湿式洗涤器系统的建模与仿真

B. Mestemaker, E. Elmazi, L. Van Biert, H.N. Van den Heuvel, K. Visser
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引用次数: 0

摘要

与公路运输相比,海运是一种相对清洁的运输方式,每吨英里的排放量较低。然而,在沿海地区排放的有害气体却令人担忧,因为这些气体会影响当地的空气质量和健康。为了减少硫氧化物 (SOX) 的排放,国际海事组织 (IMO) 在全球范围内实施了 0.5 wt% 的硫上限和排放控制区 (ECA) 0.1 wt% 的限制。船东可以选择低硫燃料或湿式洗涤器系统。湿式洗涤器系统是减少 SOX 排放的可靠方法,其捕获率高达 98%。这些系统可使用海水碱度或烧碱(如闭环系统)来中和 SOX 排放。然而,发动机的动态负载会导致排气流动条件的大幅波动,而这些波动如何影响洗涤器的效果尚不得而知。本研究探讨了动态负载对闭环湿式洗涤器去除 SOX 效率的影响。利用公开数据开发并验证了利用淡水和烧碱的闭环湿式洗涤器的动态模型。该模型采用双膜理论对气液界面进行建模。Billet 和 Schultes 液体滞留理论用于模拟填料床中的液膜厚度。在负荷波动较大或高频波动的情况下,要保持洗涤器的效率,就必须增加液体流量。洗涤器控制系统的设定点为等效达标限值的 75%,以确保在负荷波动期间符合 0.1% 的 ECA 限值。该模型和结果可用于开发更先进的控制系统,以改进洗涤器的运行并与选择性催化还原 (SCR) 系统集成,从而证明在使用高硫重油 (HFO) 时符合 IMO NOX Tier III 限制。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Modelling and Simulation of a Wet Scrubber System
Shipping is a relatively clean transport method with low emissions per ton-mile compared with road transport. However, harmful emissions emitted in coastal areas are a concern, as these affect local air quality and health. To reduce sulphur oxide (SOX ) emissions, the International Maritime Organization (IMO) implemented a global sulphur cap of 0.5 wt% and the 0.1 wt% limit in emission control areas (ECAs). Ship owners can opt for either low sulphur fuels or wet scrubber systems. Wet scrubber systems are a reliable method for reducing SOX emissions with capture rates of up to 98%. These systems may use seawater alkalinity or caustic soda (e.g. closed-loop systems) to neutralise the SOX emissions. However, the dynamic loading of engines can cause large fluctuations in the exhaust flow conditions, and it is unknown how these affect the effectiveness of the scrubber. This study explores the impact of dynamic loads on the SOX removal efficiency of closed-loop wet scrubbers. A dynamic model of a closed-loop wet scrubber utilising fresh water and caustic soda is developed and verified using publicly available data. The model applies the two-film theory to model the gas-liquid interface. Billet and Schultes liquid hold-up theory is used to model the liquid film thickness in the packed bed. Maintaining scrubber efficiency with large load fluctuations or high-frequency fluctuations requires an increased liquid flow. The scrubber control system used a set-point of 75% of the equivalent compliance limit to ensure compliance with the 0.1% ECA limit during load fluctuations. The model and results can be used to develop a more advanced control system for improved scrubber operation and integration with a selective catalytic reduction (SCR) system to demonstrate compliance with the IMO NOX Tier III limit when using high-sulphur heavy fuel oil (HFO).
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