共查询到18条相似文献,搜索用时 140 毫秒
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本文介绍了新近研制的组合环单体填料对于汽液接触过程的流体力学与传质性能。实验表明,这种填料具有比矩鞍环填料阻力小、传质效率高的优点,可以代替鲍尔环、矩鞍环等常用填料,以取得良好经济效益。 相似文献
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三种填料结构旋转床传质及压降性能对比 总被引:1,自引:0,他引:1
《化学工程》2017,(3):27-32
为了考察自主设计的新型板式旋转填料床传质及压降性能,分别以NaOH-H_2O和空气-水为实验体系,采用对比实验的研究方法,考察了转速、液量和气量对新型板式填料床、传统丝网填料床和鲍尔环填料床的传质与压降性能的影响。传质性能研究表明:在相同操作条件下,丝网填料床传质性能最优,但新型板式填料床传质性能与丝网填料床相差不大(<1.0 s~(-1));压降性能研究发现,气量是影响填料床压降的重要因素,且在相同操作条件下,压降值始终有丝网填料床>鲍尔环填料床>新型板式填料床,丝网填料床压降值与新型板式填料床相差33%以上。新型板式填料床在传质效率损失不大的情况下,损失了较低能耗,表现出优良的综合性能。 相似文献
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QH-1型扁环填料的气液接触性能 总被引:1,自引:0,他引:1
本文简要介绍了新近研制的QH-1型扁环填料对于汽液接触过程的流体力学与传质性能。实验表明,这种填料具有通量大、阻力小、传质效率高的优点,可望代替鲍尔环等常用填料,以取得良好经济效益 相似文献
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双矩鞍环(TH-Ⅲ)型颗粒填料在气液传质过程中的传递性能研究 总被引:1,自引:0,他引:1
在内径为φ600mm的有机玻璃塔中,对φ38的双矩鞍环(TH-Ⅲ)型乱堆填料的流体力学性能和传质性能进行了研究,并与NR1.5#散堆填料进行了比较,结果表明双矩鞍环颗粒填料具有更为优良的流体力学性能和传质效率. 相似文献
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The hydrodynamics and mass transfer of Plum Flower Mini Ring(PFMR),Pall Ring and Intalox Saddle were studied in a 600mm diameter column with air-oxygen-water system over a wide range of liquid loasds.It was shown from the experiments that PFMR had much lower resistance,larger throughput and higher mass transfer efficiency than Pall Ring and Intalox Saddle.It was clear from the comparison that existing equations could not predict the performance of packings very well at high liquied loads.Therefore,new semi-empirical equations of pressure drop,flooding gas velocity and height of transfer unit(HTU)were proposed based on the experimental data. 相似文献
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超重力旋转床气相压降模型研究进展 总被引:1,自引:0,他引:1
超重力旋转床是一种高效的气液接触设备,可极大地强化气液传质过程,在化工、材料、冶金、能源、环保等领域有着广泛的应用前景。气相压降是超重力旋转床设计、选型时需要考虑的一项重要指标。自从超重力旋转床问世以来,人们对其气相压降进行了较为广泛的研究。对近年来国内外超重力旋转床的气相压降模型研究进展进行了综述。分别从逆流式旋转填料床、错流式旋转填料床、折流式旋转床3方面具体介绍了各压降模型的研究方法并进行了对比,最后对超重力旋转床气相压降模型研究的方向与重点做了简要分析。 相似文献
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Flow phenomena, local heat and mass transfer and pressure drop of corrugated passages in process equipment are examined. Based on a method for measuring local heat and mass transfer, developed in previous investigations, a procedure has been formulated for the determination of local heat and mass transfer in corrugated passages. Using the analogy between heat and mass transfer, this technique allows the determination of heat transfer distributions in any structures with high local resolution. The corresponding pressure drop is presented together with the local and integral heat and mass transfer of different structures. It is shown that differences in heat and mass transfer as well as in pressure drop are due to different flow phenomena which also characterize mixing behaviour. 相似文献
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通过采用在圆管内壁填充环状金属泡沫的方法强化管内对流凝结换热,实验研究了制冷剂R134a在内壁填充环状金属泡沫管内的流动凝结的压降和换热,克服了完全填充金属泡沫管流动阻力大的缺点。用于计算传热系数的管壁温度通过热电偶测量得到。综合分析了质量流速和两相流体干度对流动凝结压降及传热系数的影响。研究结果表明内壁填充环状金属泡沫管压降远大于光管,压降随质量流速和干度的增加而迅速增大且呈非线性。通过壁面温度分布和温度波动对内壁填充环状金属泡沫管内的两相流型进行判别,发现影响该类强化管凝结换热的两种主要流型:分层流和环状流。内壁填充环状金属泡沫管的凝结传热系数大于光管,且随着质量流速和干度的增加传热系数增大,该类强化管流动凝结传热系数是光管的2倍左右。 相似文献
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A new catalyst loading method, in which catalyst particles are packed in a reactor with a novel internal, has been studied by measuring pressure drop, RTD, liquid holdup and mass transfer. It can be inferred from experimental results that the internal changes the conventional gas and liquid counter-current flow into a new cross-current flow, so the problems of excessive pressure drop and “flooding” are avoided. When pressure drop, liquid holdup, RTD and mass transfer coefficient are similar, the catalyst loading fraction of the new method is much higher than that of conventional methods. Furthermore, the reactive distillation reactor with the novel internal has advantages such as simple structure, low operating cost, and convenience for installation and removal of the catalyst. 相似文献
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A novel design of a honeycomb packing with turbulizers in the region of the boundary layer (Turbo-Pack) has been designed and investigated. The presence of turbulizers is shown to decrease the pressure drop per mass transfer unit in cases of both gas-film and liquid-film controlled mass transfer. A comparison of the best packings known so far from the literature shows that, regarding such an important parameter as pressure drop per mass transfer unit, the novel packing has significant advantages. On the basis of experimental data obtained by studying 11 different packing designs in liquids of various viscosity, equations for determining the performance characteristics of the novel packing are obtained. In the first part of this work, the data on packing design, pressure drop and loading point are presented. 相似文献