24-MMP-B5 Mineral Processing Design and Operations · May 2016
Question 1 of 8: Crushing circuit size distribution and circulating load
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Notes on this paper
National Exam 09-MMP-B5, Mill Design & Operations — May 2016, 3 hours. Candidates were instructed to answer any 6 of the 8 questions (each of equal value); all 8 are solved below as a complete study resource.
Reference texts: Wills' Mineral Processing Technology (B.A. Wills & J. Finch, 8th ed., Butterworth-Heinemann) — Ch. 4 Comminution, Ch. 8 Screening, Ch. 9 Classification, Ch. 12 Froth Flotation, Ch. 14 Solid-Liquid Separation; Mular, Halbe & Barratt (eds.), Mineral Processing Plant Design, Practice and Control (SME, 2002); Mular & Poulin, CIM Special Volume 47 (1998) preliminary capital cost estimation; SME Mining Engineering Handbook (3rd ed.).
Question 1: Crushing circuit size distribution and circulating load (1/6)
Given. Circuit-product cumulative % passing at four log-log stations: (2 mm, 46.3%), (6 mm, 67.1%), (9 mm, 85.3%), (15 mm, 99.2%). Screen aperture 15 mm; screen feed (crusher discharge) is 51.0% passing 15 mm; circuit product (screen undersize) is 99.2% passing 15 mm; screen efficiency $E=90\%$ (fraction of the -15 mm material in the feed that reports to the undersize).
Find. (a) The Gates-Gaudin-Schuhmann (GGS) distribution modulus $m$ and size modulus $K$. (b) The circulating load ratio of stream T (oversize returned to the crusher) as a percentage of new/product feed.
Fig. 1 — Closed-circuit SH cone crusher / 15 mm screen: new feed enters the crusher, crusher discharge is screened, oversize (+15 mm, stream T) recirculates to the crusher, and screen undersize (-15 mm) leaves as the circuit product.
Approach. (a) Fit $Y=100(x/K)^m$ by least-squares linear regression of $\ln Y$ against $\ln x$ over the four stations; (b) close a two-product mass balance around the screen using the feed/product -15 mm fractions and the stated efficiency.
Linearize the GGS model.$Y=100(x/K)^m \Rightarrow \ln(Y/100) = m\ln x - m\ln K$, a straight line in $\ln x$ vs. $\ln(Y/100)$.
$$\begin{aligned}
x_i &= (2,\,6,\,9,\,15)\ \text{mm}, \quad \ln x_i = (0.693,\,1.792,\,2.197,\,2.708) \\
Y_i &= (46.3,\,67.1,\,85.3,\,99.2)\%, \quad \ln(Y_i/100) = (-0.770,\,-0.399,\,-0.159,\,-0.008)
\end{aligned}$$
Least-squares slope and intercept. With $n=4$, $\sum\ln x = 7.390$, $\sum\ln(Y/100) = -1.336$, $\sum(\ln x)^2 = 14.514$, $\sum \ln x\cdot\ln(Y/100) = -1.936$:
$$m=\frac{n\sum xy - \sum x\sum y}{n\sum x^2-(\sum x)^2}=\frac{4(-1.936)-(7.390)(-1.336)}{4(14.514)-(7.390)^2}=0.386$$
The intercept gives the size modulus (100% passing size, extrapolated): $\boxed{K = 15.1\ \text{mm}}$, with distribution modulus $\boxed{m = 0.386}$.
Screen mass balance (basis: screen feed $F=1$). Let $f=0.510$ (fraction -15 mm in the screen feed = crusher discharge), $u=0.992$ (fraction -15 mm in the undersize = circuit product), and efficiency $E=(Uu)/(Ff)=0.90$ as defined in the question.
$$U = \frac{Ef}{u}F = \frac{0.90\times0.510}{0.992}(1) = 0.4627$$
Oversize (stream T) and circulating load ratio. By overall mass balance $O=F-U$, and the product leaving the circuit equals the undersize ($P=U$), so the circulating load ratio is referenced to the new/product feed:
$$O = 1-0.4627 = 0.5373 \qquad \text{C.L.}=\frac{O}{U}\times100\% = \frac{0.5373}{0.4627}\times100\%=\boxed{116.1\%}$$
Circulating load, stream T (% of new/product feed)
116.1%
Check: the GGS fit uses only the four stipulated log-log stations (not the full table), per the question's explicit instruction; the size modulus K = 15.1 mm is an extrapolated 100%-passing size, not a value actually tabulated (the true top size is closer to 20-24 mm, reflecting the imperfect log-log linearity typical of a crushed product).