کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
---|---|---|---|---|
726087 | 892582 | 2012 | 7 صفحه PDF | دانلود رایگان |

This paper presents industrial investigations on fine particle grade collection efficiency of an industrial electrostatic precipitator (ESP). Experiments are performed with a hybrid ESP and fabric filter (FF). Gas flow rates, mass inlet concentration, gaseous temperature and the ESP plate–plate distance are 20,000–40,000 Nm3/h, 15 g/Nm3, 110 °C, and 400 mm, respectively. The ESP specific collection area ranges from 10 to 20 m2/m3/s. Both single-phase and three-phase transformer-rectifiers (TRs) are used for energizing the ESP. When changing the single-phase TR to the three-phase TR, the maximum average secondary voltage is increased from 55 kV to 71 kV and average corona current rises from 31 mA to 62 mA without spark breakdown. As a result, both fine particle grade collection efficiency η(r ) and their migration velocities are significantly increased. With the single-phase TR, the velocity is around 17 cm/s for all particles. With three-phase TR, its maximum value is about 35 cm/s. For particles within 0.03–0.1 μm and 0.1–2.5 μm in diameter, the efficiencies rise from about 85% to 95% and 92, respectively. For particles of around 2.5–8.0 μm, they rise from about 87% to about 98%. Moreover, experiments show that a revised Deutsch equation log(1−η(r))/β=−αEa2S gives a good approximation via the average electric field Ea, the specific collection area S and two correction coefficients α and β, which depend on particle size.
► Particle collection efficiency can be well estimated with a modified Deutsch equation.
► Fine particle collection efficiency is investigated with an industrial ESP.
► Electrical power sources have great impact on the fine particle collection efficiency.
Journal: Journal of Electrostatics - Volume 70, Issue 3, June 2012, Pages 285–291