Question 4 of 6: Journal Bearing Sized by No-Load (Petroff) Power Loss
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Notes on this paper
Paper format. 22-Mec-B1 Advanced Machine Design — National Exams, May 2015. Open book, 3 hours, 100 marks. Part I (Problems 1–2) compulsory; answer any three of the four Part II problems (3–6). All six problems are solved here as a complete study resource.
Reference texts. R. G. Budynas & J. K. Nisbett, Shigley’s Mechanical Engineering Design (10th ed.) — deflection §4, fatigue §6, shafts §7, bolted joints §8, journal bearings §12, brakes & clutches §16; R. C. Juvinall & K. M. Marshek, Fundamentals of Machine Component Design; R. L. Norton, Machine Design: An Integrated Approach; R. C. Hibbeler, Mechanics of Materials.
Question 4: Journal Bearing Sized by No-Load (Petroff) Power Loss (20 marks)
Given. Journal bearing running unloaded (concentric) at $N=250$ rpm on ISO VG100 oil, with $L=1.2D$ and diametral clearance $c_d=0.0045D$; the friction (no-load) power must not exceed $2.5\times10^{-4}$ hp.
Given data
Quantity
Symbol
Value
Rotational speed
$N$
250 rpm (4.167 rev/s)
Lubricant
—
ISO VG100 (SAE 30)
Length / diameter
$L$
$1.2D$
Diametral clearance
$c_d$
$0.0045D$ ($c_r=0.00225D$)
No-load power limit
$P_f$
$2.5\times10^{-4}$ hp = 0.1864 W
Find. The maximum journal diameter $D$ and the oil-temperature limit that keeps the no-load loss at or below the allowance.
Approach. With no radial load the journal runs concentric, so Petroff’s equation gives the friction torque and power. Because $L$ and $c_r$ both scale with $D$, the power collapses to a product $\mu D^{3}$; the loss limit therefore fixes only $\mu D^{3}$. Larger $D$ demands lower $\mu$, i.e. a hotter (thinner) oil, so the “maximum diameter” is reached at the highest safe oil temperature.
Petroff friction power. For a concentric journal the friction torque is $T=4\pi^{2}\mu N' r^{3}L/c_r$ and the power $P_f=2\pi N'\,T$. Substituting $r=D/2$, $L=1.2D$, $c_r=0.00225D$ shows every geometric factor scales with $D^{3}$:
$$P_f=K\,\mu D^{3},\qquad K=8\pi^{4}N'^{2}\frac{(1.2)}{(0.00225)\,2^{3}}\ \text{(consistent SI units)}.$$
Solve for the required $\mu D^{3}$. Setting $P_f=0.1864$ W,
$$\boxed{\mu D^{3}=\frac{P_f}{K}=6.49\times10^{-7}\ \text{(SI: Pa\,s\,m}^3).}$$
This single group is all the loss limit constrains—diameter and viscosity trade off directly.
Viscosity of VG100 versus temperature. ISO VG100 has $\nu=100$ cSt at $40\,{}^\circ\text{C}$ and $\approx11.4$ cSt at $100\,{}^\circ\text{C}$. Fitting Walther’s equation $\log_{10}\log_{10}(\nu+0.7)=A-B\log_{10}T$ through these points gives, at $70\,{}^\circ\text{C}$, $\nu_{70}\approx27.7$ cSt; with $\rho_{70}\approx854$ kg/m$^3$ the dynamic viscosity is $\mu_{70}=\nu\rho\approx0.0237$ Pa·s.
Maximum diameter at the temperature limit. Mineral oil should not run much above $\approx70\,{}^\circ\text{C}$ in service (oxidation / film loss), so this is the practical thermal limit and gives the lowest safe $\mu$. Hence
$$\boxed{D_{\max}=\left(\frac{\mu D^{3}}{\mu_{70}}\right)^{1/3}\approx30\text{ mm}\quad(\text{30.2 mm}),\qquad T_{\text{limit}}\approx70\,{}^\circ\text{C}.}$$
Resulting proportions. With $D=30$ mm, $L=1.2D=36$ mm and $c_r=0.00225(30)=0.068$ mm—a conventional slow-speed journal.
Check. “Maximum diameter” is set by the lowest viscosity the oil may safely reach; $70\,{}^\circ\text{C}$ is taken as the mineral-oil thermal limit. A higher permitted temperature would allow a slightly larger $D$; the closure is flagged as an engineering assumption.