Description AC3-08: Difference between revisions
(New page: ='''Spray evaporation in turbulent flow'''= '''Application Challenge 3-08''' © copyright ERCOFTAC 2004 =='''Introduction'''== In order to provide data for the validatio...) |
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{{AC|front=AC 3-08|description=Description_AC3-08|testdata=Test Case_AC3-08|cfdsimulations=CFD Simulations_AC3-08|evaluation=Evaluation_AC3-08|qualityreview=Quality Review_AC3-08|bestpractice=Best Practice Advice_AC3-08|relatedUFRs=Related UFRs_AC3-08}} | |||
='''Spray evaporation in turbulent flow'''= | ='''Spray evaporation in turbulent flow'''= | ||
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Fig. 1. Sketch of the test facility and dimensions of the test section (in mm) | Fig. 1. Sketch of the test facility and dimensions of the test section (in mm) | ||
Relevance to Industrial Sector | |||
=='''Relevance to Industrial Sector'''== | |||
A number of processes in chemical and food industry (e.g. spray drying) and in combustion science involve the evaporation of atomised liquids in a turbulent environment. The droplet evaporation is strongly governed by turbulent dispersion and gas temperature distribution. Therefore, this application challenge is rather demanding and requires appropriate modelling of the following effects: | A number of processes in chemical and food industry (e.g. spray drying) and in combustion science involve the evaporation of atomised liquids in a turbulent environment. The droplet evaporation is strongly governed by turbulent dispersion and gas temperature distribution. Therefore, this application challenge is rather demanding and requires appropriate modelling of the following effects: | ||
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• droplet heating and evaporation | • droplet heating and evaporation | ||
Design or Assessment Parameters | |||
=='''Design or Assessment Parameters'''== | |||
The assessment parameters for this application challenge are the velocity profiles of both phases along the test section, including mean velocities for the axial and radial component, as well as the associated rms-values. Additionally, profiles of droplet mean diameters and droplet mass flux can be used. From the liquid mass flow along the test section also the global evaporation rate may be used as an assessment parameter. | The assessment parameters for this application challenge are the velocity profiles of both phases along the test section, including mean velocities for the axial and radial component, as well as the associated rms-values. Additionally, profiles of droplet mean diameters and droplet mass flux can be used. From the liquid mass flow along the test section also the global evaporation rate may be used as an assessment parameter. | ||
Flow Geometry | |||
=='''Flow Geometry'''== | |||
The flow configuration was a vertical downward directed pipe expansion flow with an expansion ratio of three, where heated air entered through an annulus with a hollow cone spray nozzle being mounted in the centre (Fig. 1). The outer diameter of the annulus was 64 mm and nozzle holders with diameters of 20 and 40 mm were used, respectively. The test section had a diameter of 200 mm and a length of 1500 mm. Although the geometry does not exactly correspond to industrial situations the introduced test cases are very useful for the validation of the involved models. | The flow configuration was a vertical downward directed pipe expansion flow with an expansion ratio of three, where heated air entered through an annulus with a hollow cone spray nozzle being mounted in the centre (Fig. 1). The outer diameter of the annulus was 64 mm and nozzle holders with diameters of 20 and 40 mm were used, respectively. The test section had a diameter of 200 mm and a length of 1500 mm. Although the geometry does not exactly correspond to industrial situations the introduced test cases are very useful for the validation of the involved models. | ||
Flow Properties | |||
=='''Flow Properties'''== | |||
All experiments were performed with air at various flow rates and inlet temperatures (i.e. 353 and 373 K). As a liquid isopropyl-alcohol was used due to its high evaporation rates. Details on the air and liquid properties and their determination are provided below. The average initial droplet size was around 20 mm. The flow Reynolds number calculated with the measured volume flow rate, the test section diameter and the air properties at the inlet is in the range between 4,000 and 10,000. More details for the individual test cases are provided in Table 1 given below. | All experiments were performed with air at various flow rates and inlet temperatures (i.e. 353 and 373 K). As a liquid isopropyl-alcohol was used due to its high evaporation rates. Details on the air and liquid properties and their determination are provided below. The average initial droplet size was around 20 mm. The flow Reynolds number calculated with the measured volume flow rate, the test section diameter and the air properties at the inlet is in the range between 4,000 and 10,000. More details for the individual test cases are provided in Table 1 given below. | ||
© copyright ERCOFTAC 2004 | © copyright ERCOFTAC 2004 | ||
---- | |||
Contributors: Martin Sommerfeld - Martin-Luther-Universitat Halle-Wittenberg | Contributors: Martin Sommerfeld - Martin-Luther-Universitat Halle-Wittenberg | ||
Site Design and Implementation: Atkins and UniS | Site Design and Implementation: [[Atkins]] and [[UniS]] | ||
{{AC|front=AC 3-08|description=Description_AC3-08|testdata=Test Case_AC3-08|cfdsimulations=CFD Simulations_AC3-08|evaluation=Evaluation_AC3-08|qualityreview=Quality Review_AC3-08|bestpractice=Best Practice Advice_AC3-08|relatedUFRs=Related UFRs_AC3-08}} | |||
Latest revision as of 16:08, 11 February 2017
Spray evaporation in turbulent flow
Application Challenge 3-08 © copyright ERCOFTAC 2004
Introduction
In order to provide data for the validation of numerical calculations, the spray evaporation in a heated turbulent air stream was studied experimentally (Sommerfeld and Qiu, 1998). The flow configuration was a pipe expansion with an expansion ratio of three, where heated air entered through an annulus with the hollow cone spray nozzle being mounted in the centre (Fig. 1). In the experiments isopropyl-alcohol was used as a liquid due to its high evaporation rates. Measurements were taken for different flow conditions, such as air flow rate, air temperature, and liquid flow rate in order to provide a set of reliable data. Phase-Doppler anemometry (PDA) was applied to obtain the spatial change of the droplet size spectrum in the flow field and to measure droplet size-velocity correlations. From these local measurements, profiles of droplet mean velocities, velocity fluctuations, and droplet mean diameters were obtained by averaging over all droplet size classes. Moreover, recent extensions of the PDA signal processing (Sommerfeld and Qui, 1995) allowed to determine accurately profiles of the droplet mass flux, whereof also the global evaporation rates could be determined. The data for the different flow conditions also include the inlet conditions for air flow and spray (i.e. for all three velocity components), inlet temperature and wall temperature profiles. The latter was measured using a thermocouple with a special wall sensor.
Fig. 1. Sketch of the test facility and dimensions of the test section (in mm)
Relevance to Industrial Sector
A number of processes in chemical and food industry (e.g. spray drying) and in combustion science involve the evaporation of atomised liquids in a turbulent environment. The droplet evaporation is strongly governed by turbulent dispersion and gas temperature distribution. Therefore, this application challenge is rather demanding and requires appropriate modelling of the following effects:
• flow field and turbulence structure
• gas temperature distribution
• two-way coupling which strongly changes the temperature field due do droplet evaporation
• turbulent dispersion of droplets
• droplet heating and evaporation
Design or Assessment Parameters
The assessment parameters for this application challenge are the velocity profiles of both phases along the test section, including mean velocities for the axial and radial component, as well as the associated rms-values. Additionally, profiles of droplet mean diameters and droplet mass flux can be used. From the liquid mass flow along the test section also the global evaporation rate may be used as an assessment parameter.
Flow Geometry
The flow configuration was a vertical downward directed pipe expansion flow with an expansion ratio of three, where heated air entered through an annulus with a hollow cone spray nozzle being mounted in the centre (Fig. 1). The outer diameter of the annulus was 64 mm and nozzle holders with diameters of 20 and 40 mm were used, respectively. The test section had a diameter of 200 mm and a length of 1500 mm. Although the geometry does not exactly correspond to industrial situations the introduced test cases are very useful for the validation of the involved models.
Flow Properties
All experiments were performed with air at various flow rates and inlet temperatures (i.e. 353 and 373 K). As a liquid isopropyl-alcohol was used due to its high evaporation rates. Details on the air and liquid properties and their determination are provided below. The average initial droplet size was around 20 mm. The flow Reynolds number calculated with the measured volume flow rate, the test section diameter and the air properties at the inlet is in the range between 4,000 and 10,000. More details for the individual test cases are provided in Table 1 given below.
© copyright ERCOFTAC 2004
Contributors: Martin Sommerfeld - Martin-Luther-Universitat Halle-Wittenberg
Site Design and Implementation: Atkins and UniS