successfully stored more than 80,000 tonnes considered as a definitive account. of CO2 at its renowned Otway Research Facility in The authors of the Report highlight that the Report, Victoria. CO2CRC engages the world’s leading does not constitute investment advice or a researchers to collaborate on benchtop and in-field recommendation to you on your future course of research in Australia, delivering improvements and action. The authors provide no assurance that the cost efficiencies in CCS to industry. scenarios modelled will be accepted by any relevant www.co2crc.com.au authority or third party. About Gamma Energy Technology: Conclusions in the report are based, in part, on the Gamma Energy Technology is an independent assumptions stated and on information which is energy consulting service, offering a range of publicly available. No listed author, company or technical and support services, including but not supporter of this report, nor any member or limited to power generation technology. employee thereof undertakes responsibility in any way whatsoever to any person in respect of errors in Gamma Energy Technology are proud to contribute this Report arising from information that may be to the ongoing discussions on energy in Australia as later be proven to be incorrect. we seek to solve the trilemma of energy supply - to assure energy system security and affordability so In the preparation of this Report the authors have that emissions reduction targets are delivered. considered and relied upon information sourced www.gamma-energy-technology.com.au from a range of sources believed after due enquiry to be reliable and accurate. The authors have no reason to believe that any information supplied, or Acknowledgements obtained from public sources, was false or that any material information has been withheld. The authors would like to thank EPRI for their support as an extension to the APGT and for their The authors do not imply and it should not be advice and data. Confidential soundings were taken construed that they have verified any of the from Industry. We would like to thank ACALET and information provided, or that the author’s enquiries CarbonNet for their advice for this report. The CCS could have identified any matter which a more transport and storage chapter from the APGT has extensive examination might disclose. been recreated for this document. The authors While every effort is made by the authors to ensure acknowledge chapter authors Prof. D. Wiley and Dr that the facts and opinions contained in this M.Ho (University of Sydney), Dr P. Neal and Dr G document are accurate, the authors do not make Fimbres Weihs (UNSW) and peer reviewers named in the Chapter. RETROFITTING CCS TO COAL: ENHANCING AUSTRALIA’S ENERGY SECURITY Table of Contents Key Messages ..........................................................................................................................................v Executive Briefing .................................................................................................................................. vi International Climate Change Commitments................................................................................................. vi Diversity of Electricity Supply....................................................................................................................... vii New Technologies Will Cost More ................................................................................................................ vii CCS is Not Experimental ................................................................................................................................ ix Enhancing Energy Security ............................................................................................................................. ix Retrofit Costs are Comparable with Solar PV ................................................................................................. ix Benefits to Other Industries........................................................................................................................... x Jobs in Regions ............................................................................................................................................... xi Planning for a Sustainable Energy Future ...................................................................................................... xi Conclusion ..................................................................................................................................................... xi 1.0 Introduction ................................................................................................................................... 1 1.1. What is Post-Combustion Capture and Retrofitting ............................................................................. 1 1.2. Plant equipment and layout................................................................................................................. 3 1.3. Integration of PCC into existing Coal Plant ........................................................................................... 4 2.0 Case studies ................................................................................................................................... 6 2.1. Key CCS projects to date in Australia ................................................................................................ 6 2.2. Opportunities for Australia ............................................................................................................... 7 2.3. Key International Commercial CCS projects to date ......................................................................... 8 2.3.1. SaskPower Boundary Dam, Canada - CCS Project ........................................................................... 8 2.3.2. Petra Nova, USA - Carbon Capture Project .................................................................................. 10 3.0 PCC Retrofit ................................................................................................................................. 12 3.1. Brown Coal PCC Retrofit Cost and Performance ............................................................................. 12 3.2. Brown Coal PCC Retrofit Cost of Electricity ..................................................................................... 13 3.3. Black Coal PCC Retrofit Cost and Performance ............................................................................... 16 3.4. Black Coal PCC Retrofit Cost of Electricity ....................................................................................... 17 3.5. Retrofit Summary ............................................................................................................................ 20 Appendix 1 – CO2 Transport and Storage Case Studies ............................................................................. 22 Tables and Figures List of Figures Figure 1: PCC simplified process ......................................................................................................................... 2 Figure 2: Chemical solvent scrubbing process .................................................................................................... 2 Figure 3: MEA PCC unit (excluding flue gas desulphurisation and selective catalytic reduction and cooling towers) ............................................................................................................................................................... 3 Figure 4: Typical pulverised coal plant layout before and after PCC retrofit ...................................................... 4 Figure 5: Schematic of turbine and feedwater heater circuit for plant without CO2 capture ............................. 5 Page iii RETROFITTING CCS TO COAL: ENHANCING AUSTRALIA’S ENERGY SECURITY Figure 6: Schematic
Load more

Recommended publications
  • Update on Lignite Firing
    Update on lignite firing Qian Zhu CCC/201 ISBN 978-92-9029-521-1 June 2012 copyright © IEA Clean Coal Centre Abstract Low rank coals have gained increasing importance in recent years and the long-term future of coal -derived energy supplies will have to include the greater use of low rank coal. However, the relatively low economic value due to the high moisture content and low calorific value, and other undesirable properties of lignite coals limited their use mainly to power generation at, or, close to, the mining site. Another important issue regarding the use of lignite is its environmental impact. A range of advanced combustion technologies has been developed to improve the efficiency of lignite-fired power generation. With modern technologies it is now possible to produce electricity economically from lignite while addressing environmental concerns. This report reviews the advanced technologies used in modern lignite-fired power plants with a focus on pulverised lignite combustion technologies. CFBC combustion processes are also reviewed in brief and they are compared with pulverised lignite combustion technologies. Acronyms and abbreviations CFB circulating fluidised bed CFBC circulating fluidised bed combustion CFD computational fluid dynamics CV calorific value EHE external heat exchanger GRE Great River Energy GWe gigawatts electric kJ/kg kilojoules per kilogram kWh kilowatts hour Gt billion tonnes FBC fluidised bed combustion FBHE fluidised bed heat exchanger FEGT furnace exit gas temperature FGD flue gas desulphurisation GJ
    [Show full text]
  • Solutions for Energy Crisis in Pakistan I
    Solutions for Energy Crisis in Pakistan i ii Solutions for Energy Crisis in Pakistan Solutions for Energy Crisis in Pakistan iii ACKNOWLEDGEMENTS This volume is based on papers presented at the two-day national conference on the topical and vital theme of Solutions for Energy Crisis in Pakistan held on May 15-16, 2013 at Islamabad Hotel, Islamabad. The Conference was jointly organised by the Islamabad Policy Research Institute (IPRI) and the Hanns Seidel Foundation, (HSF) Islamabad. The organisers of the Conference are especially thankful to Mr. Kristof W. Duwaerts, Country Representative, HSF, Islamabad, for his co-operation and sharing the financial expense of the Conference. For the papers presented in this volume, we are grateful to all participants, as well as the chairpersons of the different sessions, who took time out from their busy schedules to preside over the proceedings. We are also thankful to the scholars, students and professionals who accepted our invitation to participate in the Conference. All members of IPRI staff — Amjad Saleem, Shazad Ahmad, Noreen Hameed, Shazia Khurshid, and Muhammad Iqbal — worked as a team to make this Conference a success. Saira Rehman, Assistant Editor, IPRI did well as stage secretary. All efforts were made to make the Conference as productive and result oriented as possible. However, if there were areas left wanting in some respect the Conference management owns responsibility for that. iv Solutions for Energy Crisis in Pakistan ACRONYMS ADB Asian Development Bank Bcf Billion Cubic Feet BCMA
    [Show full text]
  • Carbon Footprint for Mercury Capture from Coal-Fired Boiler Flue Gas
    energies Article Carbon Footprint for Mercury Capture from Coal-Fired Boiler Flue Gas Magdalena Gazda-Grzywacz 1,* , Łukasz Winconek 2 and Piotr Burmistrz 1 1 Faculty of Energy & Fuels, AGH University of Science and Technology, Mickiewicz Avenue 30, 30-059 Krakow, Poland; [email protected] 2 Grand Activated Sp. z o.o., Białostocka 1, 17-200 Hajnówka, Poland; [email protected] * Correspondence: [email protected] Abstract: Power production from coal combustion is one of two major anthropogenic sources of mercury emission to the atmosphere. The aim of this study is the analysis of the carbon footprint of mercury removal technologies through sorbents injection related to the removal of 1 kg of mercury from flue gases. Two sorbents, i.e., powdered activated carbon and the coke dust, were analysed. The assessment included both direct and indirect emissions related to various energy and material needs life cycle including coal mining and transport, sorbents production, transport of sorbents to the power plants, and injection into flue gases. The results show that at the average mercury concentration in processed flue gasses accounting to 28.0 µg Hg/Nm3, removal of 1 kg of mercury from flue gases required 14.925 Mg of powdered activated carbon and 33.594 Mg of coke dust, respec- tively. However, the whole life cycle carbon footprint for powdered activated carbon amounted to −1 89.548 Mg CO2-e·kg Hg, whereas for coke dust this value was around three times lower and −1 amounted to 24.452 Mg CO2-e·kg Hg. Considering the relatively low price of coke dust and its lower impact on GHG emissions, it can be found as a promising alternative to commercial powdered Citation: Gazda-Grzywacz, M.; activated carbon.
    [Show full text]
  • Appendix A: Calculation of Flue Gas Composition
    Appendix A: Calculation of Flue Gas Composition Consider 100 kg of biomass (pine wood) with an Ultimate Analysis on a dry ash free basis given in Table A.1. This calculation assumes that all the carbon is burned i.e. there is no carbon in the ash or carbon monoxide formed. If there is the unburned carbon has to be sub- tracted from the value of carbon in the above table. Also that the S, N and Cl are negligible and there is no ingress of N2 in the flue or sampling system. Moisture content given in the Proximate Analysis has to be allowed for in the calculation as well. Assume the combustion reactions are C + O2 = CO2 2H2 + O2 = 2H2O Oxygen required for stoichiometric combustion = 4.33 + 1.6 − 1.3 = 4.63kg-mol Air requirement = [4.63 × 100 × 22.41 ]/[ 21]=494.1 m3 at NTP Composition of the dry flue gas from the stoichiometric combustion of 1 kg of biomass: 3 N2 from theoretical air 4.94 0.79 3.90 m . = × = 3 N2 from biomass 0.001 0.224 0.0002 m . = × = 3 CO2 from biomass 4.33 0.224 0.97 m . Total amount of dry= flue gas× per 1 kg= wood 4.872 m3. = If the concentration in the wet flue gas is required then the water content has to be included in the above calculation. © The Author(s) 2014 105 J.M. Jones et al., Pollutants Generated by the Combustion of Solid Biomass Fuels, SpringerBriefs in Applied Sciences and Technology, DOI 10.1007/978-1-4471-6437-1 106 Appendix A: Calculation of Flue Gas Composition Table A.1 Calculation of Element Molecular weight Mols O2 required flue gas composition C, 52.00 12 4.33 H, 6.20 2 1.6 O, 41.60 32 1.3 − N, 0.2 28 Therefore % CO 0.97/4.872 19.91 assuming stoichiometric combustion (0 % 2 = = O2).
    [Show full text]
  • COAL CONFERENCE University of Pittsburgh · Swanson School of Engineering ABSTRACTS BOOKLET
    Thirty-Fifth Annual INTERNATIONAL PITTSBURGH COAL CONFERENCE University of Pittsburgh · Swanson School of Engineering ABSTRACTS BOOKLET Clean Coal-based Energy/Fuels and the Environment October 15-18, 2018 New Century Grand Hotel Xuzhou Hosted by: The conference acknowledges the support of Co-hosted by: K. C. Wong Education Foundation, Hong Kong A NOTE TO THE READER This Abstracts Booklet is prepared solely as a convenient reference for the Conference participants. Abstracts are arranged in a numerical order of the oral and poster sessions as published in the Final Conference Program. In order to facilitate the task for the reader to locate a specific abstract in a given session, each paper is given two numbers: the first designates the session number and the second represents the paper number in that session. For example, Paper No. 25.1 is the first paper to be presented in the Oral Session #25. Similarly, Paper No. P3.1 is the first paper to appear in the Poster Session #3. It should be cautioned that this Abstracts Booklet is prepared based on the original abstracts that were submitted, unless the author noted an abstract change. The contents of the Booklet do not reflect late changes made by the authors for their presentations at the Conference. The reader should consult the Final Conference Program for any such changes. Furthermore, updated and detailed full manuscripts, published in the Conference Proceedings, will be sent to all registered participants following the Conference. On behalf of the Thirty-Fifth Annual International Pittsburgh Coal Conference, we wish to express our sincere appreciation and gratitude to Ms.
    [Show full text]
  • Identification and Selection of Major Carbon Dioxide Stream Compositions
    PNNL-20493 Prepared for the U.S. Department of Energy under Contract DE-AC05-76RL01830 Identification and Selection of Major Carbon Dioxide Stream Compositions GV Last MT Schmick June 2011 PNNL-20493 Identification and Selection of Major Carbon Dioxide Stream Compositions GV Last MT Schmick June 2011 Prepared for the U.S. Department of Energy under Contract DE-AC05-76RL01830 Pacific Northwest National Laboratory Richland, Washington 99352 Abstract A critical component in the assessment of long-term risk from geologic sequestration of carbon dioxide (CO2) is the ability to predict mineralogical and geochemical changes within storage reservoirs as a result of rock-brine-CO2 reactions. Impurities and/or other constituents in CO2 source streams selected for sequestration can affect both the chemical and physical (e.g., density, viscosity, interfacial tension) properties of CO2 in the deep subsurface. The nature and concentrations of these impurities are a function of both the industrial source(s) of CO2, as well as the carbon capture technology used to extract the CO2 and produce a concentrated stream for subsurface injection and geologic sequestration. This report summarizes the relative concentrations of CO2 and other constituents in exhaust gases from major non-energy-related industrial sources of CO2. Assuming that carbon capture technology would remove most of the incondensable gases N2, O2, and Ar, leaving SO2 and NOx as the main impurities, the authors of this report selected four test fluid compositions for use in geochemical experiments. These included the following: 1) a pure CO2 stream representative of food-grade CO2 used in most enhanced oil recovery projects; 2) a test fluid composition containing low concentrations (0.5 mole %) SO2 and NOx (representative of that generated from cement production); 3) a test fluid composition with higher concentrations (2.5 mole %) of SO2; and 4) test fluid composition containing 3 mole % H2S.
    [Show full text]
  • Experience from Post-Combustion Capture Pilot Plant Operations in Australia
    1st Post Combustion Capture Conference Experience from post-combustion capture pilot plant operations in Australia A. Cottrella*, P.H.M. Ferona aCoal Technology Portfolio, CSIRO Energy Technology, Newcastle, Australia Australia is highly dependent on coal for power generation and also for income and job creation through its significant exports. With this it is essential that Australia has an active program for investigating the implementation of coal combustion CO2 reduction technologies. CSIRO is a national, government funded research organization that has been tasked with challenge of addressing the issues associated with the reduction of CO2 emissions through application of post- combustion capture technologies for coal fired power stations. PCC program at CSIRO investigates many aspects of the technology and part of that has been through construction and operation of three PCC pilot plants located at Australian power station sites treating real flue gas. This paper will discuss learnings that have come from the operation of the plants. Australia is highly dependent on coal for power generation and also income and job creation through its significant exports. With this it is essential that Australia has an active program for investigating the implementation of CO2 reduction technologies as a result of the combustion of coal. CSIRO is a national, government funded research organization that has been tasked with challenge of addressing the issues associated with the reduction of CO2 emissions through application of post-combustion capture technologies for coal fired power stations. PCC program at CSIRO investigates many aspects of the technology and part of that has been through construction and operation of three PCC pilot plants located at Australian power station sites treating real flue gas.
    [Show full text]
  • Chapter 2 Flue Gases and Fuel Gases
    Zevenhoven & Kilpinen FLUE GASES and FUEL GASES 19.6.2001 2-1 Chapter 2 Flue gases and fuel gases 2.1 Introduction Combustion processes for heat and power generation and the incineration of household waste generate gaseous “by-products” that are virtually useless when their temperature is below, say, 200EC. By means of a stack of sufficient height these can be dispersed into the atmosphere without much effect to the environment at short range. At the same time the mere presence of a stack indicates that there must be reasons for actively transporting the gases away from the facilities that generate them. These reasons are that the temperature, and, more importantly, the composition of the gases are different from those of the ambient atmosphere at ground-level. The formation of ground-level ozone from traffic exhaust gases during sunny summer days is a good example of what happens when large amounts of flue gases are released at ground-level. Flue gases from combustion facilities have a composition very different from air because of high concentrations of the combustion products water (H2O) and carbon dioxide (CO2). More concern, however, goes to what is in these gases besides these bulk species, such as oxides of sulphur and nitrogen, fine dust, trace elements such as mercury and nickel, and super-toxics such as dioxins. All these compounds are actually unwanted by-products from a power plant or a waste incinerator, since the first has the objective to convert hydrocarbon fuels (CxHy) into CO2, H2O plus heat and power, whilst the second aims at reducing a large volume of solid or liquid waste into a small amount of solid ashes plus, again, CO2 and H2O from the combustion of the organic compounds.
    [Show full text]
  • Removal of CO2 from Flue Gas at High Temperature Using
    View metadata, citation and similar papers at core.ac.uk brought to you by CORE provided by Archivio della Ricerca - Università di Pisa 139 A publication of CHEMICAL ENGINEERING TRANSACTIONS VOL. 47, 2016 The Italian Association of Chemical Engineering Online at www.aidic.it/cet Guest Editors: Angelo Chianese, Luca Di Palma, Elisabetta Petrucci, Marco Stoller Copyright © 2016, AIDIC Servizi S.r.l., ISBN 978-88-95608-38-9; ISSN 2283-9216 DOI: 10.3303/CET1647024 Removal of CO from Flue Gas at High Temperature 2 Using Novel Porous Solids Monica Puccini*, Eleonora Stefanelli, Maurizia Seggiani, Sandra Vitolo Department of Civil and Industrial Engineering, University of Pisa, Largo Lucio Lazzarino 1, 56122 Pisa, Italy [email protected] Since the CO2 separation is the first and most energy intensive step of carbon capture and storage (CCS) technology, many research have targeted at improving the current technologies or developing new approaches of CO2 separation and capture. In this study, lithium orthosilicate-based pellets were developed and characterized as potential regenarable high-temperature CO2 sorbents. A mechanical method was used for pelletization of the powdered materials, namely K2CO3-doped lithium silicate (Li4SiO4). For increasing the performance of the pellets over multiple cycles an activation strategy was applied: the powdered sorbents were pelletized with a binder for enhancing their porosity by applying a thermal activation before adsorption process. Different amounts of binders (layered graphite and carbon nanotubes) were added to powered doped-sorbent in order to identify the optimal amount to ensure an adequate porosity into the pellets. The CO2 sorption properties of the obtained pellets were investigated by using a thermal gravimetric analyzer (TGA) in a controlled gas flow environment at low CO2 partial pressure (0.04 atm).
    [Show full text]
  • COAL-FIRED GENERATION: Proven and Developing Technologies
    COAL-FIRED GENERATION: Proven and Developing Technologies Brenda Buchan Christi Cao Office of Market Monitoring and Strategic Analysis Florida Public Service Commission December 2004 COAL-FIRED GENERATION: Proven and Developing Technologies INTRODUCTION The topic of coal-fired generation is appearing more frequently in the media and particularly within energy publications. This is a change from the past decade when most of the energy industry’s attention was on natural gas and the inexpensive, clean, and efficient combined cycle electric generators that burn natural gas. The returning interest to coal-fired generation is based on several factors, including: z U.S. Department of Energy (DOE) funding of new technologies to burn coal more cleanly, z High prices for natural gas as compared to coal, z Increase in demand worldwide for natural gas, z Large supply of coal in the United States, and z Government instability in some countries providing natural gas and oil resources. With these events occurring simultaneously, it is not surprising that the energy industry in the United States is once again taking a close look at coal-fired power plants. In this paper we discuss various technologies that have been developed over the past couple of decades to produce coal-fired energy with fewer air emissions and the clean coal technologies that are under development. We also examine counter-balancing issues behind coal-fired generation. Economic drivers motivating utilities and governments to invest in coal must be balanced with the environmental concerns associated with coal-burning emissions. We also discuss the investment in and use of clean coal technologies in Florida.
    [Show full text]
  • GR910 Graphite 10 Handbook
    Graphite Instruction Manual Graphite 10 Model GR910 Free-standing Multi Fuel Non-Boiler Stove Published August 2014 Please note This appliance must, at all times, be operated in accordance with the instructions to minimise the amount of smoke produced. You will need to refer to the serial number of your stove should you ever need to make a claim under the Graphite Warranty. You will find the serial number, beginning with GR, on the CE plate at the rear of the stove as well as on the lid of the outer packaging. Write the date the stove was delivered to you below as this is likely to differ from the purchase date. - - www.hi-flame.com Ref: GR910 / UK-NI-ROI / V4-05-07-14 CONTENTS Page Graphite Standard Features 3 General Dimensions 4 Technical Data 5 CPR Declaration of Performance 5 Model Graphite 10 Introduction 6 GR910 Packing List 6 Free-standing Installation Regulations 7 Multi Fuel Non-Boiler Important Safety Advice 8 Stove Assembling the Stove 9 Flue Options 10 Smoke Control Areas 12 Recommended Fuels 13 Prohibited Fuels 14 Understanding Fuel Types 15 Important: First Fires 15 Burning Wood Logs 16 Burning Mineral Fuels 20 Some Simple Tips 21 Removing Ash 22 Installation Check-list 23 Installation General Guidelines 24 PLEASE NOTE Commissioning 28 This instruction manual is also used for Trouble-shooting 28 a number of other stove models in the Routine Checks 33 Hi-Flame product range and therefore Standing Down 33 some of the stove photographs and diagrams used, which are used for Routine Maintenance 34 guidance purposes only, may differ Annual Service 36 slightly from your new Graphite stove.
    [Show full text]
  • Full-Scale Tests on the Co-Firing of Peat and Oil Shale in an Oil Shale Fired Circulating Fluidized Bed Boiler
    Oil Shale, 2017, Vol. 34, No. 3, pp. 250–262 ISSN 0208-189X doi: https//doi.org/10.3176/oil.2017.3.04 © 2017 Estonian Academy Publishers FULL-SCALE TESTS ON THE CO-FIRING OF PEAT AND OIL SHALE IN AN OIL SHALE FIRED CIRCULATING FLUIDIZED BED BOILER TÕNU PIHU(a)*, ALAR KONIST(a), DMITRI NESHUMAYEV(a), LAURI LOO(a), ARTJOM MOLODTSOV(b), ALEKSANDR VALTSEV(b) (a) Department of Energy Technology, Tallinn University of Technology, Ehitajate tee 5, 19086 Tallinn, Estonia (b) Enefit Energiatootmine AS, Elektrijaama tee 59, 40101 Auvere, Vaivara vald, Ida-Virumaa, Estonia Abstract. The paper presents analysis of data obtained from tests of oil shale (OS) and peat co-combustion in a full-scale 250 MWth (useful heat output) circulating fluidized bed (CFB) boiler. The tests were conducted at nominal boiler load, with peat thermal input up to 30%. During the experiments, gas analysis was performed and ash samples were collected. The specific con- sumption of the oil shale and peat blend per useful heat and gross electricity was calculated and other techno-economic characteristics were determined. It was found that the co-combustion of oil shale and wet peat increased the CO emission to the level of 60 mg/Nm3. The NOx concentration increased 3 from 120 to 165 mg/Nm . The SO2 and HCl emissions remained at a very low level – below 20 mg/Nm3. A significant ash reduction, approximately 4%, was measured in the case of a 30% peat content. Due to the high peat moisture, the flue gas volume increased 5–10%. As a result of addition of peat, the content of particulate matter (PM) 10/2.5 was also lower than that by conventional oil shale CFB firing.
    [Show full text]