The investigation for errors due to anisokinetic sampling on particle concentration measurement was conducted with talc and fly-ash particles of sizes in the range of 1-20μm, and also used with several dusts which were emitted from an oil combustion boiler, an alumina kiln and from a glass smelting furnace, respectively. The equation which can be widely applied for Stokes number
Sk between 0.1 and 30 was derived from the results. The empirical equation obtained is,
Cs/
Co=α(
Vo/
VS)+(1-α), where,
Co is the particle concentration in isokinetic sampling,
Cs is one in anisokinetic sampling,
Vo is the gas velocity in the duct, and
VS is gas suction velocity. Inertia function α in the equation is decided with the values of
Sk,
Vo/
VS and
Ao. Although
Ao is a coefficient correlated to
Sk and
Vo/
VS in a rigorously practical definition, Values of
Ao are approximately 1 in fine particles and 0.0625 in coarse ones respectively. It was presumed that a specific thin boundary layer was generated into stream of anisokinetic suction. Thus, it is assumed that the marginal gas velocity in the layer not only increased suddenly, but also decreased according to the values of
Vo/
Vs.
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