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| 1 | +use criterion::{criterion_group, criterion_main, Criterion}; |
| 2 | +use feos::pcsaft::{PcSaft, PcSaftParameters}; |
| 3 | +use feos_core::{ |
| 4 | + parameter::{IdentifierOption, Parameter}, |
| 5 | + Contributions, DensityInitialization, EquationOfState, PhaseEquilibrium, State, |
| 6 | +}; |
| 7 | +use ndarray::{Array, Array1}; |
| 8 | +use quantity::si::*; |
| 9 | +use std::sync::Arc; |
| 10 | + |
| 11 | +/// Evaluate NPT constructor |
| 12 | +fn npt<E: EquationOfState>( |
| 13 | + (eos, t, p, n, rho0): ( |
| 14 | + &Arc<E>, |
| 15 | + SINumber, |
| 16 | + SINumber, |
| 17 | + &SIArray1, |
| 18 | + DensityInitialization<SIUnit>, |
| 19 | + ), |
| 20 | +) { |
| 21 | + State::new_npt(eos, t, p, n, rho0).unwrap(); |
| 22 | +} |
| 23 | + |
| 24 | +/// Evaluate critical point constructor |
| 25 | +fn critical_point<E: EquationOfState>((eos, n): (&Arc<E>, Option<&SIArray1>)) { |
| 26 | + State::critical_point(eos, n, None, Default::default()).unwrap(); |
| 27 | +} |
| 28 | + |
| 29 | +/// VLE for pure substance for given temperature or pressure |
| 30 | +fn pure<E: EquationOfState>((eos, t_or_p): (&Arc<E>, SINumber)) { |
| 31 | + PhaseEquilibrium::pure(eos, t_or_p, None, Default::default()).unwrap(); |
| 32 | +} |
| 33 | + |
| 34 | +/// Evaluate temperature, pressure flash. |
| 35 | +fn tp_flash<E: EquationOfState>((eos, t, p, feed): (&Arc<E>, SINumber, SINumber, &SIArray1)) { |
| 36 | + PhaseEquilibrium::tp_flash(eos, t, p, feed, None, Default::default(), None).unwrap(); |
| 37 | +} |
| 38 | + |
| 39 | +fn bubble_point<E: EquationOfState>((eos, t, x): (&Arc<E>, SINumber, &Array1<f64>)) { |
| 40 | + PhaseEquilibrium::bubble_point( |
| 41 | + eos, |
| 42 | + t, |
| 43 | + x, |
| 44 | + None, |
| 45 | + None, |
| 46 | + (Default::default(), Default::default()), |
| 47 | + ) |
| 48 | + .unwrap(); |
| 49 | +} |
| 50 | + |
| 51 | +fn dew_point<E: EquationOfState>((eos, t, y): (&Arc<E>, SINumber, &Array1<f64>)) { |
| 52 | + PhaseEquilibrium::dew_point( |
| 53 | + eos, |
| 54 | + t, |
| 55 | + y, |
| 56 | + None, |
| 57 | + None, |
| 58 | + (Default::default(), Default::default()), |
| 59 | + ) |
| 60 | + .unwrap(); |
| 61 | +} |
| 62 | + |
| 63 | +fn bench_states<E: EquationOfState>(c: &mut Criterion, group_name: &str, eos: &Arc<E>) { |
| 64 | + let ncomponents = eos.components(); |
| 65 | + let x = Array::from_elem(ncomponents, 1.0 / ncomponents as f64); |
| 66 | + let n = &x * 100.0 * MOL; |
| 67 | + let crit = State::critical_point(&eos, Some(&n), None, Default::default()).unwrap(); |
| 68 | + let vle = if ncomponents == 1 { |
| 69 | + PhaseEquilibrium::pure(&eos, crit.temperature * 0.95, None, Default::default()).unwrap() |
| 70 | + } else { |
| 71 | + PhaseEquilibrium::tp_flash( |
| 72 | + &eos, |
| 73 | + crit.temperature, |
| 74 | + crit.pressure(Contributions::Total) * 0.95, |
| 75 | + &crit.moles, |
| 76 | + None, |
| 77 | + Default::default(), |
| 78 | + None, |
| 79 | + ) |
| 80 | + .unwrap() |
| 81 | + }; |
| 82 | + |
| 83 | + let mut group = c.benchmark_group(group_name); |
| 84 | + group.bench_function("new_npt_liquid", |b| { |
| 85 | + b.iter(|| { |
| 86 | + npt(( |
| 87 | + &eos, |
| 88 | + vle.liquid().temperature, |
| 89 | + vle.liquid().pressure(Contributions::Total) * 1.01, |
| 90 | + &n, |
| 91 | + DensityInitialization::Liquid, |
| 92 | + )) |
| 93 | + }) |
| 94 | + }); |
| 95 | + group.bench_function("new_npt_vapor", |b| { |
| 96 | + b.iter(|| { |
| 97 | + npt(( |
| 98 | + &eos, |
| 99 | + vle.vapor().temperature, |
| 100 | + vle.vapor().pressure(Contributions::Total) * 0.99, |
| 101 | + &n, |
| 102 | + DensityInitialization::Vapor, |
| 103 | + )) |
| 104 | + }) |
| 105 | + }); |
| 106 | + group.bench_function("critical_point", |b| { |
| 107 | + b.iter(|| critical_point((&eos, Some(&n)))) |
| 108 | + }); |
| 109 | + if ncomponents != 1 { |
| 110 | + group.bench_function("tp_flash", |b| { |
| 111 | + b.iter(|| { |
| 112 | + tp_flash(( |
| 113 | + &eos, |
| 114 | + crit.temperature, |
| 115 | + crit.pressure(Contributions::Total) * 0.99, |
| 116 | + &n, |
| 117 | + )) |
| 118 | + }) |
| 119 | + }); |
| 120 | + |
| 121 | + group.bench_function("bubble_point", |b| { |
| 122 | + b.iter(|| bubble_point((&eos, vle.liquid().temperature, &vle.liquid().molefracs))) |
| 123 | + }); |
| 124 | + |
| 125 | + group.bench_function("dew_point", |b| { |
| 126 | + b.iter(|| dew_point((&eos, vle.vapor().temperature, &vle.vapor().molefracs))) |
| 127 | + }); |
| 128 | + } else { |
| 129 | + group.bench_function("pure_t", |b| { |
| 130 | + b.iter(|| pure((&eos, vle.vapor().temperature))) |
| 131 | + }); |
| 132 | + group.bench_function("pure_p", |b| { |
| 133 | + b.iter(|| pure((&eos, vle.vapor().pressure(Contributions::Total)))) |
| 134 | + }); |
| 135 | + } |
| 136 | +} |
| 137 | + |
| 138 | +fn pcsaft(c: &mut Criterion) { |
| 139 | + let parameters = PcSaftParameters::from_json( |
| 140 | + vec!["methane"], |
| 141 | + "./parameters/pcsaft/gross2001.json", |
| 142 | + None, |
| 143 | + IdentifierOption::Name, |
| 144 | + ) |
| 145 | + .unwrap(); |
| 146 | + let eos = Arc::new(PcSaft::new(Arc::new(parameters))); |
| 147 | + bench_states(c, "state_creation_pcsaft_methane", &eos); |
| 148 | + |
| 149 | + let parameters = PcSaftParameters::from_json( |
| 150 | + vec!["methane", "ethane", "propane"], |
| 151 | + "./parameters/pcsaft/gross2001.json", |
| 152 | + None, |
| 153 | + IdentifierOption::Name, |
| 154 | + ) |
| 155 | + .unwrap(); |
| 156 | + let eos = Arc::new(PcSaft::new(Arc::new(parameters))); |
| 157 | + bench_states(c, "state_creation_pcsaft_methane_ethane", &eos); |
| 158 | + |
| 159 | + let parameters = PcSaftParameters::from_json( |
| 160 | + vec!["methane", "ethane", "propane"], |
| 161 | + "./parameters/pcsaft/gross2001.json", |
| 162 | + None, |
| 163 | + IdentifierOption::Name, |
| 164 | + ) |
| 165 | + .unwrap(); |
| 166 | + let eos = Arc::new(PcSaft::new(Arc::new(parameters))); |
| 167 | + bench_states(c, "state_creation_pcsaft_methane_ethane_propane", &eos); |
| 168 | +} |
| 169 | + |
| 170 | +criterion_group!(bench, pcsaft); |
| 171 | +criterion_main!(bench); |
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