Simulation of the operation of an industrial wet flue gas desulfurization system

被引:129
作者
Kallinikos, L. E. [1 ]
Farsari, E. I. [2 ]
Spartinos, D. N. [2 ]
Papayannakos, N. G. [1 ]
机构
[1] Natl Tech Univ Athens, Sch Chem Engn, GR-15780 Athens, Greece
[2] Univ Patras, Dept Chem Engn, Rion 26500, Greece
关键词
Wet flue gas desulfurization; Oxidation; Absorption; Mass transfer; Interfacial area; Dynamic model; SULFUR-DIOXIDE; AQUEOUS SLURRIES; MASS-TRANSFER; ABSORPTION; MODEL; PERFORMANCE; OXIDATION; SO2;
D O I
10.1016/j.fuproc.2010.07.020
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
In this work the simulation of a wet Rue gas desulfurization (FGD) unit with spray tower of a power plant is presented aiming at an efficient follow-up and the optimization of the FGD system operation The dynamic model developed to simulate the performance of the system has been validated with operation data collected over a long period of time All the partaking physical and chemical processes like the limestone dissolution the crystallization of calcium sulfite and gypsum and the oxidation of sulfite ions have been taken Into account for the development of the simulation model while the gas absorption by the liquid droplets was based on the two-film theory The effect of the mean diameter of the slurry droplets on the performance of the system was examined as it was used as an index factor of the normal operation of the system The operation limits of the system were investigated on the basis of the model developed It is concluded that the model is capable of simulating the system for significantly different SO2 loads and that the absorption rate of SO2 is strongly affected by the liquid dispersion in the tower (C) 2010 Elsevier B V All rights reserved
引用
收藏
页码:1794 / 1802
页数:9
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