北京化工学院化学工程系,北京化工学院化学工程系,北京化工学院化学工程系,北京化工学院化学工程系,北京化工学院化学工程系
网络首发:1982-03-25,
纸质出版:1982-03-25
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莫锡荣, 何达鑫, 江生南, 等. 管栅式喷射塔的初步探讨[J]. 化工学报, 1982,(1).
Mo Xirong, He Daxin, Jiang Shengnan, et al. A Preliminary Approach to Tube-Grid Jet[J]. CIESC Journal, 1982, (1).
管栅式喷射元件是作者研制的一种新型传质元件。本文介绍了它的结构特点
测定了它的压降和传质性能
求得了本实验条件下估算压降和传质单元数的关联式
并与锥形喷杯的压降、传质性能作了比较。
The tube-grid jet is a novel
simple and efficient device for mass-transfer. fts construction is shown in Fig. 1. The main experimental equipment employed in this study consists of a tube-grid jet unit
an absorption section and a separation section. The diameter of the absorption section is 150mm. The ratio of height to diameter of the absorption section is 10.7
and thearea ratio of tube-grid slits to absorption section 0.113. The schematic diagram of the apparatus employed in this study is given in Figure 2. The fluid-dynamic experiments have been carried out with the air-water system and the mass-transfer experiments with the ammonia-air-water system. The conditions of the present work were- the gas velocity calculated over the whole cross-sectional area of the absorption section w=2-9m/s
the gas velocity at the slits of the tube-grid w0=17-76m/s
the liquid-gas ratio w=3-501/m3. Two flow patterns were observed in the fluid-dynamic experiments. The transition of the two flow patterns occurs at where m - liquid-gas ratio
1/m3
Wo- gas velocity at the tube-grid slits
rn/s
u- viscosity of the gas
kg-s/m2
density of the gas
kg/m3
and de - equivalent diameter of the tube-grid slits
m.the pressure drop across the wet-drained tube-grid jet unit can be calculated from where La is the Lagrangian number Two operating regions for the different mass-transfer characteristics were also observed. Empiric regression equations for the number of overall gas transfer units NOG based on the tube-grid jet unit are N oo = 0. 027 W-W8 when zw<475 l/m2s
and when Mvw>475 l/m2s. It should be pointed out that the maximum deviation of all the experimental data from the above empiric correlations is ?0%. It is important to see that the pressure drop across the tube-grid unit is about 30% less than that across the cup- jet unit
and the gas mass-transfer coefficient per unit pressure drop Ky
/AP of the tube-grid jet unit is higher than that of the cup-jet unit. Besides
the construction of the tube-grid jet is simple and it is very easy to manufacture. Hence the tube-grid jet
in general
is superior to the cup- jet.
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