3.1 3.2 3.3EPR 3.4 3.5 3.6 3.7 3.8 P2 P2 P3 P3 P4 P6 P8 P10 P11 P12 P13 P15 P15 P16 P16 A1 A2 A3 Function P17 P17 P19 P29 1
2004 R404A 12 Microsoft Excel Excel Excel Excel97 No R 22-Ver2.xls HCFC CHClF2 () R 123-Ver2.xls HCFC CHCl2CF3 () 3 R 125-Ver2.xls HFC CHF2CF3 () 4 R 134a-Ver2.xls HFC CH2FCF3 () 5 R 143a-Ver2.xls HFC CF3CH3 () 6 R 32-Ver2.xls HFC CH2F2 () 7 R 404A-Ver2.xls HFC R 125/143a/134a (44/52/4mass%) () 8 R 407C-Ver2.xls HFC R 32/125/134a (23/25/52mass%) () 9 R 407E-Ver2.xls HFC R 32/125/134a (25/15/60mass%) () 10 R 410A-Ver2.xls HFC R 32/125 (50/50 mass%) () 11 R 410B-Ver2.xls HFC R 32/125 (45/55 mass%) () 12 R 507A-Ver2.xls HFC R 125/143a (50/50 mass%) () Excel CD Excel Excel (H) [ ][ ][ ] (M) (L) 2
Excel 3.1) 3.2) EPR 3.3) 3.4) p-h EPR 3.5) T- EPR 3.6) 3.1) R 22 Excel CD 3
3.2) R 22 E I E T E log(p) 1 p-h h T T-s 1 s 4
E8 n pv = E8 E E4 E5 EPR VALUE R 407C ( ) R 407C R 407C Excel Excel 5
3.3) EPR (EPR) 8 EPR R 22 2 COND 3 COMP EPR 6 5 7 EVAP 3 1 EVAP 8 4 9EPR EPR R407C EVAP EPR ERP EVAP EVAP EPR 6
EPR 1011 log(p) T 3 2 h 10 p-h 4 4 5 5 7 7 11 T-s s EPR EVAP EPR EPR EVAP EVAP EVAP E E4E5 VALUE EPR Excel 3.2) 7
3.4 12 R 22 COND EVAP CF 13 14 15 13 8
log(p) 4 5 6 3 8 11 h 14 p-h T 8 5 5 7 6 6 8 15 T-s 4 4 3 3 1 s 2 1 C5 C6C7 EPR VALUE Excel 3.2)3.3) 9
3.5 R22 16 R 22 EPR 3.2)3.4) Ctrl g Excel 10
R22 17 Ts R 22 T R123 EPR 3.2)3.4) Ctrl g Excel 11
3.7 R 22 0.00 18 R 22 12
3.8 R 22 0.00 60 19 R 22 13
R 22 Excel #VALUE Excel 18 Excel 18 18 14
Excel Excel Excel 5.1) R 22R 123 5.2) R 125R 134aR 143aR 32 15
5.3) R 404AR 407CR 407ER 410AR 410BR 507A 14 () (R22 ) (1975-11-19) () (1990-11-20) () R.Tillner-Roth, J. Li,A.Yokozeki, H.Sato, K.Watanabe Thermodynamic Properties of Pure and Blended Hydrofluorocarbon (HFC) Refrigerants HFC (1998-5-26) 16