142 lines
4.1 KiB
Markdown
142 lines
4.1 KiB
Markdown
# Entropyk — Python Bindings
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High-performance Python bindings for the [Entropyk](../../README.md) thermodynamic simulation library, built with [PyO3](https://pyo3.rs/) and [Maturin](https://www.maturin.rs/).
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## Quickstart
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### Installation (Development)
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```bash
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# From the bindings/python directory:
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pip install maturin
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maturin develop --release
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# Verify installation:
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python -c "import entropyk; print(entropyk.Pressure(bar=1.0))"
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```
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### Basic Usage
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```python
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import entropyk
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# ── 1. Physical Types (type-safe units) ──
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p = entropyk.Pressure(bar=12.0)
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print(p.to_kpa()) # 1200.0 kPa
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print(p.to_pascals()) # 1200000.0 Pa
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t = entropyk.Temperature(celsius=45.0)
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print(t.to_kelvin()) # 318.15 K
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h = entropyk.Enthalpy(kj_per_kg=420.0)
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m = entropyk.MassFlow(kg_per_s=0.05)
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# Arithmetic
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dp = entropyk.Pressure(bar=10.0) - entropyk.Pressure(bar=3.0)
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# ── 2. Build a Refrigeration Cycle ──
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system = entropyk.System()
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comp = system.add_component(entropyk.Compressor(efficiency=0.85))
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cond = system.add_component(entropyk.Condenser(ua=5000.0))
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exv = system.add_component(entropyk.ExpansionValve())
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evap = system.add_component(entropyk.Evaporator(ua=3000.0))
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system.add_edge(comp, cond)
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system.add_edge(cond, exv)
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system.add_edge(exv, evap)
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system.add_edge(evap, comp)
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system.finalize()
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# ── 3. Solve ──
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config = entropyk.FallbackConfig(
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newton=entropyk.NewtonConfig(max_iterations=200, tolerance=1e-6),
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picard=entropyk.PicardConfig(max_iterations=500, relaxation=0.5),
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)
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try:
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result = config.solve(system)
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print(f"Converged in {result.iterations} iterations")
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print(f"State: {result.state_vector}")
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except entropyk.TimeoutError:
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print("Solver timed out")
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except entropyk.SolverError as e:
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print(f"Solver failed: {e}")
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```
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## API Reference
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### Physical Types
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| Type | Constructors | Conversions |
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|------|-------------|-------------|
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| `Pressure` | `pa=`, `bar=`, `kpa=`, `psi=` | `to_pascals()`, `to_bar()`, `to_kpa()`, `to_psi()` |
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| `Temperature` | `kelvin=`, `celsius=`, `fahrenheit=` | `to_kelvin()`, `to_celsius()`, `to_fahrenheit()` |
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| `Enthalpy` | `j_per_kg=`, `kj_per_kg=` | `to_j_per_kg()`, `to_kj_per_kg()` |
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| `MassFlow` | `kg_per_s=`, `g_per_s=` | `to_kg_per_s()`, `to_g_per_s()` |
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All types support: `__repr__`, `__str__`, `__float__`, `__eq__`, `__add__`, `__sub__`
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### Components
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| Component | Constructor | Description |
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|-----------|------------|-------------|
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| `Compressor` | `(m1..m10, speed_rpm, displacement, efficiency, fluid)` | AHRI 540 performance model |
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| `Condenser` | `(ua)` | Heat rejection coil |
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| `Evaporator` | `(ua)` | Heat absorption coil |
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| `Economizer` | `(ua)` | Internal heat exchanger |
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| `ExpansionValve` | `(fluid, opening)` | Isenthalpic throttling |
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| `Pipe` | `(length, diameter, fluid, density, viscosity, roughness)` | Darcy-Weisbach pressure drop |
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| `Pump` | `(pressure_rise_pa, efficiency)` | Liquid pump |
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| `Fan` | `(pressure_rise_pa, efficiency)` | Air fan |
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| `FlowSplitter` | `(n_outlets)` | Flow distribution |
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| `FlowMerger` | `(n_inlets)` | Flow recombination |
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| `FlowSource` | `(pressure_pa, temperature_k)` | Boundary source |
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| `FlowSink` | `()` | Boundary sink |
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### Solver
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```python
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# Newton-Raphson (fast convergence)
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config = entropyk.NewtonConfig(max_iterations=100, tolerance=1e-6, line_search=True)
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# Picard / Sequential Substitution (more robust)
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config = entropyk.PicardConfig(max_iterations=500, tolerance=1e-4, relaxation=0.5)
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# Fallback (Newton → Picard on divergence)
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config = entropyk.FallbackConfig(newton=newton_cfg, picard=picard_cfg)
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result = config.solve(system) # Returns ConvergedState
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```
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### Exceptions
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```
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EntropykError (base)
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├── SolverError
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│ ├── TimeoutError
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│ └── ControlSaturationError
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├── FluidError
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├── ComponentError
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├── TopologyError
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└── ValidationError
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```
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## Running Tests
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```bash
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cd bindings/python
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maturin develop
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pytest tests/ -v
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```
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## Examples
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- [`examples/simple_cycle.py`](examples/simple_cycle.py) — Build and solve a refrigeration cycle
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- [`examples/migration_from_tespy.py`](examples/migration_from_tespy.py) — TESPy → Entropyk migration guide
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