Kiln Residence Time Calculator
Computes rotary-kiln solids residence time from the Sullivan, Maier & Ralston (1927, U.S. Bureau of Mines Technical Paper 384) relation t = 0.19 · L / (N · D · s), with the 0.19 constant cited to that source and the slope shown converted to the m/m ratio that enters the formula.
Mean solids residence time in an inclined rotary kiln from the Sullivan, Maier & Ralston (1927) empirical relation. Enter the kiln length, the INTERNAL diameter, the rotation speed and the slope — slope in m/m, per cent or degrees, always shown converted to the m/m ratio the formula consumes, because 3° and 3 % are not the same number. The result is the mean residence time in minutes and as h:min, with the peripheral speed π·D·N reported as a labelled sanity figure. SI primary; foot toggles on length and diameter only.
Calculator
Effective length material travels. SI primary; ft accepted.
INTERNAL diameter (inside the shell / lining bore). SI primary; ft accepted.
Entered as m/m (rise ÷ run). 3° ≠ 3 % — the converted m/m value below is what enters the formula.
s = 0.03 m/m (entered directly)
First estimate from the Sullivan form only — verify for critical service.
Audit trail
- Constant 0.19 — Sullivan, Maier & Ralston (1927), U.S. Bureau of Mines Technical Paper 384
- Slope: s = 0.03 m/m (entered directly)
- t = 0.19 · L / (N · D · s) = 0.19 × 30 / (2 × 2.5 × 0.03)
- t = 5.7 / 0.15 = 38 min = 0 h 38 min
- Peripheral speed π·D·N = π × 2.5 × 2 = 15.708 m/min (labelled sanity figure; not in the residence-time formula)
Worked example: L = 30 m, D = 2.5 m, N = 2 rpm, s = 0.03 m/m → t = 0.19 × 30 / (2 × 2.5 × 0.03) = 5.7 / 0.15 = 38.0 min. The same case loads by default above.
Related: Leach tank sizing · Hydraulic residence time · Heat duty · Slurry density · Leach reagent consumption
Formulas
Diagram
Worked example
A rotary kiln 30 m long, 2.5 m internal diameter, turning at 2 rpm on a 0.03 m/m slope. Find the mean solids residence time.
- 01Slope already in m/m: s = 0.03 (no conversion needed; 3 % would also give 0.03, but 3° would give tan 3° = 0.0524)
- 02Numerator: 0.19 × L = 0.19 × 30 = 5.7
- 03Denominator: N × D × s = 2 × 2.5 × 0.03 = 0.15
- 04t = 5.7 / 0.15 = 38.0 min = 0 h 38 min
- 05Peripheral speed π·D·N = π × 2.5 × 2 = 15.71 m/min (labelled sanity figure; not in the formula)
The mean solids residence time is 38.0 min (0 h 38 min) — a first estimate from the Sullivan form.
FAQ
Where does the 0.19 constant come from?
Why does the slope mode matter so much?
What about Friedman & Marshall?
Is this good enough for design?
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