24-MMP-B5 Mineral Processing Design and Operations · May 2013
Question 3 of 7: SABC Circuit – Cone Crusher Selection and Costing
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Notes on this paper
National Exams, 09-MMP-B5 Mill Design & Operations, May 2013, 3 hours, closed
book (one Casio or Sharp approved calculator permitted). Answer any five (5) of the
seven (7) questions asked – each question is of equal value (20%). Every question (1–7) is answered in full below as a complete study
resource.
Reference texts: B.A. Wills & J.A. Finch, Wills' Mineral
Processing Technology, 8th ed.; A.L. Mular, D.N. Halbe & D.J. Barratt (eds.),
Mineral Processing Plant Design, Practice, and Control (SME, 2002); A.L. Mular
& R. Poulin, CAPCOSTS: A Handbook for Estimating Mining and Mineral Processing
Equipment Costs (CIM Special Volume 47, 1998); T.J. Napier-Munn, S. Morrell, R.D.
Morrison & T. Kojovic, Mineral Comminution Circuits: Their Operation and
Optimisation (JKMRC, 1996); R.A. Arterburn, "The Sizing and Selection of
Hydrocyclones," in Mular & Bhappu (eds.), Mineral Processing Plant Design;
J.A. Finch & G.S. Dobby, Column Flotation (Pergamon, 1990); A.F. Taggart,
Handbook of Mineral Dressing.
Given. Table above, plus the crusher capacity table at R=10 mm (4 ft:
75 t/h/120 kW; 6 ft: 130 t/h/160 kW; 7 ft: 230 t/h/280 kW) and the 100(x/R) product-size
table (80% passing → 100(x/R)=162).
Find. A cone crusher size/count meeting both the required instantaneous
throughput and power draw.
Approach. Convert the average daily tonnage into the instantaneous rate
the crusher must actually clear: correct the nameplate rate for plant availability to get
the true operating-hour feed rate, take 30% of that as the circulating pebbles load, then
divide by the 60% duty-cycle fraction (the crusher must clear a whole shift's circulating
load in only 60% of the time it is available) to get the required crusher capacity. Cross-
check the resulting duty against the crusher's installed power via Bond's equation using the
CSS-derived P80.
Required instantaneous crusher throughput.
$$\dot{m}_{nameplate}=\frac{25{,}000\ \text{t/d}}{24\ \text{h}}=1{,}041.7\ \text{t/h}$$
$$\dot{m}_{operating}=\frac{1{,}041.7}{0.93}=1{,}120.1\ \text{t/h}\ \text{(true rate during running hours)}$$
$$\dot{m}_{CL}=0.30\times1{,}120.1=336.0\ \text{t/h (circulating pebbles load)}$$
$$\dot{m}_{crusher}=\frac{336.0}{0.60}=\boxed{560\ \text{t/h}}\ \text{(instantaneous duty, 60\% frequency of use)}$$
Select crusher(s) by capacity at CSS=10 mm. A single crusher size
cannot clear 560 t/h (largest unit, 7 ft, gives only 230 t/h); with identical units (standard
practice for spares/interchangeability),
$$N=\left\lceil\frac{560}{230}\right\rceil=3\ \text{crushers, capacity}=3(230)=\boxed{690\ \text{t/h}\ge560\ \text{t/h}}$$
Check power via Bond's equation at CSS=10 mm. From the 100(x/R) table
at 80% passing, 100(x/R)=162, so
$$P_{80}=1.62\times R=1.62(10\ \text{mm})=16.2\ \text{mm}=16{,}200\ \mu\text{m}$$
$$F_{80}=6.5\ \text{cm}=65{,}000\ \mu\text{m}$$
$$w=W_{iC}\left(\frac{10}{\sqrt{P_{80}}}-\frac{10}{\sqrt{F_{80}}}\right)
=17\left(\frac{10}{\sqrt{16{,}200}}-\frac{10}{\sqrt{65{,}000}}\right)=\boxed{0.669\ \text{kWh/t}}$$
$$P_{required}=w\times\dot{m}_{crusher}=0.669(560)=\boxed{375\ \text{kW}}$$
Three 7 ft crushers install 3(280)=840 kW – comfortably above the 375 kW actually
drawn, confirming capacity (not power) is the binding constraint.
SABC circuit: SAG mill in closed circuit with a
vibrating screen; oversize (pebbles) is diverted to the cone crusher on a 60% duty cycle and
the crushed product returns to the SAG mill, while screen undersize reports to the ball
mill–cyclone circuit.
Quantity
Value
Required instantaneous crusher capacity
560 t/h
Recommended selection
3 × 7 ft cone crushers
Installed capacity
690 t/h (≥560 t/h required)
Power drawn at duty
375 kW (of 840 kW installed)
Check: the 60% "frequency of use" is treated as a duty-cycle factor
(the crusher must process the full circulating load within only 60% of the available
operating time) – a standard interpretation for intermittently-diverted crusher duty,
stated explicitly as the governing assumption because the source does not otherwise define
how "frequency of use" enters the sizing calculation.
b) Current cost via Mular & Poulin
Given. cost=aXb, a=30,010, b=1.7 (at M&S index 1400);
current M&S index=1675; X=mantle diameter=7 ft (the selected crusher size).
Find. Current (index-escalated) cost of one 7 ft cone crusher, and of
the full 3-unit installation.
Approach. Evaluate the base-year cost-capacity equation at X=7 ft, then
escalate by the ratio of the current to base Marshall & Swift index.
Escalate to current M&S=1675.
$$\text{cost}_{1675}=\text{cost}_{1400}\times\frac{1675}{1400}=820{,}200(1.1964)=\boxed{\$981{,}300\ \text{per crusher}}$$
Total for the 3-crusher installation.
$$\text{cost}_{total}=3\times981{,}300=\boxed{\$2{,}944{,}000}$$