sfacchin
Chemical
- May 13, 2009
- 19
S!
I have to estimate the flow rate of purging gas, air in this case, to keep some sighting glasses and instrumentation wells in a furnace. An older engineer told that is necessary to keep a superficial velocity (flow rate/internal area of the pipe) equals to 1 m/s, but he is not sure about this value. During my calculations I've found that the total amount is, im my opinion, too large. Just for example, in the smaller furnaces the flow rate for the purging gas is about half of the air needed for the combustion. The furnaces are specially sensitive to excess of air. It are sulfur recovery furnaces, so the air flow rate must be very well measured and controlled.
The smaller furnace, a in line reheater, has a total of five locations that need to be purged: 2 flame detectors (2 in), 2 sighting glasses (2 in) and 1 pilot/igniter well (3 in).
Does anybody knows a rule of thumb or a typical design value for purging gas velocity?
I have to estimate the flow rate of purging gas, air in this case, to keep some sighting glasses and instrumentation wells in a furnace. An older engineer told that is necessary to keep a superficial velocity (flow rate/internal area of the pipe) equals to 1 m/s, but he is not sure about this value. During my calculations I've found that the total amount is, im my opinion, too large. Just for example, in the smaller furnaces the flow rate for the purging gas is about half of the air needed for the combustion. The furnaces are specially sensitive to excess of air. It are sulfur recovery furnaces, so the air flow rate must be very well measured and controlled.
The smaller furnace, a in line reheater, has a total of five locations that need to be purged: 2 flame detectors (2 in), 2 sighting glasses (2 in) and 1 pilot/igniter well (3 in).
Does anybody knows a rule of thumb or a typical design value for purging gas velocity?