22-Mec-B1 Advanced Machine Design · May 2013
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Paper format: National Exams, May 2013 — 07-Mec-B1 Advanced Machine Design. Open book, 3 hours, 100 marks. Part I (Problems 1–2) is compulsory; three of the four Part II problems (3–6) constitute a complete paper. All six problems are solved as a study resource.
Reference texts. R. G. Budynas & J. K. Nisbett, Shigley’s Mechanical Engineering Design, 10th ed. (shafts §7, bolted joints §8, bearings §12, brakes §16); R. L. Norton, Machine Design: An Integrated Approach, 5th ed.; R. C. Hibbeler, Mechanics of Materials, 10th ed. (impact loading, beam deflection); R. C. Juvinall & K. M. Marshek, Fundamentals of Machine Component Design, 5th ed. (journal bearings, friction brakes).
Question text not reproduced: the examination questions are © Engineers and Geoscientists BC. Open the official past paper (linked at the top of this page) to read the question, then follow the worked solution below.
Given. $N = 250\text{ rpm} = 4.167\text{ rev/s}$; ISO VG 100 oil; $L = 1.2D$; no-load loss limit $P_f \le 2.5\times10^{-4}\text{ hp} = 0.186\text{ W}$; diametral clearance $c_d = 0.0045D$ (radial $c_r = 0.00225D$).
Find. the maximum journal diameter $D$ and the allowable (oil) temperature limit.
Approach. The lightly-loaded (concentric) friction torque is given by Petroff’s equation; expressing it with $L$ and $c_r$ proportional to $D$ collapses the power loss to the form $P_f = K\,\mu D^3$. The budget fixes the product $\mu D^3$; the oil viscosity is then set by its temperature through the Walther (ASTM D341) chart, so the largest diameter corresponds to the lowest safe viscosity, i.e. the highest allowable oil temperature.
| Oil temperature | $\mu$ (Pa·s) | Max diameter $D$ |
|---|---|---|
| $40^\circ\text{C}$ | $0.087$ | $20\text{ mm}$ |
| $70^\circ\text{C}$ (design limit) | $0.024$ | $\approx 30\text{ mm}$ |
| $100^\circ\text{C}$ | $0.0095$ | $41\text{ mm}$ |
Check / assumptions: “No-load power loss” is the concentric Petroff loss, which fixes only the product $\mu D^3$; a second constraint is needed to isolate $D$. The maximum diameter is therefore taken at the highest sound operating temperature for a mineral oil ($\approx 70^\circ\text{C}$, above which oxidation life falls sharply), where $\mu$ is smallest. Density and viscosity–temperature values are from the standard ISO VG 100 Walther fit; a different assumed thermal limit shifts $D_{max}$ along the tabulated line.