Coverage for backend/flowsheetInternals/unitops/config/objects/stream_config.py: 100%

1from common.config_types import * 

2from common.config_utils import * 

3 

4 

5property_combinations = ( 

6 ("temperature", "pressure"), 

7 ("temperature", "vapor_frac"), 

8 ("pressure", "vapor_frac"), 

9 ("enth_mol", "pressure"), 

10 ("enth_mass", "pressure"), 

11 ("entr_mol", "temperature"), 

12 ("entr_mass", "temperature"), 

13 ("total_energy_flow", "pressure"), 

14 ("temperature", "enth_mol"), 

15 ("temperature", "enth_mass"), 

16 ("pressure", "entr_mol"), 

17 ("pressure", "entr_mass"), 

18) 

19# for each combination, add the following flows: 

20# molarFlow, massFlow, volumetricFlow 

21degrees_of_freedom = [] 

22for combination in property_combinations: 

23 for flow in ["flow_mol", "flow_mass", "flow_vol"]: 

24 degrees_of_freedom.append(combination + (flow,)) 

25 

26 

27stream_config: ObjectType = ObjectType.model_validate({ 

28 "displayType": "S", 

29 "displayName": "Stream", 

30 "is_stream": True, 

31 "ports": {}, 

32 # TODO: check if streams have inlets and outlets 

33 "graphicObject": stream_graphic(), 

34 "indexSets": ["phase","compound"], 

35 "properties": { 

36 "mole_frac_comp": { 

37 "displayName": "Compounds", 

38 "propertySetGroup": "composition", 

39 "type": "numeric", 

40 "unitType": "ratio", 

41 "indexSets": ["compound"], 

42 }, 

43 "flow_mass": { 

44 "displayName": "Mass Flow", 

45 "type": "numeric", 

46 "unitType": "massflow", 

47 }, 

48 "flow_mol": { 

49 "displayName": "Molar Flow", 

50 "type": "numeric", 

51 "unitType": "molarflow", 

52 }, 

53 "temperature": { 

54 "displayName": "Temperature", 

55 "type": "numeric", 

56 "unitType": "temperature", 

57 }, 

58 "pressure": { 

59 "displayName": "Pressure", 

60 "type": "numeric", 

61 "unitType": "pressure", 

62 }, 

63 "vapor_frac": { 

64 "displayName": "Vapor Fraction", 

65 "type": "numeric", 

66 "unitType": "ratio", 

67 }, 

68 "enth_mol": { 

69 "displayName": "Molar Specific Enthalpy", 

70 "type": "numeric", 

71 "unitType": "molarEnthalpy", 

72 }, 

73 "enth_mass": { 

74 "displayName": "Mass Specific Enthalpy", 

75 "type": "numeric", 

76 "unitType": "massEnthalpy", 

77 }, 

78 "entr_mol": { 

79 "displayName": "Molar Specific Entropy", 

80 "type": "numeric", 

81 "unitType": "molarEntropy", 

82 }, 

83 "entr_mass": { 

84 "displayName": "Mass Specific Entropy", 

85 "type": "numeric", 

86 "unitType": "massEntropy", 

87 }, 

88 "total_energy_flow": { 

89 "displayName": "Total Energy Flow", 

90 "type": "numeric", 

91 "unitType": "heatflow", 

92 }, 

93 "flow_vol": { 

94 "displayName": "Volumetric Flow", 

95 "type": "numeric", 

96 "unitType": "volumetricFlow", 

97 }, 

98 "mole_frac_phase_comp": { 

99 "displayName": "Phases", 

100 "type": "numeric", 

101 "unitType": "ratio", 

102 "indexSets": ["phase","compound"], 

103 }, 

104 }, 

105 "propertySetGroups": { 

106 "composition": { 

107 "type": "composition", 

108 "displayName": "Composition", 

109 "stateVars": ("mole_frac_comp",), 

110 }, 

111 "default": { 

112 "type": "stateVars", 

113 "displayName": "Properties", 

114 "stateVars": ("flow_mol", "temperature", "pressure"), 

115 }, 

116 }, 

117 "keyProperties": { 

118 "mass": [ 

119 "flow_mass", 

120 "temperature", 

121 "pressure", 

122 "vapor_frac" 

123 ], 

124 "molar": [ 

125 "flow_mol", 

126 "temperature", 

127 "pressure", 

128 "vapor_frac" 

129 ] 

130 } 

131})