Download - 02 Mineral Processing

Transcript
Page 1: 02 Mineral Processing

Mineral Processing

SYMPOSIUM: 02 MINERAL PROCESSING

COD AUTHOR TITLE ABSTRACT

MP01 Lorenzo Reyes USE OF BIOSOLIDS AND ITS MAIN COMPONENTS AS

FROTH FLOTATION REAGENTS FOR THE CONCENTRATION

OFF COPPER SULPHIDE ORE

MP02 Winston Rocher THE EVOLUTION OF MILL RELINING TECHNOLOGY

MP03 Luis Vinnett GAS DISPERSION MEASUREMENTS IN INDUSTRIAL

FLOTATION EQUIPMENT

MP04 Carlos Rabanal EMPIRICAL CORRELATION FOR ESTIMATING GRINDING

MEDIA CONSUMPTION

MP05 Ursula Kelm CHARACTERIZATION OF COPPER CLAYS AND

GEOMETALLURGICAL IMPLICATIONS

MP07 R. Fuentes PROGRESS MADE IN PILOT AND LABORATORY

THICKENING STUDY

MP08 N. Rojas EFFECT OF FINES CONTENT ON YIELD STRESS OF COPPER

TAILINGS

MP09 Shigeto Kuroiwa STUDY ON SEPARATION OF ARSENIC FROM COPPER

CONCENTRATE

MP11 Sergio Arellano TECHNICAL EVALUATION OF THE REPLACEMENT OF

CONVENTIONAL FLOTATION CELLS BY FLOTATION

CELLS PNEUMATIC IN THE BENEFIT OF COPPER ORES

MP13 T. Wisdom NEXT GENERATION PRESSURE FILTERS FOR HARD ROCK

TAILINGS

MP16 Francisco Abbott SEAWATER USE IN ANTOFAGASTA MINING GROUP

MP17 D. Garcia ANTAPACCAY - TINTAYA EXPANSION

MP18 E.Visariev GRINDING CYCLE OPTIMIZATION FOR PROCESSING OF

COPPER SLAG AT AURUBIS BULGARIA

MP19 V. Murariu IMPROVED DEM MODEL FOR PREDICTING CONE

CRUSHERS' PERFORMANCE

MP22 S. Castro THE EFFECT OF FLOCCULANTS AND THEIR

DEGRADATION PRODUCTS ON MOLYBDENITE

FLOTATION

MP24 Fernando Pino ADVANTAGES AND DISADVANTAGES OF BROWNFIELD

PROJECTS

MP26 C.O. Gomez FROTHER ROLES CHARACTERIZATION IN A LABORATORY

FLOTATION CELL

MP28 David Meadows SAG MILL DISCHARGE SECTION OPTIMIZATION STUDIES

AND REDESIGN

MP29 Felipe Henriquez INSTALLATION OF INTERNAL LAUNDERS ON 130 M³

FLOTATION CELLS AT MINERA LOS PELAMBRES

MP30 H. Nematollahi CONCENTRATION OF COPPER OXIDE MINERAL WITH

HYDROXAMATE

MP31 Christopher J Greet GRINDING CHEMISTRY - THE APPLICATION OF GRINDING

MEDIA TO IMPROVE METALLURGICAL RESPONSE OF

COPPER ORES

MP32 Zanin Massimiliano AMIRA P260 SILVER JUBILEE - 25 YEARS OF BENEFITS TO

MINERALS FLOTATION

MP33 Jose Davila NASH IN THE OPTIMIZATION OF COPPER FLOTATION

CONCENTRATOR CUAJONE

Page 2: 02 Mineral Processing

Mineral Processing

MP35 O. Angulo PREVENTING COPPER LOSS PRODUCTION AND FLOW

PROBLEMS BY MEASURING THE MATERIALS FLOW

PROPERTIES

MP36 Mira Bissengaliyeva THERMODYNAMIC CONSTANTS OF MINERALS OF THE

OXIDATION ZONE OF COPPER - ANTLERITE AND

PSEUDOMALACHITE

MP38 Rene Del Villar RECENT DEVELOPMENTS IN FLOTATION COLUMN

INSTRUMENTATION AND CONTROL

MP39 Raul Jara Iturre OPTIMIZACIÓN METALÚRGICA DE UN MINERAL DE

COBRE CON ALTA DISEMINACIÓN Y DUREZA

MP40 David Gwyther MARINE TAILINGS PLACEMENT: EXPERIENCES AND

LESSONS FROM THE ASIA PACIFIC REGION

MP41 C.O. Gomez MODELLING BUBBLE HYDRODYNAMICS IN FLOTATION

MP42 G. Debernardi PRIMARY CRITERIA FOR PRESSURE COPPER LEACHING

PROCESS SELECTION

MP43 Rodrigo

Huenchullán G.

STRUCTURAL DESIGN OF RECLAIM TUNNELS …

ADDRESSED AS A MINGA

MP44 Lorin Redden IMPROVED COPPER AND GOLD RECOVERY AT KGHM

INTERNATIONAL’S ROBINSON MINE

MP45 Jorge M. Menacho

and Juan Rodríguez

MODELLING BUBBLES GOING THROUGH FLOTATION

CELLS

MP47 S.E. Sánchez-Pino,

S.A. Sánchez-

Baquedano,

R.M.Imhof, H.

Sprenger

PNEUMATIC FLOTATION IMHOFLOT

PRODUCTION TECHNOLOGY IN CHILEAN MINING

MP48 Jorge M. Menacho REMOTE SOLUTIONS TO IMPROVE PROCESS RESULTS AT

CONCENTRATOR PLANTS

Page 3: 02 Mineral Processing

Mineral Processing

MP01

USE OF BIOSOLIDS AND ITS MAIN COMPONENTS AS FROTH FLOTATION

REAGENTS FOR THE CONCENTRATION OF COPPER SULPHIDE ORE

Lorenzo Reyes-Bozo

Departamento de Ciencias de la Ingeniería, Facultad de Ingeniería, Universidad Andres

Bello.

Alex Godoy-Faúndez

Facultad de Ingeniería, Universidad del Desarrollo, Santiago, Chile.

Jose Luis Salazar, Héctor Valdés-González, Eduardo Vyhmeister

Escuela de Industrias, Facultad de Ingeniería, Universidad Andres Bello.

Ronaldo Herrera-Urbina

Departamento de Ingeniería Química y Metalurgia, Universidad de Sonora, Hermosillo,

Sonora, México.

ABSTRACT

According to achieve a sustainable development, Chilean mining industry needs to

embrace the best practices to its sustainable growth as engine developments. Relationships

between mining industry and society have been historically complex due to its

environmental impacts. Whereas the ore grade has declined continuously, this has involved

an intensive energy and water consumption correlated to operational costs at different

stages of process. Indeed, the amount of organic chemical reagents used in froth flotation of

copper sulphide ores has a big impact on production costs as well as a huge effect on the

environment. In this research was evaluated, via standard methodologies at laboratory

scale, the use of biosolids and its main components (i.e., humic substances) as froth

flotation reagents for sulphide ore concentration. These substances interact through

physical and chemical ways due to differential affinities to mineralogical species such as

chalcopyrite and pyrite. Aqueous solutions prepared with biosolids show good frothing

characteristics whereas humic acid was found to act as collector for the concentration of a

copper sulphide ore. Therefore, biosolids and its main components may open an

opportunity to be used in copper sulphide flotation plants to partially replace conventional

reagents, which are more hazardous and less environment-friendly.

Page 4: 02 Mineral Processing

Mineral Processing

MP02

THE EVOLUTION OF MILL RELINING TECHNOLOGY

Winston Rocher

ABSTRACT

Over the past fifty years, technology has advanced quicker than in any other time

and this has impacted greatly on people’s lives, on the equipment and at work.

The small grinding mills had an entry in the mill feed end for the spout feeder that

didn't allow the entry of a person. The discharge of many of them had grates and the only

way for people, liners and tools to get into them was via the manhole. The liners were

installed manually with brute force, using tools like chain blocks, rope and chains,

extending mills shutdown for many hours and increasing the risk of accidents.

The increased size of mills and the high prices for metals means equipment

designers and mining companies need to work constantly to surpass their mechanised

technology, the quality of the materials and their components, increasing their capacity, by

making them faster, more accurate and safer. In addition, the operators are working more

strategically. The result has been a significant decrease of relining time and an increase in

operator's safety.

Page 5: 02 Mineral Processing

Mineral Processing

MP03

GAS DISPERSION MEASUREMENTS IN INDUSTRIAL FLOTATION

EQUIPMENT

Luis Vinnett, Juan Yianatos

ABSTRACT

An extensive database of Sauter mean bubble diameters, D32, and superficial gas

rates, JG, measured in different industrial flotation plants, is presented. Results involved

mechanical flotation cells of 10 – 300 m3 from Rougher, Cleaner and Scavenger circuits

and columns from Cleaner circuits. A significant effect of superficial gas rate on bubble

diameter was observed in mechanical cells with different bubble generation mechanisms,

cell design (self-aerated or forced air) and under different operating conditions (frother

dosage, impeller speed). This result implies a dominant effect of the superficial gas rate on

the gas dispersion. Also, higher D32 values were observed in flotation columns because of

the bubble sparger system and mainly due to lack of maintenance. From the D32 and JG

values, the bubble surface area flux, SB, was evaluated in order to determine normal

operating conditions. The gas dispersion database is useful to select proper operating

conditions and to define control criteria in flotation circuits.

Page 6: 02 Mineral Processing

Mineral Processing

MP04

EMPIRICAL CORRELATION FOR ESTIMATING GRINDING MEDIA

CONSUMPTION

Carlos Rabanal

Moly-Cop Adesur S.A.

[email protected]

ABSTRACT

The concern regarding grinding media wear is as old as the invention of the

tumbling mills. Over the years many materials and grinding media shapes have been tested,

through all this, steel grinding balls have proved to be the most effective media for

comminution in tumbling mills.

In the same way, no accurate technique for estimating the wear of the ball charge

has been developed. The mining industry still utilizes the Bond Abrasion test that was

developed in the 60´s, this test is based in the ore properties having an error higher than

60%.

Lately in 2007, Radziszewski proposed a decouple total grinding media wear model,

this model is based in decoupling the effect of abrasion, corrosion and impact wear

mechanism, this new decoupled model gets an error of +/- 17% which is an improvement in

comparison to Bond model, but still shows high degree of error.

Also In 2007, Benavente from Moly-Cop Group presented an empiric model based

in operational conditions that affect wear mechanism. This new model shows an average

error of +/- 10% which represent a higher improvement in comparison with other models.

This paper present the research developed by Moly-Cop in order to improve the

capability of the empiric model developed by Benavente to estimated grinding media wear.

The work performed includes extensive determination of Bond Abrasion Index for different

kind of ores, operational information from concentrators and statistical analysis to

determine the more significant variables over the wear.

The result of the research let us to build a more robust and confident model to

estimate grinding media wear rate. The average error of this new model was in order of +/-

5.0% which means a higher improvement over the models previously described.

Page 7: 02 Mineral Processing

Mineral Processing

MP05

CHARACTERIZATION OF COPPER CLAYS AND GEOMETALLURGICAL

IMPLICATIONS

Ursula Kelm, Oscar Jerez, Sonia Helle, Marcos Pincheira

Instituto de Geología Económica Aplicada, Universidad de Concepción, Chile

ABSTRACT

Copper clays are a common mapping term to describe parts of argillic and advanced

argillic alterations associated with Andean type copper deposits. They are very fine grained

materials with a bluish hue, which may or not expand when humidified. These “copper

clays” accompany chrysocolla, atacamite and secondary sulphide mineralization. Copper

clays have been characterized by X-ray diffraction, Qemscan, Transmission Electron

Microscopy and complemented by determination of cation exchange capacity.

Observations are contrasted with literature data on (1) the attempts of synthesis of Cu-

phyllosilicates, (2) the modification of phyllosilicates with Cu bearing molecules for

catalysis and (3) larger than clay-size phyllosilicates incorporating Cu phases between

individual sheets. For the studied copper clays, discrete copper phases were found to be

intercalated between individual phyllosilicate layers on a nanometric scale. For acid

extraction of Cu from these combined clay and Cu phase aggregates, rock texture and acid

stability of the phyllosilicate species are of fundamental importance.

Page 8: 02 Mineral Processing

Mineral Processing

MP07

PROGRESS MADE IN PILOT AND LABORATORY THICKENING STUDY

R. Fuentes, P. Garrido, T. Watt

Centro de Investigación JRI S.A., Santiago, Chile

ABSTRACT

When designing thickeners, it is necessary to take into account the variety of

geological units of different lithologies and alterations that may appear during the useful

life of the mine, especially during the first five years. Ignoring these aspects leads to

different operational problems in industrial thickeners of copper tailings and concentrate,

which are unable to comply with the overflow quality or the percentage of solids required

in the output. On the other hand, precision in determining the thickener unit area has great

impact on the thickener CAPEX.

Centro de Investigación JRI S.A. (CdI-JRI) is developing a research line (I+D)

oriented to studying thickening processes and whose main objective is focused on design.

Standard measuring of geological attribute variability conducted in a laboratory is being

contrasted with measuring carried out in batch and continuous pilot tests.

CdI-JRI has designed and built two pilot columns for this purpose, 1 and 4 meters

high respectively, equipped with a rake and different feedwells. Both implemented columns

allowed Cdl-JRI to develop its own methodology for characterizing the thickening of

mining slurries in batch and continuous tests.

This paper presents the main results obtained: thickener unit area, concentrations of

solids in underflow and overflow, the effect of the feedwell on the quality of the overflow,

and the effect of the rake on the concentration of solids in the discharge.

Page 9: 02 Mineral Processing

Mineral Processing

MP08

EFFECT OF FINES CONTENT ON YIELD STRESS OF COPPER TAILINGS

N. Rojas.

Instituto de Minerales CIMEX, Universidad Nacional de Colombia, Medellín, Colombia.

P. Garrido.

Centro de Investigación JRI S.A., Santiago, Chile

ABSTRACT

Thickening calculation and design, hydraulic transport of mine slurries, and final

disposition of tailings are some of the areas in which a rheological characterization

containing at least viscosity and yield stress is indispensable.

These rheological parameters depend on a number of variables. Among others,

concentration of solids, pH, particle size distribution, Zeta potential, and the reagents

eventually added. On the other hand, this rheology is intrinsic to each treated slurry, and

varies throughout the life of a mining operation mainly due to changes in the geological

units and/or modifications in operating conditions.

This paper studies the influence of particle- size distribution on the rheological

characteristics of tailings. Three sizes known as fines are considered: material under mesh

200 (74 micron), material under mesh 400 (37 micron), under mesh 500 (25 micron). Each

of these is incorporated into the original tailings at different percentages, generating tailings

with “a new particle-size distribution”, which are then rheologically characterized.

With these results we are able to conclude that the three sizes of fines that were

studied, especially the 37-micron size (under Tyler mesh 400), generate an increase in yield

stress, shifting the yield stress curves versus the percentage of solids towards the left. This

may have a decisive impact on the thickening, transport and disposition of slurries.

Page 10: 02 Mineral Processing

Mineral Processing

MP09

STUDY ON SEPARATION OF ARSENIC FROM COPPER CONCENTRATE

Shigeto Kuroiwa, Daisuke Sato, Tatsuya lto, Misturu Sawada

Metallurgist, Niihama Research Laboratories, Sumitomo Metal Mining Co., LTD

Tsuyoshi Hlrajima

Professor, Department of Earth Resources Engineering, Faculty of engineering,

Kyushu University

ABSTRACT

Sumitomo Metal Mining Co.LTD, Niihama Research Laboratories (NRL) has been

developing Cu/As separation technology from chemical approach (investigating and

optimizing solid-liquid interfaces) and physical approach (studying the effect of flotation

equipment).

lnfluence of oxidization on the contact angle of tennantite, chalcopyrite, bornite and

pyrite was investigated. When the surface was not oxidized, tennantite indicated similar

contact angle to non-arsenical copper minerals, chalcopyrite and bornite. The contact angle

of tennantite became smaller than that of the non-arsenical copper minerals when weak

oxidization was applied.

Effect of physical parameters of flotation equipment on separability of arsenic was

also investigated. Results agreed with proposed flotation models, however above mentioned

effect was small.

Page 11: 02 Mineral Processing

Mineral Processing

MP11

TECHNICAL EVALUATION OF THE REPLACEMENT OF CONVENTIONAL

FLOTATION CELLS BY FLOTATION CELLS PNEUMATIC IN THE BENEFIT

OF COPPER ORES

Sergio Arellano G., Gonzalo Reyes M., Víctor Conejeros T.

Universidad Católica del Norte

ABSTRACT

A company of the mining medium, located in the II Region of our country, requires

to increase the treatment capacity of the current plant. Long enough to make the

modifications, settled into place 2 G-Cell 18 type pneumatic cells that replace 100% to the

primary circuit. The implementation of this type of cells relies mainly to the reduced space

that they occupy and almost no structural alteration of what already exists, in addition,

update the process to a technology that most recent flotation that could result in

improvements mainly metallurgic.

The general objective of this work, is to evaluate technically and economically the

use of pneumatic cells, type G-Cell in a primary circuit of copper concentration.

The methodology of work considered historical results of conventional circuit, a

physical, chemical and mineralogical characterization of minerals to evaluate, samplings of

workflows to obtain data that will assist in the preparation of comparative balances of

technical results and the economic assessment that will affect the final decision of what

mineral is that will benefit. Two types of sulfide minerals were evaluated: Sulfurado 1 and

Sulfurado 2.

The main conclusion, derived from the results, both technical and economic, is

achieved by processing ore from the Sulfurado 2.

Page 12: 02 Mineral Processing

Mineral Processing

MP13

NEXT GENERATION PRESSURE FILTERS FOR HARD ROCK TAILINGS

T. Wisdom

ABSTRACT

The use of slurry impoundments have traditionally been the primary method of

disposal of waste slurry resulting from the recovery of metals and minerals. However,

current difficulties in obtaining permits to build new impoundments for grass-roots plants,

or as the existing ones near the end of their projected life, has made it necessary to explore

other alternatives for tailings disposal. Fresh water resources are becoming more precious,

and environmental pressures are increasing leading to the elimination of slurry tailings

impoundments.

It is becoming more prudent to consider filtration and dry stacking as a reasonable

and sustainable alternative. There are several obstacles to filtration as a way to treat these

tailings. Many tailings slurries are difficult to filter and higher plant throughputs have in

the past made filtration operations both costly to buy and to operate.

But as with the equipment used to mine and move the harder lower grade ores,

equipment to process the resulting tailings slurries have increased in size, efficiency, and

capacity to meet the demand, as well as to reduce the number of people needed to operate

them. This paper discusses the technical and financial considerations, OPEX and CAPEX,

that influence equipment selection and optimization of the filter pressing system to produce

a satisfactory, transportable and stackable tailings product. Multiple tailings samples have

been investigated incorporating lab and pilot scale testing. The impact of different

minerologies and grain size will be discussed.

Page 13: 02 Mineral Processing

Mineral Processing

MP16

SEAWATER USE IN ANTOFAGASTA MINING GROUP

Francisco Abbott

Minera Esperanza

Gustavo Tapia

Antofagasta Minerals S.A.

ABSTRACT

The Antofagasta plc mining group has been pioneer in the use of raw sea water in

metallurgical process at big scale. In the 90 decade, Minera Michilla began successfully the

use of sea water in the process of leaching copper oxide and secondary sulfide ore followed

by SX-EW. At the end of 2010, Minera Esperanza commissioned a grinding and flotation

plant processing 97 ktpd of sulfide ore, using raw sea water and applied an alternative

depressant for pyrite in the cleaning stage.

Page 14: 02 Mineral Processing

Mineral Processing

– 1 –

MP17

ANTAPACCAY – TINTAYA EXPANSION

D. García and J. Villanueva

Concentradora Antapaccay, Xstrata, Peru

ABSTRACT

Xstrata recently completed construction of a new 70,000 tonne per day copper

concentrator near Cusco, Peru. Plant start-up was accomplished during the last quarter of

2012. Comminution will be accomplished by primary crushing, SAG milling and pebble

crushing followed by ball milling. The Concentrator is a single line configuration,

comprising of one 40 ft. diameter x 22 ft. long (EGL) SAG mill driven by a 24,000 kW

gearless drive. The SAG mill feeds two ball mills each 26 ft. in diameter x 40 ft. long

(EGL), each driven by a 16,400 kW through gearless drive. This represents the higher

power of SAG in the world and the first 40 ft. SAG in Peru. This paper reviews the

project’s technology.

This represents the first Xstrata’s Standard Concentrator, the higher power of SAG

in the world and the first 40 ft. SAG in Peru, an overland conveyor of 6.5 km with gearless

drive, the use of an old pit as tailings dam in big mining and the higher torque of tailings

thickener. This paper reviews the history, the background, the grinding circuit design and

the operations start-up considering focus in safety, start-up strategies, main issues,

improvement opportunities.

Page 15: 02 Mineral Processing

Mineral Processing

MP18

GRINDING CYCLE OPTIMIZATION FOR PROCESSING OF COPPER SLAG AT

AURUBIS BULGARIA

E.Visariev

D. Kirilov; V. Stoilov; E. Djurova; I. Bonchev; V. Stoyanova;

aurubis bulgaria

Industrial zone

Pirdop, Bulgaria 2070

ABSTRACT

At Copper smelter Aurubis Bulgaria, the slag from Flash furnace and Converters is

processed by flotation. The scheme of slag processing comprise: crushing, two stage

grinding and flotation.

Till 2010 the first grinding stage was AG Mill 70х23 worked with classifier and the

second stage - ball mill 3.6/5.5 with hydrocyclone. In 2010, a new AG Mill 65x78 with

hydrocyclone was commissioned in order to increase the plant throughput. The second

stage of grinding cycle was not changed.

The Old AG mill processed 55-60 t/h slag with 75% content of size - 0.071 mm or

over 75 t/h with 35-40% content of size -0.071 mm.

The new AG Mill was designed for throughput of 105 t/h with over 70 % content of size -

0.071 mm. After start-up some problems with the equipment occurred – block-up of AG

Mill’s grate and pumps for cyclone feeding. One of the main problems was a fast wearing

of new AG mill hydrocyclone sand nozzles. Different nozzles materials (rubber, ceramic

and metallic) were tested.

This paper presents:

Comparison of optimal working parameters of old and new working scheme;

Change of technological parameters with different sands nozzles and its effect on

circulating load;

Page 16: 02 Mineral Processing

Mineral Processing

MP19

IMPROVED DEM MODEL FOR PREDICTING CONE CRUSHERS’ PERFORMANCE

Dr. V. Murariu and Dusty Jacobson

Metso Minerals Industries, Inc.

ABSTRACT

Cone crushers have been applied in mineral processing or comminution circuits for more

than five decades. In that period of time, the principle of machine selection and optimization

have evolved from purely empirical methods (capacity tables and product size curves based on

best practice) to include newer simulation based approaches.

These simulation techniques combine the strength of theory with traditional population

balance techniques. Metso’s crusher simulation employs DEM with a proprietary fast breakage

technique using the concept of incremental damage. This paper provides an overview of the

Metso cone crusher simulation technology, and highlights the value of the virtual machine for

equipment design and optimization.

Page 17: 02 Mineral Processing

Mineral Processing

MP22

THE EFFECT OF FLOCCULANTS AND THEIR DEGRADATION PRODUCTS

ON MOLYBDENITE FLOTATION

S. Castro

Department of Metallurgical Enginering, University of Concepcion,Chile

J.S. Laskowski

NB Keevil Institute of Mining Engineering, University of British Columbia,

Vancouver,Canada

ABSTRACT

Modern ore processing plants must have closed circuits in which process water is

recycled back after removal of fine particles in the solid/liquid separation unit operations.

Flotation of Cu-Mo ores includes two steps: a bulk flotation where molybdenite is

recovered together with Cu and Fe sulfides; and a subsequent selective flotation step where

molybdenite is separated from depressed copper sulfides. Flocculants are usually employed

in Cu-Mo concentrate thickeners preceding the selective molybdenite flotation plant.

However, the floatability of molybdenite, similarly to other naturally hydrophobic minerals,

is highly sensitive to the effect of both natural and synthetic polymers. In this work

flotation testing demostrate that conventional flocculants of the polyacrilamide type (PAM)

are strong depressants for molybdenite flotation. Additionally, shear degraded

polyacrylamides, in spite of loosing flocculation ability, are still able to depress

molybdenite flotation.

Also polyethylene oxide (PEO) have been studied in this project. The results show

that its ability to flocculate is pH dependent. In slightly acidic pH PEO and PAM showed

similar flocculation efficiencies on molybdenite suspensions. In alkaline pH, the

flocculating and depressing effects of PEO increased. In the case of PAM, a simultaneous

loss of flocculating and depressing efficiency was observed in alkaline pH. The proper use

and selection of flocculants for better molybdenite recovery is discussed.

Page 18: 02 Mineral Processing

Mineral Processing

MP24

ADVANTAGES AND DISADVANTAGES OF BROWNFIELD PROJECTS

Fernando Pino

Senior Process and Commissioning Engineer

Jacobs Engineering, Chile

ABSTRACT

Projects are classified as Greenfield or Brownfield, the latter corresponding to those

dealing with expansion, modification and/or optimization of existing operations. Usual

thinking is that Brownfield Projects are easier to define and develop than Greenfield or new

Projects; however, evidence shows that rather the opposite is true.

Advantages of Brownfield Projects are the available improved knowledge of ore

characteristics, metallurgical processing, unit operations, equipment performance and

personnel know how. However, there are serious hurdles to overcome, such as:

coordination between the EPCM Company, the Owner Project Manager and the Operations

Manager; building additional facilities within a running operation under acceptable safety

conditions; need to maintain production level during construction; connections or “tie-ins”

of new facilities to the existing ones; possible modifications required due to technological

evolution or changes in the ore nature; in this paper, some general recommendations are

drawn from the analysis of selected typical cases, comprising tie-in identification, design,

engineering, coordination and implementation; and planning the execution of modifications

during normal and extraordinary plant detentions. Additionally, cases are analyzed for

which innovations can have important effects on commissioning and start up schedule for

both project types.

Page 19: 02 Mineral Processing

Mineral Processing

MP26

FROTHER ROLES CHARACTERIZATION IN A LABORATORY

FLOTATION CELL

C.O. Gomez, P. and J. Alvarez

Universidad of Concepción

Departamento de Ingeniería Metalúrgica

Edmundo Larenas

Concepción, Chile

ABSTRACT

Frothers play two major roles in flotation: preservation of the formation bubble size

and stabilization of the froth. Many tests have been proposed to characterize one of these

two functions and to classify frother strength based on the results obtained. A technique to

characterize these two roles simultaneously, using a laboratory flotation column, was

developed and successfully used to screen and select a replacement candidate for a

particular concentrator.

The test requires column steady state operation maintaining a constant froth height,

which entails large volumes of plant water. A technique based on batch testing around a

laboratory mechanical cell not only would demand less water, but also would make

possible on-site testing. This communication presents the development results of a batch

test to characterize frother roles in a laboratory mechanical cell, which is done through the

determination of the critical coalescence concentration and the water overflow curve.

Frothers tested follows the same classification sequence previously obtained in the column

tests.

Page 20: 02 Mineral Processing

Mineral Processing

MP28

SAG MILL DISCHARGE SECTION OPTIMIZATION STUDIES AND REDESIGN

DG Meadows, Luis Vergara, Thomas McQuillan, Horacio Marin

ABSTRACT

The SAG mill is the primary work horse on the majority of comminution circuits

throughout the globe. With declining head grades the need for higher throughput circuits

has become prevalent particularly in Latin America. This paper describes the recent design

knowledge and practical experience gained in both the areas of pulp lifters and integrated

trommel design. The importance of system efficiency in terms of pulp removal is described

together with the need for enhanced slurry distribution onto the trommel screen itself.

Redesign starts with the replacement of the original OEM discharge mill linings,

generally made of Cr-Mo steel alloy castings, by liners made from a steel-rubber-ceramic

composite that acts by using each material property for specific work and application. Thus,

very hard ceramic takes care of wear resistance, the rubber matrix underneath helps absorb

impact loads and steel gives structural support, offering a more efficient solution for the

service required workloads in terms of resistance/weight ratio and endurance.

The unique and complete discharge process from the mill grates to the pebble

collection chute at the end of the trommel was studied in depth. The flow of pulp through

the SAG mill, discharge trunnion and trommel was modeled in detail using modern

techniques such as SPH/CFD and DEM. This enabled the integral design of the pulp lifters,

trunnion section, trommel and trommel panels to be optimized and then finely tuned for

maximum throughput of fresh ore.

The final result with an optimized discharge performance allows a more efficient

energy usage and or a better ore processing mill capability that enhances its performance

and so may pay back significant investment costs. Practical data relating to the influence on

circuit operating times and availability are also described.

Page 21: 02 Mineral Processing

Mineral Processing

MP29

INSTALLATION OF INTERNAL LAUNDERS ON 130 m³ FLOTATION CELLS

AT MINERA LOS PELAMBRES

F.D. Henríquez and L. Maldonado

Minera Los Pelambres

Santiago, Chile

ABSTRACT

In the last decades flotation equipment has shown a significant increase in size. At the

present moment, most of the concentrators plants operating in Chile have been fully

equipped with 130–250 m³ mechanical cells and the new projects are considering the 300

m³ cell on its flotation circuits. This dramatic increase in size poses new challenges in terms

to develop better approaches to optimize the operations.

Originally, Minera Los Pelambres rougher Cu – Mo flotation stage was equipped

with 130 m³ in volume WEMCO cells with no internal launders on it. This paper describes

the metallurgical comparison between two parallel flotation lines, one of them with recently

internal launders installed on the three first cells. For this purpose, a six month sampling

campaign was developed in order to obtain the metallurgical parameters of concentrate

grade and recovery.

The analyzed data demonstrated an improvement in the Cu and Mo recovery of about

0,11% due the effects of internal launders on cells stabilization and increase on the

available concentrate discharge perimeter. This result led to extend the installation of these

devises on the other three lines remaining on the three firs cells.

Page 22: 02 Mineral Processing

Mineral Processing

MP30

CONCENTRATION OF COPPER OXIDE MINERAL WITH HYDROXAMATE

H. Nematollahi, F. Kiani and M. Asgari-Mehrabadi

kian mine pars co.

ABSTRACT

Takhate-Gonbad porphyry copper mine is located at the 80 km northeast of Sirjan,

Kerman Province, south-east of Iran. The main mineralization zones of Takhate-Gonbad

mine include: leached, oxide, mixed and hypogene. The main purpose of this study is

beneficiation of oxide zone minerals by flotation. The flotation tests are carried out on

samples obtained from 4 boreholes.

The average grade of these samples are from 0.33 to 0.86% Total Cu. The host rock

of these boreholes are different. They are: micro-granodiorite, silicified rocks, tuff and

metamorphic rocks and calcite tuff. Regarding presence of both sulphide (i.e. chalcopyrite,

covellite) and oxide (i.e. cuprite, malachite) minerals, flotation tests are carried out in

different conditions, using different reagents.

Based on these tests, the best results are obtained at pH=10.2 with 25 g/t of PAX

and 500 g/t of octyl-hydroxamate. Under this circumstance, the grano-diorite sample is

concentrated with 83.8 % of recovery (the highest one) and the silicified sample is

concentrated with 35.0 % of recovery (the lowest one). Base on obtained results, all 4

boreholes was mixed together and flotation tests were done. The results show that it is

possible to reach concentrate with copper contents15.51% in cleaner stages and 62.9%

copper recovery in rougher stage.

Page 23: 02 Mineral Processing

Mineral Processing

MP31

GRINDING CHEMISTRY – THE APPLICATION OF GRINDING MEDIA TO

IMPROVE METALLURGICAL RESPONSE OF COPPER ORES

Christopher J Greet and Jessica Kinal

ABSTRACT

Numerous studies completed by academia and at industrial scale have consistently

demonstrated that grinding with an electrochemically inert grinding media has significant

benefits when processing copper ores.

This paper provides a summary of pulp chemical and flotation response data for a

variety of copper ores classified by geological type prepared using forged steel and high

chrome grinding media.

The results intend to show that the mineralogical character of the ore has a

profound impact on the pulp chemistry and this effects the flotation behaviour of the

sulphide minerals. Further, the choice of high chrome grinding media, to better control

the chemical environment during grinding, is driven by the mineralogy of the system

under consideration.

Page 24: 02 Mineral Processing

Mineral Processing

MP33

NASH IN THE OPTIMIZATION OF COPPER FLOTATION

CONCENTRATOR CUAJONE

J. Dávila, R. Llerena, N. Benavides and C. Curo.

SOUTHERN COPPER – SOUTHERN PERÚ

Cuajone Mining Camp

Moquegua, Perú

ABSTRACT

Since early 2011, the type of rock ore that reached Cuajone Concentrator Plant

showed high contents of basaltic andesite, andesite Intrusive (% IA +% BA) and surface

oxide ores.

This type of mineral affected the low recovery of Cu, low tonnage of treatment, and

high consumption of sparkling lime. In addition to operating flotation problems, low

stability in the area of foaming Rougher flotation stage.

To improve the recovery of copper, sulphidation was considered, which involves the

addition of reagents to provide ionS2-

and SH-. The role of these ions is to modify

completely the phisycal chemical nature of its surface structure, allowing the adsorption of

collectors on it, and its subsequent flotation. In our case we use the sodium hydrosulphide

(NaSH) as an agent to enable the affected species in the flotation of copper sulphides,

andesites and oxidized surface.

Cuajone Concentrator Plant started its trial period in 2011. With no technical

background in the industry on the conditions, dosages and addition points of NaSH, it was

experimented in different parts of the flotation. And, from September 2011, it has been

determined that the dosage of 15% concentration in the head Rougher flotation at pH 10,

improved copper recovery, reducing the consumption of frother and milk of lime, is also

achievement stabilize flotation.

The average copper recovery improved 2.3%, consumption of Cal and frother

declined by 21% and 28% respectively.

Page 25: 02 Mineral Processing

Mineral Processing

MP35

PREVENTING COPPER LOSS PRODUCTION AND FLOW PROBLEMS

BY MEASURING THE MATERIALS FLOW PROPERTIES

O. Angulo and F. Cabrejos

Jenike and Johanson Chile S.A.

ABSTRACT

Hundreds of millions of tons of copper-containing products in particulate forms

(such as ROM, crushed, agglomerated or leached ore, concentrate, or tailings), having

different characteristics (like particle size distribution, shape and density, moisture content,

chemical, mineralogical and lithological composition), are daily handled, stored and

conveyed in the world through different equipment at the different stages of the copper

minerallurgical processes. In these processes, operators commonly face problems such as

loss of production, flow blockages in the equipment, segregation, equipment wear,

uncontrolled discharge and occasionally unexpected plant shutdowns. Due to the huge

investments involved in world class projects, the mining industry is particularly sensitive to

them.

The purpose of this paper is to provide a cost effective solution to flow problems in

the mining industry, by highlighting a well proven and scientific method used to ensure

controlled and reliable flow of bulk solids, based on Jenike’s flow of solids technology and

laboratory testing [1]. Knowledge of the material flow properties allows designing new

installations or modifying existing defective equipment, and preventing production

stoppages due to the formation of chute pluggages, cohesive arches and/or “ratholes” in

silos, which are the most common causes of flow problems in the copper mining industry.

Page 26: 02 Mineral Processing

Mineral Processing

Page 27: 02 Mineral Processing

Mineral Processing

MP36

THERMODYNAMIC CONSTANTS OF MINERALS OF THE OXIDATION ZONE

OF COPPER – ANTLERITE AND PSEUDOMALACHITE

N.S. Bekturganov

SC «National scientific-technological holding “Parasat”»

18 Republic Ave.

Astana, Kazakhstan 010000

M.R. Bissengaliyeva, D.B. Gogol and Sh.T. Taimassova

The Institute of problems of complex development of mineral resources

5 Ippodromnaya Street

Karaganda, Kazakhstan 100019

ABSTRACT

Minerals of the oxidation zone of copper deposits belong to the most difficult for

enrichment. To transfer them into the easily floatable sulfide components it is necessary to

have new technologies and methods of enrichment associated with solving of a number of

theoretical issues to which the chemical enrichment refers. Optimization and intensification

of the technology process for the purpose of more complete and complex utilization of raw

materials require certain knowledge of thermodynamic properties of the oxidized minerals

since the thermodynamic analysis and a preliminary simulation of the process are necessary

for creation and choice of ore processing schemes. A basic sulfate of copper antlerite and a

basic phosphate of copper pseudomalachite relate to these minerals along with malachite,

azurite, atacamite, chrysocolla, brochantite, etc.

This paper generalizes the results of experimental studies of thermodynamic

properties of antlerite and pseudomalachite obtained by a number of the calorimetric

methods (low-temperature adiabatic calorimetry, the Tian-Calvet high-temperature melt

solution calorimetry). This resulted in obtaining such fundamental thermodynamic

constants as the heat capacity, entropy, the change of enthalpy, the enthalpy of formation

and the Gibbs energy of formation used in simulation of technological processes of

processing of the oxidized and mixed copper ores.

Page 28: 02 Mineral Processing

Mineral Processing

MP38

RECENT DEVELOPMENTS IN FLOTATION COLUMN

INSTRUMENTATION AND CONTROL

R. del Villar, J. Bouchard

Department of Mining, Materials and Metallurgical Engineering

A. Desbiens, É. Poulin

Department of Electrical and Computer Engineering

LOOP (Laboratoire d’observation et d’optimisation des procédés)

Université Laval

Québec (QC), Canada

ABSTRACT

For over two decades, the Process Observation and Optimisation Laboratory

(LOOP) has been working in developing and/or improving specific sensors for flotation

columns and their use for process control. Numerous papers have already been published

for the Mineral Processing industrial and scientific community in peer-reviewed journals

and conference proceedings, e.g. for the Copper Conference series. This paper summarizes

the latest completed milestones by the group, since the last Copper conference held in Chile

in 2003, emphasizing on results presented in North America and Europe since Copper

2010.

On the instrumentation side, developments encompass a more accurate method for

measuring electrical conductivity for flotation column sensors, a device for estimating the

bias rate, a better procedure for evaluating bubble size from images taken by bubble

viewers, and a method for on line estimation of frother concentration. In terms of process

control advances, the discussion will focus on results for bubble size control in a two-phase

system, and the application of a 3x3 multivariable predictive control to a pilot flotation

column running in parallel to industrial columns in a Québec concentrator. Current

investigations on bubble size distribution modeling and control, as well as matching bubble

size to particle size will be discussed.

Page 29: 02 Mineral Processing

Mineral Processing

MP39

METALLURGICAL OPTIMIZATION OF A HIGH DISSEMINATION

AND HIGH HARDNESS COPPER ORE

Raúl Jara Iturre

Empresa Minera Altos de Punitaqui

Miguel Aguirre 280 - Oficinas 47-48. Ovalle

Luis Tello Muñoz, Cristian Gonzalez Bravo, Hector Guinel Figueroa

Empresa Minera Altos de Punitaqui

Miguel Aguirre 280 - Oficinas 47-48. Ovalle

ABSTRACT

Minera Altos de Punitaqui owns a concentrator plant near Punitaqui City, 12 km

south from Ovalle City located in northern Chile’s Fourth Region. This Concentrator plant

processes about 3,500 DMT/day and produces 43,000 DMT/year of concentrate with 28%

copper content and some silver content.

In early 2012, the plant’s copper recovery was approximately 77%. According to

mining standards, this is a low recovery rate, although earlier mineralogical and

metallurgical studies indicated that the maximum possible recovery wouldn´t be higher

than 80% due to the high value dissemination in the feed ore.

The plant superintendence and its technical team developed a work plan resulting in

systematic enhancements to the flotation process; the operational variability decreased and

relevant conditions were modified, including the flotation circuit and process variables; to

end up that year with a steady state recovery of 80 – 82% with a quality of more than 27%

copper, 2% higher than the 2011 average.

In 2013 – without any investment in flotation cells – the flotation capacity has been

increased from 3,100 DMT/day to 3,500 DMT/day with higher copper recovery. This

comes with the bonus alternative of using the “idle” capacity to process other third party

minerals adding further profitability to the Altos de Punitaqui site.

This paper describes both the optimization strategy applied and the improvement

results, underlining the virtuous triangle made up by a well-organized operation, the

metallurgical laboratory support and the support received from the industrial process

analysis, modelling and simulation.

Page 30: 02 Mineral Processing

Mineral Processing

MP40

MARINE TAILINGS PLACEMENT: EXPERIENCES AND LESSONS FROM THE

ASIA PACIFIC REGION

D. Gwyther

Picton Group Pty Ltd

30 Malpas Drive

Wallington Vic3222, Australia

[email protected]

J. Waworuntu

P.T. Newmont Nusa Tenggara,

Jalan Sriwijaya 258 Mataram, Indonesia

[email protected]

ABSTRACT

This presentation looks at some of the advancements in operating and monitoring

that have accompanied the implementation of deep sea tailings placement (DSTP) in the

Asia Pacific region over the past 20 years. It describes the guidelines and criteria that have

been developed to ensure that DSTP systems are properly assessed and located prior to

approval and throughout operation and closure.

In considering the potential applicability of these experiences to countries such as

Chile, substantial research will clearly be required to establish equivalent criteria to achieve

the same objectives and environmental safeguards in the Chilean socio-political context.

However, just as important for gaining acceptability will be the acknowledgement by

governments and all sectors of the community of the existence of the dilemma – now or at

some time into the future – that if the currently accepted land storage methods reach their

physical or safety limits, alternative storage methods will need to be considered. DSTP

cannot be a solution without broad community acknowledgement that a dilemma about

future mine tailings management needs to be faced. It is the role of governments, informed

by scientific study, to evaluate the best solution for future tailings management for the

country in each case.

Page 31: 02 Mineral Processing

Mineral Processing

MP41

MODELLING BUBBLE HYDRODYNAMICS IN FLOTATION

C.O. Gomez and J.A. Finch

McGill University

3610 University Street

Montreal, Canada H3A 2B2

[email protected]

M. Maldonado

Departamento de Ingeniería Metalúrgica

Universidad de Santiago de Chile

Avenida Libertador Bernardo O’Higgins 3363

Santiago, Chile

ABSTRACT

Three parameters are generally used to describe gas dispersion in a flotation

machine: superficial gas (air) velocity, gas holdup and bubble size. Techniques and sensors

to measure local values of these parameters, including industrial flotation units, have been

developed.

A model relating these variables, which was developed based on a drift-flux

analysis of bubble hydrodynamics, has been available for many years. The model has been

mainly used to predict one variable (typically bubble size) from measurements of the other

two. Gas dispersion measurements in laboratory and industrial units have demonstrated

that in many cases significant differences between measurement and model prediction exist.

A reliable model to predict properties of bubble populations would help in the

selection and operation of flotation equipment. This work takes laboratory air-water data

sets to establish the adequacy of the equations in the drift-flux model. The results

demonstrated that ignoring the effect of frother on bubble terminal and swarm velocities is

the reason for the poor model prediction.

Page 32: 02 Mineral Processing

Mineral Processing

MP42

PRIMARY CRITERIA FOR PRESSURE COPPER LEACHING PROCESS

SELECTION

G. Debernardi, R. Souyris and M. Gianetti

DESSAU CHILE INGENIERÍA

Ricardo Lyon 222, Piso 10, Providencia

Santiago, Chile

[email protected]

[email protected]

J. Menacho

De Re Metallica Ingeniería

Av. del Valle 601, oficina 31, Huechuraba

Santiago, Chile

[email protected]

ABSTRACT

Several hydrometallurgical processes for high and moderate pressure leaching of

copper sulfides have been developed in the past years, such as the Total Pressure Oxidation,

Sepon, Platsol, Mt. Gordon, AAC/UBC, Dynatec, CESL, Activox and MT-DEW-SX

processes. Nowadays, several are under industrial scale application, or well tested at pilot

scale level.

The basics and current status of these processes is briefly reviewed, with special

consideration on their applicability to the leaching of different copper ores, depending on

its sulfide mineralogy and occurrence of impurities such as arsenic and the presence of

other valuable metals. A comparison of the general conditions in the autoclave leaching for

each process is presented, and a decision tree is proposed for a simple choice of the best

technology for a given application from a process point of view, before proceeding to

perform feasibility study.

Page 33: 02 Mineral Processing

Mineral

Processing

MP43

STRUCTURAL DESIGN OF RECLAIM TUNNELS …

ADDRESSED AS A MINGA

Rodrigo Huenchullán G., Civil Structural Engineer, Sr.,

This work compiles the ideas contributed from both a number of structural engineers

and designers who have addressed the structural design of reclaim tunnels as well as

from people related to other engineering disciplines, as if it was a minga(*) in order to

tackle the topic in a more comprehensive way. While in the process, an attempt will be

done to shed more light on some concepts that in structural practice have been

addressed in many different ways, mainly as a result of the scarce reference material

on criteria and national and international codes to be applied on their design. Seismic

and mineral-associated loads are specially analyzed as well as important design

aspects.

Page 34: 02 Mineral Processing

Mineral Processing

MP44

IMPROVED COPPER AND GOLD RECOVERY AT KGHM

INTERNATIONAL’S ROBINSON MINE

Lorin Redden

FLSmidth Salt Lake City, Inc.

7158 South FLSmidth Drive

Midvale, Utah 84098

[email protected]

Chase Stevens, Mark O’Brien and Thomas Bender

KGHM International Ltd., Robinson Nevada Mining Company

4232 West White Pine County Road 44

P.O. Box 382

Ruth, Nevada

ABSTRACT

In an effort to recover additional copper and gold at KGHM International’s

Robinson Mine located near Ruth, Nevada, an in-plant study was undertaken to quantify

potential flotation recoveries from the concentrator’s final tailings stream. Tests were

conducted by passing a small continuous sample of final tailings though a single 1.5 m3

demonstration flotation machine. Two phases of testing were conducted on differing ore

types. Results indicated that up to 30% of the contained copper was recoverable along

with significant quantities of gold. Based on these results, the existing flotation circuit

was expanded by installing four (4) 160 m3 FLSmidth XCELL™ flotation machines to

treat the final tailings stream. This paper reviews the results obtained from the in-plant

testing with the single 1.5 m3 flotation cell and provides a comparison to the subsequent

operational performance of multiple 160 m3 flotation machines.

Page 35: 02 Mineral Processing

Mineral Processing

MP45

MODELLING BUBBLES GOING THROUGH FLOTATION CELLS

Jorge M. Menacho and Juan Rodríguez

De Re Metallica Consultant, Av. Del Valle 601, Oficina 31, Huechuraba, Santiago,

Chile, (562)-738-4493, [email protected]

ABSTRACT

A new phenomenological approach is presented in this paper, in which bubble

dynamics is described from the bubble generator, going through the slurry phase, where

they move within a turbulent circulating field subjected to simultaneous rupture and

coalescence phenomena, both controlled by the frother HLB and dosage. Size growth

simultaneously occurs due to lower pressure as bubbles move up. After a time bubbles

arrive to a compaction zone where porosity is reduced becoming a continuous bed. Then

the bubble bed enter the froth phase moving upward in plug flow condition and

capillary drainage occurs getting bubbles even closer and promoting further

coalescence, such that in the final froth zone bubbles are nearly impervious to washing

water.

Equations representing the above-described physical model are presented and

several examples of performance are given.

Page 36: 02 Mineral Processing

Mineral Processing

MP47

PNEUMATIC FLOTATION IMHOFLOT

PRODUCTION TECHNOLOGY IN CHILEAN MINING

S.E. Sánchez-Pino1, S.A. Sánchez-Baquedano

1, R.M.Imhof

2, H. Sprenger

2

1 Ingeniería de Minerales S A

2 Maelgwyn Mineral Services L.

Washington St. 2653 Of. 501, Antofagasta, Chile, [email protected]

ABSTRACT

Pneumatic flotation technology (Imhoflot) is already in the Chilean Copper Mining

Industry since 1992, Ingeniería de Minerales S.A. (IDM) together with the designer Dr.

Rainer Imhof from Germany through his Company Maelgwyn Mineral Service Limited

(MMS).

Successful industrial application are already working at Los Pelambres in Molybdenum

Plant, Codelco Andina as pre rougher to end concentrate, also Molybdenum Plant, Las

Luces Plant in Copper concentrator, as pre rougher to end concentrate using sea water,

Minera Valle Aconcagua processing a full automatic plant fed pre concentrate from

Codelco Andina fresh tailing. Also it was a positive copper application at Minera

Michilla, using sea water and Minera Tamaya for Copper – Gold mineral.

Positive operational changes in flotation circuit designs have been installed in

production circuits using G cell and vertical cell, improving performance of flotation

circuits and quality of end products.

High concentration of bubbles and micro turbulence from aeration unit design, provide

high probability of collision and attachment, reducing dramatically the residence time,

self-sucking air, low maintenance, full automation process and small surface to montage

this kind of plants are some of the main the advantages.

Rotation phenomenon introduced in the vessel of the G Cell creates radial separation

forces which are the main key to separate faster the bubbles with concentrate from the

tailing and the high selectivity to get concentrate, introducing also a very short residence

time in the separation vessel.

As result of the industrial experience in Chile, the pneumatic flotation type G Cell can

be regarded as a technology which has to be considered to remove quickly fines and

ultra-fines liberated particles to end concentrate, reducing the recycling load in the

conventional flotation circuits and this could be consider as a pre rougher cell to

produce end concentrate directly.

Page 37: 02 Mineral Processing

Mineral Processing

MP48

REMOTE SOLUTIONS TO IMPROVE PROCESS RESULTS AT

CONCENTRATOR PLANTS

Jorge M. Menacho

De Re Metallica Consultant, Av. Del Valle 601, Oficina 31, Huechuraba, Santiago,

Chile, (562)-738-4493, [email protected]

ABSTRACT

A new approach to improve operational managing at concentrator plants is described in

this paper. It combines robust process models connected to intelligent algorithms

specially designed for specific goals, all settled into a powerful communication platform

which assure maximum usability through remote applications.

This approach combines expert knowledge and modern cloud computing technology to

produce efficient tools for monitoring, optimization and control of critical operational

issues.

Specific examples are given showing potentiality of these tools, directed toward

increasing of productivity and efficiency, reducing water and energy consumption and

improving communities and environment friendship.