C s
|
ligning (α): VSP=(-49.869)+(1.1280)×T+(-1.0188E-3)×T2+(5.0169E-7)×T3+(-1.0246E-10)×T4{\ displaystyle C_ {P} = (- 49.869) + (1.1280) \ times T + (- 1.0188E-3) \ times T ^ {2} + (5.0169E-7) \ times T ^ {3} + ( - 1.0246E-10) \ times T ^ {4}}
Varmekapasiteten til gassen i J · mol -1 · K -1 og temperatur i Kelvin, fra 298 til 1500 K.
Beregnede verdier:
208,367 J · mol -1 · K -1 ved 25 ° C.
T (K) |
T (° C) |
C s (Jkmol×K){\ displaystyle ({\ tfrac {J} {kmol \ times K}})}
|
C s (Jkg×K){\ displaystyle ({\ tfrac {J} {kg \ times K}})}
|
---|
298 |
24,85 |
208 270 |
1,529 |
378 |
104,85 |
255,949 |
1.879 |
418 |
144,85 |
277,139 |
2,034 |
458 |
184,85 |
296.737 |
2 178 |
498 |
224,85 |
314.868 |
2 311 |
538 |
264,85 |
331 649 |
2,434 |
578 |
304,85 |
347,191 |
2.548 |
618 |
344,85 |
361 599 |
2.654 |
658 |
384,85 |
374,971 |
2 752 |
698 |
424,85 |
387.400 |
2.844 |
738 |
464,85 |
398,971 |
2 929 |
778 |
504,85 |
409 765 |
3,008 |
818 |
544,85 |
419 854 |
3.082 |
858 |
584,85 |
429,306 |
3 151 |
899 |
625,85 |
438 396 |
3,218 |
|
T (K) |
T (° C) |
C s (Jkmol×K){\ displaystyle ({\ tfrac {J} {kmol \ times K}})}
|
C s (Jkg×K){\ displaystyle ({\ tfrac {J} {kg \ times K}})}
|
---|
939 |
665,85 |
446.737 |
3 279 |
979 |
705,85 |
454.605 |
3,337 |
1.019 |
745,85 |
462.042 |
3 392 |
1.059 |
785,85 |
469 084 |
3.443 |
1.099 |
825,85 |
475 758 |
3 492 |
1.139 |
865,85 |
482089 |
3.539 |
1.179 |
905,85 |
488,093 |
3.583 |
1 219 |
945,85 |
493 781 |
3,625 |
1.259 |
985,85 |
499,155 |
3,664 |
1.299 |
1025,85 |
504,214 |
3,701 |
1339 |
1065,85 |
508 949 |
3.736 |
1.379 |
1 105,85 |
513 345 |
3,768 |
1.419 |
1 145,85 |
517 381 |
3 798 |
1.459 |
1.185,85 |
521 029 |
3.825 |
1500 |
1 226,85 |
524 331 |
3.849 |
|
ligning (γ): VSP=(-71,384)+(1.2266)×T+(-1.1733E-3)×T2+(6.0467E-7)×T3+(-1.2738E-10)×T4{\ displaystyle C_ {P} = (- 71.384) + (1.2266) \ times T + (- 1.1733E-3) \ times T ^ {2} + (6.0467E-7) \ times T ^ {3} + ( - 1.2738E-10) \ times T ^ {4}}
Varmekapasiteten til gassen i J · mol -1 · K -1 og temperatur i Kelvin, fra 298 til 1500 K.
Beregnede verdier:
205,047 J · mol -1 · K -1 ved 25 ° C.
T (K) |
T (° C) |
C s (Jkmol×K){\ displaystyle ({\ tfrac {J} {kmol \ times K}})}
|
C s (Jkg×K){\ displaystyle ({\ tfrac {J} {kg \ times K}})}
|
---|
298 |
24,85 |
204,946 |
1 504 |
378 |
104,85 |
254 683 |
1,869 |
418 |
144,85 |
276,604 |
2,030 |
458 |
184,85 |
296.770 |
2 178 |
498 |
224,85 |
315 325 |
2.315 |
538 |
264,85 |
332 410 |
2,440 |
578 |
304,85 |
348,155 |
2.556 |
618 |
344,85 |
362 683 |
2,662 |
658 |
384,85 |
376 108 |
2,761 |
698 |
424,85 |
388,540 |
2 852 |
738 |
464,85 |
400 076 |
2 937 |
778 |
504,85 |
410.809 |
3.015 |
818 |
544,85 |
420,822 |
3.089 |
858 |
584,85 |
430,193 |
3.158 |
899 |
625,85 |
439 201 |
3.224 |
|
T (K) |
T (° C) |
C s (Jkmol×K){\ displaystyle ({\ tfrac {J} {kmol \ times K}})}
|
C s (Jkg×K){\ displaystyle ({\ tfrac {J} {kg \ times K}})}
|
---|
939 |
665,85 |
447 469 |
3,285 |
979 |
705,85 |
455.276 |
3 342 |
1.019 |
745,85 |
462 667 |
3 396 |
1.059 |
785,85 |
469.679 |
3.448 |
1.099 |
825,85 |
476,339 |
3 496 |
1.139 |
865,85 |
482 671 |
3.543 |
1.179 |
905,85 |
488 685 |
3.587 |
1 219 |
945,85 |
494,389 |
3.629 |
1.259 |
985,85 |
499.780 |
3,669 |
1.299 |
1025,85 |
504,847 |
3,706 |
1339 |
1065,85 |
509,572 |
3.740 |
1.379 |
1 105,85 |
513 930 |
3,772 |
1.419 |
1 145,85 |
517 886 |
3,801 |
1.459 |
1.185,85 |
521.400 |
3 827 |
1500 |
1 226,85 |
524.491 |
3.850 |
|
|
---|