Dust collection efficiency analysis in a two-dimensional circulating granular bed filter.
Dust collection efficiency data were analyzed to determine better operating conditions for a two-dimensional circulating granular bed filter (CGBF). The dust collection efficiency in the granular bed was affected by the following operating parameters: the louver angle, the solids mass flow rate, and the particle size of the bed material. Experimental results showed that higher dust collection efficiency occurs when the solids mass flow rates were 20.34 +/- 0.24, 21.50 +/- 0.11, and 30.51 +/- 0.57 g/sec at louver angles of 45 degrees, 30 degrees, and 20 degrees, respectively. Optimal dust collection efficiency peaked with a louver angle of 30 degrees. Average particle sizes of bed material by sieve diameters (microm) of 795 microm had higher dust collection efficiency than the average collector particle size of 1500 microm. Dust collection efficiency is influenced by bed material attrition phenomenon, causing dust collection efficiency to decrease rapidly. The dust collection efficiency analysis not only found the system free of design defects but also assisted in the operation of the two-dimensional CGBF system.
Bai
Jing-Cheng
JC
Department of Chemical Engineering, Feng Chia University, Taiwan, Republic of China.
Wu
Shu-Yii
SY
Lee
An-Sheng
AS
D000393:Air Pollutants / Q000302:isolation & purification*; D000397:Air Pollution / Q000517:prevention & control*; D002244:Carbon; D003031:Coal; D060729:Coal Ash; D004391:Dust / Q000032:analysis / Q000517:prevention & control*; D004784:Environmental Monitoring; D005374:Filtration / Q000295:instrumentation; D010316:Particle Size; D052638:Particulate Matter; D011210:Power Plants; D012822:Silicon Dioxide
D000393:Air Pollutants; D003031:Coal; D060729:Coal Ash; D004391:Dust; D052638:Particulate Matter; D002244:Carbon; D012822:Silicon Dioxide