op9
Industrial
- Aug 18, 1999
- 111
I hope this hasn't appeared before as I tried to post it as Combustion air flow but it didn't appear!!
I have been doing some tests on an Asphalt plant burner which is suffering from a lack of combustion air due mainly to the inability of the exhaust fan and system to draw adequate suction at the burner. I have taken pitot tube measurements in a straight exhaust duct area and come up with a flowrate of 7428 ACFM (measured at 162degF). To try and get some appreciation of how much additional exhaust fan capacity I need, I am comparing it to specs published by NAPA which state values of 12000 ACFM (at 290degF). How do I directly compare my reading on the same datum temperature?
I did a calculation based on the gas laws V/T = Constant using absolute temp values. This converted my reading to 8957 ACFM. Is this the correct procedure?
Basically I am saying that if if you measure flow in a duct at one temp, then further down the same duct the temperature is raised (or lowered)what flowrate will you measure?
Would appreciate any comments.
Rod.
I have been doing some tests on an Asphalt plant burner which is suffering from a lack of combustion air due mainly to the inability of the exhaust fan and system to draw adequate suction at the burner. I have taken pitot tube measurements in a straight exhaust duct area and come up with a flowrate of 7428 ACFM (measured at 162degF). To try and get some appreciation of how much additional exhaust fan capacity I need, I am comparing it to specs published by NAPA which state values of 12000 ACFM (at 290degF). How do I directly compare my reading on the same datum temperature?
I did a calculation based on the gas laws V/T = Constant using absolute temp values. This converted my reading to 8957 ACFM. Is this the correct procedure?
Basically I am saying that if if you measure flow in a duct at one temp, then further down the same duct the temperature is raised (or lowered)what flowrate will you measure?
Would appreciate any comments.
Rod.