What is the Formula for Calculating Heat Exchange in a Boiler Flue?

Click For Summary
SUMMARY

The discussion focuses on calculating heat exchange in a boiler flue connected to two 150 HP boilers, each producing 33,000 BTUH with less than 80% efficiency. The heat exchanger, constructed from 304 Stainless steel, features a 1" tube with 7 fins per inch and a total surface area of 95 square feet. The user aims to achieve a heat transfer of 250,000 BTUH with a desired temperature differential (dT) of 10°F at a flow rate of 15 GPM, while considering the potential benefits of increasing the pipe size to 2" for a flow rate of 40 GPM. The user seeks assistance with the Q= U*A*LMTD calculations necessary for this configuration.

PREREQUISITES
  • Understanding of heat exchanger principles
  • Familiarity with the Q= U*A*LMTD formula
  • Knowledge of fluid dynamics, specifically flow rates in piping systems
  • Experience with boiler efficiency metrics and calculations
NEXT STEPS
  • Research the Q= U*A*LMTD calculations for heat exchangers
  • Learn about optimizing flow rates in 1" and 2" piping systems
  • Investigate the impact of fin design on heat transfer efficiency
  • Explore methods to enhance boiler efficiency beyond 80%
USEFUL FOR

Engineers, HVAC professionals, and technicians involved in boiler systems and heat exchanger design, as well as anyone looking to optimize heat transfer in industrial applications.

Liljob
Messages
2
Reaction score
0
I have a heat exchanger for a boiler flue. The flue is connected to two big (150 HP) boilers. A boiler HP = 33,000 BTUH. The are less than 80% efficient.

The heat exchanger problem is this:

The Flue contains gas temps above 300 F. The CFM is problematic but apparently the actual CFM could be increased by a factor of 4 or more due to the oxygen and moisture content of the flue gases. In any case the ambient temp in the flue is a near 300 F when the boiler(s) are operating.

The heat exchanger is made of 304 Stainless. It's a 1" tube with 7 fins per inch and the fins are .5" high. The length of the tubing is 360" and it is configured in a coil 30" in diameter. There are 95 square feet of surface area on the heat exchanger due to the fins.

The design entering water into the tube is 80 F and leaving 90 F.

So I have a 300 F heat source (steady) and I want a 10 F dT with a flow rate of 15 GPM. ( I can't get much more flow into a 1" pipe.)

I want to pick up 250,000 BTUH from this configuration and I am not adept at the Q= U*A*LMTD calcs to put this together.

Further, if it makes sense to do so, I would like to increase the Pipe size to 2" and put 40 GPM through this.

Any help would be greatly appreciated.
 
Engineering news on Phys.org
I'm sorry you are not generating any responses at the moment. Is there any additional information you can share with us? Any new findings?
 
Thanks, Greg,

Let me revisit this and I'll get back to you.
 

Similar threads

  • · Replies 34 ·
2
Replies
34
Views
6K
  • · Replies 4 ·
Replies
4
Views
3K
Replies
1
Views
3K
  • · Replies 3 ·
Replies
3
Views
2K
  • · Replies 3 ·
Replies
3
Views
3K
Replies
22
Views
5K
  • · Replies 9 ·
Replies
9
Views
6K
Replies
6
Views
4K
  • · Replies 4 ·
Replies
4
Views
6K
  • · Replies 12 ·
Replies
12
Views
3K