Calculation of net and gross heating values for natural gas systems. The number of binary mixtures with interaction parameters has increased from toincluding many mixtures of ethylene, propylene, methanol, ethanol, toluene, benzene, cyclohexane, sulfur dioxide, ammonia, dodecane, acetone, and butylene.Įxpanded support for natural gas systems, including the addition of the GERG mixture model for natural gas fluids, which includes binary interaction parameters for the following fluids: argon, butane, carbon monoxide, carbon dioxide, decane, ethane, helium, heptane, hexane, hydrogen, hydrogen sulfide, isobutane, isopentane, methane, nitrogen, nonane, octane, oxygen, pentane, propane, and water.Ĭonvergence along the saturation lines is now better for complex mixtures due to new algorithms for finding phase boundaries and the addition of analytical derivatives in the calculation of the fugacity. New features include: Additional pure fluids and updated equations of state and transport equations, including cyclopentane, Ryf, and Rze E. You can change your cookie settings through your browser. They were placed on your computer when you launched this website. Our policy towards the use of cookies Techstreet, a Clarivate Analytics brand, uses cookies to improve your online experience.
