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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.

Question 3: SABC Circuit – Cone Crusher Selection and Costing (20%)

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.

a) Cone crusher size and number

ParameterValue
Ore tonnage25,000 tpd
Circulating load (SAG circuit)30%
Availability (SAG mill & crusher)93%
Cone crusher CSS, R1 cm = 10 mm
Cone crusher feed F806.5 cm
Frequency of cone crusher use60%
Work index WiC17 kWh/t

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.

  1. Required instantaneous crusher throughput. $$\dot{m}_{nameplate}=\frac{25{,}000\ \text{t/d}}{24\ \text{h}}=1{,}041.7\ \text{t/h}$$ $$\dot{m}_{operating}=\frac{1{,}041.7}{0.93}=1{,}120.1\ \text{t/h}\ \text{(true rate during running hours)}$$ $$\dot{m}_{CL}=0.30\times1{,}120.1=336.0\ \text{t/h (circulating pebbles load)}$$ $$\dot{m}_{crusher}=\frac{336.0}{0.60}=\boxed{560\ \text{t/h}}\ \text{(instantaneous duty, 60\% frequency of use)}$$
  2. 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), $$N=\left\lceil\frac{560}{230}\right\rceil=3\ \text{crushers, capacity}=3(230)=\boxed{690\ \text{t/h}\ge560\ \text{t/h}}$$
  3. 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.
SAG MillSAG ScreenCone Crusher(60% duty)Sump /Pump BoxBall MillsHydrocyclonesNew feed25,000 tpdDischargeOversize(pebbles)Crushed pebbles(recycled to SAG)UndersizeCyclone feedU/FO/F toflotation
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.
QuantityValue
Required instantaneous crusher capacity560 t/h
Recommended selection3 × 7 ft cone crushers
Installed capacity690 t/h (≥560 t/h required)
Power drawn at duty375 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.

  1. Base-year (M&S=1400) cost. $$\text{cost}_{1400}=aX^{b}=30{,}010(7)^{1.7}=30{,}010(27.33)=\boxed{\$820{,}200}$$
  2. Escalate to current M&S=1675. $$\text{cost}_{1675}=\text{cost}_{1400}\times\frac{1675}{1400}=820{,}200(1.1964)=\boxed{\$981{,}300\ \text{per crusher}}$$
  3. Total for the 3-crusher installation. $$\text{cost}_{total}=3\times981{,}300=\boxed{\$2{,}944{,}000}$$
QuantityValue
Cost per 7 ft crusher, M&S=1400USD 820,200
Cost per 7 ft crusher, current M&S=1675USD 981,300
Total, 3 crushers≈USD 2.94 million