A double-pipe heat exchanger consists of two hairpins connected in series. Each hairpin is 20 ft long with the follow configuration: Outer pipe: 4-in. schedule 40 Inner pipe: 2-in. schedule 40 with 36 fins Fin height: 0.75 in. The petroleum fraction of Problem 4.2 will flow in the annulus at a rate of 20,000 lb/h. (a) Calculate the heat-transfer coefficient, ho, for the annulus. (b) Calculate the total pressure drop, Po, for the annulus. Ans. (a) 94 Btu/h ft² °F. (b) 3.6 psi. = 4.5in APf= Do D₁ = 4.43in DHydr = 0.43in| Fin thickness: 0.035 in. Nozzles: 2-in. schedule 40 Return bends: Internal T A = (4.5² — 4.43²) = 0.076ft² 4 fLpV² 2gc Di f→ Darcyfric
A double-pipe heat exchanger consists of two hairpins connected in series. Each hairpin is 20 ft long with the follow configuration: Outer pipe: 4-in. schedule 40 Inner pipe: 2-in. schedule 40 with 36 fins Fin height: 0.75 in. The petroleum fraction of Problem 4.2 will flow in the annulus at a rate of 20,000 lb/h. (a) Calculate the heat-transfer coefficient, ho, for the annulus. (b) Calculate the total pressure drop, Po, for the annulus. Ans. (a) 94 Btu/h ft² °F. (b) 3.6 psi. = 4.5in APf= Do D₁ = 4.43in DHydr = 0.43in| Fin thickness: 0.035 in. Nozzles: 2-in. schedule 40 Return bends: Internal T A = (4.5² — 4.43²) = 0.076ft² 4 fLpV² 2gc Di f→ Darcyfric
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
Section: Chapter Questions
Problem 1.1P
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![(4.5) A double-pipe heat exchanger consists of two hairpins connected in series. Each hairpin is 20 ft long with the following
configuration:
Outer pipe: 4-in. schedule 40
Inner pipe: 2-in. schedule 40 with 36 fins
Fin height: 0.75 in.
The petroleum fraction of Problem 4.2 will flow in the annulus at a rate of 20,000 lb/h.
(a) Calculate the heat-transfer coefficient, ho, for the annulus.
(b) Calculate the total pressure drop, A Po, for the annulus.
Ans. (a) 94 Btu/h ft2 °F. (b) 3.6 psi.
ΔΡΑ
= 4.5in
=
Do
D₁ = 4.43in
DHydr = 0.43in|
TT
A
1 = (4.5² — 4.43²) = 0.076ft²
Fin thickness: 0.035 in.
Nozzles: 2-in. schedule 40
Return bends: Internal
fL₂V²
2gc Di
f→ Darcyfric](/v2/_next/image?url=https%3A%2F%2Fcontent.bartleby.com%2Fqna-images%2Fquestion%2Fd47fc2c3-8f4b-4085-b234-bc909be774e3%2Fb2c08553-5ae9-4291-b6e8-8f6bc6267a73%2F76qmz3n_processed.png&w=3840&q=75)
Transcribed Image Text:(4.5) A double-pipe heat exchanger consists of two hairpins connected in series. Each hairpin is 20 ft long with the following
configuration:
Outer pipe: 4-in. schedule 40
Inner pipe: 2-in. schedule 40 with 36 fins
Fin height: 0.75 in.
The petroleum fraction of Problem 4.2 will flow in the annulus at a rate of 20,000 lb/h.
(a) Calculate the heat-transfer coefficient, ho, for the annulus.
(b) Calculate the total pressure drop, A Po, for the annulus.
Ans. (a) 94 Btu/h ft2 °F. (b) 3.6 psi.
ΔΡΑ
= 4.5in
=
Do
D₁ = 4.43in
DHydr = 0.43in|
TT
A
1 = (4.5² — 4.43²) = 0.076ft²
Fin thickness: 0.035 in.
Nozzles: 2-in. schedule 40
Return bends: Internal
fL₂V²
2gc Di
f→ Darcyfric
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