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MRGC performance evaluation model of gas leak infrared imaging detection system

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Abstract

Gas leak infrared imaging detection technology has become one of the most effective means to detect gas leaks. We propose a novel MRGC (minimum resolvable gas concentration) model that is suitable for evaluating the performance of passive GLIIDSs (gas leak infrared imaging detection systems). An MRGC equivalent calculation method and a direct MRGC measurement method based on the MRTD (minimum resolvable temperature difference) model are also proposed. The MRGC measurement system is designed and built. The measured and calculated results are in good agreement, which verifies the MRGC model’s correctness and demonstrates the effectiveness of the MRGC performance evaluation method.

© 2014 Optical Society of America

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Figures (11)

Fig. 1
Fig. 1 Image of the four-bar pattern.
Fig. 2
Fig. 2 Part of the infrared absorption spectrum of ethylene (1ppm·m@296K, Pacific Northwest National Laboratory).
Fig. 3
Fig. 3 MRGC measurement target and gas chamber.
Fig. 4
Fig. 4 Schematic diagram of the MRTD measurement system.
Fig. 5
Fig. 5 Plot of the simulated MRTD(f) curve.
Fig. 6
Fig. 6 Plot of the simulated MRGC(f, Tgas) surface.
Fig. 7
Fig. 7 Plots of the simulated MRGC(f) curves for various gas temperatures.
Fig. 8
Fig. 8 Plot of the relationship between MRGC(f0) and the gas temperature Tgas (the blue curve). The red vertical line is the asymptote Tgas = 300 K.
Fig. 9
Fig. 9 Block diagram of the MRGC measurement system.
Fig. 10
Fig. 10 Setup of the MRGC measurement system.
Fig. 11
Fig. 11 Results of the calculated and measured MRGC of ethylene [Tgas ≈293.15 ± 0.2 K; the green line is the calculated MRGC value (corresponding to the left axis), the red line is the measured MRGC value (corresponding to the left axis), and the blue line is the measured negative MRTD value (corresponding to the right axis)].

Equations (15)

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SNR 0 = V s V n = ΔT NETD
V s V n = D 0 2 αβ 4 ( A d Δf ) 1/2 λ 1 λ 2 D * ( λ ) τ α ( λ ) τ 0 ( λ )Δ M tb dλ
Δ M tb = ε t ( λ )M( λ, T t ) ε b ( λ )M( λ, T b )
M( λ,T )= c 1 λ 5 1 exp( c 2 / λT )1
Δ M tb b =M( λ, T t )M( λ, T b ) T M(λ, T b )ΔT
SNR V (f)= p corr ( f ) SNR 0 = p corr ( f ) D 0 2 αβ 4 ( A d Δf ) 1/2 λ 1 λ 2 D * ( λ )Δ M tb dλ = p corr ( f )ΔT D 0 2 αβ 4 ( A d Δf ) 1/2 λ 1 λ 2 D * ( λ ) M(λ, T b ) T dλ
MRTD(f)= SNR DT NETD p corr (f) = SNR DT p corr ( f ) D 0 2 αβ 4 ( A d Δf ) 1/2 λ 1 λ 2 D * ( λ ) M(λ, T b ) T dλ
SNR V = p corr V s V n
Δ M gas-b =[ 1 τ gas ( λ ) ]M( λ, T gas )+ τ gas (λ)M( λ, T t )M( λ, T b )
τ gas ( λ )=exp[ α gas ( λ )cl ]
Δ M gas-b (λ)=[ 1 τ gas ( λ ) ][ M( λ, T gas )M( λ, T b ) ]
SNR V (f)= p corr (f) D 0 2 αβ 4 ( A d Δf ) 1/2 λ 1 λ 2 D * ( λ )[ 1 τ gas ( λ ) ][ M( λ, T gas )M( λ, T b ) ] dλ
MRTD(f) cl λ 1 λ 2 D * ( λ ) α gas (λ)[ M( λ, T gas )M( λ, T b ) ] dλ λ 1 λ 2 D * ( λ ) M(λ, T b ) T dλ
MRGC( f, T gas )= c min l=MRTD(f) λ 1 λ 2 D * ( λ ) M(λ, T b ) T dλ λ 1 λ 2 D * ( λ ) α gas (λ)[ M( λ, T gas )M( λ, T b ) ] dλ
λ 1 λ 2 D * ( λ )Δ M gas-b dλ= λ 1 λ 2 D * ( λ )Δ M tb b dλ
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