2006
DOI: 10.1139/tcsme-2006-0036
|View full text |Cite
|
Sign up to set email alerts
|

Generalization of an Analytical Two-Phase Steam Flow Calculator to High-Pressure Cases

Abstract: Extension of a recently developed analytical two-phase steam flow calculator to high pressure cases is performed in this paper. The initial solution, obtained in earlier study was developed for low pressure cases. In low pressure cases, the vapor portion of the two-phase mixture reliably obeys the ideal gas Equation of State (EOS). In the present high pressure study, real gas effects are included using the more suitable EOS of “Lee-Kesler”. The model similar to the low pressure model assumes local equilibrium … Show more

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
1
1
1

Citation Types

0
3
0

Year Published

2010
2010
2017
2017

Publication Types

Select...
2

Relationship

0
2

Authors

Journals

citations
Cited by 2 publications
(3 citation statements)
references
References 12 publications
0
3
0
Order By: Relevance
“…Energies 2017, 10, 1285 11 of 36 degree is high, is rapid with a steep slope, but after the nucleation region has a slow growth and the flow relatively reaches equilibrium state. It should be noted that the difference between the radius calculated from theory is also reported in the results of other studies [2,41]. As mentioned, at this stage the aim of using inverse modeling is to obtain an optimum value for the parameter which will be calculated in the next section.…”
Section: Moore Nozzle Type Amentioning
confidence: 75%
“…Energies 2017, 10, 1285 11 of 36 degree is high, is rapid with a steep slope, but after the nucleation region has a slow growth and the flow relatively reaches equilibrium state. It should be noted that the difference between the radius calculated from theory is also reported in the results of other studies [2,41]. As mentioned, at this stage the aim of using inverse modeling is to obtain an optimum value for the parameter which will be calculated in the next section.…”
Section: Moore Nozzle Type Amentioning
confidence: 75%
“…The temperature of the droplets can be determined by capillarity effect, and since the droplets have very small size, their temperatures are assumed uniform through the droplets. With the definition of T s as the saturation temperature at the local pressure, P, the temperature equation for water droplet can be shown as (9) where r * is the critical droplet radius that will be described subsequently.…”
Section: Energy Equationsmentioning
confidence: 99%
“…(12)). Where γ is the specific heat ratio (average value for γ of superheated steam equal to 1.32 has been used throughout this study [9]) and is the equilibrium latent heat. The gas constant and temperature of gas are R, and T g respectively.…”
Section: Nucleationmentioning
confidence: 99%