24-MMP-B5 Mineral Processing Design and Operations · Undated paper
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 and Operations — May 2019, 3 hours. Candidates were instructed to answer any 6 of the 8 questions (each of equal value, 16.7%); 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. 13 Leaching, 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; Doll & Barratt (2010) SAG mill design correlations; 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; screening 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 $m$, size modulus $K$, and $d_{50}$, $d_{80}$, $d_{20}$ for the circuit product. (b) The circulating load ratio of stream T (oversize returned to the crusher via the bin) as a percentage of the new/product feed.
Fig. 1 — Closed-circuit SH cone crusher / 15 mm screen: new feed and recycled oversize T combine through the intermediate ore bin ahead of the crusher; crusher discharge is screened; oversize (+15 mm, stream T) recirculates, and undersize (-15 mm) leaves as the circuit product C.
Approach. (a) Fit $Y=100(x/K)^m$ by least-squares linear regression of $\ln Y$ against $\ln x$ over the four stipulated stations, then invert the fit for $d_{50}$, $d_{80}$, $d_{20}$; (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. $\ln(Y/100)$.
$$x_i=(2,6,9,15)\ \text{mm},\quad Y_i=(46.3,67.1,85.3,99.2)\%$$
Least-squares slope and intercept. With $n=4$, regressing $\ln Y_i$ on $\ln x_i$:
$$m=\frac{\sum(\ln x_i-\overline{\ln x})(\ln Y_i-\overline{\ln Y})}{\sum(\ln x_i-\overline{\ln x})^2}=0.386$$
$$K=\exp\!\left(\frac{\ln100-b}{m}\right)=\boxed{15.1\ \text{mm}}\qquad m=\boxed{0.386}$$
($K$ is the extrapolated 100%-passing size — the size modulus — not a value actually tabulated.)
Invert the fit for the requested size fractions.$d_P = K(P/100)^{1/m}$:
$$d_{50}=15.1(0.50)^{1/0.386}=\boxed{2.50\ \text{mm}}\qquad d_{80}=15.1(0.80)^{1/0.386}=\boxed{8.45\ \text{mm}}$$
$$d_{20}=15.1(0.20)^{1/0.386}=\boxed{0.233\ \text{mm}}\qquad \frac{d_{80}}{d_{20}}=\frac{8.45}{0.233}=\boxed{36.3}$$
($d_{50}$, $d_{80}$ cross-check within a few percent against direct linear interpolation of the full table — 2.58 mm and 8.28 mm respectively — since the fit uses only the four stipulated stations; $d_{20}$ lies below the smallest tabulated size, 0.5 mm, so it is necessarily a GGS extrapolation.)
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), efficiency $E=(Uu)/(Ff)=0.90$:
$$U=\frac{Ef}{u}F=\frac{0.90\times0.510}{0.992}=0.4627$$
Oversize (stream T) and circulating load ratio.$O=F-U$, and the product leaving the circuit equals the undersize ($P=U$), so:
$$O=1-0.4627=0.5373\qquad \text{C.L.}=\frac{O}{U}\times100\%=\frac{0.5373}{0.4627}\times100\%=\boxed{116.1\%}$$
Final Results — Question 1
Quantity
Value
GGS distribution modulus, $m$
0.386
GGS size modulus, $K$
15.1 mm
d50 / d80 / d20 (circuit product)
2.50 / 8.45 / 0.233 mm
d80/d20 ratio
36.3
Circulating load, stream T (% of new/product feed)
116.1%
Fig. 2 — GGS log-log plot of the four stipulated stations with the fitted line $Y=100(x/K)^m$; $d_{50}$, $d_{80}$ and $d_{20}$ read off the fit.
Check: the GGS fit uses only the four stipulated log-log stations (per the question's explicit instruction), not the full 11-row table; K = 15.1 mm is an extrapolated 100%-passing size, and d20 = 0.233 mm is a GGS extrapolation below the smallest tabulated size (0.5 mm) — both carry more uncertainty than d50/d80, which fall inside the tabulated range.