共查询到19条相似文献,搜索用时 187 毫秒
1.
在TDBY-300多功能填料塔实验装置中,以空气-氨气-水为物系,对金属矩鞍环填料的流体力学与传质性能进行了研究,获得了该填料的几何特性参数和P/Z~Fv、H0~Fv、Hoc~G、HETP~G及KGa~G等关系曲线.结果表明,该填料具有压降适中、通量高、气液分布均匀及传质性能稳定等优点,比较适用于清洁、碱腐蚀性流体的气-液吸收、精馏和萃取等传质分离工业过程. 相似文献
2.
3.
4.
泡沫碳化硅波纹规整填料的流体力学及传质性能 总被引:1,自引:0,他引:1
将碳化硅陶瓷材料用于精馏过程,将该材料与波纹板类填料形状相结合开发出泡沫碳化硅波纹规整填料和光滑碳化硅波纹规整填料.对2种填料进行了流体力学性能与传质性能的测试,研究了泡沫结构对规整填料性能的影响.在直径100mm的有机玻璃塔中使用空气-水体系对填料进行干填料压降、湿填料压降、泛点气速、持液量等流体力学性能测试;在直径100mm的常压玻璃塔中,使用环己烷-正庚烷标准物系进行全回流操作,对填料进行传质性能测试.实验结果表明,在填料外形相同的情况下,与光滑填料相比,泡沫填料的干、湿填料压降较高,泛点气速相当,持液量增大,传质效率显著提高. 相似文献
5.
在TLXS-1型填料塔试验装置中,以空气-氨-水为物系,对φ12mm瓷拉西环填料的流体力学及传质性能进行试验测定。获得了该塔的泛点特性和△P/Z~G、HOG—G、KY~G等相关曲线。试验研究结果对该吸收塔的操作和工程设计具有参考价值。 相似文献
6.
在液-液萃取过程中,提高分散相的表面更新速率可有效提高萃取的传质效率.研究发现,在萃取过程中使用气体搅拌可以增加液液之间的接触面积,促进液相内的湍动和循环.据此,本文在气-液-液萃取条件下对不同填料的传质性能进行了测定.实验表明,通入气相后分散相液滴呈现稳定的“油包气”空心状态,这种结构大大降低了分散相液滴的传质层厚度,减小了传质距离,极大地强化传质效率.在适宜气速下,气-液-液萃取效率较传统萃取效率提高20%~40%.通过与散装填料对比,发现规整填料更利于强化萃取效果,传质效率提高约50%. 相似文献
7.
8.
塑料TGJ型填料的流体力学及传质性能研究 总被引:7,自引:1,他引:7
在内径φ600MM塔中,以空气-氨-水为物系,对塑料TGJ型填料的流体力学及传质性能进行了研究。获得了该填料的几何特性、泛点填料因子、压降填料因子及传质系数等有关参数。结果表明,塑料TGJ型填料具有通量大、压降低、气液分布均匀、不易堵塞及传质性能良好等优点。 相似文献
9.
10.
11.
12.
13.
14.
在内径Φ30 0mm的填料塔中研究了孔板波纹填料的结构参数对液相轴向混合特性、流体力学和传质性能的影响 .研究结果表明 ,轴向返混参数随开孔率、倾角的增加及盘高的减小而增加 ,填料层压降随开孔率、盘高的增加及倾角的减小而降低 ,传质单元高度随倾角的增加、盘高的减小而降低 ,开孔率对传质单元高度的影响有一个适宜值 .通过对实验数据的回归分析得出了轴向返混参数、填料层压降及传质单元高度的关联式 .该研究结果对孔板波纹填料的开发与设计具有参考价值 相似文献
15.
16.
We designed and built a flexible gas-liquid pilot plant to evaluate the performances of different packings. Dynamic methods involving transferable and non-transferable tracers were used to achieve this goal. A model taking into account axial dispersions in both phases represented the packing mass transfer performances. Mass transfer coefficient, liquid and gas phases axial dispersions and holdup were estimated by performing a time domain fitting of the model response to experimental data. This method has been applied successfully to a commercially available packing (polypropylene Ralu flow 25 from Raschig). 相似文献
17.
Randomly packed bed reactors are widely used in chemical process industries, because of their low cost and ease of use compared to other packing methods. However, the pressure drops in such packed beds are usually much higher than those in other packed beds, and the overall heat transfer performances may be greatly lowered. In order to reduce the pressure drops and improve the overall heat transfer performances of packed beds, structured packed beds are considered to be promising choices. In this paper, the flow and heat transfer inside small pores of some novel structured packed beds are numerically studied, where the packed beds with ellipsoidal or non-uniform spherical particles are investigated for the first time and some new transport phenomena are obtained. Three-dimensional Navier–Stokes equations and RNG k–ε turbulence model with scalable wall function are adopted for present computations. The effects of packing form and particle shape are studied in detail and the flow and heat transfer performances in uniform and non-uniform packed beds are also compared with each other. Firstly, it is found that, with proper selection of packing form and particle shape, the pressure drops in structured packed beds can be greatly reduced and the overall heat transfer performances will be improved. The traditional correlations of flow and heat transfer extracted from randomly packings are found to overpredict the pressure drops and Nusselt number for all these structured packings, and new correlations of flow and heat transfer are obtained. Secondly, it is also revealed that, both the effects of packing form and particle shape are significant on the flow and heat transfer in structured packed beds. With the same particle shape (sphere), the overall heat transfer efficiency of simple cubic (SC) packing is the highest. With the same packing form, such as face center cubic (FCC) packing, the overall heat transfer performance of long ellipsoidal particle model is the best. Furthermore, with the same particle shape and packing form, such as body center cubic (BCC) packing with spheres, the overall heat transfer performance of uniform packing model is higher than that of non-uniform packing model. The models and results presented in this paper would be useful for the optimum design of packed bed reactors. 相似文献
18.
The rotating packed bed (RPB) with split packing is a novel gas–liquid contactor, which intensifies the mass transfer processes controlled by gas-side resistance. To assess its efficacy, the mass transfer characteristics with adjacent rings in counter-rotation and co-rotation modes in a split packing RPB were studied experimentally. The physical absorption system NH3–H2O was used for characterizing the gas volumetric mass transfer coeffi-cient (kyae) and the effective interfacial area (ae) was determined by chemical absorption in the CO2–NaOH sys-tem. The variation in kyae and ae with the operating conditions is also investigated. The experimental results indicated that kyae and ae for counter-rotation of the adjacent packing rings in the split packing RPB were higher than those for co-rotation, and both counter-rotation and co-rotation of the split packing RPB were superior over conventional RPBs under the similar operating conditions. 相似文献
19.
为适应催化反应精馏填料需要高持液量及高效率的应用特点,开发了一种新型多层丝网填料PACTU-800,并通过设计中试装置对其进行了流体力学性能测试及传质性能测试。以空气-水为测试物系的冷模实验表明,F因子为0—0.55时,喷淋密度增大则压降增大,F>0.55时,压降变化没有明显规律;并经拟合得到泛点气速公式,与贝恩-霍根公式计算值相对误差为9.1%;以正庚烷-甲基环己烷为测试物系的热模实验表明:该填料理论板数较高,且F因子对其影响不大;F>2.3时,压降开始急剧增大。结果说明:PACTU-800操作弹性大,持液量大,适合高气液负荷下操作;其通量大,压降变化小,停留时间长,效率较高且较恒定。 相似文献