A new equation of state for carbon dioxide covering the fluid region from the triple-point temperature to 1100 K at pressures up to 800 MPa,,triple,dioxide,pressures,covering,fluid,carbon君,已阅读到文档的结尾了呢~~ 立即下载 相似精选,再来一篇 ...
A New Equation of State for Carbon Dioxide Covering the Fluid Region from the Triple-Point Temperature to 1100 K at Pressures up to 800 MPa R. Span and W. Wagner Lehrstuhl fur Thermodynamik, Ruhr-Universitat Bochum, D-44780 Bochum, Germany Received 25 May 1994 This work reviews the ...
A New Equation of State for Carbon Dioxide Covering the Fluid Region from the Triple-Point Temperature to 1100 K at Pressures up to 800 MPa Span R., Wagner W., "A New Equation of State for Carbon Dioxide Covering the Fluid Region from the Triple-Point Temperature to 1100 K at Pressures...
A new equation of state for carbon dioxide covering the fluid region from the triple-point temperature to 1100 K at pressures up to 800 MPa J. Phys. Chem. Ref. Data, 25 (1996), pp. 1509-1596, 10.1063/1.555991 View in ScopusGoogle Scholar [36] G. Manzolini, M. Binotti, E. Morosi...
Based on theoretical results for hard-dipolar spheres and the computer simulation data for n-butane a new equation of state is applied to the correlation of thermodynamic properties for ten pure polar and nonpolar fluids: methane, ethane, n-butane, water, ammonia, carbon dioxide, acetonitrile, ...
With the introduction of carbon capture and storage (CCS) as a means to reduce carbon emissions, a need has arisen for accurate and efficient simulation tools. In this work, we propose a method for dynamic simulations of carbon dioxide using the Span–Wagner reference equation of state. The ...
It combines molecular dynamics simulation on the one side with density gradient theory using an equation of state (EOS) on the other. The new method is applied here to predict bubble nucleation rates in metastable liquid carbon dioxide (CO2). The molecular model of CO2 is taken from previous ...
For Schemes 2–5, the energy balance of the whole process, mainly composed of the granulation and gasification steps, is expressed by the following equation, where the calculations and the related simplifications of each part regarding the energy balance are more complex (Supplementary note 4): $...
(2009) were the first to employ the Span-Wagner state equation (1996) to the wellbore flow and heat transfer model, improving the calculated accuracy. Wang et al. (2016a, 2016b) and Li et al. (2017b) introduced the specific enthalpy gradient equation of compressible fluid into the energy...
Future hydrogen demand levels reaching up 3000 TgH2/year were recently applied to derive an equilibrium global surface temperature increase29. However, the climate steady-state to a perturbation in hydrogen emissions will be reached over centuries, providing that all other parameters are constant. ...