Numerical Investigation on Flow and Thermal Characteristics of Spray Evaporation Process in Boiler Desuperheater

Jianqing Wang (), Baoqing Liu, Bin Du, Kaifei Wu, Qi Lin, Bohai Liu and Minghui Cheng
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Jianqing Wang: Zhejiang Academy of Special Equipment Science, Hangzhou 310018, China
Baoqing Liu: Institute of Advanced Equipmentt, Zhejiang University, Hangzhou 310027, China
Bin Du: Zhejiang Academy of Special Equipment Science, Hangzhou 310018, China
Kaifei Wu: Zhejiang Academy of Special Equipment Science, Hangzhou 310018, China
Qi Lin: Zhejiang Academy of Special Equipment Science, Hangzhou 310018, China
Bohai Liu: Zhejiang Academy of Special Equipment Science, Hangzhou 310018, China
Minghui Cheng: Zhejiang Academy of Special Equipment Science, Hangzhou 310018, China

Energies, 2025, vol. 18, issue 14, 1-20

Abstract: The spray evaporation process in the boiler desuperheater involves complex droplet behaviors and fluid–thermal coupling, and its temperature distribution characteristics greatly affect the performance and safety of industrial processes. To better understand the process characteristics and develop the optimal desuperheater design, computational fluid dynamics (CFDs) was applied to numerically investigate the flow and thermal characteristics. The Eulerian–Lagrangian approach was used to describe the two-phase flow characteristics. Both primary and secondary droplet breakup, the coupling effect of gas–liquid and stochastic collision and coalescence of droplets were considered in the model. The plain-orifice atomizer model was applied to simulate the atomization process. The numerical model was validated with the plant data. The spray tube structure was found to greatly affect the flow pattern, resulting in the uneven velocity distribution, significant temperature difference, and local reverse flow downstream of the orifices. The velocity and temperature distributions tend to be more uniform due to the complete evaporation and turbulent mixing. Smaller orifices are beneficial for generating smaller-sized droplets, thereby promoting the mass and heat transfer between the steam and droplets. Under the same operating conditions, the desuperheating range of cases with 21, 15, and 9 orifices is 33.7 K, 32.0 K, and 29.8 K, respectively, indicating that the desuperheater with more orifices (i.e., with smaller orifices) shows better desuperheating ability. Additionally, a venturi-type desuperheater was numerically studied and compared with the straight liner case. By contrast, discernible differences in velocity and temperature distribution characteristics can be observed in the venturi case. The desuperheating range of the venturi and straight liner cases is 38.1 K and 35.4 K, respectively. The velocity acceleration through the venturi throat facilitates the droplet breakup and improves mixing, thereby achieving better desuperheating ability and temperature uniformity. Based on the investigation of the spray evaporation process, the complex droplet behaviors and fluid–thermal coupling characteristics in an industrial boiler desuperheater under high temperature and high pressure can be better understood, and effective guidance for the process and design optimizations can be provided.

Keywords: computational fluid dynamics; spray evaporation process; desuperheater; numerical simulation; droplet breakup (search for similar items in EconPapers)
JEL-codes: Q Q0 Q4 Q40 Q41 Q42 Q43 Q47 Q48 Q49 (search for similar items in EconPapers)
Date: 2025
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