Winston Water Engineering Unit operations
Design sheetsSheets Material compatibilityMaterials Ask a questionAsk SupportSupport
Home  ›  Unit operations  ›  Thermal Drying
Dewatering and drying

D-1300Thermal Drying

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.

Cutaway — Thermal Drying
Wet cakeDried productVapour

How it works

  1. Why anyone bothers — A tonne of cake at 22 % dry solids is 780 kg of water you are paying to cart away. Dry it to 92 % and the same solids weigh a quarter as much, stop smelling, stop rotting and become a fuel. Everything after this is the price of that.
  2. The water left is the hard water — Dewatering takes the water between the particles, and stops when only the water inside the cells is left. No press, no centrifuge and no amount of polymer will take that — it has to be boiled, and boiling is 2.26 MJ for every kilogram.
  3. The sticky phase — Between roughly 40 and 60 % dry solids the cake is neither pumpable nor free-flowing: it is glue. It climbs screws, welds itself to heating surfaces and stops dryers dead. Watch the band on the scale below — every machine here has to carry the cake through it.
  4. Two ways through it — A convective belt dryer never enters the band: it mixes dried granulate back into the wet feed until the mixture is already past 60 %. A conductive dryer drives straight through on torque, which is why its gearbox is the most expensive part of it.
  5. The off-gas decides the project — Convective drying needs about four kilograms of air for every kilogram of water, and all of it leaves humid and smelling of sludge. Conductive drying makes a vapour stream you can condense. On a site with houses nearby that single difference usually settles the choice before the fuel bill is opened.
  6. The product is a fuel — Dry solids from undigested sludge carry 20–24 MJ/kg; digestion burns off the volatile fraction and leaves 10–13. Coal is 25–30. From undigested sludge the granulate can carry more energy than the dryer burned to make it, which is the whole argument for drying rather than landfilling; from digested sludge it usually cannot. Move the calorific value and watch the bars on the right cross.
  7. Convective belt — Large works making a granulate for sale. Gentle, low temperature, and it steps around the sticky phase by mixing dried product back into the feed. Hot air driven through a moving bed.

Design parameters

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.

ParameterUnitDefaultRange
Machine
Dryer typeConvective belt4 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 feedkg/h5,000200 – 20,000
Cake dry solids in% DS2212 – 45
Product dry solids out% DS9255 – 97
Heat source efficiency%8560 – 98
Fuel priceSGD/kWh0.0450.01 – 0.25
Electricity tariffSGD/kWh0.220.05 – 0.6
The sludge
Calorific value of dry solidsMJ/kg DS168 – 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.

Live parameters

Same correlations as the design sheet.

Machine

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
The sludge
© 2026 Winston Water Engineering. All rights reserved.The equations themselves belong to the engineering literature and to anyone who needs them. The sheets, calculators, drawings and workbook that present them here do not — please link to a page rather than republish it.