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Technical Paper

Characteristics of particle emissions and their atmospheric dilution during co-combustion of coal and wood pellets in a large combined heat and power plant

, , , ORCID Icon, , , , , , , , , , & ORCID Icon show all
Pages 97-108 | Received 21 May 2018, Accepted 05 Sep 2018, Published online: 07 Nov 2018

Figures & data

Table 1. Properties of coal and industrial pellets (Mylläri et al. Citation2017).

Figure 1. (a) Measurement setup used in stack measurements. (b) Measurement setup installed in the helicopter.

Figure 1. (a) Measurement setup used in stack measurements. (b) Measurement setup installed in the helicopter.

Table 2. Flue-gas concentrations of CO2, SO2, NOx, O2, and CO, total particle number (Ntot, >2.5 nm), dust, flue-gas flow rate, and temperature in the stack during the measurements. Mean values (± standard deviation) are presented for both flue-gas cleaning situations (“FGD+FF off” and “FGD+FF on”) for coal + 10.5% industrial pellets. Emission factors for BCPM1 (EFBC, ng MJ−1) and emission factors for particle number and mass (MJ−1 and μg MJ−1) are shown for the co-combustion situation and coal combustion situation. See Supplementary Table SI1 for CO2, SO2, NOx, N>2.5 nm, and dust concentrations in (mg Nm−3 or m−3) when reduced to 6% O2.

Figure 2. (a) Particle number size distribution of solid particles measured at the stack in “FGD+FF on/off” situations with ELPI and SMPS. (b) Particle volume size distribution calculated from SMPS and ELPI results. (c, d) TEM images of particles collected on TEM grids in (c) “FGD+FF off” and (d) “FGD+FF on” situations. A mixture of industrial pellets and coal was used as a fuel in the experiment.

Figure 2. (a) Particle number size distribution of solid particles measured at the stack in “FGD+FF on/off” situations with ELPI and SMPS. (b) Particle volume size distribution calculated from SMPS and ELPI results. (c, d) TEM images of particles collected on TEM grids in (c) “FGD+FF off” and (d) “FGD+FF on” situations. A mixture of industrial pellets and coal was used as a fuel in the experiment.

Figure 3. Concentration of CO2 (black line, ppm, y-axis on the left), concentration of SO2 (blue line, ppb, y-axis on the left), and ΔNtot (red line, 1 cm−3, y-axis on the right) in flue-gas plume diluting in the atmosphere as a function of flue-gas plume age after the emission from stack. ΔNtot is the particle number concentration in the flue-gas plume after subtracting the background particle number concentration from measured values. The gray vertical lines present the 2-km distance from the stack. A mixture of 10.5% industrial pellets and coal was used as a fuel in the experiment.

Figure 3. Concentration of CO2 (black line, ppm, y-axis on the left), concentration of SO2 (blue line, ppb, y-axis on the left), and ΔNtot (red line, 1 cm−3, y-axis on the right) in flue-gas plume diluting in the atmosphere as a function of flue-gas plume age after the emission from stack. ΔNtot is the particle number concentration in the flue-gas plume after subtracting the background particle number concentration from measured values. The gray vertical lines present the 2-km distance from the stack. A mixture of 10.5% industrial pellets and coal was used as a fuel in the experiment.

Figure 4. Median particle number size distribution measured from the atmosphere with a helicopter in “FGD+FF off/on” (upper/ lower) situations. The measurement data were classified to 5-sec time intervals based on the plume age. Measurements were made with EEPS. The mixture of industrial pellets and coal was used as a fuel during the experiment.

Figure 4. Median particle number size distribution measured from the atmosphere with a helicopter in “FGD+FF off/on” (upper/ lower) situations. The measurement data were classified to 5-sec time intervals based on the plume age. Measurements were made with EEPS. The mixture of industrial pellets and coal was used as a fuel during the experiment.
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