2010
DOI: 10.1007/978-94-007-0317-9_7
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Simulation of Distributed Detection of Ammonia Gas

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“…The first scenario is considered by assuming a first order diffusion model of the hydrocarbon in question through the cladding layers. According to [ 24 ], the mass concentration of the chemical agent in question will grow in time until reaching a steady-state concentration profile that varies linearly between the initial concentration of 0 mol/L at the core/cladding interface and the ambient concentration of the hydrocarbon in the medium surrounding the cladding. This results in the diffusion modeled RI profile depicted by Figure 4 .…”
Section: Characterization Of Otdr Traces Using Established Theoretmentioning
confidence: 99%
“…The first scenario is considered by assuming a first order diffusion model of the hydrocarbon in question through the cladding layers. According to [ 24 ], the mass concentration of the chemical agent in question will grow in time until reaching a steady-state concentration profile that varies linearly between the initial concentration of 0 mol/L at the core/cladding interface and the ambient concentration of the hydrocarbon in the medium surrounding the cladding. This results in the diffusion modeled RI profile depicted by Figure 4 .…”
Section: Characterization Of Otdr Traces Using Established Theoretmentioning
confidence: 99%