Open fwitte opened 1 month ago
Hello @fwitte! Thanks for updating this PR. We checked the lines you've touched for PEP 8 issues, and found:
Line 63:80: E501 line too long (98 > 79 characters) Line 65:80: E501 line too long (104 > 79 characters) Line 72:80: E501 line too long (114 > 79 characters) Line 75:80: E501 line too long (83 > 79 characters) Line 86:80: E501 line too long (98 > 79 characters) Line 152:24: E222 multiple spaces after operator Line 222:80: E501 line too long (87 > 79 characters) Line 232:25: E222 multiple spaces after operator Line 238:80: E501 line too long (81 > 79 characters) Line 239:80: E501 line too long (89 > 79 characters) Line 259:80: E501 line too long (90 > 79 characters) Line 260:80: E501 line too long (85 > 79 characters) Line 264:80: E501 line too long (84 > 79 characters) Line 265:80: E501 line too long (81 > 79 characters) Line 270:80: E501 line too long (87 > 79 characters) Line 293:80: E501 line too long (83 > 79 characters) Line 324:24: E222 multiple spaces after operator Line 366:26: E222 multiple spaces after operator Line 373:80: E501 line too long (85 > 79 characters) Line 384:80: E501 line too long (86 > 79 characters) Line 385:80: E501 line too long (81 > 79 characters) Line 389:80: E501 line too long (153 > 79 characters) Line 392:80: E501 line too long (172 > 79 characters)
Line 1:80: E501 line too long (93 > 79 characters) Line 90:1: E402 module level import not at top of file Line 102:80: E501 line too long (80 > 79 characters) Line 120:16: E225 missing whitespace around operator Line 128:80: E501 line too long (123 > 79 characters) Line 129:80: E501 line too long (107 > 79 characters)
Especially in heat pump or refrigeration machine applications, the condenser component may have a significant heat transfer share from the desuperheating of the working fluid. The heat transfer coefficients for desuperheating and condensation usually differ strongly, therefore using an overall
kA
(UA
) value for the complete process to model part load may not be correct. Therefore an approach is implemented with a moving boundary, which will split the virtual area of the condenser into a desuperheating and a condensation part. The split will happen proportionally to the heat transfer of each subprocess and be validated using reference data.