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NUMERICAL SIMULATION OF HEAVY FUEL OIL COMBUSTION CHARACTERISTICS AND NOX EMISSIONS IN CALCINER IN CEMENT INDUSTRY

机译:水泥工业煅烧炉重型燃油燃烧特性和NOx排放的数值模拟

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The aim of the present study is to numerically investigate the combustion characteristics of Heavy Fuel Oil (HFO) and NO_x emissions inside a calciner used in cement industry. The calciner is a furnace placed before the rotary Kiln its main objectives are the reduction of CO_2 emissions and air pollutions while enhancing the cement quality through separating the calcination and clinkering processes. In order to conduct the present investigations the calciner at CEMEX Egypt Cement Company was considered and real dimensions and operating conditions were applied. The combustion model was based on the conserved scalar (mixture fraction) and prescribed Probability Density Function (PDF) approach. The (RNG) k-ε turbulence model has been used. The HFO droplet trajectories were predicted by solving the momentum equations for the droplets using Lagrangian treatment. The radiation heat transfer equation was solved using PI method. The formation of thermal NO_x from molecular nitrogen was modeled according to the extended Zeldovich mechanism. The effects of varying the burner's swirl number and viscosity grade on the combustion performance of HFO and the resulting NO_x emissions were considered. The burner's swirl number influences the mixing rate of air and fuel. A small swirl number ≤ 0.6 is not desired as it elongates the flame; increases flue gases temperatures and increases the NO_x emissions inside the calciner. A swirl number ≥ 0.6 is found optimal for good combustion characteristics and NO_x emissions concentration. Meanwhile, it was found that the HFO viscosity has a significant effect on the injection velocity and must be considered as a function of temperature during the analysis as this will significantly affects the combustion characteristics.
机译:本研究的目的是在水泥行业中使用的煅烧炉内的重型燃料油(HFO)和NO_X排放的燃烧特性。煅烧炉是一个炉子,在旋转窑之前,其主要目标是通过分离煅烧和克制工艺来提高CENCE质量的CO_2排放和空气污染的减少。为了进行本调查,考虑了CEMEX埃及水泥公司的煅烧炉,并采用了实际维度和运营条件。燃烧模型基于保守的标量(混合级分)和规定的概率密度函数(PDF)方法。已经使用(RNG)K-ε湍流模型。通过利用拉格朗日治疗解决液滴的动量方程来预测HFO液滴轨迹。使用PI方法解决了辐射传热方程。根据延长的Zeldovich机制模拟来自分子氮的热NO_X的形成。考虑了改变燃烧器的旋流数和粘度等级对HFO的燃烧性能和所得到的NO_X排放的影响。燃烧器的漩涡号码影响空气和燃料的混合速度。当它伸长火焰时,不需要小旋流≤0.6;增加烟道气温度并增加煅烧炉内的NO_X排放。对于良好的燃烧特性和NO_X排放浓度,最佳地找到旋流≥0.6。同时,发现HFO粘度对注射速度有显着影响,并且必须考虑在分析期间温度的函数,因为这会显着影响燃烧特性。

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