Abstract

The development of a round liquid jet under the influence of a confined coaxial flow of an immiscible liquid of comparable density (central to annular flow density ratio of 8:10) was investigated in the vicinity of the nozzle exit. Two flow regimes were considered; one where the annular flow is faster than the central jet, so the central liquid jet is accelerated and one where the annular flow is slower, so the central liquid jet is decelerated. The central jet was visualised by high speed photography. Three modes of jet development were identified and classified in terms of the Reynolds number, Re, of the central jet which was in the range of 525 < Re < 2725, a modified definition of the Weber number, We, which allows the distinction between accelerating and deceleration flows and was in the range of −22 < We < 67 and the annular to central Momentum Ratio, MR, of the two streams which was in the range of 3.6 < MR < 91. By processing the time resolved jet images using Proper Orthogonal Decomposition (POD), it was possible to reduce the description of jet morphology to a small number of spatial modes, which isolated the most significant morphologies of the jet development. In this way, the temporal and spatial characteristics of the instabilities on the interface were clearly identified which highlights the advantages of POD over direct observation of the images. Relationships between the flow parameters and the interfacial waves were established. The wavelength of the interfacial instability was found to depend on the velocity of the fastest moving stream, which is contrary to findings for fluids with large density differences.

Highlights

  • Latter the central jet becomes elongated due to momentum transfer between the two streams leading to deceleration and acceleration of the central jet, respectively

  • Three modes of jet development were identified and classified in terms of the Reynolds number, Re, of the central jet which was in the range of 525 < Re < 2725, a modified definition of the Weber number, We, which allows the distinction between accelerating and deceleration flows and was in the range of −22 < We < 67 and the annular to central Momentum Ratio, momentum ratio (MR), of the two streams which was in the range of 3.6 < MR < 91

  • By processing the time resolved jet images using Proper Orthogonal Decomposition (POD), it was possible to reduce the description of jet morphology to a small number of spatial modes, which isolated the most significant morphologies of the jet development

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Summary

INTRODUCTION

Latter the central jet becomes elongated due to momentum transfer between the two streams leading to deceleration and acceleration of the central jet, respectively. For the analysis of the morphology of the central jet beyond the direct observation of the jet characteristics, the Proper Orthogonal Decomposition (POD) method will be used. This method was originally proposed by Pearson[20] for the optimal description of multidimensional datasets when reducing the number of dimensions. For the jets of the current investigation, we consider less intense interaction between the two streams for either for accelerated or decelerated central liquid jets and jet morphologies that are not chaotic can be expected, so that a more definite description of their characteristics can be derived.

EXPERIMENTAL ARRANGEMENT
MORPHOLOGY OF THE CENTRAL LIQUID JET
Straight jet
Varicose jet
Findings
DISCUSSION
CONCLUSIONS
Full Text
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