Computational investigation of hydrodynamics, coal combustion and NOx emissions in a tangentially fired pulverized coal boiler at various loads
Graphical abstract
Introduction
As the most widely used combustion systems, tangentially fired pulverized coal boilers have been used extensively in coal-fired power plants, owing to their favorable coal flexibility, good flame stability, high combustion efficiency, and easy operation (Liu, Fan, & Wu, 2017; Park et al., 2013; Sankara, Santhosh Kumara, & Balasubramanian, 2019). During their history of ∼50 years, improvements in tangentially fired pulverized coal boilers have been targeted with respect to their efficiency and the environment (Beer, 2000).
In recent years, the increase in intermittent renewable energy has driven coal-fired power plants to undertake deep peak-load regulation, and boilers are operated frequently under variable load conditions (Gu, Dong, Chen, Wang, & Li, 2016; Wang et al., 2018). During the load change, fuel and air that are introduced into the boilers are adjusted; the hydrodynamics, temperature and oxygen distribution in the furnaces vary; and the combustion rates and char burnout change. These changes further affect NOx emissions from the boilers. In the new market situation of deep peak-load regulation, a better understanding of the hydrodynamics, coal combustion and NOx formation in the boilers at different loads, especially for intermediate and low loads, is of utmost importance.
Because full-scale experiments are restricted by expense, computational fluid dynamics (CFD) simulations have been used to investigate tangentially fired pulverized coal boilers (Belosevic, Sijercic, Oka, & Tucakovic, 2006; Choi & Kim, 2009; Fan, Qian, Ma, Sun, & Cen, 2001; Tan et al., 2017; Wu, Fan, Liu, & Bian, 2019; Zha, Li, Wang, & Che, 2017). Several studies have been devoted to the CFD modeling of gas flow, heat transfer, coal combustion and NOx emissions at variable/low loads. For example, Shi, Li, Yang, and Duan (2019) analyzed flow and heat transfer in a 1000-MW tangentially fired pulverized coal boiler at various loads. At a 50% boiler load, the furnace-temperature change was irregular, and the heat transfer deteriorated in the water-cooled wall region. Belosevic, Sijercic, Tucakovic, and Crnomarkovic (2008) developed a comprehensive CFD model to predict complex turbulent reactive flows in a tangentially fired boiler. The influence of burner configuration and boiler load on the combustion processes was evaluated. Al-Abbas, Naser, and Hussein (2013) presented a CFD study for brown coal combustion in a 550 MW tangentially fired furnace under different operating conditions. The effects of load change on velocity, temperature, species concentrations and char consumption were predicted. Based on their improved CFD model, Belosevic, Tomanovi, Crnomarkovic, and Milicevic (2019) indicated that the operating conditions at low loads affect the flow/temperature fields, flame geometry, combustion reactions and species concentrations. Yuan et al. (2019) presented a detailed CFD simulation of the variable load combustion in a 660-MW supercritical swirling opposed boiler. NOx emissions were lowest at a boiler load of 30%, a primary air ratio of 0.2, and a pulverized coal size of 50 μm. A reduction in boiler load decreased the combustion stability, and the NOx emissions increased.
The above research shows that the use of CFD in tangentially fired pulverized coal boilers provides extensive information on the combustion characteristics and boiler performance. The temperature distributions, species concentrations and heat flux under different conditions were obtained numerically. Problems in variable load combustion, such as heat transfer deterioration and a decrease in combustion stability, could be predicted. The combustion performance and NOx emissions may be improved by optimizing the operating conditions. However, compared with full-load combustion simulations, limited CFD simulations exist regarding variable load combustions. The influence of load change on the hydrodynamics, heat transfer, coal combustion and NOx emissions is not fully understood. A comprehensive CFD model for tangentially fired pulverized coal boilers at various loads is needed.
This work focused on CFD investigations of hydrodynamics, coal combustion and NOx emissions in a 630-MW tangentially fired pulverized coal boiler at various loads (630, 440 and 300 MW; a relative load of 100%, 70% and 48%), and aimed to clarify the effects of load change on the furnace processes. To achieve this aim, a comprehensive CFD model, including gas–particle flow, heat transfer, coal combustion and NOx formation, was established. Based on the grid independence and model validation, the flow field, temperature profile, species concentration and NOx emission characteristics were predicted numerically for different boiler loads. The effect of burner angle on the furnace processes was evaluated. Such a comprehensive simulation study is expected to provide useful guidelines for tangentially fired pulverized coal boilers that are operated under different conditions.
Section snippets
Boiler specifications
The 630-MW tangentially fired pulverized coal boiler that was simulated in this study is an industrial boiler that is used in a Chinese coal-fired power plant. The boiler height, width, and depth were 63,550, 18,816 and 17,696 mm, respectively. Six separate platen and twenty rear platen superheaters existed at the top of the boiler furnace. Fig. 1(a) provides a schematic diagram of the furnace structure.
Twenty-four direct current burners were arranged in six layers at the lower corners of the
Computing domain and mesh
To avoid an excessively high computational cost, the region from the bottom hopper to the horizontal flue outlet, instead of the whole boiler, was chosen as the computing domain. The entire computing domain was subdivided into three parts: a bottom hopper, combustion zone and upper zone.
A structured mesh was used to obtain more accurate simulation results. At the inlets of the primary/secondary air, refined meshes were used to reduce the numerical errors. Three sets of meshes with grid numbers
Grid independence and model verification
Table 3 shows the predicted oxygen contents, flue-gas temperatures and NOx concentration at the outlet of the horizontal flue as a function of grid numbers. With an increase in grid number from 1,252,367 to 1,581,018 and 1,825,972, the oxygen content changed from 5.5% to 5.02% and 5.05%, the gas temperature varied from 1314 to 1200 and 1212 K, and the NOx concentration changed from 270 to 247 and 250 mg/m3, respectively. When the grid number exceeded 1,581,018, the predicted species contents
Conclusions
- (1)
For various loads, the air–fuel formed firing circles in the furnace center. With a decrease in boiler loads, the velocity deviations decreased in the lower furnace but tended to increase in the upper furnace. The mean residual time of particles increased from 11.2 to 13.1 and 14.5 s as the loads decreased from 630 to 440 and 300 MW, respectively.
- (2)
On various cross sections, the furnace temperature was small in the center and large near the wall. With a decrease in load, the high-temperature zone
Declaration of interests
Authors declare that they have no known competing financial interests or personal relationships that could have appeared to influence the work reported in this paper.
Acknowledgments
The authors acknowledge the support from the National Nature Science Foundation of China (No. 51476058) and SINOPEC project (No. 318015-6).
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