MantasTemperatura (°F) Conductividad (BTU pulg/ hr ft^2 °F) Temperatura (°C)

100 0.25 38200 0.3 93300 0.38 149400 0.47 204500 0.58 260

0.050911743981650.05146457070751

50 100 150 200 250 300 350 400 450 500 5500

0.10.20.30.40.50.60.7

f(x) = 0.199658760388205 exp( 0.00213208459140434 x )R² = 0.998830297212298

Relación conductividad y temperatura para mantas

Temperatura (°F)Cond

uctiv

idad

(BTU

pul

g/hr

ftÞ^

2 °F

)

0 50 100 150 200 250 3000

0.02

0.04

0.06

0.08

0.1

f(x) = 0.0492093212806864 exp( 0.00180286347389263 x )R² = 0.999000898510711

Relación conductividad y tempera-tura para silicato de calcio

Temperatura (°C)

Cond

uctiv

idad

(W/M

°C)

Conductividad (W/m °C) Temperatura (°C) Conductividad (BTU pulg/ hr ft^2 °F)0.053 38 0.240.058 79 0.290.064 93 0.320.071 121 0.340.079 163 0.4

0.274708302539040.28683576846795

0 50 100 150 200 250 3000

0.02

0.04

0.06

0.08

0.1

f(x) = 0.0492093212806864 exp( 0.00180286347389263 x )R² = 0.999000898510711

Relación conductividad y tempera-tura para silicato de calcio

Temperatura (°C)

Cond

uctiv

idad

(W/M

°C)

20 40 60 80 100 120 140 160 1800

0.050.1

0.150.2

0.250.3

0.350.4

0.45

f(x) = 0.210774338909569 exp( 0.00401884740928805 x )

Relación conductividad y temperatura para cañuelas

Temperatura Conductividad (BTU pulg/ hr ft^2 °F)

-18 0.238 0.2552 0.2866 0.393 0.36

0.236443710.24393704

20 40 60 80 100 120 140 160 1800

0.050.1

0.150.2

0.250.3

0.350.4

0.45

f(x) = 0.210774338909569 exp( 0.00401884740928805 x )

Relación conductividad y temperatura para cañuelas

-40 -20 0 20 40 60 80 1000

0.05

0.1

0.15

0.2

0.25

0.3

0.35

0.4

f(x) = 0.214175226315482 exp( 0.0052401814762502 x )R² = 0.98024481406002

Conductividad (BTU pulg/ hr ft^2 °F)

Espesor (m) Longitud (m) Área (m^2) Costo (COP) Calor0.075 1.15807843 0.5457316 $ 9,277.44 0.02046494

0.15 0.81888511 0.77178104 $ 13,120.28 0.057883580.25 0.63430568 0.99636503 $ 16,938.21 0.12454563

0.405 0.49835761 1.26816565 $ 21,558.82 0.25680354Espesor (m) Longitud (m) Área (m^2) Costo (COP) Calor

0.0075 3.66216555 0.17257549 $ 2,588.63 0.000647160.0175 2.39745012 0.26361341 $ 3,954.20 0.002306620.0225 2.11435227 0.29890951 $ 4,483.64 0.00336273

0.03 1.83108278 0.34515097 $ 5,177.26 0.00517726Espesor (m) Longitud (m) Área (m^2) Costo (COP) Calor

0.0127 2.81427637 0.22456927 $ 5,614.23 0.001426010.0254 1.98999391 0.31758891 $ 7,939.72 0.004033380.0762 1.14892352 0.55008013 $ 13,752.00 0.020958050.1016 0.99499695 0.63517782 $ 15,879.45 0.03226703

Espesor (m) Longitud (m) Área (m^2) Costo (COP) Calor0.0254 1.98999391 0.31758891 $ 6,351.78 0.004033380.0508 1.40713819 0.44913855 $ 8,982.77 0.011408120.0762 1.14892352 0.55008013 $ 11,001.60 0.020958050.1016 0.99499695 0.63517782 $ 12,703.56 0.03226703

Mantas para tubería

Silicato de Calcio

Cañuelas aislantes

Lana Mineral

0 0.05 0.1 0.15 0.2 0.25 0.3 0.35 0.4 0.45 $-

$5,000.00

$10,000.00

$15,000.00

$20,000.00

$25,000.00

Relación Costo vs Espesor

MantaSilicatoCañuelasLana Mineral

Espesor (m)

Cost

o ($

CO

P)

0 0.05 0.1 0.15 0.2 0.25 0.3 $-

$5,000.00

$10,000.00

$15,000.00

$20,000.00

$25,000.00

Relacion entre calor liberado y costo

MantasSilicatoCañuelasLana Mineral

Calor (W/ m K)

Cost

o ($

CO

P)

0 0.02 0.04 0.06 0.08 0.1 0.12 0.140

0.01

0.02

0.03

0.04

0.05

0.06

0.07

Relación entre espesor y calor liberado

MantasSilicatoCañuelasLana Mineral

Espesor (m)

Calo

r ( W

/m K

)

0 0.05 0.1 0.15 0.2 0.25 0.3 $-

$5,000.00

$10,000.00

$15,000.00

$20,000.00

$25,000.00

Relacion entre calor liberado y costo

MantasSilicatoCañuelasLana Mineral

Calor (W/ m K)

Cost

o ($

CO

P)

0 0.02 0.04 0.06 0.08 0.1 0.12 0.140

0.01

0.02

0.03

0.04

0.05

0.06

0.07

Relación entre espesor y calor liberado

MantasSilicatoCañuelasLana Mineral

Espesor (m)

Calo

r ( W

/m K

)