• Author / Uploaded
• Luis Celis

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SQUARE Agua destilada flujo masico (kg/h) Tin Tout densidad viscosidad (miu) prandt K Cp temperatura media ΔP distacia entre bafles diametro coraza 3/4" OD numero de tubos Pt (m) Ds Np

Agua 80000 140000 35 20 25 25.7115716063 996 996.8576897 7.98E-04 8.78E-04 5.42 6.03753369 0.615 0.6081385146 4178 4180 estandar 30 22.8557858031 120000 12 in 0.3048

137 tabla 8,3 0.0254 0.38735 1

CORAZA H2O DESTILADA Acs Gs Vs De Res Nus ho Uf

0.02928366 758.860819386 0.7619084532 0.0239074987 22734.9173352603 TURBULENTO 154.824991666 3982.7407781668 1562.8725625068

Asf Lf friccion coraza fs Nbf ΔPsf

85.7940815732 Asc 10.4364674364 Lc 0.2644733276 33.2403787283 Nbc 42893.0910698956 ΔPsc

C

46.8415185492 5.6980618482 17.6944286357 23418.60282364

flujo masico (kg/s) Q(caliente) TABLA 8,1 do di mui w ΔTlm Kw

22.2222222222 flujo masico (kg/s) 928444.444444444 Q(frio)

0.0191 0.0166 8.64E-04 Tw 6.9242864451 52

38.8888889 928447.696

26.4278929

B

0.0063

TUBOS H2O Act Gt Vt Ret f Nut hi Uc

Fouling resistences 0.0296501316 1311.5924568244 1.3157268789 24804.4072535883 TURBULENTO 0.0061925332 433.2400230926 15871.6833800482 2862.5292319564

tubos ΔPt ΔPtc

agua destilada Agua de cuidad

6002324244409.4 3834054285473.52

tabla 5,11 0.000088 0.000176

SQUARE Agua destilada

Agua 80000 35 25 996 0.000798 5.42 0.615 4178 30 120000 12 in

flujo masico (kg/h) Tin Tout densidad viscosidad (miu) prandt K Cp temperatura media ΔP distacia entre bafles diametro coraza 3/4" OD numero de tubos Pt (m) Ds Np Nb CORAZA H2O DESTILADA Acs Gs Vs De Res Nus ho Uf

140000 20 25.7115716063 996.8576897 0.0008777648 6.03753369 0.6081385146 4180 estandar 22.8557858031

0.03312414 670.8769562688 0.6735712412 0.0239074987 20098.9848905924 TURBULENTO 144.6789921161 3721.7435986563 1486.4287250712

Asf Lf friccion coraza fs Nbf ΔPsf

90.2062869579 Asc 8.4933750213 Lc 0.270738824 26.8654036133 Nbc 31591.0110666444 ΔPsc

177 tabla 8,3 0.0254 0.43815 1 87.1410879702

0.3048

C

51.2537239339 4.8257955547 14.8326625811 17949.4912672459

flujo masico (kg/s) Q(caliente)

22.2222222 flujo masico (kg/s) 928444.444 Q(frio)

38.8888889 928447.696

TABLA 8,1 do di mui w ΔTlm Kw

0.0191 0.0166 0.00086444 Tw 6.92428645 52

26.4278929

B

0.0063

TUBOS H2O Act Gt Vt Ret f Nut hi Uc

Fouling resisttabla 5,11 0.0383071 1015.18738 1.01838747 19198.8915 TURBULENTO 0.00660668 357.746413 13105.9863 2616.10681

tubos ΔPt ΔPtc

3218990840401.53 2146310091922.07

agua destilad Agua de cuid

0.000088 0.000176

SQUARE Agua destilada

Agua 80000 140000 35 20 25 25.7115716063 996 996.8576897 0.000798 0.0008777648 5.42 6.03753369 0.615 0.6081385146 4178 4180 estandar 30 22.8557858031 120000 12 in

flujo masico (kg/h) Tin Tout densidad viscosidad (miu) prandt K Cp temperatura media ΔP distacia entre bafles diametro coraza 3/4" OD numero de tubos Pt (m) Ds Np Nb CORAZA H2O DESTILADA Acs Gs Vs De Res Nus ho Uf

0.03696462 601.1754543188 0.6035898136 0.0239074987 18010.7786681932 TURBULENTO 136.2079873503 3503.8342304739 1416.1073406338

Asf Lf friccion coraza fs Nbf ΔPsf

94.6857715293 Asc 7.0445533748 Lc 0.2764409957 22.1120517546 Nbc 23974.3568410093 ΔPsc

224 tabla 8,3 0.0254 0.48895 1 71.546101557

0.3048

C

55.7332085053 4.1465106713 12.6040376354 14111.6010042369

flujo masico (kg/s) Q(caliente) TABLA 8,1 do di mui w ΔTlm Kw

22.2222222222 flujo masico (kg/s) 928444.44444445 Q(frio)

0.0191 0.0166 0.0008644412 Tw 6.9242864451 52

38.8888888889 928447.695556

26.4278929016

B

0.0063

TUBOS H2O Act Gt Vt Ret f Nut hi Uc

Fouling resisttabla 5,11 0.0484790472 802.1793151113 0.8047079572 15170.552650632 TURBULENTO 0.0070251926 300.5786832343 11011.65505678 2405.8406058486

tubos ΔPt ΔPtc

1826792912243.07 1264035931231.52

agua destilad Agua de cuid

0.000088 0.000176

SQUARE Agua destilada Agua flujo masico (kg/h) 80000 140000 flujo masico (kg/s) Tin 35 20 Q(caliente) Tout 25 25.7115716063 densidad 996 996.8576897 TABLA 8,1 viscosidad (miu) 0.000798 0.0008777648 do prandt 5.42 6.03753369 di K 0.615 0.6081385146 mui w Cp 4178 4180 estandar ΔTlm temperatura media 30 22.8557858031 Kw ΔP 120000 distacia entre bafles 12 in 0.3048 B diametro coraza 3/4" OD numero de tubos 124 tabla 8,3 Pt (m) 0.0254 C 0.0063 Ds 0.38735 Np 2 Nb 72.1686204095 CORAZA H2O DESTILADA TUBOS H2O Acs 0.02928366 Act Gs 758.860819386 Gt Vs 0.7619084532 Vt De 0.0239074987 Ret Res 22734.9173352603 TURBULENTO f Nus 154.824991666 Nut ho 3982.7407781668 hi Uf 1647.5966535755 Uc P 0.3807714404 R Asf 105.691307353 Asc 55.10356317 Lf 7.1023872687 Lc 3.702923687 friccion coraza fs 0.2644733276 Nbf 22.3017955008 Nbc 11.14869976 ΔPsf 29190.2739873062 ΔPsc 15218.73602

22.22222222 flujo masico (kg/s) 928444.4444 Q(frio)

38.8888889 928447.696

0.0191 0.0166 0.000864441 Tw 6.924286445 52

26.4278929

Fouling resisttabla 5,11 0.013418308 2898.196235 2.907331974 54809.73861 TURBULENTO 0.005131053 793.2890204 29062.02449 3160.17031 1.750831591 F

tubos ΔPt ΔPtc

38275982224265.2 25689122292704.8

agua destilad Agua de cuid

0.77

0.000088 0.000176

SQUARE Agua destilada flujo masico (kg/h) Tin Tout densidad viscosidad (miu) prandt K Cp temperatura media ΔP distacia entre bafles diametro coraza 3/4" OD numero de tubos Pt (m) Ds Np Nb CORAZA H2O DESTILADA Acs Gs Vs De Res Nus ho Uf P Asf Lf friccion coraza fs Nbf ΔPsf

Agua 80000 140000 flujo masico (kg/s) 35 20 Q(caliente) 25 25.7115716063 996 996.8576897 TABLA 8,1 0.000798 0.0008777648 do 5.42 6.03753369 di 0.615 0.6081385146 mui w 4178 4180 estandar ΔTlm 30 22.8557858031 Kw 120000 12 in 0.3048 B

166 tabla 8,3 0.0254 0.43815 2 55.4207036808 0.03312414 670.8769562688 0.6735712412 0.0239074987 20098.9848905924 TURBULENTO 144.6789921161 3721.7435986563 1575.9896545196 0.3807714404 110.4935199336 Asc 5.5464548909 Lc 0.270738824 17.1970304819 Nbc 20629.9754100784 ΔPsc

C

0.0063

TUBOS H2O Act Gt Vt Ret f Nut hi Uc R 59.9057757 3.00709655 8.86580234 11184.8612

22.2222222 flujo masico (kg/s) 928444.444 Q(frio)

38.8888889 928447.696

0.0191 0.0166 0.00086444 Tw 6.92428645 52

26.4278929

Fouling resistences 0.01796322 2164.91767 2.17174196 40942.2144 TURBULENTO 0.0054874 633.714896 23216.0503 2906.84232 1.75083159 F

tubos ΔPt ΔPtc

18938892519652.7 13328175627870.1

agua destilada Agua de cuidad

0.77

tabla 5,11 0.000088 0.000176

SQUARE Agua destilada flujo masico (kg/h) Tin Tout densidad viscosidad (miu) prandt K Cp temperatura media ΔP distacia entre bafles diametro coraza 3/4" OD numero de tubos Pt (m) Ds Np Nb CORAZA H2O DESTILADA Acs Gs Vs De Res Nus ho Uf P Asf Lf friccion coraza fs Nbf ΔPsf

Agua 80000 35 25 996 0.000798 5.42 0.615 4178 30 120000 12 in

140000 20 25.7115716063 996.8576897 0.0008777648 6.03753369 0.6081385146 4180 estandar 22.8557858031

220 tabla 8,3 0.0254 0.48895 2 42.7953840217 0.03696462 601.1754543188 0.6035898136 0.0239074987 18010.7786681932 TURBULENTO 136.2079873503 3503.8342304739 1508.0741977605 0.3807714404 115.4695468999 Asc 4.3735243136 Lc 0.2764409957 13.3488330498 Nbc 14884.1845562489 ΔPsc

0.3048

C

64.8818027128 2.457463022 7.0625427231 8363.3542509448

flujo masico (kg/s) Q(caliente)

22.2222222222 flujo masico (kg/s) 928444.444444444 Q(frio)

TABLA 8,1 do di mui w ΔTlm Kw

0.0191 0.0166 0.0008644412 Tw 6.9242864451 52

38.8888889 928447.696

26.4278929

B

0.0063

TUBOS H2O Act Gt Vt Ret f Nut hi Uc R

Fouling resisttabla 5,11 0.023806675 1633.5287871358 1.638678022 30892.7617612872 TURBULENTO 0.0058678767 511.3058619914 18731.6136998627 2683.9057644185 1.7508315906 F

tubos ΔPt ΔPtc

9688620775114.11 7111178687797.58

agua destilad Agua de cuid

0.77

0.000088 0.000176

SQUARE Agua destilada flujo masico (kg/h) Tin Tout densidad viscosidad (miu) prandt K Cp temperatura media ΔP distacia entre bafles diametro coraza 3/4" OD numero de tubos Pt (m) Ds Np Nb CORAZA H2O DESTILADA Acs Gs Vs De Res Nus ho Uf P Asf Lf friccion coraza fs Nbf ΔPsf

Agua 80000 140000 35 20 25 25.7115716063 996 996.8576897 0.000798 0.0008777648 5.42 6.03753369 0.615 0.6081385146 4178 4180 estandar 30 22.8557858031 120000 12 in

116 tabla 8,3 0.0254 0.38735 4 35.3849814841 0.02928366 758.860819386 0.7619084532 0.0239074987 22734.9173352603 TURBULENTO 154.824991666 3982.7407781668 1697.2373227338 0.3807714404 102.60005597 Asc 3.6850753902 Lc 0.2644733276 11.0901423564 Nbc 15145.3808748332 ΔPsc

0.3048

C

52.0123117829 1.8681207172 5.1290049776 7677.8347212926

flujo masico (kg/s) Q(caliente)

22.2222222 flujo masico (kg/s) 928444.444 Q(frio)

38.8888889 928447.696

TABLA 8,1 do di mui w ΔTlm Kw

0.0191 0.0166 0.00086444 Tw 6.92428645 52

26.4278929

B

0.0063

TUBOS H2O Act Gt Vt Ret f Nut hi Uc R

Fouling resisttabla 5,11 0.00627631 6196.14368 6.21567526 117179.441 TURBULENTO 0.0043506 1438.10377 52684.7162 3347.98893 1.75083159 F

tubos ΔPt ΔPtc

215261126696872 163116268770403

agua destilad Agua de cuid

0.77

0.000088 0.000176

SQUARE Agua destilada flujo masico (kg/h) Tin Tout densidad viscosidad (miu) prandt K Cp temperatura media ΔP distacia entre bafles diametro coraza 3/4" OD numero de tubos Pt (m) Ds Np Nb CORAZA H2O DESTILADA Acs Gs Vs De Res Nus ho Uf P Asf Lf friccion coraza fs Nbf ΔPsf

Agua 80000 140000 flujo masico (kg/s) 35 20 Q(caliente) 25 25.711571606 996 996.8576897 TABLA 8,1 0.000798 0.0008777648 do 5.42 6.03753369 di 0.615 0.6081385146 mui w 4178 4180 estandar ΔTlm 30 22.855785803 Kw 120000 12 in 0.3048 B

158 tabla 8,3 0.0254 0.43815 4 26.0088873296 0.03312414 670.8769562688 0.6735712412 0.0239074987 20098.9848905924 TURBULENTO 144.6789921161 3721.7435986563 1631.7911195186 0.3807714404 106.7150336976 Asc 2.8140077399 Lc 0.270738824 8.2323088581 Nbc 10466.6695431161 ΔPsc

C

22.2222222 928444.444

0.0191 0.0166 0.00086444 6.92428645 52

0.0063

TUBOS H2O Act Gt Vt Ret f Nut hi Uc R

0.00854876 4549.06751 4.56340715 86030.4758 0.00464495 1127.2357 41296.1112 3102.5308 1.75083159

56.1272895 1.48004102 3.85577762 5504.99561

tubos ΔPt ΔPtc

flujo masico (kg/s) Q(frio)

38.8888889 928447.696

Tw

26.4278929

Fouling resisttabla 5,11 agua destilad Agua de cuid TURBULENTO

F

0.77

105499592189680 83468009115263.6

0.000088 0.000176

SQUARE flujo masico (kg/h) Tin Tout densidad viscosidad (miu) prandt K Cp temperatura media ΔP distacia entre bafles diametro coraza 3/4" OD numero de tubos Pt (m) Ds Np Nb CORAZA H2O DESTILADA Acs Gs Vs De Res Nus ho Uf P Asf Lf friccion coraza fs Nbf ΔPsf

Agua destilada Agua cruda 80000 140000 flujo masico (kg/s) 35 20 Q(caliente) 25 25.7115716063 996 996.8576897 TABLA 8,1 0.000798 0.00096386 do 5.42 6.03753369 di 0.615 0.6031 mui w 4178 4180.8577 estandar ΔTlm 30 22.8557858031 Kw 120000 12 in 0.3048 B

204 tabla 8,3 0.0254 0.48895 4 20.1643324181 0.03696462 601.1754543188 0.6035898136 0.0239074987 18010.7786681932 TURBULENTO 136.2079873503 3503.8342304739 1566.0071628898 0.3807714404 111.1978593926 Asc 2.2710308212 Lc 0.2764409957 6.450888521 Nbc 7728.8793778693 ΔPsc

C

22.2222222 928444.444

0.0191 0.0166 0.00086444 6.92428645 52

0.0063

TUBOS H2O Act Gt Vt Ret f Nut hi Uc R

0.01103764 3523.29738 3.53440358 60679.701 0.0050149 858.373194 31185.8357 2873.06242 1.75083159

60.6101152 1.23786052 3.06122217 4212.74539

tubos ΔPt ΔPtc

flujo masico (kg/s) Q(frio)

38.8888889 928638.205

Tw

26.4278929

Fouling resisttabla 5,11 agua destilad Agua de cuid TURBULENTO

F

49509559658085.9 40344489265854.1

0.77

0.000088 0.000176