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input and output files made the code much easier to use. For the user, these input and output files made the information very readable, and the files could be used in papers and presentations without significantly altering their format. CYCLES II eliminated Dostal’s option of optimizing heat exchanger volumes. CYCLES II, therefore could only produce results for the cycle defined by the user and the user would have to make judgments about how to size the heat exchangers. The goal with CYCLES III was to include all of the best features of the previous editions, along with some new features. After completion, the new developments in CYCLES III are: 1. Extended use of the easy to read Legault code structure and nomenclature 2. Inclusion of both optimization and single point calculations 3. Inclusion of both Simple and Recompression Cycles 4. The ability to model impure working fluids (or a variety of different working fluids) 5. An interface for the headers in TSCYCO 6. A convenient code manual (see Appendix A) for troubleshooting 2.2.1 Extended Use of the Legault Nomenclature CYCLES II incorporated an easy to read nomenclature, but Legault recommended that the use of it be extended further into some of the subroutines and that the structure should be simplified further. Though it may be contrary to some programmers’ preference, the use of a large variable module has been incorporated in CYCLES III so that the program code is easily readable and understandable for new users. Variable names are more intuitive than in the original CYCLES. For example, Legault changed temperature variables in the LTR from Dostal’s structure: trl(1) inlet temperature of the cold side (°C) trl(2) outlet temperature of the cold side (°C) trl(3) (not used) trl(4) inlet temperature of the hot side (°C) trl(5) real outlet temperature of the hot side (°C) trl(6) ideal outlet temperature of the hot side (°C) to a derived type structure that looks like: ltr.TinCold ltr.ToutCold ltr.TinHot ltr.ToutHot ltr.ToutHoti inlet temperature of the cold side (K) outlet temperature of the cold side (K) inlet temperature of the hot side (K) real outlet temperature of the hot side (K) ideal outlet temperature of the hot side (K) 27PDF Image | Supercritical Carbon Dioxide Cycle Analysis
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