HEAT CAPACITY AND CALORIFIC INTENSITY CURVES 361 TABLE 3 POINTS FOR HEAT CAPACITY CURVES OF PKODUCTS OF COMBUSTION COMPUTATIONS MADE ON BASIS OF 100 VOLUMES OF GAS BURNED Values of Heat Capacity per gram molecule from Les Sources de L'Energie Calorifique by Damour, Carnot and Rengade, based on the work of Mallard and Le Chatelier. Refer to Table 7. HEAT CAPACITY OF PRODUCTS OF COMBUSTION. (Note Below) (1) Temperatures (2) (3) 400° (4) 800° (5) 1200° (6) 1600° (7) 2000° (8) 2400° (9) 2800° N2+ C02 H20 51.42 15.74 22.68 427 63 84 881 143 187 1370 245 315 1,887 364 462 2,431 501 630 3,005 657 819 3,607 832 1,035 60% air S~ 574 1211 1930 2,713 3,562 4,481 5474 Curve points N2 + C02 H2O 164.56 26.12 25.34 464 104 94 958 237 209 1489 406 351 2,050 603 516 2,641 832 703 3,265 1,091 915 3,920 1,380 1,156 80% air s — 662 1404 2246 3 169 4 176 5 271 6 456 Curve points N2 CO2 H20 177.70 36.50 28.20 501 140 104 1034 331 232 1608 568 391 2,213 843 574 2,852 1,162 783 3,526 1,524 1,048 4,232 1,929 1,287 100% air S A — 751 1597 2567 3 730 4 797 6 098 7448 Curve points 33=20% 32.85 93 192 29S 410 526 652 783 120% a:r £/!+# = 844 1789 2865 4,140 5,323 6,750 8,231 Curve points C=40% 65.70 185 383 595 819 1,055 1,304 1,565 140% air SA-j-C = 936 2172 3460 4,549 5,852 7,402 9,013 Curve points £> = 80% 131.40 371 765 1189 1,637 2,109 2,607 3,130 180% air 2A+I> = ..... 1122 2362 3756 5,367 6,906 8,705 10,578 Curve points $ = 160% 262.8C 742 1530 2378 3,274 4,218 5,214 6,160 260% air SA-j-# = 1493 3127 4945 7,004 9,015 11,212 13,608 Curve points -P = 240% 394.20 1113 2295 3567 4,911 6,327 7,821 340% air SA-fF = 1864 3892 6134 8,641 11,124 13,919 Curve points 0 = 320% 525.60 1484 3060 4756 6,548 8,436 ----- 420% air SA+£ = 2235 4657 7223 10,278 13,233 Curve points // = 400% 657 00 1853 3824 5946 8 187 500% air 2A + H-~ 2609 5421 8513 11 917 Curve points This computation has been carried out further than necessary in order to approximate the limits in regard to combustion conditions, both with excess and deficient air supply.