연구동향 분석
박사

연소시스템 효율향상을 위한 연소생성물 타르의 생성기작규명

어승희 2016년

논문상세정보
    • 저자 어승희
    • 기타서명 A Study on Tar Fouling Mechanism to Improve the Combustion System Efficiency
    • 형태사항 26 cm: xvi, 172 p. :: 삽도
    • 일반주기 강원대학교 논문은 저작권에 의해 보호받습니다, 지도교수 : 김대현, 참고문헌 : p.154-169
    • 학위논문사항 학위논문(박사)-, 바이오시스템공학과, 강원대학교 대학원, 2016. 2
    • KDC 6, 530.263
    • 발행지 춘천
    • 언어 kor
    • 출판년 2016
    • 발행사항 강원대학교
    • 주제어 목재펠릿보일러 연소생성물 타르 타르생성기작
    유사주제 논문( 6)
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' 연소시스템 효율향상을 위한 연소생성물 타르의 생성기작규명' 의 주제별 논문영향력
논문영향력 선정 방법
논문영향력 요약
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  • 530.263
  • 목재펠릿보일러
  • 연소생성물 타르
  • 타르생성기작
동일주제 총논문수 논문피인용 총횟수 주제별 논문영향력의 평균
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' 연소시스템 효율향상을 위한 연소생성물 타르의 생성기작규명' 의 참고문헌

  • 최신 연소공학
    김광렬 김영주 노수영 도서출판 동화기술 [1999]
  • 연소공학
    송규근 최병철 청문각 [2007]
  • 연소공학
    안수길 채재우 홍명석 원창출판사 [1998]
  • 에너지관리공단 신 재생에너지센터
    년 신 재생에너지 보급통 계.http://www.knrec.or.kr/ [2014]
  • 에너지관리공단
    신 재생에너지 RD&D 전략 2030시리즈 바이오(목 질계),5 [2008]
  • 신 재생에너지관련 법,기본계획,정책 및 제도
    최보선 2014년 신 재생에너지 백서.http://www.knrec.or.kr/ [2014]
  • 신 재생에너지 자원잠재량 및 기술개발
    윤창열 최창기 2014년 신 재생에너지 백서.http://www.knrec.or.kr/ [2014]
  • 신 재생에너지 원별 기술동향 -재생에너지 바이오
    이진석 2014년 신 재생에너지 백서.http://www.knrec.or.kr/ [2014]
  • 산림청
    http://www.forest.go.kr/ [2013]
  • 보일러의 수종별 벌채부산물을 이용한 연소특성 분석
    김대현 목재펠릿 오재헌 최윤성 한국산림휴양학회 년 산림과학 공동학술대회, 889-892 [2013]
  • 바이오-폐기물 발전 전략보고서
    한국에너지기술평가원 http://www.ketep.re.kr/ [2012]
  • 목질바이오매스
  • 목질계 바이오매스의 에너지 활용방안
    김인숙 소현정 이정임 경기개발연구원,정 책연구 2009-35,12. [2009]
  • 목재펠릿보일러의 연료공급 장치의 형태에 따른 연소특성에 관한 연구
    김대현 어승희 오광철 오재헌 최윤성 에너지 공학,24(2):120-128 [2015]
  • 목재펠릿 연소 시 발생하는 타르 , 재, 클링커 생성 특성 분석 및 함수율 변화에 따른 목재펠릿보일러의 성능 연구
  • 리튬브로마이드(LiBr)수용 액을 활용한 온실 제습을 위한 연구
    강상묵 김대현 어승희 우종철 이정빈 강원 농업생명환경연구,24(2): 24-29 [2012]
  • 농림축산식품부
    http://www.mafra.go.kr/ [2015]
  • 국내 에너지 현황 및 전망
    부경진 2014년 신 재생에너지 백서. http://www.knrec.or.kr/ [2014]
  • ㈜규원에너지
    http://www.kyuwontech.co.kr/ [2015]
  • 「목재펠 릿 규격 품질기준」
    국립산림과학원(KoreaForestResearch Institute,KFRI) [2013]
  • 「목재칩 규격 품질기준」
    국립산림과학원(KoreaForestResearch Institute,KFRI) [2013]
  • 「목재브 리켓 규격 품질기준」
    국립산림과학원(Korea ForestResearch Institute,KFRI) [2013]
  • ŚwierczyńskiD.,Libs S.,Courson C.,Kiennemann A.,2007.Steam reforming oftarfrom a biomassgasification processoverNi/olivine catalystusing toluene as a modelcompound.Applied Catalysis B: Environmental,74(3):211-222.
  • ŚwierczynskiD.,Courson C.,Kiennemann A.,2008.Study ofsteam reforming oftoluene used as modelcompound oftar produced by biomass gasification.ChemicalEngineering and Processing:Process Intensification,47(3):508-513.
  • t검정(t-test).교육평가용어사전
    송인섭 한국교육평가학회 [2004]
  • YuH.,ZhangZ.,LiZ.,ChenD.,2014.Characteristicsoftarformation during cellulose, hemicellulose and lignin gasification. Fuel: 118, 250-256.
  • Yoon S.J.,Son Y.I.,Kim Y.K.,Lee J.G.,2009.Removaloftarand sootinthesyngasproducedfrom gasificationofwoodchipby using catalyticreformer.Trans.oftheKorean Hydrogen and New Energy Society,20(6):519-525.
  • Yang H.,YanR.,Chen H.,LeeD.H.,Zheng C.,2007.Characteristics of hemicellulose, cellulose and lignin pyrolysis. Fuel, 86(12): 1781-1788.
  • Watkinson A.P., Wilson D.I., 1997. Chemical reaction fouling: A review.ExperimentalThermalandFluidScience,14(4):361-374.
  • Wang Y.,KinoshitaC.M.,1993.Kineticmodelofbiomassgasification. SolarEnergy,51(1):19-25.
  • Vıˆjeu R.,Gerun L.,Tazerout M.,Castelain C.,Bellettre J.,2008. Dimensionalmodelling of wood pyrolysis using a nodalapproach. Fuel,87(15):3292-3303.
  • VuthaluruH.B.,VuthaluruR.,2010.Controlofashrelatedproblemsin a large scale tangentially fired boilerusing CFD modelling.Applied Energy,87(4):1418-1426.
  • Versteeg H.K., Malalasecera W., 1995. An introduction to ComputationalFluid Dynamics – The Finite Volume Method.pp. 21-24.
  • VanPaasenS.V.B.,KielJ.H.A.,2004.Tarformationinafluidised-bed gasifier. Impact of fuel properties and operating conditions. ECN-C-04-013.
  • United Nations – Intergovernmental Panel on Climate Change (IPCC), 2006. Framework Convention on Climate Change. http://unfccc.int/
  • TurnsS.R.,1996.Anintroductiontocombustion.McGraw-hill.
  • TillmanD.A.,2012.Woodasanenergyresource.Elsevier.
  • TaylorC.J.,2006.Theeffectsofbiologicalfouling controlatcoastal andestuarinepowerstations.MarinePollutionBulletin,53(1):30-48.
  • Tarasov D.,ShahiC.,Leitch M.,2013.Effectofadditives on wood pelletphysicaland thermalcharacteristics:a review.Isrn Forestry, 2013.
  • Taralas G., Kontominas M.G., Kakatsios X., 2003. Modeling the thermaldestruction oftoluene (C7H8)as tar-related species forfuel gascleanup.Energy& Fuels,17(2):329-337.
  • Sun Y.C.,Wen J.L.,Xu F.,Sun R.C.,2011.Structuraland thermal characterization of hemicelluloses isolated by organic solvents and alkaline solutions from Tamarix austromongolica. Bioresource Technology,102(10):5947-5951.
  • SpearpointM.J.,QuintiereJ.G.,2000.Predicting theburning ofwood usinganintegralmodel.CombustionandFlame,123(3):308-325.
  • Soltes E.J., Elder T.J.. 1981. Pyrolysis. Organic Chemicals from Biomass,63-99.
  • Solomon P.R.,Hamblen D.G.,Carangelo R.,Serio M.,DeshpandeG., 1988.Generalmodelofcoaldevolatilization.Energy & Fuels,2(4): 405-422.
  • SimellP.A.,Hirvensalo E.K.,Smolander V.T.,Krause A.O.I.,1999. Steam reforming ofgasification gas taroverdolomite with benzene asamodelcompound.Industrial& Engineering Chemistry Research, 38(4):1250-1257.
  • Sim B.S.,Kim J.J.,ChoiK.S.,Oh H.Y.,Jang J.H.,Kang S.B.,2013. Guide vane optimization ofthe wood pelletboiler using numerical analysis.ProceedingsoftheKSCFE 2013SpringConference,276-280.
  • Shafizadeh F.,1982.Introduction to pyrolysisofbiomass.Journalof AnalyticalandAppliedPyrolysis,3(4):283-305.
  • SchlichtingH,1979.Boundarylayertheory,McGraw-Hill.
  • Sandberg J.,Sand U.,Fdhila R.B.,2006.Long time investigation of the effectoffouling on the super‐heaters in a circulating fluidized biomass boiler. International journal of energy research, 30(13): 1037-1053.
  • Sandberg J.,Fdhila R.B.,DahlquistE.,Avelin A.,2011b.Dynamic simulation offouling in a circulating fluidized biomass-fired boiler. AppliedEnergy,88(5):1813-1824.
  • Sandberg J., Karlsson C., Fdhila R.B., 2011a. A 7year long measurementperiodinvestigating thecorrelationofcorrosion,deposit and fuelin a biomass fired circulated fluidized bed boiler.Applied Energy,88(1):99-110.
  • RostamiA.,Murthy J.,HajaligolM.,2004.Modeling ofsmoldering processinaporousbiomassfuelrod.Fuel,83(11-12):1527-1536.
  • Romeo L.M.,Gareta R.,2009.Fouling controlin biomass boilers. Biomassandbioenergy,33(5):854-861.
  • RobinsonA.L.,BuckleyS.G.,YangN.,BaxterL.L.,2001.Experimental measurements ofthe thermalconductivity ofash deposits:Part2. Effectsofsinteringanddepositmicrostructure.Energy& fuels,15(1): 75-84.
  • Radmanesh R.,ChaoukiJ.,Guy C.,2006.Biomass gasification in a bubbling fluidized bed reactor: experiments and modeling. AIChE Journal,52(12):4258-4272.
  • Rabou L.P.,Zwart R.W.,Vreugdenhil B.J.,Bos L.,2009.Tar in biomassproducergas,theEnergy researchCentreoftheNetherlands (ECN) experience:an enduring challenge.Energy & Fuels,23(12): 6189-6198.
  • Qu T.,GuoW.,Shen L.,XiaoJ.,ZhaoK.,2011.ExperimentalStudy of Biomass Pyrolysis Based on Three Major Components: Hemicellulose, Cellulose, and Lignin. Industrial & Engineering ChemistryResearch,50(18):10424-10433.
  • Persson T., Riedel J., Berghel J., Bexell U., Win K.M., 2013. Emissionsanddepositpropertiesfrom combustionofwoodpelletwith magnesium additives.Journal of Fuel Chemistry and Technology, 41(5):530-539.
  • Persson H.,Bachs A.,L fgren B.E.,Dahlstr m J.E.,Bj rkman B., 2001. Erfarenheter fr n anv ndning av pelletsbr nnare och pelletskaminer.[Experiencesfrom theuseofpelletburnersandpellet stoves].STEM reportP,12231-1.
  • ParkH.Y.,JoY.,Kim Y.J.,(Versteeg,H.K.,Malalasecera원저)
    전산유체 따라잡기(An introduction to ComputationalFluid Dynamics – TheFiniteVolumeMethod) [2010]
  • Park W.C.,AtreyaA.,Baum H.R.,2010.Experimentaland theoretical investigation of heat and mass transfer processes during wood pyrolysis.CombustionandFlame,157(3):481-494.
  • Park H.C.,ChoiS.H.,Kim S.J.,ChoiY.S.,2011.Study forThermal Flow Characteristics with Varying Tube Shapes of Gas Boiler. ProceedingsoftheKSME 2011SpringConference,499-500.
  • Pancharatnam S., 1972. Transient behavior of a solar pond and prediction ofevaporation rates.Industrial& Engineering Chemistry ProcessDesignandDevelopment,11(2):287-292.
  • Palma C.F., 2013. Modelling of tar formation and evolution for biomassgasification:A review.AppliedEnergy,111:129-141.
  • P sfai M., Simonics R., Li J., Hobbs P.V., Buseck P.R., 2003. Individualaerosolparticlesfrom biomassburning in southern Africa: 1. Compositions and size distributions of carbonaceous particles. JournalofGeophysicalResearch:Atmospheres(1984–2012),108(D13).
  • O₂및 CO 농도에 따른 목재펠릿 보일러 의 최적연소조건 규명
    김대현 오재헌 황진성 한국산림휴양학회 2013년 산림과학 공동학술대회, 885-888 [2013]
  • Ozden E., Tari I., 2010. Shell side CFD analysis of a small shell-and-tube heatexchanger.Energy Conversion and Management, 51(5):1004-1014.
  • NowakowskaM.,HerbinetO.,DufourA.,Glaude,P.A.,2014.Detailed kinetic study of anisole pyrolysis and oxidation to understand tar formation during biomass combustion and gasification.Combustion andFlame,161(6):1474-1488.
  • Novozhilov V., Moghtaderi B., Fletcher D.F., Kent J.H., 1996. Computationalfluid dynamics modelling of wood combustion.Fire SafetyJournal,27(1):69-84.
  • Nosek R.,Jandačka J.,Holubcik M.,2011.Increasing the melting temperatureofash by adding differenttypesofadditivesinto wood pellets.CareTech.
  • NorinagaK.,ShojiT.,Kudo S.,HayashiJ.I.,2013.Detailed chemical kinetic modelling of vapour-phase cracking of multi-component molecularmixturesderived from thefastpyrolysisofcellulose.Fuel, 103:141-150.
  • Norinaga K., Sakurai Y., Sato R., Hayashi J.I., 2011. Numerical simulation of thermalconversion of aromatic hydrocarbons in the presence ofhydrogen and steam using a detailed chemicalkinetic model.ChemicalEngineeringJournal,178:282-290.
  • Norinaga K., Deutschmann O., Saegusa N., Hayashi, J.I., 2009. Analysis ofpyrolysis products from lighthydrocarbons and kinetic modelingforgrowthofpolycyclicaromatichydrocarbonswithdetailed chemistry.JournalofAnalyticalandAppliedPyrolysis,86(1):148-160.
  • Nishimura M.,IwasakiS.,Horio M.,2009.The role of potassium carbonate on cellulose pyrolysis.Journalofthe Taiwan Institute of ChemicalEngineers,40(6):630-637.
  • Niksa S.,1988.Rapid coaldevolatilization as an equilibrium flash distillation.AIChE Journal,34(5):790-802.
  • Niksa S,Kerstein A.R.,1991.FLASHCHAIN theory for rapid coal devolatilizationkinetics.1.Formulation.Energy& Fuels,5(5):647-665.
  • Newnan D.G.,Eschenbach T.,LavelleJ.P.,2004.Engineering economic analysis(Vol.3).OxfordUniversityPress.
  • NeeftJ.P.A.,KnoefH.A.M.,OjaniP.,1999.Behaviouroftarinbiomass gasification systems.Tarrelated problemsand theirsolutions,Energy from WasteandBiomass,Enschede/Petten,BTG/ECN,Novem-EWAB, 9919:74.
  • NarvaezI.,OrioA.,AznarM.P.,CorellaJ.,1996.Biomassgasification with air in an atmospheric bubbling fluidized bed. Effect of six operationalvariablesonthequalityoftheproducedraw gas.Industrial & EngineeringChemistryResearch,35(7):2110-2120.
  • NIST (National Institute of Standards and Technology), 2011. http://www.nist.gov/
  • N meth Z.,P sfaiM.,Nyirő-K saI.,Aalto P.,KulmalaM.,SalmaI., 2015. Images and properties of individual nucleated particles. AtmosphericEnvironment,123:166-170.
  • MottR.A.,SpoonerC.E.,1940.Thecalorific value ofcarbon in coal: theDulongrelationship.Fuel,19(226):242.
  • MorfP.,HaslerP.,NussbaumerT.,2002.Mechanismsand kineticsof homogeneous secondary reactions oftarfrom continuous pyrolysis of woodchips.Fuel,81(7):843-853.
  • Mohamed Gas-el-Hak, 1995. Stokes’ hypothesis for a newtonian, isotropicfluid.JournalofFluidsEngineering,117(1):3-5.
  • Moghadam R.A.,Yusup S.,Uemura Y.,Chin B.L.F.,Lam H.L.,Al Shoaibi A., 2014. Syngas production from palm kernel shell and polyethylene waste blend in fluidized bed catalytic steam co-gasificationprocess.Energy,75:40-44.
  • MilneT.A.,Abatzoglou N.,EvansR.J.,1998.Biomass gasifier“tars”: Their nature,formation,and conversion:NationalRenewable Energy Laboratory,NREL/TP-570-25357.
  • MayerhoferM.,FendtS.,SpliethoffH.,GadererM.,2014.Fluidizedbed gasification ofbiomass–In bedinvestigationofgasandtarformation. Fuel,117:1248-1255.
  • Lloyd W.G.,DavenportD.A.,1980.Applying thermodynamicsto fossil fuels:Heats of combustion from elementalcompositions.Journalof chemicaleducation,57.1:56.
  • LiY.,Liu H.,2000.High-pressure densification ofwood residues to form anupgradedfuel.BiomassandBioenergy,19(3):177-186.
  • LiC.,SuzukiK.,2010.Resources,properties and utilization oftar. Resources,ConservationandRecycling,54(11):905-915.
  • LiC.,SuzukiK.,2009.Tarproperty,analysis,reforming mechanism and modelfor biomass gasification - An overview.Renewable and SustainableEnergyReviews,13(3):594-604.
  • LiB.,Brink A.,Hupa M.,2013.CFD investigation ofslagging on a super-heater tube in a kraft recovery boiler. Fuel Processing Technology,105:149-153.
  • L fgren B.E.,Arkel v O.,2004.Testav olika produktkombinationer videldningmedtr pelletsochF ltunders kningavolikapelletskvalitet vid utleverans och v rmek lla. [Test of Different Kinds of Combinations ofProducts when Firing Wood FuelPellets and Field Survey ofDifferentKinds ofPelletQuality when Delivering and at theHeatingDevice]. FAB-report2004:03.Lidk ping,Sweden.
  • KyotoProtocol,2005.http://www.kyotoprotocol.com/
  • Kwak W.S.,Jung S.H.,Kim Y.I.,2008.Boiler litter supplementation improves storage and feed-nutritionalvalue ofsawdust-based spent mushroom substrate.BioresourceTechnology,99(8):2947-2955.
  • KuokkanenM.J.,VilppoT.,KuokkanenT.,StoorT.,Niinim kiJ.,2011. Additives in wood pellet production–a pilot-scale study of binding agentusage.BioResources,6(4):4331-4355.
  • Koppejan J.,Van Loo S.(Eds.),2012.The handbook of biomass combustionandco-firing.Routledge.
  • Klason T.,BaiX.S.,2007.Computationalstudy of the combustion processand NO formation in asmall-scalewood pelletfurnace.Fuel, 86:1465-1474.
  • Kim D.H.,Jenkins,B.M.,Yore,M.W.,Kim N.J.,2007.Saltrecovery from agriculturaldrainage water using a liquid film solar-assisted concentrator–Simulation and modelvalidation.Solar Energy,81(10): 1314-1321.
  • Kim D.H.,Jenkins B.M.,Rumsey T.R.,Yore M.W.,Kim N.J.,2007. Simulation and modelvalidation ofa horizontalshallow basin solar concentrator.Solarenergy,81(4):463-475.
  • KielJ.H.A.,Van Paasen S.V.B.,NeeftJ.P.A.,DeviL.,PtasinskiK.J., Janssen F.J.J.G.,BramerE.A.,2004.Primary measures to reduce tar formationinfluidised-bedbiomassgasifiers.ECN,ECN-C-04-014.
  • KernD.Q.,SeatonR.E.,1959.A theoreticalanalysisofthermalsurface fouling.BritishChemicalEngineering,4(5):258-262.
  • Kang S.K.,ChoiK.S.,Yoon J.Y.,2009.Characteristics ofcombustion andheatexchangerofdomesticgasboilerequippedwith2-stageheat exchanger.ProceedingsoftheKSME 2009SpringConference,386-389.
  • Kang S.K.,ChoiK.S.,Yoon J.Y.,2008.Numericalsimulation on the flow and heattransfer in the combustion chamber ofdomestic gas boilerwith2-stageheatexchanger.ProceedingsoftheKFMA Annual Meeting,607-613.
  • Kafle Sagar,2016.A study on tar fouling reduction in wood pellet boiler using additives. [Master thesis] Department of Biosystems Engineering,KangwonNationalUniversity.
  • KS B 6205,육상용 보일러의 열 정산 방식(Land boilers– Heat balancing)
    한국산업표준(KoreaStandards) [2014]
  • Jess A., 1996, Mechanisms and kinetics of thermal reactions of aromatic hydrocarbons from pyrolysis of solid fuels. Fuel, 75(12): 1441-1448.
  • Janse A.M.C.,WesterhoutR.W.J.,Prins W.,2000.Modelling offlash pyrolysis of a single wood particle. Chemical Engineering and Processing:ProcessIntensification,39(3):239-252.
  • JamialahmadiM.,M ller-SteinhagenH.,2000.Crystallizationofcalcium sulfate dihydrate from phosphoric acid. Developments in Chemical EngineeringandMineralProcessing,8(5-6):587-604.
  • Incropera F.P.,DeWittD.P.,1996.Introduction to HeatTransfer(3rd Edition).
  • Incropera F.P., Lavine A.S., Bergman T.L., DeWitt D.P., 2013. Principlesofheatandmasstransfer,Wiley.
  • Hosoya T., Kawamoto H., Saka S., 2008. Pyrolysis gasification reactivitiesofprimary tarandcharfractionsfrom celluloseandlignin as studied with a closed ampoule reactor.JournalofAnalyticaland AppliedPyrolysis,83(1):71-77.
  • Hans Hartmann, 2003. 「Handbuch Bioenergie-Kleinanlagen」. Bundesministerium f r - Ern hrung, Landwirtschaft und Verbraucherschutz.ISBN 3-00-011041-0,96.
  • Grieco E.,BaldiG.,2011.Analysis and modelling ofwood pyrolysis. ChemicalEngineeringScience,66(4):650-660.
  • GrantD.M.,Pugmire R.J.,Thomas H.,FletcherT.H.,Kerstein A.R., 1989.Chemicalmodelofcoaldevolatilization using percolation lattice statistics.Energy& Fuels,3(2):175-186.
  • GiudicianniP.,Cardone G.,RagucciR.,2013.Cellulose,hemicellulose and lignin slow steam pyrolysis:Thermaldecomposition ofbiomass componentsmixtures.JournalofAnalyticalandAppliedPyrolysis,100: 213-222.
  • Genetti D., Fletcher T.H., Pugmire RJ., 1999. Development and applicationofacorrelationof13C NMR chemicalstructuralanalysesof coal based on elemental composition and volatile matter content. Energy& Fuels,13(1):60-68.
  • Gas Technology Institute (GTI), 1978. Coal conversion systems technical data book. ERDA No. FE-2286-32, NTIS, Springfield, Virginia.
  • Garcı́a X.A.,Alarcon N.A.,Gordon A.L.,1999.Steam gasification of tarsusingaCaO catalyst.Fuelprocessingtechnology,58(2):83-102.
  • FiaschiD.,MicheliniM.,2001.A two-phaseone-dimensionalbiomass gasificationkineticsmodel.BiomassandBioenergy,21(2):121-132.
  • FaravelliT.,FrassoldatiA.,Migliavacca G.,RanziE.,2010.Detailed kinetic modeling ofthe thermaldegradation oflignins.Biomass and Bioenergy,34(3):290-301.
  • Epstein N.,1997.Elementsofparticledeposition onto nonporoussolid surfacesparalleltosuspension flows.ExperimentalThermaland Fluid Science,14(4):323-334.
  • Eggleston H.S.,BuendiaL.,MiwaK.,NgaraT.andTanabeK.,2006. IPCC GuidelinesforNationalGreenhouseGasInventories,Preparedby theNationalGreenhouseGasInventoriesProgramme.Published:IGES, Japan.http://www.ipcc-nggip.iges.or.jp/
  • ETB (EngineeringToolBox),2015.http://www.engineeringtoolbox.com/
  • Dou B.,Gao J.,Sha X.,Baek S.W.,2003.Catalytic cracking oftar component from high-temperature fuel gas. Applied thermal engineering,23(17):2229-2239.
  • DeviL.,PtasinskiK.J.,Janssen F.J.,van Paasen S.V.,Bergman P.C., Kiel J.H., 2005a. Catalytic decomposition of biomass tars: use of dolomiteanduntreatedolivine.RenewableEnergy,30(4):565-587.
  • DeviL.,PtasinskiK.J.,Janssen F.J.,2003.A review ofthe primary measuresfortareliminationinbiomassgasificationprocesses.Biomass andBioenergy,24(2):125-140.
  • Devi.L.,PtasinskiK.J.,Janssen F.J.,2005b.Pretreated olivine as tar removalcatalystforbiomassgasifiers:investigation using naphthalene asmodelbiomasstar.FuelProcessingTechnology,86(6):707-730.
  • Delgado J.,Aznar M.P.,Corella J.,1997.Biomass gasification with steam in fluidizedbed:effectivenessofCaO,MgO,andCaO-MgO for hotraw gas cleaning.Industrial& Engineering Chemistry Research, 36(5):1535-1543.
  • DeJong W., nala .,AndriesaJ.,HeinbK.R.G.,SpliethoffaH.,2003. Thermochemical conversion of brown coal and biomass in a pressurised fluidised bed gasifierwith hotgasfiltration using ceramic channelfilters:measurements and gasifiermodelling.Applied Energy, 74(3):425-437.
  • CollazoJ.,PorteiroJ.,PatinoD.,GranadaE.,2012.Numericalmodeling ofthecombustion ofdensified wood underfixed-bed conditions.Fuel, 93:149-159.
  • Chaney J.,Liu H.,LiJ.,2012.An overview ofCFD modelling of small-scale fixed-bed biomass pelletboilers with preliminary results from a simplified approach.Energy Conversion and Management,63: 149-156.
  • Byun Y.C.,ParkS.H.,Hwang J.H.,LeeJ.M.,Kim J.S.,2002.Study of nozzlecharcteristicson clinkerformation in aCFBC boilerwith CFD calculation.JournalofEnergyEngineering,11(3):224-229.
  • Bryden K.M.,Ragland K.W.,Rutland C.J.,2002.Modeling thermally thickpyrolysisofwood.BiomassandBioenergy,22(1):41-53.
  • BrageC.,YuQ.,Sj str m K.,1996.Characteristicsofevolution oftar from woodpyrolysisinafixed-bedreactor.Fuel,75(2):213-219.
  • BoieW.,1953.Fueltechnologycalculations.Energietechnik,3:309-316.
  • Bloomberg New Energy Finance, 2015. Australia’s 2030 emissions pledgeinlinewithotherOECD nations,butlacksthetoolstodeliver. http://about.bnef.com/
  • BenkoussasB.,ConsalviJ.L.,PorterieB.,SardoyN.,LoraudJ.C.,2007. Modelling thermaldegradation of woody fuelparticles.International JournalofThermalSciences,46(4):319-327.
  • BarmanN.S.,GhoshS.,DeS.,2012.Gasificationofbiomassinafixed bed downdraftgasifier- A realistic modelincluding tar.Bioresource Technology,107:505-511.
  • Bansal B., Chen X.D., M ller-Steinhagen H., 2008. Analysis of ‘classical’ deposition rate law for crystallisation fouling. Chemical EngineeringandProcessing:ProcessIntensification,47(8):1201-1210.
  • Baker E.G., Brown M.D., Elliott D.C., Mudge L.K., 1988, Characterization and treatment of tars and biomass gasifiers (No. PNL-SA-16148;CONF-880850--19).Pacific NorthwestLab.,Richland, WA (USA).
  • BIOMASA Association,2011.The EffectofAdditives forProduction CostsandParametersofWoodPellets.BIOMASA Association,1-6.
  • Aznar M.P.,Caballero M.A.,Gil J.,Mart n J.A.,Corella J.,1998. Commercialsteam reforming catalyststoimprovebiomassgasification with steam-oxygen mixtures.2.Catalytic tar removal.Industrial& engineeringchemistryresearch,37(7):2668-2680.
  • AntalM.J.,AllenS.G.,DaiX.ShimizuB.,Tam M.S.,GronliM.,2000. Attainmentofthetheoreticalyield ofcarbon from biomass.Industrial & EngineeringChemistryResearch,39(11):4024-4031.
  • Ahn J.,Kim J.J.,2011.Heattransfercharacteristics of0.5 t/h class non-furnace boiler with a metalfiber burner.Transactions of the KoreanSocietyofMechanicalEngineers,B35(2):215-220.
  • Ahn J., Jang J.H., 2014. CFD Study on partial-load combustion characteristicsofa4-step-gratewoodpelletboiler.Transactionsofthe KoreanSocietyofMechanicalEngineers,B38(4):365-371.
  • Ahanj M.D.,RahimiM.,AlsairafiA.A.,2012.CFD modeling of a radianttube heater.InternationalCommunications in Heatand Mass Transfer,39(3):432-438.
  • Abu El-Rub Z.,BramerE.A.,Brem G.,2004.Review ofcatalystsfor tar elimination in biomass gasification processes. Industrial & engineeringchemistryresearch,43(22):6911-6919.