![]() Finally, you would need to implement a transport model that worked under these conditions, since REFPROP does not seem to provide these, and Cantera's mixture averaged and multicomponent models only apply to ideal gases. Refprop library of NIST 1,3-Butadiene (vinylethylene, CH2CH-CHCH2) 1-Butene (CH3-CH2-CHCH2) 1-Butyne (ethyl acetylene, C4H6) 1-Pentene (C5H10) 2,2-. Thermodynamic properties of the refrigerant blends are calculated using the NIST Standard Reference Database 23: Reference Fluid Thermodynamic and Transport Properties REFPROP, Version 10.0 5. Chebyshev polynomials as a function of T and P). Site is running on IP address 132.163.4.175, host name 132.163.4.175 (Boulder United States) ping response time 4ms Excellent ping. You would also need a reaction mechanism that was valid under conditions where real gas effects are important, although at least on this front Cantera does support fairly arbitrary parameterizations of rate constants (e.g. In addition, at least in the case of Cantera, the governing equations of the flame are implemented specifically for ideal gases, so you would need to reformulate the governing equations for a more arbitrary equation of state and implement that as well. If you wanted to use those equations of state for a flame simulation, you would also need to have equations of state for all of the unstable intermediate species present in the flame. REFPROP implements non-ideal equations of states for a set of stable species. Setting aside the software interfacing for a moment, I'm not sure how this would work. ![]()
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