resultados labo caudal

Presión(Psi) presion (KPa)Temperatura Subida

40 275.788 139.3 147 143.1550 344.735 145 152 148.560 413.682 150 158 15465 448.1555 152 160 15670 482.629 155 163 15975 517.1025 157 165 16180 551.576 159 167 16385 586.0495 161 170 165.590 620.523 164 171 167.595 654.9965 166 173 169.5

100 689.47 168 175 171.5105 723.9435 170 177 173.5110 758.417 171 178 174.5115 792.8905 173 179 176120 827.364 175 179 177125 861.8375 177 180 178.5130 896.311 178 178.5

Presión

143.15 275.788 141.668823700372148.5 344.735 148.921831855408154 413.682 154.548662584257156 448.1555 157.014673504332159 482.629 159.313549011284161 517.1025 161.475269021748163 551.576 163.521796635186

165.5 586.0495 165.469792520151167.5 620.523 167.332250851522169.5 654.9965 169.119538395842171.5 689.47 170.840083100031173.5 723.9435 172.500846687686174.5 758.417 174.107658714746176 792.8905 175.665458708275177 827.364 177.178475530812

178.5 861.8375 178.650362784465178.5 896.311 180.084302747188

Temperatura Bajada

Tempertatura Promedio

Temperatura experimental

promedio (Kpa)temperatura

teórica

P1 (Psi) P3 (mmHg)

18 13 145 37038 34 145 405

P1 (Psi) P3 (mmHg)

18 13 145 37038 34 145 405

Ensayo P3 (mmHg)

1 13 145 2617.82 34 145 2615.1

Ensayo P2 (Psi)

1 18 124.1 105.972 38 262 76.734

Ensayo X11 0.9432 0.94

Temperatura T3 (°F)

Volumen Condensado (cc)

Temperatura T3 (°F)

Volumen Condensado (cc)

T3 (˚F) h3 (KJ/Kg)

P2 (KPa) T2 (˚C)

error Hfg experimental hfg tablas error

1.05% 2489.44825727094 2172 14.62%0.28% 2585.32672471543 2147.7 20.38%0.36% 2687.76196272934 2135.4 25.87%0.65% 2665.83100317055 2120.3 25.73%0.20% 2738.29446518299 2114 29.53%0.29% 2722.73033232367 2100 29.65%0.32% 2711.69599058987 2096 29.37%0.02% 2742.84854508574 2090 31.24%0.10% 2737.14673315626 2080 31.59%0.22% 2734.26818210574 2075 31.77%0.39% 2733.80309419543 2069 32.13%0.58% 2735.41972839873 2060 32.79%0.23% 2674.7191281602 2055 30.16%0.19% 2650.61259860901 2049 29.36%0.10% 2599.63160108489 2042 27.31%0.08% 2582.08724091406 2036 26.82%0.88% 2482.7761931866 2030 22.30%

1010

1010

15.246 0.024268660632315.34 0.0264015645372

440.28 2684.9 0.971548.86 2172 0.97

Volumen Salida (cc)

Volumen Salida (cc)

v (m3/kg) mc (Kg)

hf (KJ/Kg)

hfg (KJ/Kg) x2

140 145 150 155 160 165 170 175 180 1850

100

200

300

400

500

600

700

800

900

1000

f(x) = 0.213339401229721 x² − 52.4765370961486 x + 3429.16797279112

Diagrama Presión en función de la Temperatura del Vapor

Temperatura (°C)Pr

esió

n (K

Pa)

140 145 150 155 160 165 170 175 180 1850

100

200

300

400

500

600

700

800

900

1000

f(x) = 0.213339401229721 x² − 52.4765370961486 x + 3429.16797279112

Diagrama Presión en función de la Temperatura del Vapor

Temperatura (°C)

Pres

ión

(KPa

)