Urea melt sprayed onto falling curtains of recycled granules in a rotating drum · lifting flights, deflector pans and fixed baffles that form the curtains, an industrial heat and mass balance, air or water-mist cooling, and the granule it makes
A urea granulation drum is not a dryer: it is a slowly turning horizontal drum full of recycled granules, where lifting flights and fixed internals make the granules fall as curtains through sprays of hot urea melt. Each pass adds a thin layer that freezes before the granule lands, so the product grows layer by layer. This page covers the drum itself — the internals that form the curtains, the flows of melt, recycle and air it handles, how the heat of solidification is taken away, and the granule that results.
Rotary drum granulators in which a urea (or similar) melt is sprayed onto falling curtains of recycled granules: lifting flights, deflector pans and fixed curtain structures, melt spray manifolds, recycle and seed feed, cooling by air or water mist, and product size and strength. Phosphate and NPK ammoniator-granulators fed with slurry and ammonia are covered on the Rotary drum granulator for compound fertilizers page; whole urea finishing plants and the choice between prilling and granulation on the Urea granulation and prilling system page; prill towers on the Prilling tower page; rotary dryers on the Drying drum (rotary drum dryer) page; drum shell fabrication and ovality on the Rotating drum shell page.
01
TVA's US patent 3,877,415 (filed 1973) puts a deflector pan, fixed in space inside the upper part of a rotating drum with lifting flights, to catch the particles falling from the flights and gather them into a dense, narrow cascade covering only about 1–10% of the drum cross-section, which is then sprayed. The pan's horizontally projected width may be 40–80% of the drum diameter. [2]
Fertimont's US patent 4,686,115 (priority 1985) replaces the single cascade with fixed inner structures that form two or three vertical curtains, and drops part of the lifted granules directly onto a fixed baffle in the lower half of the drum to form a descending bed. It states that a two-curtain drum offers about twice the sprayed surface of a single-curtain one, and a three-curtain drum, whose middle curtain is sprayed on both sides, about four times — and that spraying less liquid per curtain at the same capacity gives granules with more, thinner layers. [1]
The TVA examples in this patent coat urea with sulfur; TVA's later patent 4,213,924 used the same 4 ft × 6 ft drum with flights canted 15° forward and the 20½ in pan for urea melt granulation (next sections). [3] Editorial note: ask a drum supplier which internal arrangement it uses for urea melt and for its measured curtain density.
| TVA drum (patent examples) | Pilot drum | Larger drum |
|---|---|---|
| Diameter × length | 3 ft × 2 ft (≈0.91 × 0.61 m) | 4 ft × 6 ft (≈1.22 × 1.83 m) [2] |
| Lifting flights | 16, about 2 in wide | 24, 3 in wide, 6 ft long [2] |
| Dams / bed depth | Dams 4 in; bed depth 2–4 in; bed depth to flight width about 2:1 | Annular dams 5 in [2] |
| Deflector pan | — | 20½ in wide, 6 ft long, at 35° from horizontal [2] |
| Drum speed / capacity | 4–15 rpm; about 1,000 lb/h | — [2] |
Give the supplier the product rate, melt concentration and temperature, the granule size wanted, and whether the drum must also handle coating or additive sprays; ask for the internal arrangement drawing and the number and position of spray manifolds.
02
Example 1 of the Fertimont patent gives a complete operating point for a two-curtain urea drum: 6 m long, 2 m in diameter, 30 blades, 6 rpm. Two manifolds entering from opposite ends, each with 30 single-fluid flat-cone nozzles behind a gauze filter, sprayed urea melt of 99% by weight at 140 °C and 6.5 bar. [1]
Editorial calculation: the recycle ratio is 62,500 ÷ 21,688.7 ≈ 2.9 kg of recycle per kg of melt, and the drum circulates 300,000 ÷ 83,335 ≈ 3.6 times its throughput internally. Air works out at 11,500 ÷ 21,688.7 ≈ 0.53 Nm³ per kg of melt. Melt plus recycle (84,188.7 kg/h) exceeds the product leaving the drum by about 854 kg/h; the patent states that fines entrained by the air were removed in a wet separator and recovered, so that stream belongs in the scrubber design. [1]
| Stream (Fertimont Example 1) | Value |
|---|---|
| Urea melt fed | 21,688.7 kg/h, 99% urea, 140 °C, 6.5 bar [1] |
| Recycled granules | 62,500 kg/h [1] |
| Air, co-current | 11,500 Nm³/h at 25 °C in; 85 °C out [1] |
| Internal circulation | 300,000 kg/h: curtain 1 100,000; curtain 2 120,000; direct onto lower baffle 80,000 [1] |
| Product leaving drum | 83,335 kg/h at 100 °C, 0.3% relative humidity [1] |
| Average residence time | 110 s [1] |
| After the drum | Fluid-bed cooled to 49 °C; screened to 2–4 mm grade; oversize ground and returned with fines [1] |
Ask for the supplier's balance at your rate: melt, recycle, air flow and temperatures, dust load to the scrubber, and product temperature at the drum outlet.
03
TVA's US patent 4,213,924 (filed 1978) absorbs part of the heat released as the melt freezes by evaporating water atomised into the drum as an extremely fine mist, evaporated without striking the granules or the internals. Its urea example in the 4 ft × 6 ft drum gives the figures below. [3]
The patent sets the droplet evaporation time at no more than 2 seconds and preferably no more than 1 second, otherwise the moisture can condense on the granules or a surface inside the granulator, and it reports no increase in product moisture over conventional pan or drum granulation of urea. [3]
Editorial calculation: 76,000 Btu/h is about 70% of the 108,400 Btu/h released by the urea, which is the share of the cooling duty taken off the air. By contrast, the Fertimont drum in the previous section cools with air alone, co-current, heating 11,500 Nm³/h from 25 °C to 85 °C, and finishes cooling in a fluid bed after the drum. [3] [1]
| TVA urea example | Value |
|---|---|
| Urea melt | 300 °F (≈149 °C), sprayed at 250 psig, 698 lb/h [3] |
| Cooling air | Enters at 84 °F, 400–600 acfm [3] |
| Water mist | Median droplet 50–60 µm or finer; 70.7 lb/h; started once granules reach 190 °F [3] |
| Granule temperature limit | Not above 220 °F (≈104 °C) for good urea solidification [3] |
| Seed / recycle | −8 mesh seed 13.4 lb/h; undersize recycle 299 lb/h at 160 °F [3] |
| Product | 1,011 lb/h discharged at 190 °F [3] |
| Heat removed | 108,400 Btu/h from the urea; 76,000 Btu/h by evaporating water [3] |
Ask whether the drum is air-cooled, mist-cooled or both, the air flow and its direction, and how the supplier prevents mist reaching the granules or the drum wall.
04
Fertimont reports the grade product of its Example 1 as follows, and attributes the hardness, low dusting and sphericity to the larger number of thin layers its multi-curtain drum builds. [1]
For comparison, TVA's mist-cooled urea granulation reports a product moisture no higher than that of conventional pan or drum granulation. [3] Editorial note: crushing loads and dust figures depend on the test method; ask the supplier to state the method, granule size and conditioning behind any strength figure quoted.
| Grade product (Fertimont Example 1) | Value |
|---|---|
| Average particle size (Sauter) | 2.97 mm [1] |
| Number of coatings per granule | 9–10 [1] |
| Squeezing load | 2.5 kg on a 2.5 mm granule; 3 kg on a 3 mm granule [1] |
| Densities | Actual 1,319; apparent 1,263; bulk 756 kg/m³ [1] |
| Total porosity | 0.035 cm³/g [1] |
| Powderiness / crushability | 130 ppm / 0.8% [1] |
05
Paste it into your enquiry below or into an email to a maker, then replace every bracket.
Capacity: [t/h product; operating hours] Melt: [urea concentration; temperature; additive or formaldehyde] Product: [size range; mean size; crushing strength; moisture] Drum: [diameter × length; speed; internals (flights, pans, curtains)] Sprays: [manifolds; nozzles; pressure; filter] Recycle: [ratio; seed preparation; crusher] Cooling: [air flow and direction; water mist; after-cooler] Emissions: [dust and ammonia to scrubber]
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Flights lift recycled granules and drop them as curtains through urea melt sprays; Fertimont's 2 m × 6 m drum at 6 rpm fed 21,689 kg/h of 99% melt onto 62,500 kg/h of recycle. [1]
A fixed pan in the upper drum that gathers falling particles into a dense cascade covering about 1–10% of the cross-section; its projected width may be 40–80% of the drum diameter. [2]
By air, or in TVA's process also by a 50–60 µm water mist that removed 76,000 Btu/h of the 108,400 Btu/h released by the urea in its example. [3]
Fertimont reports 2–4 mm grade product of 2.97 mm Sauter mean with 9–10 layers and a 3 kg squeezing load on a 3 mm granule. [1]
Sources checked 2026-10-12. Drum internals, an industrial operating point and product properties come from Fertimont's US patent 4,686,115; the deflector pan and pilot drums from TVA's US patent 3,877,415; water-mist cooling and its urea example from TVA's US patent 4,213,924.
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