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Prediction of Riser Gas Holdup in Three- Phase External Loop Air Lift Fluidized Bed Reactor

机译:三相外环气举流化床反应器中提升气含率的预测

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Hydrodynamics is an important issue for design and development of three phase external-loop airlift fluidized bed. This paper deals on the experimental investigations on the effect of superficial gas and liquid velocities and properties of solids on the riser gas holdup of a three phase external-loop airlift fluidized bed reactor and it was characterized using Newtonian and non Newtonian systems. Water, 65% and 85% of glycerol and n-butanol were used as Newtonian liquids and different concentration of Carboxyl Methyl Cellulose (CMC) i.e., 0.2%, 0.5% and 1% were used as non Newtonian liquids. Spherical glass beads, bearl saddles and rasching rings of different sizes were used as solid phase. The phase flow rates and properties of solid particle had significant effect on the hydrodynamic characteristics of the external-loop airlift fluidized bed reactor such as riser gas holdup. Unified correlations have been developed to estimate the riser gas holdup as a function of superficial phase velocities, properties of solid particle and physical properties of both Newtonian and Non-Newtonian liquid systems. The predicting ability of the correlations were tested with the experimental data and found to be good fit with an absolute average relative error (AARD) of ± 9.7 % for riser gas holdup.
机译:流体力学是三相外环气举流化床设计与开发的重要课题。本文针对三相外循环气举流化床反应器的表观气体和液体速度以及固体物性对提升管含气量的影响进行了实验研究,并使用牛顿和非牛顿系统对其进行了表征。将水,65%和85%的甘油和正丁醇用作牛顿液体,并将不同浓度的羧甲基纤维素(CMC)(即0.2%,0.5%和1%)用作非牛顿液体。使用不同大小的球形玻璃珠,胡须鞍和环作为固相。固体颗粒的相流速和性质对外环气举流化床反应器的流体动力学特性(如立管气体滞留率)有显着影响。已经开发出统一的相关性,以估计冒口气体滞留量与表面相速度,固体颗粒性质以及牛顿和非牛顿液体系统的物理性质的关系。通过实验数据对相关性的预测能力进行了测试,发现其与上升气体滞留量的绝对平均相对误差(AARD)为±9.7%,非常适合。

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