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test travis

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This commit is contained in:
Rod Persky
2014-05-17 17:44:21 +10:00
parent e9e4f5d824
commit 58aa23c95b
2 changed files with 53 additions and 42 deletions
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15
.travis.yml
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@@ -3,17 +3,14 @@ virtualenv:
system_site_packages: true
python:
- "2.7"
- "3.2"
- "3.3"
# command to install dependencies
install:
- gcc -v
- pip -q install cython --install-option="--no-cython-compile"
- cd wrappers/Python
- python setup.py install # Install CoolProp
- cd ../SharedLibrary
- mkdir build
- cmake .. -DCOOLPROP_TESTING=ON
- cmake .. -DCOOLPROP_TESTING=ON
- make
- ctest
# command to run tests
script:
- pwd
@@ -23,6 +20,6 @@ script:
notifications:
email:
recipients:
- ian.h.bell@gmail.com
- rodney.persky@gmail.com
on_success: never # default: change
on_failure: always # default: always
on_failure: always # default: always

80
Web/examples/C++/Example.cpp
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@@ -1,11 +1,13 @@
#include "CoolProp.h"
#include "HumidAirProp.h"
#include "CPState.h"
//#include "CPState.h"
#include <iostream>
#include <stdlib.h>
#pragma GCC diagnostic ignored "-Wwrite-strings" //Ignore char* warnings
using namespace CoolProp; // For normal CoolProp calls
using namespace HumidAir; // For HAPropsSI
int main() {
double T, h, p, D;
@@ -13,89 +15,101 @@ int main() {
printf("CoolProp gitrevision:\t%s\n", get_global_param_string("gitrevision").c_str());
printf("CoolProp fluids:\t%s\n", get_global_param_string("FluidsList").c_str());
printf("\n************ USING EOS *************\n");
printf("FLUID STATE INDEPENDENT INPUTS\n");
printf("Critical Density Propane: %f kg/m^3\n", Props1("Propane", "rhocrit"));
//printf("Critical Density Propane: %f kg/m^3\n", PropsSI1("Propane", "rhocrit"));
printf("\nTWO PHASE INPUTS (Pressure)\n");
printf("Density of saturated liquid Propane at 101.325 kPa: %f kg/m^3\n", Props("D", 'P', 101.325, 'Q', 0, "Propane"));
printf("Density of saturated vapor R290 at 101.325 kPa: %f kg/m^3\n", Props("D", 'P', 101.325, 'Q', 1, "R290"));
printf("Density of saturated liquid Propane at 101.325 kPa: %f kg/m^3\n", PropsSI("D", "P", 101.325, "Q", 0, "Propane"));
printf("Density of saturated vapor R290 at 101.325 kPa: %f kg/m^3\n", PropsSI("D", "P", 101.325, "Q", 1, "R290"));
printf("\nTWO PHASE INPUTS (Temperature)\n");
printf("Density of saturated liquid Propane at 300 K: %f kg/m^3\n", Props("D", 'T', 300, 'Q', 0, "Propane"));
printf("Density of saturated vapor R290 at 300 K: %f kg/m^3\n", Props("D", 'T', 300, 'Q', 1, "R290"));
printf("Density of saturated liquid Propane at 300 K: %f kg/m^3\n", PropsSI("D", "T", 300, "Q", 0, "Propane"));
printf("Density of saturated vapor R290 at 300 K: %f kg/m^3\n", PropsSI("D", "T", 300, "Q", 1, "R290"));
printf("\nSINGLE PHASE CYCLE (Propane)\n");
p = Props("P", 'T', 300, 'D', 1, "Propane");
h = Props("H", 'T', 300, 'D', 1, "Propane");
p = PropsSI("P", "T", 300, "D", 1, "Propane");
h = PropsSI("H", "T", 300, "D", 1, "Propane");
printf("T,D -> P,H : 300,1 -> %f,%f\n", p, h);
T = Props("T", 'P', p, 'H', h, "Propane");
D = Props("D", 'P', p, 'H', h, "Propane");
T = PropsSI("T", "P", p, "H", h, "Propane");
D = PropsSI("D", "P", p, "H", h, "Propane");
printf("P,H -> T,D : %f, %f -> %f, %f\n", p, h, T, D);
/* enable_TTSE_LUT not currently in V5
printf("\n************ USING TTSE ***************\n");
enable_TTSE_LUT("Propane");
printf("TWO PHASE INPUTS (Pressure)\n");
printf("Density of saturated liquid Propane at 101.325 kPa: %f kg/m^3\n", Props("D", 'P', 101.325, 'Q', 0, "Propane"));
printf("Density of saturated vapor R290 at 101.325 kPa: %f kg/m^3\n", Props("D", 'P', 101.325, 'Q', 1, "R290"));
printf("Density of saturated liquid Propane at 101.325 kPa: %f kg/m^3\n", PropsSI("D", "P", 101.325, "Q", 0, "Propane"));
printf("Density of saturated vapor R290 at 101.325 kPa: %f kg/m^3\n", PropsSI("D", "P", 101.325, "Q", 1, "R290"));
printf("\nTWO PHASE INPUTS (Temperature)");
printf("Density of saturated liquid Propane at 300 K: %f kg/m^3\n", Props("D", 'T', 300, 'Q', 0, "Propane"));
printf("Density of saturated vapor R290 at 300 K: %f kg/m^3\n", Props("D", 'T', 300, 'Q', 1, "R290"));
printf("Density of saturated liquid Propane at 300 K: %f kg/m^3\n", PropsSI("D", "T", 300, "Q", 0, "Propane"));
printf("Density of saturated vapor R290 at 300 K: %f kg/m^3\n", PropsSI("D", "T", 300, "Q", 1, "R290"));
printf("\nSINGLE PHASE CYCLE (propane)\n");
p = Props("P", 'T', 300, 'D', 1, "Propane");
h = Props("H", 'T', 300, 'D', 1, "Propane");
p = PropsSI("P", "T", 300, "D", 1, "Propane");
h = PropsSI("H", "T", 300, "D", 1, "Propane");
printf("T,D -> P,H : 300,1 -> %f,%f", p, h);
T = Props("T", 'P', p, 'H', h, "Propane");
D = Props("D", 'P', p, 'H', h, "Propane");
T = PropsSI("T", "P", p, "H", h, "Propane");
D = PropsSI("D", "P", p, "H", h, "Propane");
printf("P,H -> T,D : %f, %f -> %f, %f\n", p, h, T, D);
disable_TTSE_LUT("Propane");
*/
/* get_fluid_param_string not currently in V5
try
{
printf("\n************ USING REFPROP ***************\n");
std::string RPName = std::string("REFPROP-")+get_fluid_param_string("Propane","REFPROPname");
printf("TWO PHASE INPUTS (Pressure)");
printf("Density of saturated liquid Propane at 101.325 kPa: %f kg/m^3\n", Props("D", 'P', 101.325, 'Q', 0, RPName));
printf("Density of saturated vapor R290 at 101.325 kPa: %f kg/m^3\n", Props("D", 'P', 101.325, 'Q', 1, RPName));
printf("Density of saturated liquid Propane at 101.325 kPa: %f kg/m^3\n", PropsSI("D", "P", 101.325, "Q", 0, RPName));
printf("Density of saturated vapor R290 at 101.325 kPa: %f kg/m^3\n", PropsSI("D", "P", 101.325, "Q", 1, RPName));
printf("\nTWO PHASE INPUTS (Temperature)");
printf("Density of saturated liquid Propane at 300 K: %f kg/m^3\n", Props("D", 'T', 300, 'Q', 0, RPName));
printf("Density of saturated vapor R290 at 300 K: %f kg/m^3\n", Props("D", 'T', 300, 'Q', 1, RPName));
printf("Density of saturated liquid Propane at 300 K: %f kg/m^3\n", PropsSI("D", "T", 300, "Q", 0, RPName));
printf("Density of saturated vapor R290 at 300 K: %f kg/m^3\n", PropsSI("D", "T", 300, "Q", 1, RPName));
printf("\nSINGLE PHASE CYCLE (propane)\n");
p = Props("P", 'T', 300, 'D', 1, RPName);
h = Props("H", 'T', 300, 'D', 1, RPName);
p = PropsSI("P", "T", 300, "D", 1, RPName);
h = PropsSI("H", "T", 300, "D", 1, RPName);
printf("T,D -> P,H : 300,1 -> %f,%f\n", p, h);
T = Props("T", 'P', p, 'H', h, RPName);
D = Props("D", 'P', p, 'H', h, RPName);
T = PropsSI("T", "P", p, "H", h, RPName);
D = PropsSI("D", "P", p, "H", h, RPName);
printf("P,H -> T,D : %f, %f -> %f, %f\n", p, h, T, D);
}
catch (std::exception &e)
{
printf("\n************ CANT USE REFPROP ************\n");
}
*/
/* set_standard_unit_system not currently in V5
printf("\n************ CHANGE UNIT SYSTEM (default is kSI) *************\n");
set_standard_unit_system(UNIT_SYSTEM_SI);
printf("Vapor pressure of water at 373.15 K in SI units (Pa): %f\n", Props("P", 'T', 373.15, 'Q', 0, "Water"));
printf("Vapor pressure of water at 373.15 K in SI units (Pa): %f\n", PropsSI("P", "T", 373.15, "Q", 0, "Water"));
set_standard_unit_system(UNIT_SYSTEM_KSI);
printf("Vapor pressure of water at 373.15 K in kSI units (kPa): %f\n", Props("P", 'T', 373.15, 'Q', 0, "Water"));
printf("Vapor pressure of water at 373.15 K in kSI units (kPa): %f\n", PropsSI("P", "T", 373.15, "Q", 0, "Water"));
*/
printf("\n************ BRINES AND SECONDARY WORKING FLUIDS *************\n");
printf("Density of 50%% (mass) ethylene glycol/water at 300 K, 101.325 kPa: %f kg/m^3\n", Props("D", 'T', 300, 'P', 101.325, "EG-50%"));
printf("Viscosity of Therminol D12 at 350 K, 101.325 kPa: %f Pa-s\n", Props("V", 'T', 350, 'P', 101.325, "TD12"));
printf("Density of 50%% (mass) ethylene glycol/water at 300 K, 101.325 kPa: %f kg/m^3\n", PropsSI("D", "T", 300, "P", 101.325, "EG-50%"));
printf("Viscosity of Therminol D12 at 350 K, 101.325 kPa: %f Pa-s\n", PropsSI("V", "T", 350, "P", 101.325, "TD12"));
printf("\n************ HUMID AIR PROPERTIES *************\n");
printf("Humidity ratio of 50%% rel. hum. air at 300 K, 101.325 kPa: %f kg_w/kg_da\n", HAProps("W", "T", 300, "P", 101.325, "R", 0.5));
printf("Relative humidity from last calculation: %f (fractional)\n", HAProps("R", "T", 300, "P", 101.325, "W", HAProps("W", "T", 300, "P", 101.325, "R", 0.5)));
// HAProps API broken in V5
//printf("\n************ HUMID AIR PROPERTIES *************\n");
//printf("Humidity ratio of 50%% rel. hum. air at 300 K, 101.325 kPa: %f kg_w/kg_da\n", HAPropsSI('W', 'T', 300, 'P', 101.325, 'R', 0.5));
//printf("Relative humidity from last calculation: %f (fractional)\n", HAPropsSI('R', 'T', 300, 'P', 101.325, 'W', HAPropsSI('W', 'T', 300, 'P', 101.325, 'R', 0.5)));
return 0;
}