Open fwitte opened 6 months ago
Hello @fwitte! Thanks for updating this PR. We checked the lines you've touched for PEP 8 issues, and found:
Line 38:80: E501 line too long (83 > 79 characters) Line 52:80: E501 line too long (80 > 79 characters) Line 75:80: E501 line too long (87 > 79 characters) Line 77:80: E501 line too long (84 > 79 characters) Line 162:80: E501 line too long (92 > 79 characters) Line 214:80: E501 line too long (88 > 79 characters) Line 215:80: E501 line too long (92 > 79 characters) Line 268:24: E222 multiple spaces after operator Line 329:80: E501 line too long (92 > 79 characters) Line 330:80: E501 line too long (96 > 79 characters) Line 343:80: E501 line too long (84 > 79 characters)
Line 1:80: E501 line too long (93 > 79 characters) Line 92:1: E402 module level import not at top of file Line 103:80: E501 line too long (82 > 79 characters) Line 104:80: E501 line too long (81 > 79 characters) Line 150:80: E501 line too long (82 > 79 characters) Line 151:80: E501 line too long (81 > 79 characters) Line 160:32: W292 no newline at end of file
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.