Producing Dry Saturated Steam in a Fire Tube Boiler

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SUMMARY

The discussion focuses on producing dry saturated steam in a fire tube boiler, specifically addressing the calculation of maximum and minimum mass flow rates per tube based on flue gas density and gas velocities. Participants emphasize the importance of calculating the heat load and suggest utilizing available resources such as institutional libraries and online materials related to heat exchanger design. The conversation highlights the necessity of understanding specific engineering principles to solve the posed problem effectively.

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  • Understanding of fire tube boiler operation
  • Knowledge of heat exchanger design principles
  • Familiarity with fluid dynamics, specifically gas velocities
  • Ability to perform thermal calculations, including heat load determination
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Engineering students, mechanical engineers, and professionals involved in boiler design and thermal systems optimization will benefit from this discussion.

MaisieMitchell
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Homework Statement
Dry saturated steam at a temperature of 180ºC is to be produced in a
fire tube boiler from the cooling of 50 000 kg h–1 of flue gases from a
pressurised combustion process. The gases enter the tubes of the
boiler at 1600ºC and leave at 200ºC. The feed water is externally
preheated to 180ºC before entering the boiler.
The mean specific heat capacity of the flue gases is 1.15 kJ kg–1 K–1.
The latent heat of vaporisation of the water at 180ºC is 2015 kJ kg–1.
Feed water temperature = 180ºC.
The tubes within the boiler are to be 25 mm inside diameter with a
wall thickness of 3 mm. The average flue gas velocity through the
tubes to maintain the overall heat transfer coefficient value and to
minimise pressure losses is to be more than 22 m s–1 and less than
28 m s–1.
Assuming that the average density of the flue gases is 1.108 kg m–3,
calculate:
(i) the minimum and maximum number of tubes in each pass
(ii) the overall length of tubes at each of these numbers of tubes
(iii) the minimum number of tube passes in each case, if the length
of a boiler tube is to be less than 5 metres.
Relevant Equations
mg = n (Π/4 χ d^2 x v) x ρ (ρ is density)
Stuck with i & ii can somebody please guide me. none of my coursework material has anything similar in to help me work this one out.
 
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Hello,
MaisieMitchell said:
Stuck with

where in your attempt at solution that you need to post before we are allowed to provide assistance (according to the PF guidelines) ?

A picture of the flowchart with some annotations might also be helpful !

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Based on the average density of the flue gas, the ID of the tubes, and the maximum and minimum average gas velocities, what is the maximum mass flow rate per tube and what is the minimum mass for rate per tube

Have you calculated the heat load? If so, what is it?
 
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MaisieMitchell said:
none of my coursework material has anything similar
What course is that ? database design ? or some branch of engineering where heat exchanger design fits in ?

Does your institution have a library ? Or can you access google heat exchanger design ?:welcome:
:smile:
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Thanks all. Following on from plenty of googling about it I now understand the question. Appreciate all the help and guidance.
 
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Ok, best wishes !

:smile:

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