Heat loss of a steel steam pipe

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Discussion Overview

The discussion revolves around a heat transfer problem involving a steel steam pipe, focusing on calculating heat loss per unit length due to convection and radiation. Participants explore the necessary parameters and methods for determining the convection coefficient in the context of a re-insulation project in a plant setting.

Discussion Character

  • Technical explanation
  • Homework-related
  • Debate/contested

Main Points Raised

  • One participant presents a heat transfer scenario involving a steel steam pipe and seeks assistance in calculating heat loss, specifically mentioning the need to find the convection coefficient (h).
  • Another participant provides a link to a website that may assist with the calculations.
  • A participant questions the authenticity of the scenario, suggesting it resembles a schoolwork question.
  • A later reply indicates that the original poster resolved their issue by calculating the Reynolds number and using it to find the Nusselt number, which in turn helps determine the convection coefficient.
  • Another participant acknowledges the resolution and credits a specific user for their help.

Areas of Agreement / Disagreement

There is no consensus on the authenticity of the scenario, as some participants suggest it may be a schoolwork question while others treat it as a practical issue. The discussion remains unresolved regarding the initial query about the convection coefficient.

Contextual Notes

Participants express uncertainty about the calculation of the convection coefficient and the relevance of the scenario to practical applications versus academic exercises.

Batman318
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I have a heat transfer question, I work in a plant and am doing a re-insulation project. If an unexposed steel steam pipe (k=47) of diameter 10 inches, maintains an internal temperature of 460F and is exposed to ambient air (70F) flowing at 5 mph across the pipe. Determine the heat loss per unit length. The inside diameter of the pipe is 9.224 inches and the O.D. is 10.75 inches. Emissivity can be taken as 0.8. σ = 5.6669 x 10^-8.

I know you need to find (q/L)rad and (q/L)convection but I'm having trouble figuring out h, the convection coefficient. can anyone help?
 
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Batman318 said:
I have a heat transfer question, I work in a plant and am doing a re-insulation project. If an unexposed steel steam pipe (k=47) of diameter 10 inches, maintains an internal temperature of 460F and is exposed to ambient air (70F) flowing at 5 mph across the pipe. Determine the heat loss per unit length. The inside diameter of the pipe is 9.224 inches and the O.D. is 10.75 inches. Emissivity can be taken as 0.8. σ = 5.6669 x 10^-8.

I know you need to find (q/L)rad and (q/L)convection but I'm having trouble figuring out h, the convection coefficient. can anyone help?

For working in a plant and doing a project, that sure sounds like the wording of a schoolwork question...
 
berkeman said:
For working in a plant and doing a project, that sure sounds like the wording of a schoolwork question...

haha wish it was. Finally figured it out, after reading my heat transfer book from a few years ago (thank you very much :cool:), you just have to find the reynolds number and use that to find the Nusselt's number which gives you h.
 
Glad you figured it out. Q_Goest is the guy to thank in this case.
 

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