流化床反应器构型设计对废水处理效能的影响综述

Effects of fluidized bed reactor configuration design on wastewater treatment efficiency: a review

  • 摘要: 流化床反应器因其高效的传质、传热性能及良好的混合特性,在工业生产和废水处理领域得到广泛应用。然而,在实际工程化应用中,对流化床反应器的构型参数设计尚未形成系统且科学的认知,这成为限制其进一步发展的关键问题。总结了流化床技术在水处理领域的发展和应用现状,从构型参数的角度出发,系统探讨了流化床反应器的设计优化策略,重点分析了反应器形状、高径比、内部结构、载体材料、底隙高度及导流筒直径比等参数对其处理效能、流体动力学特性及运行稳定性的影响。研究表明,流化床反应器构型参数通过调控流体力学行为与传质效率共同决定废水处理效能,具有较高的高径比(8~12)、相当的升/降区截面积(导流筒直径比0.6~0.8)的圆柱形流化床反应器更有利于废水处理。本研究为流化床反应器的科学设计与工程化应用提供了理论参考。

     

    Abstract: Fluidized bed reactors (FBRs) are widely used in industrial production and wastewater treatment due to their efficient mass and heat transfer performance, as well as excellent mixing characteristics. However, in practical engineering applications, the design of FBR configuration parameters has not yet formed a systematic and scientific understanding, which has become a key issue limiting its further development. This paper summarizes the development and application status of fluidized bed technology in the field of water treatment, and systematically discusses the design optimization strategy of FBRs from the perspective of configuration parameters, focusing on the influence of parameters such as reactor shape, height-to-diameter ratio, internal structure, supporting materials, bottom clearance height, and draft tube-to-reactor diameter ratio on treatment efficiency, hydrodynamic characteristics, and operational stability. The results indicate that the configuration parameters of FBRs collectively determine wastewater treatment efficiency by regulating hydrodynamic behavior and mass transfer efficiency. A cylindrical FBR with a relatively high height-to-diameter ratio (8-12) and a balanced cross-sectional area ratio between the riser and downcomer (draft tube diameter ratio of 0.6-0.8) is more conducive to effective wastewater treatment. This study provides a theoretical foundation for the scientific design and engineering application of FBRs.

     

/

返回文章
返回