scorcher
Chemical
- May 15, 2002
- 20
Our plant burns liquid sulphur to produce SO2 to be fed directally to another plant on site.
The SO2 is cooled initially in a waste heat boiler, then further cooled to around 160C as the transfer pipe supplies it to a final packed tower.
This tower contacts the gas stream with 98% acid to remove any SO3. The top of the tower has about has a meter of 1" packing acting as a demister, before the gas, now cooled to about 60 is passed to a packed tower on the next process.
We know there is significent entrainment/mist in the exit stream from the tower. As i understand it, if the mist is entrainment, the patricles will be easily removed by a demister knitted pad, however, if it is acid mist, we will need a coaleaser or candle filter.
The aim is to reduce the mass of acid carried over, rather than remove every last drop of liquid. What might be the most cost effective solution.
What methods of determining droplet size are available?
THanks
Scorcher
The SO2 is cooled initially in a waste heat boiler, then further cooled to around 160C as the transfer pipe supplies it to a final packed tower.
This tower contacts the gas stream with 98% acid to remove any SO3. The top of the tower has about has a meter of 1" packing acting as a demister, before the gas, now cooled to about 60 is passed to a packed tower on the next process.
We know there is significent entrainment/mist in the exit stream from the tower. As i understand it, if the mist is entrainment, the patricles will be easily removed by a demister knitted pad, however, if it is acid mist, we will need a coaleaser or candle filter.
The aim is to reduce the mass of acid carried over, rather than remove every last drop of liquid. What might be the most cost effective solution.
What methods of determining droplet size are available?
THanks
Scorcher