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Numerical simulations of coal gasification at high temperature in an entrained flow reactor.

机译:夹带流反应器高温下煤气化的数值模拟。

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Entrained flow coal gasification is becoming increasingly important particularly in the development of Integrated Coal Gasification Combined Cycle (IGCC) technology for the production of electricity. However, there is a lack of knowledge worldwide for the gasification process and more especially for the chemical reactions (reactions rates, constants) that take place under high temperature and pressure. Therefore, two gasifiers have been designed and built at the Institute for Energy Systems (Lehrstuhl für Energiesysteme - LES) at the Technische Universitat München. The first, the atmospheric entrained flow gasifier can operate at very high temperature, up to 1700 °C - 1 bar , the second , high pressure and temperature gasifier- up to 1800 °C and 1-50 bar. In an ongoing project, a great variety of experiments under different conditions are performed to determine chemical reactions rates at high temperature conditions. The final goal of such investigations is to extend the validity of these models for high pressure and temperature conditions using the high pressure pilot scale gasifier built in LES. In the present paper different operating temperatures and fuel composition have been used and tested. The performed CFD numerical simulations of pulverized coal gasification are compared to experimental data.
机译:夹带的流动煤气化越来越重要,特别是在综合煤气化联合循环(IGCC)技术的开发中越来越重要。然而,对于气化过程缺乏全球知识,并且更特别适用于在高温和压力下发生的化学反应(反应率,常数)。因此,在Technische UniversitatMünchen的能源系统(LehrstuhlFürEnergiesysteme-les)设计和建造了两个煤气。首先,大气夹带的流动气化器可以在非常高的温度下运行,高达1700°C-1巴,第二,高压和温度气化器 - 高达1800°C和1-50巴。在持续的项目中,进行不同条件下的各种实验,以确定高温条件下的化学反应率。此类调查的最终目标是使用内置在LES中的高压试验秤气化器来扩展这些模型的有效性。在本文中,已经使用并测试了不同的操作温度和燃料组合物。将粉煤气化的执行的CFD数值模拟与实验数据进行比较。

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