Introduction to biomass combustion and pollutant reduction in wood stoves and boilers

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Introduction to biomass combustion and pollutant reduction in wood stoves and boilers
Introduction
          to biomass combustion
          and pollutant reduction
          in wood stoves and boilers

          Prof. Dr. Thomas Nussbaumer

          Verenum Research, Zürich
          Lucerne University of Applied Sciences and Arts, Horw
          Swiss Federal Office of Energy, Delegate in IEA Task 32

          Switzerland

          IEA Webinar 06 May 2021

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Introduction to biomass combustion and pollutant reduction in wood stoves and boilers
Content

          1. Intro: The role of bioenergy for
                         a) Energy Supply / Climate Change

                                   b) Air Pollution

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Introduction to biomass combustion and pollutant reduction in wood stoves and boilers
World energy supply 1990 to 2017
          Total in ktoe/a                                               Share in %

                                                                                Coal

                                                                          Natural Gas

                                                                            Nuclear
                                                                                Hydro

                                                                                                           Wind, Solar
                                                        olar
                                      Hydro   W   ind&S                                     Wind&Solar
                                                                       Biofuels and waste
                                                                                                         9.1%

                                                                                  Oil

                            https://www.iea.org/data-and-statistics   20.1.20

Facts or hypotheses
1. Solar energy has largest potential but causes need for energy storage
2. Wood from sustainable forestry is renewable and net CO2 free (and easily storable)
      Verenum             and can ideally complement solar energy as storable fuel
Introduction to biomass combustion and pollutant reduction in wood stoves and boilers
Target conflict

          Global effect of smoke from biomass on mortality
          Mio deaths per year

Verenum                         [OECD/IEA: Energy Poverty, IEA, Paris 2010]
Introduction to biomass combustion and pollutant reduction in wood stoves and boilers
Content

          1. Intro

          2. Pollutant formation with focus on Particulate
             Matter (PM) and Organic Compounds (OC)

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Introduction to biomass combustion and pollutant reduction in wood stoves and boilers
Pollutants from biomass combustion

                                   CO
                                                    + hn      SOA
                                 VOC
                             EC + POA
                                                                PIA
                                                                      PM10
  hn                                           Salts
                                                                SIA
                                               NOx
               CO2

Cfix
            C
       Ca, K, Cl, N

           Ash
          CaO, KCl, ..

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Introduction to biomass combustion and pollutant reduction in wood stoves and boilers
Products from                        Products from Incomplete Combustion                                           Products from
             Complete                                            (PIC)                                                          Complete
            Combustion                                                                                                         Combustion
          Solid            Particulate              Matter                       G a s         p h a s e             p o l l u t a n t s

                                                                                                                                                                         Chimney
                                                                  Droplets Gas

                                    Biomass
                Salts                + Char
                                                   Soot               COC                  VOC              CO            CO2        H2O      NOX

                                     > 10 µm       < 100 nm
                                                  –H2                                              +O2              +O2

    KCl, K2SO4               Ash                    PAH
     oxides                 CaCO3                                                 t<   t>                             Gas phase
                                                                                                                      combustion
     < 100 nm             > 1–10 µm

                                                                                                                                                in combustion chamber
                                                 T > 800°           T < 800°      T > 550°

                                                                                                                                                 Consecutive reactions
                                                              O2 = 0

                                                                                                                                                                            by secondary air
                                                                                                                       +O2
   Condensation                                                                                             CO
                                                        Secondary >700°            Primary
    Coagulation                                            Tars                     Tars

     Nucleation                                                                   O2 = 0
                                                                                   CmHn        +O2          +O2
                                                                                  CO, H2     T > 800°      +CO2
                                                                    Devolatilisation Pyrolysis                        Gasification

                                                                                                                                                Solid fuel conversion
  K+, Na+, Cl–, SO 42–,                                                                                      C
   OH –, CO 32–, NO 3–      CaCO3                                                                          (Char)

                                                                                                                                                                             by primary air
                                              u > 0.1 m/s                        T > 300° + O2

                                                                                                                                                     in fuel bed
Zn-, Mg-, Fe-, Al-oxides
Waste: Cu, Cr, Pb, (Cd)                                                          CxHyOz
                          Evaporation                                                                         T > 100°
    Evaporation           Entrainment                                              H2O
                                        1      u > 0.1 m/s
                     2
                                               T > 800°                   K, Na, Ca, S, Cl, N

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u Gas velocity, t Residence time,  short/long    COC: Condensable Organic Compounds
1 Solid-particle-path, 2 Solid-vapour-particle-path VOC: Volatile Organic Compounds           T: [Evans and Milne, 1987], H 2: [Jess, 1996]
Introduction to biomass combustion and pollutant reduction in wood stoves and boilers
PM10                                   Atmosphere
        PIA                 POA + EC/BC                     SOA

Solid        Particulate      Matter                      G a s     p h a s e        p o l l u t a n t s

                                                                                                                         Chimney
                                          Droplets Gas

                  Biomass
    Salts          + Char
                              Soot             COC                VOC         CO

            100 000
[mg/Nm3]
(11% O 2)
             10 000

 CO
              1 000

                100

                                                                                  [Nussbaumer, T., Energy & Fuels,
                10                                                                17, No 6, 2003, 1510–1521, 17]
                      0       1           2          3          4       [–]   5   [Lauber, A.; Nussbaumer, T., 13th ETH-Con-
                                                                                  ference on Combustion Generated Nano-

   Verenum                                                   λ
                                              Excess Air Ratio l                  particles, June 22 – 24 2009, Zurich 2009]
Introduction to biomass combustion and pollutant reduction in wood stoves and boilers
Solid            Particulate     Matter                  G a s    p h a s e   p o l l u t a n t s
                                                   Droplets Gas

                                Biomass
                Salts            + Char
                                          Soot         COC                VOC     CO

SCHMID energy solutions

                  Graph: [Schmid]

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Introduction to biomass combustion and pollutant reduction in wood stoves and boilers
Solid     Particulate       Matter                   G a s                       p h a s e                   p o l l u t a n t s
                                      Droplets Gas

               Biomass
  Salts         + Char
                            Soot          COC                                 VOC                       CO

  Influence of combustion phase                                                        Influence of operation
             Start-up                                                                     (log wood boiler)

                                                        PM [mg/mn3] @13% O2
                                                                                                                                                            d   )
                                                                                                                                                      t (ba
                                                                                                                                               star

                                                                                                                            o   d)
                                                                                                                      t (go
                                                                                                               star

                                                                                                   ry
                                                                                            iona
                                                                                     stat

                                                                                                               CO               [mg/m n3] @13% O 2

     [Bäfver, L. et al, Biomass and                                              [Good, J., Obermayr, D., Nussbaumer, T.,
    Bioenergy 35 (2011) 3648–3655]                                            11. Holzenergie-Symposium, ETH Zürich 2010]

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Solid         Particulate             Matter                      G a s    p h a s e           p o l l u t a n t s
                                                          Droplets Gas

                             Biomass
             Salts            + Char
                                             Soot             COC                VOC          CO

Toxicity             low                 medium                 high

                              Influence of operation ... and technology

                                                                                       [P. Zotter et al., Environ. Sci. Technol.,
                                                                                            2019 Apr 2; 53(7): 3959-3968]
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 [Klippel, N.; Nussbaumer, T., 15th Eur. Biomass Conf., Berlin 2007]
Content

          1. Intro

          2. Pollutant formation

          3. Measures for resid. wood combustion (RWC)
             3.1 Primary measures

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Measure 1
                                                   e.g. in wood stoves
Diffusion
flame
                                        1000°
                                     O2 = 0
       O2

        [H.R. Christen, Allgemeine Chemie, 1971]

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1-stage combustion

                               CO2, H2O, O2, N2
                                  CO, CxHy

                                         + air at
                                          l>1
                                         O2 + N2

                                wood C H O

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Limitations

     Problem 6:                            Problem 4:
  flame quenching                      gas tightness inside

                                           Problem 3:
     Problem 5:                            air tightness
  heat release from
combustion (radiation)
                                            Problem 2:
                                       mixing of gas and air

                                            Problem 1:
                                          air distribution

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Limitations

   Problem 6:
flame quenching
                                Overfilling can cause quenching

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Avoid quenching

                            3. hot combustion chamber

                            2. Mixing improvement

                            1. Quenching avoided

air
                            and (additionally and mandatory):

                                    appropriate start-up ..

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.. appropriate start-up: technology dependent,
                  e.g. for updraft as a rule: ignition from the top

                    [www.holzenergie.ch]                         [www.holzenergie.ch]

[T. Nussbaumer et al., EU Biomass Conference 2008]   [H. Hartmann, 20th ETH-Conf. on Nanop., Zürich, 2016]

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Appropriate fuel: technology dependent

                                      Moisture content                                                                        Log size
              10,000                                                                                    300
                                CO   OGC                                                                                           Stove 1   Stove 2     Stove 3
                                                                                         mg/Nm³
                                                                                         (13 250
    mg/Nm³
      8,000
   (13 % O2)
                                                                                             % O2)
                                                                                                                       211                             Undiluted flue gas

                                                                                    Particle emission
Gaseous emission

                                                                                                        200
                   6,000
                                                                                                        150
                                                                                                              123
                   4,000                                                                                                     105
                                                                                                                                             85
                                                                                                        100
                                                                                                                                                               65    74
                   2,000                                                                                                                34
                                                                                                        50
                                                                                                                                                  22                      21
                      0                                                                                  0
                           0     5   10      15     20    25    30   35   %
                                                                          40   45                                    n=3                   n=3                       n=3
                                          Fuel moisture content                                                     5x5 cm               7x7 cm                     9x9 cm
                                                                                                                                         Log size
                                                                                                                                   Stove 1    Stove 2      Stove 3

                                                     [H. Hartmann, 20th ETH-Conf. on Comb. Gen. Nanoparticles, Zürich, 2016
                                                           and TFZ-Bericht 36, www.tfz.bayern.de] and additional info by
                                                         [R. Mack et al. Central European Biomass Conference, Graz 2020]

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Measure 2
                                                   e.g. in wood boiler
Diffusion                                                        Premixed
flame                                                            flame                                     1540°

                                      1000°                                                                1560°
                                      O2 = 0                                                               520°
       O2                                                                                                  O2 > 0
                                                                                                           300°

                                                                         O2

        [H.R. Christen, Allgemeine Chemie, 1971]                          [H.R. Christen, Allgemeine Chemie, 1971]

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2-stage combustion: principle in downdraft boiler

                                               wood CHoval
                                                      HO
                                                       Hoval

                                                              + air with
                                                              l1              T > 800o
                                                                                 t > 0.3-0.5 s

                                                  CO2, H2O, N2

 Verenum   [Nussbaumer, Energy & Fuels, Vol. 17, No 6, 2003, 1510–1521, 17]
Titel              2-stage combustion: examples in stoves
            Bionic Fire                                            Tiba (Sirius)                            Attika (Juna)

                                                                                                                  https://attika.ch/
 Specht TwinFire Xeoos http://www.specht-ofen.de             Tiba AG & Hochschule Luzern 2012
                                                                                                         [Zotter et al. 2017, 21st ETH Conf.
[W. Wiest., 13. Holzenergie-Symposium, Zürich 2014]   [T. Nussbaumer & P. Odermatt, TGA 5 2013, 54–58]     on Comb. gen. Nanoparticles]

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Improvements since 1975/80
Titel

                Boilers                                                        Stoves
        [BEST (formerly BLT), AUT]                                             [HKI, GER]
                                                                  Industrieverband Haus-, Heiz und Küchentechnik   PM

                                                                   CO                PM

   [L. Lasselsberger, BLT Wieselburg (A) 2016]]            [V. Schmatloch, Kachelofen&Kamin, Januar 2018]

                                                  Approach: "Technical Guidelines for design of low emission
                                                    stoves, presentation 2 by Morten Warming (DTI, DK)

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Anforderungen für tiefe Emissionen
                    „Gap“
         between type-test and reality

      chimney sweeper measurements
               PM real-life

                                                        PM type-test

                                          Conclusion:        „no correlation“

                                                [German Biomass Research Center –
Verenum                              Deutsches Biomasseforschungszentrum, DBFZ, Leipzig 2014]
Anforderungen für tiefe Emissionen
                    „Gap“
         between type-test and reality

                       Approach: "Real life" test methods:
                 presentation 3 by Gabriel Reichert (BEST, AUT)

Verenum   [C. Schmidl et al., «Be Real» 14. Holzenergie-Symp., Zürich 2016]
Content

          1. Intro

          2. Pollutant formation

          3. Measures
             3.1 Primary measures
             3.2 Secondary measures

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Titel                                                                            Electrostatic
                          Catalysts    Aerosols
                                           Inserts from Biomass               Precipitators (ESP)
                                       Combustion

                                                                                                      [Oekosolve
                                                                                                      2019]

                CO         > 70%               CO            > 70%
 Reduction

                VOC        > 40%               VOC           > 70%

                PM        30% - 40%             oxidizable PM                         PM        60% - 80%

                                                                              [V. Schmatloch, EMPA    [D. Jud, Oekosolve,
              [G. Reichert et al., BEST, 13.    [M. Aleysa, Fraunhofer IBP,                            CEBC Graz 2020]
             Holzenergie-Symp., Zürich 2014]                                     Dübendorf, 2004]
                                               15. Holzenergie-Symp., 2018]

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Titel                                                 Electrostatic
           Catalysts Aerosols   Inserts from Biomass
                                                   Precipitators (ESP)
                     Combustion
                     Pressure drop         Temperature control needed

             Aging                               Soot causes re-entrainment

           Limited effect during cold start       and/or limited availability

                              Periodic cleaning needed

                                                            a s ure s         easures
                                                 nd ary me         primary m bustion
                                           Seco        repla ce)       lete com
                                            t (but not    o f in c omp
                                   om plemen d in case
                             can c y are limite
                             ince the
                            s
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Content

          1. Intro

          2. Pollutant formation

          3. Measures

          4. Consequences for low emissions

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Requirements for low emissions
1.   Appropriate ignition and start-up
2.   Appropriate fuel (moisture, size, ash) and fuel amount
3.   Technology with 2-stage combustion, secondary air and hot comb. chamb.:
                  Target for T T T:   l = 1.5-2.5, T > 800o, t > 0.3-0.5 s
                  Options:            - forced draft with ventilator
                                      - inserts for mixing and/or catalytic effect
                                      - combustion control
4.   Optional secondary measure: ESP with monitoring
5.   For boilers: heat storage tank

         Remaining challenges:        - cold start
                                      - ambient conditions, mostly for natural draft
                                      - operator influence

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Requirements for low emissions

          are valid for all combustion types

                          but:

                    - for automatic combustion safely applicable
                      (in small scale for wood pellets)

                    - for manual devices highly challenging
                      most important in real-life

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PM emissions in small scale in real-life conditions

 limit for boilers 20 mg/m3
   with uncertainty 31 mg/m3:
                                                         pellet boilers: 64% meet emission limit
                                                         other boilers: 25% meet; 75% exceed

                   PM in mg/m3 @ 13 % O2

                   [A. Kather, N. Woltersdorf: Feinstaubemissionen aus biomasse-befeuerten
Verenum                        Kleinfeuerungsanlagen, IET, TUHH, Hamburg 2013]
1. Intro

          2. Pollutant formation

          3. Measures

          4. Consequences

          5. Conclusions

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1.   RWC contributes to PM and OC hence their emissions need to be reduced
2.   Primary measures are:
         - combustion design
         - ideal start-up and appropriate fuel
         - ideal operation with appropriate air supply and high temperature
3.   The technology has been improved by:
         - thermal insulation, air tightness, secondary air and hot combustion ch.
         - modern devices achieve low emissions on test-bench
4.   Secondary measures can further reduce emissions,
         but cannot replace primary measures
5.   Main reason for high impact of RWC is the
         «gap» between test-bench results and non-ideal operation in real life
6.   Control systems and monitoring can assist to improve real-life operation
7.   Information und inspections remain necessary

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Acknowledgements
          Swiss Federal Office of Energy
          Swiss Federal Office for the Environment
          Swiss National Research Foundation
          Innosuisse and SCCER Biosweet
          IEA Bioenergy Task 32

          Info
          www.verenum.ch
          www.hslu.ch
          www.holzenergie-symposium.ch

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