SharpProp 3.2.1

There is a newer version of this package available.
See the version list below for details.
dotnet add package SharpProp --version 3.2.1                
NuGet\Install-Package SharpProp -Version 3.2.1                
This command is intended to be used within the Package Manager Console in Visual Studio, as it uses the NuGet module's version of Install-Package.
<PackageReference Include="SharpProp" Version="3.2.1" />                
For projects that support PackageReference, copy this XML node into the project file to reference the package.
paket add SharpProp --version 3.2.1                
#r "nuget: SharpProp, 3.2.1"                
#r directive can be used in F# Interactive and Polyglot Notebooks. Copy this into the interactive tool or source code of the script to reference the package.
// Install SharpProp as a Cake Addin
#addin nuget:?package=SharpProp&version=3.2.1

// Install SharpProp as a Cake Tool
#tool nuget:?package=SharpProp&version=3.2.1                

SharpProp

Build & Tests CodeQL NuGet Platform License Codecov

A simple, full-featured, lightweight, cross-platform CoolProp wrapper for C#.

Overview

Project structure

  • Fluid class - for pure fluids and binary mixtures.
  • Mixture class - for mixtures with pure fluids components.
  • FluidsList enum - list of all available fluids.
  • Input record - inputs for the Fluid and Mixture classes.
  • HumidAir class - for humid air.
  • InputHumidAir record - inputs for the HumidAir class.

Unit safety

All calculations of thermophysical properties are unit safe (thanks to UnitsNet). This allows you to avoid errors associated with incorrect dimensions of quantities, and will help you save a lot of time on their search and elimination. In addition, you will be able to convert all values to many other dimensions without the slightest difficulty.

List of properties

For instances of Fluid and Mixture:

  • Compressibility - compressibility factor (dimensionless).
  • Conductivity - thermal conductivity (by default, W/m/K).
  • CriticalPressure - absolute pressure at the critical point (by default, kPa).
  • CriticalTemperature - temperature at the critical point (by default, °C).
  • Density - mass density (by default, kg/m3).
  • DynamicViscosity - dynamic viscosity (by default, mPa*s).
  • Enthalpy - mass specific enthalpy (by default, kJ/kg).
  • Entropy - mass specific entropy (by default, kJ/kg/K).
  • FreezingTemperature - temperature at freezing point (for incompressible fluids) (by default, °C).
  • InternalEnergy - mass specific internal energy (by default, kJ/kg).
  • KinematicViscosity - kinematic viscosity (by default, cSt).
  • MaxPressure - maximum pressure limit (by default, kPa).
  • MaxTemperature - maximum temperature limit (by default, °C).
  • MinPressure - minimum pressure limit (by default, kPa).
  • MinTemperature - minimum temperature limit (by default, °C).
  • MolarMass - molar mass (by default, g/mol).
  • Phase - phase state (enum).
  • Prandtl - Prandtl number (dimensionless).
  • Pressure - absolute pressure (by default, kPa).
  • Quality - mass vapor quality (by default, %).
  • SoundSpeed - sound speed (by default, m/s).
  • SpecificHeat - mass specific constant pressure specific heat (by default, kJ/kg/K).
  • SurfaceTension - surface tension (by default, N/m).
  • Temperature - temperature (by default, °C).
  • TriplePressure - absolute pressure at the triple point (by default, kPa).
  • TripleTemperature - temperature at the triple point (by default, °C).

For instances of HumidAir:

  • Compressibility - compressibility factor (dimensionless).
  • Conductivity - thermal conductivity (by default, W/m/K).
  • Density - mass density per humid air unit (by default, kg/m3).
  • DewTemperature - dew-point temperature (by default, °C).
  • DynamicViscosity - dynamic viscosity (by default, mPa*s).
  • Enthalpy - mass specific enthalpy per humid air (by default, kJ/kg).
  • Entropy - mass specific entropy per humid air (by default, kJ/kg/K).
  • Humidity - absolute humidity ratio (by default, g/kg d.a.).
  • KinematicViscosity - kinematic viscosity (by default, cSt).
  • PartialPressure - partial pressure of water vapor (by default, kPa).
  • Prandtl - Prandtl number (dimensionless).
  • Pressure - absolute pressure (by default, kPa).
  • RelativeHumidity - relative humidity ratio (by default, %).
  • SpecificHeat - mass specific constant pressure specific heat per humid air (by default, kJ/kg/K).
  • Temperature - dry-bulb temperature (by default, °C).
  • WetBulbTemperature - wet-bulb temperature (by default, °C).

NB. If the required property is not present in the instance of the fluid, then you can add it by extending the Fluid, Mixture or HumidAir classes (see how to add other properties).

Examples

Pure fluids

To calculate the specific heat of saturated water vapor at 1 atm:

using System;
using SharpProp;
using UnitsNet.NumberExtensions.NumberToPressure;
using UnitsNet.NumberExtensions.NumberToRatio;
using UnitsNet.Units;
var waterVapour = new Fluid(FluidsList.Water);
waterVapour.Update(Input.Pressure((1).Atmospheres()), Input.Quality((100).Percent()));
Console.WriteLine(waterVapour.SpecificHeat.JoulesPerKilogramKelvin); // 2079.937085633241
Console.WriteLine(waterVapour.SpecificHeat);                         // 2.08 kJ/kg.K
Console.WriteLine(waterVapour.SpecificHeat
    .ToUnit(SpecificEntropyUnit.CaloriePerGramKelvin));              // 0.5 cal/g.K

Incompressible binary mixtures

To calculate the dynamic viscosity of propylene glycol aqueous solution with 60 % mass fraction at 100 kPa and -20 °C:

using System;
using SharpProp;
using UnitsNet.NumberExtensions.NumberToPressure;
using UnitsNet.NumberExtensions.NumberToRatio;
using UnitsNet.NumberExtensions.NumberToTemperature;
using UnitsNet.Units;
var propyleneGlycol = new Fluid(FluidsList.MPG, (60).Percent());
propyleneGlycol.Update(Input.Pressure((100).Kilopascals()), Input.Temperature((-20).DegreesCelsius()));
Console.WriteLine(propyleneGlycol.DynamicViscosity?.PascalSeconds); // 0.13907391053938878
Console.WriteLine(propyleneGlycol.DynamicViscosity);                // 139.07 mPa·s
Console.WriteLine(propyleneGlycol.DynamicViscosity?
    .ToUnit(DynamicViscosityUnit.Poise));                           // 1.39 P

Mixtures

To calculate the density of ethanol aqueous solution (with ethanol 40 % mass fraction) at 200 kPa and 277.15 K:

using System;
using System.Collections.Generic;
using SharpProp;
using UnitsNet;
using UnitsNet.NumberExtensions.NumberToPressure;
using UnitsNet.NumberExtensions.NumberToRatio;
using UnitsNet.NumberExtensions.NumberToTemperature;
using UnitsNet.Units;
var mixture = new Mixture(new List<FluidsList> {FluidsList.Water, FluidsList.Ethanol}, 
    new List<Ratio> {(60).Percent(), (40).Percent()});
mixture.Update(Input.Pressure((200).Kilopascals()), Input.Temperature((277.15).Kelvins()));
Console.WriteLine(mixture.Density.KilogramsPerCubicMeter);               // 883.3922771627759
Console.WriteLine(mixture.Density);                                      // 883.39 kg/m3
Console.WriteLine(mixture.Density.ToUnit(DensityUnit.GramPerDeciliter)); // 88.34 g/dl

Humid air

To calculate the wet bulb temperature of humid air at 99 kPa, 30 °C and 50 % relative humidity:

using System;
using SharpProp;
using UnitsNet.NumberExtensions.NumberToPressure;
using UnitsNet.NumberExtensions.NumberToRelativeHumidity;
using UnitsNet.NumberExtensions.NumberToTemperature;
using UnitsNet.Units;
var humidAir = new HumidAir();
humidAir.Update(InputHumidAir.Pressure((99).Kilopascals()), 
    InputHumidAir.Temperature((30).DegreesCelsius()), InputHumidAir.RelativeHumidity((50).Percent()));
// or use:
// var humidAir1 = 
//     HumidAir.WithState(InputHumidAir.Pressure((99).Kilopascals()), 
//         InputHumidAir.Temperature((30).DegreesCelsius()), InputHumidAir.RelativeHumidity((50).Percent()));
Console.WriteLine(humidAir.WetBulbTemperature.Kelvins); // 295.0965785590792
Console.WriteLine(humidAir.WetBulbTemperature);         // 21.95 °C
Console.WriteLine(humidAir.WetBulbTemperature
    .ToUnit(TemperatureUnit.DegreeFahrenheit));         // 71.5 °F

Equality of instances

You can simply determine the equality of Fluid, Mixture and HumidAir instances by its state. Just use the Equals method or the equality operators (== or !=). Exactly the same way you can compare inputs (Input, InputHumidAir or any IKeyedInput record).

For example:

using System;
using SharpProp;
using UnitsNet.NumberExtensions.NumberToPressure;
using UnitsNet.NumberExtensions.NumberToRelativeHumidity;
using UnitsNet.NumberExtensions.NumberToTemperature;
var humidAir = HumidAir.WithState(InputHumidAir.Pressure((1).Atmospheres()),
    InputHumidAir.Temperature((20).DegreesCelsius()), InputHumidAir.RelativeHumidity((50).Percent()));
var humidAirWithSameState = HumidAir.WithState(InputHumidAir.Pressure((101325).Pascals()),
    InputHumidAir.Temperature((293.15).Kelvins()), InputHumidAir.RelativeHumidity((50).Percent()));
Console.WriteLine(humidAir == humidAirWithSameState);               // true
Console.WriteLine(InputHumidAir.Pressure((1).Atmospheres()) == 
                  InputHumidAir.Pressure((101.325).Kilopascals())); // true

Converting to a JSON string

The Fluid, Mixture and HumidAir classes have an extension method AsJson, which performs converting of instance to a JSON string. For example, converting a Fluid instance to an indented JSON string:

using System;
using SharpProp;
using SharpProp.Extensions;
using UnitsNet.NumberExtensions.NumberToRatio;
using UnitsNet.NumberExtensions.NumberToTemperature;
var refrigerant = new Fluid(FluidsList.R32);
refrigerant.Update(Input.Temperature((5).DegreesCelsius()), Input.Quality((100).Percent()));
Console.WriteLine(refrigerant.AsJson());

As a result:

{
  "Name": "R32",
  "Fraction": {
    "Unit": "RatioUnit.Percent",
    "Value": 100.0
  },
  "Compressibility": 0.8266625877210833,
  "Conductivity": {
    "Unit": "ThermalConductivityUnit.WattPerMeterKelvin",
    "Value": 0.013435453854396475
  },
  "CriticalPressure": {
    "Unit": "PressureUnit.Kilopascal",
    "Value": 5782.0
  },
  "CriticalTemperature": {
    "Unit": "TemperatureUnit.DegreeCelsius",
    "Value": 78.10500000000002
  },
  "Density": {
    "Unit": "DensityUnit.KilogramPerCubicMeter",
    "Value": 25.89088151061046
  },
  "DynamicViscosity": {
    "Unit": "DynamicViscosityUnit.MillipascalSecond",
    "Value": 0.012606543144761657
  },
  "Enthalpy": {
    "Unit": "SpecificEnergyUnit.KilojoulePerKilogram",
    "Value": 516.1057800378023
  },
  "Entropy": {
    "Unit": "SpecificEntropyUnit.KilojoulePerKilogramKelvin",
    "Value": 2.1362654412978777
  },
  "FreezingTemperature": null,
  "InternalEnergy": {
    "Unit": "SpecificEnergyUnit.KilojoulePerKilogram",
    "Value": 479.35739743435374
  },
  "MaxPressure": {
    "Unit": "PressureUnit.Kilopascal",
    "Value": 70000.0
  },
  "MaxTemperature": {
    "Unit": "TemperatureUnit.DegreeCelsius",
    "Value": 161.85000000000002
  },
  "MinPressure": {
    "Unit": "PressureUnit.Kilopascal",
    "Value": 0.04799989387605937
  },
  "MinTemperature": {
    "Unit": "TemperatureUnit.DegreeCelsius",
    "Value": -136.80999999999997
  },
  "MolarMass": {
    "Unit": "MolarMassUnit.GramPerMole",
    "Value": 52.024
  },
  "Phase": "TwoPhase",
  "Prandtl": 1.2252282243443504,
  "Pressure": {
    "Unit": "PressureUnit.Kilopascal",
    "Value": 951.448019691762
  },
  "Quality": {
    "Unit": "RatioUnit.Percent",
    "Value": 100.0
  },
  "SoundSpeed": {
    "Unit": "SpeedUnit.MeterPerSecond",
    "Value": 209.6337575990297
  },
  "SpecificHeat": {
    "Unit": "SpecificEntropyUnit.KilojoulePerKilogramKelvin",
    "Value": 1.3057899441785379
  },
  "SurfaceTension": {
    "Unit": "ForcePerLengthUnit.NewtonPerMeter",
    "Value": 0.010110117241546162
  },
  "Temperature": {
    "Unit": "TemperatureUnit.DegreeCelsius",
    "Value": 5.0
  },
  "TriplePressure": {
    "Unit": "PressureUnit.Kilopascal",
    "Value": 0.04799989387605937
  },
  "TripleTemperature": {
    "Unit": "TemperatureUnit.DegreeCelsius",
    "Value": -136.80999999999997
  }
}

Deep cloning

The Fluid, Mixture and HumidAir classes have an extension method Clone, which performs deep (full) copy of instance:

using System;
using SharpProp;
using SharpProp.Extensions;
using UnitsNet.NumberExtensions.NumberToPressure;
using UnitsNet.NumberExtensions.NumberToTemperature;
var water = new Fluid(FluidsList.Water);
water.Update(Input.Pressure((1).Atmospheres()), Input.Temperature((20).DegreesCelsius()));
var clone = water.Clone();
Console.WriteLine(water == clone); // true
water.Update(Input.Pressure((1).Atmospheres()), Input.Temperature((30).DegreesCelsius()));
Console.WriteLine(water == clone); // false

Adding other properties

Adding other inputs

Product Compatible and additional computed target framework versions.
.NET net5.0 is compatible.  net5.0-windows was computed.  net6.0 was computed.  net6.0-android was computed.  net6.0-ios was computed.  net6.0-maccatalyst was computed.  net6.0-macos was computed.  net6.0-tvos was computed.  net6.0-windows was computed.  net7.0 was computed.  net7.0-android was computed.  net7.0-ios was computed.  net7.0-maccatalyst was computed.  net7.0-macos was computed.  net7.0-tvos was computed.  net7.0-windows was computed.  net8.0 was computed.  net8.0-android was computed.  net8.0-browser was computed.  net8.0-ios was computed.  net8.0-maccatalyst was computed.  net8.0-macos was computed.  net8.0-tvos was computed.  net8.0-windows was computed. 
Compatible target framework(s)
Included target framework(s) (in package)
Learn more about Target Frameworks and .NET Standard.

NuGet packages (1)

Showing the top 1 NuGet packages that depend on SharpProp:

Package Downloads
VCRC

Cross-platform vapor-compression refrigeration cycles analysis tool

GitHub repositories

This package is not used by any popular GitHub repositories.

Version Downloads Last updated
7.3.0 407 10/3/2024
7.2.11 830 8/29/2024
7.2.10 784 7/2/2024
7.2.9 418 6/11/2024
7.2.8 875 3/19/2024
7.2.7 589 2/21/2024
7.2.6 310 1/19/2024
7.2.4 203 1/16/2024
7.2.3 305 12/27/2023
7.2.2 234 12/20/2023
7.2.1 303 12/10/2023
7.2.0 275 11/30/2023
7.1.0 315 11/15/2023
7.0.6 190 11/10/2023
7.0.5 363 10/11/2023
7.0.4 356 9/26/2023
7.0.3 351 9/6/2023
7.0.2 347 8/31/2023
7.0.1 226 8/30/2023
7.0.0 394 8/4/2023
6.0.4 1,151 3/18/2023
6.0.3 367 3/10/2023
6.0.2 408 3/5/2023
6.0.1 437 2/26/2023
6.0.0 492 2/18/2023
5.0.0 1,055 12/4/2022
4.4.1 5,302 11/21/2022
4.4.0 473 11/15/2022
4.3.3 636 11/7/2022
4.3.2 533 11/2/2022
4.3.1 690 9/12/2022
4.2.5 615 9/5/2022
4.2.4 646 8/17/2022
4.2.3 642 8/5/2022
4.2.2 634 7/22/2022
4.2.1 668 7/4/2022
4.2.0 667 6/29/2022
4.1.0 459 6/27/2022
4.0.3 871 6/22/2022
4.0.2 644 6/14/2022
4.0.1 663 6/7/2022
4.0.0 557 5/27/2022
3.2.4 579 5/7/2022
3.2.3 726 4/24/2022
3.2.2 864 4/6/2022
3.2.1 711 4/4/2022
3.2.0 735 3/22/2022
3.1.19 680 3/11/2022
3.1.18 685 3/4/2022
3.1.17 652 3/1/2022
3.1.16 668 2/17/2022
3.1.15 656 2/12/2022
3.1.14 728 1/29/2022
3.1.13 410 1/10/2022
3.1.11 559 12/8/2021
3.1.10 477 12/5/2021
3.1.9 1,535 11/28/2021
3.1.8 426 11/27/2021
3.1.7 3,312 11/25/2021
3.1.6 311 11/23/2021
3.1.4 363 11/16/2021
3.1.3 357 11/13/2021
3.1.2 426 11/6/2021
3.1.1 394 11/5/2021
3.1.0 404 10/29/2021
3.0.4 371 10/26/2021
3.0.3 483 10/24/2021
3.0.2 473 10/23/2021
3.0.1 378 10/22/2021
3.0.0 403 10/21/2021
2.0.4 382 10/18/2021
2.0.3 424 10/17/2021
2.0.2 364 10/15/2021
2.0.1 361 10/5/2021
2.0.0 356 9/27/2021
1.1.0 422 9/18/2021
1.0.6 344 9/18/2021
1.0.5 433 9/15/2021
1.0.4 370 9/15/2021
1.0.3 389 9/15/2021
1.0.2 366 9/15/2021
1.0.1 438 9/12/2021

- Bump UnitsNet from 4.126.0 to 4.127.0.
- Bump UnitsNet.NumberExtensions from 4.126.0 to 4.127.0.