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首页> 外文期刊>Bioresource Technology: Biomass, Bioenergy, Biowastes, Conversion Technologies, Biotransformations, Production Technologies >MATHEMATICAL MODELLING OF STEADY STATE UPDRAFT GASIFICATION OF JUTE STICK PARTICLES OF DEFINITE SIZES PACKED RANDOMLY - AN ANALYTICAL APPROACH
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MATHEMATICAL MODELLING OF STEADY STATE UPDRAFT GASIFICATION OF JUTE STICK PARTICLES OF DEFINITE SIZES PACKED RANDOMLY - AN ANALYTICAL APPROACH

机译:随机装填有限尺寸黄麻胶粒的稳态超气化气化的数学模型-一种解析方法

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An experimental study was carried out on an insulated MS reactor of total length 1650 mm and constant diameter 76 mm for updraft gasification of jute stick particles with air as the gasifying agent. The results and performances were evaluated for different sizes of jute stick particles at various superficial air inlet velocities ranging from 0.0337 to 0.1011 m s(-1) at STP. Accordingly, the superficial mass velocities of solid particles were changed from 0.0225 to 0.0950 kg/(m(2) s(1)). The calorific value of the producer gas was found to be in the range of 4306-4912 kJ Sm-3. An attempt was made to develop a predictive model of the gasification system. Gas diffusion through the solid pores was postulated to be controlling the rate processes in the developed non-equilibrium, mechanistic model. Approach to solve the governing equations was analytical and the total process was found to be controlled by a few dimensionless numbers containing the process variables. Comparison of experimental data and the model predictions indicated the validity of the model under the given circumstances. (C) 1997 Published by Elsevier Science. [References: 16]
机译:在总长度为1650 mm,恒定直径为76 mm的绝热MS反应器上进行了实验研究,以空气作为气化剂对黄麻棒状颗粒进行上浮气化。在STP时,对于不同大小的黄麻棒状颗粒,其表观进气速度范围为0.0337至0.1011 m s(-1),对结果和性能进行了评估。因此,固体颗粒的表面质量速度从0.0225更改为0.0950 kg /(m(2)s(1))。发现生产气的热值在4306-4912 kJ Sm-3的范围内。尝试开发气化系统的预测模型。假设气体在固体孔隙中的扩散将控制已开发的非平衡机理模型中的速率过程。解决控制方程的方法是分析性的,发现整个过程由包含过程变量的几个无量纲数控制。实验数据和模型预测的比较表明了在给定情况下模型的有效性。 (C)1997年由Elsevier Science出版。 [参考:16]

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