TY - JOUR
T1 - Axial mixing in modern packings, gas and liquid phases
T2 - I. Single-phase flow
AU - Macías-Salinas, Ricardo
AU - Fair, James R.
PY - 1999/2
Y1 - 1999/2
N2 - An experimental study was conducted in a 0.43-m-ID packed column to determine the axial mixing properties of air and water under single-phase flow conditions. The packings used were 25.4-mm ceramic Raschig rings, one modern random packing, 25.4-mm metal Pall rings; two structured packings, Sulzer BX and Flexipac 2. The column was operated at ambient conditions with flow rates varying from 0.4 to 4 kg/m2 · s for the gas and from 3.25 to 8.5 kg/m2 · s for the liquid. Axial mixing was experimentally determined via dynamic response studies based on the pulse injection technique. The diffusion-type model served to reproduce the experimental response curves satisfactorily and proved to be a suitable means of describing axial mixing in both phases. The results confirm previous observations for first-generation packings. Axial mixing is much greater in the liquid than in the gas; axial mixing in the gas increases with gas rate, whereas axial mixing in the liquid decreases with liquid rate. It was also found that the two structured packings produce the lowest levels of axial mixing in the gas. Surprisingly, the greatest mixing effects in the liquid were obtained for Flexipac 2 structured packing. Correlations were developed to represent the experimental mixing and liquid holdup data, yielding an average ± 16% difference between experimental and correlated data. Mixing measurements in gas or liquid under two-phase flow conditions will be discussed in Part II.
AB - An experimental study was conducted in a 0.43-m-ID packed column to determine the axial mixing properties of air and water under single-phase flow conditions. The packings used were 25.4-mm ceramic Raschig rings, one modern random packing, 25.4-mm metal Pall rings; two structured packings, Sulzer BX and Flexipac 2. The column was operated at ambient conditions with flow rates varying from 0.4 to 4 kg/m2 · s for the gas and from 3.25 to 8.5 kg/m2 · s for the liquid. Axial mixing was experimentally determined via dynamic response studies based on the pulse injection technique. The diffusion-type model served to reproduce the experimental response curves satisfactorily and proved to be a suitable means of describing axial mixing in both phases. The results confirm previous observations for first-generation packings. Axial mixing is much greater in the liquid than in the gas; axial mixing in the gas increases with gas rate, whereas axial mixing in the liquid decreases with liquid rate. It was also found that the two structured packings produce the lowest levels of axial mixing in the gas. Surprisingly, the greatest mixing effects in the liquid were obtained for Flexipac 2 structured packing. Correlations were developed to represent the experimental mixing and liquid holdup data, yielding an average ± 16% difference between experimental and correlated data. Mixing measurements in gas or liquid under two-phase flow conditions will be discussed in Part II.
UR - http://www.scopus.com/inward/record.url?scp=0040439799&partnerID=8YFLogxK
U2 - 10.1002/aic.690450203
DO - 10.1002/aic.690450203
M3 - Artículo
SN - 0001-1541
VL - 45
SP - 222
EP - 239
JO - AIChE Journal
JF - AIChE Journal
IS - 2
ER -