Welcome to DJB Consultants Inc.

Optimize Mining and Processing Rates

These are some of the tools that can be used to influence the design and operation of AG/SAG Mills.

Optimizing Mill Feed Size

Optimizing Mill Feed Size


Estimation of Preliminary Capital Costs

Preliminary CAPEX (Crushing, Grinding & HPGR Circuits)

Estimation of Operating Cost Parameters

Preliminary OPEX (Crushing &Grinding)

Results Comparison

These charts show a range of application for different comminution flow-sheet protocols, as well as two project examples of one test protocol vs another.

Matching Motor to Mill Operation

It is important to install sufficient motor power at its rated speed to cover the range of expected ore hardness vs mill throughput objectives. This chart shows that many SAG Mills are underpowered relative to possible maximum operating conditions.

Bench Marking Power for SAG Mills

Large Mill Power

Simulation of Mill Sizing “Millpower2000”

Comminution test results are entered into the “Millpower2000” database (please refer to the table) on a project basis for simulation. Different combinations of mill sizes, motor powers, and operating conditions can be simulated to assess ranges of mill throughput objectives and ore hardnesses on a “sample frequency” basis (please refer to the chart).

Ore Characterization

Objectives

Testing Ore Composites

Tests and Models

Tests and Models


Calculation & Methodology

Calculation & Methodology

Selection of a ‘Design Point’ on the chart will define the required motor powers for the grinding circuit to process hard to soft ore types, consistent with a range of mill throughput within the Payback period and future potential for an expansion which would be determined from entry of data into the mine block model.

Specific Energy Requirement and Design

These equations form the Basis of DJB’s “Millpower2000” Simulation Program for estimating power requirements and mill sizes vs mill throughput objectives. It is an iterative process, but the software can accommodate a large number of geo-comminution samples in a time-efficient manner.

Basic Equations

Empirical Formula (Barratt)
Overall Power Requirement, ASAG Circuit (1979)

Modified power requirement based on El Teniente Surveys (1986)
EBM= (ESSBM * -ESAG) + Contingency (1986)

With a Bond Work index-based Phantom Cyclone Approach (1989)
*ESSBM for secondary/tertiary crushing and single-stage ball milling (Rowland, 1982)

Net power for AG/SAG mills
kW (net) = PN * ρ * D2.5 * L

Legend

PN = power number*
ρ = mill charge density (Loveday, 1979)
D = diameter (net effective inside shell liners/lifters)
L = effective grinding length (inside feed end and grate discharge liners along the mill shell)

*Based on contact (1986-1987) with:
– Highland Valley Copper (Lornex), Afton, Island Copper & Similkameen and update (1992-1993) with:
– Kennecott (Copperton)

Assessment of Comminution Test Results

It is important to examine comminution test results on a “parameter vs. parameter” basis vs. petrographical texture and DJB’s Millpower2000 database.

Comminution Fracture Analysis

Comminution Fracture Analysis


Coarse test measures strength of the fractures.
• PQ core highlighting planes of weakness.

Medium test measures strength of the inter-fracture matrix.
• Fractures are typically 20-50mm apart.

QA / QC

Some test protocols are more amenable to particular ore types, whereas other protocols are amenable to most ore types.

Breaking Energy by Size

Homogenous ores show consistent and predicable behaviour over a range of sizes.
(eg., SMC, DWI)

Other models use discontinuous size bands rather than continuous functions.
(eg., Millpower 2000, CEET)


Both examples use 3 size bands.

Third-Party Monitoring of Comminution Test Protocols

This is considered to be important, not only to check on laboratory procedures, but also to check on the test equipment standards.

Our Clients: