petepsingpy
Chemical
- Apr 4, 2003
- 9
Anyone ever have experience with something like this? We want to spray steam into a glass-lined tank through a 2" dip leg. The dipleg points straight towards the bottom head of the tank, which is about 2 ft under the dipleg. The pressure at the end of the dipleg where it enters the tank (submerged under liquid) would be about 150 mmHg, when you consider the head of liquid above the end of the pipe.
I estimated that at the target rate of steam flow of 300 lb/hr, the velocity in the end of the tube would be 600 ft/s. That sounds quite high to me, but I have no feel for the potential to damage the vessel. Nitrogen is routinely sparged the same way, but my best estimate is that the velocity is < 150 ft/s.
Any comments appreciated.
Thanks
I estimated that at the target rate of steam flow of 300 lb/hr, the velocity in the end of the tube would be 600 ft/s. That sounds quite high to me, but I have no feel for the potential to damage the vessel. Nitrogen is routinely sparged the same way, but my best estimate is that the velocity is < 150 ft/s.
Any comments appreciated.
Thanks