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CALCULO DE FLUJOS Y PRESIONES POR ECUACIONES SEMIEMPIRICAS
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CALCULO DE CAUDALES CON ECUACIONES SEMIEMPIRICAS
DATOS: ECUACION DE PANHANDLE A
Propiedades del Gas Natural:
G 0.6193
G 0.6193
Tf 80 oF 540 oR
Nodo P Tuberia DN Di Pp Z S Le Q Q3=Q1+Q2 Q3a‐Q3
No (m) (pies) (Psia) No (Km) millas (pulg) (pulg) (Psia) (millas) (pie3/dia) (pie3/dia) (pie3/dia)
1 1000 3280 8400 1500 0000 1 20 12 427 8 7 625 1337 756 0 7916 ‐0 0178245 12 3169 84483896 9
L
Elevación:H
1 1000 3280.8400 1500.0000 1 20 12.427 8 7.625 1337.756 0.7916 ‐0.0178245 12.3169 84483896.9
2 900 2952.7560 1200.0000 2 30 18.641 8 7.625 1180.671 0.8092 0 18.6410 19194201.4
3 900 2952.7560 1161.1280 3 10 6.214 10 9.562 1106.495 0.8183 0.00862147 6.2409 103678176.0 103678098.2 ‐77.79
4 950 3116.7980 1050.0000 4 5 3.107 6 5.761 940.524 0.8406 0 3.1070 54384536.4 Q3=Q4+Q5
5 950 3116.7980 821.7725 5 6 3.728 6 5.761 940.524 0.8406 0 3.7280 49293561.8 103678098.2 0.007
6 950 3116 7980 800 0000 6 10 6 214 10 7 859 810 935 0 8595 0 6 2140 103678098 2 0 00
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6 950 3116.7980 800.0000 6 10 6.214 10 7.859 810.935 0.8595 0 6.2140 103678098.2 0.00
DN= 10 pul Di= 9.562 pulg
P i d d d l G N t l ECUACION DE AGA
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Propiedades del Gas Natural: ECUACION DE AGA
G 0.6193 Tubería:
Tf 80 oF 540 oR e= 0.0018 pulg
Vis 1.431 9.60E‐06 lb/pie s
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Nodo P Tuberia DN Di Pp Z visc S Le Qs Re f Q Q3=Q1+Q2 Q3a‐Q3 Q‐Qs
No (m) (pies) (Psia) No (Km) millas (pulg) (pulg) (Psia) (lb/pie s) (millas) (pie3/dia) (pie3/dia) (pie3/dia) (pie3/dia)
1 1000 3280.8400 1500.0000 1 20 12.427 8 7.625 1337.546 0.7916 9.60E‐06 ‐0.0178245 12.3169 62270173.9 7115906.192 0.01421276 62270173.9 0.0
2 900 2952.7560 1200.0000 2 30 18.641 8 7.625 1180.442 0.8092 9.20E‐06 0 18.6410 15834883.2 1809526.719 0.01423575 15834883.2 0.0
3 900 2952.7560 1160.6656 3 10 6.214 10 9.562 1106.256 0.8183 9.10E‐06 0.00862147 6.2409 78105109.2 7117388.762 0.01357082 78105109.2 78105057.1 ‐52.10 0.0
Elevación:H L
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4 950 3116.7980 1050.0000 4 5 3.107 6 5.761 931.205 0.8419 8.70E‐06 0 3.1070 40830761.2 6175606.064 0.01507438 40830761.2 Q3=Q4+Q5 0.0
5 950 3116.7980 801.2700 5 6 3.728 6 5.761 931.205 0.8419 8.70E‐06 0 3.7280 37274315.0 5637697.626 0.01507510 37274315.0 78105076.2 ‐19.07 0.0
6 950 3116.7980 800.0000 6 10 6.214 10 8.0676481 800.635 0.8611 8.50E‐06 0 6.2140 78105057.1 8435720.705 0.01404725 78105057.1 0.00 0.0
DN= 10 pul Di= 9.562 pulg
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Calculo de Flujos GN-Ecuación Semiempirica.pdf

  • 1. CALCULO DE FLUJOS Y PRESIONES POR ECUACIONES SEMIEMPIRICAS 2 Re 5 . 14 7 . 3 / log Re 02 . 5 7 . 3 / log 2                                                  D D f CALCULO DE CAUDALES CON ECUACIONES SEMIEMPIRICAS DATOS: ECUACION DE PANHANDLE A Propiedades del Gas Natural: G 0.6193 G 0.6193 Tf 80 oF 540 oR Nodo P Tuberia DN Di Pp Z S Le Q Q3=Q1+Q2 Q3a‐Q3 No (m) (pies) (Psia) No (Km) millas (pulg) (pulg) (Psia) (millas) (pie3/dia) (pie3/dia) (pie3/dia) 1 1000 3280 8400 1500 0000 1 20 12 427 8 7 625 1337 756 0 7916 ‐0 0178245 12 3169 84483896 9 L Elevación:H 1 1000 3280.8400 1500.0000 1 20 12.427 8 7.625 1337.756 0.7916 ‐0.0178245 12.3169 84483896.9 2 900 2952.7560 1200.0000 2 30 18.641 8 7.625 1180.671 0.8092 0 18.6410 19194201.4 3 900 2952.7560 1161.1280 3 10 6.214 10 9.562 1106.495 0.8183 0.00862147 6.2409 103678176.0 103678098.2 ‐77.79 4 950 3116.7980 1050.0000 4 5 3.107 6 5.761 940.524 0.8406 0 3.1070 54384536.4 Q3=Q4+Q5 5 950 3116.7980 821.7725 5 6 3.728 6 5.761 940.524 0.8406 0 3.7280 49293561.8 103678098.2 0.007 6 950 3116 7980 800 0000 6 10 6 214 10 7 859 810 935 0 8595 0 6 2140 103678098 2 0 00 2 Re 5 . 14 7 . 3 / log Re 02 . 5 7 . 3 / log 2                                                  D D f 6 950 3116.7980 800.0000 6 10 6.214 10 7.859 810.935 0.8595 0 6.2140 103678098.2 0.00 DN= 10 pul Di= 9.562 pulg P i d d d l G N t l ECUACION DE AGA 2      Propiedades del Gas Natural: ECUACION DE AGA G 0.6193 Tubería: Tf 80 oF 540 oR e= 0.0018 pulg Vis 1.431 9.60E‐06 lb/pie s Re 5 . 14 7 . 3 / log Re 02 . 5 7 . 3 / log 2                                                 D D f Nodo P Tuberia DN Di Pp Z visc S Le Qs Re f Q Q3=Q1+Q2 Q3a‐Q3 Q‐Qs No (m) (pies) (Psia) No (Km) millas (pulg) (pulg) (Psia) (lb/pie s) (millas) (pie3/dia) (pie3/dia) (pie3/dia) (pie3/dia) 1 1000 3280.8400 1500.0000 1 20 12.427 8 7.625 1337.546 0.7916 9.60E‐06 ‐0.0178245 12.3169 62270173.9 7115906.192 0.01421276 62270173.9 0.0 2 900 2952.7560 1200.0000 2 30 18.641 8 7.625 1180.442 0.8092 9.20E‐06 0 18.6410 15834883.2 1809526.719 0.01423575 15834883.2 0.0 3 900 2952.7560 1160.6656 3 10 6.214 10 9.562 1106.256 0.8183 9.10E‐06 0.00862147 6.2409 78105109.2 7117388.762 0.01357082 78105109.2 78105057.1 ‐52.10 0.0 Elevación:H L 2 Re 5 . 14 7 . 3 / log Re 02 . 5 7 . 3 / log 2                                                  D D f 4 950 3116.7980 1050.0000 4 5 3.107 6 5.761 931.205 0.8419 8.70E‐06 0 3.1070 40830761.2 6175606.064 0.01507438 40830761.2 Q3=Q4+Q5 0.0 5 950 3116.7980 801.2700 5 6 3.728 6 5.761 931.205 0.8419 8.70E‐06 0 3.7280 37274315.0 5637697.626 0.01507510 37274315.0 78105076.2 ‐19.07 0.0 6 950 3116.7980 800.0000 6 10 6.214 10 8.0676481 800.635 0.8611 8.50E‐06 0 6.2140 78105057.1 8435720.705 0.01404725 78105057.1 0.00 0.0 DN= 10 pul Di= 9.562 pulg 2 Re 5 . 14 7 . 3 / log Re 02 . 5 7 . 3 / log 2                                                  D D f 2 Re 5 . 14 7 . 3 / log Re 02 . 5 7 . 3 / log 2                                                  D D f