Estimate the convective heat-transfer coefficient for natural convection from a horizontal steam pipe. The outside surface temperature of the insulated pipe is 80°C. The surrounding air temperature is 25°C. The outside diameter of the insulated pipe is 10 cm. please help me if my answer is wrong

Introduction to Chemical Engineering Thermodynamics
8th Edition
ISBN:9781259696527
Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Chapter1: Introduction
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Estimate the convective heat-transfer coefficient for natural convection from a horizontal
steam pipe. The outside surface temperature of the insulated pipe is 80°C. The
surrounding air temperature is 25°C. The outside diameter of the insulated pipe is 10 cm. please help me if my answer is wrong. 

Prodtem 4.16:
horreomtal cylinder:
for
V,
0.317 Ne
D- 0,1m
NNu: 0.6 +
(0.550
3,08 = 1-
air
Free Cmveetin
alir Properties
a Te
Mar
Too + To
20 + 86
( 3. lox103)
(m.sIE X10-)e
P= 1.057
らん
ト- 3.JDX16 K"
They-K
4 - 1016
5,351,333
Nor Npr
pea
k
6.0272
M=
19. 515 x10" Pa.s
- 5 1 g13 (0.a1)
Mer - 6.71
3799 446
י רV
6.397 (3799 446)"
6.6 +
יר ס
Transcribed Image Text:Prodtem 4.16: horreomtal cylinder: for V, 0.317 Ne D- 0,1m NNu: 0.6 + (0.550 3,08 = 1- air Free Cmveetin alir Properties a Te Mar Too + To 20 + 86 ( 3. lox103) (m.sIE X10-)e P= 1.057 らん ト- 3.JDX16 K" They-K 4 - 1016 5,351,333 Nor Npr pea k 6.0272 M= 19. 515 x10" Pa.s - 5 1 g13 (0.a1) Mer - 6.71 3799 446 י רV 6.397 (3799 446)" 6.6 + יר ס
0.387 (379466^(Y^) - (1 +( 0. 559÷0.7)
4.613
NNn = hd
Nam 'k
h=
4. 413(0.6272)
=
1.254
6.1
m² -K
Q
-h
VT
- - Th D DT
- -T(1, 254) (01)(20 – 80)
= 23.64 Wm
Transcribed Image Text:0.387 (379466^(Y^) - (1 +( 0. 559÷0.7) 4.613 NNn = hd Nam 'k h= 4. 413(0.6272) = 1.254 6.1 m² -K Q -h VT - - Th D DT - -T(1, 254) (01)(20 – 80) = 23.64 Wm
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