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Gases & Vapores III

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Tópicos: Tabela de Vapor Saturado - Referência de Pressão | Tabela de Vapor Saturado - Referência de Temperatura |


1) Tabela de Vapor Saturado - Referência de Pressão

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Pressão abs Temp saturação Entalpia espec da água Entalpia
espec de vaporiz
Entalpia espec do vapor Volume espec da água Volume espec do vapor Entropia espec da água Entropia
espec de vaporiz
Entropia espec do vapor Calor espec vapor Calor espec vapor
pabs tsat hf hfg hg vf vg sf sfg sg cv cp
bar °C kJ/kg kJ/kg kJ/kg dm3/kg m3/kg kJ/kg K kJ/kg K kJ/kg K kJ/kg K kJ/kg K
1 99,6 417,5 2257,6 2675,2 1,043 1,694 1,303 6,056 7,359 1,525 2,043
2 120,2 504,8 2201,7 2706,6 1,060 0,886 1,530 5,597 7,127 1,577 2,127
3 133,6 561,6 2163,7 2725,3 1,073 0,606 1,672 5,320 6,992 1,616 2,195
4 143,6 604,9 2133,6 2738,6 1,083 0,462 1,777 5,119 6,896 1,651 2,256
5 151,9 640,4 2108,2 2748,7 1,092 0,375 1,861 4,960 6,821 1,682 2,312
6 158,9 670,7 2086,0 2756,7 1,100 0,316 1,932 4,829 6,760 1,710 2,365
7 165,0 697,4 2066,0 2763,4 1,107 0,273 1,993 4,715 6,708 1,736 2,415
8 170,4 721,3 2047,7 2768,9 1,114 0,240 2,046 4,616 6,663 1,762 2,464
9 175,4 743,0 2030,7 2773,7 1,120 0,215 2,095 4,527 6,622 1,785 2,511
10 179,9 762,9 2014,8 2777,8 1,126 0,194 2,139 4,447 6,586 1,808 2,557
11 184,1 781,4 1999,9 2781,3 1,131 0,177 2,179 4,374 6,553 1,830 2,602
12 188,0 798,7 1985,7 2784,4 1,137 0,163 2,217 4,306 6,523 1,852 2,646
13 191,6 815,0 1972,1 2787,1 1,142 0,151 2,252 4,243 6,495 1,873 2,689
14 195,1 830,3 1959,1 2789,5 1,147 0,141 2,284 4,184 6,468 1,893 2,732
15 198,3 844,9 1946,7 2791,5 1,152 0,132 2,315 4,129 6,444 1,912 2,775
16 201,4 858,8 1934,6 2793,4 1,157 0,124 2,344 4,077 6,421 1,931 2,816
17 204,3 872,0 1923,0 2795,0 1,162 0,117 2,372 4,027 6,399 1,950 2,858
18 207,2 884,7 1911,7 2796,4 1,166 0,110 2,398 3,980 6,378 1,969 2,899
19 209,8 897,0 1900,7 2797,7 1,170 0,105 2,423 3,935 6,358 1,987 2,940
pabs tsat hf hfg hg vf vg sf sfg sg cv cp
20 212,4 908,7 1890,0 2798,8 1,175 0,100 2,447 3,892 6,340 2,004 2,981
21 214,9 920,1 1879,6 2799,7 1,179 0,095 2,470 3,851 6,322 2,022 3,021
22 217,3 931,0 1869,5 2800,5 1,183 0,091 2,492 3,812 6,304 2,039 3,062
23 219,6 941,7 1859,5 2801,2 1,187 0,087 2,514 3,774 6,288 2,055 3,102
24 221,8 952,0 1849,8 2801,8 1,191 0,083 2,534 3,737 6,272 2,072 3,142
25 224,0 962,0 1840,2 2802,2 1,195 0,080 2,554 3,702 6,256 2,088 3,182
26 226,1 971,7 1830,9 2802,6 1,199 0,077 2,574 3,667 6,241 2,104 3,222
27 228,1 981,2 1821,7 2802,9 1,203 0,074 2,592 3,634 6,227 2,120 3,262
28 230,1 990,5 1812,6 2803,1 1,207 0,071 2,611 3,602 6,213 2,136 3,301
29 232,0 999,5 1803,7 2803,2 1,210 0,069 2,628 3,571 6,199 2,151 3,341
30 233,9 1008,3 1795,0 2803,3 1,214 0,067 2,645 3,540 6,186 2,166 3,381
31 235,7 1016,9 1786,3 2803,3 1,217 0,065 2,662 3,510 6,173 2,181 3,421
32 237,5 1025,4 1777,8 2803,2 1,221 0,062 2,679 3,482 6,160 2,196 3,461
33 239,2 1033,6 1769,4 2803,1 1,225 0,061 2,694 3,453 6,148 2,211 3,501
34 240,9 1041,7 1761,2 2802,9 1,229 0,059 2,710 3,426 6,136 2,226 3,541
35 242,6 1049,7 1753,0 2802,6 1,232 0,057 2,725 3,399 6,124 2,240 3,581
36 244,2 1057,5 1744,9 2802,3 1,236 0,055 2,740 3,373 6,113 2,254 3,621
37 245,8 1065,1 1736,9 2802,0 1,239 0,054 2,754 3,347 6,101 2,268 3,661
38 247,4 1072,6 1729,0 2801,6 1,242 0,052 2,769 3,322 6,090 2,282 3,702
39 248,9 1080,0 1721,1 2801,1 1,245 0,051 2,783 3,297 6,080 2,296 3,742
40 250,4 1087,3 1713,4 2800,7 1,249 0,050 2,796 3,273 6,069 2,310 3,783


2) Tabela de Vapor Saturado - Referência de Temperatura

(Topo | Fim pág)

Temp saturação Pressão abs Entalpia espec da água Entalpia
espec de vaporiz
Entalpia espec do vapor Volume espec da água Volume espec do vapor Entropia espec da água Entropia
espec de vaporiz
Entropia espec do vapor Calor espec vapor Calor espec vapor
tsat pabs hf hfg hg vf vg sf sfg sg cv cp
°C bar kJ/kg kJ/kg kJ/kg dm3/kg m3/kg kJ/kg K kJ/kg K kJ/kg K kJ/kg K kJ/kg K
100 1,01 419,10 2256,66 2675,76 1,0437 1,674 1,307 6,048 7,355 1,526 2,044
105 1,21 440,22 2243,39 2683,61 1,0477 1,420 1,363 5,933 7,296 1,538 2,062
110 1,43 461,37 2229,93 2691,31 1,0519 1,211 1,419 5,820 7,239 1,550 2,082
115 1,69 482,57 2216,28 2698,85 1,0562 1,037 1,474 5,710 7,183 1,562 2,103
120 1,98 503,81 2202,42 2706,23 1,0606 0,892 1,528 5,602 7,130 1,576 2,126
125 2,32 525,10 2188,33 2713,43 1,0652 0,771 1,582 5,496 7,078 1,590 2,150
130 2,70 546,44 2174,00 2720,44 1,0700 0,669 1,635 5,393 7,027 1,605 2,176
135 3,13 567,83 2159,43 2727,26 1,0750 0,582 1,687 5,291 6,978 1,621 2,203
140 3,61 589,28 2144,59 2733,87 1,0801 0,509 1,739 5,191 6,930 1,638 2,233
145 4,15 610,78 2129,47 2740,26 1,0853 0,446 1,791 5,093 6,884 1,656 2,265
150 4,76 632,35 2114,06 2746,41 1,0908 0,393 1,842 4,996 6,838 1,674 2,299
155 5,43 653,98 2098,34 2752,33 1,0964 0,347 1,893 4,901 6,794 1,694 2,335
160 6,18 675,69 2082,30 2757,99 1,1022 0,307 1,943 4,807 6,750 1,715 2,374
165 7,00 697,46 2065,91 2763,38 1,1082 0,273 1,993 4,715 6,708 1,736 2,415
170 7,91 719,32 2049,17 2768,49 1,1145 0,243 2,042 4,624 6,666 1,759 2,460
175 8,92 741,26 2032,05 2773,30 1,1209 0,217 2,091 4,534 6,625 1,784 2,507
180 10,02 763,28 2014,54 2777,82 1,1275 0,194 2,140 4,446 6,585 1,809 2,558
185 11,22 785,41 1996,61 2782,01 1,1344 0,174 2,188 4,358 6,546 1,835 2,612
190 12,54 807,63 1978,25 2785,88 1,1415 0,157 2,236 4,271 6,507 1,863 2,670
195 13,98 829,97 1959,43 2789,40 1,1489 0,141 2,284 4,185 6,469 1,892 2,731
tsat pabs hf hfg hg vf vg sf sfg sg cv cp
200 15,54 852,42 1940,14 2792,56 1,1565 0,127 2,331 4,100 6,431 1,923 2,797
205 17,23 874,99 1920,35 2795,34 1,16 0,115 2,378 4,016 6,394 1,954 2,867
210 19,06 897,70 1900,04 2797,74 1,1726 0,104 2,425 3,933 6,357 1,988 2,943
215 21,04 920,54 1879,19 2799,73 1,18 0,095 2,471 3,850 6,321 2,022 3,023
220 23,18 943,54 1857,76 2801,30 1,1900 0,086 2,518 3,767 6,285 2,058 3,109
225 25,48 966,70 1835,73 2802,43 1,20 0,078 2,564 3,685 6,249 2,096 3,201
230 27,95 990,04 1813,07 2803,10 1,2087 0,072 2,610 3,603 6,213 2,135 3,299
235 30,60 1013,55 1789,74 2803,30 1,22 0,065 2,656 3,522 6,178 2,175 3,405
240 33,45 1037,27 1765,72 2802,99 1,2291 0,060 2,701 3,441 6,142 2,217 3,519
245 36,49 1061,20 1740,96 2802,16 1,24 0,055 2,747 3,360 6,107 2,261 3,641
250 39,74 1085,35 1715,43 2800,78 1,2513 0,050 2,793 3,279 6,072 2,306 3,772
Referências
Bouché, Ch. Leitner, A. Sans, F. Dubbel - Manual da Construção de Máquinas. São Paulo: Hemus, 1979.
Cengel, Y. A. Michael A. B. Thermodynamics: An Engineering Approach. New York: McGraw-Hill, 2006.
Giek, Kurt. Manual de Fórmulas Técnicas. São Paulo: Hemus.
Kaviany, Massoud. Principles of Heat Transfer. USA: Wiley.
Rohsenow, W. M. Hartnett, J. R. Cho, Y. I. Handbook of Heat Transfer. McGraw-Hill, 1998.

Topo | Rev: Set/2018