Lala
4
Sistema: Metanol(A) Agua(B) DIAGRAMA T-x,y a Presió Constantes d A1 7.87863 8.07131 presión en K A2 1473.11 1730.63 Ingrese la Presión, mmM A3 230 233.426 T °C 99.99682973 98.23482973 A12 0.7923 96.47282973 A21 0.5434 94.71082973 92.94882973 91.18682973 89.42482973 87.66282973 85.90082973 84.13882973 82.37682973 80.61482973 78.85282973 77.09082973 75.32882973 73.56682973 71.80482973 70.04282973 68.28082973 66.51882973 64.75 2 1 3 sat A lnP A T A B vB A A vA B vB A vA A A P P x P P P y x P
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Transcript of Lala
Sistema: Metanol(A) Agua(B) DIAGRAMA T-x,y a Presión constanteConstantes d A1 7.87863 8.07131
presión en Ki A2 1473.11 1730.63 Ingrese la Presión, mmMercurio, =A3 230 233.426 TsA=
TsB=
T °C PsA99.99682973 2597.870018298.23482973 2458.4088822
A12 0.7923 96.47282973 2325.0492205A21 0.5434 94.71082973 2197.5932452
92.94882973 2075.846779491.18682973 1959.619278489.42482973 1848.72384887.66282973 1742.977261385.90082973 1642.199972584.13882973 1546.216129182.37682973 1454.853581280.61482973 1367.943889178.85282973 1285.322327877.09082973 1206.827889875.32882973 1132.30328573.56682973 1061.594938571.80482973 994.5529857470.04282973 931.0312655168.28082973 870.8873102366.51882973 813.98233389
64.75 759.97854461
21
3
sat AlnP A
T A
B vBA
A vA B vB
A vAA A
P Px
P P
Py x
P
760 1 atm64.75072308 puro
99.99682974 puro
Raoult-DaltonPsB xAsupuesto xA calculado yA xA
759.9999998 1.84E-11 4.29753653 1 1.5625748E-11 2.703558E-10713.2442328 0.004346697 4.24584523 1.00633247 0.004345476 0.0596985868668.9110709 0.009074182 4.19073269 1.0132077 0.0090729025 0.1163365027626.9013319 0.01421165 4.13211485 1.02066464 0.0142336321 0.1698050519587.1186109 0.019851271 4.06925292 1.02883256 0.0198841378 0.2206402313549.4692525 0.026082379 4.00155065 1.03783475 0.0260947593 0.2691123513513.8623217 0.032950638 3.92898645 1.04772943 0.0329522671 0.3149218618480.2095743 0.04055767 3.85104725 1.05865308 0.0405590276 0.3582036222
448.425425 0.04903017 3.76712704 1.0707744 0.0490408462 0.3991040299418.426915 0.058543476 3.67636251 1.08432617 0.0585555315 0.4378783169
390.1336785 0.069349361 3.57749359 1.09964139 0.069307394 0.4749271775363.4679077 0.081571919 3.47078566 1.11686096 0.0815442857 0.5095926612338.3543168 0.095626141 3.35439504 1.13651999 0.0956098849 0.542486952314.7201055 0.112396591 3.22372209 1.15977292 0.1120405823 0.575363729292.4949208 0.131523717 3.08472581 1.18600876 0.1313114631 0.6044631316271.6108182 0.154646191 2.92966952 1.21730172 0.1544771454 0.6328533856252.0022218 0.183734655 2.75260866 1.25598047 0.183176722 0.661835234233.6058838 0.219622205 2.55827082 1.3025927 0.2193495103 0.6882931363
216.360843 0.273001138 2.31048703 1.36954786 0.2702342834 0.7227970366200.2083824 0.342602944 2.04647887 1.45238467 0.3412467287 0.7509304957185.0353377 1.000056465 0.99996128 1.98548996 1.0001296228 0.9999895071
A B
Temperatura Liquido Vapor Temperatura100 0 0 100
96.4 0.02 0.134 96.493.5 0.04 0.23 93.591.2 0.06 0.304 91.289.3 0.08 0.365 89.387.7 0.1 0.418 87.784.4 0.15 0.517 84.481.7 0.2 0.579 81.7
78 0.3 0.665 7875.3 0.4 0.729 75.373.1 0.5 0.779 73.171.2 0.6 0.825 71.269.3 0.7 0.87 69.367.5 0.8 0.915 67.5
66 0.9 0.958 6665 0.95 0.979 65
64.5 1 1 64.5
Raoult-DaltonyA
