Difficulty: Easy
Correct Answer: 0.05 to 0.15
Explanation:
Introduction / Context:Rotary dryers are widely used in chemical and process industries to reduce moisture in granular, crystalline, or lumpy solids. A key operating parameter is the solid hold-up, meaning the fraction of the dryer shell volume that is actually occupied by solids at any moment under steady operation. Correctly estimating hold-up helps size the dryer, set residence time, and predict gas–solid contacting efficiency.
Given Data / Assumptions:
Concept / Approach:Inside a rotary dryer, solids are lifted and showered through the hot gas stream. Only a relatively small fraction of the cylinder cross-section is filled because excessive fill would suppress cascading and curtain formation, hurt heat/mass transfer, and increase power draw. Industry practice and pilot data typically show hold-up values in the low percentage range of total shell volume.
Step-by-Step Solution:
Define solid hold-up H as volume of solids inside the shell divided by the internal shell volume.For flighted rotary dryers with proper speed and slope, H is intentionally kept low to sustain good showering and cascade.Empirical ranges from design practice indicate H ≈ 0.05–0.15 (i.e., 5–15% of shell volume) for free-flowing solids at typical throughputs.Verification / Alternative check:Mass balance on solids (throughput = hold-up / residence time) combined with measured residence times in test units yields hold-up values generally in this 0.05–0.15 range for most granular products. Higher values are exceptional and can indicate suboptimal lifter design or sluggish materials.
Why Other Options Are Wrong:
Common Pitfalls:Confusing mass hold-up with volumetric hold-up; ignoring the effect of flight design and rotational speed; assuming sticky or highly cohesive solids behave like free-flowing materials.
Final Answer:0.05 to 0.15
Discussion & Comments