Department of Mechanical Engineering, National Chao Tung University, Hsinchu, Taiwan, Republic of China.
J Air Waste Manag Assoc. 2011 Aug;61(8):815-25. doi: 10.3155/1047-3289.61.8.815.
Two important factors that affect in-stack opacity--light extinction by emitted particles and that by water moisture after a flue gas desulfurization (FGD) unit--are investigated. The mass light extinction coefficients for particles and water moisture, k(p) and k(w), respectively, were determined using the Lambert-Beer law of opacity with a nonlinear least-squares regression method. The estimated k(p) and k(w) values vary from 0.199 to 0.316 m2/g and 0.000345 to 0.000426 m2/g, respectively, and the overall mean estimated values are 0.229 and 0.000397 m2/g, respectively. Although k(w) is 3 orders of magnitude smaller than k(p), experimental results show that the effect on light extinction by water moisture was comparable to that by particles because of the existence of a considerable mass of water moisture after a FGD unit. The mass light extinction coefficient was also estimated using Mie theory with measured particle size distributions and a complex refractive index of 1.5-ni for fly ash particles. The k(p) obtained using Mie theory ranges from 0.282 to 0.286 m2/g and is slightly greater than the averaged estimated k(p) of 0.229 m2/g from measured opacity. The discrepancy may be partly due to a difference in the microstructure of the fly ash from the assumption of solid spheres because the fly ash may have been formed as spheres attached with smaller particles or as hollow spheres that contained solid spheres. Previously reported values of measured k(p) obtained without considering the effects of water moisture are greater than that obtained in this study, which is reasonable because it reflects the effect of extinction by water moisture in the flue gas. Additionally, the moisture absorbed by particulate matter, corresponding to the effect of water moisture on the particulates, was clarified and found to be negligible.
研究了影响层内不透明度的两个重要因素——经烟气脱硫 (FGD) 装置排放的颗粒的光消光和水湿气的光消光。使用光密度的朗伯-比尔定律和非线性最小二乘法回归方法,分别确定了颗粒和水湿气的质量消光系数 k(p)和 k(w)。估计的 k(p)和 k(w)值分别在 0.199 到 0.316 m2/g 和 0.000345 到 0.000426 m2/g 之间变化,总平均估计值分别为 0.229 和 0.000397 m2/g。尽管 k(w)比 k(p)小 3 个数量级,但实验结果表明,由于 FGD 装置后存在相当大量的水湿气,水湿气对光消光的影响可与颗粒相媲美。还使用 Mie 理论和测量的颗粒尺寸分布以及 1.5-ni 的复折射率来估计质量消光系数。使用 Mie 理论得到的 k(p)在 0.282 到 0.286 m2/g 之间,略大于从测量的不透明度获得的平均估计的 k(p)0.229 m2/g。这种差异可能部分是由于飞灰的微观结构与假设的固体球体不同所致,因为飞灰可能已经形成了带有较小颗粒的球体或包含固体球体的空心球体。以前报道的在不考虑水湿气影响的情况下测量得到的 k(p)值大于本研究中的值,这是合理的,因为它反映了烟道气中水湿气对消光的影响。此外,还澄清并发现颗粒物质吸收的水分(对应于水湿气对颗粒物质的影响)可以忽略不计。