a31ford
Computer
- Jun 13, 2002
- 78
.
Greetings All.
I'm not that good at this so please bear with me...
I'm looking for a basic simple conversion rate or factor that I can use to get "close" for finding the following.
(Close being "relitively near a reasonable answer")
I have a flame that I would like to put a horazontal firetube heat exchanger at the "Far End" of the flame. (After actual flame area, and simply in the flue gas path).
Here are the things I can work with, for the "simple" calculation.
A) Temperature of flame (F or C) (Really temp. of flue gases)
B) Thickness of steel used in firetubes (decimal or fractonal inches), With a surface area of one square inch.
C) The above A & B would give sum "C"
Eg: 1300f flue gases, with 1/8" steel would equal "N" where N is a devisor or dividand that I could use to figure out how many square inches of firetube surface area I would need to transfer heat from the flue gases to water, on the "outside" of the firetubes.
I relize that in actuality this is a much more complex calculation to take all factors into consideration (like reducing temperature of flue gases due to contact of said gasies with the fire tubes) etc. etc.
I'm simply too stupid to be able to do all those calcuations and keep track of it all...
There must be a simple method that will give a 'close" result (say +/- 200 degrees F, or something like that)
The end result is to capture the heat of the flue gases to water, without condensing the flue gases in the firetubes or chimney, assuming this unit is "always on, and runing".
Thank you in advance, if anyone can come up with a "Simpletons use" version of this calculation.
Regards,
Greg Manning
Greetings All.
I'm not that good at this so please bear with me...
I'm looking for a basic simple conversion rate or factor that I can use to get "close" for finding the following.
(Close being "relitively near a reasonable answer")
I have a flame that I would like to put a horazontal firetube heat exchanger at the "Far End" of the flame. (After actual flame area, and simply in the flue gas path).
Here are the things I can work with, for the "simple" calculation.
A) Temperature of flame (F or C) (Really temp. of flue gases)
B) Thickness of steel used in firetubes (decimal or fractonal inches), With a surface area of one square inch.
C) The above A & B would give sum "C"
Eg: 1300f flue gases, with 1/8" steel would equal "N" where N is a devisor or dividand that I could use to figure out how many square inches of firetube surface area I would need to transfer heat from the flue gases to water, on the "outside" of the firetubes.
I relize that in actuality this is a much more complex calculation to take all factors into consideration (like reducing temperature of flue gases due to contact of said gasies with the fire tubes) etc. etc.
I'm simply too stupid to be able to do all those calcuations and keep track of it all...
There must be a simple method that will give a 'close" result (say +/- 200 degrees F, or something like that)
The end result is to capture the heat of the flue gases to water, without condensing the flue gases in the firetubes or chimney, assuming this unit is "always on, and runing".
Thank you in advance, if anyone can come up with a "Simpletons use" version of this calculation.

Regards,
Greg Manning