Difficulty: Medium
Correct Answer: hG = 1.004 * G^0.37
Explanation:
Introduction / Context:
During the constant-rate period of drying, convective heat transfer from air to a wet surface dominates. Empirical correlations relate the heat-transfer coefficient per unit mass flux (hG) to air mass velocity G. Flow orientation matters: parallel flow over a plane differs from perpendicular impingement jets hitting the surface.
Given Data / Assumptions:
Concept / Approach:
Parallel flow correlations often show a stronger dependence on G (exponent near 0.8), while impingement jets provide high local turbulence but the scaling exponent tends to be lower, reflecting different boundary-layer development and stagnation-point heat transfer behavior for the metric hG defined here. A widely cited switch is from 0.0176 * G^0.8 (parallel) to 1.004 * G^0.37 (perpendicular).
Step-by-Step Solution:
Identify the given base: hG_parallel = 0.0176 * G^0.8.Apply orientation change to perpendicular impingement: hG_perp = 1.004 * G^0.37.Confirm units and exponents align with empirical data sets for impinging flow conditions.
Verification / Alternative check:
Drying literature and equipment vendor data show reduced exponent values for impingement configurations when hG is expressed per unit G in the given units, matching the presented correlation.
Why Other Options Are Wrong:
(b) keeps the 0.8 exponent, which suits parallel flow; (c) uses the small coefficient with the impingement exponent; (d) is unrealistic; (e) contradicts extensive empirical evidence.
Common Pitfalls:
Mixing SI and English units; applying correlations outside their validity ranges (very low or high G); ignoring humidity effects on properties.
Final Answer:
hG = 1.004 * G^0.37
Discussion & Comments