hollerg
Chemical
- Mar 22, 1999
- 97
I am debottlenecking a continuous dryer which fouls at high production rates. The dryer is 316 stainless steel
Adhesion (cohesion) of the sodium organic salt to the mill finished stainless steel is very high at the operating temperature 300 F. It is highly agglomerating and forms crust if not mechanically disturbed.
The dryer is built as a heated horizontal cylinder (16 in dia, 60" long, containing a 3" center shaft with a spiral of blades that intermesh with stationary hooks, to clean the heated blades (~ 3 mm clearance).
Heat transfer surface cannot be added. What coatings and/or surface finish will limit fouling allowing me to push the heat transfer higher?
If I only modify the cylinder interior, I imagine sliding but the hooks would result in surface renewal. Is there a negative to not coating the hooks, shaft and blade? Poor forced convective surface renewal? Poor bulk turnover? Increased stress on the hooks?
If I modify all surfaces, can I be too slick?
Adhesion (cohesion) of the sodium organic salt to the mill finished stainless steel is very high at the operating temperature 300 F. It is highly agglomerating and forms crust if not mechanically disturbed.
The dryer is built as a heated horizontal cylinder (16 in dia, 60" long, containing a 3" center shaft with a spiral of blades that intermesh with stationary hooks, to clean the heated blades (~ 3 mm clearance).
Heat transfer surface cannot be added. What coatings and/or surface finish will limit fouling allowing me to push the heat transfer higher?
If I only modify the cylinder interior, I imagine sliding but the hooks would result in surface renewal. Is there a negative to not coating the hooks, shaft and blade? Poor forced convective surface renewal? Poor bulk turnover? Increased stress on the hooks?
If I modify all surfaces, can I be too slick?