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A.1 Introduction Appendix A. CYCLES III Code Manual This Appendix is intended to expand upon David Legault’s SB thesis, which explains the operation of CYCLES II. Legault’s thesis is an excellent companion to CYCLES II, however, the changes in CYCLES III demand a short manual to assist in its use. A.2 Inputs and Outputs For the new user, the input is mostly self-explanatory. Comments identify what each input parameter is. The comments from the beginning of the input file, called HXdata.txt, are shown below: Main cycle input data for CYCLES III itables iprop icase itype Table trigger, if 0 old tables are used, if 1 new tables created Property trigger, if 0 tables are used, if 1 polynomials are used Case trigger: 0 runs a single operating point, 1 optimizes Cycle you are running: 0 for simple, 1 for recompression The following are data concerned with the working fluid ifluid mix ifltwo fracgas This is the first fluid, 0-CO2, 1-Ethane, 2-Helium IDs if there is a 2nd fluid, 0-pure, 1-2nd fluid exists IDs 2nd fluid, 0-He, 1-Air,2-Hydrogen,3-Nitrogen,4-Methane This is the mole fraction of the 2nd fluid(if applicable) It is recommended that tables are always used, as the same fluid will likely be used several times, and the calculations will be much faster than if the polynomials are used. CYCLES III should include tables with it. If not, or if a new fluid is needed, new tables are created by changing itables to 1 and running the code. The table generation subroutine will take considerably longer when mixtures are involved (especially air, which is a mixture of Nitrogen, Oxygen, and Argon). The tables consist of values for the thermal conductivity, density, enthalpy, viscosity, and specific heat over a temperature and pressure range that is defined by the user. The range and spacing of data point in the table are determined in createtables.txt, which looks like: 132PDF Image | Supercritical Carbon Dioxide Cycle Analysis
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