use approx::assert_relative_eq; use feos_core::parameter::{IdentifierOption, Parameter}; use feos_core::{Contributions, PhaseEquilibrium}; use feos_pcsaft::{PcSaft, PcSaftParameters}; use quantity::si::*; use std::error::Error; use std::rc::Rc; #[test] fn vle_pure_temperature() -> Result<(), Box> { let params = PcSaftParameters::from_json( vec!["propane"], "tests/test_parameters.json", None, IdentifierOption::Name, )?; let saft = Rc::new(PcSaft::new(Rc::new(params))); let temperatures = [ 170.0 * KELVIN, 200.0 * KELVIN, 250.0 * KELVIN, 300.0 * KELVIN, 350.0 * KELVIN, ]; for &t in temperatures.iter() { let state = PhaseEquilibrium::pure(&saft, t, None, Default::default())?; assert_relative_eq!(state.vapor().temperature, t, max_relative = 1e-10); assert_relative_eq!( state.vapor().pressure(Contributions::Total), state.liquid().pressure(Contributions::Total), max_relative = 1e-8 ); } Ok(()) } #[test] fn vle_pure_pressure() -> Result<(), Box> { let params = PcSaftParameters::from_json( vec!["propane"], "tests/test_parameters.json", None, IdentifierOption::Name, )?; let saft = Rc::new(PcSaft::new(Rc::new(params))); let pressures = [0.1 * BAR, 1.0 * BAR, 10.0 * BAR, 30.0 * BAR, 44.0 * BAR]; for &p in pressures.iter() { let state = PhaseEquilibrium::pure(&saft, p, None, Default::default())?; println!( "liquid-p: {} vapor-p: {} p:{}", state.liquid().pressure(Contributions::Total), state.vapor().pressure(Contributions::Total), p ); println!( "liquid-T: {} vapor-T: {}", state.liquid().temperature, state.vapor().temperature ); assert_relative_eq!( state.liquid().pressure(Contributions::Total), p, max_relative = 1e-8 ); assert_relative_eq!( state.vapor().pressure(Contributions::Total), state.liquid().pressure(Contributions::Total), max_relative = 1e-8 ); assert_relative_eq!( state.vapor().temperature, state.liquid().temperature, max_relative = 1e-10 ); } Ok(()) }