Figures & data
Figure. 1. Probability Density Function for a ratio of
, obtained using Equation (10) at
and various values of the Reynolds-averaged combustion progress variable
, specified in legends.
![Figure. 1. Probability Density Function P2(R2,c¯) for a ratio of R2=(∇⋅ρD∇cˆ+Wˆ)/(ρuSL|∇c|ˆ), obtained using Equation (10) at Δ/δL=1.15 and various values of the Reynolds-averaged combustion progress variable c¯, specified in legends.](/cms/asset/c5a59a5b-9bf9-4797-ab4b-d9b52defac1d/tctm_a_1520304_f0001_oc.jpg)
Figure 2. Probability Density Functions (a) and (b)
for a ratio of
. Different curves show results obtained using different normalised filter widths
, specified in legends.
![Figure 2. Probability Density Functions (a) P3(R3,c¯=0.5) and (b) Pω,3(ωˆ=0.15±0.005,R3,c¯=0.5) for a ratio of R3=Wˆ/ρχˆ. Different curves show results obtained using different normalised filter widths Δ/δL, specified in legends.](/cms/asset/56de390b-b6c7-4486-a014-6563c1519335/tctm_a_1520304_f0002_oc.jpg)
Figure 3. Reaction rate (red double-dashed-dotted line), FSD
(black double-dotted-dashed line), SDR
(blue dotted-dashed line), and ratios of
(black short-dashed line) and
(blue long-dashed line) vs. the normalised distance
counted from the position of peak rate
in the laminar flame that propagates from right to left.
![Figure 3. Reaction rate W/ρu (red double-dashed-dotted line), FSD SL∇c (black double-dotted-dashed line), SDR ρD∇c⋅∇c/ρu (blue dotted-dashed line), and ratios of W/(ρuSL∇c) (black short-dashed line) and W/(ρD∇c⋅∇c) (blue long-dashed line) vs. the normalised distance ξ=xmax{|∇c|(x)} counted from the position of peak rate W/ρu in the laminar flame that propagates from right to left.](/cms/asset/59f7fb3a-1dc5-4286-ba74-c3d25f848de0/tctm_a_1520304_f0003_oc.jpg)
Figure 5. (a) Ratios (dotted-dashed and dotted lines) and
(dashed and solid lines) conditioned to the filtered combustion progress variable
and evaluated using various normalised filter widths
specified in legends at the Reynolds-averaged combustion progress variable
. (b) A ratio of
conditioned to
and evaluated using
(solid and dashed lines) and 1.73 (dotted-dashed lines) at various values of the Reynolds-averaged combustion progress variable
, specified in legends.
![Figure 5. (a) Ratios ⟨R3|ρcˆ/ρˆ⟩=⟨Wˆ/ρχˆ|ρcˆ/ρˆ⟩ (dotted-dashed and dotted lines) and ⟨R4|ρcˆ/ρˆ⟩=⟨(∇⋅ρD∇cˆ+Wˆ)/ρχˆ|ρcˆ/ρˆ⟩ (dashed and solid lines) conditioned to the filtered combustion progress variable ⟨ρcˆ/ρˆ⟩ and evaluated using various normalised filter widths Δ/δL specified in legends at the Reynolds-averaged combustion progress variable c¯=0.5. (b) A ratio of ⟨R2|ρcˆ/ρˆ⟩=⟨(∇⋅ρD∇cˆ+Wˆ)/(ρuSLΣˆ)|ρcˆ/ρˆ⟩ conditioned to ⟨ρcˆ/ρˆ⟩ and evaluated using Δ/δL=1.15 (solid and dashed lines) and 1.73 (dotted-dashed lines) at various values of the Reynolds-averaged combustion progress variable c¯, specified in legends.](/cms/asset/5274411d-2394-4968-b9e4-3d7d05049744/tctm_a_1520304_f0005_oc.jpg)
Figure 6. Mean reaction rate vs. Reynolds-averaged combustion progress variable . 1 –
. 2 –
, where
[Citation27], 3 –
, where the ratio
is averaged over all cells characterised by
, 4 –
, where the ratio
is averaged over transverse plane provided that
.
.
![Figure 6. Mean reaction rate vs. Reynolds-averaged combustion progress variable c¯. 1 – Wˆ¯/ρu. 2 – 2ρχˆ¯/[ρu(2cm−1)], where cm=0.88 [Citation27], 3 – ⟨R3⟩ρχˆ¯/ρu, where the ratio ⟨R3⟩=⟨Wˆ/ρχˆ⟩ is averaged over all cells characterised by 0.01<cˆ(x,t)<0.99, 4 – R3¯ρχˆ¯/ρu, where the ratio R3¯(c¯) is averaged over transverse plane provided that 0.01<cˆ(x,t)<0.99. Δ/δL=2.88.](/cms/asset/f05ede1f-771f-4419-97aa-530bda6d651c/tctm_a_1520304_f0006_oc.jpg)
Figure 7. Subgrid conditioned PDFs obtained at
and (a)
or (b)
. Note that the PDFs are shown in linear and logarithmic scales in (a) and (b), respectively. The PDF sampling was performed for all grid points within a filter volume centred around a point
at instant
, followed by averaging the PDFs
for all
and
such that
. Values of
are specified in legends.
![Figure 7. Subgrid conditioned PDFs Pˆ(c|cˆ) obtained at c¯=0.5 and (a) Δ/δL=1.15 or (b) Δ/δL=2.88. Note that the PDFs are shown in linear and logarithmic scales in (a) and (b), respectively. The PDF sampling was performed for all grid points within a filter volume centred around a point x at instant t, followed by averaging the PDFs P(c,x,t) for all x and t such that cˆ∗+0.005≤cˆ(x,t)<cˆ∗+0.005. Values of cˆ∗ are specified in legends.](/cms/asset/7755aab2-f0a4-4693-bbf2-f39878f2ded3/tctm_a_1520304_f0007_oc.jpg)