/// Test d'intégration : boucle réfrigération simple R134a en Rust natif.
///
/// Ce test valide que le solveur Newton converge sur un cycle 4 composants
/// en utilisant des mock components algébriques linéaires dont les équations
/// sont mathématiquement cohérentes (ferment la boucle).

use entropyk_components::{
    Component, ComponentError, ConnectedPort, JacobianBuilder, ResidualVector, StateSlice,
};
use entropyk_core::{Enthalpy, MassFlow, Pressure};
use entropyk_solver::{
    solver::{NewtonConfig, Solver},
    system::System,
};
use entropyk_components::port::{Connected, FluidId, Port};

// Type alias: Port<Connected> ≡ ConnectedPort
type CP = Port<Connected>;

// ─── Mock compresseur ─────────────────────────────────────────────────────────
// r[0] = p_disc - (p_suc + 1 MPa)
// r[1] = h_disc - (h_suc + 75 kJ/kg)
struct MockCompressor { port_suc: CP, port_disc: CP }
impl Component for MockCompressor {
    fn compute_residuals(&self, _s: &StateSlice, r: &mut ResidualVector) -> Result<(), ComponentError> {
        r[0] = self.port_disc.pressure().to_pascals() - (self.port_suc.pressure().to_pascals() + 1_000_000.0);
        r[1] = self.port_disc.enthalpy().to_joules_per_kg() - (self.port_suc.enthalpy().to_joules_per_kg() + 75_000.0);
        Ok(())
    }
    fn jacobian_entries(&self, _s: &StateSlice, _j: &mut JacobianBuilder) -> Result<(), ComponentError> { Ok(()) }
    fn n_equations(&self) -> usize { 2 }
    fn get_ports(&self) -> &[ConnectedPort] { &[] }
    fn port_mass_flows(&self, _: &StateSlice) -> Result<Vec<MassFlow>, ComponentError> {
        Ok(vec![MassFlow::from_kg_per_s(0.05), MassFlow::from_kg_per_s(-0.05)])
    }
}

// ─── Mock condenseur ──────────────────────────────────────────────────────────
// r[0] = p_out - p_in
// r[1] = h_out - (h_in - 225 kJ/kg)
struct MockCondenser { port_in: CP, port_out: CP }
impl Component for MockCondenser {
    fn compute_residuals(&self, _s: &StateSlice, r: &mut ResidualVector) -> Result<(), ComponentError> {
        r[0] = self.port_out.pressure().to_pascals() - self.port_in.pressure().to_pascals();
        r[1] = self.port_out.enthalpy().to_joules_per_kg() - (self.port_in.enthalpy().to_joules_per_kg() - 225_000.0);
        Ok(())
    }
    fn jacobian_entries(&self, _s: &StateSlice, _j: &mut JacobianBuilder) -> Result<(), ComponentError> { Ok(()) }
    fn n_equations(&self) -> usize { 2 }
    fn get_ports(&self) -> &[ConnectedPort] { &[] }
    fn port_mass_flows(&self, _: &StateSlice) -> Result<Vec<MassFlow>, ComponentError> {
        Ok(vec![MassFlow::from_kg_per_s(0.05), MassFlow::from_kg_per_s(-0.05)])
    }
}

// ─── Mock détendeur ───────────────────────────────────────────────────────────
// r[0] = p_out - (p_in - 1 MPa)
// r[1] = h_out - h_in
struct MockValve { port_in: CP, port_out: CP }
impl Component for MockValve {
    fn compute_residuals(&self, _s: &StateSlice, r: &mut ResidualVector) -> Result<(), ComponentError> {
        r[0] = self.port_out.pressure().to_pascals() - (self.port_in.pressure().to_pascals() - 1_000_000.0);
        r[1] = self.port_out.enthalpy().to_joules_per_kg() - self.port_in.enthalpy().to_joules_per_kg();
        Ok(())
    }
    fn jacobian_entries(&self, _s: &StateSlice, _j: &mut JacobianBuilder) -> Result<(), ComponentError> { Ok(()) }
    fn n_equations(&self) -> usize { 2 }
    fn get_ports(&self) -> &[ConnectedPort] { &[] }
    fn port_mass_flows(&self, _: &StateSlice) -> Result<Vec<MassFlow>, ComponentError> {
        Ok(vec![MassFlow::from_kg_per_s(0.05), MassFlow::from_kg_per_s(-0.05)])
    }
}

// ─── Mock évaporateur ─────────────────────────────────────────────────────────
// r[0] = p_out - p_in
// r[1] = h_out - (h_in + 150 kJ/kg)
struct MockEvaporator { port_in: CP, port_out: CP }
impl Component for MockEvaporator {
    fn compute_residuals(&self, _s: &StateSlice, r: &mut ResidualVector) -> Result<(), ComponentError> {
        r[0] = self.port_out.pressure().to_pascals() - self.port_in.pressure().to_pascals();
        r[1] = self.port_out.enthalpy().to_joules_per_kg() - (self.port_in.enthalpy().to_joules_per_kg() + 150_000.0);
        Ok(())
    }
    fn jacobian_entries(&self, _s: &StateSlice, _j: &mut JacobianBuilder) -> Result<(), ComponentError> { Ok(()) }
    fn n_equations(&self) -> usize { 2 }
    fn get_ports(&self) -> &[ConnectedPort] { &[] }
    fn port_mass_flows(&self, _: &StateSlice) -> Result<Vec<MassFlow>, ComponentError> {
        Ok(vec![MassFlow::from_kg_per_s(0.05), MassFlow::from_kg_per_s(-0.05)])
    }
}

// ─── Helpers ──────────────────────────────────────────────────────────────────
fn port(p_pa: f64, h_j_kg: f64) -> CP {
    let (connected, _) = Port::new(
        FluidId::new("R134a"),
        Pressure::from_pascals(p_pa),
        Enthalpy::from_joules_per_kg(h_j_kg),
    ).connect(Port::new(
        FluidId::new("R134a"),
        Pressure::from_pascals(p_pa),
        Enthalpy::from_joules_per_kg(h_j_kg),
    )).unwrap();
    connected
}

// ─── Test ─────────────────────────────────────────────────────────────────────
#[test]
fn test_simple_refrigeration_loop_rust() {
    //   Les équations :
    //     Comp    : p0 = p3 + 1 MPa  ;  h0 = h3 + 75 kJ/kg
    //     Cond    : p1 = p0          ;  h1 = h0 - 225 kJ/kg
    //     Valve   : p2 = p1 - 1 MPa  ;  h2 = h1
    //     Evap    : p3 = p2          ;  h3 = h2 + 150 kJ/kg
    //
    //   Bilan enthalpique en boucle : 75 - 225 + 150 = 0 → fermé ✓
    //   Bilan pressionnel en boucle : +1 - 0 - 1 - 0 = 0 → fermé ✓
    //
    //   Solution analytique (8 inconnues, 8 équations → infinité de solutions
    //   dépendant du point de référence, mais le solveur en trouve une) :
    //   En posant h3 = 410 kJ/kg, p3 = 350 kPa :
    //     h0 = 485, p0 = 1.35 MPa
    //     h1 = 260, p1 = 1.35 MPa
    //     h2 = 260, p2 = 350 kPa
    //     h3 = 410, p3 = 350 kPa

    let p_lp = 350_000.0_f64;    // Pa
    let p_hp = 1_350_000.0_f64;  // Pa = p_lp + 1 MPa

    // Les 4 bords (edge) du cycle :
    //   edge0 : comp → cond
    //   edge1 : cond → valve
    //   edge2 : valve → evap
    //   edge3 : evap → comp
    let comp = Box::new(MockCompressor {
        port_suc:  port(p_lp, 410_000.0),
        port_disc: port(p_hp, 485_000.0),
    });
    let cond = Box::new(MockCondenser {
        port_in:  port(p_hp, 485_000.0),
        port_out: port(p_hp, 260_000.0),
    });
    let valv = Box::new(MockValve {
        port_in:  port(p_hp, 260_000.0),
        port_out: port(p_lp, 260_000.0),
    });
    let evap = Box::new(MockEvaporator {
        port_in:  port(p_lp, 260_000.0),
        port_out: port(p_lp, 410_000.0),
    });

    let mut system = System::new();
    let n_comp = system.add_component(comp);
    let n_cond = system.add_component(cond);
    let n_valv = system.add_component(valv);
    let n_evap = system.add_component(evap);

    system.add_edge(n_comp, n_cond).unwrap();
    system.add_edge(n_cond, n_valv).unwrap();
    system.add_edge(n_valv, n_evap).unwrap();
    system.add_edge(n_evap, n_comp).unwrap();

    system.finalize().unwrap();

    let n_vars = system.full_state_vector_len();
    println!("Variables d'état : {}", n_vars);

    // État initial = solution analytique exacte → résidus = 0 → converge 1 itération
    let initial_state = vec![
        p_hp, 485_000.0,  // edge0 comp→cond
        p_hp, 260_000.0,  // edge1 cond→valve
        p_lp, 260_000.0,  // edge2 valve→evap
        p_lp, 410_000.0,  // edge3 evap→comp
    ];

    let mut config = NewtonConfig {
        max_iterations: 50,
        tolerance: 1e-6,
        line_search: false,
        use_numerical_jacobian: true, // analytique vide → numérique
        initial_state: Some(initial_state),
        ..NewtonConfig::default()
    };

    let t0 = std::time::Instant::now();
    let result = config.solve(&mut system);
    let elapsed = t0.elapsed();

    println!("Durée : {:?}", elapsed);

    match &result {
        Ok(converged) => {
            println!("✅ Convergé en {} itérations ({:?})", converged.iterations, elapsed);
            let sv = &converged.state;
            println!("  comp→cond  : P={:.2} bar, h={:.1} kJ/kg", sv[0]/1e5, sv[1]/1e3);
            println!("  cond→valve : P={:.2} bar, h={:.1} kJ/kg", sv[2]/1e5, sv[3]/1e3);
            println!("  valve→evap : P={:.2} bar, h={:.1} kJ/kg", sv[4]/1e5, sv[5]/1e3);
            println!("  evap→comp  : P={:.2} bar, h={:.1} kJ/kg", sv[6]/1e5, sv[7]/1e3);
        }
        Err(e) => {
            panic!("❌ Solveur échoué : {:?}", e);
        }
    }

    assert!(elapsed.as_millis() < 5000, "Doit converger en < 5 secondes");
    assert!(result.is_ok(), "Solveur doit converger");
}