Tablas Listo

7/25/2019 Tablas Listo

1/101

t2[C] t1[C] T2[C] P entrada [psi]

43.2

16.2

86.6

2

50.1 97.9

51.4 98.0

54.0 97.0

60.6 97.5

Tw[C]

1 2 3 4

97.3 96.2 97.7 94.1

t2[K] t1[K] T2[K] P[Kpa]

316.4

289.4

359.8

13.790

323.3 371.1

324.6 371.2

327.2 370.2

333.8 370.7

Cp agua [J/(Kg*K)] Masa agua [Kg]

29.7 4178.12 6.0780

33.15 4178 6.1440

33.8 4178 5.2100

35.1 4178.02 5.5740

38.4 4178.68 4.2360

Interpolacin

a T constante

T cp agua

25 4180

30 4178

35 4178

40 4179

T2[C] Temperatura de entrada [C]

Temppr!medi!

Masa "!ndensad![Kg]


2/101

86.6

101.9780259657

0.3920

97.9 0.3740

98.0 0.3000

97.0 0.3240

97.5 0.3020

Interpolacin

a P constante

P[kPa] T[C]

101.325 99.97

125 105.97

Calculo de calor del vapor

# $ap!r entrada[K%/Kg] #& $ap!r sa

0.0333

2633.6823

362.

0.0314 410.

0.0275 410.

0.0238 406.

0.0163 408.

endimient!

76.48%

103.91%

114.08%

121.13%

116.13%

Calculo coefciente global de transer

64.4144

0.5319231584

65.6642

64.9429

62.9698

59.1090

Calculo velocidad

u%! msi"!t!ta' $ap!r

[Kg/s]

Temperaturalogaritmica [K]

Area de transerencia[m!]


3/101

densidad

29.7 0.1708263069

0.0002968126

996

33.15 0.1705245629 994

33.8 0.1583105439 994

35.1 0.1357195033 993.

38.4 0.0757917338 992.

T[C]

25

30

35

40

"e#nold

29.7 8.0358E-04 8.0676E-07

33.15 7.4886E-04 7.5282E-07

33.8 7.3872E-04 7.4282E-07

35.1 7.1866E-04 7.2303E-07

38.4 6.7444E-04 6.7939E-07

T[C] visc

25 8.91E-04

30 7.98E-04

35 7.20E-04

40 6.53E-04

Perdidas de calor al ambiente

calo co!v"cci#!

Tw pr!m [C] Tin& e-t [C] T pe'i"u'a [K]

95.95 25 60.48 333.63

calo a$iaci#!

Temppr!medi!

'u%! masi"!en du"t!

[Kg/s]

area du"t![m,2]

Temppr!medi!

.is"!sidad dinmi"a[m,2/s]

.is"!sidad"inemti"a [m,2/s]

T pe'i"u'a[C]


4/101


95.95 25 60.48 333.63

620.225687

Placas sol$a$as

t2[C] t1[C] T2[C] P entrada [psi]

40.0

16.2

21.0

2

41.5 20.8

43.6 20.8

63.2 21.3

79.4 23.2

Tw[C]

1 2 3 4

95.2 41.1 25 86.8

t2[K] t1[K] T2[K] P[Kpa]

313.2

289 4

294.2

13 790

314.7 294.0

316 8 294 0

T pe'i"u'a[C]

t!ta'perdid! [0]


5/101

336.4 294.5

352.6 296.4

Cp agua [J/(Kg*K)] Masa agua [Kg]

28.1 4178.76 5.3440

28.85 4178.46 5.7000

29.9 4178.04 4.8620

39.7 4178.94 4.3480

47.8 4180.56 3.2120

Interpolacin

a T constante

T cp agua

25 4180

30 4178

35 4178

40 4179

45 4180

50 4181

T2[C] Temperatura de entrada [C]

21.0

101.9780259657

0.1660

20.8 0.1920

20.8 0.1800

21.3 0.2880

23.2 0.2920

Interpolacin

a P constante

P[kPa] T[C]

101.325 99.97

125 105.97

Calculo $" calo $"l vapo

# $ap!r entrada[K%/Kg] #& $ap!r sa

0.0112 88.1

Temppr!medi!

Masa "!ndensad![Kg]

u%! msi"!t!ta' $ap!r

[Kg/s]


6/101

0.0117

2633.6823

87.2

0.0110 87.2

0.0109 89.3

0.0108 97.3

Rendimiento %

1.2488493952 124.88493951921.2237545738 122.37545738

1.2057285279 120.5728527852

1.1571869708 115.7186970808

1.1377634126 113.7763412571

Calculo coefciente global de transerencia de calor

22.3512

0.6

21.6899

21.1651

16.6015

13.3024

Calculo velocidad

densidad

28.1 0.0298480786

0.0001938

996.

28.85 0.0288578372 995.

29.9 0.0246751929 995.

39.7 0.0136215539 992.

47.8 0.0098660769 989.

T[C]

25

30

35

40

"e#nold

Temperaturalogaritmica [K] Area de transerencia[m!]

Temppr!medi!

'u%! masi"!en du"t!

[Kg/s]

areatrans$ersa'du"t! [m,2]

Temppr!medi!

.is"!sidad dinmi"a[m,2/s]

.is"!sidad"inemti"a [m,2/s]


7/101

28.1 8.3520E-04 8.3834E-07

28.85 8.2332E-04 8.2663E-07

29.9 8.0668E-04 8.1021E-07

39.7 6.5145E-04 6.5646E-07

47.8 5.2315E-04 5.2861E-07

T[C] visc

25 8.91E-0430 7.98E-04

35 7.20E-04

40 6.53E-04

Perdidas de calor al ambiente

calo co!v"cci#!


52.88 25 38.94 312.09

calo a$iaci#!


52.88 25 38.94 312.09

14.1658332

T pe'i"u'a[C]

T pe'i"u'a[C]

t!ta'perdid! [0]


8/101

magua[gr] m"!nd[gr] [s] Tw pr!m [C] Tin& e-t[C]

6386 778 11.86

95.95 25

6452 760 12.01

5518 686 10.97

5882 710 13.69

4544 688 18.63

5 6 7

95.9 95.6 95.2 95.2 91.9

magua[+g] m"!nd [Kg] [s] Tw[K] Tin& e-t[C]

6.3860 0.7780 11.86

369.10 298

6.4520 0.7600 12.01

5.5180 0.6860 10.97

5.8820 0.7100 13.69

4.5440 0.6880 18.63

0.5125 57812.36 57.81

0.5116 72456.33 72.46

0.4749 69846.11 69.85

0.4072 64302.20 64.30

0.2274 42185.69 42.19

#& $ap!r entrada [K%/Kg] #&g $ap!r entrada[K%/Kg]

u%! msi"! agua[Kg/s]

'u%! Ca'!r agua[0]

'u%! Ca'!ragua [+0]

u%! msi"!"!ndensad![Kg/s]


9/101

0.0331

427.5272 2251.1787

0.0311

0.0273

0.0237

0.0162

Interpolacin Interpolacin

a p constante a p constante

P[kPa] &' vapo P[kPa] &' vapo

101.325 419.06 101.325 2256.5

125 444.36 125 2240.6

'ida[K%/Kg] Ca'!r $ap!r [+0]

464 75.5953

164 69.7314

380 61.2254

220 53.0862

300 36.3264

ncia de calor Uo

Uo [$%m!&K]

1687.287319805

2074.429494312

2021.907543588

1919.750758799

1341.722773614


10/101

[+g/m,3]

.06 0.5778123891

.74 0.5775571444

.48 0.5363291291

962 0.4600341559

708 0.2572278084

$"!si$a$

997

996

994

992.1

e 8stad! Pr

13923.2 Turbulento 5.4632 0.0288

14914.2 Turbulento 5.0483 0.0282

14036.0 Turbulento 4.9716 0.0287

12368.9 Turbulento 4.8198 0.0297

7360.2 Turbulento 4.4832 0.0344

T[C] P

25 6.14

30 5.42

35 4.83

40 4.32

densidad [+g/m,3] K [0/(m*K)] .is"!sidad "in

1.049496 2.88E-02 1.9

T[C] $"!si$a$ T[C] ( T[C]

300 1.1614 300 2.63E-02 300

350 0.995 350 3.00E-02 350

$e'!"idad media[m/s]

a"t!r de&ri""i9n &


11/101

5.67E-08 0.81 368.18616

magua[gr] m"!nd[gr] [s] Tw pr!m [C] Tin& e-t[C]

5652 552 14.92

52.88 25

6008 578 16.46

5170 566 16.42

4656 674 26.60

3520 678 27.13

Pr!medi!

42.2 27 52.883333333

magua[+g] m"!nd[Kg] [s] Tw[K] Tin& e-t[C]

5.6520 0.5520 14.92

326 03 298

6.0080 0.5780 16.46

5 1700 0 5660 16 42

C!nstante de:te&an ;!'t


12/101

4.6560 0.6740 26.60

3.5200 0.6780 27.13

0.3582 35622.30 35.62

0.3463 36608.49 36.61

0.2961 33897.29 33.90

0.1635 32104.94 32.10

0.1184 31280.76 31.28

#& $ap!r entrada [K%/Kg] #&g $ap!r entrada[K%/Kg]

0.0111

427.5272 2251.1787

0.0117

0.0110

0.0108

0.0108

Interpolacin Interpolacin

a p constante a p constante

P[kPa] &' vapo P[kPa] &' vapo

101.325 419.06 101.325 2256.5

125 444.36 125 2240.6

'ida[K%/Kg] Ca'!r $ap!r [+0]

180 28.5241

u%! msi"! agua[Kg/s]

'u%! Ca'!r agua[0]

'u%! Ca'!ragua [+0]

u%! msi"!"!ndensad!

[Kg/s]


13/101

774 29.9149

774 28.1135

789 27.7440

646 27.4932

o

Uo [$%m!&K]

2656.256344396

2813.021656172

2669.276488472

3223.096160699

3919.181211586

[+g/m,3]

)*+"o $" pl

446 0.1545954213 12

941 0.1495041473

434 0.127880099 $i+"!sio!"s

702 0.070827052 alo+/

648 0.0514401943 0.3$"!si$a$

997

996

994

992.1

e 8stad! Pr

$e'!"idad media[m/s]

an"#!/espes!r de p'a"a


14/101

687.9 Laminar 5.7099

53.6842

674.7 Laminar 5.5557

588.8 Laminar 5.4318

402.5 Laminar 4.3506

363.0 Laminar 3.5244

T[C] P

25 6.1430 5.42

35 4.83

40 4.32

densidad [+g/m,3] K [0/(m*K)] .is"!sidad "in

1.1211589333 2.72E-02 1.71

T[(] $"!si$a$ T[(] ( T[C]

300 1.1614 300 2.63E-02 300

350 0.995 350 3.00E-02 350

5.67E-08 0.70 8.25181567

C!nstante de:te&an ;!'t


15/101

Masa pr!=eta [gr]

716

308 386

1> 11 12 Pr!medi!

98.5 97.9 95.9 95.95

Masa pr!=eta [Kg]

95.4588157895

0.308 0.386

Presi!n a=s!'uta +P?

entrada [+Pa]

109.248

# $ap!r entrada[K%/Kg] #& $ap!r sa'ida[K%/Kg]

Patm(mm@g)

Masa =a'de[gr]

Patm(KPa)

Masa =a'de[Kg]


16/101

2633.6823

362.7464

410.3164

410.7380

406.5220

408.6300

Interpolacin

a T constante

T[C] &' vapo

85 356.02

90 377.04

95 398.09

100 419.17


17/101

Au Bnie'ins+i K [0/(m*K)] # [0/(m,2*K)]

97.5776 0.6145 3084.54

100.5223 0.6200 3206.16

94.6750 0.6211 3024.73

83.5426 0.6232 2678.01

50.3948 0.6284 1629.12

T[C] k

25 0.607

30 0.615

35 0.623

40 0.631

emti"a [m,2/s] Pr [1/K]

E-05 0.7023 2.9974E-03

visc T[C] P

1.59E-05 300 0.7070

2.09E-05 350 0.7000


18/101

Masa pr!=eta [gr]

716

308 386

Masa pr!=eta [Kg]

95 4588157895

0.308 0.386

Presi!n a=s!'uta +P?

Patm(mm@g)

Masa =a'de[gr]

Patm(KPa)

Masa =a'de[Kg]


19/101

entrada [+Pa]

109.248

# $ap!r entrada[K%/Kg] #& $ap!r sa'ida[K%/Kg]

2633.6823

88.1180

87.2774

87.2774

89.3789

97.3646

Interpolacin

a T constante

T[C] &' vapo

20 83.915

25 104.93


20/101

cas po $o!$" cicula agua ',a

lacas sol$a$as

a!c&o+/ s"paaci#! "!" placas+/

0.102 0.0019

pgi!a 450 i!cop"a

Au K [0/(m*K)] # [0/(m,2*K)]

. . . ..

.

.

.

.

.

.

.

..

co co"ci"!

Co"ci"!


21/101

8.2300 0.6120 1350.06

8.2300 0.6132 1352.71

8.2300 0.6148 1356.42

8.2300 0.6305 1391.01

8.2300 0.6435 1419.60

T[C] k

25 0.60730 0.615

35 0.623

40 0.631

emti"a [m,2/s] Pr [1/K]

E-05 0.7053 3.2042E-03

visc T[(] P

1.59E-05 300 0.7070

2.09E-05 350 0.7000


22/101#& sa'ida trampa $ap!r[K%/Kg] #&g sa'ida tra


23/101

411.5029 22

Interpolacin Inter

a P constante a P c

P[kPa] &' vapo P[kPa]

75 384.44 75

100 417.51 100


24/101

Br a Au

14667202 10300666 28.462

7000.0 9000.0 11000.0 13000.0 150 .1500.00

1700.00

1900.00

2100.00

2300.00

2500.00

2700.00

2900.00

3100.00

3300.00

'/ 0.2120994851 68.9150177818 0.9968293762

co co"ci"!" p"licula vs "!ol$s paa las u:",as "! u! ;

"!ol$s o:"!i$os

Co"ci"!" p"licula &


25/101


26/101

#& sa'ida trampa $ap!r[K%/Kg] #&g sa'ida tra

411.5029 22

Interpolacin Inter

a P constante a P c

P[kPa] &' vapo P[kPa]

75 384.44 75

100 417.51 100


27/101

$i+"o &i$ulico

0.0037305101

300.0 350.0 400.0 450.0 500.0 550.0 600.0 650.0 700.0 750.01300.00

1320.00

1340.00

1360.00

1380.00

1400.00

1420.00

1440.00

'/ - 0.1909172931 1477.7042971375 0.9110210631

" p"licula vs "!ol$s paa las u:",as "! u! ;C $" placas sol$a$as

"!ol$s o:"!i$os

" p"licula &


28/101

=o!giu$ caac",sica

0.3

Br a Au

40434022 28518406 38.232


29/101mpa $ap!r[K%/Kg] D $ap!r &'as# D "!ndensad!


30/101

61.2238 0.7087 99.2913

polacin

onstante

&'g vapo

2278

2257.5


31/101

'i(metro cora)a *m+ 0.1735

,argo cora)a *m+ 1.38

Area superfcial [m!] 0.752191529

# "!n$ [0/m,2*K] "!n$ [0]

4.7227 252.039526271

00.0 17000.0

$" u:os coa


32/101


33/101

mpa $ap!r[K%/Kg] D $ap!r &'as# D "!ndensad!

61.2238 0.7087 99.2913

polacin

onstante

&'g vapo

2278

2257.5


34/101


35/101

Area superfcial [m!] 0.0612

# "!n$ [0/m,2*K] "!n$ [0]

3.4657 5.9140175585


36/101u%! msi"! t!ta' $ap!r

[Kg/s]


37/101

0.0333

0.0314

0.0275

0.0238

0.0163


38/101


39/101


40/101

0.0112

0.0117

0.0110

0.0109

0.0108

u%! msi"! t!ta' $ap!r[Kg/s]


41/101


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99/101

Medi"i!nes t2[C] t1[C] T2[C] P entrada [psi] magua[gr]

1 43.2

16.2

86.6

2

6386

2 50.1 97.9 6452

3 51.4 98.0 55184 54.0 97.0 5882

5 60.6 97.5 4544

Medi"i!nes m"!nd[gr] [s] Tw pr!m [C] Tin& e-t[C]

1 778 11.86

95.95 25 716

2 760 12.01

3 686 10.97

4 710 13.69

5 688 18.63

Patm(mm@g)


100/101

Tw[C]1 2 3 4

97.3 96.2 97.7 94.1 95.9

5 6 7 1> 11

95.2 95.2 91.9 98.5 97.9

Pr!medi!

as$a$

$a$


101/101

95.6

12

95.9

95.95

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