Tablas Del Trabajo de NIST

8/17/2019 Tablas Del Trabajo de NIST.

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COMPONENTE N-HEXANO

Entalpía H = 0 at the normal boiling point for saturate li!ui"

Entropía S = 0 at the normal boiling point for saturated liquid.

#nforma$i%n e la &ase 'í!uia

(atos en Cur)a e *atura$i%n

Temperature Pressure Density Volume Internal Enthalpy Entropy Cv Cp Sound Joule- Viscosity Therm. Surf. Phase

Temperatura Críti$a +T$, ."/ &

Presi%n Críti$a +P$, 440.04 psia

(ensia Críti$a +($, 14,557 Lbm/Ft

Fa!tor "!#ntri!o 0.$%%

&unto de 'bulli!i(n )ormal 155.7*F

+omento ipolo 0.05 eb-e


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320.42 132.67 31.621 0.031625 9130.8 9197.8 13.115 47.161 62.124 1614.6 0.0025069 6.4209e-05 0.088713 0.00033012 liquid

340.42 162.23 30.582 0.032699 10370. 10455. 14.687 48.126 64.262 1452.7 0.0043853 5.8757e-05 0.086313 0.00026914 liquid

360.42 196.51 29.442 0.033965 11646. 11752. 16.266 49.106 66.899 1284.5 0.0070510 5.3521e-05 0.083903 0.00021100 liquid

380.42 236.03 28.160 0.035511 12966. 13099. 17.862 50.116 70.448 1107.2 0.011138 4.8377e-05 0.081400 0.00015610 liquid400.42 281.47 26.660 0.037509 14342. 14511. 19.492 51.187 75.975 916.21 0.018185 4.3143e-05 0.078649 0.00010502 liquid

420.42 333.69 24.767 0.040376 15806. 16021. 21.190 52.393 87.314 703.44 0.033073 3.7469e-05 0.075298 5.8745e-05 liquid

440.42 393.92 21.837 0.045793 17471. 17759. 23.096 54.011 136.33 452.08 0.082011 3.0199e-05 0.070069 1.9310e-05 liquid

#nforma$i%n e la &ase e apor

(atos en Cur)a e *atura$i%n

Temperature

(F

Pressure

(psia

Density

(l!m"ft#

Volume

(ft#"l!m

Internal

Ener$y

(%tu"l!-

mole

Enthalpy

(%tu"l!-

mole

Entropy

(%tu"l!-

mole&'

Cv

(%tu"l!-

mole&'

Cp

(%tu"l!-

mole&'

Sound

Spd.

(ft"s

Joule-

Thomson

(F"psia

Viscosity

(l!m"ft&s

Therm.

Cond.

("m&)

Phase

-139.58 0.00018523 4.6469e-06 2.1520e+05 2827.0 3463.1 23.012 22.842 24.830 448.05 4.7352 2.0538e-06 0.0052567 vapor

- 119.58 0.00 08 327 1 1 .96 62 e- 05 5 08 60 . 3 29 2.0 39 67 .8 2 1.554 2 3.65 5 25 .64 3 46 1.19 3 .7 253 2 .6110 e- 06 0 .0 05 82 01 v ap or

- 99 .5 76 0 .0 03 098 0 6 .90 91 e- 05 1 44 74 . 3 77 2.9 44 88 .4 2 0.431 2 4.44 7 26 .43 5 4 73.94 2 .9 764 2 .8 86 9e- 06 0 .0 06 40 71 v ap or

- 79 .5 76 0 .00 98 43 5 0.000 20 80 0 4 80 7.6 4 26 9.3 50 24 .5 1 9.582 2 5.23 4 27 .22 4 4 86.31 2 .4 101 3 .0 84 4e- 06 0 .0 07 02 12 v ap or

- 59 .5 76 0 .0 27 38 7 0.000 54 99 2 1 81 8.4 4 78 1.2 55 75 .9 1 8.963 2 6.03 2 28 .02 5 4 98.28 1 .9 745 3 .2 58 8e- 06 0 .0 07 66 55 v ap or

-39.576 0.068077 0. 0013025 767. 74 5308. 5 6142.6 18. 537 26.851 28. 850 509. 83 1.6346 3.4267e-06 0.0083435 vapor -19.576 0.15369 0. 0028093 355. 96 5851. 4 6724.4 18. 274 27.698 29. 706 520. 93 1.3663 3.5935e-06 0.0090581 vapor

0.42400 0.31942 0. 0055921 178. 82 6409. 7 7321.2 18. 149 28.578 30. 602 531. 51 1.1522 3.7609e-06 0.0098120 vapor

20.424 0.61801 0.010390 96. 251 6983. 5 7932.7 18. 144 29.494 31. 541 541. 49 0.98004 3.9298e-06 0.010607 vapor


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40.424 1. 1237 0.018186 54. 986 7572. 7 8558.7 18. 241 30.447 32. 527 550. 79 0.84053 4.1002e-06 0.011446 vapor

60.424 1. 9352 0.030234 33. 075 8177. 2 9198.6 18. 426 31.437 33. 561 559. 31 0.72682 4.2725e-06 0.012331 vapor

80.424 3. 1784 0.048062 20. 807 8796. 6 9851.9 18. 686 32.460 34. 643 566. 93 0.63366 4.4466e-06 0.013262 vapor

100. 42 5. 0067 0.073483 13. 609 9430. 7 10518. 19. 012 33.515 35. 774 573. 54 0.55701 4.6230e-06 0.014242 vapor 120. 42 7. 6016 0.10860 9.2079 10079. 11196. 19. 393 34.599 36. 954 579. 01 0.49374 4.8018e-06 0.015271 vapor

140. 42 11. 172 0.15583 6.4174 10741. 11885. 19. 823 35.708 38. 184 583. 21 0.44138 4.9834e-06 0.016351 vapor

160. 42 15. 951 0.21789 4.5895 11415. 12583. 20. 293 36.838 39. 464 586. 01 0.39800 5.1686e-06 0.017484 vapor

180. 42 22. 196 0.29790 3.3569 12102. 13291. 20. 798 37.986 40. 798 587. 27 0.36205 5.3579e-06 0.018671 vapor

200. 42 30. 185 0.39939 2.5038 12800. 14006. 21. 332 39.149 42. 192 586. 82 0.33235 5.5526e-06 0.019914 vapor

220. 42 40. 216 0.52649 1.8994 13508. 14727. 21. 888 40.325 43. 655 584. 49 0.30794 5.7538e-06 0.021216 vapor

240. 42 52. 604 0.68402 1.4619 14224. 15452. 22. 462 41.510 45. 201 580. 08 0.28811 5.9636e-06 0.022580 vapor

260. 42 67. 682 0.87785 1.1392 14948. 16178. 23. 049 42.705 46. 856 573. 35 0.27230 6.1844e-06 0.024010 vapor

280. 42 85. 801 1.1152 0.89666 15675. 16903. 23. 642 43.909 48. 654 564. 01 0.26017 6.4198e-06 0.025513 vapor

300. 42 107.33 1. 4056 0.71143 16404. 17622. 24. 236 45.122 50. 656 551. 72 0.25150 6.6746e-06 0.027099 vapor

320. 42 132.67 1. 7616 0.56766 17130. 18332. 24. 824 46.348 52. 958 536. 05 0.24630 6.9560e-06 0.028780 vapor

340. 42 162.23 2.2011 0.45432 17848. 19024. 25. 397 47.590 55. 731 516. 43 0.24477 7.2750e-06 0.030577 vapor

360. 42 196.51 2. 7509 0.36351 18548. 19688. 25. 943 48.858 59. 300 492. 14 0.24746 7.6493e-06 0.032524 vapor

380. 42 236.03 3. 4551 0.28942 19219. 20309. 26. 444 50.164 64. 353 462. 22 0.25539 8.1093e-06 0.034681 vapor

400. 42 281.47 4. 3943 0.22757 19835. 20857. 26. 870 51.533 72. 632 425. 36 0.27031 8.7155e-06 0.037162 vapor

420. 42 333.69 5. 7458 0.17404 20348. 21275. 27. 160 53.017 90. 054 379. 84 0.29469 9. 6112e-06 0.040239 vapor

440. 42 393.92 8. 0717 0.12389 20613. 21392. 27. 132 54.753 156.38 323. 22 0.32801 1.1304e-05 0.044836 vapor


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Tablas Del Trabajo de NIST