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CFD MODELING OF BIOMASS COMBUSTION FOR A 130MW COAL-FIRED BOILER CONVERSION

机译:130MW燃煤锅炉转换的生物质燃烧的CFD型燃烧

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Biomass co-firing and coal-to-biomass conversion on existing coal-fired boilers have seen increased interest, especially in Europe, due to regulatory drivers of CO_2 reduction. Understanding in-furnace combustion and heat transfer of biomass co-firing or 100% conversion becomes critical in designing systems to meet expected performance of the boilers. In this paper, the in-furnace combustion of coal-to-biomass conversion for a 130MW wall-fired utility boiler was studied using ANSYS FLUENT Computational Fluid Dynamics (CFD) code. The application of Rotating Opposed Fired Air (ROFA) was modeled and evaluated for combustion improvement and NOx reduction. The modeling results found that biomass combustion and heat transfer patterns are different from coal due to the difference of fuel physical and chemical properties, particle size and ash concentration in the flue gas. Near-burner flames of the biomass case are stable under modeled conditions using the proposed biomass replacement burner. Overall gas temperature and peak temperature in the combustion zone are lower than coal case. The predicted model outlet gas temperature for biomass case increases by 43°C from coal baseline due to reduced radiant heat transfer to waterwall and radiation dominated superheater. The predicted un-burned carbon (UBC) loss of the biomass case is lower than that of the coal baseline case because of the improved combustion by ROFA. NOx emission from the biomass case is significantly reduced in comparison with coal baseline case, predominantly due to low nitrogen biomass fuel along with combustion staging afforded by the ROFA system. The predicted NOx emission of the 100% biomass case is below 200 mg/Nm~3 Industrial Emission Directive (IED) compliance limit with primary method only. Ash deposition tends to increase due to high alkali mineral content, but is likely manageable with proper sootblowing for this woody biomass. Corrosion on waterwalls tends to be less for biomass, but corrosion on leading-edge superheater surfaces needs to be addressed for this particular biomass fuel by applying in-furnace additives.
机译:由于CO_2减少的监管司机,现有燃煤锅炉的生物质共用和煤对生物量转化率增加了兴趣,特别是在欧洲。理解炉内燃烧和生物质共用的传热或100%转换在设计系统方面是至关重要的,以满足锅炉的预期性能。本文使用ANSYS流畅的计算流体动力学(CFD)代码,研究了130MW壁式锅炉煤与生物量转换的炉 - 生物量转换的炉内燃烧。模拟旋转相对的烧制空气(ROFA)的施加,并评估燃烧改善和降低NOx。由于燃料气体中的燃料物理和化学性质,粒度和灰分浓度的差异,模拟结果发现生物质燃烧和传热模式不同于煤,烟道气中的粒度和灰分浓度。使用所提出的生物质置换燃烧器,生物质壳体的近燃烧器火焰在建模条件下是稳定的。燃烧区的总体气体温度和峰值温度低于煤壳。由于对水坑和放射线主导的过热器的辐射热传递减小,生物质壳体的预测模型出口气体温度从煤基线增加43°C。由于ROFA的燃烧改善,预测的未燃烧的碳(UBC)损失低于煤基线案例的损失。与煤基线情况相比,生物质壳体的NOx排放显着降低,主要是由于低氮生物量燃料以及ROFA系统提供的燃烧分期。预测的100%生物质案例的排放量低于200mg / nm〜3工业排放指令(IED)合规限额仅用主要方法。由于高碱性矿物质含量,灰分沉积趋于增加,但可能是这种木质生物质的适当射击。对于生物质的水坑腐蚀趋于较少,但是通过施加炉内添加剂,需要针对该特定生物质燃料进行腐蚀。

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