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where <math>\rho_l</math> is the liquid density, <math>u_{j p}</math> is the liquid velocity at inlet ports and <math>D_{\text {in }}</math> is the hydraulic diameter of the inlet ports. The <math>R e_{i n}=1330</math>. The presented case is one of three inlet pressure cases <math>\left(p_{\text {in }}=0.25,0.5,1 \mathrm{MPa}\right)</math> measured and studied in [2].
where <math>\rho_l</math> is the liquid density, <math>u_{j p}</math> is the liquid velocity at inlet ports and <math>D_{\text {in }}</math> is the hydraulic diameter of the inlet ports. The <math>R e_{i n}=1330</math>. The presented case is one of three inlet pressure cases <math>\left(p_{\text {in }}=0.25,0.5,1 \mathrm{MPa}\right)</math> measured and studied in <ref name="Cejpek2"> O. Cejpek, M. Maly, J. Slama, M. M. Avulapati, and J. Jedelsky, Continuum Mechanics and Thermodynamics 34 (6), 1497 (2022) </ref>.
The interaction of the spray with the cross-flowing air is controlled by the ratio of the momentum of liquid to the air momentum (see '''Equation (10)''') and by the Weber number which relies on the surface tension forces of the liquid film with the drag forces of the airflow ('''Equations (11) and (12)'''). <math>We</math> and <math>q</math> values for the experimental regimes are outlined in '''Table 2'''.
The interaction of the spray with the cross-flowing air is controlled by the ratio of the momentum of liquid to the air momentum (see '''Equation (10)''') and by the Weber number which relies on the surface tension forces of the liquid film with the drag forces of the airflow ('''Equations (11) and (12)'''). <math>We</math> and <math>q</math> values for the experimental regimes are outlined in '''Table 2'''.


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== References ==
<references/>


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Revision as of 09:19, 17 May 2023

Lib:Create_Ercoftac_Article_Form

Front Page

Introduction

Review of experimental studies

Description

Experimental Set Up

Measurement Quantities and Techniques

Data Quality and Accuracy

Measurement Data and Results

Description of Study Test Case

The conical liquid sheet produced by water spraying in PSA was investigated in cross-flow of non-heated, non-pressurised air. The atomiser was operated continuously in cold-flow (non-reacting) conditions. It generated a water spray at inlet pressure, , of 0.5 MPa. The flow conditions of the atomiser are described by Reynolds number:

where is the liquid density, is the liquid velocity at inlet ports and is the hydraulic diameter of the inlet ports. The . The presented case is one of three inlet pressure cases measured and studied in [1]. The interaction of the spray with the cross-flowing air is controlled by the ratio of the momentum of liquid to the air momentum (see Equation (10)) and by the Weber number which relies on the surface tension forces of the liquid film with the drag forces of the airflow (Equations (11) and (12)). and values for the experimental regimes are outlined in Table 2.

The description can be kept fairly short if reference can be made to a publication or a link to a data base where details are given. For other cases a more detailed, self-contained description should be provided.

Table 2 Experimental regimes, basic characteristics of the flow and spray

[m/s]

[MPa]

[kg/hour]

[–]

We [–]

[–]

q [–]

0

0.508

6.71

0.44

0.0

0.5


8

0.498

6.72

0.43

0.5

0.85

3642.0

16

0.491

6.68

0.42

1.8

1.5

938.8

32

0.493

6.69

0.43

7.1

3.4

227.1

References

  1. O. Cejpek, M. Maly, J. Slama, M. M. Avulapati, and J. Jedelsky, Continuum Mechanics and Thermodynamics 34 (6), 1497 (2022)


Contributed by: Ondrej Cejpek, Milan Maly, Ondrej Hajek, Jan Jedelsky — Brno University of Technology

Front Page

Introduction

Review of experimental studies

Description

Experimental Set Up

Measurement Quantities and Techniques

Data Quality and Accuracy

Measurement Data and Results


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