TY - JOUR
T1 - The effect of liquid co-flow on gas fractions, bubble velocities and chord lengths in bubbly flows. Part I
T2 - Uniform gas sparging and liquid co-flow
AU - Muilwijk, Corné
AU - Van den Akker, Harry E.A.
N1 - Publisher Copyright:
© 2020 The Authors
PY - 2021/4
Y1 - 2021/4
N2 - Unique experiments were performed in a homogeneously sparged rectangular 400×200×2630 mm (W×D×H) bubble column with and without liquid co-flow. Bubbles in the range 4–7 mm were produced by needle spargers, which resulted in a very uniform bubble size. Dual-tip optical fibre probes were used to measure horizontal profiles of gas fractions, bubble velocities and bubble chord lengths for superficial gas velocities Usg in the range 0.63–6.25 cm/s and superficial liquid velocities Usl up to 20 cm/s. Images of the bubble column were captured and a Bubble Image Velocimetry technique was adopted to calculate bubble (parcel) velocities. For low gas fractions, when a homogeneous flow regime occurred, both methods agreed very well and the optical fibre probes were found to be rather accurate for our bubbles. A liquid co-flow was found to have a calming effect and to stabilize a homogeneous bubbly flow regime, with less spatial variation in gas fractions and bubble velocities. Bubble chord lengths were almost normally distributed and do not exhibit the theoretical triangular probability density functions. The mean cord lengths were in the range 1.9–3.5 mm and found to increase with Usg and to decrease slightly with increasing Usl, while a liquid co-flow significantly reduced the standard deviation of the chord length distribution.
AB - Unique experiments were performed in a homogeneously sparged rectangular 400×200×2630 mm (W×D×H) bubble column with and without liquid co-flow. Bubbles in the range 4–7 mm were produced by needle spargers, which resulted in a very uniform bubble size. Dual-tip optical fibre probes were used to measure horizontal profiles of gas fractions, bubble velocities and bubble chord lengths for superficial gas velocities Usg in the range 0.63–6.25 cm/s and superficial liquid velocities Usl up to 20 cm/s. Images of the bubble column were captured and a Bubble Image Velocimetry technique was adopted to calculate bubble (parcel) velocities. For low gas fractions, when a homogeneous flow regime occurred, both methods agreed very well and the optical fibre probes were found to be rather accurate for our bubbles. A liquid co-flow was found to have a calming effect and to stabilize a homogeneous bubbly flow regime, with less spatial variation in gas fractions and bubble velocities. Bubble chord lengths were almost normally distributed and do not exhibit the theoretical triangular probability density functions. The mean cord lengths were in the range 1.9–3.5 mm and found to increase with Usg and to decrease slightly with increasing Usl, while a liquid co-flow significantly reduced the standard deviation of the chord length distribution.
KW - Bubble column
KW - Bubble image velocimetry
KW - Chord length distribution
KW - Gas hold-up
KW - Liquid co-flow
KW - Optical fibre probe
UR - http://www.scopus.com/inward/record.url?scp=85100667778&partnerID=8YFLogxK
U2 - 10.1016/j.ijmultiphaseflow.2020.103498
DO - 10.1016/j.ijmultiphaseflow.2020.103498
M3 - Article
AN - SCOPUS:85100667778
SN - 0301-9322
VL - 137
JO - International Journal of Multiphase Flow
JF - International Journal of Multiphase Flow
M1 - 103498
ER -