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A Development of Computer Model for Simulating the Transport Phenomena in COREX Melter-gasifier

机译:COREX熔炉气化炉输送现象模拟计算机模型的开发。

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The computer model, which could simulate the transport phenomena of the COREX melter-gasifier considering the pyrolysis behavior of raw coal, was developed. This model was made up of 192 ordinary differential equations for gas and solid phases in the 1-dimensional fixed bed part and balance equations for gas phase in the combustion zone and the freeboard zone of O-dimensioanl assumption. This coupled non-linear equations are calculated by the LSODE packages and Gibbs free energy minimization method. The effluent gas temperature showed good agreement with the operational data. The temperature of the gas was decreased linearly with the distance from the combustion zone. The predicted melting position of ore and flux mixture was 2.0 m high from the combustion zone. CO was mainly generated i n the combustion zone and H_2 was mainly produced during the devolatilization of coal. The fixed bed in the melter-gasifier could be divide into four distinct zones. Each zone has its own reaction characteristics such as heating zone, primary pyrolysis zone, secondary pyrolysis zone and gasification zone.
机译:开发了一种计算机模型,该模型可以考虑原煤的热解行为来模拟COREX熔融气化炉的输送现象。该模型由192个一维固定床部件中的气相和固相的常微分方程以及O-尺寸假设的燃烧区和干舷区中的气相平衡方程组成。通过LSODE软件包和吉布斯自由能最小化方法计算出该耦合的非线性方程。出气温度与运行数据吻合良好。气体温度随着距燃烧区的距离线性降低。矿石和助熔剂混合物的预计熔化位置距离燃烧区高2.0 m。 CO主要产生于燃烧区,H_2主要产生于煤的脱挥发分。熔融气化炉中的固定床可以分为四个不同的区域。每个区具有其自己的反应特性,例如加热区,一级热解区,二级热解区和气化区。

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