hollerg
Chemical
- Mar 22, 1999
- 97
Anyone have experience with trading off dryer wall smoothness for heat transfer to paste/powder systems?
I have a paste that drys into a free flowing powder, if low enough in moisture. Too much moisture and the organic salt tends to coheasive/ adheasive. At higher temperature differentials and rates, the agitated LIST Discotherm dryer loses some heat transfer.
The fouling is periodic. Lowering the inventory restores the lost heat treansfer. That the fouling clears so easily makes me think that a packed solids layer forms against the cylindrical wall. Lowering the inventory allows material to be dislodged by the impeller and gravity.
So, to reduce adheasion/friction/surface energy of the wall, I was thinking of adding a diamond like coating. It's low friction, and has high thermal conductivity.
What are the heat transfer ramifications of doing this? Should heat transfer should go up because of less "fouling" rather than down because of a coating?
I have a paste that drys into a free flowing powder, if low enough in moisture. Too much moisture and the organic salt tends to coheasive/ adheasive. At higher temperature differentials and rates, the agitated LIST Discotherm dryer loses some heat transfer.
The fouling is periodic. Lowering the inventory restores the lost heat treansfer. That the fouling clears so easily makes me think that a packed solids layer forms against the cylindrical wall. Lowering the inventory allows material to be dislodged by the impeller and gravity.
So, to reduce adheasion/friction/surface energy of the wall, I was thinking of adding a diamond like coating. It's low friction, and has high thermal conductivity.
What are the heat transfer ramifications of doing this? Should heat transfer should go up because of less "fouling" rather than down because of a coating?