Transient Natural Convection Heat Transfer to CO2 in the Supercritical Region

2018 ◽  
Vol 140 (9) ◽  
Author(s):  
G. Janardhana Reddy ◽  
Hussain Basha ◽  
N. S. Venkata Narayanan

Present research paper investigates the transient laminar free convective supercritical carbon dioxide flow past a semi-infinite vertical cylinder using numerical methods. Two new thermodynamic models for the supercritical fluid (SCF) flow are considered. Based on these models, for supercritical carbon dioxide, two new equations for thermal expansion coefficient are obtained on the basis of Redlich–Kwong equation of state (RK-EOS) and Van der Waals equation of state (VW-EOS). Based on the calculated values of thermal expansion coefficient, it is shown that not only RK-EOS is closer to experimental values but also gives greater accuracy when compared to VW-EOS validating RK-EOS as suitable model for predicting natural convective properties of carbon dioxide under supercritical condition. The governing equations of SCF flow are solved numerically using Crank–Nicolson implicit finite difference scheme. Numerical simulations are performed for carbon dioxide in the region of its critical point. Results in subcritical, supercritical, and near-critical regions are shown graphically and discussed for different physical parameters. From the obtained numerical results, it is clear that the steady-state time increases for the increasing values of reduced temperature and reduced pressure for carbon dioxide in supercritical region.

Author(s):  
Hussain Basha ◽  
G. Janardhana Reddy ◽  
N. S. Venkata Narayanan

Abstract The present paper studies through numerical methods, the thermodynamic heat transfer characteristics of free convection flow of supercritical nitrogen over a vertical cylinder. In the present analysis, the values of volumetric thermal expansion coefficient ($\beta$) are evaluated based on Redlich-Kwong equation of state (RK-EOS) and Van der Waals equation of state (VW-EOS). The calculated analytical thermal expansion coefficient values using RK-EOS are very close to NIST data values in comparison with VW-EOS. A set of coupled nonlinear partial differential equations (PDEs) governing the supercritical fluid (SCF) flow are derived, converted into non-dimensional form with the help of suitable dimensionless quantities and solved using Crank-Nicolson implicit finite difference method. The simulations are carried out for nitrogen in the supercritical region. The obtained numerical data is expressed in terms of graphs and tables for various values of physical parameters. The increasing value of reduced temperature decreases the average Nusselt number and skin-friction coefficient, whereas amplifying value of reduced pressure enhance the heat transfer rate and wall shear stress in the SCF region. Present results are compared with the previous results and the two are found to be in good agreement, i. e. the numerically generated results found to be in agreement with existing results.


Author(s):  
Hussain Basha ◽  
G. Janardhana Reddy ◽  
N.S. Venkata Narayanan

Present numerical study examines the free convection heat transfer characteristics of supercritical water flow past a stretching sheet. A suitable equation for thermal expansion coefficient in supercritical fluid region is derived based on the equation of state approach (EOS) in terms of compressibility factor, pressure and temperature. In the present study Redlich-Kwong equation of state (RK-EOS) is used to calculate the thermal expansion coefficient in supercritical region. The values of thermal expansion coefficient calculated through RK-EOS lies close to the NIST data values when compared to the other equations of state like VW-EOS (Van der Waals equation of state) and Ideal gas-EOS. Also, the behaviour of Nusselt number is studied to characterize the heat transfer characteristics of supercritical water. However, the equations governing the supercritical fluid flow past a stretching sheet are coupled and nonlinear in nature. Hence, Runge-Kutta fourth-order integration scheme with shooting technique (RK-SM) is used to solve these equations. Numerical computations are performed for supercritical water (SCW) under the influence of various control parameters. Similarity solutions are obtained in terms of flow profiles in supercritical fluid region. Present study reports that, the normal velocity profile decreases and temperature field increases for the increasing values of reduced pressure and reduced temperature. Also, axial velocity profile shows the dual behaviour for the increasing values of unsteady parameter, reduced temperature and reduced pressure in the supercritical boundary layer region. Further, the component of normal velocity profile decays for the increasing values of unsteady parameter in supercritical fluid region. The calculated values of thermal expansion coefficient using Redlich-Kwong equation of state lies in the proximity of NIST data values when compared to Van der Waals and Ideal gas equations of state. Also, the local skin-friction coefficient decreases for the increasing values of reduced pressure and reduced temperature.


1969 ◽  
Vol 42 (5) ◽  
pp. 1409-1411
Author(s):  
B. E. Eichinger ◽  
P. J. Flory

Abstract The density, thermal expansion coefficient, and thermal pressure coefficient for polyisobutylene of mol wt 40,000 have been accurately determined from 0 to 150°. Results are compared with the reduced equation of state employed in the theory of solutions. The characteristic parameters v*, T*, and p* required for the treatment of polyisobutylene solutions are obtained from the experimental results.


2016 ◽  
Vol 10 (1) ◽  
pp. 18-28 ◽  
Author(s):  
Maria Y. Dwi ◽  
Jessica Julian ◽  
Jindrayani N. Putro ◽  
Adi T. Nugraha ◽  
Yi-Hsu Ju ◽  
...  

The solubility data of acetophenone in supercritical carbon dioxide (scCO2) were measured using a static method at several temperatures (313.15, 323.15, 333.15, and 343.15K) and pressures ranging from10 MPa to 28 MPa. The density based models (Chrastil and Del valle– Aguilera models) and the Peng-Robinson equation of state (PR-EOS) with quadratic and Stryjek-Vera combining rules were employed to correlate the experimental data. Good correlations between the calculated and experimental solubility data were obtained. The sum of squared errors (SSE) are 0.38 % and 0.37 % for Chrastil and Del Valle – Aguilera models, respectively; and 9.07 % for Peng-Robinson equation of state with quadratic combining rule and 4.00 % for Peng-Robinson equation of state with Stryjek-Vera combining rule.


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