1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60 61 62 63 64 65 66 67 68 69 70 71 72 73 74 75 76 77 78 79 80 81 82 83 84 85 86 87 88 89 90 91 92 93 94 95 96 97 98 99 100 101 102 103 104 105 106 107 108 109 110 111 112 113 114 115 116 117 118 119 120 121 122 123 124 125 126 127 128 129 130 131 132 133 134 135 136 137 138 139 140 141 142 143 144 145 146 147 148 149 150 151 152 153 154 155 156 157 158 159 160 161 162 163 164 165 166 167 168 169 170 171 172 173 174 175 176 177 178 179 180 181 182 183 184 185 186 187 188 189 190 191 192 193 194 195 196 197 198 199 200 201 202 203 204 205 206 207 208 209 210 211 212 213 214 215 216 217 218 219 220 221 222 223 224 225 226 227 228 229 230 231 232 233 234 235 236 237 238 239 240 241 242 243 244 245 246 247 248 249 250 251 252 253 254 255 256 257 258 259 260 261 262 263 264 265 266 267 268 269 270 271 272 273 274 275 276 277 278 279 280 281 282 283 284 285 286 287 288 289 290 291 292 293 294 295 296 297 298 299 300 301 302 303 304 305 306 307 308 309 310 311 312 313 314 315 316 317 318 319 320 321 322 323 324 325 326 327 328 329 330 331 332 333 334 335 336 337 338 339 340 341 342 343 344 345 346 347 348 349 350 351 352 353 354 355 356 357 358 359 360 361 362 363 364 365 366 367 368 369 370 371 372 373 374 375 376 377 378 379 380 381 382 383 384 385 386 387 388 389 390 391 392 393 394 395 396 397 398 399 400 401 402 403 404 405 406 407 408 409 410 411 412 413 414 415 416 417 418 419 420 421 422 423 424 425 426 427 428 429 430 431 432 433 434 435 436 437 438 439 440 441 442 443 444 445 446 447 448 449 450 451 452 453 454 455 456 457 458 459 460 461 462 463 464 465 466 467 468 469 470 471 472 473 474 475 476 477 478 479 480 481 482 483 484 485 486 487 488 489 490 491 492 493 494 495 496 497 498 499 500 501 502 503 504 505 506 507 508 509 510 511 512 513 514 515 516 517 518 519 520 521 522 523 524 525 526 527 528 529 530 531 532 533 534 535 536 537 538 539 540 541 542 543 544 545 546 547 548 549 550 551 552 553 554 555 556 557 558 559 560 561 562 563 564 565 566 567 568 569 570 571 572 573 574 575 576 577 578 579 580 581 582 583 584 585 586 587 588 589 590 591 592 593 594 595 596 597 598 599 600 601 602 603 604 605 606 607 608 609 610 611 612 613 614 615 616 617 618 619 620 621 622 623 624 625 626 627 628 629 630 631 632 633 634 635 636 637 638 639 640 641 642 643 644 645 646 647 648 649 650 651 652 653 654 655 656 657 658 659 660 661 662 663 664 665 666 667 668 669 670 671 672 673 674 675 676 677 678 679 680 681 682 683 684 685 686 687
#![allow(warnings)]
//#![warn(missing_docs)]
/*!
# IF97
IF97 is the high-speed package of IAPWS-IF97 in Rust. It is suitable for computation-intensive calculations,such as heat cycle calculations, simulations of non-stationary processes, real-time process monitoring and optimizations.
Through the high-speed package, the results of the IAPWS-IF97 are accurately produced at about 5-15x speed-up compared to the `powi()` of the Rust standard library when computing the basic equations of Region 1,2,3.
* The comparison results of the computing-time are obtained using the [criterion.rs](https://bheisler.github.io/criterion.rs/book/index.html).
**The Fast Algorithm**
1. The shortest addition chain computes integer powers of a number.([the paper in chinese](https://github.com/thermalogic/SEUIF97/blob/master/doc/水和水蒸汽热力性质IAPWS-IF97公式的通用计算模型.pdf))
2. The recursive algorithm computes the polynomial values of the base variable and its derivatives
In IF97, [36 thermodynamic, transport and further properties](#properties) can be calculated.
The following input pairs are implemented:
```txt
(p,t) (p,h) (p,s) (p,v)
(t,h) (t,s) (t,v)
(p,x) (t,x) (h,x) (s,x)
(h,s)
```
## Usage
The type of functions are provided in the if97 package:
```rust
fn(f64,f64,i32) -> f64;
``````
* the first,second input parameters: the input propertry pairs
* the third input parameter: the property ID of the calculated property - [o_id](#properties)
* the return: the calculated property value of o_id
```rust
pt(p:f64,t:f64,o_id:i32)->f64
ph(p:f64,h:f64,o_id:i32)->f64
ps(p:f64,s:f64,o_id:i32)->f64
pv(p:f64,v:f64,o_id:i32)->f64
th(t:f64,h:f64,o_id:i32)->f64
ts(t:f64,s:f64,o_id:i32)->f64
tv(t:f64,v:f64,o_id:i32)->f64
px(p:f64,x:f64,o_id:i32)->f64
tx(p:f64,x:f64,o_id:i32)->f64
hx(h:f64,x:f64,o_id:i32)->f64
sx(s:f64,x:f64,o_id:i32)->f64
hs(h:f64,s:f64,o_id:i32)->f64
```
**Example**
```rust
use if97::*;
fn main() {
let p:f64 = 3.0;
let t:f64= 300.0-273.15;
let h=pt(p,t,OH);
let s=pt(p,t,OS);
let v=pt(p,t,OV);
println!("p={p:.6} t={t:.6} h={t:.6} s={s:.6} v={v:.6}");
}
```
## Properties
| Propertry | Unit | Symbol | o_id | o_id(i32)|
| ------------------------------------- | :---------: |:------:|------:|:--------:|
| Pressure | MPa | p | OP | 0 |
| Temperature | °C | t | OT | 1 |
| Density | kg/m³ | ρ | OD | 2 |
| Specific Volume | m³/kg | v | OV | 3 |
| Specific enthalpy | kJ/kg | h | OH | 4 |
| Specific entropy | kJ/(kg·K) | s | OS | 5 |
| Specific exergy | kJ/kg | e | OE | 6 |
| Specific internal energy | kJ/kg | u | OU | 7 |
| Specific isobaric heat capacity | kJ/(kg·K) | cp | OCP | 8 |
| Specific isochoric heat capacity | kJ/(kg·K) | cv | OCV | 9 |
| Speed of sound | m/s | w | OW | 10 |
| Isentropic exponent | | k | OKS | 11 |
| Specific Helmholtz free energy | kJ/kg | f | OF | 12 |
| Specific Gibbs free energy | kJ/kg | g | OG | 13 |
| Compressibility factor | | z | OZ | 14 |
| Steam quality | | x | OX | 15 |
| Region | | r | OR | 16 |
| Isobari cubic expansion coefficient | 1/K | ɑv | OEC | 17 |
| Isothermal compressibility | 1/MPa | kT | OKT | 18 |
| Partial derivative (∂V/∂T)p | m³/(kg·K) |(∂V/∂T)p| ODVDT | 19 |
| Partial derivative (∂V/∂p)T | m³/(kg·MPa) |(∂v/∂p)t| ODVDP | 20 |
| Partial derivative (∂P/∂T)v | MPa/K |(∂p/∂t)v| ODPDT | 21 |
| Isothermal throttling coefficient | kJ/(kg·MPa) | δt | OIJTC | 22 |
| Joule-Thomson coefficient | K/MPa | μ | OJTC | 23 |
| Dynamic viscosity | Pa·s | η | ODV | 24 |
| Kinematic viscosity | m²/s | ν | OKV | 25 |
| Thermal conductivity | W/(m.K) | λ | OTC | 26 |
| Thermal diffusivity | m²/s | a | OTD | 27 |
| Prandtl number | | Pr | OPR | 28 |
| Surface tension | N/m | σ | OST | 29 |
| Static Dielectric Constant | | ε | OSDC | 30 |
| Isochoric pressure coefficient | 1/K | β | OPC | 31 |
| Isothermal stress coefficient | kg/m³ | βp | OBETAP| 32 |
| Fugacity coefficient | | fi | OFI | 33 |
| Fugacity | MPa | f* | OFU | 34 |
| Relative pressure coefficient | 1/K | αp | OAFLAP| 35|
*/
mod algo;
mod common;
mod r1;
mod r2;
mod r3;
mod r4;
mod r5;
pub use common::propertry_id::*;
use common::*;
use r1::*;
use r2::*;
use r3::*;
use r4::*;
use r5::*;
/// pt(p,t,o_id) - the propertry of o_id(thermodynamic,transport,etc)
///
/// # Examples
///
/// ```
/// use if97::*;
///
/// let p:f64 = 3.0;
/// let t:f64= 300.0-273.15;
/// let h=pt(p,t,OH);
/// let s=pt(p,t,OS);
/// let v=pt(p,t,OV);
/// println!("p={p:.6} t={t:.6} h={h:.6} s={s:.6} v={v:.6}");
/// ```
///
pub fn pt(p: f64, t: f64, o_id: i32) -> f64 {
match o_id {
OP => return p,
OT => return t,
OST => return surface_tension(t + K),
ODV | OKV | OTC | OSDC => {
let d: f64 = pt_thermal(p, t, OD);
let mut value: f64 = 0.0;
if o_id == ODV || o_id == OKV {
value = viscosity(d, t + 273.15);
if o_id == OKV {
value /= d; // Kinematic viscosity=Dynamic viscosity/density
}
} else {
if o_id == OTC {
value = thcond(d, t + 273.15)
} else {
if o_id == OSDC {
value = static_dielectric(d, t + 273.15);
};
}
};
value
}
OPR | OTD => {
let d: f64 = pt_thermal(p, t, OD);
let cp: f64 = pt_thermal(p, t, OCP);
let tc: f64 = thcond(d, t + 273.15);
let mut value: f64 = 0.0;
if o_id == OTD {
value = thermal_diffusivity(tc, cp, d);
} else if o_id == OPR {
let dv: f64 = viscosity(d, t + 273.15);
value = prandtl_number(dv, cp, tc);
}
value
}
_ => pt_thermal(p, t, o_id),
}
}
/// ph(p,h,o_id) - the propertry of o_id (thermodynamic,transport,etc)
///
/// # Examples
///
/// ```
/// use if97::*;
///
/// let p:f64 = 3.0;
/// let h:f64= 0.115331273e+3;
/// let t=ph(p,h,OT);
/// println!("p={p:.6} h={h:.6} t={t:.6}");
/// ```
///
pub fn ph(p: f64, h: f64, o_id: i32) -> f64 {
match o_id {
OP => return p,
OH => return h,
OST => {
let t: f64 = ph_thermal(p, h, OT);
return surface_tension(t + K);
}
ODV | OKV | OTC | OSDC => {
let d: f64 = ph_thermal(p, h, OD);
let t: f64 = ph_thermal(p, h, OT);
let mut value: f64 = 0.0;
if o_id == ODV || o_id == OKV {
value = viscosity(d, t + 273.15);
if o_id == OKV {
value /= d; // Kinematic viscosity=Dynamic viscosity/density
}
} else {
if o_id == OTC {
value = thcond(d, t + 273.15)
} else {
if o_id == OSDC {
value = static_dielectric(d, t + 273.15);
};
}
};
value
}
OPR | OTD => {
let d: f64 = ph_thermal(p, h, OD);
let t: f64 = ph_thermal(p, h, OT);
let cp: f64 = ph_thermal(p, h, OCP);
let tc: f64 = thcond(d, t + 273.15);
let mut value: f64 = 0.0;
if o_id == OTD {
value = thermal_diffusivity(tc, cp, d);
} else if o_id == OPR {
let dv: f64 = viscosity(d, t + 273.15);
value = prandtl_number(dv, cp, tc);
}
value
}
_ => ph_thermal(p, h, o_id),
}
}
/// ps(p,s,o_id) - the propertry of o_id (thermodynamic,transport,etc)
///
/// # Examples
///
///```
/// use if97::*;
///
/// let p:f64= 3.0;
/// let s:f64= 0.392294792;
/// let t=ps(p,s,OT);
/// println!("p={p:.6} s={s:.6} t={t:.6}");
/// ```
pub fn ps(p: f64, s: f64, o_id: i32) -> f64 {
match o_id {
OP => return p,
OS => return s,
OST => {
let t: f64 = ps_thermal(p, s, OT);
return surface_tension(t + K);
}
ODV | OKV | OTC | OSDC => {
let d: f64 = ps_thermal(p, s, OD);
let t: f64 = ps_thermal(p, s, OT);
let mut value: f64 = 0.0;
if o_id == ODV || o_id == OKV {
value = viscosity(d, t + 273.15);
if o_id == OKV {
value /= d; // Kinematic viscosity=Dynamic viscosity/density
}
} else {
if o_id == OTC {
value = thcond(d, t + 273.15)
} else {
if o_id == OSDC {
value = static_dielectric(d, t + 273.15);
};
};
};
value
}
OPR | OTD => {
let d: f64 = ps_thermal(p, s, OD);
let t: f64 = ps_thermal(p, s, OT);
let cp: f64 = ps_thermal(p, s, OCP);
let tc: f64 = thcond(d, t + 273.15);
let mut value: f64 = 0.0;
if o_id == OTD {
value = thermal_diffusivity(tc, cp, d);
} else if o_id == OPR {
let dv: f64 = viscosity(d, t + 273.15);
value = prandtl_number(dv, cp, tc);
}
value
}
_ => ps_thermal(p, s, o_id),
}
}
/// hs(h,s,o_id) - the propertry of o_id (thermodynamic,transport,etc)
///
/// # Examples
///
///```
/// use if97::*;
///
/// let h:f64= 0.115331273e+3;;
/// let s:f64= 0.392294792;
/// let p=hs(h,s,OP);
/// let t=hs(h,s,OT);
/// println!("h={h:.6} s={s:.6} p={p:.6} t={t:.6}");
/// ```
///
pub fn hs(h: f64, s: f64, o_id: i32) -> f64 {
match o_id {
OH => return h,
OS => return s,
OST => {
let t: f64 = hs_thermal(h, s, OT);
return surface_tension(t + K);
}
ODV | OKV | OTC | OSDC => {
let d: f64 = hs_thermal(h, s, OD);
let t: f64 = hs_thermal(h, s, OT);
let mut value: f64 = 0.0;
if o_id == ODV || o_id == OKV {
value = viscosity(d, t + 273.15);
if o_id == OKV {
value /= d; // Kinematic viscosity=Dynamic viscosity/density
}
} else {
if o_id == OTC {
value = thcond(d, t + 273.15)
} else {
if o_id == OSDC {
value = static_dielectric(d, t + 273.15);
};
};
};
value
}
OPR | OTD => {
let d: f64 = hs_thermal(h, s, OD);
let t: f64 = hs_thermal(h, s, OT);
let cp: f64 = hs_thermal(h, s, OCP);
let tc: f64 = thcond(d, t + 273.15);
let mut value: f64 = 0.0;
if o_id == OTD {
value = thermal_diffusivity(tc, cp, d);
} else if o_id == OPR {
let dv: f64 = viscosity(d, t + 273.15);
value = prandtl_number(dv, cp, tc);
}
value
}
_ => hs_thermal(h, s, o_id),
}
}
/// px(p,x,o_id) - the propertry of o_id (thermodynamic)
///
/// # Examples
///
///```
/// use if97::*;
///
/// let p: f64 = 0.1;
/// let x: f64 = 0.0; // x= 0.0 saturation water ,x=1.0 saturation steam
/// let t: f64 = px(p, x, OT);
/// let h: f64 = px(p, x, OH);
/// println!("px: p={p:.6} x={x:.6} t={t:.6} h={h:.6}");
///```
pub fn px(p: f64, x: f64, o_id: i32) -> f64 {
if p > P_MAX4 || p < P_MIN4 || x > 1.0 || x < 0.0 {
return INVALID_VALUE as f64;
}
match o_id {
OP => return p,
OX => return x,
OT => return px_reg4(p, x, o_id) - 273.15,
_ => return px_reg4(p, x, o_id),
}
}
/// tx(t,x,o_id) - the propertry of o_id (thermodynamic)
///
/// # Examples
///
///```
/// use if97::*;
///
/// let t: f64 =372.755919-273.15;
/// let x: f64 = 0.0; // x= 0.0 saturation water ,x=1.0 saturation steam
/// let p: f64 = tx(t, x, OP);
/// let h: f64 = tx(t, x, OH);
/// println!("tx: p={p:.6} x={x:.6} t={t:.6} h={h:.6}");
/// ```
///
pub fn tx(t: f64, x: f64, o_id: i32) -> f64 {
let T: f64 = t + 273.15;
if T > T_MAX4 || T < T_MIN4 || x > 1.0 || x < 0.0 {
return INVALID_VALUE as f64;
}
Tx_reg4(T, x, o_id)
}
/// pv(p,v,o_id) - the propertry of o_id (thermodynamic,transport,etc)
///
/// # Examples
///
///```
/// use if97::*;
///
/// let p:f64= 3.0;
/// let v:f64= 0.100215168e-2;
/// let t=pv(p,v,OT);
/// println!("p={p:.6} v={v:.6} t={t:.6}");
/// ```
pub fn pv(p: f64, v: f64, o_id: i32) -> f64 {
match o_id {
OP => return p,
OV => return v,
OST => {
let t: f64 = pv_thermal(p, v, OT);
return surface_tension(t + K);
}
ODV | OKV | OTC | OSDC => {
let d: f64 = 1.0 / v;
let t: f64 = pv_thermal(p, v, OT);
let mut value: f64 = 0.0;
if o_id == ODV || o_id == OKV {
value = viscosity(d, t + 273.15);
if o_id == OKV {
value /= d; // Kinematic viscosity=Dynamic viscosity/density
}
} else {
if o_id == OTC {
value = thcond(d, t + 273.15)
} else {
if o_id == OSDC {
value = static_dielectric(d, t + 273.15);
};
};
};
value
}
OPR | OTD => {
let d: f64 = 1.0 / v;
let t: f64 = pv_thermal(p, v, OT);
let cp: f64 = pv_thermal(p, v, OCP);
let tc: f64 = thcond(d, t + 273.15);
let mut value: f64 = 0.0;
if o_id == OTD {
value = thermal_diffusivity(tc, cp, d);
} else if o_id == OPR {
let dv: f64 = viscosity(d, t + 273.15);
value = prandtl_number(dv, cp, tc);
}
value
}
_ => pv_thermal(p, v, o_id),
}
}
/// tv(t,v,o_id) - the propertry of o_id (thermodynamic,transport,etc)
///
/// # Examples
///
///```
/// use if97::*;
///
/// let t:f64=300.0-273.15;
/// let v:f64= 0.100215168e-2;
/// let p=tv(t,v,OP);
/// println!("t={p:.6} v={v:.6} p={p:.6}");
/// ```
pub fn tv(t: f64, v: f64, o_id: i32) -> f64 {
match o_id {
OT => return t,
OV => return v,
OST => return surface_tension(t + K),
ODV | OKV | OTC | OSDC => {
let d: f64 = 1.0 / v;
let mut value: f64 = 0.0;
if o_id == ODV || o_id == OKV {
value = viscosity(d, t + 273.15);
if o_id == OKV {
value /= d; // Kinematic viscosity=Dynamic viscosity/density
}
} else {
if o_id == OTC {
value = thcond(d, t + 273.15)
} else {
if o_id == OSDC {
value = static_dielectric(d, t + 273.15);
};
};
};
value
}
OPR | OTD => {
let d: f64 = 1.0 / v;
let cp: f64 = tv_thermal(t, v, OCP);
let tc: f64 = thcond(d, t + 273.15);
let mut value: f64 = 0.0;
if o_id == OTD {
value = thermal_diffusivity(tc, cp, d);
} else if o_id == OPR {
let dv: f64 = viscosity(d, t + 273.15);
value = prandtl_number(dv, cp, tc);
}
value
}
_ => tv_thermal(t, v, o_id),
}
}
/// th(t,h,o_id) - the propertry of o_id(thermodynamic,transport,etc)
///
/// # Examples
///
///```
/// use if97::*;
///
/// let t:f64=300.0-273.15;
/// let h:f64=0.115331273e+3;
/// let p=th(t,h,OP);
/// println!("t={p:.6} h={h:.6} p={p:.6}");
/// ```
pub fn th(t: f64, h: f64, o_id: i32) -> f64 {
match o_id {
OT => return t,
OH => return h,
OST => return surface_tension(t + K),
ODV | OKV | OTC | OSDC => {
let d: f64 = th_thermal(t, h, OD);
let mut value: f64 = 0.0;
if o_id == ODV || o_id == OKV {
value = viscosity(d, t + 273.15);
if o_id == OKV {
value /= d; // Kinematic viscosity=Dynamic viscosity/density
}
} else {
if o_id == OTC {
value = thcond(d, t + 273.15)
} else {
if o_id == OSDC {
value = static_dielectric(d, t + 273.15);
};
};
};
value
}
OPR | OTD => {
let d: f64 = th_thermal(t, h, OD);
let cp: f64 = th_thermal(t, h, OCP);
let tc: f64 = thcond(d, t + 273.15);
let mut value: f64 = 0.0;
if o_id == OTD {
value = thermal_diffusivity(tc, cp, d);
} else if o_id == OPR {
let dv: f64 = viscosity(d, t + 273.15);
value = prandtl_number(dv, cp, tc);
}
value
}
_ => th_thermal(t, h, o_id),
}
}
/// ts(t,s,o_id) - the propertry of o_id (thermodynamic,transport,etc)
///
/// # Examples
///
///```
/// use if97::*;
///
/// let t:f64=300.0-273.15;
/// let s:f64=0.392294792;
/// let p=ts(t,s,OP);
/// println!("t={p:.6} s={s:.6} p={p:.6}");
/// ```
pub fn ts(t: f64, s: f64, o_id: i32) -> f64 {
match o_id {
OT => return t,
OS => return s,
OST => return surface_tension(t + K),
ODV | OKV | OTC | OSDC => {
let d: f64 = ts_thermal(t, s, OD);
let mut value: f64 = 0.0;
if o_id == ODV || o_id == OKV {
value = viscosity(d, t + 273.15);
if o_id == OKV {
value /= d; // Kinematic viscosity=Dynamic viscosity/density
}
} else {
if o_id == OTC {
value = thcond(d, t + 273.15)
} else {
if o_id == OSDC {
value = static_dielectric(d, t + 273.15);
};
};
};
value
}
OPR | OTD => {
let d: f64 = ts_thermal(t, s, OD);
let cp: f64 = ts_thermal(t, s, OCP);
let tc: f64 = thcond(d, t + 273.15);
let mut value: f64 = 0.0;
if o_id == OTD {
value = thermal_diffusivity(tc, cp, d);
} else if o_id == OPR {
let dv: f64 = viscosity(d, t + 273.15);
value = prandtl_number(dv, cp, tc);
}
value
}
_ => ts_thermal(t, s, o_id),
}
}
/// hx(h,x,o_id) - the propertry of o_id (thermodynamic)
///
/// # Examples
///
///```
/// use if97::*;
///
/// let h: f64 =1094.690434;
/// let x: f64 = 0.3;
/// let p: f64 = hx(h, x, OP);
/// let t: f64 = hx(h, x, OT);
/// println!("hx: h={p:.6} x={x:.6} p={p:.6} t={t:.6}");
/// ```
///
pub fn hx(h: f64, x: f64, o_id: i32) -> f64 {
if h > H_MAX4 || h < H_MIN4 || x > 1.0 || x < 0.0 {
return INVALID_VALUE as f64;
}
match o_id {
OH => return h,
OX => return x,
_ => hx_reg4(h, x, o_id),
}
}
/// sx(s,x,o_id) - the propertry of o_id (thermodynamic)
///
/// # Examples
///
///```
/// use if97::*;
///
/// let s: f64 =3.119434;
/// let x: f64 = 0.3;
/// let p: f64 = sx(s, x, OP);
/// let t: f64 = sx(s, x, OT);
/// println!("sx: s={p:.6} x={x:.6} p={p:.6} t={t:.6}");
/// ```
///
pub fn sx(s: f64, x: f64, o_id: i32) -> f64 {
if s > S_MAX4 || s < S_MIN4 || x > 1.0 || x < 0.0 {
return INVALID_VALUE as f64;
}
match o_id {
OS => return s,
OX => return x,
_ => sx_reg4(s, x, o_id),
}
}