CIESC Journal

• 化工学报 • 上一篇    

泡罩齿缝张开程度与空气流量的关系

路秀林,丁伯民,璩定一   

  1. 华东化工学院化工机械系 ,华东化工学院化工机械系 ,华东化工学院化工机械系
  • 出版日期:1965-09-25 发布日期:1965-09-25

THE CORRELATION OF SLOT OPENING OF A BUBBLE CAP WITH AIR FLOW RATE

Department of Process Equipment, Hua Tung Institute of Chemical Technology Lu XIU-LIN, TING BEE-MING, JU TIKG-YIH   

  • Online:1965-09-25 Published:1965-09-25

摘要: 本文是前文的继续。利用空气-水系统,分别对矩形、三角形和梯形三种型式的单一齿缝进行实验,发现了前人工作的不足之处;并进一步考虑到泡罩的实际操作情况,指出在Rogers-Thiele积分式中,将泡罩环隙气速的影响予以忽略是不够妥当的。在此基础上,提出了具有环隙气速影响的积分式,并在具有矩形齿缝的单泡罩内,对相应的积分式加以验证。验证结果,当Re>2000时,齿缝张开程度的计算值与实验值相比,其最大偏差为±3%,表明该式尚能反映操作的实际情况。

Abstract: In the present paper, as a second part of the previous paper published in this journal (No.1, 16-23, 1958), the authors made further experimental studies on single slots of different shapes and dimensions to correlate slot opening with air flow rate. Considering the vapor velocity in the annular space between the riser and the bubble cap in operation, which had been neglected in the single slot studies, the authors presented a new approach to evaluate the slot opening, which was tested experimentally. (1) For single slot studies, experimental conditions were extended as follows. Slot dimensions, rectangular slots, 6=2.27-25.28mm; triangular slots, B/H=0.255-1.40; trapezoidal slots, (B2-B1)/H=0.072 -0.796. Air flow rates. Vs≤357×102litres/hr. Immersed depth. 30mm. The results shows that the value of the discharge coefficient u in the Rogers-Thiele formula is not a constant but a function of Reynolds number as well as slot dimensions. For definite slot dimensions, the value of u will be a constant only when the air flow Reynolds number is high. ( 2 ) With the effects of the annular space vapor velocity considered, the authors proposed the following formulas as a modification of those of Rogers and Thiele. Rectangular slots. Triangular slots. Trapezoidal slots. It is apparent that the Rogers-Thiele formulas are only special forms of the above with a= 0.( 3 ) Formula (6) was tested experimentally in a single bubble cap, with the following experimental conditions. Bubble cap shape and dimensions. Circular cap with 40 rectangular slots; Cap I.D., 100mm; Riser O.D., 68mm; Slot width, 4mm; Slot height, 25mm. System. Air-water. Operating conditions. Static immersed depth, 15mm; Air flow rates,V = 22.1-111.0 cubic metres/hr. The results point out that the formulas proposed in the previous paper can be applied to bubble caps at Re≥2600 without appreciable error. The experimental data were compared with the calculated values of slot opening from the Rogers-Thiele formula, the Cross-Ryder formula, the formulas in the previous paper,and formula (6 ) in this paper. It has been found that when Re≥2000, the maximum deviation for formula (6 ) was 3%, while that for the other formulas were 17.5%, 9.2% and 8.5% respectively. After making a theoretical analysis, the authors are of the opinion that the formulas proposed can represent to a certain extent the operating conditions of a bubble cap. Similar results could be anticipated from a bubble cap with triangular or trapezoidal slots, but further experimental studies will be needed.