ThermofluidStream.Idealized.Tests.Processes.PolytropicPerfectGas.Fixed3 differences from the reference file

startTime: 0

stopTime: 1

Simulated using tolerance: 1e-06

• sink5.inlet.state.p (javascript) (csv)
• sink5.inlet.state.T (javascript) (csv)
• sink4.inlet.state.p (javascript) (csv)
• sink4.inlet.state.T (javascript) (csv)
• P_n1.w_i_is (javascript) (csv)
• P_n1.w_i (javascript) (csv)
• P_n1.w_f (javascript) (csv)
• P_n1.w_exp_net (javascript) (csv)
• P_n1.w_exp (javascript) (csv)
• P_n1.w_amb (javascript) (csv)
• P_n1.pRatio (javascript) (csv)
• P_n1.outletSpec_actual (javascript) (csv)
• P_n1.log_pRatio (javascript) (csv)
• P_n1.log_TRatio_is (javascript) (csv)
• P_n1.log_TRatio (javascript) (csv)
• P_n1.h_out (javascript) (csv)
• P_n1.eta_is (javascript) (csv)
• P_n1.dT_is (javascript) (csv)
• P_n1.dT (javascript) (csv)
• P_n1.T_out_is (javascript) (csv)
• P_n1.TRatio_is (javascript) (csv)
• P_n1.TRatio (javascript) (csv)
• P_eta_pol1.w_i_is (javascript) (csv)
• P_eta_pol1.w_i (javascript) (csv)
• P_eta_pol1.w_f (javascript) (csv)
• P_eta_pol1.w_exp_net (javascript) (csv)
• P_eta_pol1.w_exp (javascript) (csv)
• P_eta_pol1.w_amb (javascript) (csv)
• P_eta_pol1.pRatio (javascript) (csv)
• P_eta_pol1.outletSpec_actual (javascript) (csv)
• P_eta_pol1.log_pRatio (javascript) (csv)
• P_eta_pol1.log_TRatio_is (javascript) (csv)
• P_eta_pol1.log_TRatio (javascript) (csv)
• P_eta_pol1.h_out (javascript) (csv)
• P_eta_pol1.eta_is (javascript) (csv)
• P_eta_pol1.dT_is (javascript) (csv)
• P_eta_pol1.dT (javascript) (csv)
• P_eta_pol1.T_out_is (javascript) (csv)
• P_eta_pol1.TRatio_is (javascript) (csv)
• P_eta_pol1.TRatio (javascript) (csv)