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| Mathematical constants | |
| const double | SMALL = 1.0e-23 | 
| considered a very small number | |
| const double | LARGE = 1.0e+23 | 
| considered a very large number | |
| const double | PI = 3.14159265358979323846 | 
| ratio of circle perimeter over its diameter:   | |
| Constants used to identify flow arrangement in heat exchangers | |
| const unsigned | COUNTER_FLOW = 1 | 
| counter flow | |
| const unsigned | PARALLEL_FLOW = 2 | 
| parallel flow | |
| const unsigned | CROSS_FLOW_BOTH_UNMIXED = 3 | 
| cross flow, both unmixed | |
| const unsigned | CROSS_FLOW_BOTH_MIXED = 4 | 
| cross flow, both mixed | |
| const unsigned | CROSS_FLOW_1_UNMIXED = 5 | 
| cross flow, first stream unmixed | |
| const unsigned | CROSS_FLOW_2_UNMIXED = 6 | 
| cross flow, second stream unmixed | |
| Physical constants | |
| const double | ABS_ZERO = -273.16 | 
| absolute zero temperature in [deg_C] | |
| const double | KELV_ZERO = 273.16 | 
| 0 [deg_C] in [K] | |
| const double | BOLTZ = 5.67E-8 | 
| Stefan-Boltzmann constant [W/(m^2*K^4)]. | |
| const double | CP_AIR = 1006.0 | 
| specific heat capacity of dry air [J/(kg*K)] | |
| const double | MW_AIR = 28.9645 | 
| molar weight of dry air [g/mol] | |
| const double | CP_VAP = 1805.0 | 
| specific heat capacity of water vapor [J/(kg*K)] | |
| const double | CP_WAT = 4186.0 | 
| specific heat capacity of liquid water [J/(kg*K)] | |
| const double | MW_WATER = 18.01528 | 
| molar weight of liquid water [g/mol] | |
| const double | MW_RATIO = 0.62197 | 
| ratio of molar weights of liquid water over dry air [-] | |
| const double | HF_VAP = 2.501E6 | 
| latent heat of vaporization of water [J/kg] | |
| const double | LAMBDA_AIR = 0.0243 | 
| thermal conductivity of dry air [W/(m*K)] | |
| const double | LAMBDA_WAT = 0.554 | 
| thermal conductivity of liquid water [W/(m*K)] | |
| const double | PRANDTL_AIR = 0.71 | 
| Prandtl number for dry air [-]. | |
| const double | RHO_AIR = 1.2 | 
| density of air [kg/m^3] | |
| const double | RHO_WAT = 998.0 | 
| density of water [kg/m^3] | |
| const double | VISC_WAT = 1.0E-3 | 
| dynamic viscosity for liquid water [kg/(m*s)] | |
| const double | R_AIR = 287.053 | 
| specific gas constant for ideal air [J/(kg*K)] | |
| const double | R_0 = 8314.34 | 
| universal gas constant [kJ/(mol*K)] | |
| const double | P_ATM = 101325.0 | 
| atmospheric pressure in [kg/(m*s^2)] or [Pa] | |
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| considered a very small number 
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| considered a very large number 
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ratio of circle perimeter over its diameter:  
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| counter flow 
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| parallel flow 
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| cross flow, both unmixed 
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| cross flow, both mixed 
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| cross flow, first stream unmixed 
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| cross flow, second stream unmixed 
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| absolute zero temperature in [deg_C] 
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| 0 [deg_C] in [K] 
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| Stefan-Boltzmann constant [W/(m^2*K^4)]. 
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| specific heat capacity of dry air [J/(kg*K)] 
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| molar weight of dry air [g/mol] 
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| specific heat capacity of water vapor [J/(kg*K)] 
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| specific heat capacity of liquid water [J/(kg*K)] 
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| molar weight of liquid water [g/mol] 
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| ratio of molar weights of liquid water over dry air [-] 
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| latent heat of vaporization of water [J/kg] 
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| thermal conductivity of dry air [W/(m*K)] 
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| thermal conductivity of liquid water [W/(m*K)] 
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| Prandtl number for dry air [-]. 
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| density of air [kg/m^3] 
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| density of water [kg/m^3] 
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| dynamic viscosity for liquid water [kg/(m*s)] 
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| specific gas constant for ideal air [J/(kg*K)] 
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| universal gas constant [kJ/(mol*K)] 
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| atmospheric pressure in [kg/(m*s^2)] or [Pa] 
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