tablas de flujo compresible (version 1)

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TABLAS DE FLUJO COMPRESIBLE Ingrese el número de Mach M FLUJO ISENTRÓPICO Tabla A.1 Funciones para flujo isentrópico unidimensional para un gas perfecto [ Calor específico y peso molecular constantes ] k = 1.67 M M* 0 0 1 1 1 0 0.01 0.011554 56.23451 0.99986 0.99995 0.999967 43.28073 56.22981 0.012922 77.39395 0 #DIV/0! 1 1 1 #DIV/0! #DIV/0! 0 #DIV/0! 0.26 0.297065 2.261406 0.910745 0.967129 0.977855 1.831666 2.138641 0.321332 3.275358 0 #DIV/0! 1 1 1 #DIV/0! #DIV/0! 0 #DIV/0! 0 #DIV/0! 1 1 1 #DIV/0! #DIV/0! 0 #DIV/0! 4.32 1.853525 6.74486 0.000256 0.051969 0.137895 1.196519 0.048335 0.107736 2.139596 0 #DIV/0! 1 1 1 #DIV/0! #DIV/0! 0 #DIV/0! 0 #DIV/0! 1 1 1 #DIV/0! #DIV/0! 0 #DIV/0! 3.2 1.756585 3.41103 0.002 0.108433 0.225713 1.162936 0.083484 0.213033 2.079544 0 #DIV/0! 1 1 1 #DIV/0! #DIV/0! 0 #DIV/0! 0 #DIV/0! 1 1 1 #DIV/0! #DIV/0! 0 #DIV/0! 0 #DIV/0! 1 1 1 #DIV/0! #DIV/0! 0 #DIV/0! 0 #DIV/0! 1 1 1 #DIV/0! #DIV/0! 0 #DIV/0! 0 #DIV/0! 1 1 1 #DIV/0! #DIV/0! 0 #DIV/0! 0 #DIV/0! 1 1 1 #DIV/0! #DIV/0! 0 #DIV/0! 0 #DIV/0! 1 1 1 #DIV/0! #DIV/0! 0 #DIV/0! 0 #DIV/0! 1 1 1 #DIV/0! #DIV/0! 0 #DIV/0! 0 #DIV/0! 1 1 1 #DIV/0! #DIV/0! 0 #DIV/0! 0 #DIV/0! 1 1 1 #DIV/0! #DIV/0! 0 #DIV/0! * A A o p p o T To * I I * o A p A P w f I f

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Page 1: Tablas de Flujo Compresible (Version 1)

TABLAS DE FLUJO COMPRESIBLE

Ingrese el número de Mach M

FLUJO ISENTRÓPICO

Tabla A.1

Funciones para flujo isentrópico unidimensional para un gas perfecto[ Calor específico y peso molecular constantes ]

k = 1.67

M M*

0 0 1 1 1 0 0

0.01 0.011554 56.234506 0.9998601 0.99995 0.9999665 43.280734 56.2298107 0.01292199 77.3939498 0.0218191

0 #DIV/0! 1 1 1 #DIV/0! #DIV/0! 0 #DIV/0! 0

0.26 0.2970649 2.2614064 0.910745 0.9671294 0.9778555 1.8316664 2.13864099 0.32133166 3.27535799 0.5285036

0 #DIV/0! 1 1 1 #DIV/0! #DIV/0! 0 #DIV/0! 0

0 #DIV/0! 1 1 1 #DIV/0! #DIV/0! 0 #DIV/0! 0

4.32 1.8535246 6.7448603 0.0002556 0.0519689 0.1378948 1.1965186 0.04833527 0.10773558 2.13959641 0.0201937

0 #DIV/0! 1 1 1 #DIV/0! #DIV/0! 0 #DIV/0! 0

0 #DIV/0! 1 1 1 #DIV/0! #DIV/0! 0 #DIV/0! 0

3.2 1.7565849 3.4110304 0.0020003 0.1084326 0.2257133 1.1629357 0.08348385 0.21303283 2.07954387 0.0675329

0 #DIV/0! 1 1 1 #DIV/0! #DIV/0! 0 #DIV/0! 0

0 #DIV/0! 1 1 1 #DIV/0! #DIV/0! 0 #DIV/0! 0

0 #DIV/0! 1 1 1 #DIV/0! #DIV/0! 0 #DIV/0! 0

0 #DIV/0! 1 1 1 #DIV/0! #DIV/0! 0 #DIV/0! 0

0 #DIV/0! 1 1 1 #DIV/0! #DIV/0! 0 #DIV/0! 0

0 #DIV/0! 1 1 1 #DIV/0! #DIV/0! 0 #DIV/0! 0

0 #DIV/0! 1 1 1 #DIV/0! #DIV/0! 0 #DIV/0! 0

0 #DIV/0! 1 1 1 #DIV/0! #DIV/0! 0 #DIV/0! 0

0 #DIV/0! 1 1 1 #DIV/0! #DIV/0! 0 #DIV/0! 0

0 #DIV/0! 1 1 1 #DIV/0! #DIV/0! 0 #DIV/0! 0

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Page 2: Tablas de Flujo Compresible (Version 1)

ONDA DE CHOQUE NORMAL

Page 3: Tablas de Flujo Compresible (Version 1)

ONDA DE CHOQUE NORMAL

Choque normal unidimensional de un gas perfecto( Calor específico y peso molecular constantes )

k = 1.26

Mx My

1.00 1.00000 1.00000 1.00000 1.00000 1.0000000 1.8081161

1.01 0.99012 1.02241 1.01775 1.00458 0.9999987 1.8284661

1.02 0.98048 1.04505 1.03559 1.00914 0.9999899 1.8491887

1.03 0.97107 1.06791 1.05352 1.01366 0.9999664 1.8702769

1.04 0.96188 1.09099 1.07154 1.01815 0.9999217 1.8917242

1.05 0.95290 1.11429 1.08965 1.02261 0.9998497 1.9135245

1.06 0.94412 1.13782 1.10785 1.02705 0.9997447 1.9356720

1.07 0.93555 1.16157 1.12613 1.03147 0.9996016 1.9581614

1.08 0.92717 1.18554 1.14449 1.03587 0.9994154 1.9809876

1.09 0.91897 1.20974 1.16293 1.04025 0.9991816 2.0041461

1.10 0.91096 1.23416 1.18146 1.04461 0.9988961 2.0276322

1.11 0.90312 1.25880 1.20006 1.04895 0.9985551 2.0514420

1.12 0.89544 1.28367 1.21873 1.05328 0.9981550 2.0755713

1.13 0.88793 1.30876 1.23748 1.05760 0.9976925 2.1000167

1.14 0.88058 1.33407 1.25630 1.09027 0.9971647 2.1247745

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Page 4: Tablas de Flujo Compresible (Version 1)

FLUJO FANNO

Page 5: Tablas de Flujo Compresible (Version 1)

Tabla A.1

Funciones para flujo isentrópico unidimensional para un gas perfecto[ Calor específico y peso molecular constantes ]

k = 1.4

M M*

0 0 1 1 1 0 0

0.01 0.0109543 57.873843 0.99993 0.99995 0.99998 45.64948 57.8697917 0.01183145 84.5264124 0.017279

0.02 0.021908 28.94213 0.9997201 0.9998 0.99992 22.83364 28.9340278 0.02365864 42.2796859 0.0345517

0.03 0.0328604 19.300542 0.9993703 0.9995501 0.99982 15.232315 19.2883876 0.03547732 28.2047667 0.051812

0.04 0.0438108 14.481486 0.9988808 0.9992004 0.9996801 11.434618 14.4652783 0.04728323 21.1727976 0.0690537

0.05 0.0547586 11.59144 0.998252 0.9987511 0.9995002 9.1583705 11.5711816 0.05907215 16.9580069 0.0862705

0.06 0.0657031 9.66591 0.9974841 0.9982023 0.9992805 7.6428474 9.64159138 0.07083983 14.1518035 0.1034564

0.07 0.0766436 8.29153 0.9965775 0.9975542 0.999021 6.5620227 8.26314782 0.08258209 12.150505 0.1206051

0.08 0.0875796 7.26161 0.9955329 0.9968072 0.9987216 5.7528834 7.22917111 0.09429472 10.6522702 0.1377105

0.09 0.0985103 6.46134 0.9943506 0.9959615 0.9983826 5.1248666 6.42483914 0.10597357 9.48940896 0.1547666

0.1 0.1094351 5.82183 0.9930314 0.9950174 0.998004 4.6236343 5.78125867 0.1176145 8.56130711 0.1717673

0.11 0.1203534 5.29923 0.9915759 0.9939755 0.9975858 4.2146078 5.25458855 0.12921339 7.80393719 0.1887067

0.12 0.1312645 4.86432 0.989985 0.9928361 0.9971283 3.8747344 4.81560138 0.14076619 7.17461402 0.2055787

0.13 0.1421678 4.49686 0.9882594 0.9915997 0.9966314 3.5880546 4.44406282 0.15226884 6.64378612 0.2223775

0.14 0.1530626 4.18240 0.9864001 0.9902668 0.9960953 3.3431685 4.12551977 0.16371736 6.19034513 0.2390972

0.15 0.1639483 3.9103428 0.9844082 0.988838 0.9955202 3.1317161 3.84937332 0.17510778 5.79881141 0.2557321

0.16 0.1748242 3.6727386 0.9822845 0.9873138 0.9949061 2.9474274 3.60767429 0.18643621 5.45757509 0.2722764

0.17 0.1856898 3.463509 0.9800303 0.9856949 0.9942532 2.7855076 3.39434391 0.19769876 5.15775789 0.2887245

0.18 0.1965443 3.2779265 0.9776468 0.9839819 0.9935617 2.6422273 3.20465426 0.20889165 4.89245433 0.3050709

0.19 0.2073873 3.1122587 0.9751351 0.9821756 0.9928318 2.5146422 3.03487278 0.2200111 4.65621262 0.3213101

0.2 0.2182179 2.963520 0.9724967 0.9802767 0.9920635 2.4003968 2.88201343 0.23105343 4.4446712 0.3374366

0.21 0.2290356 2.8292936 0.9697328 0.9782859 0.9912571 2.2975841 2.74365895 0.24201499 4.25429915 0.3534451

0.22 0.2398399 2.7076021 0.966845 0.9762041 0.9904128 2.204644 2.61783159 0.2528922 4.08220746 0.3693305

0.23 0.25063 2.5968121 0.9638347 0.9740321 0.9895308 2.1202874 2.50289757 0.26368156 3.92600944 0.3850875

0.24 0.2614054 2.4955625 0.9607034 0.9717707 0.9886112 2.0434402 2.3974954 0.27437961 3.78371609 0.4007113

0.25 0.2721655 2.402710 0.9574528 0.969421 0.9876543 1.9732001 2.30048146 0.28498298 3.65365657 0.4161967

0.26 0.2829097 2.3172873 0.9540846 0.9669838 0.9866604 1.9088033 2.21088805 0.29548837 3.53441699 0.4315391

0.27 0.2936373 2.2384706 0.9506003 0.9644601 0.9856295 1.8495995 2.12789086 0.30589254 3.42479286 0.4467336

0.28 0.3043478 2.1655536 0.9470019 0.9618509 0.9845621 1.7950311 2.05078334 0.31619234 3.32375166 0.4617757

0.29 0.3150406 2.0979276 0.9432911 0.9591572 0.9834582 1.7446171 1.97895639 0.32638469 3.23040324 0.4766609

0.3 0.3257152 2.0350653 0.9394697 0.9563802 0.9823183 1.6979411 1.91188215 0.33646658 3.14397605 0.4913847

0.31 0.3363708 1.9765071 0.9355397 0.9535208 0.9811424 1.65464 1.84910086 0.34643511 3.06379803 0.505943

0.32 0.3470071 1.9218513 0.931503 0.9505802 0.979931 1.6143963 1.79021023 0.35628743 2.98928105 0.5203316

0.33 0.3576233 1.8707447 0.9273616 0.9475595 0.9786843 1.5769307 1.73485676 0.3660208 2.91990824 0.5345465

0.34 0.368219 1.8228758 0.9231175 0.94446 0.9774025 1.5419969 1.68272853 0.37563254 2.85522345 0.5485837

0.35 0.3787936 1.7779687 0.9187728 0.9412827 0.9760859 1.5093767 1.63354926 0.38512009 2.79482262 0.5624396

0.36 0.3893466 1.7357783 0.9143296 0.938029 0.9747349 1.4788761 1.5870734 0.39448094 2.73834652 0.5761104

0.37 0.3998773 1.696086 0.9097899 0.9347 0.9733497 1.4503221 1.54308193 0.40371271 2.68547471 0.5895928

0.38 0.4103854 1.6586962 0.9051561 0.931297 0.9719306 1.4235597 1.50137888 0.41281307 2.63592043 0.6028832

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Page 6: Tablas de Flujo Compresible (Version 1)

0.39 0.4208701 1.6234335 0.9004301 0.9278212 0.9704781 1.39845 1.46178841 0.42177981 2.58942629 0.6159784

0.379 0.4093356 1.6623367 0.9056236 0.9316406 0.9720741 1.4261594 1.50545136 0.41190901 2.64073412 0.6015629Tabla A.1

Funciones para flujo isentrópico unidimensional para un gas perfecto[ Calor específico y peso molecular constantes ]

k = 1.4

M M*

0.40 0.4313311 1.59014 0.8956144 0.924274 0.9689922 1.3748679 1.42415226 0.4306108 2.5457606 0.6288754

0.41 0.4417678 1.5586734 0.890711 0.9206567 0.9674735 1.3527003 1.38832759 0.439304 2.5047142 0.6415712

0.42 0.4521796 1.5289048 0.8857224 0.9169707 0.9659223 1.3318451 1.35418519 0.44785748 2.46609784 0.654063

0.43 0.4625662 1.5007175 0.8806507 0.9132171 0.9643388 1.3122095 1.32160787 0.45626939 2.42973982 0.6663479

0.44 0.4729269 1.4740054 0.8754982 0.9093975 0.9627234 1.2937092 1.29048909 0.46453796 2.39548401 0.6784236

0.45 0.4832614 1.4486718 0.8702674 0.9055132 0.9610764 1.2762675 1.2607318 0.47266155 2.36318814 0.6902875

0.46 0.4935691 1.4246285 0.8649605 0.9015656 0.9593983 1.259814 1.23224736 0.48063859 2.33272226 0.7019374

0.47 0.5038495 1.401795 0.8595798 0.897556 0.9576893 1.2442846 1.2049547 0.4884676 2.30396745 0.7133711

0.48 0.5141021 1.3800973 0.8541278 0.893486 0.9559498 1.2296205 1.1787795 0.49614722 2.27681466 0.7245866

0.49 0.5243266 1.3594677 0.8486068 0.8893569 0.9541803 1.2157674 1.15365352 0.50367615 2.25116373 0.735582

0.50 0.5345225 1.3398438 0.8430192 0.8851701 0.952381 1.2026756 1.12951397 0.51105322 2.22692247 0.7463557

0.51 0.5446892 1.3211681 0.8373673 0.8809272 0.9505523 1.1902992 1.10630299 0.51827732 2.20400589 0.756906

0.52 0.5548265 1.3033878 0.8316536 0.8766295 0.9486946 1.1785959 1.08396718 0.52534747 2.18233554 0.7672314

0.53 0.5649338 1.2864538 0.8258805 0.8722785 0.9468083 1.1675264 1.06245715 0.53226274 2.16183882 0.7773306

0.54 0.5750106 1.2703211 0.8200503 0.8678756 0.9448938 1.1570544 1.04172719 0.53902234 2.14244853 0.7872025

0.55 0.5850567 1.2549476 0.8141654 0.8634224 0.9429514 1.1471463 1.02173492 0.54562554 2.12410229 0.796846

0.56 0.5950716 1.2402944 0.8082282 0.8589203 0.9409816 1.1377708 1.00244097 0.5520717 2.1067422 0.8062602

0.57 0.6050549 1.2263255 0.8022411 0.8543707 0.9389848 1.1288988 0.98380875 0.55836028 2.09031436 0.8154442

0.58 0.6150061 1.2130072 0.7962065 0.8497752 0.9369612 1.1205031 0.96580418 0.56449084 2.0747686 0.8243974

0.59 0.624925 1.2003083 0.7901266 0.8451352 0.9349115 1.1125585 0.94839552 0.570463 2.06005811 0.8331193

0.60 0.6348111 1.1881995 0.784004 0.8404522 0.9328358 1.1050415 0.93155311 0.5762765 2.0461392 0.8416095

0.61 0.644664 1.1766537 0.7778408 0.8357277 0.9307347 1.0979298 0.91524926 0.58193114 2.03297102 0.8498677

0.62 0.6544834 1.1656455 0.7716394 0.8309631 0.9286086 1.091203 0.89945806 0.58742682 2.02051533 0.8578937

0.63 0.664269 1.1551511 0.7654022 0.8261598 0.9264578 1.0848416 0.88415525 0.59276352 2.00873633 0.8656876

0.64 0.6740204 1.1451483 0.7591314 0.8213195 0.9242828 1.0788275 0.86931808 0.59794129 1.99760042 0.8732493

0.65 0.6837372 1.1356162 0.7528294 0.8164434 0.9220839 1.0731437 0.85492522 0.60296028 1.98707606 0.8805792

0.66 0.6934191 1.1265352 0.7464983 0.8115332 0.9198617 1.0677742 0.8409566 0.60782071 1.97713361 0.8876775

0.67 0.7030659 1.1178871 0.7401404 0.8065902 0.9176164 1.0627039 0.82739338 0.61252289 1.96774518 0.8945447

0.68 0.7126771 1.1096546 0.7337579 0.8016158 0.9153486 1.0579186 0.81421782 0.61706718 1.95888454 0.9011813

0.69 0.7222525 1.1018216 0.727353 0.7966115 0.9130586 1.0534049 0.80141319 0.62145403 1.95052693 0.907588

0.70 0.7317917 1.0943727 0.7209279 0.7915788 0.9107468 1.0491504 0.78896375 0.62568398 1.94264902 0.9137655

0.71 0.7412946 1.0872936 0.7144847 0.786519 0.9084137 1.045143 0.77685463 0.62975762 1.93522877 0.9197148

0.72 0.7507607 1.0805709 0.7080255 0.7814336 0.9060597 1.0413715 0.76507177 0.63367562 1.92824537 0.9254367

0.73 0.7601899 1.0741918 0.7015524 0.7763239 0.9036852 1.0378254 0.75360192 0.6374387 1.92167915 0.9309324

0.74 0.7695818 1.0681443 0.6950676 0.7711914 0.9012906 1.0344944 0.7424325 0.64104768 1.91551146 0.9362031

0.75 0.7789362 1.0624171 0.6885729 0.7660374 0.8988764 1.0313692 0.73155164 0.64450341 1.90972467 0.9412499

0.76 0.7882528 1.0569994 0.6820705 0.7608632 0.8964429 1.0284407 0.72094808 0.64780684 1.90430208 0.9460743

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Page 7: Tablas de Flujo Compresible (Version 1)

0.77 0.7975315 1.0518812 0.6755622 0.7556703 0.8939906 1.0257002 0.71061114 0.65095894 1.89922781 0.9506777

0.78 0.8067719 1.0470528 0.66905 0.75046 0.8915199 1.0231398 0.7005307 0.65396076 1.89448683 0.9550617

0.79 0.8159738 1.0425053 0.6625359 0.7452336 0.8890311 1.0207517 0.69069714 0.65681342 1.89006484 0.9592278

Tabla A.1

Funciones para flujo isentrópico unidimensional para un gas perfecto[ Calor específico y peso molecular constantes ]

k = 1.4

M M*

0.80 0.825137 1.03823 0.6560216 0.7399924 0.8865248 1.0185285 0.68110132 0.65951808 1.88594828 0.96317770.81 0.8342613 1.0342189 0.6495091 0.7347377 0.8840013 1.0164633 0.67173458 0.66207595 1.88212422 0.96691330.82 0.8433465 1.0304643 0.6430001 0.7294708 0.8814611 1.0145494 0.66258864 0.6644883 1.87858039 0.97043640.83 0.8523924 1.0269589 0.6364964 0.7241929 0.8789045 1.0127805 0.65365565 0.66675645 1.87530509 0.97374880.84 0.8613988 1.0236958 0.6299998 0.7189053 0.876332 1.0111506 0.64492813 0.66888176 1.87228718 0.9768527

0.85 0.8703655 1.0206685 0.6235118 0.7136093 0.873744 1.0096541 0.63639893 0.67086565 1.86951604 0.979750.86 0.8792923 1.0178709 0.6170343 0.708306 0.8711408 1.0082853 0.62806125 0.67270956 1.86698154 0.98244290.87 0.8881791 1.0152969 0.6105688 0.7029967 0.868523 1.0070391 0.61990861 0.67441501 1.86467404 0.98493360.88 0.8970257 1.012941 0.6041169 0.6976825 0.8658908 1.0059105 0.61193481 0.67598352 1.86258429 0.98722430.89 0.9058319 1.0107981 0.5976802 0.6923646 0.8632448 1.0048947 0.60413394 0.67741668 1.86070351 0.9893173

0.90 0.9145976 1.0088629 0.5912601 0.6870442 0.8605852 1.0039873 0.59650033 0.67871609 1.85902326 0.9912150.91 0.9233227 1.0071307 0.5848581 0.6817223 0.8579125 1.0031838 0.58902859 0.6798834 1.85753551 0.99291980.92 0.932007 1.0055971 0.5784758 0.6764002 0.8552271 1.0024802 0.58171354 0.6809203 1.85623255 0.99443410.93 0.9406505 1.0042576 0.5721144 0.6710787 0.8525295 1.0018723 0.57455024 0.68182849 1.85510703 0.99576040.94 0.9492528 1.0031083 0.5657754 0.6657592 0.8498198 1.0013565 0.56753394 0.68260972 1.8541519 0.9969014

0.95 0.9578141 1.0021452 0.55946 0.6604425 0.8470987 1.000929 0.56066011 0.68326575 1.8533604 0.99785940.96 0.9663341 1.0013646 0.5531696 0.6551298 0.8443664 1.0005864 0.5539244 0.68379837 1.85272607 0.99863730.97 0.9748128 1.000763 0.5469053 0.649822 0.8416233 1.0003254 0.54732263 0.6842094 1.85224271 0.99923760.98 0.9832501 1.0003371 0.5406685 0.6445201 0.8388699 1.0001427 0.54085081 0.68450069 1.85190437 0.9996630.99 0.9916458 1.0000838 0.5344603 0.6392252 0.8361064 1.0000352 0.53450509 0.68467408 1.85170536 0.9999162

1.00 1 1 0.5282818 0.6339381 0.8333333 1 0.52828179 0.68473146 1.8516402 11.01 1.0083125 1.0000829 0.5221341 0.6286599 0.830551 1.0000343 0.52217736 0.68467471 1.85170364 0.99991711.02 1.0165832 1.0003297 0.5160183 0.6233913 0.8277598 1.0001353 0.5161884 0.68450576 1.85189065 0.99967041.03 1.0248122 1.000738 0.5099353 0.6181334 0.82496 1.0003004 0.51031165 0.68422652 1.85219638 0.99926261.04 1.0329993 1.0013052 0.5038863 0.612887 0.8221521 1.0005271 0.50454394 0.68383892 1.85261617 0.9986965

1.05 1.0411446 1.0020291 0.4978721 0.6076529 0.8193363 1.000813 0.49888227 0.68334491 1.85314556 0.99797511.06 1.0492478 1.0029074 0.4918936 0.6024319 0.8165132 1.0011558 0.49332371 0.68274645 1.85378024 0.9971011.07 1.0573092 1.0039381 0.4859517 0.597225 0.8136829 1.0015532 0.48786547 0.6820455 1.85451609 0.99607741.08 1.0653285 1.0051192 0.4800474 0.5920328 0.8108459 1.002003 0.48250483 0.68124403 1.85534912 0.99490691.09 1.0733058 1.0064489 0.4741813 0.5868562 0.8080025 1.0025034 0.47723919 0.680344 1.85627552 0.9935924

1.10 1.081241 1.0079253 0.4683542 0.5816959 0.805153 1.0030521 0.47206606 0.6793474 1.85729158 0.9921371.11 1.0891342 1.0095469 0.4625669 0.5765527 0.8022978 1.0036473 0.46698301 0.6782562 1.85839378 0.99054341.12 1.0969853 1.0113121 0.4568201 0.5714272 0.7994372 1.0042873 0.4619877 0.67707237 1.85957869 0.98881451.13 1.1047944 1.0132193 0.4511145 0.5663201 0.7965716 1.0049701 0.45707789 0.67579791 1.86084303 0.98695321.14 1.1125614 1.0152671 0.4454507 0.5612322 0.7937012 1.0056941 0.45225141 0.67443478 1.86218362 0.9849625

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1.15 1.1202864 1.0174543 0.4398292 0.5561641 0.7908264 1.0064576 0.44750615 0.67298496 1.86359742 0.98284511.16 1.1279693 1.0197796 0.4342508 0.5511163 0.7879476 1.0072591 0.44284009 0.67145041 1.86508148 0.9806041.17 1.1356102 1.0222419 0.4287158 0.5460896 0.7850649 1.008097 0.43825127 0.6698331 1.86663297 0.9782421.18 1.1432091 1.02484 0.4232249 0.5410846 0.7821788 1.0089699 0.43373781 0.66813498 1.86824914 0.97576211.19 1.150766 1.0275729 0.4177785 0.5361017 0.7792896 1.0098762 0.42929788 0.66635801 1.86992737 0.9731669

Tabla A.1

Funciones para flujo isentrópico unidimensional para un gas perfecto[ Calor específico y peso molecular constantes ]

k = 1.4

M M*

1.20 1.158281 1.0304398 0.412377 0.5311416 0.7763975 1.0108147 0.4249297 0.66450412 1.8716651 0.97045951.21 1.1657541 1.0334395 0.407021 0.5262048 0.7735029 1.011784 0.42063157 0.66257524 1.87345988 0.96764251.22 1.1731854 1.0365715 0.4017107 0.5212919 0.770606 1.0127828 0.41640183 0.6605733 1.87530934 0.96471881.23 1.1805749 1.0398348 0.3964465 0.5164033 0.7677072 1.0138099 0.41223888 0.6585002 1.8772112 0.96169121.24 1.1879226 1.0432289 0.3912288 0.5115395 0.7648067 1.0148641 0.40814117 0.65635785 1.87916324 0.9585624

1.25 1.1952286 1.0467529 0.3860579 0.506701 0.7619048 1.0159443 0.4041072 0.65414812 1.88116334 0.95533531.26 1.202493 1.0504064 0.380934 0.5018882 0.7590018 1.0170493 0.40013552 0.65187288 1.88320944 0.95201251.27 1.2097158 1.0541888 0.3758575 0.4971016 0.7560979 1.0181781 0.39622472 0.64953399 1.88529955 0.94859671.28 1.2168972 1.0580996 0.3708285 0.4923415 0.7531935 1.0193296 0.39237343 0.6471333 1.88743175 0.94509071.29 1.2240371 1.0621383 0.3658472 0.4876085 0.7502889 1.0205029 0.38858032 0.64467262 1.8896042 0.941497

1.30 1.2311357 1.0663045 0.3609139 0.4829028 0.7473842 1.0216969 0.38484412 0.64215376 1.89181509 0.93781841.31 1.238193 1.070598 0.3560287 0.4782248 0.7444797 1.0229108 0.38116357 0.63957851 1.8940627 0.93405741.32 1.2452091 1.0750183 0.3511917 0.473575 0.7415757 1.0241435 0.37753748 0.63694865 1.89634536 0.93021671.33 1.2521842 1.0795653 0.346403 0.4689535 0.7386725 1.0253944 0.37396467 0.63426592 1.89866144 0.92629881.34 1.2591183 1.0842386 0.3416628 0.4643607 0.7357702 1.0266624 0.370444 0.63153207 1.9010094 0.9223062

1.35 1.2660114 1.0890382 0.3369711 0.459797 0.7328692 1.0279469 0.36697436 0.6287488 1.90338772 0.91824141.36 1.2728638 1.0939639 0.3323279 0.4552626 0.7299696 1.0292469 0.36355469 0.62591781 1.90579494 0.9141071.37 1.2796754 1.0990155 0.3277333 0.4507578 0.7270718 1.0305618 0.36018394 0.62304078 1.90822965 0.90990531.38 1.2864465 1.104193 0.3231872 0.4462828 0.7241759 1.0318908 0.3568611 0.62011935 1.91069048 0.90563881.39 1.2931771 1.1094964 0.3186898 0.4418379 0.7212822 1.0332332 0.35358518 0.61715517 1.91317613 0.9013098

1.40 1.2998674 1.1149257 0.3142409 0.4374233 0.7183908 1.0345883 0.35035523 0.61414985 1.91568531 0.89692071.41 1.3065174 1.1204809 0.3098405 0.4330392 0.7155021 1.0359555 0.34717032 0.61110496 1.91821679 0.89247391.42 1.3131272 1.1261621 0.3054885 0.4286859 0.7126162 1.037334 0.34402955 0.60802209 1.92076938 0.88797161.43 1.3196971 1.1319695 0.3011848 0.4243634 0.7097333 1.0387234 0.34093203 0.60490277 1.92334193 0.88341611.44 1.326227 1.137903 0.2969294 0.420072 0.7068537 1.0401229 0.33787692 0.60174852 1.92593331 0.8788095

1.45 1.3327172 1.143963 0.2927222 0.4158119 0.7039775 1.041532 0.33486337 0.59856085 1.92854246 0.87415421.46 1.3391678 1.1501496 0.288563 0.4115831 0.7011049 1.0429501 0.33189058 0.59534123 1.93116833 0.86945211.47 1.3455789 1.156463 0.2844516 0.4073859 0.6982363 1.0443767 0.32895775 0.59209111 1.93380992 0.86470561.48 1.3519506 1.1629035 0.2803879 0.4032203 0.6953716 1.0458113 0.32606413 0.58881192 1.93646623 0.85991661.49 1.3582831 1.1694714 0.2763718 0.3990864 0.6925112 1.0472533 0.32320896 0.58550507 1.93913634 0.8550872

1.50 1.3645765 1.1761671 0.2724031 0.3949844 0.6896552 1.0487023 0.32039151 0.58217194 1.94181932 0.85021941.51 1.3708309 1.1829907 0.2684815 0.3909144 0.6868038 1.0501577 0.31761108 0.57881389 1.94451431 0.84531521.52 1.3770466 1.1899428 0.2646068 0.3868763 0.6839571 1.0516192 0.31486697 0.57543225 1.94722043 0.8403765

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1.53 1.3832236 1.1970237 0.2607789 0.3828704 0.6811154 1.0530863 0.31215851 0.57202833 1.94993686 0.83540541.54 1.3893622 1.2042338 0.2569975 0.3788965 0.6782788 1.0545584 0.30948504 0.56860342 1.95266282 0.8304035

1.55 1.3954623 1.2115736 0.2532623 0.3749548 0.6754475 1.0560354 0.30684592 0.56515878 1.95539751 0.82537291.56 1.4015243 1.2190435 0.2495731 0.3710454 0.6726216 1.0575166 0.30424053 0.56169566 1.9581402 0.82031521.57 1.4075482 1.2266441 0.2459297 0.3671682 0.6698013 1.0590017 0.30166826 0.55821525 1.96089017 0.81523241.58 1.4135343 1.2343759 0.2423318 0.3633232 0.6669868 1.0604904 0.29912851 0.55471877 1.9636467 0.8101261.59 1.4194826 1.2422393 0.238779 0.3595105 0.6641782 1.0619823 0.2966207 0.55120737 1.96640914 0.8049979

Tabla A.1

Funciones para flujo isentrópico unidimensional para un gas perfecto[ Calor específico y peso molecular constantes ]

k = 1.4

M M*

1.6 1.4253933 1.250235 0.2352712 0.35573 0.6613757 1.063477 0.29414426 0.5476822 1.96917681 0.79984961.61 1.4312666 1.2583636 0.2318079 0.3519818 0.6585793 1.0649742 0.29169866 0.54414438 1.9719491 0.79468291.62 1.4371027 1.2666256 0.228389 0.3482658 0.6557893 1.0664736 0.28928333 0.540595 1.97472538 0.78949931.63 1.4429017 1.2750217 0.225014 0.344582 0.6530058 1.0679748 0.28689777 0.53703515 1.97750507 0.78430041.64 1.4486638 1.2835525 0.2216827 0.3409303 0.6502289 1.0694775 0.28454145 0.53346586 1.9802876 0.7790877

1.65 1.4543891 1.2922188 0.2183948 0.3373108 0.6474587 1.0709815 0.28221387 0.52988817 1.98307241 0.77386281.66 1.4600778 1.3010212 0.2151499 0.3337233 0.6446954 1.0724864 0.27991455 0.52630308 1.98585897 0.7686271.67 1.4657302 1.3099604 0.2119476 0.3301678 0.6419392 1.073992 0.277643 0.52271158 1.98864676 0.76338191.68 1.4713463 1.3190371 0.2087877 0.3266442 0.63919 1.075498 0.27539875 0.51911461 1.99143528 0.75812881.69 1.4769263 1.3282522 0.2056698 0.3231525 0.6364481 1.0770041 0.27318136 0.51551312 1.99422405 0.7528691

1.7 1.4824704 1.3376064 0.2025935 0.3196925 0.6337136 1.0785101 0.27099036 0.51190803 1.99701261 0.74760411.71 1.4879789 1.3471004 0.1995585 0.3162643 0.6309865 1.0800157 0.26882533 0.50830022 1.9998005 0.74233511.72 1.4934517 1.3567352 0.1965644 0.3128676 0.628267 1.0815207 0.26668583 0.50469057 2.0025873 0.73706351.73 1.4988892 1.3665115 0.1936108 0.3095024 0.6255552 1.083025 0.26457145 0.50107992 2.00537257 0.73179041.74 1.5042915 1.3764301 0.1906975 0.3061686 0.6228512 1.0845281 0.26248177 0.4974691 2.00815591 0.7265171

1.75 1.5096588 1.386492 0.1878239 0.3028661 0.620155 1.0860301 0.26041641 0.49385891 2.01093694 0.72124471.76 1.5149913 1.3966981 0.1849898 0.2995948 0.6174669 1.0875305 0.25837497 0.49025015 2.01371527 0.71597431.77 1.5202891 1.4070492 0.1821948 0.2963544 0.6147869 1.0890294 0.25635706 0.48664358 2.01649054 0.71070721.78 1.5255524 1.4175462 0.1794385 0.293145 0.612115 1.0905263 0.25436231 0.48303994 2.01926239 0.70544441.79 1.5307814 1.4281902 0.1767204 0.2899664 0.6094514 1.0920213 0.25239036 0.47943996 2.02203049 0.7001868

1.8 1.5359763 1.4389821 0.1740403 0.2868184 0.6067961 1.093514 0.25044084 0.47584433 2.02479451 0.69493571.81 1.5411373 1.4499227 0.1713977 0.2837009 0.6041493 1.0950044 0.24851341 0.47225375 2.02755413 0.68969191.82 1.5462645 1.4610133 0.1687922 0.2806137 0.601511 1.0964922 0.24660772 0.46866888 2.03030904 0.68445651.83 1.5513582 1.4722547 0.1662236 0.2775568 0.5988813 1.0979773 0.24472343 0.46509037 2.03305896 0.67923031.84 1.5564185 1.4836479 0.1636913 0.2745299 0.5962603 1.0994596 0.24286021 0.46151883 2.03580359 0.6740144

1.85 1.5614455 1.4951941 0.161195 0.2715329 0.593648 1.1009389 0.24101775 0.45795489 2.03854267 0.66880951.86 1.5664396 1.5068943 0.1587342 0.2685656 0.5910445 1.102415 0.23919572 0.45439913 2.04127593 0.66361661.87 1.5714008 1.5187496 0.1563087 0.2656279 0.5884499 1.1038879 0.23739382 0.45085212 2.04400312 0.65843641.88 1.5763294 1.530761 0.153918 0.2627196 0.5858643 1.1053573 0.23561174 0.44731442 2.04672399 0.65326991.89 1.5812255 1.5429297 0.1515618 0.2598406 0.5832876 1.1068232 0.23384918 0.44378656 2.04943831 0.6481177

1.9 1.5860894 1.5552568 0.1492396 0.2569905 0.5807201 1.1082854 0.23210585 0.44026907 2.05214585 0.6429806

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1.91 1.5909211 1.5677434 0.146951 0.2541694 0.5781617 1.1097439 0.23038147 0.43676245 2.0548464 0.63785951.92 1.5957209 1.5803908 0.1446957 0.2513769 0.5756125 1.1111985 0.22867576 0.43326717 2.05753974 0.63275491.93 1.600489 1.5932001 0.1424733 0.248613 0.5730725 1.112649 0.22698843 0.42978373 2.06022568 0.62766761.94 1.6052256 1.6061724 0.1402833 0.2458774 0.5705418 1.1140955 0.22531923 0.42631255 2.06290402 0.6225982

1.95 1.6099308 1.619309 0.1381255 0.24317 0.5680204 1.1155378 0.22366789 0.4228541 2.06557457 0.61754731.96 1.6146049 1.6326112 0.1359994 0.2404905 0.5655085 1.1169757 0.22203414 0.41940877 2.06823717 0.61251571.97 1.619248 1.6460801 0.1339046 0.2378387 0.563006 1.1184093 0.22041774 0.415977 2.07089163 0.60750391.98 1.6238602 1.659717 0.1318408 0.2352146 0.560513 1.1198384 0.21881844 0.41255916 2.07353779 0.60251241.98 1.624779 1.6624647 0.1314317 0.234693 0.5600155 1.1201237 0.2185006 0.4118773 2.07406601 0.6015165

Tabla A.1

Funciones para flujo isentrópico unidimensional para un gas perfecto[ Calor específico y peso molecular constantes ]

k = 1.4

M M*

2.00 1.6329932 1.6875 0.1278045 0.2300481 0.5555556 1.1226828 0.21567014 0.40576679 2.0788046 0.59259262.01 1.6375142 1.7016487 0.1258313 0.2275055 0.5530912 1.124098 0.21412067 0.40239297 2.08142496 0.58766542.02 1.6420051 1.7159705 0.1238875 0.2249897 0.5506365 1.1255083 0.21258734 0.39903451 2.08403643 0.58276062.03 1.6464662 1.7304669 0.1219728 0.2225004 0.5481915 1.1269138 0.21106994 0.39569174 2.08663888 0.57787872.04 1.6508976 1.7451391 0.1200868 0.2200375 0.5457562 1.1283143 0.20956822 0.39236496 2.08923218 0.5730202

2.05 1.6552995 1.7599886 0.1182292 0.2176008 0.5433306 1.1297099 0.20808199 0.38905447 2.09181622 0.56818552.06 1.659672 1.7750168 0.1163995 0.21519 0.5409148 1.1311004 0.20661102 0.38576056 2.09439089 0.5633752.07 1.6640155 1.7902249 0.1145974 0.2128051 0.5385088 1.1324857 0.20515509 0.38248348 2.09695606 0.5585892.08 1.6683299 1.8056145 0.1128225 0.2104456 0.5361125 1.1338659 0.20371402 0.37922351 2.09951164 0.55382812.09 1.6726156 1.8211869 0.1110746 0.2081116 0.5337262 1.1352408 0.20228758 0.37598088 2.10205752 0.5490925

2.10 1.6768728 1.8369436 0.1093532 0.2058026 0.5313496 1.1366105 0.20087559 0.37275584 2.10459362 0.54438252.11 1.6811015 1.8528861 0.1076579 0.2035187 0.528983 1.1379748 0.19947784 0.3695486 2.10711985 0.53969862.12 1.685302 1.8690158 0.1059885 0.2012594 0.5266262 1.1393337 0.19809415 0.36635938 2.10963611 0.5350412.13 1.6894744 1.8853341 0.1043445 0.1990247 0.5242794 1.1406872 0.19672432 0.36318838 2.11214233 0.530412.14 1.693619 1.9018427 0.1027257 0.1968143 0.5219425 1.1420353 0.19536817 0.36003579 2.11463843 0.5258058

2.15 1.6977359 1.918543 0.1011317 0.194628 0.5196155 1.1433778 0.19402551 0.35690179 2.11712434 0.52122892.16 1.7018253 1.9354366 0.0995621 0.1924655 0.5172985 1.1447148 0.19269618 0.35378656 2.11959999 0.51667932.17 1.7058873 1.952525 0.0980167 0.1903268 0.5149914 1.1460463 0.19137998 0.35069024 2.12206533 0.51215732.18 1.7099223 1.9698097 0.096495 0.1882115 0.5126943 1.1473721 0.19007676 0.347613 2.12452027 0.50766332.19 1.7139302 1.9872924 0.0949968 0.1861195 0.5104072 1.1486923 0.18878633 0.34455497 2.12696479 0.5031972

2.20 1.7179114 2.0049745 0.0935217 0.1840506 0.5081301 1.1500068 0.18750853 0.34151628 2.12939881 0.49875942.21 1.7218659 2.0228579 0.0920693 0.1820045 0.505863 1.1513156 0.1862432 0.33849707 2.13182229 0.49435012.22 1.725794 2.0409439 0.0906395 0.1799811 0.5036058 1.1526187 0.18499017 0.33549744 2.13423518 0.48996942.23 1.7296959 2.0592344 0.0892318 0.1779801 0.5013587 1.1539161 0.18374929 0.3325175 2.13663744 0.48561742.24 1.7335717 2.0777309 0.087846 0.1760013 0.4991215 1.1552077 0.1825204 0.32955734 2.13902904 0.4812943

2.25 1.7374215 2.096435 0.0864817 0.1740445 0.4968944 1.1564935 0.18130334 0.32661706 2.14140993 0.47700022.26 1.7412456 2.1153486 0.0851387 0.1721095 0.4946773 1.1577736 0.18009796 0.32369674 2.14378009 0.47273532.27 1.7450442 2.1344733 0.0838165 0.1701962 0.4924701 1.1590478 0.17890412 0.32079646 2.14613948 0.46849972.28 1.7488173 2.1538107 0.082515 0.1683042 0.490273 1.1603162 0.17772167 0.31791627 2.14848807 0.46429342.29 1.7525653 2.1733626 0.0812338 0.1664334 0.4880858 1.1615787 0.17655047 0.31505624 2.15082585 0.4601165

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Page 11: Tablas de Flujo Compresible (Version 1)

2.30 1.7562882 2.1931308 0.0799726 0.1645836 0.4859086 1.1628354 0.17539037 0.31221642 2.15315278 0.45596922.31 1.7599862 2.213117 0.0787311 0.1627546 0.4837414 1.1640862 0.17424123 0.30939686 2.15546885 0.45185142.32 1.7636595 2.233323 0.0775091 0.1609462 0.4815842 1.1653312 0.17310292 0.3065976 2.15777404 0.44776332.33 1.7673082 2.2537505 0.0763063 0.1591581 0.4794369 1.1665702 0.17197531 0.30381866 2.16006834 0.44370482.34 1.7709326 2.2744014 0.0751223 0.1573902 0.4772996 1.1678034 0.17085825 0.30106008 2.16235174 0.4396761

2.35 1.7745328 2.2952774 0.0739569 0.1556423 0.4751722 1.1690307 0.16975162 0.29832187 2.16462422 0.43567722.36 1.7781089 2.3163805 0.0728098 0.1539142 0.4730548 1.1702521 0.1686553 0.29560405 2.16688578 0.4317082.37 1.7816611 2.3377124 0.0716808 0.1522056 0.4709473 1.1714675 0.16756915 0.29290663 2.16913641 0.42776862.38 1.7851897 2.359275 0.0705696 0.1505164 0.4688496 1.1726771 0.16649304 0.2902296 2.1713761 0.4238592.39 1.7886947 2.3810702 0.0694758 0.1488464 0.4667619 1.1738808 0.16542687 0.28757298 2.17360487 0.4199792

Tabla A.1

Funciones para flujo isentrópico unidimensional para un gas perfecto[ Calor específico y peso molecular constantes ]

k = 1.4

M M*

2.4 1.7921763 2.4030999 0.0683994 0.1471954 0.464684 1.1750786 0.1643705 0.28493674 2.1758227 0.41612922.41 1.7956347 2.4253659 0.0673399 0.1455632 0.462616 1.1762704 0.16332383 0.28232089 2.1780296 0.41230892.42 1.79907 2.4478702 0.0662971 0.1439496 0.4605578 1.1774564 0.16228672 0.27972539 2.18022558 0.40851842.43 1.8024825 2.4706148 0.0652708 0.1423544 0.4585095 1.1786365 0.16125907 0.27715023 2.18241063 0.40475762.44 1.8058722 2.4936015 0.0642608 0.1407774 0.4564709 1.1798106 0.16024076 0.27459538 2.18458477 0.4010264

2.45 1.8092393 2.5168324 0.0632667 0.1392184 0.4544422 1.1809789 0.15923169 0.27206081 2.18674801 0.39732482.46 1.812584 2.5403094 0.0622884 0.1376772 0.4524232 1.1821413 0.15823173 0.26954648 2.18890035 0.39365282.47 1.8159065 2.5640345 0.0613255 0.1361537 0.4504139 1.1832978 0.15724079 0.26705236 2.19104182 0.39001042.48 1.8192068 2.5880098 0.060378 0.1346477 0.4484144 1.1844485 0.15625875 0.26457839 2.19317241 0.38639732.49 1.8224853 2.6122372 0.0594454 0.1331589 0.4464246 1.1855933 0.15528552 0.26212454 2.19529216 0.3828136

2.5 1.8257419 2.6367188 0.0585277 0.1316872 0.4444444 1.1867322 0.15432099 0.25969074 2.19740106 0.37925932.51 1.8289768 2.6614566 0.0576245 0.1302325 0.442474 1.1878653 0.15336505 0.25727696 2.19949915 0.37573412.52 1.8321903 2.6864528 0.0567356 0.1287944 0.4405131 1.1889926 0.15241761 0.25488312 2.20158644 0.37223812.53 1.8353825 2.7117093 0.0558609 0.1273729 0.4385619 1.190114 0.15147856 0.25250916 2.20366295 0.36877112.54 1.8385534 2.7372284 0.0550001 0.1259678 0.4366202 1.1912297 0.15054782 0.25015503 2.20572871 0.365333

2.55 1.8417034 2.7630121 0.054153 0.1245789 0.4346881 1.1923395 0.14962528 0.24782065 2.20778373 0.36192392.56 1.8448324 2.7890626 0.0533193 0.123206 0.4327655 1.1934435 0.14871084 0.24550595 2.20982804 0.35854342.57 1.8479408 2.815382 0.0524989 0.1218489 0.4308525 1.1945418 0.14780443 0.24321085 2.21186167 0.35519162.58 1.8510285 2.8419725 0.0516915 0.1205075 0.4289489 1.1956344 0.14690593 0.24093529 2.21388464 0.35186832.59 1.8540958 2.8688362 0.050897 0.1191815 0.4270548 1.1967211 0.14601527 0.23867917 2.21589697 0.3485734

2.6 1.8571429 2.8959754 0.0501152 0.1178709 0.4251701 1.1978022 0.14513236 0.23644243 2.2178987 0.34530682.61 1.8601697 2.9233922 0.0493458 0.1165755 0.4232948 1.1988775 0.1442571 0.23422497 2.21988986 0.34206842.62 1.8631766 2.9510889 0.0485886 0.115295 0.4214288 1.1999472 0.14338941 0.23202671 2.22187046 0.3388582.63 1.8661637 2.9790678 0.0478436 0.1140294 0.4195722 1.2010112 0.14252921 0.22984756 2.22384056 0.33567552.64 1.869131 3.007331 0.0471103 0.1127784 0.4177249 1.2020695 0.1416764 0.22768742 2.22580017 0.3325208

2.65 1.8720787 3.0358809 0.0463888 0.1115419 0.4158869 1.2031221 0.14083091 0.22554622 2.22774933 0.32939372.66 1.875007 3.0647198 0.0456788 0.1103197 0.4140581 1.2041692 0.13999266 0.22342384 2.22968807 0.32629412.67 1.8779161 3.0938499 0.0449801 0.1091117 0.4122385 1.2052106 0.13916156 0.2213202 2.23161643 0.3232219

*

A

A o

p

p o

T

To *

I

I * o

A p

A P wf If

Page 12: Tablas de Flujo Compresible (Version 1)

2.68 1.880806 3.1232735 0.0442925 0.1079177 0.4104282 1.2062465 0.13833754 0.21923519 2.23353443 0.32017692.69 1.8836768 3.1529931 0.0436159 0.1067376 0.4086269 1.2072767 0.13752051 0.21716871 2.23544212 0.317159

2.7 1.8865288 3.183011 0.04295 0.1055712 0.4068348 1.2083014 0.1367104 0.21512067 2.23733953 0.31416792.71 1.8893621 3.2133294 0.0422948 0.1044183 0.4050518 1.2093206 0.13590714 0.21309096 2.2392267 0.31120372.72 1.8921768 3.2439509 0.04165 0.1032787 0.4032778 1.2103343 0.13511064 0.21107947 2.24110367 0.30826612.73 1.894973 3.2748778 0.0410155 0.1021524 0.4015129 1.2113425 0.13432083 0.20908611 2.24297046 0.30535492.74 1.8977509 3.3061126 0.0403911 0.1010392 0.3997569 1.2123452 0.13353764 0.20711075 2.24482712 0.30247

2.75 1.9005105 3.3376576 0.0397767 0.099939 0.39801 1.2133425 0.13276101 0.2051533 2.24667369 0.29961132.76 1.9032522 3.3695153 0.0391721 0.0988515 0.3962719 1.2143343 0.13199084 0.20321364 2.24851021 0.29677862.77 1.9059758 3.4016882 0.038577 0.0977766 0.3945427 1.2153207 0.13122709 0.20129166 2.25033672 0.29397172.78 1.9086817 3.4341788 0.0379915 0.0967143 0.3928224 1.2163018 0.13046967 0.19938725 2.25215325 0.29119042.79 1.9113699 3.4669895 0.0374153 0.0956642 0.3911108 1.2172774 0.12971852 0.1975003 2.25395985 0.2884347

Tabla A.1

Funciones para flujo isentrópico unidimensional para un gas perfecto[ Calor específico y peso molecular constantes ]

k = 1.4

M M*

2.8 1.9140406 3.5001229 0.0368483 0.0946264 0.3894081 1.2182478 0.12897357 0.19563069 2.25575656 0.28570432.81 1.9166938 3.5335814 0.0362903 0.0936007 0.3877141 1.2192128 0.12823476 0.19377831 2.25754341 0.2829992.82 1.9193298 3.5673678 0.0357412 0.0925869 0.3860288 1.2201725 0.12750201 0.19194305 2.25932046 0.28031872.83 1.9219486 3.6014844 0.0352008 0.0915848 0.3843523 1.2211269 0.12677527 0.19012479 2.26108774 0.27766332.84 1.9245504 3.6359339 0.0346691 0.0905945 0.3826843 1.2220761 0.12605447 0.1883234 2.2628453 0.2750325

2.85 1.9271352 3.6707189 0.0341458 0.0896156 0.381025 1.2230201 0.12533954 0.18653879 2.26459317 0.27242622.86 1.9297033 3.705842 0.0336308 0.0886481 0.3793742 1.2239588 0.12463044 0.18477082 2.2663314 0.26984422.87 1.9322547 3.7413059 0.033124 0.0876919 0.3777319 1.2248924 0.12392708 0.18301937 2.26806004 0.26728642.88 1.9347896 3.7771131 0.0326253 0.0867467 0.3760982 1.2258208 0.12322942 0.18128434 2.26977912 0.26475252.89 1.937308 3.8132663 0.0321345 0.0858126 0.3744729 1.2267441 0.12253739 0.1795656 2.2714887 0.2622424

2.9 1.9398102 3.8497682 0.0316515 0.0848893 0.3728561 1.2276623 0.12185094 0.17786303 2.27318881 0.25975592.91 1.9422961 3.8866216 0.0311762 0.0839768 0.3712476 1.2285753 0.12117 0.17617652 2.2748795 0.25729292.92 1.944766 3.923829 0.0307084 0.0830748 0.3696475 1.2294834 0.12049452 0.17450594 2.27656081 0.25485312.93 1.94722 3.9613933 0.0302481 0.0821834 0.3680557 1.2303863 0.11982444 0.17285117 2.27823279 0.25243642.94 1.9496581 3.9993172 0.029795 0.0813023 0.3664722 1.2312843 0.11915971 0.17121209 2.27989548 0.2500427

2.95 1.9520806 4.0376035 0.0293492 0.0804314 0.3648969 1.2321772 0.11850027 0.16958858 2.28154893 0.24767172.96 1.9544874 4.0762549 0.0289104 0.0795706 0.3633298 1.2330652 0.11784607 0.16798053 2.28319318 0.24532322.97 1.9568787 4.1152742 0.0284786 0.0787198 0.3617709 1.2339483 0.11719704 0.16638781 2.28482827 0.24299722.98 1.9592547 4.1546642 0.0280536 0.0778789 0.3602202 1.2348264 0.11655315 0.1648103 2.28645426 0.24069332.99 1.9616154 4.1944278 0.0276353 0.0770478 0.3586775 1.2356997 0.11591433 0.16324788 2.28807119 0.2384115

3.00 1.963961 4.2345679 0.0272237 0.0762263 0.3571429 1.236568 0.11528054 0.16170043 2.2896791 0.23615163.10 1.9866081 4.6573106 0.0234487 0.0685172 0.3422313 1.2449893 0.109208 0.14702293 2.30527231 0.21471623.20 2.0078586 5.1209575 0.0202278 0.0616542 0.328084 1.2529508 0.10358546 0.13371161 2.32001409 0.1952763.30 2.0278117 5.6286468 0.0174768 0.0555412 0.3146633 1.2604771 0.09837061 0.12165117 2.33394998 0.17766263.40 2.0465595 6.1836988 0.0151246 0.0500927 0.3019324 1.2675922 0.09352596 0.1107317 2.34712471 0.1617155

3.50 2.0641874 6.7896205 0.0131109 0.0452327 0.2898551 1.2743198 0.08901817 0.10084974 2.3595817 0.1472836

*

A

A o

p

p o

T

To *

I

I * o

A p

A P wf If

Page 13: Tablas de Flujo Compresible (Version 1)

3.60 2.0807742 7.450111 0.0113847 0.040894 0.2783964 1.2806823 0.08481753 0.09190889 2.3713628 0.13422623.70 2.096393 8.1690665 0.0099029 0.037017 0.2675227 1.2867014 0.08089746 0.08382004 2.38250803 0.1224133.80 2.1111111 8.9505853 0.008629 0.0335494 0.2572016 1.2923977 0.07723418 0.07650131 2.39305546 0.11172453.90 2.1249909 9.7989735 0.007532 0.0304445 0.2474023 1.2977906 0.07380631 0.06987788 2.4030412 0.1020515

4.00 2.1380899 10.71875 0.0065861 0.0276616 0.2380952 1.3028986 0.07059462 0.06388165 2.41249934 0.09329454.10 2.1504614 11.714652 0.005769 0.0251644 0.2292526 1.3077389 0.06758177 0.05845086 2.42146199 0.08536324.20 2.1621544 12.79164 0.0050621 0.022921 0.2208481 1.312328 0.06475209 0.05352961 2.42995934 0.07817614.30 2.1732144 13.954904 0.0044494 0.0209034 0.2128565 1.3166811 0.06209138 0.04906744 2.43801972 0.07165944.40 2.1836833 15.209867 0.0039176 0.0190867 0.2052545 1.3208126 0.05958678 0.0450189 2.4456697 0.0657468

4.50 2.1936001 16.562195 0.0034553 0.017449 0.1980198 1.3247358 0.05722662 0.04134304 2.45293412 0.06037854.60 2.2030005 18.017795 0.0030526 0.0159709 0.1911315 1.3284634 0.05500024 0.03800307 2.45983626 0.05550074.70 2.2119178 19.582828 0.0027012 0.0146353 0.18457 1.3320071 0.05289796 0.03496591 2.46639785 0.05106514.80 2.2203828 21.26371 0.0023943 0.013427 0.1783167 1.3353778 0.05091093 0.03220188 2.47263922 0.0470285

Tabla A.1

Funciones para flujo isentrópico unidimensional para un gas perfecto[ Calor específico y peso molecular constantes ]

k = 1.4

M M*

4.9 2.2284241 23.067119 0.0021256 0.0123326 0.1723544 1.3385858 0.04903106 0.02968431 2.47857936 0.04335185 2.236068 25 0.00189 0.0113402 0.1666667 1.3416408 0.04725096 0.02738926 2.48423601 0.046 2.2952762 53.179784 0.0006334 0.0051936 0.1219512 1.3654768 0.03368202 0.01287578 2.52837172 0.01880417 2.3333333 104.14286 0.0002416 0.0026088 0.0925926 1.3809524 0.02515628 0.00657492 2.55702694 0.00960228 2.3590713 190.10938 0.0001024 0.0014135 0.0724638 1.3914835 0.01947273 0.00360178 2.57652671 0.00526019 2.3772174 327.1893 4.739E-05 0.000815 0.0581395 1.3989387 0.01550421 0.00209277 2.59033106 0.0030563

10 2.3904572 535.9375 2.356E-05 0.0004948 0.047619 1.4043936 0.01262835 0.00127763 2.60043168 0.0018659

0 0 0 0 1.4289 0 0 2.6458 0

k = 1.4

0.79 0.815974 1.042505 0.662536 0.745234 0.889031 1.020752 0.690697 0.656813 1.890065 0.959228

*

A

A o

p

p o

T

To *

I

I * o

A p

A P wf If

Page 14: Tablas de Flujo Compresible (Version 1)

Tabla A.1

Funciones para flujo isentrópico unidimensional para un gas perfecto[ Calor específico y peso molecular constantes ]

[ b ] k = 1

M M**

A

A o

p

p o

T

To *

I

I * o

A p

A Pwf If

Page 15: Tablas de Flujo Compresible (Version 1)

Tabla A.1

Funciones para flujo isentrópico unidimensional para un gas perfecto[ Calor específico y peso molecular constantes ]

[ b ] k = 1

M M**

A

A o

p

p o

T

To *

I

I * o

A p

A Pwf If

Page 16: Tablas de Flujo Compresible (Version 1)

Tabla A.1

Funciones para flujo isentrópico unidimensional para un gas perfecto[ Calor específico y peso molecular constantes ]

[ c ] k = 1.1

M M**

A

A o

p

p o

T

To *

I

I * o

A p

A Pwf If

Page 17: Tablas de Flujo Compresible (Version 1)

Tabla A.1

Funciones para flujo isentrópico unidimensional para un gas perfecto[ Calor específico y peso molecular constantes ]

[ c ] k = 1.1

M M**

A

A o

p

p o

T

To *

I

I * o

A p

A Pwf If

Page 18: Tablas de Flujo Compresible (Version 1)

Tabla A.1

Funciones para flujo isentrópico unidimensional para un gas perfecto[ Calor específico y peso molecular constantes ]

[ d ] k = 1.2

M M**

A

A o

p

p o

T

To *

I

I * o

A p

A Pwf If

Page 19: Tablas de Flujo Compresible (Version 1)

Tabla A.1

Funciones para flujo isentrópico unidimensional para un gas perfecto[ Calor específico y peso molecular constantes ]

[ d ] k = 1.2

M M**

A

A o

p

p o

T

To *

I

I * o

A p

A Pwf If

Page 20: Tablas de Flujo Compresible (Version 1)

Tabla A.1

Funciones para flujo isentrópico unidimensional para un gas perfecto[ Calor específico y peso molecular constantes ]

[ e ] k = 1.3

M M**

A

A o

p

p o

T

To *

I

I * o

A p

A Pwf If

Page 21: Tablas de Flujo Compresible (Version 1)

Tabla A.1

Funciones para flujo isentrópico unidimensional para un gas perfecto[ Calor específico y peso molecular constantes ]

[ e ] k = 1.3

M M**

A

A o

p

p o

T

To *

I

I * o

A p

A Pwf If

Page 22: Tablas de Flujo Compresible (Version 1)

Tabla A.1

Funciones para flujo isentrópico unidimensional para un gas perfecto[ Calor específico y peso molecular constantes ]

[ f ] k = 1.67

M M**

A

A o

p

p o

T

To *

I

I * o

A p

A Pwf If

Page 23: Tablas de Flujo Compresible (Version 1)

Tabla A.1

Funciones para flujo isentrópico unidimensional para un gas perfecto[ Calor específico y peso molecular constantes ]

[ f ] k = 1.67

M M*

*

A

A o

p

p o

T

To *

I

I * o

A p

A Pwf If

Page 24: Tablas de Flujo Compresible (Version 1)

724.4992

Page 25: Tablas de Flujo Compresible (Version 1)

Tabla 2

Choque normal unidimen sional de un gas perdecto( Calor específico y peso molecular constantes )

k = 1.4

Mx My

1.00 1.00000 1.00000 1.00000 1.00000 1.0000000 1.89292921.01 0.99013 1.02345 1.01669 1.00664 0.9999987 1.91521441.02 0.98052 1.04713 1.03344 1.01325 0.9999900 1.93789661.03 0.97115 1.07105 1.05024 1.01981 0.9999670 1.96096831.04 0.96203 1.09520 1.06709 1.02634 0.9999233 1.9844225

1.05 0.95313 1.11958 1.08398 1.03284 0.9998530 2.00825291.06 0.94445 1.14420 1.10092 1.03931 0.9997507 2.03245321.07 0.93598 1.16905 1.11790 1.04575 0.9996115 2.05701801.08 0.92771 1.19413 1.13492 1.05217 0.9994307 2.08194191.09 0.91965 1.21945 1.15199 1.05856 0.9992042 2.1072199

1.10 0.91177 1.24500 1.16908 1.06494 0.9989280 2.13284741.11 0.90408 1.27078 1.18621 1.07129 0.9985987 2.15882001.12 0.89656 1.29680 1.20338 1.07763 0.9982131 2.18513371.13 0.88922 1.32305 1.22057 1.08396 0.9977681 2.21178461.14 0.88204 1.34953 1.23779 1.09027 0.9972611 2.2387690

1.15 0.87502 1.37625 1.25504 1.09658 0.9966898 2.26608351.16 0.86816 1.40320 1.27231 1.10287 0.9960518 2.29372501.17 0.86145 1.43038 1.28961 1.10916 0.9953454 2.32169031.18 0.85488 1.45780 1.30693 1.11544 0.9945686 2.34997671.19 0.84846 1.48545 1.32426 1.12172 0.9937201 2.3785813

1.20 0.84217 1.51333 1.34161 1.12799 0.9927984 2.40750161.21 0.83601 1.54145 1.35898 1.13427 0.9918023 2.43673531.22 0.82999 1.56980 1.37636 1.14054 0.9907309 2.46627991.23 0.82408 1.59838 1.39376 1.14682 0.9895833 2.49613341.24 0.81830 1.62720 1.41116 1.15309 0.9883588 2.5262936

1.25 0.81264 1.65625 1.42857 1.15938 0.9870568 2.55675861.26 0.80709 1.68553 1.44599 1.16566 0.9856768 2.58752651.27 0.80164 1.71505 1.46341 1.17195 0.9842187 2.61859571.28 0.79631 1.74480 1.48084 1.17825 0.9826822 2.64996431.29 0.79108 1.77478 1.49827 1.18456 0.9810671 2.6816308

1.30 0.78596 1.80500 1.51570 1.19087 0.9793736 2.71359361.31 0.78093 1.83545 1.53312 1.19720 0.9776018 2.74585141.32 0.77600 1.86613 1.55055 1.20353 0.9757519 2.77840281.33 0.77116 1.89705 1.56797 1.20988 0.9738242 2.81124631.34 0.76641 1.92820 1.58538 1.21624 0.9718191 2.8443809

1.35 0.76175 1.95958 1.60278 1.22261 0.9697371 2.87780521.36 0.75718 1.99120 1.62018 1.22900 0.9675787 2.91151821.37 0.75269 2.02305 1.63757 1.23540 0.9653445 2.94551871.38 0.74829 2.05513 1.65494 1.24181 0.9630352 2.9798058

y

x

p

p

y

x

yT

Tx

oy

ox

p

poy

x

p

P

Page 26: Tablas de Flujo Compresible (Version 1)

1.39 0.74396 2.08745 1.67231 1.24825 0.9606516 3.0143783

Tabla 2

Choque normal unidimen sional de un gas perdecto( Calor específico y peso molecular constantes )

k = 1.4

Mx My

1.40 0.73971 2.12000 1.68966 1.25469 0.9581944 3.04923541.41 0.73554 2.15278 1.70699 1.26116 0.9556645 3.08437621.42 0.73144 2.18580 1.72430 1.26764 0.9530629 3.11979971.43 0.72741 2.21905 1.74160 1.27414 0.9503903 3.15550521.44 0.72345 2.25253 1.75888 1.28066 0.9476479 3.1914918

1.45 0.71956 2.28625 1.77614 1.28720 0.9448367 3.22775891.46 0.71574 2.32020 1.79337 1.29377 0.9419577 3.26430551.47 0.71198 2.35438 1.81058 1.30035 0.9390120 3.30113111.48 0.70829 2.38880 1.82777 1.30695 0.9360008 3.33823491.49 0.70466 2.42345 1.84493 1.31357 0.9329253 3.3756163

1.50 0.70109 2.45833 1.86207 1.32022 0.9297865 3.41327481.51 0.69758 2.49345 1.87918 1.32688 0.9265858 3.45120961.52 0.69413 2.52880 1.89626 1.33357 0.9233244 3.48942021.53 0.69073 2.56438 1.91331 1.34029 0.9200034 3.52790611.54 0.68739 2.60020 1.93033 1.34703 0.9166243 3.5666667

1.55 0.68410 2.63625 1.94732 1.35379 0.9131883 3.60570151.56 0.68087 2.67253 1.96427 1.36057 0.9096966 3.64501001.57 0.67768 2.70905 1.98119 1.36738 0.9061507 3.68459181.58 0.67455 2.74580 1.99808 1.37422 0.9025517 3.72444631.59 0.67147 2.78278 2.01493 1.38108 0.8989011 3.7645732

1.60 0.66844 2.82000 2.03175 1.38797 0.8952003 3.80497201.61 0.66545 2.85745 2.04852 1.39488 0.8914504 3.84564241.62 0.66251 2.89513 2.06526 1.40182 0.8876529 3.88658381.63 0.65962 2.93305 2.08197 1.40879 0.8838092 3.92779601.64 0.65677 2.97120 2.09863 1.41578 0.8799206 3.9692786

1.65 0.65396 3.00958 2.11525 1.42280 0.8759884 4.01103121.66 0.65119 3.04820 2.13183 1.42985 0.8720140 4.05305341.67 0.64847 3.08705 2.14836 1.43693 0.8679987 4.09534511.68 0.64579 3.12613 2.16486 1.44403 0.8639439 4.13790571.69 0.64315 3.16545 2.18131 1.45117 0.8598509 4.1807351

1.70 0.64054 3.20500 2.19772 1.45833 0.8557211 4.22383291.71 0.63798 3.24478 2.21408 1.46552 0.8515557 4.26719881.72 0.63545 3.28480 2.23040 1.47274 0.8473562 4.31083261.73 0.63296 3.32505 2.24667 1.47999 0.8431237 4.35473401.74 0.63051 3.36553 2.26289 1.48727 0.8388597 4.3989027

1.75 0.62809 3.40625 2.27907 1.49458 0.8345654 4.44333851.76 0.62570 3.44720 2.29520 1.50192 0.8302421 4.4880412

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Page 27: Tablas de Flujo Compresible (Version 1)

1.77 0.62335 3.48838 2.31128 1.50929 0.8258910 4.53301041.78 0.62104 3.52980 2.32731 1.51669 0.8215134 4.57824611.79 0.61875 3.57145 2.34329 1.52412 0.8171106 4.6237478

Tabla 2

Choque normal unidimen sional de un gas perdecto( Calor específico y peso molecular constantes )

k = 1.4

Mx My

1.80 0.61650 3.61333 2.35922 1.53158 0.8126838 4.66951561.81 0.61428 3.65545 2.37510 1.53907 0.8082342 4.71554901.82 0.61209 3.69780 2.39093 1.54659 0.8037630 4.76184801.83 0.60993 3.74038 2.40671 1.55415 0.7992715 4.80841241.84 0.60780 3.78320 2.42244 1.56173 0.7947607 4.8552419

1.85 0.60570 3.82625 2.43811 1.56935 0.7902319 4.90233631.86 0.60363 3.86953 2.45373 1.57700 0.7856862 4.94969561.87 0.60158 3.91305 2.46930 1.58468 0.7811247 4.99731951.88 0.59957 3.95680 2.48481 1.59239 0.7765485 5.04520781.89 0.59758 4.00078 2.50027 1.60014 0.7719588 5.0933604

1.90 0.59562 4.04500 2.51568 1.60792 0.7673566 5.14177721.91 0.59368 4.08945 2.53103 1.61573 0.7627430 5.19045791.92 0.59177 4.13413 2.54633 1.62357 0.7581190 5.23940251.93 0.58988 4.17905 2.56157 1.63144 0.7534857 5.28861081.94 0.58802 4.22420 2.57675 1.63935 0.7488441 5.3380826

1.95 0.58618 4.26958 2.59188 1.64729 0.7441951 5.38781781.96 0.58437 4.31520 2.60695 1.65527 0.7395398 5.43781641.97 0.58258 4.36105 2.62196 1.66328 0.7348790 5.48807811.98 0.58047 4.41638 2.63991 1.67293 0.7292804 5.54873931.99 0.57907 4.45345 2.65182 1.67939 0.7255452 5.5893904

2.00 0.57735 4.50000 2.66667 1.68750 0.7208739 5.64044082.01 0.57565 4.54678 2.68145 1.69564 0.7162008 5.69175392.02 0.57397 4.59380 2.69618 1.70382 0.7115269 5.74332962.03 0.57231 4.64105 2.71085 1.71203 0.7068530 5.79516772.04 0.57068 4.68853 2.72546 1.72027 0.7021799 5.8472682

2.05 0.56906 4.73625 2.74002 1.72855 0.6975084 5.89963092.06 0.56747 4.78420 2.75451 1.73686 0.6928394 5.95225582.07 0.56589 4.83238 2.76895 1.74521 0.6881737 6.00514272.08 0.56433 4.88080 2.78332 1.75359 0.6835119 6.05829162.09 0.56280 4.92945 2.79764 1.76200 0.6788548 6.1117024

2.10 0.56128 4.97833 2.81190 1.77045 0.6742032 6.16537502.11 0.55978 5.02745 2.82610 1.77893 0.6695578 6.21930922.12 0.55829 5.07680 2.84024 1.78745 0.6649193 6.27350502.13 0.55683 5.12638 2.85432 1.79601 0.6602883 6.32796242.14 0.55538 5.17620 2.86835 1.80459 0.6556655 6.3826812

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Page 28: Tablas de Flujo Compresible (Version 1)

2.15 0.55395 5.22625 2.88231 1.81322 0.6510516 6.43766142.16 0.55254 5.27653 2.89621 1.82188 0.6464472 6.49290282.17 0.55115 5.32705 2.91005 1.83057 0.6418529 6.54840552.18 0.54977 5.37780 2.92383 1.83930 0.6372692 6.60416932.19 0.54840 5.42878 2.93756 1.84806 0.6326969 6.6601942

Tabla 2

Choque normal unidimen sional de un gas perdecto( Calor específico y peso molecular constantes )

k = 1.4

Mx My

2.20 0.54706 5.48000 2.95122 1.85686 0.6281363 6.71648012.21 0.54572 5.53145 2.96482 1.86569 0.6235882 6.77302692.22 0.54441 5.58313 2.97837 1.87456 0.6190529 6.82983462.23 0.54311 5.63505 2.99185 1.88347 0.6145311 6.88690302.24 0.54182 5.68720 3.00527 1.89241 0.6100232 6.9442322

2.25 0.54055 5.73958 3.01863 1.90138 0.6055297 7.00182212.26 0.53930 5.79220 3.03194 1.91040 0.6010511 7.05967262.27 0.53805 5.84505 3.04518 1.91944 0.5965879 7.11778372.28 0.53683 5.89813 3.05836 1.92853 0.5921404 7.17615522.29 0.53561 5.95145 3.07149 1.93765 0.5877091 7.2347872

2.30 0.53441 6.00500 3.08455 1.94680 0.5832945 7.29367962.31 0.53322 6.05878 3.09755 1.95599 0.5788969 7.35283242.32 0.53205 6.11280 3.11049 1.96522 0.5745167 7.41224542.33 0.53089 6.16705 3.12338 1.97448 0.5701543 7.47191862.34 0.52974 6.22153 3.13620 1.98378 0.5658100 7.5318521

2.35 0.52861 6.27625 3.14897 1.99311 0.5614842 7.59204572.36 0.52749 6.33120 3.16167 2.00249 0.5571773 7.65249932.37 0.52638 6.38638 3.17432 2.01189 0.5528894 7.71321302.38 0.52528 6.44180 3.18690 2.02134 0.5486211 7.77418672.39 0.52419 6.49745 3.19943 2.03082 0.5443725 7.8354204

2.40 0.52312 6.55333 3.21190 2.04033 0.5401439 7.89691402.41 0.52206 6.60945 3.22430 2.04988 0.5359356 7.95866742.42 0.52100 6.66580 3.23665 2.05947 0.5317479 8.02068072.43 0.51996 6.72238 3.24894 2.06910 0.5275811 8.08295372.44 0.51894 6.77920 3.26117 2.07876 0.5234353 8.1454865

2.45 0.51792 6.83625 3.27335 2.08846 0.5193107 8.20827902.46 0.51691 6.89353 3.28546 2.09819 0.5152077 8.27133122.47 0.51592 6.95105 3.29752 2.10797 0.5111264 8.33464302.48 0.51493 7.00880 3.30951 2.11777 0.5070671 8.39821442.49 0.51395 7.06678 3.32145 2.12762 0.5030298 8.4620454

2.50 0.51299 7.12500 3.33333 2.13750 0.4990148 8.52613592.51 0.51203 7.18345 3.34516 2.14742 0.4950223 8.59048592.52 0.51109 7.24213 3.35692 2.15737 0.4910523 8.65509532.53 0.51015 7.30105 3.36863 2.16737 0.4871052 8.7199642

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p

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Page 29: Tablas de Flujo Compresible (Version 1)

2.54 0.50923 7.36020 3.38028 2.17739 0.4831809 8.7850925

2.55 0.50831 7.41958 3.39187 2.18746 0.4792797 8.85048012.56 0.50741 7.47920 3.40341 2.19756 0.4754016 8.91612712.57 0.50651 7.53905 3.41489 2.20770 0.4715468 8.98203342.58 0.50562 7.59913 3.42631 2.21788 0.4677153 9.04819902.59 0.50474 7.65945 3.43767 2.22809 0.4639074 9.1146238

Tabla 2

Choque normal unidimen sional de un gas perdecto( Calor específico y peso molecular constantes )

k = 1.4

Mx My

2.60 0.50387 7.72000 3.44898 2.23834 0.4601230 9.18130782.61 0.50301 7.78078 3.46023 2.24863 0.4563623 9.24825102.62 0.50216 7.84180 3.47143 2.25896 0.4526253 9.31545342.63 0.50131 7.90305 3.48257 2.26932 0.4489120 9.38291492.64 0.50048 7.96453 3.49365 2.27972 0.4452227 9.4506355

2.65 0.49965 8.02625 3.50468 2.29015 0.4415573 9.51861522.66 0.49883 8.08820 3.51565 2.30063 0.4379158 9.58685402.67 0.49802 8.15038 3.52657 2.31114 0.4342983 9.65535182.68 0.49722 8.21280 3.53743 2.32168 0.4307049 9.72410862.69 0.49642 8.27545 3.54824 2.33227 0.4271356 9.7931245

2.70 0.49563 8.33833 3.55899 2.34289 0.4235903 9.86239922.71 0.49485 8.40145 3.56969 2.35355 0.4200691 9.93193302.72 0.49408 8.46480 3.58033 2.36425 0.4165721 10.00172562.73 0.49332 8.52838 3.59092 2.37498 0.4130992 10.07177722.74 0.49256 8.59220 3.60146 2.38576 0.4096504 10.1420876

2.75 0.49181 8.65625 3.61194 2.39657 0.4062258 10.21265692.76 0.49107 8.72053 3.62237 2.40741 0.4028253 10.28348502.77 0.49033 8.78505 3.63274 2.41830 0.3994488 10.35457202.78 0.48960 8.84980 3.64307 2.42922 0.3960965 10.42591772.79 0.48888 8.91478 3.65334 2.44018 0.3927681 10.4975222

2.80 0.48817 8.98000 3.66355 2.45117 0.3894639 10.56938552.81 0.48746 9.04545 3.67372 2.46221 0.3861836 10.64150752.82 0.48676 9.11113 3.68383 2.47328 0.3829272 10.71388832.83 0.48606 9.17705 3.69389 2.48439 0.3796948 10.78652772.84 0.48538 9.24320 3.70389 2.49554 0.3764863 10.8594259

2.85 0.48469 9.30958 3.71385 2.50672 0.3733015 10.93258272.86 0.48402 9.37620 3.72375 2.51794 0.3701405 11.00599822.87 0.48335 9.44305 3.73361 2.52920 0.3670033 11.07967232.88 0.48269 9.51013 3.74341 2.54050 0.3638896 11.15360502.89 0.48203 9.57745 3.75316 2.55183 0.3607996 11.2277964

2.90 0.48138 9.64500 3.76286 2.56321 0.3577330 11.30224632.91 0.48073 9.71278 3.77251 2.57462 0.3546900 11.3769548

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Page 30: Tablas de Flujo Compresible (Version 1)

2.92 0.48010 9.78080 3.78211 2.58607 0.3516702 11.45192182.93 0.47946 9.84905 3.79167 2.59755 0.3486738 11.52714742.94 0.47884 9.91753 3.80117 2.60908 0.3457006 11.6026316

2.95 0.47821 9.98625 3.81062 2.62064 0.3427505 11.67837422.96 0.47760 10.05520 3.82002 2.63224 0.3398234 11.75437542.97 0.47699 10.12438 3.82937 2.64387 0.3369193 11.83063502.98 0.47638 10.19380 3.83868 2.65555 0.3340381 11.90715312.99 0.47578 10.26345 3.84794 2.66726 0.3311797 11.9839297

Tabla 2

Choque normal unidimen sional de un gas perdecto( Calor específico y peso molecular constantes )

k = 1.4

Mx My

3.00 0.47519 10.33333 3.85714 2.67901 0.3283439 12.06096473.50 0.45115 14.12500 4.26087 3.31505 0.2129476 16.24200094.00 0.43496 18.50000 4.57143 4.04687 0.1387562 21.06808104.50 0.42355 23.45833 4.81188 4.87509 0.0916979 26.53866515.00 0.41523 29.00000 5.00000 5.80000 0.0617163 32.6534743

6.00 0.40416 41.83333 5.26829 7.94059 0.0296509 46.81520577.00 0.39736 57.00000 5.44444 10.46939 0.0153515 63.55262638.00 0.39289 74.50000 5.56522 13.38672 0.0084878 82.86546819.00 0.38980 94.33333 5.65116 16.69273 0.0049639 ###

10.00 0.38758 116.50000 5.71429 20.38750 0.0030448 ###

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Page 31: Tablas de Flujo Compresible (Version 1)

Tabla 2

Choque normal unidimensional de un gas perfecto( Calor específico y peso molecular constantes )

k = 1.0

Mx My

1.00

1.05

1.10

1.15

1.20

1.25

1.30

1.35

1.40

1.45

1.50

1.55

1.60

1.65

1.70

1.75

1.80

1.85

1.90

1.95

2.00

2.05

2.10

2.15

2.20

2.25

2.30

2.35

2.40

2.45

2.50

2.55

2.60

2.65

2.70

2.75

2.80

y

x

p

p

y

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Page 32: Tablas de Flujo Compresible (Version 1)

2.85

2.90

2.95

3.00

3.50

3.50

4.00

4.50

5.00

6.00

7.00

8.00

9.00

10.00

Page 33: Tablas de Flujo Compresible (Version 1)

464.36139

Page 34: Tablas de Flujo Compresible (Version 1)

Tabla 2

Línea de Fanno; flujo de un gas perfecto, unidimensional, adiabático yde área constante

( Calor específico y peso molecular constantes )

k = 1.4

M

0 1.20000

0.01 1.19998 109.543416 57.873843 7134.404540.02 1.19990 54.770065 28.942130 1778.449880.03 1.19978 36.5115513 19.300542 787.0813870.04 1.19962 27.3817471 14.481486 440.352214

0.05 1.19940 21.9034271 11.591444 280.0203060.06 1.19914 18.2508495 9.665910 193.0310820.07 1.19883 15.6415534 8.291525 140.6550140.08 1.19847 13.6843088 7.261610 106.7182160.09 1.19806 12.1617653 6.461342 83.4961172

0.10 1.19760 10.9435131 5.821829 66.921560.11 1.19710 9.94656388 5.299230 54.68789550.12 1.19655 9.11559228 4.864318 45.4079620.13 1.19596 8.4122961 4.496859 38.20700310.14 1.19531 7.80931667 4.182400 32.511306

0.15 1.19462 7.28659101 3.910343 27.93196750.16 1.19389 6.82907187 3.672739 24.197830.17 1.19310 6.42525257 3.463509 21.11517820.18 1.19227 6.0661835 3.277926 18.54265450.19 1.19140 5.74479918 3.112259 16.3751637

0.2 1.19048 5.45544726 2.963520 14.53326650.21 1.18951 5.19355203 2.829294 12.95602190.22 1.18850 4.95536975 2.707602 11.59605440.23 1.18744 4.73780779 2.596812 10.41608990.24 1.18633 4.53828896 2.495562 9.38648053

0.25 1.18519 4.35464843 2.402710 8.483408840.26 1.18399 4.18505446 2.317287 7.687566580.27 1.18276 4.02794666 2.238471 6.983169530.28 1.18147 3.88198758 2.165554 6.357214490.29 1.18015 3.74602426 2.097928 5.79891264

0.3 1.17878 3.61905747 2.035065 5.299253110.31 1.17737 3.50021693 1.976507 4.850663440.32 1.17592 3.38874115 1.921851 4.446743470.33 1.17442 3.28396095 1.870745 4.08205470.34 1.17288 3.1852859 1.822876 3.75195255

0.35 1.17130 3.09219303 1.777969 3.452451750.36 1.16968 3.00421752 1.735778 3.180117520.37 1.16802 2.92094477 1.696086 2.931977190.38 1.16632 2.84200386 1.658696 2.70544783

*

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T *

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o

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V

V *

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Page 35: Tablas de Flujo Compresible (Version 1)

0.39 1.16457 2.76706191 1.623433 2.49827682Tabla 2

Línea de Fanno; flujo de un gas perfecto, unidimensional, adiabático yde área constante

( Calor específico y peso molecular constantes )

k = 1.4

M

0.40 1.16279 2.69581933 1.590140 2.308492650.41 1.16097 2.62800577 1.558673 2.134364080.42 1.15911 2.56337663 1.528905 1.974366030.43 1.15721 2.50171007 1.500718 1.827150970.44 1.15527 2.44280443 1.474005 1.69152484

0.45 1.15329 2.38647598 1.448672 1.566426690.46 1.15128 2.33255695 1.424629 1.450911350.47 1.14923 2.28089388 1.401795 1.344134760.48 1.14714 2.23134609 1.380097 1.245341290.49 1.14502 2.18378439 1.359468 1.15385301

0.50 1.14286 2.13808994 1.339844 1.069060310.51 1.14066 2.0941532 1.321168 0.990413940.52 1.13843 2.05187308 1.303388 0.917417990.53 1.13617 2.01115611 1.286454 0.849623870.54 1.13387 1.97191578 1.270321 0.78662509

0.55 1.13154 1.93407182 1.254948 0.728052570.56 1.12918 1.89754974 1.240294 0.673570710.57 1.12678 1.86228027 1.226326 0.622873820.58 1.12435 1.8281989 1.213007 0.575683020.59 1.12189 1.79524553 1.200308 0.53174348

0.60 1.11940 1.76336404 1.188200 0.490822050.61 1.11688 1.73250201 1.176654 0.452705090.62 1.11433 1.70261038 1.165646 0.417196570.63 1.11175 1.67364325 1.155151 0.384116380.64 1.10914 1.64555755 1.145148 0.35329885

0.65 1.10650 1.61831287 1.135616 0.324591370.66 1.10383 1.59187127 1.126535 0.297853230.67 1.10114 1.56619706 1.117887 0.272954520.68 1.09842 1.54125665 1.109655 0.249775190.69 1.09567 1.5170184 1.101822 0.22820414

0.70 1.09290 1.4934525 1.094373 0.208138510.71 1.09010 1.47053078 1.087294 0.189482920.72 1.08727 1.44822667 1.080571 0.172148850.73 1.08442 1.42651504 1.074192 0.15605410.74 1.08155 1.40537213 1.068144 0.14112224

0.75 1.07865 1.38477543 1.062417 0.127282140.76 1.07573 1.36470364 1.056999 0.11446756

*

T

T *

p

p *o

o

p

p *

V

V *

I

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Lmaxf

Dh

Page 36: Tablas de Flujo Compresible (Version 1)

0.77 1.07279 1.34513655 1.051881 0.102616760.78 1.06982 1.32605498 1.047053 0.091672160.79 1.06684 1.30744075 1.042505 0.08157997

1.20000 #DIV/0! #DIV/0! #DIV/0!1.20000 #DIV/0! #DIV/0! #DIV/0!1.20000 #DIV/0! #DIV/0! #DIV/0!1.20000 #DIV/0! #DIV/0! #DIV/0!1.20000 #DIV/0! #DIV/0! #DIV/0!1.20000 #DIV/0! #DIV/0! #DIV/0!1.20000 #DIV/0! #DIV/0! #DIV/0!1.20000 #DIV/0! #DIV/0! #DIV/0!1.20000 #DIV/0! #DIV/0! #DIV/0!1.20000 #DIV/0! #DIV/0! #DIV/0!

M #VALUE! #VALUE! #VALUE! #VALUE!1.20000 #DIV/0! #DIV/0! #DIV/0!

0.80 1.06383 1.28927656 1.038230 0.072289970.81 1.06080 1.27154597 1.034219 0.063755190.82 1.05775 1.25423336 1.030464 0.055931670.83 1.05469 1.23732385 1.026959 0.048778270.84 1.05160 1.22080325 1.023696 0.04225644

0.85 1.04849 1.20465808 1.020669 0.036330040.86 1.04537 1.18887545 1.017871 0.030965150.87 1.04223 1.17344308 1.015297 0.026129950.88 1.03907 1.15834925 1.012941 0.021794540.89 1.03589 1.14358274 1.010798 0.01793083

0.90 1.03270 1.12913287 1.008863 0.014512390.91 1.02950 1.11498939 1.007131 0.011514360.92 1.02627 1.10114253 1.005597 0.008913340.93 1.02304 1.0875829 1.004258 0.006687290.94 1.01978 1.07430155 1.003108 0.00481545

0.95 1.01652 1.06128988 1.002145 0.003278220.96 1.01324 1.04853965 1.001365 0.002057140.97 1.00995 1.03604297 1.000763 0.001134790.98 1.00664 1.02379227 1.000337 0.00049470.99 1.00333 1.01178027 1.000084 0.00012133

1.00 1.00000 1 1.000000 01.01 0.99666 0.98844475 1.000083 0.000116831.02 0.99331 0.97710808 1.000330 0.000458691.03 0.98995 0.9659838 1.000738 0.001013171.04 0.98658 0.95506595 1.001305 0.0017685

1.05 0.98320 0.9443488 1.002029 0.002713581.06 0.97982 0.93382684 1.002907 0.003837851.07 0.97642 0.92349476 1.003938 0.005131351.08 0.97302 0.91334746 1.005119 0.00658461.09 0.96960 0.90337999 1.006449 0.00818865

1.10 0.96618 0.89358761 1.007925 0.0099351.11 0.96276 0.88396575 1.009547 0.011815581.12 0.95932 0.87450999 1.011312 0.013822731.13 0.95589 0.86521607 1.013219 0.015949211.14 0.95244 0.85607987 1.015267 0.01818811

1.15 0.94899 0.84709743 1.017454 0.02053289

Page 37: Tablas de Flujo Compresible (Version 1)

1.16 0.94554 0.83826492 1.019780 0.022977351.17 0.94208 0.82957862 1.022242 0.025515561.18 0.93861 0.82103495 1.024840 0.028141931.19 0.93515 0.81263047 1.027573 0.03085112

Tabla 2

Línea de Fanno; flujo de un gas perfecto, unidimensional, adiabático yde área constante

( Calor específico y peso molecular constantes )

k = 1.4

M

1.20 0.93168 0.80436182 1.030440 0.033638071.21 0.92820 0.79622576 1.033440 0.036497951.22 0.92473 0.78821916 1.036572 0.039426191.23 0.92125 0.78033899 1.039835 0.042418431.24 0.91777 0.77258232 1.043229 0.04547052

1.25 0.91429 0.76494631 1.046753 0.048578521.26 0.91080 0.7574282 1.050406 0.051738691.27 0.90732 0.75002532 1.054189 0.054947441.28 0.90383 0.7427351 1.058100 0.058201391.29 0.90035 0.73555502 1.062138 0.0614973

1.30 0.89686 0.72848265 1.066305 0.064832091.31 0.89338 0.72151564 1.070598 0.068202831.32 0.88989 0.71465171 1.075018 0.071606731.33 0.88641 0.70788863 1.079565 0.075041141.34 0.88292 0.70122424 1.084239 0.07850352

1.35 0.87944 0.69465647 1.089038 0.081991471.36 0.87596 0.68818327 1.093964 0.08550271.37 0.87249 0.68180268 1.099015 0.089035011.38 0.86901 0.67551278 1.104193 0.092586331.39 0.86554 0.6693117 1.109496 0.09615468

1.40 0.86207 0.66319764 1.114926 0.099738171.41 0.85860 0.65716883 1.120481 0.103335011.42 0.85514 0.65122357 1.126162 0.106943491.43 0.85168 0.64536019 1.131969 0.110561971.44 0.84822 0.63957707 1.137903 0.11418891

1.45 0.84477 0.63387263 1.143963 0.117822821.46 0.84133 0.62824535 1.150150 0.121462321.47 0.83788 0.62269372 1.156463 0.125106041.48 0.83445 0.6172163 1.162904 0.128752731.49 0.83101 0.61181166 1.169471 0.13240118

1.50 0.82759 0.60647843 1.176167 0.136050221.51 0.82416 0.60121527 1.182991 0.139698761.52 0.82075 0.59602087 1.189943 0.143345761.53 0.81734 0.59089395 1.197024 0.146990221.54 0.81393 0.58583326 1.204234 0.15063121

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T *

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o

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Page 38: Tablas de Flujo Compresible (Version 1)

1.55 0.81054 0.5808376 1.211574 0.154267821.56 0.80715 0.57590577 1.219044 0.157899211.57 0.80376 0.57103664 1.226644 0.161524561.58 0.80038 0.56622907 1.234376 0.16514311.59 0.79701 0.56148197 1.242239 0.16875411

Tabla 2

Línea de Fanno; flujo de un gas perfecto, unidimensional, adiabático yde área constante

( Calor específico y peso molecular constantes )

k = 1.4

M

1.6 0.79365 0.55679425 1.250235 0.172356891.61 0.79030 0.55216489 1.258364 0.175950781.62 0.78695 0.54759286 1.266626 0.179535171.63 0.78361 0.54307715 1.275022 0.183109461.64 0.78027 0.53861681 1.283553 0.18667309

1.65 0.77695 0.53421087 1.292219 0.190225531.66 0.77363 0.52985842 1.301021 0.193766281.67 0.77033 0.52555853 1.309960 0.197294861.68 0.76703 0.52131033 1.319037 0.200810831.69 0.76374 0.51711296 1.328252 0.20431376

1.7 0.76046 0.51296555 1.337606 0.207803261.71 0.75718 0.5088673 1.347100 0.211278941.72 0.75392 0.50481738 1.356735 0.214740461.73 0.75067 0.500815 1.366511 0.218187471.74 0.74742 0.4968594 1.376430 0.22161967

1.75 0.74419 0.49294982 1.386492 0.225036751.76 0.74096 0.48908551 1.396698 0.228438441.77 0.73774 0.48526575 1.407049 0.231824481.78 0.73454 0.48148984 1.417546 0.235194641.79 0.73134 0.47775707 1.428190 0.23854867

1.8 0.72816 0.47406677 1.438982 0.241886371.81 0.72498 0.47041828 1.449923 0.245207551.82 0.72181 0.46681093 1.461013 0.248512011.83 0.71866 0.46324411 1.472255 0.25179961.84 0.71551 0.45971718 1.483648 0.25507015

1.85 0.71238 0.45622952 1.495194 0.258323531.86 0.70925 0.45278055 1.506894 0.261559591.87 0.70614 0.44936968 1.518750 0.264778211.88 0.70304 0.44599632 1.530761 0.26797931.89 0.69995 0.44265993 1.542930 0.27116274

1.9 0.69686 0.43935993 1.555257 0.274328441.91 0.69379 0.4360958 1.567743 0.277476331.92 0.69073 0.43286701 1.580391 0.28060634

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T *

p

p *o

o

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Page 39: Tablas de Flujo Compresible (Version 1)

1.93 0.68769 0.42967302 1.593200 0.283718391.94 0.68465 0.42651334 1.606172 0.28681244

1.95 0.68162 0.42338747 1.619309 0.289888441.96 0.67861 0.4202949 1.632611 0.292946341.97 0.67561 0.41723517 1.646080 0.295986121.98 0.67262 0.4142078 1.659717 0.299007751.99 0.66964 0.41121232 1.673523 0.30201122

Tabla 2

Línea de Fanno; flujo de un gas perfecto, unidimensional, adiabático yde área constante

( Calor específico y peso molecular constantes )

k = 1.4

M

2.00 0.66667 0.40824829 1.687500 0.30499652.01 0.66371 0.40531526 1.701649 0.30796362.02 0.66076 0.40241278 1.715971 0.310912512.03 0.65783 0.39954044 1.730467 0.313843232.04 0.65491 0.3966978 1.745139 0.31675578

2.05 0.65200 0.39388446 1.759989 0.319650172.06 0.64910 0.39110002 1.775017 0.322526422.07 0.64621 0.38834406 1.790225 0.325384562.08 0.64334 0.3856162 1.805614 0.328224612.09 0.64047 0.38291606 1.821187 0.33104661

2.10 0.63762 0.38024325 1.836944 0.333850582.11 0.63478 0.37759742 1.852886 0.336636582.12 0.63195 0.37497818 1.869016 0.339404652.13 0.62914 0.3723852 1.885334 0.342154822.14 0.62633 0.3698181 1.901843 0.34488716

2.15 0.62354 0.36727655 1.918543 0.347601722.16 0.62076 0.36476022 1.935437 0.350298552.17 0.61799 0.36226875 1.952525 0.352977712.18 0.61523 0.35980184 1.969810 0.355639272.19 0.61249 0.35735915 1.987292 0.35828328

2.20 0.60976 0.35494037 2.004975 0.360909822.21 0.60704 0.35254518 2.022858 0.363518952.22 0.60433 0.35017329 2.040944 0.366110742.23 0.60163 0.34782439 2.059234 0.368685272.24 0.59895 0.34549818 2.077731 0.37124261

2.25 0.59627 0.34319437 2.096435 0.373782842.26 0.59361 0.34091269 2.115349 0.376306032.27 0.59096 0.33865283 2.134473 0.378812272.28 0.58833 0.33641454 2.153811 0.381301642.29 0.58570 0.33419753 2.173363 0.38377421

2.30 0.58309 0.33200154 2.193131 0.38623008

*

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T *

p

p *o

o

p

p *

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2.31 0.58049 0.32982631 2.213117 0.388669332.32 0.57790 0.32767157 2.233323 0.391092042.33 0.57532 0.32553707 2.253751 0.39349832.34 0.57276 0.32342256 2.274401 0.39588821

2.35 0.57021 0.3213278 2.295277 0.398261842.36 0.56767 0.31925253 2.316381 0.400619292.37 0.56514 0.31719652 2.337712 0.402960662.38 0.56262 0.31515954 2.359275 0.405286022.39 0.56011 0.31314135 2.381070 0.40759548

1.20000 #DIV/0! #DIV/0! #DIV/0!1.20000 #DIV/0! #DIV/0! #DIV/0!1.20000 #DIV/0! #DIV/0! #DIV/0!1.20000 #DIV/0! #DIV/0! #DIV/0!1.20000 #DIV/0! #DIV/0! #DIV/0!1.20000 #DIV/0! #DIV/0! #DIV/0!1.20000 #DIV/0! #DIV/0! #DIV/0!1.20000 #DIV/0! #DIV/0! #DIV/0!1.20000 #DIV/0! #DIV/0! #DIV/0!

M #VALUE! #VALUE! #VALUE! #VALUE!1.20000 #DIV/0! #DIV/0! #DIV/0!

2.4 0.55762 0.31114172 2.403100 0.409889132.41 0.55514 0.30916043 2.425366 0.412167062.42 0.55267 0.30719726 2.447870 0.414429362.43 0.55021 0.30525199 2.470615 0.416676132.44 0.54777 0.30332441 2.493602 0.41890747

2.45 0.54533 0.3014143 2.516832 0.421123462.46 0.54291 0.29952146 2.540309 0.423324222.47 0.54050 0.29764568 2.564035 0.425509822.48 0.53810 0.29578675 2.588010 0.427680372.49 0.53571 0.29394449 2.612237 0.42983596

2.5 0.53333 0.2921187 2.636719 0.431976692.51 0.53097 0.29030917 2.661457 0.434102662.52 0.52862 0.28851573 2.686453 0.436213962.53 0.52627 0.28673819 2.711709 0.438310692.54 0.52394 0.28497635 2.737228 0.44039294

2.55 0.52163 0.28323005 2.763012 0.442460822.56 0.51932 0.28149909 2.789063 0.444514422.57 0.51702 0.27978331 2.815382 0.446553832.58 0.51474 0.27808252 2.841972 0.448579152.59 0.51247 0.27639657 2.868836 0.45059049

2.6 0.51020 0.27472527 2.895975 0.452587922.61 0.50795 0.27306847 2.923392 0.454571562.62 0.50571 0.271426 2.951089 0.45654152.63 0.50349 0.26979769 2.979068 0.458497832.64 0.50127 0.26818339 3.007331 0.46044064

2.65 0.49906 0.26658294 3.035881 0.462370042.66 0.49687 0.26499619 3.064720 0.464286122.67 0.49469 0.26342298 3.093850 0.466188962.68 0.49251 0.26186316 3.123274 0.468078682.69 0.49035 0.26031658 3.152993 0.46995536

2.7 0.48820 0.25878311 3.183011 0.47181909

Page 41: Tablas de Flujo Compresible (Version 1)

2.71 0.48606 0.25726258 3.213329 0.473669962.72 0.48393 0.25575486 3.243951 0.475508082.73 0.48182 0.25425982 3.274878 0.477333542.74 0.47971 0.2527773 3.306113 0.47914641

2.75 0.47761 0.25130718 3.337658 0.480946812.76 0.47553 0.24984932 3.369515 0.482734812.77 0.47345 0.24840358 3.401688 0.484510522.78 0.47139 0.24696984 3.434179 0.486274012.79 0.46933 0.24554797 3.466989 0.48802539

1.20000 #DIV/0! #DIV/0! #DIV/0!Tabla 2

Línea de Fanno; flujo de un gas perfecto, unidimensional, adiabático yde área constante

( Calor específico y peso molecular constantes )

k = 1.4

M

2.8 0.46729 0.24413783 3.500123 0.489764732.81 0.46526 0.24273931 3.533581 0.491492142.82 0.46323 0.24135227 3.567368 0.493207692.83 0.46122 0.2399766 3.601484 0.494911482.84 0.45922 0.23861218 3.635934 0.4966036

2.85 0.45723 0.23725888 3.670719 0.498284132.86 0.45525 0.23591659 3.705842 0.499953152.87 0.45328 0.23458519 3.741306 0.501610772.88 0.45132 0.23326456 3.777113 0.503257052.89 0.44937 0.2319546 3.813266 0.50489209

2.9 0.44743 0.23065519 3.849768 0.506515972.91 0.44550 0.22936623 3.886622 0.508128782.92 0.44358 0.22808759 3.923829 0.50973062.93 0.44167 0.22681918 3.961393 0.511321512.94 0.43977 0.22556089 3.999317 0.5129016

2.95 0.43788 0.22431262 4.037603 0.514470952.96 0.43600 0.22307425 4.076255 0.516029632.97 0.43413 0.2218457 4.115274 0.517577742.98 0.43226 0.22062685 4.154664 0.519115352.99 0.43041 0.21941762 4.194428 0.52064255

3.00 0.42857 0.21821789 4.234568 0.522159413.10 0.41068 0.20672301 4.657311 0.536776593.20 0.39370 0.19607994 5.120958 0.550443783.30 0.37760 0.1862086 5.628647 0.563231913.40 0.36232 0.17703802 6.183699 0.57520672

3.50 0.34783 0.16850509 6.789621 0.586428983.60 0.33408 0.16055357 7.450111 0.596954723.70 0.32103 0.15313316 8.169066 0.606835573.80 0.30864 0.14619883 8.950585 0.61611903

*

T

T *

p

p *o

o

p

p *

V

V *

I

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Page 42: Tablas de Flujo Compresible (Version 1)

3.90 0.29688 0.13971012 9.798973 0.62484877

4.00 0.28571 0.13363062 10.718750 0.633064934.10 0.27510 0.12792751 11.714652 0.640804434.20 0.26502 0.12257111 12.791640 0.648101194.30 0.25543 0.11753458 13.954904 0.654986394.40 0.24631 0.11279356 15.209867 0.66148873

4.50 0.23762 0.10832593 16.562195 0.66763464.60 0.22936 0.10411155 18.017795 0.673448314.70 0.22148 0.10013209 19.582828 0.678952254.80 0.21398 0.09637078 21.263710 0.68416705

Tabla 2

Línea de Fanno; flujo de un gas perfecto, unidimensional, adiabático yde área constante

( Calor específico y peso molecular constantes )

k = 1.4

M

4.9 0.20683 0.09281233 23.067119 0.689111755 0.20000 0.08944272 25.000000 0.693803926 0.14634 0.06375767 53.179784 0.729875287 0.11111 0.04761905 104.142857 0.752802168 0.08696 0.03686049 190.109375 0.768191619 0.06977 0.02934836 327.189300 0.77898519

10 0.05714 0.02390457 535.937500 0.78683083

0.00000 0

0.79

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Page 43: Tablas de Flujo Compresible (Version 1)

M

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M

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M

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M

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M

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M

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M

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M

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M

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M

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Lmaxf

Dh

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Lmaxf

Dh

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Lmaxf

Dh

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Lmaxf

Dh

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Lmaxf

Dh

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Lmaxf

Dh

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Lmaxf

Dh