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Determination of the kinetic constants of the process of plasma gasification of coal-water fuel

机译:水煤浆等离子气化过程动力学常数的确定

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The chemical kinetics of processes of thermal transformations of carbon-containing media was studied at high-temperature processing (2000 K ≤ T ≤ 5000 K) in the chamber of a plasma-jet reactor using water vapor as an oxidizer. The chemical reactions rate was calculated according to the method of determining the kinetic constants of the process of gasification of coal-water fuel. The influence of the temperature of the gaseous environment in the chamber on the time of complete carbon conversion of the fuel particles is established. An example of calculating the parameters of the gasification process of coke residue particles with a size of (5 - 20)·10~(-5)m with an oxidizer excess coefficient α = 0.45 and fuel consumption m _(f)= 100 kg/hr is given. The expediency of the process of vapor-plasma gasification at the temperature of gases in the reactor chamber up to 3000 K is shown.
机译:在以水蒸气为氧化剂的等离子体喷射反应器腔室中,在高温处理(2000 K≤T≤5000 K)下研究了含碳介质热转化过程的化学动力学。根据确定水煤燃料气化过程的动力学常数的方法计算化学反应速率。确定了腔室内的气体环境温度对燃料颗粒完全碳转化的时间的影响。计算尺寸为(5-20​​)·10〜(-5)m,氧化剂过量系数α= 0.45,燃料消耗m _(f)= 100 kg的焦渣颗粒气化过程参数的示例/ hr被给出。示出了在反应器腔室内的气体温度高达3000K下的蒸气-等离子体气化过程的便利性。

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