In this study, the mean droplet diameter in the cavity zone and the total mass transfer area of a multi-stage highspeed disperser(HSD) reactor with different packing combinations were measured and evaluated. The effec...In this study, the mean droplet diameter in the cavity zone and the total mass transfer area of a multi-stage highspeed disperser(HSD) reactor with different packing combinations were measured and evaluated. The effects of rotational speed and packing radius, as well as the packing ring radius and numbers, on the mean droplet diameter and the total mass transfer area were evaluated. A model was established to calculate the mass transfer area in the cavity zone in the HSD reactor, and it was found that the packings contribute 61%–82% of the total mass transfer area. A correlation for predicting the mass transfer area in the packing zone was regressed by the dimensionless analysis method. An enhancement factor based on the mass transfer area in the packing zone was proposed to evaluate the effect of packing combination on mass transfer area. Two optimum packing combinations were proposed in consideration of the mean droplet diameter and the enhancement factor.展开更多
迁移时间是复合绝缘子人工污秽试验中的重要参数,为了说明迁移时间对于污层憎水性能描述的局限性,本文对染污复合绝缘子的憎水迁移过程进行了研究。通过测量高温硫化硅橡胶(high temperature vulcanizing silicon rubber,HTV)试片污层...迁移时间是复合绝缘子人工污秽试验中的重要参数,为了说明迁移时间对于污层憎水性能描述的局限性,本文对染污复合绝缘子的憎水迁移过程进行了研究。通过测量高温硫化硅橡胶(high temperature vulcanizing silicon rubber,HTV)试片污层表面液滴接触角、液滴水平投影面积及HTV芯棒的污闪电压,发现污层憎水性能随迁移时间增长呈波动性增长。污层表面憎水性小分子不断向空气扩散,是导致憎水性呈波动性增长的内因;污层内部水分含量的变化,则是导致憎水性能呈波动性增长的主要原因;当试品所处迁移环境空气流通性较好时,有利于促进试品污层干燥,减小憎水性随迁移时间增长过程中的波动性。研究认为:染污复合绝缘子污层表面憎水性能随迁移时间总体上是增长的,但是,憎水性波动过程的存在,以及迁移过程受迁移环境的影响显著,使得单一的迁移时间不是描述污层憎水性能的理想参数。要提高复合绝缘子人工污秽试验与自然污秽试验间的等价性,需要寻找更合适的参数来描述试品污层的憎水性状态。展开更多
基金Supported by the National Natural Science Foundation of China(21676007,21506005)
文摘In this study, the mean droplet diameter in the cavity zone and the total mass transfer area of a multi-stage highspeed disperser(HSD) reactor with different packing combinations were measured and evaluated. The effects of rotational speed and packing radius, as well as the packing ring radius and numbers, on the mean droplet diameter and the total mass transfer area were evaluated. A model was established to calculate the mass transfer area in the cavity zone in the HSD reactor, and it was found that the packings contribute 61%–82% of the total mass transfer area. A correlation for predicting the mass transfer area in the packing zone was regressed by the dimensionless analysis method. An enhancement factor based on the mass transfer area in the packing zone was proposed to evaluate the effect of packing combination on mass transfer area. Two optimum packing combinations were proposed in consideration of the mean droplet diameter and the enhancement factor.
文摘迁移时间是复合绝缘子人工污秽试验中的重要参数,为了说明迁移时间对于污层憎水性能描述的局限性,本文对染污复合绝缘子的憎水迁移过程进行了研究。通过测量高温硫化硅橡胶(high temperature vulcanizing silicon rubber,HTV)试片污层表面液滴接触角、液滴水平投影面积及HTV芯棒的污闪电压,发现污层憎水性能随迁移时间增长呈波动性增长。污层表面憎水性小分子不断向空气扩散,是导致憎水性呈波动性增长的内因;污层内部水分含量的变化,则是导致憎水性能呈波动性增长的主要原因;当试品所处迁移环境空气流通性较好时,有利于促进试品污层干燥,减小憎水性随迁移时间增长过程中的波动性。研究认为:染污复合绝缘子污层表面憎水性能随迁移时间总体上是增长的,但是,憎水性波动过程的存在,以及迁移过程受迁移环境的影响显著,使得单一的迁移时间不是描述污层憎水性能的理想参数。要提高复合绝缘子人工污秽试验与自然污秽试验间的等价性,需要寻找更合适的参数来描述试品污层的憎水性状态。