CIESC Journal

• 化工学报 • 上一篇    下一篇

网孔塔板的流体力学

路秀林,赵大企,刘玉民,黄丽华   

  1. 上海化工学院化学工程研究所 ,上海化工学院化学工程研究所 ,上海化工学院化学工程研究所 ,抚顺石油二厂
  • 出版日期:1980-09-25 发布日期:1980-09-25

Hydrodynamics of Perform Trays

Lu Xiu-lin and Zhao Da-qi Chem, Eng. Research Center, Shanghai Institute of Chemical Technology Liu Yu-min and Huang Li-hua Second Petroleum Refinery,Fushun   

  • Online:1980-09-25 Published:1980-09-25

摘要: 木文以空气-水系统在1200×400mm矩形装置内对网孔塔板的流体力学进行了试验研究。试验所采用的塔板参数和操作条件为:塔板开口宽度为3、3.5、4、4.5及4.7mm;塔板开孔率为9.9、12.3、13.2、14.9及15.4%; 挡沫板宽度为150、200、250、300mm;板间距为400、500、600、700及800mm;液流强度为20、30、45、60m~3/m·h;气体空塔速度为0.60—2.8m/s。测定了各有关参数对塔板压降、雾沫夹带和泄漏的影响,并对试验数据进行了关联,得出了计算塔板压降、雾沫夹带、泄漏、上限气速、下限气速及操作弹性等的关系式,以便用于网孔塔板的设计。

Abstract: The hydrodynamics of perform trays were studied using air-water system in a column with a 1200 x 400mm rectangular cross section to determine the effect of tray geometrical parameters and operating conditions on the pressure drop, entrainment and weeping. Geometrical variables and operating range were mainly as follows: slot widths, 3, 3.5, 4, 4.5 and 4.7mm; tray free areas, 9.9, 12.3, 14.9 and 15.4%; deflector widths, 150, 200, 250 and 300mm; tray spa-cings, 400, 500, 600, 700 and 800mm; liquid flow rates per unit weir length, 20, 30, 45 and 60m3/m.h; and superficial gas velocities, 0.60 to 2.8m/s. Experimental data were correlated and correlations were presented for calculating the pressure drop, entrainment and liquid weeping. Furthermore, based on the experimental results for the entrainment and weeping from the tray,the expressions were given also to predict the upper limiting hole velocity at which the entrainment from the tray is 10%, the lower limiting hole velocity at which the liquid weeping from the tray is 5%. In addition, the effect of inlet weir on the weeping were tested and a simiempirical model was derived for the inlet weir design. These correlations, as mentioned above, can be applied to the design of perform trays.