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IEA Energy Conservation and
Emissions Reduction in Combustion
         (E.C.E.R.C.) I. A.


             Belgian Contributions




 Presentation of ECERC
 Studies at UCL
 Studies at UMons
 Studies at ULg
 Conclusions and Perspectives
IEA "Energy Conservation and Emissions
Reduction in Combustion" I. A.
 Tasks shared and not costs shared I.A.
 12 participant countries : BEL, CAN, CHE, DEU, FIN, GBR, ITA, JPN,
                            KOR, NOR, SWE and USA
 Executive Committee (ExCo) : 1 delegate and 1 alternate per
                              participant country
 Chair and vice-chair of the ExCo are elected (each year) by rotating
 procedure
 3 Meetings per year:
     March 2012: Strategy group (USA)
     April 2012: ExCo in Paris (France)
     October 2012: Task Leaders Meeting (TLM) + ExCo (Republic of Korea)
 I.A.'s public web site : http://ieacombustion.net/default/aspx




Active Research Activities (March 2011)
 Annex 1: Individual Contributor Tasks
 Annex 2: Sprays in Combustion (Collaborative Task): CHE, FIN, JPN
 Annex 3: Homogeneous Charge Compression Ignition
          (Collaborative Task): CAN, JPN, KOR, SWE
 Annex 4: Advanced Hydrogen Fueled Internal Combustion
          Engines (Collaborative Task): CAN, JPN, KOR, USA
 Annex 5: Alternative Fuels (Collaborative Tasks): BEL, CHE, FIN,
          KOR, SWE
 Annex 6: Nanoparticles Diagnostics (Collaborative Tasks): CAN, ITA
 Annex 7: Hydrogen Enriched Lean Premixed Combustion for Ultra-
          Low Emission Gas Turbine Combustors (Collaborative
          Task): CHE, NOR, SWE
 Annex 8: Supporting Activities
Annex 1: Individual Contributor Tasks

  Area 1 : Advanced Piston Engine Technology
  Area 2 : Advanced Furnace Technology
             Subarea 2.1 : Burner Phenomena (UMons, ULg)
             Subarea 2.2 : Gas Flows
             Subarea 2.3 : Fuel/air Mixing
             Subarea 2.4 : Flame processes (UCL)
             Subarea 2.5 : Postflame process

  Area 3 : Fundamentals (development of diagnostics tool
           and simulation codes)
  Area 4 : Advanced Gas Turbine Technology




Belgian activities
(Advanced Furnace Technology : Area 2)


  Subtask 2.1H : INVESTIGATION ON COMBUSTION IN OIL BURNER
  FLAMES
         Contributor : Université de Liège
                                     Liè
                       Thermodynamics Laboratory – Thermotechnics

  Subtask 2.1I : STUDY OF COMBUSTION AND HEAT TRANSFER
  PHENOMENA IN INDUSTRIAL FURNACES FIRED WITH GAS BURNERS
  USING PREHEATED AIR
         Contributor : Faculté Polytechnique de l’Université de Mons
                       Thermal Engineering and Combustion Unit

  Subtask 2.4F : CHEMICAL KINETICS STUDIES OF FLAMES AND SOOT
  FORMATION
         Contributor : Université catholique de Louvain
                       Institute of Mechanics, Materials and Civil Engineering
Presentation of ECERC
   Studies at UCL
   Studies at UMons
   Studies at ULg
   Conclusions and Perspectives




             SUBTASK 2.4.F
Chemical Kinetics Studies of Flames and Soot
                 Formation

Institute of Mechanics, Materials and Civil Engineering
    Pôle TFL – Thermodynamics and Fluid mechanics

           Université catholique de Louvain

                    Véronique Dias and Hervé Jeanmart
        Veronique.Dias@uclouvain.be and Herve.Jeanmart@uclouvain.be
Chemical Kinetics Studies of Flames and
   Soot Formation

    Experimental studies of hydrocarbons and/or oxygenated species, by
               analysis flame structures at low pressure


       Elaboration of kinetic model to understand emission formation:
        conversion of reactants, formation of pollutants, effects of
additives…
additives…

      Reduction of the kinetic model according to initial conditions



           Use of reduced mechanisms in industrial processes
                     (engines, furnaces, boilers, …)




        Experimental studies




                                                            1.2E-01                                              2.00E+03
                                                                                                                 1.80E+03
                                                            1.0E-01                                              1.60E+03
     Premixed flat flames stabilized on a                                                                        1.40E+03
                                                                                                                            Temperature (K)




                                                            8.0E-02
     burner at low pressure, analyzed
                                            Mole fraction




                                                                                                                 1.20E+03
                                                            6.0E-02                                              1.00E+03
     by:                                                                                                         8.00E+02
                                                                                                X-CO2
                                                            4.0E-02
     -mass spectrometry (MS)                                                                    X-TOLUENE
                                                                                                X-C6H6
                                                                                                                 6.00E+02
                                                                                                                 4.00E+02
     -or by gas chromatography (GC).                        2.0E-02                             Temperature
                                                                                                                 2.00E+02
                                                            0.0E+00                                              0.00E+00
                                                                   0.00   0.33 0.65 0.96 1.28 1.61        1.93
                                                                           Height Above the Burner (cm)
Modelisation

   Elaboration of kinetic model
   Predict the evolution for concentrations of present species in
   the flame (from fresh gases to burned gases)


   Interest
   Obtain valuable informations: degree of conversion rate of
   reactants, formation rate of pollutants, effects of additives on
   the soot formation,…

   Integration of these kinetic mechanisms in CFD simulation
   models of industrial processes (engines, boilers, furnaces...)




Elaboration of « UCL » kinetic model

The kinetic model includes the detailed formation and consumption
reactions of species from C1 to C10. It contains 568 reactions and
107 chemical species.

This reaction mechanism has been extended and validated using
flat flames experiments:
-Methane (CH4), ethane (C2H6)
-Ethylene (C2H4), acetylene (C2H2), isobutene (iC4H8)
-Benzene (C6H6)
-Dimethoxymethane (C3H8O2), diethoxymethane (C5H12O2), ethanol (C2H5OH)
-Formaldehyde (CH2O), acetaldehyde (CH3CHO)




http://veroniquedias.github.com/UCLouvain-Mechanism/
Flames with additives
Objectives of experiments                                                                   φ
                                                       C2H4 /O2 /Ar with C3H8O2 or C5H12O2 (φ = 2.5)
                                                                                  4.5E-02
Observe and measure the reduction of
concentrations for the soot precursors (with                                      4.0E-02
φ constant) with additives C3H8O2 (DMM) et
                                                                                  3.5E-02
C5H12O2 (DEM).




                                                               Fraction molaire
                                                                                  3.0E-02
 By   keeping      the    equivalence      ratio
constant,(φ), the ratio C/O decrease :                                            2.5E-02

 → Reduction of mole fractions for                                                2.0E-02
hydrocarbons produced in the rich ethylene                                        1.5E-02
flame.                                                                                             - 19,8 % with DMM
                                                                                  1.0E-02
                                                                                                   - 16,4 % with DEM
Objectives of modelisation                                                        5.0E-03

                                                                                  0.0E+00
Elaborate a kinetic model able to predict                                                   0        10         20          30
the concentration of species present in these                                                    Distance au brûleur (mm)
flames
                                                                                                   C2H2
Understand the effect of the additives on
the reduction of soot precursors formation




Flames of methylal (DMM)
                           OH H          CH3OCH2OCH3                               H OH
                           OH O                                                    OH O

  CH3OêHOCH3 (DMM2)                                                                         CH3OCH2OêH2 (DMM1)



          CH3OCHO                                                                               CH3OêH2
             H
            OH

           CH3OêO                                                                    O2
                                                                                                 Rich flame of DMM
             M
                                                                                                 Lean flame of DMM
                              H
             CH3O•                           CH2O
                              O              H     OH
                                            OH     O
                                                          M                                 OH
                                             HêO                          CO                       CO2
                                                          O2
Conclusions and perspectives
Elaboration of the reaction mechanism, named « UCL »:

Past studies:      Methane (CH4), ethane (C2H6)
                   Ethylene (C2H4), acetylene (C2H2), isobutene (iC4H8)
                   Benzene (C6H6)
                   Dimethoxymethane (C3H8O2), diethoxymethane (C5H12O2)
                   Ethanol (C2H5OH)
                   Formaldehyde (CH2O), acetaldehyde (CH3CHO)

Present studies:   Acetic acid (CH3COOH)


Future experimental and modeling studies of flame structure:
                   Triacetine (C9H14O6)
                   Methyl valerate or methyl pentanoate (CH3CH2CH2CH2COOCH3)



           => Use of the mechanism in industrial processes
                   (engines, furnaces, boilers, …)




Conclusions and perspectives




                                                   Application of the
                                                  mechanism of ethyl
                                                acetate and ethanol in an
                                                      HCCI engine
Publications
2008-2011: 17 articles ( ≈ 30 posters / oral presentations)

V. Dias, J. Vandooren, Comb. and Flame 158 (2011) 848-859 ;
V. Detilleux, J. Vandooren, Proc. Comb. Inst. 33 (2011) 217-224 ;
X. Lories, J. Vandooren, D. Peeters, Int. J. Quant. Chem. DOI:10.1002/qua.23035 (2011) ;
N. Leplat, P. Dagaut, C. Togbé, J. Vandooren, Comb. and Flame 158 (2011) 705-725 ;
X. Lories, J. Vandooren, D. Peeters, Int. J. Quant. Chem. DOI:10.1002/qua.23142 (2011) ;
X. Lories, J. Vandooren, D. Peeters, Computional and Theoretical Chemistry 966 (2011) 244-249 ;
V. Dias, J. Vandooren, Fuel 89 (2010) 2633-2639 ;
V. Dias, X. Lories, J. Vandooren, Combust. Sci. And Tech. 182 (2010) 350-364.
N. Leplat, J. Vandooren, Combust. Sci. and Tech. 182 (2010) 436-448 ;
X. Lories, J. Vandooren, D. Peeters, Phys. Chem. Chem. Phys. 12 (2010) 3762-3771
C. Renard, V. Dias, P. J. Van Tiggelen, J. Vandooren, Proc. Comb. Inst. 32 (2009) 631-637 ;
V. Detilleux, J. Vandooren, J. Phys. Chem. A 113 (2009) 10913-10922 ;
V. Dias, C. Renard, J. Vandooren, Z. Phys. Chem. 223 (2009) 565-577 ;
V. Detilleux, J. Vandooren, Combustion, Explosion and Shock Waves 45 (2009) ;
X. Lories, J. Vandooren, D. Peeters, Chem. Phys. Letters 452 (2008) 29-32 ;
N. Leplat, A. Seydi, J. Vandooren, Combust. Sci. and Tech. 180 (2008) 519-532 ;
V. Detilleux, J. Vandooren, Combust. Sci. and Tech. 180 (2008) 1347-1469;




        Presentation of ECERC
        Studies at UCL
        Studies at UMons
        Studies at ULg
        Conclusions and Perspectives
SUBTASK 2.1.I
     Study of Combustion and Heat Transfer in
    Industrial Furnaces Fired with Gas Burners
                Using Preheated Air

     Faculty of Engineering of the University of Mons
       Pôle Energie – Thermal Engineering and Combustion Unit

                               Delphine Lupant
                         Delphine.Lupant@umons.ac.be




POLYTECH
= Faculty of Engineering of the University of Mons (founded thanks to the
association of the University of Mons-Hainaut and the Faculty of
Engineering of Mons)


Research is organized around 5 multidisciplinary research centers :
   Information and Technologies
   Materials
   Risks
   Biochemical systems and bioprocesses (BIOSYS)
   Energy:                                                  Thermal
                                                            Engineering &
        3 themes :                                          Combustion Unit
                Energy and buildings
                Combustion and problems of CO2
                Transport and production of electrical energy
Participation in ECERC since 1992
       Context: Reduction of NOx emission in furnaces with air preheating at high
       temperature (Rational use of energy)
       Methodology:
        o Run experiments on furnaces built in our laboratory (funded by SPF)
        o Concurrently, use a commercial software (ANSYS Fluent) to model the
          combustion and use the measurements as validation data
       Benefits:
        o Guidance and services contracts for industrial partners (FIB, Drever)
        o Expertise in numerical modeling (AGC, Arcelor,…)
       Since 2000: Flameless Oxidation or Diluted Combustion
                   = New Combustion technique which combine
                   high efficiency + very low NOx emission




  Diluted combustion furnaces
       At semi-industrial scale (300kW)
          semi-
        o Commercial burner (REGEMAT WS)
        o Fired with natural gas + air
        o Furnace is available for international
          research partners (IFRF)
        o Used to test industrial burners (services
          contracts)
        o Main results:
EXP: heat transfer, emissions, efficiency
SIM: validation of global combustion
models with temperature and species
measurements in the furnace
Diluted combustion furnaces
      At laboratory scale I (3kW)
      o Simplified geometry (co-flow)
      o Fed with natural gas or synthetic mixture
        (CH4, CO, H2, N2, CO2)
          The objective was to study the evolution of
          the operating conditions required to sustain
          diluted combustion with low calorific value
          gases (products from gasification of biomass
          or from steel industry)
          Diluted combustion offers a smart way to
          solve flame stabilization problems Preheated and                  Combustion
                                                                             chamber
          encountered in standard burners          diluted air
          due to the significant variations of their
          heating value (fuel flexibility)                               Fuel




Diluted combustion furnaces
      At laboratory scale II (30kW) = current project
      o Configuration similar to industrial furnaces (burner
        geometry, injection velocities, load) but at small scale
                                   50%COG
Species     NG     COG     BFG                  Wood gas
                                   50%BFG
CH4         90%    35%       -       18%            1%
H2            -    60%     5%        33%           16%
CO            -     5%     25%       15%           21%                          Fuel
CO2         1%             25%       13%           12%
                                                                   Preheated air
N2          2%             45%       21%           50%
          The objective is to study the evolution of the heat transfer (in the furnace
          and to the load), the combustion efficiency, the NO and CO emissions
          with those alternative fuels and give rules of design for industrial furnaces
          Interest from industrial partner (sponsorship from Arcelor-Mittal)
Publications
       2006-2011
1      D. Lupant, B. Pesenti, E. Sezgin, P. Lybaert:          Flameless combustion of CH4/CO/H2 fuel blends
       Proceedings of the "European Combustion Meeting ECM 2011", Cardiff, 2011
2      E. Sezgin, D. Lupant, B. Pesenti, P. Lybaert: Développement de diagramme de stabilité de flamme en
       combustion diluée, Actes du Congrès Annuel de la Société Française de Thermique, pp 351-356, 2010
3      D. Lupant, B. Pesenti, P. Lyabert: Impact des sondes de prélèvement sur la mesure d’espèces réactives en
       oxydation sans flamme, Actes du Congrès Annuel de la Société Française de Thermique, pp 363-368, 2010
4      D. Lupant, B. Pesenti, P. Lybaert: Influence of probe sampling on reacting species measurement in diluted
       combustion, Experimental Thermal and Fluid Science 34, 516–522, 2010
5      E. Sezgin, B. Pesenti, D. Lupant, P. Lybaert: Development of stability diagrams of flame in diluted combustion,
       Proceedings of the "European Combustion Meeting ECM 2009", Vienne, 2009
6      G. Seggio, B. Pesenti, P. Lybaert, P. Ngendakumana: Feasibility study of the diluted combustion in a semi-
       industrial boiler at low temperatures, Proceedings of the 8th european conference on industrial furnaces and boilers,
       Vilamoura, 2008
7      D. Lupant, B. Pesenti, P. Lybaert: Characterization of flameless combustion of natural gas in a laboratory scale
       furnace, Proceedings of the "European Combustion Meeting ECM 2007", Chania, 2007
8      D. Lupant, B. Pesenti, P. Evrard, P. Lybaert: Numerical and experimental characterization of a self-regenerative
       flameless oxidation burner operation in a pilot-scale furnace, Combustion Science and Technology (I. Glassman
       and R. A. Yetter eds.), Vol 179: 437–453, 2007
9-10   D. Lupant, B. Pesenti, P. Lybaert: Assessment of combustion models of a self-regenerative flameless oxidation
       burner, Proceedings of the 7th European Conference on Industrial Furnaces and Boilers, Porto, 2006 + Proceedings of
       the 7th National Congress on Theoretical and Applied Mechanics, Mons, 2006




            Presentation of ECERC
            Studies at UCL
            Studies at UMons
            Studies at ULg
            Conclusions and Perspectives
SUBTASK 2.1.H
  The use of liquid biofuels in heating systems :
                     a review

                   University of Liège
         Thermodynamics Laboratory – Thermotechnics

                     Philippe Ngendakumana

                     pngendakumana@ulg.ac.be




 17% of CO2 emissions in Europe are related to
space heating function of gas and oil-fired boilers




                                               Ref: ecoboiler.org
There are different pathways to convert
biomass to biofuels




Vegetable oils combustion is feasable
if the viscosity is reduced

   Vegetable oil viscosity is 35 mm²/s at 40° compared
                                            C
     to 2.7mm²/s for gasoil
       it must be reduced by preheating (to 80° or
                                              C)
     mixing to gasoil

   LHV of vegetable oils (37MJ/kg) 10% lower than LHV
     of diesel (43MJ/kg)

   Vegetable oil must be appropriately stored to avoid
     oxidation and filtration problems
CO emissions reduction with vegetable
oil addition




                    Alonso et al., Energy & Fuels, Vol. 22, No 5, 2008.




Biodiesels are good candidates to
petroleum diesel fuel substitution

 Biodiesels have similar physical properties to diesel
   fuels (viscosity 4mm²/s at 40°
                                C)

 LHV of biodiesels (37MJ/kg) 10% lower than LHV
   of diesel (43MJ/kg)

 Quality requirements are defined in the standards
  EN14213

 They are quite stable but strong oxidizing agents
   must be avoided
Burning biodiesel decreases most
pollutants emissions




                 Macor et Pavanello, Energy, Vol. 34, pp. 2025-2032, 2009.




Bioethanol combustion in heating systems is
more problematic


  Bioethanol is less viscous than diesel and can lead to
    lubrification problems in the pumps

  LHV of bioethanol is 35% lower than that of the diesel
       quantity of fuel injected must be adapted (greater
    capacity injection nozzle or increased injection
    pressure)

  Storage is more hazardous as bioethanol flash point is
    around 13° (compared to 60° for diesel fuel)
              C                  C
Bioethanol flame emissivity decreases
compared to diesel fuel flame emissivity




    Barroso et al., Fuel processing technology, Vol. 91, pp. 1537-1550, 2010.




Bioliquids combustion in heating
systems: Some conclusions

 Vegetable oils can be burnt in boilers if their viscosity is
   reduced

 Biodiesels are good candidates to fuel oil substitution.
   Pollutants emissions are mainly decreased but there
   is no clear trend for NOx emissions
 Bioethanol combustion is more difficult to achieve in
   conventional burners (low viscosity, low energy
   content, low vapor pressure, different flame
   emissivity)
Future work : What are the effects of fuel
composition on flame temperature and
pollutants emission?

                           370 KW boiler equipped
                           with visualisation windows
                           We will burn biodiesels of
                           various origins and
                           compositions:
                              to evaluate the effects of fuel
                           composition on flame
                           temperature and NOx
                           emissions
                               to evaluate the boiler
                           performance working with
                           different biodiesels




 Other topics

 • Combustion control and performance of
 household condensing boilers

 • Feasibility study of the diluted combustion
 in a semi-industrial boiler at low
 temperatures (compared to furnaces)

 • Combustion of wood pellets in a domestic
 heating boiler
Publications
2006-2011
L. Arias, S.Torres, D. Sbarbaro, P. Ngendakumana : On the spectral bands measurements for combustion monitoring,
       doi:10.1016/j.combustflame.2010.09.018

D. Makaire, P. Ngendakumana : Simulation model of a gas-fired condensing boiler at full load operation in steady-
      state regime, ASME-ATI-UIT 2010 Conference on Thermal and Environmental Issues in Energy Systems.

D. Makaire, P. Ngendakumana : Modelling the thermal efficiency of condensing boilers working in steadystate
      conditions, Paper presented at 21st "journées d'études" of the Belgian Section of the Combustion Institute, Liège
      (Belgium), May 2010

D. Makaire, P. Ngendakumana : Modèle de simulation des performances d'une chaudière fioul à condensation de
      chauffage domestique, Energies et transports durables : SFT10, Le Touquet (France), 25-28 mai 2010

K. Sartor, P. Ngendakumana : Natural Gas as an Alternative Fuel for Spark Ignition Engines, Paper presented
      at 21st "Journées d’Etudes" of the Belgian Section of the Combustion Institute, Liège (Belgium), May 2010

Luis E. Arias Parada. Arias : Photodiode-based sensor for flame sensing and combustion process monitoring, by
      means the global detection of flame spectral information, PhD thesis, University of Concepcion (Chile), March 2009

D. Makaire and Ph. Ngendakumana, Simulation model of a semi-industrial fuel oil boiler in steady-state regime.
      Proceedings of the 5th European Thermal-Sciences Conference (EUROTHERM 2008). Eindhoven (The Netherlands),
      May 18-22, 2008

G. Seggio, B. Pesenti, P. Lybaert, P. Ngendakumana: Feasibility study of the diluted combustion in a semi-industrial
      boiler at low temperatures, Proceedings of the 8th european conference on industrial furnaces and boilers, Vilamoura,
      2008

A.    Ballant, D. Makaire, P. Ngendakumana : Modelling of a domestic gas-fired condensing boiler, Paper presented at
      21st "journées d'études" of the Belgian Section of the Combustion Institute,, GENT (Belgium), May 6-8, 2008




            Presentation of ECERC
            Studies at UCL
            Studies at UMons
            Studies at ULg
            Conclusions and Perspectives
Conclusions and Perspectives

   Future works:

   Combustion of gases           with   low    calorific   values      in
   furnaces(UMons-UCL)
   Transition from commercial to open-source CFD software for
   combustion (UMons-UCL)
   Feasibility studies of diluted combustion without air preheating
   (UMons-ULg)
   Lending of experimental equipments, troubleshooting of
   experiments and measurement techniques (ULg-UMons-UCL)




Conclusions and Perspectives

Complementary themes and efforts among Belgian partners
Balance between fundamental and applied research
Scientific production (publications, thesis)

Outcomes:
   Kinetic models (UCL)
   Experimental database (UCL, UMons)
   Semi-industrial size test facilities (UMons, ULg)

Perspectives:
    Facilities available for industrial test
    Industrial deployment of numerical tools and know how
    Insights into long-term research plans at an international level
    through the ECERC agreement (TLM and ExCo)

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8. véronique dias ecerc - emissions reduction in combustion

  • 1. IEA Energy Conservation and Emissions Reduction in Combustion (E.C.E.R.C.) I. A. Belgian Contributions Presentation of ECERC Studies at UCL Studies at UMons Studies at ULg Conclusions and Perspectives
  • 2. IEA "Energy Conservation and Emissions Reduction in Combustion" I. A. Tasks shared and not costs shared I.A. 12 participant countries : BEL, CAN, CHE, DEU, FIN, GBR, ITA, JPN, KOR, NOR, SWE and USA Executive Committee (ExCo) : 1 delegate and 1 alternate per participant country Chair and vice-chair of the ExCo are elected (each year) by rotating procedure 3 Meetings per year: March 2012: Strategy group (USA) April 2012: ExCo in Paris (France) October 2012: Task Leaders Meeting (TLM) + ExCo (Republic of Korea) I.A.'s public web site : http://ieacombustion.net/default/aspx Active Research Activities (March 2011) Annex 1: Individual Contributor Tasks Annex 2: Sprays in Combustion (Collaborative Task): CHE, FIN, JPN Annex 3: Homogeneous Charge Compression Ignition (Collaborative Task): CAN, JPN, KOR, SWE Annex 4: Advanced Hydrogen Fueled Internal Combustion Engines (Collaborative Task): CAN, JPN, KOR, USA Annex 5: Alternative Fuels (Collaborative Tasks): BEL, CHE, FIN, KOR, SWE Annex 6: Nanoparticles Diagnostics (Collaborative Tasks): CAN, ITA Annex 7: Hydrogen Enriched Lean Premixed Combustion for Ultra- Low Emission Gas Turbine Combustors (Collaborative Task): CHE, NOR, SWE Annex 8: Supporting Activities
  • 3. Annex 1: Individual Contributor Tasks Area 1 : Advanced Piston Engine Technology Area 2 : Advanced Furnace Technology Subarea 2.1 : Burner Phenomena (UMons, ULg) Subarea 2.2 : Gas Flows Subarea 2.3 : Fuel/air Mixing Subarea 2.4 : Flame processes (UCL) Subarea 2.5 : Postflame process Area 3 : Fundamentals (development of diagnostics tool and simulation codes) Area 4 : Advanced Gas Turbine Technology Belgian activities (Advanced Furnace Technology : Area 2) Subtask 2.1H : INVESTIGATION ON COMBUSTION IN OIL BURNER FLAMES Contributor : Université de Liège Liè Thermodynamics Laboratory – Thermotechnics Subtask 2.1I : STUDY OF COMBUSTION AND HEAT TRANSFER PHENOMENA IN INDUSTRIAL FURNACES FIRED WITH GAS BURNERS USING PREHEATED AIR Contributor : Faculté Polytechnique de l’Université de Mons Thermal Engineering and Combustion Unit Subtask 2.4F : CHEMICAL KINETICS STUDIES OF FLAMES AND SOOT FORMATION Contributor : Université catholique de Louvain Institute of Mechanics, Materials and Civil Engineering
  • 4. Presentation of ECERC Studies at UCL Studies at UMons Studies at ULg Conclusions and Perspectives SUBTASK 2.4.F Chemical Kinetics Studies of Flames and Soot Formation Institute of Mechanics, Materials and Civil Engineering Pôle TFL – Thermodynamics and Fluid mechanics Université catholique de Louvain Véronique Dias and Hervé Jeanmart Veronique.Dias@uclouvain.be and Herve.Jeanmart@uclouvain.be
  • 5. Chemical Kinetics Studies of Flames and Soot Formation Experimental studies of hydrocarbons and/or oxygenated species, by analysis flame structures at low pressure Elaboration of kinetic model to understand emission formation: conversion of reactants, formation of pollutants, effects of additives… additives… Reduction of the kinetic model according to initial conditions Use of reduced mechanisms in industrial processes (engines, furnaces, boilers, …) Experimental studies 1.2E-01 2.00E+03 1.80E+03 1.0E-01 1.60E+03 Premixed flat flames stabilized on a 1.40E+03 Temperature (K) 8.0E-02 burner at low pressure, analyzed Mole fraction 1.20E+03 6.0E-02 1.00E+03 by: 8.00E+02 X-CO2 4.0E-02 -mass spectrometry (MS) X-TOLUENE X-C6H6 6.00E+02 4.00E+02 -or by gas chromatography (GC). 2.0E-02 Temperature 2.00E+02 0.0E+00 0.00E+00 0.00 0.33 0.65 0.96 1.28 1.61 1.93 Height Above the Burner (cm)
  • 6. Modelisation Elaboration of kinetic model Predict the evolution for concentrations of present species in the flame (from fresh gases to burned gases) Interest Obtain valuable informations: degree of conversion rate of reactants, formation rate of pollutants, effects of additives on the soot formation,… Integration of these kinetic mechanisms in CFD simulation models of industrial processes (engines, boilers, furnaces...) Elaboration of « UCL » kinetic model The kinetic model includes the detailed formation and consumption reactions of species from C1 to C10. It contains 568 reactions and 107 chemical species. This reaction mechanism has been extended and validated using flat flames experiments: -Methane (CH4), ethane (C2H6) -Ethylene (C2H4), acetylene (C2H2), isobutene (iC4H8) -Benzene (C6H6) -Dimethoxymethane (C3H8O2), diethoxymethane (C5H12O2), ethanol (C2H5OH) -Formaldehyde (CH2O), acetaldehyde (CH3CHO) http://veroniquedias.github.com/UCLouvain-Mechanism/
  • 7. Flames with additives Objectives of experiments φ C2H4 /O2 /Ar with C3H8O2 or C5H12O2 (φ = 2.5) 4.5E-02 Observe and measure the reduction of concentrations for the soot precursors (with 4.0E-02 φ constant) with additives C3H8O2 (DMM) et 3.5E-02 C5H12O2 (DEM). Fraction molaire 3.0E-02 By keeping the equivalence ratio constant,(φ), the ratio C/O decrease : 2.5E-02 → Reduction of mole fractions for 2.0E-02 hydrocarbons produced in the rich ethylene 1.5E-02 flame. - 19,8 % with DMM 1.0E-02 - 16,4 % with DEM Objectives of modelisation 5.0E-03 0.0E+00 Elaborate a kinetic model able to predict 0 10 20 30 the concentration of species present in these Distance au brûleur (mm) flames C2H2 Understand the effect of the additives on the reduction of soot precursors formation Flames of methylal (DMM) OH H CH3OCH2OCH3 H OH OH O OH O CH3OêHOCH3 (DMM2) CH3OCH2OêH2 (DMM1) CH3OCHO CH3OêH2 H OH CH3OêO O2 Rich flame of DMM M Lean flame of DMM H CH3O• CH2O O H OH OH O M OH HêO CO CO2 O2
  • 8. Conclusions and perspectives Elaboration of the reaction mechanism, named « UCL »: Past studies: Methane (CH4), ethane (C2H6) Ethylene (C2H4), acetylene (C2H2), isobutene (iC4H8) Benzene (C6H6) Dimethoxymethane (C3H8O2), diethoxymethane (C5H12O2) Ethanol (C2H5OH) Formaldehyde (CH2O), acetaldehyde (CH3CHO) Present studies: Acetic acid (CH3COOH) Future experimental and modeling studies of flame structure: Triacetine (C9H14O6) Methyl valerate or methyl pentanoate (CH3CH2CH2CH2COOCH3) => Use of the mechanism in industrial processes (engines, furnaces, boilers, …) Conclusions and perspectives Application of the mechanism of ethyl acetate and ethanol in an HCCI engine
  • 9. Publications 2008-2011: 17 articles ( ≈ 30 posters / oral presentations) V. Dias, J. Vandooren, Comb. and Flame 158 (2011) 848-859 ; V. Detilleux, J. Vandooren, Proc. Comb. Inst. 33 (2011) 217-224 ; X. Lories, J. Vandooren, D. Peeters, Int. J. Quant. Chem. DOI:10.1002/qua.23035 (2011) ; N. Leplat, P. Dagaut, C. Togbé, J. Vandooren, Comb. and Flame 158 (2011) 705-725 ; X. Lories, J. Vandooren, D. Peeters, Int. J. Quant. Chem. DOI:10.1002/qua.23142 (2011) ; X. Lories, J. Vandooren, D. Peeters, Computional and Theoretical Chemistry 966 (2011) 244-249 ; V. Dias, J. Vandooren, Fuel 89 (2010) 2633-2639 ; V. Dias, X. Lories, J. Vandooren, Combust. Sci. And Tech. 182 (2010) 350-364. N. Leplat, J. Vandooren, Combust. Sci. and Tech. 182 (2010) 436-448 ; X. Lories, J. Vandooren, D. Peeters, Phys. Chem. Chem. Phys. 12 (2010) 3762-3771 C. Renard, V. Dias, P. J. Van Tiggelen, J. Vandooren, Proc. Comb. Inst. 32 (2009) 631-637 ; V. Detilleux, J. Vandooren, J. Phys. Chem. A 113 (2009) 10913-10922 ; V. Dias, C. Renard, J. Vandooren, Z. Phys. Chem. 223 (2009) 565-577 ; V. Detilleux, J. Vandooren, Combustion, Explosion and Shock Waves 45 (2009) ; X. Lories, J. Vandooren, D. Peeters, Chem. Phys. Letters 452 (2008) 29-32 ; N. Leplat, A. Seydi, J. Vandooren, Combust. Sci. and Tech. 180 (2008) 519-532 ; V. Detilleux, J. Vandooren, Combust. Sci. and Tech. 180 (2008) 1347-1469; Presentation of ECERC Studies at UCL Studies at UMons Studies at ULg Conclusions and Perspectives
  • 10. SUBTASK 2.1.I Study of Combustion and Heat Transfer in Industrial Furnaces Fired with Gas Burners Using Preheated Air Faculty of Engineering of the University of Mons Pôle Energie – Thermal Engineering and Combustion Unit Delphine Lupant Delphine.Lupant@umons.ac.be POLYTECH = Faculty of Engineering of the University of Mons (founded thanks to the association of the University of Mons-Hainaut and the Faculty of Engineering of Mons) Research is organized around 5 multidisciplinary research centers : Information and Technologies Materials Risks Biochemical systems and bioprocesses (BIOSYS) Energy: Thermal Engineering & 3 themes : Combustion Unit Energy and buildings Combustion and problems of CO2 Transport and production of electrical energy
  • 11. Participation in ECERC since 1992 Context: Reduction of NOx emission in furnaces with air preheating at high temperature (Rational use of energy) Methodology: o Run experiments on furnaces built in our laboratory (funded by SPF) o Concurrently, use a commercial software (ANSYS Fluent) to model the combustion and use the measurements as validation data Benefits: o Guidance and services contracts for industrial partners (FIB, Drever) o Expertise in numerical modeling (AGC, Arcelor,…) Since 2000: Flameless Oxidation or Diluted Combustion = New Combustion technique which combine high efficiency + very low NOx emission Diluted combustion furnaces At semi-industrial scale (300kW) semi- o Commercial burner (REGEMAT WS) o Fired with natural gas + air o Furnace is available for international research partners (IFRF) o Used to test industrial burners (services contracts) o Main results: EXP: heat transfer, emissions, efficiency SIM: validation of global combustion models with temperature and species measurements in the furnace
  • 12. Diluted combustion furnaces At laboratory scale I (3kW) o Simplified geometry (co-flow) o Fed with natural gas or synthetic mixture (CH4, CO, H2, N2, CO2) The objective was to study the evolution of the operating conditions required to sustain diluted combustion with low calorific value gases (products from gasification of biomass or from steel industry) Diluted combustion offers a smart way to solve flame stabilization problems Preheated and Combustion chamber encountered in standard burners diluted air due to the significant variations of their heating value (fuel flexibility) Fuel Diluted combustion furnaces At laboratory scale II (30kW) = current project o Configuration similar to industrial furnaces (burner geometry, injection velocities, load) but at small scale 50%COG Species NG COG BFG Wood gas 50%BFG CH4 90% 35% - 18% 1% H2 - 60% 5% 33% 16% CO - 5% 25% 15% 21% Fuel CO2 1% 25% 13% 12% Preheated air N2 2% 45% 21% 50% The objective is to study the evolution of the heat transfer (in the furnace and to the load), the combustion efficiency, the NO and CO emissions with those alternative fuels and give rules of design for industrial furnaces Interest from industrial partner (sponsorship from Arcelor-Mittal)
  • 13. Publications 2006-2011 1 D. Lupant, B. Pesenti, E. Sezgin, P. Lybaert: Flameless combustion of CH4/CO/H2 fuel blends Proceedings of the "European Combustion Meeting ECM 2011", Cardiff, 2011 2 E. Sezgin, D. Lupant, B. Pesenti, P. Lybaert: Développement de diagramme de stabilité de flamme en combustion diluée, Actes du Congrès Annuel de la Société Française de Thermique, pp 351-356, 2010 3 D. Lupant, B. Pesenti, P. Lyabert: Impact des sondes de prélèvement sur la mesure d’espèces réactives en oxydation sans flamme, Actes du Congrès Annuel de la Société Française de Thermique, pp 363-368, 2010 4 D. Lupant, B. Pesenti, P. Lybaert: Influence of probe sampling on reacting species measurement in diluted combustion, Experimental Thermal and Fluid Science 34, 516–522, 2010 5 E. Sezgin, B. Pesenti, D. Lupant, P. Lybaert: Development of stability diagrams of flame in diluted combustion, Proceedings of the "European Combustion Meeting ECM 2009", Vienne, 2009 6 G. Seggio, B. Pesenti, P. Lybaert, P. Ngendakumana: Feasibility study of the diluted combustion in a semi- industrial boiler at low temperatures, Proceedings of the 8th european conference on industrial furnaces and boilers, Vilamoura, 2008 7 D. Lupant, B. Pesenti, P. Lybaert: Characterization of flameless combustion of natural gas in a laboratory scale furnace, Proceedings of the "European Combustion Meeting ECM 2007", Chania, 2007 8 D. Lupant, B. Pesenti, P. Evrard, P. Lybaert: Numerical and experimental characterization of a self-regenerative flameless oxidation burner operation in a pilot-scale furnace, Combustion Science and Technology (I. Glassman and R. A. Yetter eds.), Vol 179: 437–453, 2007 9-10 D. Lupant, B. Pesenti, P. Lybaert: Assessment of combustion models of a self-regenerative flameless oxidation burner, Proceedings of the 7th European Conference on Industrial Furnaces and Boilers, Porto, 2006 + Proceedings of the 7th National Congress on Theoretical and Applied Mechanics, Mons, 2006 Presentation of ECERC Studies at UCL Studies at UMons Studies at ULg Conclusions and Perspectives
  • 14. SUBTASK 2.1.H The use of liquid biofuels in heating systems : a review University of Liège Thermodynamics Laboratory – Thermotechnics Philippe Ngendakumana pngendakumana@ulg.ac.be 17% of CO2 emissions in Europe are related to space heating function of gas and oil-fired boilers Ref: ecoboiler.org
  • 15. There are different pathways to convert biomass to biofuels Vegetable oils combustion is feasable if the viscosity is reduced Vegetable oil viscosity is 35 mm²/s at 40° compared C to 2.7mm²/s for gasoil it must be reduced by preheating (to 80° or C) mixing to gasoil LHV of vegetable oils (37MJ/kg) 10% lower than LHV of diesel (43MJ/kg) Vegetable oil must be appropriately stored to avoid oxidation and filtration problems
  • 16. CO emissions reduction with vegetable oil addition Alonso et al., Energy & Fuels, Vol. 22, No 5, 2008. Biodiesels are good candidates to petroleum diesel fuel substitution Biodiesels have similar physical properties to diesel fuels (viscosity 4mm²/s at 40° C) LHV of biodiesels (37MJ/kg) 10% lower than LHV of diesel (43MJ/kg) Quality requirements are defined in the standards EN14213 They are quite stable but strong oxidizing agents must be avoided
  • 17. Burning biodiesel decreases most pollutants emissions Macor et Pavanello, Energy, Vol. 34, pp. 2025-2032, 2009. Bioethanol combustion in heating systems is more problematic Bioethanol is less viscous than diesel and can lead to lubrification problems in the pumps LHV of bioethanol is 35% lower than that of the diesel quantity of fuel injected must be adapted (greater capacity injection nozzle or increased injection pressure) Storage is more hazardous as bioethanol flash point is around 13° (compared to 60° for diesel fuel) C C
  • 18. Bioethanol flame emissivity decreases compared to diesel fuel flame emissivity Barroso et al., Fuel processing technology, Vol. 91, pp. 1537-1550, 2010. Bioliquids combustion in heating systems: Some conclusions Vegetable oils can be burnt in boilers if their viscosity is reduced Biodiesels are good candidates to fuel oil substitution. Pollutants emissions are mainly decreased but there is no clear trend for NOx emissions Bioethanol combustion is more difficult to achieve in conventional burners (low viscosity, low energy content, low vapor pressure, different flame emissivity)
  • 19. Future work : What are the effects of fuel composition on flame temperature and pollutants emission? 370 KW boiler equipped with visualisation windows We will burn biodiesels of various origins and compositions: to evaluate the effects of fuel composition on flame temperature and NOx emissions to evaluate the boiler performance working with different biodiesels Other topics • Combustion control and performance of household condensing boilers • Feasibility study of the diluted combustion in a semi-industrial boiler at low temperatures (compared to furnaces) • Combustion of wood pellets in a domestic heating boiler
  • 20. Publications 2006-2011 L. Arias, S.Torres, D. Sbarbaro, P. Ngendakumana : On the spectral bands measurements for combustion monitoring, doi:10.1016/j.combustflame.2010.09.018 D. Makaire, P. Ngendakumana : Simulation model of a gas-fired condensing boiler at full load operation in steady- state regime, ASME-ATI-UIT 2010 Conference on Thermal and Environmental Issues in Energy Systems. D. Makaire, P. Ngendakumana : Modelling the thermal efficiency of condensing boilers working in steadystate conditions, Paper presented at 21st "journées d'études" of the Belgian Section of the Combustion Institute, Liège (Belgium), May 2010 D. Makaire, P. Ngendakumana : Modèle de simulation des performances d'une chaudière fioul à condensation de chauffage domestique, Energies et transports durables : SFT10, Le Touquet (France), 25-28 mai 2010 K. Sartor, P. Ngendakumana : Natural Gas as an Alternative Fuel for Spark Ignition Engines, Paper presented at 21st "Journées d’Etudes" of the Belgian Section of the Combustion Institute, Liège (Belgium), May 2010 Luis E. Arias Parada. Arias : Photodiode-based sensor for flame sensing and combustion process monitoring, by means the global detection of flame spectral information, PhD thesis, University of Concepcion (Chile), March 2009 D. Makaire and Ph. Ngendakumana, Simulation model of a semi-industrial fuel oil boiler in steady-state regime. Proceedings of the 5th European Thermal-Sciences Conference (EUROTHERM 2008). Eindhoven (The Netherlands), May 18-22, 2008 G. Seggio, B. Pesenti, P. Lybaert, P. Ngendakumana: Feasibility study of the diluted combustion in a semi-industrial boiler at low temperatures, Proceedings of the 8th european conference on industrial furnaces and boilers, Vilamoura, 2008 A. Ballant, D. Makaire, P. Ngendakumana : Modelling of a domestic gas-fired condensing boiler, Paper presented at 21st "journées d'études" of the Belgian Section of the Combustion Institute,, GENT (Belgium), May 6-8, 2008 Presentation of ECERC Studies at UCL Studies at UMons Studies at ULg Conclusions and Perspectives
  • 21. Conclusions and Perspectives Future works: Combustion of gases with low calorific values in furnaces(UMons-UCL) Transition from commercial to open-source CFD software for combustion (UMons-UCL) Feasibility studies of diluted combustion without air preheating (UMons-ULg) Lending of experimental equipments, troubleshooting of experiments and measurement techniques (ULg-UMons-UCL) Conclusions and Perspectives Complementary themes and efforts among Belgian partners Balance between fundamental and applied research Scientific production (publications, thesis) Outcomes: Kinetic models (UCL) Experimental database (UCL, UMons) Semi-industrial size test facilities (UMons, ULg) Perspectives: Facilities available for industrial test Industrial deployment of numerical tools and know how Insights into long-term research plans at an international level through the ECERC agreement (TLM and ExCo)