Dewatering stops at about a quarter dry solids, because what is left is inside the cells rather than between the particles. Past that the only way on is to boil it off — roughly a kilowatt-hour for every kilogram of water, which is why the fuel bill, not the machine, is the whole economics of a drying plant.
The panel opposite runs the same correlations as the D-1300 design sheet, so the animation and the calculator cannot disagree. Every parameter below is live — drag one and the picture responds.
| Parameter | Unit | Default | Range |
|---|---|---|---|
| Machine | |||
| Dryer type | Convective belt | 4 options | |
| Convective machines move a large humid air stream that has to be deodorised. Conductive ones make a small vapour stream that simply condenses. That difference decides more projects than the heat duty does. | |||
| Duty | |||
| Wet cake feed | kg/h | 5,000 | 200 – 20,000 |
| Cake dry solids in | % DS | 22 | 12 – 45 |
| Product dry solids out | % DS | 92 | 55 – 97 |
| Heat source efficiency | % | 85 | 60 – 98 |
| Fuel price | SGD/kWh | 0.045 | 0.01 – 0.25 |
| Electricity tariff | SGD/kWh | 0.22 | 0.05 – 0.6 |
| The sludge | |||
| Calorific value of dry solids | MJ/kg DS | 16 | 8 – 26 |
| Undigested sludge 20–24, digested 10–13. Digestion burns off the volatile solids that would have been the fuel, and it is the difference between a dryer that pays its own heat bill and one that does not. | |||
The full D-1300 design calculation — governing equations, accepted envelopes and the worked sizing — is in the design calculator workbook. Everything on this page stays free.
Same correlations as the design sheet.
Convective machines move a large humid air stream that has to be deodorised. Conductive ones make a small vapour stream that simply condenses. That difference decides more projects than the heat duty does.