ProcessJim
Chemical
- Jan 4, 2010
- 15
I have been asked to investigate meands of reducing the CO level in flue gas from our rotary furnace. The options we are looking into are:
Provision of a controlled excess of O2 to the burner nozzle (Simplest option but concerns over product quality)
Installation of afterburner in exhaust chamber, and, the prefered option currently owing to cost and simplicity, that is, injection of pure O2 into the furnace exhuast gas stream.
I believe I have done necessary theoretical calcs to establish O2 qty required and heat evolved but I have no practical experience of this kind of system. I understand that ensuring that there is sufficient temperature in exhaust gas for reaction to occur is important.
Can anyone advise on potential pitfalls of such a system or matters to be taken into consideration?
Many thanks,
James
Provision of a controlled excess of O2 to the burner nozzle (Simplest option but concerns over product quality)
Installation of afterburner in exhaust chamber, and, the prefered option currently owing to cost and simplicity, that is, injection of pure O2 into the furnace exhuast gas stream.
I believe I have done necessary theoretical calcs to establish O2 qty required and heat evolved but I have no practical experience of this kind of system. I understand that ensuring that there is sufficient temperature in exhaust gas for reaction to occur is important.
Can anyone advise on potential pitfalls of such a system or matters to be taken into consideration?
Many thanks,
James