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ADVANCES IN MINE TAILINGS AND WATER MANAGEMENT IN THE MINING INDUSTRY FOR A CIRCULAR ECONOMY Natalia Andrea Araya Gómez Thesis presented in accordance to the requirements to obtain the degree of Ph.D. in Mineral Process Engineering Supervisors Luis Cisternas Ph.D. - Andrzej Kraslawski Ph.D. Laboratory of Optimization and Modelling Department of Chemical and Mineral Process Engineering Universidad de Antofagasta Antofagasta, Chile 2020

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Page 1: ADVANCES IN MINE TAILINGS AND WATER MANAGEMENT …

ADVANCES IN MINE TAILINGS AND WATER

MANAGEMENT IN THE MINING INDUSTRY

FOR A CIRCULAR ECONOMY

Natalia Andrea Araya Gómez

Thesis presented in accordance to the requirements to obtain the degree of Ph.D. in

Mineral Process Engineering

Supervisors

Luis Cisternas Ph.D. - Andrzej Kraslawski Ph.D.

Laboratory of Optimization and Modelling

Department of Chemical and Mineral Process Engineering Universidad de Antofagasta

Antofagasta, Chile

2020

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AVANCES EN EL MANEJO DE RELAVES Y DE

AGUA EN LA INDUSTRIA MINERA PARA UNA

ECONOMÍA CIRCULAR

Natalia Andrea Araya Gómez

Tesis para optar al grado de Doctor en Ciencias de la Ingeniería de Procesos de

Minerales

Profesor Patrocinante Luis Cisternas Ph.D.

Profesor copatrocinante

Andrzej Kraslawski Ph.D.

Laboratorio de Optimización y Modelamiento Departamento de Ingeniería Química y Procesos de Minerales

Universidad de Antofagasta Antofagasta, Chile

2020

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Supervisors

Professor Luis Cisternas Arapio Departamento de Ingeniería Química y Procesamiento de Minerales Universidad de Antofagasta Chile

Professor Andrzej Kraslawski

Industrial Engineering and Management

LUT School of Engineering Science

Lappeenranta-Lahti University of Technology

Finland

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Abstract

Natalia Araya Gómez

The mining industry consumes vast quantities of water and energy to produce a metal

or mineral product from mineral resources on the earth’s crust, leaving an enormous

amount of mining waste.

The linear thinking of the economy needs to be replaced with the circular economy to

achieve sustainable development goals. In this context, the mining industry needs to

improve in several aspects, such as reducing primary resource consumption and

improve the efficiency of its processes. Strategies to reduce water and energy

consumption, recycle water and wastes, and to recover energy are needed.

The objective of this thesis is to develop methodologies to advance towards the

circular economy in mining, with a focus on mine tailings and water management.

The strategies and tools proposed are meant to be applied in mining processes to

mitigate environmental impacts.

The strategies proposed in water management include an integrated water

distribution network to supply water to several mine plants while recovering energy

using energy recovery devices. The method used is mathematical optimization to

design the water distribution network. The methodology is validated with a case

study that corresponds to an area of the Antofagasta Region. Results show that the

optimal solution is an integrated system with energy recovery devices in areas with a

complex topography where energy production is feasible.

Reducing waste is a key component of the circular economy. Mine tailings are the

main waste produced by the mining industries. Re-processing of mine tailings to

obtain critical materials is proposed, the methodology is an economic assessment

validated with a case study of tailing deposits of the Antofagasta Region. The

economic evaluation considers the discounted cash flow method, sensitivity analysis,

and real options analysis. Results show that an investment based on re-processing

mine tailings to obtain critical materials is feasible in some cases.

The contribution of this thesis is a collection of methodologies to improve mine

tailings and water management to improve mining processes. About mine tailings

management, the strategy proposed is re-processing mine tailings, which will reduce

the amount of waste produced by mining plants and will reduce the need for mining

primary ores. In the case of water management, the mining industry needs to reduce

the demand for freshwater. To supply seawater is still an expensive option but having

an integrated water distribution network with energy recovery devices will reduce

the total cost of the network.

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Keywords: Water Distribution Networks, water management, mine tailings, mining,

circular economy, critical materials, resource valorization, economic assessment

Resumen La industria minera consume grandes cantidades de agua y energía para producir un

producto metálico o mineral a partir de recursos minerales en la corteza terrestre,

dejando una enorme cantidad de desechos mineros.

El pensamiento lineal de la economía necesita ser reemplazado por la economía

circular para lograr los objetivos de desarrollo sostenible. En este contexto, la industria

minera necesita mejorar en varios aspectos, como reducir el consumo de recursos

primarios y mejorar la eficiencia de sus procesos. Se necesitan estrategias para reducir

el consumo de agua y energía, reciclar agua y desechos, y recuperar energía.

El objetivo de esta tesis es desarrollar metodologías para avanzar hacia la economía

circular en la minería, con un enfoque en los relaves mineros y la gestión del agua. Las

estrategias y herramientas propuestas están destinadas a aplicarse en los procesos

mineros para mitigar los impactos ambientales de estos.

Las estrategias propuestas en la gestión del agua incluyen una red integrada de

distribución de agua para proveer de agua a varias plantas mineras mientras se

recupera energía utilizando dispositivos de recuperación de energía. El método

utilizado es la optimización matemática para diseñar la red de distribución de agua.

La metodología fue validada con un caso de estudio que corresponde a un área de la

Región de Antofagasta. Los resultados muestran que la solución óptima es un sistema

integrado con dispositivos de recuperación de energía en áreas con una topografía

compleja donde la producción de energía es factible.

Reducir la cantidad de residuos es un componente clave de la economía circular. Los

relaves mineros son los principales desechos producidos por las industrias mineras.

Se propone el reprocesamiento de relaves mineros para obtener materiales críticos, la

metodología consiste en una evaluación económica validada con un caso de estudio

de relaves mineros de la Región de Antofagasta. La evaluación económica considera

el método de descuentos de flujos, el análisis de sensibilidad y el análisis de opciones

reales. Los resultados muestran que en algunos casos es factible una inversión basada

en el reprocesamiento de relaves de minas para obtener materiales críticos.

La contribución de esta tesis es una colección de metodologías para mejorar la gestión

de los relaves mineros y la gestión del agua en los procesos mineros. Acerca de la

gestión de relaves mineros, la estrategia propuesta es reprocesar los relaves mineros,

lo que reducirá la cantidad de relaves producidos por las plantas mineras y reducirá

la necesidad de extraer minerales primarios. En el caso de la gestión del agua, la

industria minera necesita reducir la demanda de agua dulce. Suministrar agua de mar

sigue siendo una opción costosa, pero tener una red integrada de distribución de agua

con dispositivos de recuperación de energía reducirá el costo total de la red.

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Acknowledgment I would like to express my deepest appreciation to Professor Luis Cisternas for being

my supervisor and for encouraging me to pursue a double degree with LUT

University. I must also thank the project Anillo Agua de Mar Atacama ACT 1201 -

ANID in which I started my thesis research. I’m also grateful of the collaboration

developed in the project Anillo Grant ACM 170005 - ANID.

I would also like to extend my deepest gratitude to Professor Teófilo Graber as head

of the Ph.D. program in Mineral Process Engineering and to all members of Ph.D. in

the Mineral Process Engineering program for all the support during the duration of

my Ph.D. studies.

I would also like to express my deepest gratitude to Professor Andrzej Kraslawski, my

supervisor at LUT University, for support during the realization of the double degree

for my Ph.D. studies.

I would also like to extend my gratitude to Professor Edelmira Gálvez for her support

and collaboration in my firsts two years of my Ph.D. studies in project Anillo Agua de

Mar Atacama ACT 1201-ANID.

I am also grateful to Freddy Lucay for support and collaboration in my research while

being in the Project Anillo Agua de Mar Atacama, resulting in two publications.

I am extremely grateful to ANID for the grant (2017, No. 21170815) for pursuing

doctoral studies.

I am also grateful to Ella and Georg Ehrnrooth Foundation for a grant to continue my

doctoral studies in LUT University.

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List of publications

Publication I

Araya, N., Lucay, F. A, Cisternas, L. A., Gálvez, E. D. (2018). Design of desalinated

Water Distribution Networks: Complex Topography, Energy Production, and Parallel

Pipelines. Industrial and Engineering Chemistry Research, 57, 9879-9888. DOI:

10.1021/acs.iecr.7b05247.

Publication II

Araya, N., Kralawski, A., Cisternas, L. A. (2019). Towards mine tailings valorization:

Recovery of critical materials from Chilean mine tailings. Journal of Cleaner

Production, 263, 121555. DOI: 10.1016/j.jclepro.2020.121555

Publication III (submitted)

Araya, N., Rámirez, Y., Kraslawski, A., Cisternas, L. A. (2019) Real options valuation

of processing mine tailings to obtain critical materials. Sustainable Development

(submitted).

Book Chapters

Araya, N., Cisternas, L. A., Lucay, F. A., Gálvez, E. D. (2017). Design of desalinated

water distribution networks including energy recovery devices. In Computer Aided

Chemical Engineering Vol. 40, pp. 925-930. Elsevier.

Herrera, S., Araya, N., Cisternas, L., Gálvez, E. (2016) Diseño de plantas

desalinizadoras y redes de distribución de agua: una mirada holística. “Agua de Mar

Atacama: Oportunidades y avances para el uso sostenible del agua de mar en

minería”. Capítulo 3. RIL Editores. ISBN: 978-956-01-0388-8.

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Preface

This thesis titled Advances in mine tailings and water management for a circular

economy presents the work performed during the Ph.D. studies started in April 2015

and finished in June 2020. This Ph.D. thesis was developed under a joint supervision

agreement between Universidad de Antofagasta in Chile and LUT University in

Finland.

This document is arranged in two sections. The first section contains the thesis

overview divided into six chapters. The first chapter is the introduction and provides

a context about the background of the study and the motivation and scope of this

thesis. The second chapter, theoretical background, gives an overview of the literature

context. The third chapter contains the research methodology and methods developed

during the study. The fourth chapter contains a review of the results and publications

obtained during the duration of the Ph.D. studies. The fifth chapter is Conclusion, and

it summarizes the theoretical contribution of this Ph.D. thesis, it also provides the

limitation found and future suggestions. Chapter six contains the references. The

second section includes the articles published during the Ph.D. study. The first article,

“Design of desalinated water distribution networks: Complex topography, energy

production, and parallel pipelines” was published in the Journal Industrial and

Engineering Chemistry Research. The second article titled “Towards mine tailings

valorization: Recovery of critical materials from Chilean mine tailings” was published

in the Journal of Cleaner Production. The third article, currently submitted in

Sustainable Development, is titled “Feasibility of re-processing mine tailings to obtain

critical materials using real options analysis.”

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Prefacio

La tesis titulada Advances in mine tailings and water management for a circular

economy presenta el trabajo realizado durante los estudios de doctorado que

comenzaron en abril de 2015 y terminaron en junio 2020. Los estudios de doctorado

fueron realizados bajo un convenio de doble graduación entre la Universidad de

Antofagasta en Chile y LUT University en Finlandia.

Este documento está dividido en dos secciones. La primera sección contiene una

visión general dividida en seis capítulos. El primer capítulo es la introducción, la que

provee un contexto sobre los antecedentes del estudio, la motivación y objetivos de la

tesis. El segundo capítulo, antecedentes generales, proporciona una visión sobre el

contexto de la literatura. El tercer capítulo contiene la metodología de investigación y

los métodos desarrollados durante los estudios de doctorado. El cuarto capítulo

contiene la revisión de los resultados y las publicaciones realizadas durante los

estudios de doctorado. El quinto capítulo, las conclusiones, resume las contribuciones

teóricas de la tesis de doctorado, también proporciona las limitaciones y sugerencias

para investigaciones futuras. El sexto capítulo contiene las referencias. La segunda

sección contiene los artículos publicados durante los estudios de doctorado. El primer

artículo “Design of desalinated water distribution networks: Complex topography,

energy production, and parallel pipelines” fue publicado en la revista Journal

Industrial and Engineering Chemistry Research. El Segundo artículo titulado

“Towards mine tailings valorization: Recovery of critical materials from Chilean mine

tailings” fue publicado en la revista Journal of Cleaner Production. El tercer artículo,

fue enviado a la revista Sustainable Development tiene como título “Feasibility of re-

processing mine tailings to obtain critical materials using real options analysis”.

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Contents

Abstract..................................................................................................................................... 1

Resumen ................................................................................................................................... 2

Acknowledgment .................................................................................................................... 3

List of publications .............................................................................................................. 4

Book Chapters ..................................................................................................................... 4

Preface ....................................................................................................................................... 5

Prefacio ..................................................................................................................................... 6

SECTION I: DISSERTATION OVERVIEW ......................................................................... 9

1. Introduction ................................................................................................................... 10

1.1. Background .......................................................................................................... 10

1.2. Motivation and Scope ........................................................................................ 11

2. Theoretical Background ............................................................................................... 14

2.1. Circular economy and sustainability in mining ............................................. 14

2.2. Water supply for mining ................................................................................... 15

2.3. Mine tailings ........................................................................................................ 16

3. Research Methodology ................................................................................................. 18

3.1. Water Distribution Network (WDN) design for areas with complex

topography considering the energy recovery devices ................................................. 18

3.1.1. Optimization of Water Distribution Networks (WDN) ............................ 18

3.1.2. Problem Statement .......................................................................................... 18

3.1.3. Mathematical Formulation ............................................................................ 19

3.2. An economic evaluation of re-processing of mine tailings to obtain critical

materials ............................................................................................................................. 19

3.2.1. Project valuation Tools ................................................................................... 19

3.2.2. Discounted Cash Flow (DCF) ........................................................................ 20

3.2.3. Real Options Analysis (ROA) ........................................................................ 20

3.2.4. Sensitivity Analysis......................................................................................... 21

4. Publications and Results Reviews .............................................................................. 22

4.1. Publication I: Design of desalinated water distribution networks: Complex

topography, energy production, and parallel pipelines ............................................. 22

4.1.1. Research Objective .............................................................................................. 22

4.1.2. Contributions ....................................................................................................... 22

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4.2. Publication II: Towards mine tailings valorization: Recovery of critical materials

from Chilean mine tailings .............................................................................................. 23

4.2.1. Research Objective .............................................................................................. 23

4.2.2. Contributions ....................................................................................................... 23

4.3. Publication III: Feasibility of re-processing mine tailings to obtain critical

materials using real options analysis (submitted in Science of The Total

Environment) ..................................................................................................................... 23

4.3.1. Research objective ............................................................................................... 23

4.3.2. Contributions ....................................................................................................... 24

5. Conclusions .................................................................................................................... 25

5.1. Theoretical Contribution of the Study ............................................................. 27

5.2. Limitation and Future Research Suggestions ................................................. 27

References .............................................................................................................................. 29

SECTION II: PUBLICATIONS ............................................................................................ 35

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SECTION I: DISSERTATION OVERVIEW

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1. Introduction 1.1. Background

Mining is water and energy-intensive activity, an industry that is needed to ensure the

wellbeing of modern society, moreover mining is present in civilization since ancient

times. Mining activities are usually located in remote and arid areas where water

resources are scarce (Cisternas and Gálvez, 2018; Herrera-León et al., 2019; Ramírez et

al., 2019).

Environmental and social awareness in the last decades around the use of resources

has increased. Nowadays, terms like “circular economy” and “sustainability” resonate

in different fields, mining is no exception (Adibi et al., 2015; Caron et al., 2016; Dong

et al., 2019; Gorman and Dzombak, 2018; Lottermoser, 2011; Reyes-Bozo et al., 2014).

A circular economy is an economy that is restorative and regenerative by design, using

principles of reusing, recovery, recycling, it is about looking beyond the take-make-

waste extractive industrial model (Kirchherr et al., 2017). The concept of circular

economy recognizes the need to work on all scales, while sustainability focuses on

three pillars: economic, environmental, and social, to meet the demands of the present,

ensuring the ability of future generations to also meet their needs.

In Chile, there are numerous mineral processing plants, since Chile is the world´s first

producer of copper. Other metallic elements extracted in Chile are silver,

molybdenum, and gold. As well as for non-metallic elements as boron, iodine, lithium

carbonate, among others (SERNAGEOMIN, 2019). Most of the mining facilities in

Chile are located in the Atacama Desert in Northern Chile, as it features plenty of

minerals. Mining is the principal activity in this area. Usually, plants are located away

from the seashore, so in case of using desalinated water, piping water through long

distances is a must (Herrera-León et al., 2019). Seawater use in mining has been

growing since mines need to reduce the amount of raw water intake from

groundwater and freshwater sources since these are limited and scarce (Cisternas and

Gálvez, 2018). The methodologies developed in this thesis are applied to study cases

based on the mining industry in Northern Chile, specifically the copper mining

activities develop in the Antofagasta Region.

Reducing water consumption and increasing energy efficiency are two essential

requirements to have a more sustainable mining industry. A typical base-metal mine

site consists of an underground or open-pit mine and a mineral processing plant or

mill (Gunson et al., 2010). Most mills use wet processes such as froth flotation to

separate valuable minerals from the non-valuable minerals in the ore. Wet processes

require less energy, but they can use large quantities of water (Gunson et al., 2010).

Currently, each plant has built its desalination plant and water distribution system.

Since mining plants are located far away from the seashore, a way of reducing the

energy used for pumping desalinated water through different mine sites is to have an

integrated water supply system, where industrial symbiosis can be achieved between

desalination companies and mining plants (Cisternas and Gálvez, 2018; Herrera-León

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et al., 2019; Ihle and Kracht, 2018). Energy can be saved by using an integrated water

supply system, efficiency can be achieved by using fewer pipelines and pump stations

if energy recovery systems are placed in the pipelines, energy can be produced and

used in the network (Corcoran et al., 2016; McNabola et al., 2014; Nogueira-Vilanova

and Perrella-Balestieri, 2014a, 2014b; Zakkour et al., 2002).

Another issue in mining is mine tailings, which are the waste produced in mining

processing plants. They are a mixture of fined solid materials remaining after the

recoverable metals and minerals have been extracted from mined ore, together with

water, which includes also dissolved metals and ore processing reagents (Edraki et al.,

2014). Mine tailings can account for 95-99% of the crushed and ground ores (Edraki et

al., 2014).

Environmental impacts and land use aspects should be considered when choosing a

tailing disposal method (Adiansyah et al., 2017). Environmental impacts of tailings

dam failures include human fatalities, contamination of water, and soil (Kossoff et al.,

2014). One of the most severe environmental problems associated with mine tailings

is acid mine drainage, which is produced when sulfide minerals are exposed to

oxygen and water (Akcil and Koldas, 2006). Acid mine drainage is one of the most

significant forms of water pollution (Moodley et al., 2017). Mine tailings management

is crucial in mining operations because of the irreversible impacts of tailings

(Adiansyah et al., 2015).

Mine tailings contain several elements that are not separated from the mineral in the

processing plant. Mine tailings could be reprocessed to obtain valuable elements

contained in them (Binnemans et al., 2015; Falagán et al., 2017). The valorization of

mine tailings is still at its infancy, globally speaking (Kinnunen and Kaksonen, 2019).

Critical materials are a group of materials that are considered of large economic

importance and have high risk in their supply. Now, secondary sources like metal

scrap and mine tailings have a promising future as critical materials sources. Using

secondary sources to recover critical materials has multiple benefits: it allows to

reduce primary ore extraction, decrease the amount of waste, hence decreasing its

environmental impact, give value to waste, contributes to industrial symbiosis, among

others.

1.2. Motivation and Scope

A requirement to achieve sustainable development is to reduce primary resource

consumption, consequently mining activities on primary sources. However, the

demand for metals will continue to exist throughout the transition to a more

sustainable society. Therefore, research must be conducted to explore the role of the

mining industry in the circular economy paradigm and identify strategies for it to

transitioning to a more sustainable mining industry.

In mining, circular economy advocates for reducing primary resource extraction by

replacing it with secondary sources, reducing raw water intake by reusing or recycling

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water, reducing energy dependency, reducing the environmental footprint, reducing

greenhouse gas emissions (Lèbre et al., 2017).

Effective water management in the mining industry can reduce the dependence on

freshwater sources that are scarce in arid regions where most of the mining facilities

are located. In 2018, in Chile freshwater consumption reached 13.36 m3/s, more than

three times seawater consumption, which reached 3.99 m3/s (COCHILCO, 2019a).

Integrated water supply systems between desalination plants and several industries

reduce energy consumption (Herrera-León et al., 2019) and the stress on freshwater

resources. Different strategies can be applied to reduce water consumption and

optimize its use.

Mine tailings are a critical issue in mining as tailings are the waste of processing plants

and are produced in large quantities. In Chile, to March of 2018, 740 tailing deposits

are registered in a national cadaster, being the majority located in the north of the

country. Currently, 101 tailing deposits are in active use, which will accumulate 14,470

million cubic meters, of the 16,000 million cubic meters of the total of tailings stored

in the country, ergo 90.6% of stored tailings come from active mining operations

(SERNAGEOMIN, 2018).

Strategies to save water, recover energy, and reducing waste are needed to make the

mining industry more sustainable and to help to achieve the circular economy. The

motivation of this thesis is to elaborate research to contribute to the literature on water

and tailings management in the mining industry by providing methodologies and

tools that mitigate the environmental impact of mining activities.

This thesis aims to propose strategies to manage water and tailings in the mining

industry. Optimized water distribution networks and efficient water use in tailing

management are proposed as water management strategies. Recovery of critical

materials and reducing water content in tailings are the tailings management

strategies proposed as well. The aim is attained by fulfilling the following specific

objectives and the related research questions:

1. To design integrated water supply systems that include energy recovery

devices in areas with complex topography

RQ 1.1. Is an integrated water supply system that includes energy recovery devices a

feasible option in areas with complex topography?

RQ 1.2. Is it economically and technically feasible to use energy recovery devices in the

water supply system?

RQ 1.3. When using parallel pipes is a feasible option in the water supply system?

2. To investigate the feasibility of re-processing mine tailings to obtain critical

materials

RQ 2.1. What critical materials can be recovered from mine tailings?

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RQ 2.2. What are the challenges in the production of critical materials using mine tailings

as a source?

RQ 2.3. Is it economically feasible to invest in a project developed around the idea of re-

processing mine tailings to obtain critical materials?

3. To develop a methodology to assess the feasibility of re-processing mine

tailings to obtain critical materials

RQ 3.1. How can real options improve the decision to invest in a project using mine tailings

as a source of critical materials?

RQ 3.2. How can the net present values variables influence real options performance?

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2. Theoretical Background Building on the literature review, this section explains the main concepts used in the

thesis and the current situation of the mining industry encompassing the concepts and

definitions used in this thesis.

The demand for copper expected to increase and to exceed copper mineral resources

by mid-century. The increase in copper demand will be associated with a strong

increase in the energy demand and, consequently, the environmental impacts

(Elshkaki et al., 2016). Environmental impacts associated with mining are stress and

pollution of water resources, air pollution, land usage, and production of several

waste streams.

In Chile, mining is a long-standing industry, since the country owns vast mineral

resources. Most of the mining activity is located in the Atacama Desert, northern Chile,

where sulfides ores containing copper are abundant; additionally, non-metallic

resources are also found in the area. Therefore, Chile produces various elements, such

as copper, silver, molybdenum, lithium, boron, among others (SERNAGEOMIN,

2019). Mining represents 10% of the national Gross Domestic Product (Reporte

Minero, 2018). To achieve sustainable mining, the Chilean state must balance

economic growth with the strictness of environmental policies by continuing to

address the challenge of energy use, water scarcity, indigenous rights, and

governmental organization (Ghorbani and Kuan, 2017).

2.1. Circular economy and sustainability in mining

The circular economy is a concept that resonates lately, which describes an economic

system that is based on business models that replaces the linear economy thinking,

with reducing, alternatively reusing, recycling, and recovering materials in

production/distributions and consumption processes, thus operating at all levels, to

accomplish sustainable development, which implies creating environmental quality,

economic prosperity and social equity, to the benefit of current and future generations

(Kirchherr et al., 2017).

Mining is a global industry, and it is often located in remote, ecologically sensitive,

and less-developed areas that include indigenous land and territories. If managed

poorly, mining can lead to environmental degradations, displaced populations,

inequality, and increased conflict, among other challenges (World Economic Forum,

2016). In the report “Mapping Mining to the Sustainable Development Goals: An

Atlas, 17 Sustainable Development Goals (SDGs) are presented. This report presents

an overview of the opportunities and challenges that the mining industry needs to

address, from exploration through production and finally mine closure. SDG6 is about

water in mining, the goal includes reduce water consumption, use alternatives water

sources as seawater and greywater, integrate technical, social, economic, and political

water concerns and identify high-value water areas. About waste, SDG 12 is about

mining and responsible consumption, the mining industry should aim to minimize

the production of waste and give value to waste (World Economic Forum, 2016).

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2.2. Water supply for mining

Mining consumes large quantities of water; in Chile, water consumption in mining

was 62.7 m3/s in 2018, where 72% correspond to recirculated water, 22% to freshwater

from inland sources, and 6% to seawater (COCHILCO, 2019a). However, mine water

use accounts for a small portion of overall use (Gunson et al., 2012). Nevertheless,

when mining sites are located in areas where water is a scarce resource, then mine

water consumption can have a significant impact on local water resources (Northey et

al., 2016). There is clear overexploitation of water resources in northern Chile, water

resources are insufficient to meet environmental, domestic, and industrial

requirements (Aitken et al., 2016).

Most mineral processing plants use wet processes, such as flotation, which typically

takes place at 25-30% solids by mass (Gunson et al., 2012). Water and energy are

interconnected as water needs energy to be treated and transported until the

processing plant. The mining industry consumes vast quantities of energy. In Chile,

copper mining consumed 176,745 TJ in 2018, which represents 14% of overall energy

consumption in the country (COCHILCO, 2019b). As freshwater sources are getting

scarce, water from other sources is needed. Recycled water from the processes and

desalinated water are options to fulfill the water requirements in the processing plant.

Seawater requires energy to be desalinated and transported until the mining site

(Cisternas and Gálvez, 2018).

Nowadays, freshwater sources are scarce, hence other water sources are needed to

fulfill the demand for water that the mining industry requires. The advances in

desalination technologies, reduction of membrane cost, and lower energy

consumption have made seawater a viable source of freshwater for mining (Knops et

al., 2013). Reverse osmosis (RO) is the desalination process most utilized worldwide

due to its simplicity and lower energy consumption in comparison to distillation-

based thermal processes (Shenvi et al., 2015).

2.2.1. Optimization of water supply systems

The water supply system consists of the water treatment plant, pipeline, and pump

station to supply water to an industrial site or urban community. Methodologies to

design water supply systems usually result in mixed-integer non-linear problems

(MINLP) models (Araya et al., 2018). The water supply system is transformed into a

network to be analyzed, and this is called Water Distribution Network (WDN).

Optimization of WDN has been done by several authors with different approaches

(Ahmetović and Grossmann, 2011; Atilhan et al., 2011; El‐Halwagi, 1992; Herrera-

León et al., 2019; Lira-Barragán et al., 2016; Liu et al., 2011). An integrated water supply

system has demonstrated to be more efficient economically and technically than

having an independent water supply to each mining processing plant (Herrera-León

et al., 2019).

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The reliability of WDN can be improved by adding a parallel pipeline (Gupta et al.,

2014). Parallel pipelines are arranged to divide flow, keeping the head loss at the same

rate, meaning that head loss in all parallel pipes remains the same (Swamee, 2001).

2.2.2. Energy production in water supply systems

The use of pumps as turbines (PATS) could be an option to produce energy in the

network that can be used to reduce the dependency of external sources of energy.

PATs have been used in WDN instead of pressure reducing valves to reduce pressure.

Additionally, PATs can produce electricity the same way turbines are used in

hydropower generation (Corcoran et al., 2016; De Marchis et al., 2014; McNabola et

al., 2014; Tricarico et al., 2014; Zakkour et al., 2002). The energy efficiency of water

supply systems can be increased through the recovery of hydraulic energy implicit in

the volumes of water transported through the supply system (Nogueira-Vilanova and

Perrella-Balestieri, 2014b).

2.3. Mine tailings

A critical issue in mining is the waste streams that are discarded from the processing

plants, being mine tailings, the main waste produced in mineral processing plants,

obtained after using wet processes, such as flotation. Mine tailings consist in a

combination of fine-grained solid materials remaining after the recoverable metals

and minerals have been extracted from mined ore, together with the water used in the

recovery process (Industry.gov.au, 2016), which includes dissolved metals and ore

processing reagents (Edraki et al., 2014). Mine tailings can account for 95-99% of the

crushed and ground ores (Edraki et al., 2014).

2.3.1. Environmental impacts of mine tailings

Environmental implications of tailings dam failures include human fatalities,

contamination of water, and soil (Kossoff et al., 2014). One of the most severe

environmental problems associated with mine tailings is acid mine drainage, which is

produced when sulfide minerals are exposed to oxygen and water (Akcil and Koldas,

2006). Acid mine drainage is one of the most significant forms of water pollution

(Moodley et al., 2017). Mine tailings management is a crucial issue in mining

operations because of the irreversible impacts of tailings (Adiansyah et al., 2015).

2.3.2. Water reclamation in mine tailings

There are a variety of ways to stored mine tailings. Conventional tailing disposal

consists of transport tailings as a slurry to an impoundment or dam. Large volumes

are required to be transported with the tailings to a storage facility (Edraki et al., 2014).

Tailings in conventional residues disposal have approximately 60% water content.

Dewatering technologies, such as thickeners and filters, can reduce water content in

tailings until 20% of water (Gunson et al., 2012). Water-energy nexus in mine tailings

is associated with the pumping system and the technology used in processing the

tailings (Adiansyah et al., 2016). Environmental impacts and land use aspects should

be considered when choosing a tailing disposal method (Adiansyah et al., 2017).

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2.3.3. Re-processing of mine tailings

Re-processing of tailings with the objective of extract valuable elements is a novel

approach of mine tailing management. Studies about geochemical content of mine

tailings have been done with samples of tailings storage facilities to analyze the

content of valuable elements such as critical materials (Ceniceros-Gómez et al., 2018;

Markovaara-Koivisto et al., 2018; Moran-Palacios et al., 2019; Tunsu et al., 2019). The

next step seems to be the re-processing of secondary sources to obtain elements of

interest. However, the environmental implications are still unknown, as re-processing

tailing with such purpose is still not at an industrial level. Further analysis of Reuse

opportunities of mine tailings is needed in the ongoing discussion of sustainable

tailings management (Adiansyah et al., 2017).

Critical raw materials (CRMs) are those raw materials that are highly important to the

European economy and but have high risk associated with their supply (European

Commission, 2017). The most recent list of CRMs includes 27 raw materials, which

consists of three groups elements: heavy rare earth elements (HREEs), light rare earth

elements (LREEs), and PGMs (platinum group metals). As the supply of these

materials is of high risk, the diversification of their sources is needed. Secondary

sources like recycling from landfills and industrials waste as mine tailings appear as

options for obtaining CRMs.

Re-mining wastes and re-processing tailings are possible connections between the

primary resource sector and the waste management sector, which would close a loop

in the circular economy (Lèbre et al., 2017).

The potential use of secondary sources, like landfills and mine tailings facilities, faces

several challenges. The environmental impacts will vary according to the

characteristics of the minerals and rocks and techniques used. There is a need for

statistics about waste facilities with official data about volumes and composition of

waste sites (Careddu et al., 2018). The valorization of mine tailings is still at its infancy.

To valorize mine tailings, the mining industry needs to advance in filling the

knowledge gaps of mine tailings management. The situation is expected to improve

as the mining industry needs to shift from a linear economy to a circular economy

(Kinnunen and Kaksonen, 2019).

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3. Research Methodology After having collected knowledge from literature, methodologies were designed to

examine the issues identified in the previous stage. Next, the required quantitative

data were collected from research articles, public government reports and datasheets,

and company reports. The research methodology is divided into two sections. Section

1 explains the methodology developed to fulfill objective 1, and Section 2 describes

the methodology developed to achieve objectives 2 and 3.

3.1. Water Distribution Network (WDN) design for areas with

complex topography considering the energy recovery devices

This section is intended to explain the process and development of the methodology

designed to answer objective 1 and that is later presented in this document in

publication “Design of Desalinated Water Distribution Networks: Complex

Topography, Energy Production, and Parallel Pipelines.”

3.1.1. Optimization of Water Distribution Networks (WDN)

Water supply systems are usually divided into four components: water intake, storage

and water treatment, water pumping, and the water pipelines for the water

distribution. The WDN for this thesis will be defined as the set of water treatment

plants and the water distribution network, which is composed of pumping stations

and the pipeline to a mining plant.

To analyze WDN, basic principles of fluid mechanics have applied: the continuity

equation, the momentum principle (or conservation of momentum), and the energy

equation. A related principle is the Bernoulli equation, which derives from the motion

equation (Chanson, 2004). Darcy-Weisbach and Hazen Williams equations are applied

to know head loss along pipelines (Swamee, 2001).

WDN design is a complex problem that includes the determination of demand, the

optimal layout of WDN, the dimension of the components like pipes pumps, valves,

tanks, and other components (Amit and Ramachandran, 2009). When designing a

WDN, the goal is to reduce the initial investment and operational costs of the system.

The primary constraint is that the desired demands are supplied with adequate

pressure heads at withdrawal locations. Additionally, the water flow in a WDN, and

the pressure heads at nodes must satisfy the governing laws of conservation of mass

and energy (Amit and Ramachandran, 2009). Providing water at minimal cost results

in an optimization problem, which has been solved using linear programming (LP),

non-linear programming (NLP), Mixed Integer Non-Linear Programming (MINLP),

Mixed Integer Linear Programming (MILP), dynamic programming, and heuristic-

based optimization methods (Amit and Ramachandran, 2009; D’Ambrosio et al.,

2015).

3.1.2. Problem Statement

To achieve objective number 1, a methodology was designed to represent the WDN,

including the selection of desalination plants, specifically RO plants, to supply mining

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sites. The model includes energy recovery devices for energy production located in

areas where due to the difference of altitude between 2 points is possible to produce

energy like in the hydropower industry, these energy recovery devices are known as

PATs. Additionally, parallel pipelines are considered to split the water flow when

needed.

Mine sites are located away from the coast; these sites have a water requirement that

needs to be fulfilled with desalinated water coming from RO plants located on the

coast. The area features a complex topography, which means several changes in

altitude from the coast until the mine site. The only option to fulfill the water

requirement needed is desalinated water from RO plants. The methodology proposed

by Herrera-León et al., 2019 was used as a reference for this methodology.

3.1.3. Mathematical Formulation

A superstructure was used to represent the WDN, which includes RO plants,

pipelines, pump stations, PATs, and the mine sites as nodes. Distances between nodes

and altitude of each node were designed base on topography data obtained in Google

Earth. The superstructure also includes the option to use parallel pipelines.

The objective function minimized the total annualized cost of RO plants, pipes, pump

stations, and PATs required to supply several mine sites located in an isolated area far

away from the coast. The objective function is not linear, so the problem results in an

MINLP problem, which is transformed into a MILP problem using a piecewise

methodology extracted from Lin et al., 2013. This methodology allows converting a

non-linear programming problem into a linear programming problem or a mixed-

integer convex programming problem for obtaining an approximated global optimum

solution.

3.2. An economic evaluation of re-processing of mine tailings to

obtain critical materials

This section is intended to explain the methodology designed to complete objectives

2 and 3. It also presents an overview of the methods applied in publications 2 and 3.

3.2.1. Project valuation Tools

Project valuation is probably the most crucial part of the selection process because it

assigns a monetary value to the project. Broadly defined, the project value is the net

difference between the project revenues and costs over its entire life cycle. If the net

revenues of the project during the production phase are higher than the investment

costs, the project is considered worthy of investment (Kodukula and Papudesu, 2006).

The quality of the project valuation will depend on how they effectively include these

three factors:

Cash flow streams through the entire life cycle of the project

The discount rate used to discount future cash flows to account for their

uncertainty

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Availability of management’s contingent decisions to change the course of the

project

Project cash flows represent the revenues and the costs of the project through the

entire life cycle of the project. The costs should include the initial investment for the

project and the production phase.

Valuation methods assume that money today is worth more than in the future, so to

acknowledge that a discount rate is used. The discount rate is the rate that is utilized

to convert the future value of the project cash flows to today’s money. The discount

rate is adjusted to the risk perceived to be associated with the project, so the higher

the risk, the higher the discount rate (Kodukula and Papudesu, 2006).

3.2.2. Discounted Cash Flow (DCF)

Discounted Cash Flow (DCF) is a valuation method that is based on calculating future

cash flows of a project to decide whether it is feasible or not to invest. DCF is based on

the estimation of the Net Present Value (NPV) of the project in its entire project life

(Kodukula and Papudesu, 2006).

NPV is the preferred metric for project valuation under most circumstances (Arnold,

2014). To calculate NPV, cash outflows, which are the costs of the project, are deducted

from the cash inflows, which represents the revenues of the project. Additionally, all

cash flows are discounted to generate NPV. If the NPV is positive, then the project is

feasible because the revenues exceed the expenses of the project. On the contrary, if

the NPV is negative, then the project is not feasible because the costs are higher than

the revenues. If the NPV is zero, then the return of the project is equal to the expenses.

Traditional valuation tools, including the DCF method, have been employed for many

decades in the economic evaluation of projects. Although these methods have been

effective in many cases, under specific conditions, they have certain challenges. One

of the biggest dilemmas when using DCF is to choose a discount rate. The main factors

that determine the discount rate for a given cash flow stream is the magnitude and the

type of risk (Kodukula and Papudesu, 2006). An important consideration to determine

the discount rate is whether there is uncertainty associated with the cash flow streams.

There are several methods designed to consider uncertainty when calculating the

NPV, such as: to increase the discount rate, to apply sensitivity analysis, to compare

pessimistic and optimistic cash flows or, to estimate the expected cash flows through

scenario planning and the probability distribution (Gaspars-Wieloch, 2019).

3.2.3. Real Options Analysis (ROA)

When there is considerable uncertainty related to the project cash flows, and

contingent decisions are involved, traditional tools don’t include the flexibility to

change the course of the project and its possible outcome (Kodukula and Papudesu,

2006). ROA addresses the issue of choices a manager may have throughout the life of

the project and how those choices can enhance the value of a project (Arnold, 2014).

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ROA is a complement to traditional methods as the DCF method, which seeks to

analyze different possible choices for an investment project to give flexibility to the

project, unlike conventional valuation methods. A real option is a right, but not an

obligation, to undertake business initiatives that are connected to and exist on real

assets or within real assets (Trigeorgis, 1993).

ROA adds value to an economic analysis like the DCF method by considering different

options such as wait to invest, abandon an investment, or expand a business. Then,

more opportunities and flexibility are available when a project is surrounded by

considerable uncertainty.

ROA can be applied using different methods such as Black & Scholes Equation,

Decision trees or binomial trees, Datar-Mathews model, which uses cash flow

scenarios combined with Monte Carlo simulation, and Fuzzy Pay-off Method (Collan,

2011).

3.2.4. Sensitivity Analysis

As a complement to the DCF method, sensitivity analysis (SA) can be performed on

the NPV to explore the sensitivity of key input parameters. Sensitivity analysis is the

study of how the uncertainty in the inputs of a mathematical model or system can be

distributed into different sources of uncertainty in its inputs. Alongside sensitivity

analysis, uncertainty analysis is usually performed. Uncertainty analysis assesses the

uncertainty in model outputs that derives from the uncertainty in the inputs. Methods

to perform SA include simulation and scenario techniques. Global sensitivity analysis

methods consider the changes in model outputs as input factors change all together

over specified ranges. These methods have the ability to manage non-linear and non-

additive responses and to observe relationships between multiple factors.

Monte Carlo Simulation is a method that consists of the simulation of thousands of

possible project scenarios, calculation of the NPV for each scenario using the DFC

method, and analyzing the probability distribution of the NPV results (Kodukula and

Papudesu, 2006).

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4. Publications and Results Reviews An overview of the publications is included in chapter 4, which includes the

objectives, findings, and contributions of each publication of this doctoral dissertation.

The overall purpose of the dissertation is to…

4.1. Publication I: Design of desalinated water distribution networks:

Complex topography, energy production, and parallel pipelines

4.1.1. Research Objective

The objective of this publication is to provide a methodology to design the water

distribution network (WDN) and reverse osmosis (RO) plants to supply mining

companies with desalinated water, the mathematical model considers the following

elements to design the WDN: energy recovery devices, parallel pipelines, and complex

topography. Energy recovery devices considered in the model are PATs for producing

energy in the network using hydropower principles. Parallel pipelines are considered

when the water requirement is large and cannot be supplied with one pipeline. In this

study complex topography means

4.1.2. Contributions

PATs are often used in urban water distribution networks to reduce pressure, and

there are some applications to produce energy. The main contribution of this study is

proposing the use of energy recovery devices in areas with the mining industry where

they are yet not used. These devices can be used in areas with complex topography,

meaning isolated areas and presents changes in elevation as the pipelines go from the

seashore to the mining site. Mining sites are usually located in areas suffering from

water scarcity; thus, the use of desalinated water is a must.

A methodology to simultaneously design the WDN to supply several mining sites

located in an area with complex topography, additionally to find the location and sizes

of desalination plants, pipelines, pump stations, and energy recovery devices, was

addressed. A case study based on an area in northern Chile was used to validate the

model. A superstructure was used to represent the WDN, which includes RO plants,

pipelines, pump stations, and energy recovery devices. The objective of the model is

to minimize the total annual cost by finding the optimal WDN.

Results show the use of PATs in a region with complex topography is indeed feasible

for producing energy in the WDN in areas like the Coastal Cordillera, where larger

elevations in altitude are often avoided by mining companies. The use of parallel

pipelines is a feasible option to supply with desalinated water to several mining sites,

instead of having their own RO plant and own pipeline system for each mining site.

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4.2. Publication II: Towards mine tailings valorization: Recovery of critical

materials from Chilean mine tailings

4.2.1. Research Objective

This study aims to conduct a technical and economic assessment of the valorization of

mine tailings of Chile as a source of critical materials. In recent years, the use of

secondary sources, such as mining waste and electrical waste, has gained importance.

This research adds knowledge to that field of study by adding a novel techno-

economic assessment for producing critical materials by re-processing mine tailings.

4.2.2. Contributions

Results show that mine tailings facilities of the copper industry in Chile store valuable

elements such as critical materials. Therefore, the evaluation of geochemical content

alongside the identification of suitable technologies, and an economic analysis will

help to find alternative sources of critical materials, as is the case of re-processing mine

tailings with such purpose.

The DCF method is a method widely used in economic assessment but is not a decisive

metric for a final decision on real investment. To ensure the robustness of the

assessment, a sensitivity analysis was performed on the results of the NPV, by

analyzing the effect of the market prices of critical materials, capital, and operating

costs on the options assessed for producing critical materials. The options analyzed

were producing rare earths concentrate or producing vanadium pentoxide. Results

show that under certain conditions the production of vanadium pentoxide is feasible.

The main contribution of this study is to show the economic potential of Chilean mine

tailings by performing a techno-economic assessment of the valorization of tailings.

4.3. Publication III: Feasibility of re-processing mine tailings to obtain critical

materials using real options analysis (submitted in Sustainable

Development)

4.3.1. Research objective

This study aims to propose a framework to assess the feasibility of re-processing mine

tailings to obtain critical materials, considering flexibility aspects, such as waiting for

investment in the case of a negative outcome in the present.

The NPV estimated with the DCF is used as a starting point; then, with ROA, different

outcomes for an investment project are assessed. ROA is applied using binomial tree

analysis. The binomial tree is built by using the method of risk-neutral probabilities.

For re-processing mine tailings, technology development and business models are still

needed. To study the influence of several variables on the NPV outcome, Monte Carlo

simulation is applied to perform sensitivity and uncertainty analyses.

The framework developed in this study is applied to a case study based on active mine

tailings located in the Antofagasta Region in Northern Chile. This region features

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several mining projects based on copper resources, leaving tremendous volumes of

mine tailings that are stored without any economic purpose.

4.3.2. Contributions

The novelty of this study is to consider ROA and sensitivity analysis to provide

flexibility to the economic assessment of re-processing mine tailings, acknowledging

the uncertainties involved. Traditional valuation tools such as the DCF method are

statistic methods that do not consider the uncertainty of the variables used to estimate

the profitability of an investment.

ROA gives additional value, so decision-makers can explore alternatives while

waiting to uncertainty to clear off to invest, to re-estimate the project payoff, or they

can decide to abandon a project.

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5. Conclusions Reducing primary ore extraction and reducing waste are part of the strategies that the

mining industry needs to apply for implementing sustainable manufacturing.

Reducing approaches in every manufacturing and processing industry is the core of

the circular economy. Re-processing mine tailings will reduce the amount of waste

that a mining plant left behind, and it will reduce the need for primary mining ores.

Another challenge for the mining industry is to reduce and optimize the demand for

freshwater, especially in arid zones where water is a scarce resource. The purpose of

this thesis is to develop methodologies to improve water and mine tailings

management in mining processes.

The conclusions, related to the research questions, are presented below:

RQ 1.1. Is an integrated water supply system that includes energy recovery devices a

feasible option in areas with complex topography?

A methodology was developed to simultaneously design a water distribution network

to supply mining plants located in an area with complex topography with desalinated

water, as well as the location and size of desalination plants, pipelines, pump stations,

and PATs stations. The methodology was validated with a case study that

corresponds to a geographic area located in the Antofagasta region, which includes

four mining plants (Araya et al., 2018). This area features several changes in altitude,

as is located in the Atacama Desert, which is cross by the Coastal Cordillera.

The optimal solution resulted in a WDN that considers one desalination plant to

supply the four mining plants, as well as PATs located in locations with altitude.

Additionally, the optimal solution included the use of parallel pipelines. A ranking of

solutions was presented, which showed that an integrated system prevails to the

traditional water supply system, which consists of a desalination plant and a set of

pumping stations and pipelines to each mining plant (Araya et al., 2018).

RQ 1.2. Is it economically and technically feasible to use energy recovery devices in the

water supply system?

The use of energy recovery devices, in this case, PATs is feasible in the presence of a

great difference in altitude between two nodes. Having an integrated system to supply

desalinated water to several mining plants reduces the costs of the water supply

system and enhances the industrial symbiosis between different companies.

Moreover, the use of PATs can reduce the costs by producing energy, which can be

used in the water distribution network (Araya et al., 2018, 2017).

The difference of altitude between two nodes, in which the option of using PATS was

considered, was varied to understand in which situations PATs are a feasible option,

from both technical and economic aspects. This analysis showed that there is a

difference in altitude where the option of PATs is no technically possible(Araya et al.,

2018).

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RQ 1.3. When using parallel pipes is a feasible option in the water supply system?

Parallel pipes are needed when the water flow is larger than the maximum water flow

allowed in industrial pipelines, so in the case of an integrated water supply system

using parallel pipes is a feasible option to supply water to several mining companies.

The optimal solution features parallel pipes, as a set of three pipes and two pipes.

Furthermore, the three first solutions include parallel pipes, demonstrating that

parallel pipes are needed when having to supply several mines (Araya et al., 2018).

RQ 2.1. What critical materials can be recovered from mine tailings?

Mine tailings contain several elements, including some critical materials. A

methodology to assess the valorization of mine tailings was developed, with the focus

on the recovery of critical materials. The methodology was validated with a case study

that corresponds to inactive mine tailings deposits located in the Antofagasta region

(Araya et al., 2020). Mine tailings of copper mining in Chile contains several critical

materials, including rare earths, vanadium, cobalt, and scandium. A ranking of critical

materials that could be extracted from mine tailings was presented, the critical

materials were evaluated according to the quantity present in tailings deposits and

the price of the critical material. This analysis showed that rare earths, cobalt,

scandium, and vanadium could be extracted from inactive mine tailings in the

Antofagasta Region, due to their price and quantity (Araya et al., 2020).

RQ 2.2. What are the challenges in the production of critical materials using mine tailings

as a source?

Emerging technologies for recovering critical materials from mine tailings were

reviewed, showing that Technology development is still much needed to make the

recovery of critical materials from mine tailings at an industrial scale. At this time,

most of the research is still in the laboratory and pilot-scale (Araya et al., 2020). Further

research should address new strategies to anticipate the future use of material beyond

the closing of a mine (Lèbre et al., 2017).

RQ 2.3. Is it economically feasible to invest in a project developed around the idea of re-

processing mine tailings to obtain critical materials?

The economic assessment developed to assess the production of critical materials from

mine tailings showed that, in certain conditions, the recovery of critical materials is

feasible. DCF method was used to calculate the NPV of two projects, one based on the

production of rare earths concentrate and another one based on the production of

vanadium pentoxide. Results showed that a project based on the recovery of

vanadium pentoxide is feasible (Araya et al., 2020).

Alongside the DCF method, a sensitivity analysis was performed on the inputs of

NPV, to understand which variables have a more significant effect on the NPV. The

inputs variables studied were capital expenditures, operational expenditures, price of

the critical material, and discount rate (Araya et al., 2020).

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RQ 3.1. How can real options improve the decision to invest in a project using mine tailings

as a source of critical materials?

A project based on the recovery of critical materials from mine tailings can have great

uncertainty in their inputs. ROA complements traditional valuation methods such as

the DCF, by including other options for investment. ROA provides flexibility to a

project based on the re-processing of mine tailings, acknowledging the uncertainties

involved.

RQ 3.2. How can the net present value variables influence real options performance?

The inputs of the NPV can have uncertainties that affect the outcome. Using the NPV

as a decisive metric for investments can lead to errors in the decision-making process.

The NPV is used as a starting point to ROA since it is a complement to traditional tools

rather than a method by itself.

5.1.Theoretical Contribution of the Study

This thesis contributes with a collection of methodologies to assess water management

and mine tailings management in mining. The mining industry is facing many

challenges as industries need to fulfill sustainable development goals to achieve a

circular economy.

The first contribution of this thesis is to provide a methodology to design integrated

water supply systems to provide desalinated water to several mining plants. The

novel contribution of this methodology is to include the option of placing energy

recovery devices in locations where the difference of altitude can be advantageous to

produce energy as it is done in hydropower plants. Additionally, the methodology

includes parallel pipes to fulfill the demand of several mine plants at the same time.

The other contributions of the thesis are embedded in the field of mine tailings

management. These contributions are a methodology to assess the feasibility of re-

processing mine tailings to obtain critical materials and a methodology to assess the

feasibility of re-processing mine tailings with a real options approach. The novelty of

theses methodologies is to assess the feasibility of projects based on the idea of

obtaining critical materials from a secondary source such as mine tailings.

5.2.Limitation and Future Research Suggestions

A limitation of this study is the difficulty to find data about technologies suitable for

recovering critical materials from mine tailings. Data about capital expenses,

operational expenses, and prices are not easy to find.

Another limitation is that all the methodologies presented in this thesis are validated

with case studies of the copper mining industry in the Antofagasta Region. These

methodologies could be applied to other case studies, but some considerations and

changes should be made.

Future research suggestions will be focused on implementing the circular economy in

mining processes with a focus on mine tailings management. Mine tailings are the

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biggest sink of water of the mineral processing, so efforts should be made to create a

framework that integrates water management for mine tailings with the re-processing

of mine tailings. Future studies should also incorporate an environmental assessment

of projects based on the re-processing of mine tailings.

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References

Adiansyah, J.S., Haque, N., Rosano, M., Biswas, W., 2017. Application of a life cycle assessment to compare environmental performance in coal mine tailings management. J. Environ. Manage. 199, 181–191. https://doi.org/10.1016/j.jenvman.2017.05.050

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Gorman, M.R., Dzombak, D.A., 2018. A review of sustainable mining and resource management: Transitioning from the life cycle of the mine to the life cycle of the mineral. Resour. Conserv. Recycl. 137, 281–291. https://doi.org/10.1016/j.resconrec.2018.06.001

Gunson, A.J., Klein, B., Veiga, M., Dunbar, S., 2012. Reducing mine water requirements. J. Clean. Prod. 21, 71–82. https://doi.org/10.1016/j.jclepro.2011.08.020

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Lèbre, É., Corder, G., Golev, A., 2017. The Role of the Mining Industry in a Circular Economy: A Framework for Resource Management at the Mine Site Level. J. Ind. Ecol. 21, 662–672. https://doi.org/10.1111/jiec.12596

Lin, M.H., Carlsson, J.G., Ge, D., Shi, J., Tsai, J.F., 2013. A review of piecewise linearization methods. Math. Probl. Eng. 2013. https://doi.org/10.1155/2013/101376

Lira-Barragán, L.F., Ponce-Ortega, J.M., Guillén-Gosálbez, G., El-Halwagi, M.M., 2016. Optimal Water Management under Uncertainty for Shale Gas Production. Ind. Eng. Chem. Res. 55, 1322–1335. https://doi.org/10.1021/acs.iecr.5b02748

Liu, S., Konstantopoulou, F., Gikas, P., Papageorgiou, L.G., 2011. A mixed integer optimisation approach for integrated water resources management. Comput. Chem. Eng. 35, 858–875. https://doi.org/10.1016/j.compchemeng.2011.01.032

Lottermoser, B.G., 2011. Recycling, reuse and rehabilitation of mine wastes. Elements 7, 405–410. https://doi.org/10.2113/gselements.7.6.405

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Moodley, I., Sheridan, C.M., Kappelmeyer, U., Akcil, A., 2017. Environmentally sustainable acid mine drainage remediation: Research developments with a focus on waste/by-products. Miner. Eng. 126, 1–14. https://doi.org/10.1016/j.mineng.2017.08.008

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SECTION II: PUBLICATIONS

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PUBLICATION I

Araya, N., Lucay, F.A., Cisternas, L.A., Gálvez, E.D.

Design of Desalinated Water Distribution Networks: Complex Topography, Energy

Production, and Parallel Pipelines.

Industrial & Engineering Chemical Research

https://doi.org/10.1021/acs.iecr.7b05247

Vol 57 (30), 9879-9888, 2018

Reprinted with the permission of Industrial & Engineering Chemical Research, Copyright ©

2018, American Chemical Society

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Design of Desalinated Water Distribution Networks: ComplexTopography, Energy Production, and Parallel PipelinesNatalia Araya,† Freddy A. Lucay,† Luis A. Cisternas,† and Edelmira D. Galvez*,‡

†Depto. de Ing. Química y Procesos de Minerales, Universidad de Antofagasta, Antofagasta, Chile‡Depto. de Ing. Metalurgia y Minas, Universidad Catolica del Norte, Antofagasta, Chile

ABSTRACT: A methodology was developed to determinate thelocation and size of desalination plants, the water distributionnetwork, and the location and size of energy recovery devices toprovide desalinated water in regions with complex topography. Thenovelty of this methodology is that energy recovery devices such aspumps as turbines are incorporated to produce energy. Anothernovelty is the consideration of using multiple pipelines. Themethodology proposed uses a superstructure with a set ofalternatives in which the optimal solution is found. A mathematicalmodel is generated that corresponds to a mixed integer nonlinearprogramming (MINLP) problem, which is linearized to become amixed integer linear programming (MILP) problem solved usingthe CPLEX solver in GAMS. A case study is presented todemonstrate the applicability of the methodology to real sizeproblems.

1. INTRODUCTION

Water and energy are vital elements to the well being ofsociety. At a basic level, electricity generation requires water,and water treatment and transport require electricity. World-wide energy consumption destined for water supply represents7% of global energy consumption.1 Hamiche et al.2 reviewedthe nexus between water and energy comprehensively andpresented a classification system; their work suggested that thisnexus should be explored widely.Nowadays, fresh water sources are scarce, and nontraditional

water sources are utilized more every day to fulfill theincreasing demand for both human and industrial consump-tion. The advance in desalination processes, reduction ofmembrane cost, and lower energy consumption have madeseawater a viable source of freshwater.3

Reverse osmosis (RO) is a feasible option to provide waterfor isolated and desert areas where there is access to seawater.RO is the desalination process most utilized worldwide; morethan 50% of desalination plants correspond to RO plants dueto its simplicity and because its energy requirements are minorwhen compared to distillation-based thermal processes.4

The transport of desalinated water in areas with complextopology, e.g., areas with mountains, is a major challenge forseveral reasons. On the one hand, the transport costs due tothe elevations are significant, which can be several times thecost of desalting, and on the other hand, finding only upwarddistribution systems is difficult. An example corresponds to thenorth of Chile (Antofagasta Region) where there are severalmining plants located at high altitude in a desert area. Fromthis area, Chile produces more than half of the Chilean copper

production (35% of the world’s copper production) and othermetallic elements like silver, gold, and molybdenum andnonmetallic minerals like potassium nitrate, lithium carbonate,and boron. The Antofagasta Region is located in the AtacamaDesert, the driest nonpolar desert of the world, and water isneeded to process these ore resources. Water is a limitedresource due to the overexploitation of groundwater sources.On the other hand, the Antofagasta Region has a large seacoast; therefore, seawater has become the main source of freshwater for the mining industry and urban populations.The mines are often located far from the coast and, more

importantly, at high altitudes. These changes in elevation arethe result of the presence in the coast of the Coastal Cordillera,which is a mountain range, and the presence of the AndesMountains. Mine elevations vary between 1000 and 4000 mabove sea level. In the region, there are several mining plantsalready using desalinated water obtained through RO. Eachmining company has a desalination plant with a waterdistribution network (WDN) to provide fresh water for itsprocesses without any integration between companies. Theneed to develop a more efficient desalination and WDNsystem, for example, through the integration of several WDNs,motivates this work.

Special Issue: 2017 European Symposium on Computer-AidedProcess Engineering

Received: December 22, 2017Revised: June 5, 2018Accepted: June 7, 2018Published: June 7, 2018

Article

pubs.acs.org/IECRCite This: Ind. Eng. Chem. Res. XXXX, XXX, XXX−XXX

© XXXX American Chemical Society A DOI: 10.1021/acs.iecr.7b05247Ind. Eng. Chem. Res. XXXX, XXX, XXX−XXX

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There have been several works regarding the design of ROplants and water supply systems. The methodologies to designwater supplies systems usually result in mixed integer nonlinearproblem (MINLP) models. Amit and Ramachandran5 realizeda review of the current status of optimization models fordesigning water distribution networks and presented recom-mendations for future research; Coehlo and Andrade-Campos1

provided a review about methods to achieve water supplysystem efficiency, which also included design optimization.Khor et al.6 provided state of the art water networks synthesisfocusing on a single site and continuous process problems,where major modeling and computational challenges werediscussed exploring issues such as nonconvexity and non-linearity.El-Halwagi7 introduced the novel notion of synthesizing RO

networks applied to waste reduction. The synthesis wasformulated as MINLP, and the objective of this work was tominimize the total annualized cost of RO networks. Since then,considerable research has been made regarding the design ofRO plants and water distribution systems.Liu et al.8 considered using desalinated water, wastewater,

and reclaimed water to supply water deficient areas using amixed integer linear programming (MILP) model taking intoaccount geographical aspects of the region; however, this workdid not consider using energy production. Ahmetovic andGrossman9 proposed a general superstructure and a model tooptimize integrated process water networks using MINLP andNLP models, considering multiple sources of water anddifferent qualities of water; the methodology was applied indifferent case studies. Atilhan et al.10 proposed a novelapproach for the design of desalination and water distributionnetworks considering first a source-interception sink repre-sentation; then, an optimization problem was formulatedresulting in a NLP problem whose objective was to meet therequirements for the sinks at the minimum cost while satisfyingconstraints for the sinks. The methodology was applied to acase study. Lira-Barragan et al.11 proposed that mathematicalprogramming models for synthetizing WDN associated withshale gas production take into account uncertainties, and theproposed superstructure for water integration allows themanagement of fresh water consumption and wastewaterstreams. Liang et al.12 proposed a convex model, whichcorresponded to a MINLP problem, to obtain the optimaldesign of water distribution systems using the Hanoi network,which is a known problem of the looped water distributionnetwork as a case study.13 Gonzalez-Bravo et al.14 proposed amultiobjective optimization approach for synthesizing waterdistribution networks considering domestic, agricultural, andindustrial users involving dual purpose plants consideringenvironmental, economic, and social aspects. Gonzalez-Bravoet al.15 presented an approach to design water and energydistribution networks based on a multistakeholder environ-ment where a multiobjective model considering economic,environmental, and social impacts was applied in a stressedscheme, and the proposed method identified the optimalsolution to minimize the dissatisfaction level of the involvedstakeholders.The WDN including RO selection in complex topography

has not been studied in depth. Herrera et al.16 developed amodel to design water distribution networks considering ROplants to supply mining plants located in high areas that areisolated and arid, up to 4000 m above sea level. They used asuperstructure to design the whole system using a MINLP

model. The methodology was demonstrated with a case study,and its application was adaptable to similar problems.However, they did not consider WDN design including siteswith changes in the elevations resulting from the presence ofmountains.The use of pumps as turbines (PATs) can be an option of

producing energy in the network that can be used to supplyenergy for water pumping. Pumps operating as turbines can beused in water distribution systems to reduce pressure instead ofusing pressure reducing valves. Additionally, they can produceelectricity.17

There are some reviews on energy efficiency in water supplysystems that include hydropower generation and PATsimplementation. Vilanova and Balestieri18 presented modelsof hydropower recovery in water supply systems that could beapplied in a water distribution network design. Zakkour et al.19

reviewed some emerging technologies and practices forsustainable water utility. McNabola et al.20 presented a reviewof energy use in the water industry and opportunities formicrohydropower (MHP) energy recovery.Vilanova and Balestieri21 evaluated the possibilities and

benefits of recovering and producing energy in water supplysystems. They illustrate technical, economic, and environ-mental aspects of hydropower recovery in water supply systemsusing a case study. Corcoran et al.22 developed a methodologyto find the optimal location of turbines in a water distributionnetwork using a MINLP approach and an evolutionaryapproach as a comparison. Tricarico et al.17 presented amethodology to implement PATs combined with pumpscheduling to recover energy and pressure water regime in awater distribution network, showing clear economic benefits.De Marchis et al.23 analyzed the application of PATs in a waterdistribution network using a hydrodynamic model. The modelwas demonstrated to correctly represent the impact of energyrecovery on water supply distribution. Carravetta et al.24

presented the implementation of microhydroelectric plantswhich included PATs in urban water networks. The project ofa small hydroelectric plant was performed at the inlet node of areal network. The case study showed that the installation ofsmall hydroelectric plants could provide interesting economicbenefits for the manager of pipe networks in urban areas. Noneof the works reviewed analyzed the implementation of PATs ina WDN on a larger scale; furthermore, none consideredproducing energy like that in the hydropower industry fromthe downfall of water in a WDN that included RO plants andindustrial sites with a large requirement of water.Parallel pipelines are arranged to divide flow and to keep the

head loss at the same rate, meaning that head loss in all parallelpipes remains the same.25 The reliability of a water distributionnetwork can be improved by adding a parallel pipe to anexisting one.26 In actual industrial operations, more than onepipeline is often utilized to provide higher flows, mainly inmining operations which require a great amount of water intheir operations, so one pipeline cannot satisfy the waterrequirements. Parallel pipes must be included in the WDNdesign.The objective of this work is to provide a methodology to

design the WDN and selection of RO plants to supplyindustrial plants with desalinated water. The developed modelfor this methodology considers using energy recovery devicessuch as pumps as turbines for energy production in thenetwork in places where there is a considerable difference ofheight that allows producing energy like in the hydropower

Industrial & Engineering Chemistry Research Article

DOI: 10.1021/acs.iecr.7b05247Ind. Eng. Chem. Res. XXXX, XXX, XXX−XXX

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industry. Another novelty of the work is to considerer morethan one pipeline in cases where flows are high.Pumps as turbines are usually used in urban water

distribution networks to reduce pressure, and there are someapplications of energy production. The novelty of this workrelies in proposing the use of energy recovery devices in areaswhere they are usually not used, meaning areas that have acomplex topography that are also isolated and suffering fromwater scarcity, so the only source of fresh water is desalinatedwater.

2. PROBLEM STATEMENTIndustrial sites such as mining plants are water consumers thatare located far away from the coast, in areas with a complextopography; by complex, this refers to an area with changes inelevation between the RO plants and water consumers. Waterdemand of industrial sites can only be satisfied with desalinatedwater from RO plants located along the coast; no other optionwas taken into account as the industrial sites are located inisolated areas, which means that water is a scarce resource. Themethodology used by Herrera et al.16,27 was used as a referencein this work.A superstructure was used to represent the WDN, which

included RO plants; pipelines; nodes with pump stations,pumps as turbines, or just a junction; and industrial sites. Somenodes of the WDN are located in mountains where there is apronounced altitude, so pipelines have to ascend and thendescend, so the downfall of water is used to produce energywith the passage of water through a pumping station withpumps as turbines (PATs) like in Figure 1. The possibility of

producing energy with water passing through the downstreamwas evaluated and compared to water ascending through theWDN until reaching industrial sites in the traditional way ofavoiding the descend of water.Another consideration in the superstructure is to use more

than one pipeline until three pipelines are allowed; the choicebetween using one, two, or three pipelines depends mainly onthe requirements of water of each consumer’s site. There is amaximum velocity allowed in a pipeline, which is used as arestriction in the model. The diameters of the pipelines aredetermined by the model by choosing between a set of discretediameters that are commercial sizes.The objective of the model was to minimize total annual

cost and find the locations and sizes of RO plants, locationsand sizes of pumping stations, locations of PATs, pipediameters, operational conditions of pumping stations, andnumber of pipelines in the WDN in order to providedesalinated water to industrial sites.

3. MATHEMATICAL FORMULATIONFour sets were used to represent the superstructure: RO plantsSO = {so| so is an RO plant}; nodes which can be pumpingstations, pumping stations working as turbines, or just ajunction without a pumping stations, so N = {n|, n is a node};industrial sites or water consumers SI = {si|, si is industrialsite}; and the set of diameters D = {d|, d is a diameter}.Distances and elevations of each point were designated basedon the topography data obtained using Google Earth, anddistances were defined as Li,j and elevations as ΔZi,j.Water flow is only in one direction, from RO plants located

along the shore to the user that are industrial sites, which areusually mining plants. Bidirectional flow makes no sense giventhe high costs of transporting water from a low altitude to ahigh altitude location. Only feasible connections betweennodes were considered in the WDN.Known parameters are the water requirements of industrial

sites, according to the needs of its facilities, water capacities ofRO plants, altitude of each node, and distances between eachnode.The model has equations of continuity for RO plants, nodes,

and mining plants; these equations are presented as eqs 1−3

∑* = ∀ ∈∈

Q Q so SOson N

so n,(1)

∑ ∑= ∀ ∈∈ ∈

Q Q n Ni input

i nj output

n j, ,(2)

∑* = ∀ ∈∈

Q Q si SIsin N

n si,(3)

where Qi,j is the volumetric flow pumped from i to j;constraints associated with the maximum production capacityof RO plants and desalinated water demands of the miningplants were also included in the model.

3.1. Pipe Diameter. For selecting the pipe diameter frompoints i to j, a disjunction expressed using the Convex Hullmethod28,29 was used (eq 4).

∨=

∀ ∈∈

Ä

Ç

ÅÅÅÅÅÅÅÅÅÅÅ

É

Ö

ÑÑÑÑÑÑÑÑÑÑÑ

y

D Di j FIJ( , )

d D

i j d

i j d

, ,

, (4)

The friction factor is assumed to be a function of the pipediameter and the roughness. The Reynolds number isconsidered big enough to not represent a contribution to thefriction factor.30 A set of discrete values were considered tochoose diameter. The values used for the diameter were 0.7,0.8, 0.9, 1, and 1.1 m.

3.2. Objective Function. The objective function mini-mizes the total annualized cost of desalination plants, pipes,pumping stations, and pumps as turbines required to supplyindustrial sites located in a geography with complex top-ography. This function includes four terms that are costs: (1)cost of producing desalinated water, (2) costs of pumpingstations, (3) costs of pumps as turbines stations, and (4) costsof pipelines. The fifth term is the valorization of energyproduced by PATs that can be used in the grid.

∑ ∑ ∑ ∑

= + + +

∈ ∈ ∈ ∈

TC C C C C

E

so SOSO

i j FI Ji j

n Nn

n NPAT

n NPATs

, ,,

(5)

Figure 1. Mountain scheme: Point A represents a node with a pumpstation. Point B represents a node that is only a junction betweenpipes. Point C represents a PATs station and a traditional pumpstation.

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The cost of producing desalinated water was extracted fromthe database cost raised by Wittholz et al.31 The function usedincluded UPC, which is the unit cost of producing desalinatedwater.

∨ = × × *

≤ * ≤

∀ ∈∈

Ä

Ç

ÅÅÅÅÅÅÅÅÅÅÅÅÅÅÅÅÅÅÅ

É

Ö

ÑÑÑÑÑÑÑÑÑÑÑÑÑÑÑÑÑÑÑ

y

C PA UPC Q

Q Q Q

so SOc C

so c

so so c so

cLO

so cUP

,

,

(6)

The cost of water transport is represented by a functionproposed by Swamee;25 this function includes two functions:annualized capital cost of pipelines and operational and capitalcost of pumping stations. So, the function that described theannualized capital cost of pipelines proposed by Swamee25 isdescribed below

=+

∀ ∈( )

Ck L D

Pi j FIJ

1( , )i j

PH

H i j i jm

L,

, ,i j

b

,

(7)

where kP is a proportionality constant; Hi,j is the pressure head;Hb is the length parameter; Li,j is the pipe length; Di,j is the pipediameter; and m is the exponent.The function to estimate pumping station costs is

ρη

ρη

=+

+ ×

× ∀ ∈∈

ikjjjjj

y{zzzzzC

k s gP

F F E g

Q H n N

(1 ) 8.76n

N b

L

D A C

j outputn j n j, ,

(8)

where kN is a proportionality constant; sb is the standbyfraction; ρ is the mass density of water; g is the gravitationalacceleration; η is the combined efficiency of pump and primemover; FD is the daily averaging factor; FA is the annualaveraging factor; EC is the unit electrical cost ($/kW h); and PLis the plant life years.The function includes the pumping head Hn,j, which is

calculated with the Darcy−Weisbach equation, which is

π= + Δ +H H z

fL Q

gD

8n j n j

n j n j

n j, 0 ,

, ,2

2,

5(9)

where Δzn,j is the elevation difference from n to j; H0 is theterminal head; f is the friction factor; and Ln,j is the length ofthe pipe from n to j.3.3. Pumps as Turbines (PATs) for Energy Production.

For pumps as turbines stations, the net head for producingenergy was also calculated with the Darcy−Weisbach equationextracted from ref 32. In turbines, the net head is the actualhead used to produce energy. Net head is the gross head whichis the difference in height between two points minus the headloss. So, in the case of pumps as turbines, the head loss wouldhave a minus sign in the Darcy−Weisbach equation. Thevalorization of the energy produced in a year by PATs iscalculated using the next equation:

∑ ρ η=ikjjjjj

y{zzzzzE g Q H t E

USDyearPATs

n

N

n n C

PATS

(10)

where NPATS is the number of PATs; Qn,k is the hourly flowthrough the nth PATs (m3/s); Hn,k is the net head (m) acrossthe same PATs at the same time; η is the efficiency; t is

operating hours in a year (h); and EC is the electricity cost($/kW h).33

To obtain the cost of pumps as turbines CPAT, the price ofthese devices was estimated using catalogs from the pumpscompany’s using the net head and the flow as a reference. Civilwork and maintenance work of PATs was estimated usingvalues from ref 33.

3.4. Parallel Pipelines. In order to distribute thedesalinated water flow, the superstructure has the option ofchoosing up to three parallel pipelines depending on the waterflow. The velocity of water has a maximum value of 1.5 m/s;34

this condition is fulfilled using the next equation

π≤Q v

D

4n j n ji j

, ,,

2

(11)

The diameter of pipelines is the same for all pipelines ifmore than one is chosen. So, the next conditions must befulfilled

∑= ∀ ∈=

Q Q n Nn jp

n jp

,1

3

,(12)

= = =H H H Hn j n j n j n j, ,1

,2

,3

(13)

The total water flow is the sum of the water flow of eachpipeline where p is the pipeline, and the head drop is the samefor every pipeline and corresponds to the total head drop.

3.5. Piecewise Linearization. The objective function isnot linear because UPC and Q3 are not linear, Q3 appears whenthe Darcy−Weisbach equation is multiplied for the water flow,soQ2 is multiplied for Q. Since the objective function is notlinear, the model is a MINLP model.UPC is the amortized capital cost and the operating cost of

obtaining desalinated water and is included in the cost ofproducing desalinated water; this cost is a compound of thenext form

= × ×C Q UPC cte2SO SO (14)

where QSO is the desalinated water flow, and cte2 is a constantwhich includes desalination plant availability and time andmoney conversions to obtain the requirements units.To obtain the global optimum in short time, UPC and Q3

were linearized using a piecewise methodology extracted fromLin et al.35 Piecewise methodologies allowed us to convert anonlinear programming problem into a linear programmingproblem or a mixed-integer convex programming problem forobtaining an approximated global optimal solution.

4. CASE STUDYAn area of the Antofagasta region was used as a case study; thisarea is mainly desert and isolated and features significantchanges in elevation due to the presence of the CoastalCordillera that crosses this area. The case study contained fourmining plants that can be supplied water by three potential ROplants. Between the RO plants and the mining plants, there arepotential pumping stations, and since there are mountains inthe area, PATs were considered in some points. Connectionsthat were unfeasible were not considered as an option.Locations of RO plants and industrial sites were determined

on assumptions based on actual places where RO plants andmining plants could be located. Pipeline lengths weredetermined based on real data about the water supplies of

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different mining companies. The area was chosen using GoogleEarth; distances between points and elevations weredetermined using this software. Figure 2 shows the chosenarea as a case study.RO plants are located on the coast, so their elevation is zero.

There is a zone where the Coastal Cordillera goes throughabout 40 km of extension; this zone is where the use of PATswas considered and compared to the possibility of avoidingthese mountains and to only go up until reaching the miningsites. Elevation of pumping stations varied from 0 to 2.860 kmabove sea level, and mining plants were located between 3.046and 3.875 km above sea level. The elevation of each node isshown in Table 1, and the distance between each node isshown in Table 2.

5. RESULTSThe model was solved as a MILP problem using the Cplexsolver in a GAMS environment. GAMS stands for GeneralAlgebraic Modeling System; it is a high-level modelingsoftware for mathematical programming and optimization.

GAMS is designed for modeling linear programming (LP),mixed integer linear programming (MILP), and mixed integernonlinear programming (MINLP) problems.36 The Cplexsolver in GAMS is designed to solve large and difficultproblems quickly and works to solve the majority of linearproblems (LP).37

The global optimum was found in a short time aslinearization allows a model to be obtained that can be solvedquickly using Cplex, which is a desirable attribute for complexmodels like this one.

5.1. Global Optimum. The requirements of desalinatedwater of the WDN was 3.2 m3/s in total; the requirements foreach mining plant was 0.8 m3/s. These values were similar tothe requirements of the mining plants in the area.

Figure 2. Superstructure. SO are RO plants with a pumping station; n are pumping stations; P are PATs stations, and Si are industrial sites.

Table 1. Height Above Sea Level of Each Node

NodesHeight above sea level

(km) NodesHeight above sea level

(km)

SO1-n1 0 n12 2.860SO2-n2 0 n13 2.720SO3-n3 0 n14 1.585n4 2.116 n15 1.755n5 1.364 n16 2.453n6 2.231 n17 2.874n7 2.431 Si1 3.485n8 1.753 Si2 3.046n9 1.375 Si3 3.339n10 1.765 Si4 3.875n11 1.382

Table 2. Distances between Each Node

NodesDistance between nodes

(km) NodesDistance between nodes

(km)

n1-n4 40.7 n6-n9 22.5n1-n5 43.9 n7-n8 59.9n2-n4 30.7 n7-n10 47.2n2-n5 75.4 n10-n15 14.3n2-n7 34.8 n8-n12 45.7n2-n8 80.7 n8-n13 40.2n3-n7 63.4 n11-si1 80.7n3-n8 50.4 n11-si2 55.9n4-n5 46.1 n12-si3 53.6n4-n6 22.7 n12-si4 51.5n5-n14 64.9 n13-si3 62.1n13-si4 49.6 n15-si2 54.3n14-si1 55.9 n15-si3 55.0n14-si2 51.2 n15-si4 76.5n14-n16 49.1 n16-si3 37.7n14-n17 67.2 n17-si4 53.7

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The global optimum solution considers using only one ROplant to supply all mining sites; in n9, there were PATs sincethe previous node, n6, is located at a high altitude. In node n9,a PATs station was followed by a traditional pump station. Allpipelines going between n2 and n11 considered using threepipelines to fulfill the water requirements of the three industrialsites (continuous line in Figure 3). Between n2 and n13, therewere two pipes to supply si4. When the requirements of waterof the industrial sites were elevated, parallel pipes that camefrom one single RO plant seemed to be a suitable solution tosupply more than one industrial site instead of using differentRO plants with a single or double pipeline to supply eachindustrial site, which is the conventional way. The optimalsolution generated 168,593 MW-h/year, which considering0.12 USD/kW-h represents a saving of 20.231 million USD/

year. Furthermore, considering that energy is produced fromfossil fuels, this energy production can contribute to reducinggreenhouse gas emissions.A ranking of the first three optimal solutions was made to

compare them economically and operationally (Table 3). Thethree first solutions considered using PATs in the same area;the first two solutions considered only the SO2 RO plant tosupply desalinated water. Instead, the third solution consideredusing desalinated water from SO2 and SO3. Additionally, theWDN of solutions 1 and 2 used seven pumping stations,whereas the WDN of solution 3 used eight pumping stations.The differences in costs between these optimal solutions wereless than one million USD/year. More details are present inTable 3, and solutions 2 and 3 are illustrated in Figures 4 and5, respectively.

Figure 3. Optimal solution. Solid line represents three parallel pipes, and segmented line represents two parallel pipes.

Table 3. Ranking of Solutions

Solution RO plants No. of pumping stations No. of PATs stations Energy generated by PATs (MW-h/year) Total cost (million USD/year)

1 SO2 7 1 168,593 250.712 SO2 7 1 168,593 251.553 SO2-SO3 8 1 168,593 251.78

Figure 4. Solution 2. Solid line represents three pipes, and segmented line represents two pipes.

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Figure 5. Solution 3. Solid line represents three pipes, and segmented line represents two pipes.

Figure 6. Solution found when big changes in altitude are avoided. Solid line represents three pipes, and segmented line represents two pipes.

Figure 7. Traditional water supply system for mining plants.

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By way of comparison, a network was designed withoutconsidering the PATs. For this purpose, the pipes in the areawhere the PATs could be installed were not considered in thesuperstructure. The optimal solution without PATs is shown inFigure 6, which considered the SO1 RO plant and fivepumping stations. The cost was 258.52 million USD/year; thisis 7.81 million USD/year more expensive than the option withPATs. This difference was due to a higher cost in the pipes, areduction in costs for not considering the equipment for PATs,and an increase in energy costs.Another comparison was made to compare the optimal

solution with the water supply strategy currently used bymining companies, where each company had its own RO plantand water distribution network. Since there is no energyproduction, and mining companies usually avoid puttingpipelines in places with pronounced changes in elevations,the pipelines were located where there was not a big differencein altitude. The cost of this system (Figure 7) was 258.56million USD/year.The optimal solution was considered going through n6,

which was 2.231 km above sea level; the next pump stationcoupled to a PATs station was n9, which was 1.375 km abovesea level, so 0.856 km was the difference in height and 22.47km the distance between each point. In order to analyze theeffect of height in the optimal solution, several differences ofheight between n6 and n9 were used. Results are shown inTable 4.The optimal solution generated 168,593 MW-h/year, which

is 20.231 million USD/year that can be utilized in the network.If the height of the mountains was 200 m less high, the optimalsolution still considered energy generation with an importantamount of energy generated, 127,950 MW-h/year.With a height of 1.831 km, the optimal solution considered

two RO plants, SO1 and SO3, which were located at theextremes of the network, instead of choosing SO2 as theoptimal solutions as in the cases of 2.231 and 2.031 km ofheight solutions. Energy production was low in comparisonwith the solutions obtained when elevations were higher; this isdue to the water flow sent to n6 was 0.2 m3/s, which was verylow in comparison to 2.4 m3/s which is the water flow sent ton6 where the elevation was 2.231 km. The reason for such lowwater flow is that the net head was lower as the gross head,which is the actual elevation of the mountains, was lower.Head loss was high due to the distance between each point andwater velocity, so the gross head had to be high to compensatefor the head loss.

6. CONCLUSIONS

A methodology to simultaneously design a WDN to supplyindustrial sites located in regions with complex topography,find the location and sizes of desalination plants, pipelines,pump stations, and PATs stations, was addressed. A case studywas used to validate the model.

Results showed that using PATs in a region with complextopography was feasible for producing energy in the WDN bypassing through a region with changes in elevation like theCoastal Cordillera where big changes in altitude are oftenavoided by mining companies.Linearization of two functions allowed us to find the global

optimum with low computational cost, which is a desiredattribute for complex models.Using parallel pipes is a feasible option to supply several

industrial sites using water from one RO plant when therequirements of water are elevated, instead of having a differentRO plant supply every industrial site with its respectivepipeline.In the future, more elements will be added to the model

such as considering more than one water quality to supplymultiple users and multiple sources of water to broaden thewater offer. Another element that can be included is usingrenewable energies like solar energy.

■ AUTHOR INFORMATIONCorresponding Author*E-mail: [email protected] D. Galvez: 0000-0001-9558-443XNotesThe authors declare no competing financial interest.

■ ACKNOWLEDGMENTSThe financial support from CONICYT (Fondecyt 1171341) isgratefully acknowledged. N.A. thanks CONICYT for thenational Ph.D. scholarship.

■ NOMENCLATURECSO = Annualized cost of RO plants (million USD/year)Ci,j = Annualized cost of pipelines (million USD/year)Cn = Annualized cost of pumping stations (million USD/year)CPAT = Annualized cost of PATs stations (million USD/year)Di,j = Diameter of pipeline between i and j (m)EC = Unit electrical cost ($/(kW-h))EPAT = Valorization of energy generated by PATs in oneyear (million USD/year)f = Friction factor (dimensionless)FA = Annual average factor (dimensionless)FD = Daily average factor (dimensionless)g = Gravitational acceleration (m/s2)Hi,j = Pressure head (m)Hb = Length parameter (m)Hn,j = Pumping head (m)H0 = Terminal head (m)Hn,k = Net head (m)

Table 4. Comparison between Different Heights of Nodes

Q(m3/s)

Height n6(km)

ΔH n6 and n9(km) RO plants

No. of pumpingstations

No. of PATsstations

Total cost(million USD/year)

Energy generated by PATs(MW-h/year)

3.2 2.231 0.856 SO2 7 1 250.71 168,5933.2 2.031 0.656 SO2 7 1 254.67 127,9503.2 1.831 0.456 SO1-SO3 10 1 257.08 76303.2 1.631 0.256 SO1-SO3 10 1 257.95 39313.2 1.431 0.056 SO1 5 0 258.52 0

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kN = Proportionality constant for pumping stations(dimensionless)kP = Proportionality constant for pipelines (dimensionless)Li,j = Pipe length (m)PA = Desalination plant availability (dimensionless)PL = Desalination plant life (years)Qi,j = Volumetric flow pumped from i to j (m3/s)Qi,n = Volumetric flow pumped from i to n (m3/s)Qn,j = Volumetric flow pumped from n to j (m3/s)Qn,si = Volumetric flow pumped from n to an industrial site(m3/s)Qsi = Volumetric flow required in an industrial site (m3/s)Qso = Volumetric flow pumped from RO plant (m3/s)Qso,n = Volumetric flow pumped from a RO plant to n(m3/s)Qn,k = Volumetric flow through PATs (m3/h)sb = Standby fraction (dimensionless)t = Operating hours in a year (h)TC = Total annualized cost (million USD/year)UPC = Unit cost of producing desalinated water (USD)vn,j = Water velocity (m/s)yi,j,d = Disjunction to choose diameterρ = Water density (kg/m3)Δzn,j = Elevation difference from n to j (m)η = Combined efficiency of pump and prime mover

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(13) Fujiwara, O.; Khang, D. B. A Two-Phase DecompositionMethod for Optimal Design of Looped Water Distribution Networks.Water Resour. Res. 1990, 26 (4), 539−549.(14) Gonzalez-Bravo, R.; Napoles-Rivera, F.; Ponce-Ortega, J. M.;El-Halwagi, M. M. Multiobjective Optimization of Dual-PurposePower Plants and Water Distribution Networks. ACS SustainableChem. Eng. 2016, 4 (12), 6852−6866.(15) Gonzalez-Bravo, R.; Fuentes-Cortes, L. F.; Ponce-Ortega, J. M.Defining Priorities in the Design of Power and Water DistributionNetworks. Energy 2017, 137, 1026−1040.(16) Herrera, S.; Cisternas, L. A.; Galvez, E. D. Simultaneous Designof Desalination Plants and Distribution Water Network. Comput.-Aided Chem. Eng. 2015, 37 (June), 1193−1198.(17) Tricarico, C.; Morley, M. S.; Gargano, R.; Kapelan, Z.; DeMarinis, G.; Savic, D.; Granata, F. Integrated Optimal Cost andPressure Management for Water Distribution Systems. Procedia Eng.2014, 70, 1659−1668.(18) Nogueira Vilanova, M. R.; Perrella Balestieri, J. A. Energy andHydraulic Efficiency in Conventional Water Supply Systems.Renewable Sustainable Energy Rev. 2014, 30, 701−714.(19) Zakkour, P. D.; Gaterell, M. R.; Griffin, P.; Gochin, R. J.;Lester, J. N. Developing a Sustainable Energy Strategy for a WaterUtility. Part II: A Review of Potential Technologies and Approaches.J. Environ. Manage. 2002, 66 (2), 115−125.(20) McNabola, A.; Coughlan, P.; Corcoran, L.; Power, C.;Williams, A. P.; Harris, I.; Gallagher, J.; Styles, D. Energy Recoveryin the Water Industry Using Micro-Hydropower: An Opportunity toImprove Sustainability. Water Policy 2014, 16 (1), 168−183.(21) Vilanova, M. R. N.; Balestieri, J. A. P. Hydropower Recovery inWater Supply Systems: Models and Case Study. Energy Convers.Manage. 2014, 84, 414−426.(22) Corcoran, L.; Mcnabola, A.; Coughlan, P. Optimization ofWater Distribution Networks for Combined Hydropower EnergyRecovery and Leakage Reduction. J. Water Resour. Plan. Manage.2016, 142 (2), 04015045.(23) De Marchis, M.; Fontanazza, C. M.; Freni, G.; Messineo, A.;Milici, B.; Napoli, E.; Notaro, V.; Puleo, V.; Scopa, A. EnergyRecovery in Water Distribution Networks. Implementation of Pumpsas Turbine in a Dynamic Numerical Model. Procedia Eng. 2014, 70,439−448.(24) Carravetta, A.; Fecarotta, O.; Sinagra, M.; Tucciarelli, T. Cost-Benefit Analysis for Hydropower Production in Water DistributionNetworks by a Pump as Turbine. J. Water Resour. Plan. Manag. 2014,140 (6), 04014002.(25) Swamee, P. K. Optimal Design of Pumping Mains. J. Transp.Eng. 2001, 127 (3), 264−267.(26) Gupta, R.; Baby, A.; Arya, P. V.; Ormsbee, L. UpgradingReliability of Water Distribution Networks Recognizing ValveLocations. Procedia Eng. 2014, 89, 370−377.(27) Herrera-Leon, S.; Lucay, F.; Kraslawski, A.; Cisternas, L. A.;Galvez, E. D. Optimization Approach to Designing Water SupplySystems in Non-Coastal Areas Suffering from Water Scarcity. WaterResour. Manage. 2018, 32 (7), 2457.(28) Iqbal, K. Fundamental Engineering Optimization Methods;Bookboon.com, 2013; Vol. 53.(29) Hendrix, E. M. T.; G.-Toth, B. Introduction to Nonlinear andGlobal Optimization; Springer, 2010; Vol. 37.(30) Swamee, P. K.; Jain, A. K. Explicit Equations for Pipe FlowProblems. J. Hydraul. Div., Am. Soc. Civ. Eng. 1976, 102, 657−664.(31) Wittholz, M. K.; O’Neill, B. K.; Colby, C. B.; Lewis, D.Estimating the Cost of Desalination Plants Using a Cost Database.Desalination 2008, 229 (1−3), 10−20.(32) Swamee, P. K.; Sharma, A. K. Design of Water Supply PipeNetworks; Wiley, 2008.(33) Fontana, N.; Giugni, M.; Portolano, D. Losses Reduction andEnergy Production in Water-Distribution Networks. J. Water Resour.Plan. Manag. 2012, 138 (3), 237−244.(34) Water Pipeline Design Guidelines; Saskatchewan Environment,April 2004.

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J

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PUBLICATION II

Araya, N., Kraslawski, A., Cisternas, L.A.

Towards mine tailings valorization: Recovery of critical materials from Chilean mine

tailings.

Journal of Cleaner Production

Vol 263, 2020

https://doi.org/10.1016/j.jclepro.2020.121555

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Towards mine tailings valorization: Recovery of critical materials fromChilean mine tailings

Natalia Araya a, b, *, Andrzej Kraslawski b, Luis A. Cisternas a

a Departamento de Ingeniería Química y Procesos de Minerales, Universidad de Antofagasta, Antofagasta, 1240000, Chileb School of Engineering Science, Lappeenranta-Lahti University of Technology (LUT University), Lappeenranta, FI-53851, Finland

a r t i c l e i n f o

Article history:Received 16 June 2019Received in revised form6 March 2020Accepted 5 April 2020Available online 9 April 2020

Handling editor:Yutao Wang

Keywords:Mine tailingsCritical raw materialsTechno-economic assessmentDiscounted cash flowSensitivity analysis

a b s t r a c t

The mining industry produces large volumes of mine tailings e a mix of crushed rocks and process ef-fluents from the processing of mineral ores. Mine tailings are a major environmental issue due to im-plications related to their handling and storage. Depending on the mined ore and the process used, itmay be possible to recover valuable elements from mine tailings, among them critical raw materials(CRMs) like rare earths, vanadium, and antimony.

The aim of this study was to investigate the techno-economic feasibility of producing critical rawmaterials from mine tailings. Data from 477 Chilean tailings facilities were analyzed and used in thetechno-economic assessment of the valorization of mine tailings in the form of CRMs recovery. A reviewof applicable technologies was performed to identify suitable technologies for mine tailings processing.To assess the economic feasibility of CRMs production, net present value (NPV) was calculated using thediscounted cash flow (DCF) method. Sensitivity analysis and design of experiments were performed toanalyze the influence of independent variables on NPV. Two options were assessed, rare earth oxides(REOs) production and vanadium pentoxide (V2O5) production. The results show that it is possible toproduce V2O5 with an NPV of 76 million US$. In the case of REOs, NPV is positive but rather low, whichindicates that the investment is risky. Sensitivity analysis and the ANOVA run using the design of ex-periments indicated that the NPV of REOs is highly sensitive to the price of REOs and to the discount rate.

© 2020 Elsevier Ltd. All rights reserved.

1. Introduction

Mine tailings are waste from the processing of mineral ores.They are a mixture of ground rocks and process effluents generatedduring processing of the ores, and their composition depends onthe nature of the mined rock and the recovery process used. Incopper mining, tailings can account for 95e99% of crushed andground ores (Edraki et al., 2014). Worldwide, mine tailings areproduced at a rate of anywhere from five to fourteen billion tonsper year (Adiansyah et al., 2015; Edraki et al., 2014; Schoenberger,2016).

In view of the volumes of mine waste produced and the natureof the chemicals involved, the storage and handling of mine tailingsis a significant environmental problem. Mine tailings are a source of

serious contamination of soils and groundwater with nearbycommunities particularly badly affected by the results of eolian andwater erosion of tailing disposal sites (Mendez and Maier, 2008).Another cause of environmental pollution frommine tailings is acidmine drainage (AMD) (Larsson et al., 2018; Moodley et al., 2017).AMD is formed from the exposure of sulfide ores and minerals towater and oxygen, once the ore is exposed, sulfate and heavymetals are released into the water (Moodley et al., 2017). AMD isconsidered one of the most significant forms of water pollution andthe USA Environmental Protection Agency (US-EPA) considers it tobe the second only to global warming and ozone depletion in termsof ecological risk (Moodley et al., 2017).

Tailing storage facilities (TSF), also called tailing deposits, are thesource of most mining-related disasters (Schoenberger, 2016). Ap-proaches to the handling and storage of mine tailings includeriverine disposal, wetland retention, backfilling, dry stacking andstorage behind damned impoundments (Kossoff et al., 2014). Minetailings dam failures can have catastrophic consequences. 237 casesof significant tailings accidents were reported for the period 1971 to2009 (Adiansyah et al., 2015). More recently, in January 2019, an

* Corresponding author. School of Engineering Science, LUT University, FI-53851,Lappeenranta, Finland.

E-mail addresses: [email protected] (N. Araya), [email protected] (A. Kraslawski), [email protected] (L.A. Cisternas).

Contents lists available at ScienceDirect

Journal of Cleaner Production

journal homepage: www.elsevier .com/locate/ jc lepro

https://doi.org/10.1016/j.jclepro.2020.1215550959-6526/© 2020 Elsevier Ltd. All rights reserved.

Journal of Cleaner Production 263 (2020) 121555

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accident at the C�orrego do Feij~ao mine in Brumadinho in themetropolitan region of Belo Horizonte in southeastern Brazil killedat least 65 people with about 280 people were missing (De S�a,2019).

To achieve a circular economy model, the valorization of minetailings is crucial for the mining industry, which needs to improveits processes to minimize its environmental impact and close theloops (Kinnunen and Kaksonen, 2019). Different approaches totailings valorization can be taken, such as reprocessing to extractmetals and minerals, tailings as backfill material, tailings as con-struction material, energy recovery and carbon dioxide sequestra-tion (Lottermoser, 2011).

Challenges that the mining industry needs to face to achieve thevalorization of tailings aligned with circular economy principlesinclude improving the rather limited knowledge about mineralogy,impurities concentration, and the quantity of tailings; developingnew business models that take account of price development,lower disposal costs, and market demand; providing institutionalimpulse indispensable to encourage the transformation from alinear to a circular economy; technology development to makeprocesses economically feasible since most mine tailings have lowgrades of different elements mixed with residues of previous pro-cesses (Kinnunen and Kaksonen, 2019; Lottermoser, 2011).

Due to the geological heterogeneity of the rocks mined and thecontinuous flow processes used in mineral processing, tailingsdeposits contain large quantities of valuable elements whose re-covery could bring potential economic benefits. A number ofstudies have investigated the recovery of valuable elements frommine tailings (Ahmadi et al., 2015; Alcalde et al., 2018; Anderssonet al., 2018; Ceniceros-G�omez et al., 2018; Falag�an et al., 2017;Figueiredo et al., 2018; Khalil et al., 2019; Khorasanipour, 2015;Mohamed et al., 2017; Sracek et al., 2010).

As shown by recent studies (Ceniceros-G�omez et al., 2018;Markovaara-Koivisto et al., 2018; Moran-Palacios et al., 2019; Tunsuet al., 2019), among elements contained in mine tailings, there aremany critical raw materials (CRMs). Raw materials have significanteconomic importance and are utilized in the manufacture of a widerange of goods. In particular, critical rawmaterials can be applied inareas such as alternative energy production and communicationsdevices, and they play a significant role in the development ofglobally competitive and eco-friendly innovations. Securing accessto a stable supply of many raw materials has become a majorchallenge for national and regional economies with a limited pro-duction, which relies on imports of numerous minerals and metals(European Commission, 2017a).

Many studies have examined the criticality of raw materials.This study utilizes the list compiled by the European Commission(EC), where raw materials are considered critical when they areboth of high economic importance for the European Union (EU) andvulnerable to supply disruptions (European Commission, 2017b).The term “vulnerable to supply disruption”means that their supplyis associated with a high risk of not meeting the demand of the EUindustry. High economic importancemeans that the rawmaterial isof fundamental importance to industry sectors that create addedvalue and jobs, which may be lost in the case of inadequate supplyand if adequate substitutes cannot be found (Blengini et al., 2017).The most critical metals are those for which supply constraintsresult from the fact that they are largely or entirely mined as by-products, generate environmental impacts during production,have no effective substitutes, and are mined in areas prone togeopolitical conflict (Graedel et al., 2015).

In 2011, the European Commission (EC) published a list of 14 rawmaterials that are critical for emerging technologies of Europeanindustries, so-called critical raw materials (CRMs) (EuropeanCommission, 2017a, 2014, 2011). The list has been updated twice

since 2011, the last update was in 2017, and it currently containstwenty-seven CRMs including 3 element groups: light rare earthelements (LREEs), heavy rare earth elements (HREES) and platinumgroup elements.

According to the International Union for Pure and AppliedChemistry (IUPAC), rare earth elements (REEs) are a group of 17elements that includes lanthanides, composed of 15 elements, andyttrium and scandium, which are included in this group due to thesimilarity in chemical characteristics. REEs can be found in over 250different minerals (Jordens et al., 2013; Sadri et al., 2017). REEs havean important role in the transition to green technologies because oftheir use in crucial components such as permanent magnets andrechargeable batteries, and their use as catalysts (Binnemans et al.,2013a). China is responsible for almost 80% of the global supply ofREEs, such monopoly has raised concerns about a possible shortageof supply, (Hornby and Sanderson, 2019; Vekasi and Hunnewell,2019).

Other elements on the list of CRMs are platinum group elements(PGEs), which include ruthenium (Ru), rhodium (Rh), palladium(Pd), osmium (Os), iridium (Ir) and platinum (Pt). These metals arevery rare in the Earth’s continental crust, ranging from 0.022 ppbfor iridium to 0.52 to Pd (Mudd et al., 2018).

Nowadays, due to the increasing demand for CRMs, new sourcesare being sought, and secondary sources such as metal scrap andindustrial waste are attracting more attention. The use of thehitherto unexploited secondary sources can reduce demand forvirgin materials and, in consequence, contribute to a decrease inmining production. One of the core principles of the circulareconomy is the reduction and minimization of resource use, andways to achieve that goal include recycling and reuse of wastes(Kirchherr et al., 2017). Mine tailings from mineral processing of acertain branch of the metal industry could be used as a source in aprocess designed to obtain one or more critical raw materials, asimplified flowsheet of this idea is shown in Fig. 1.

Chile has a long history of mining and large-scale mining startedin the first decade of the twentieth century. In 2016, Chileanminingexports were valued at 30,379 million USD according to the Na-tional Service of Geology and Mining (SERNAGEOMIN), 90% ofwhich came from copper mining (SERNAGEOMIN, 2017). Chile isthe world’s leading producer of copper. Currently, a decrease in thegrade of mined copper ores is being observed, which increases theamount of processed ore and, consequently, leads to greater tailingsdeposits for the same level of copper production. Currently, Chileproduces 1,400,000 tons of mine tailings daily and there are 696tailings storage facilities (TSF) (SERNAGEOMIN, 2018).

The objective of this study is to conduct a technical and eco-nomic assessment of the valorization of mine tailings of Chile as asource of CRMs. Therefore, the research questions addressed in thispaper are:

What critical materials can be recovered from mine tailings?What are the challenges in the production of critical materials

using mine tailings as a source?In recent years, the use of secondary sources for obtaining raw

materials has gained growing importance. This research supple-ments these works with a techno-economic feasibility study forproducing critical raw materials from mine tailings.

The data used in the study refer to mine tailings samples of 477Chilean copper mining industrial deposits. These data have notbeen previously used to assess the economic potential of the re-covery of critical materials.

2. Methodology

The first step to evaluate the recovery of CRMs from mine tail-ings is the calculation of the amount of each CRM present in

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tailings. The feasibility of recovery is next assessed for criticalmaterials found in larger quantities.

In the technological assessment, technologies for processingmine tailings are first examined. If no technologies are available,technologies for processing ore, as an analogous process, areconsidered taking into account differences between the processingof ore and processing of waste.

In the economic assessment, the discounted cash flow (DCF)method is used to assess the feasibility of the options for the re-covery CRMs frommine tailings. This method has beenwidely usedfor valuation projects (De Reyck et al., 2008; Kodukula andPapudesu, 2006; �Zi�zlavský, 2014). DCF is a commonly adoptedeconomic valuation technique and consists of discounting expectedcash flow of a future project at a given discount rate and thensumming all the cash flows of a determined period of time (Ib�a~nez-For�es et al., 2014; �Zi�zlavský, 2014).

Sensitivity analysis is performed to assess the impact of variousparameters on the NPV of CRMs recovery from mining tailings.Sensitivity analysis is a tool used to analyze how different values ofa set of independent variables affect a dependent variable. The saleprice of critical materials, operating costs, capital costs, and dis-count rate are the main inputs in the DCF method, then thesevariables are studied in the sensitivity analysis. These variables andinteractions among them were also tested using a design of ex-periments with response surface methodology.

3. Mine tailings assessment

Mining is one of the main economic activities in Chile due to thecountry’s favorable geochemical and mineralogical characteristics.Chile is the world’s leading producer of copper, producing 5,552.6thousand tons of copper in 2016 (SERNAGEOMIN, 2017), theworld’ssecond supplier of molybdenum, producing 62,746.1 tons in 2017,and the second producer of lithium, producing 77,284 tons oflithium carbonate in 2017 (SERNAGEOMIN, 2017). For some regionsin Chile, mining is the main economic activity; most mining activityis found in the Atacama Desert in northern Chile.

The Atacama Desert is the driest non-polar desert on the earth,and its copper ore deposits are world-class porphyry copper de-posits (Oyarzún et al., 2016; Tapia et al., 2018). Porphyry depositsare the principal sources of copper and molybdenum(Khorasanipour and Jafari, 2017). Porphyry deposits consist ofdistributed and stockwork sulfide mineralization located in varioushost rocks that have been altered by hydrothermal solutions intoroughly concentric zonal patterns (Dold and Fontbot�e, 2001).

Chilean mining processing plants produce large quantities ofwaste every year. Tailings dams are the most common type of

tailing deposit in the country (Ghorbani and Kuan, 2017). Previ-ously, prior to the adoption of appropriate regulations, tailings wereabandoned in deposits and no efforts were made to ensure thesafety of the nearby communities but nowadays the handling andstorage of tailings are strictly regulated. In 2011, the Law 22.551waspromulgated. It regulates the closing of mining facilities andspecifies that tailings must be physically and chemically stabilized(Ministerio de Minería, 2011; SERNAGEOMIN, 2011).

In Chile, there are 696 mine tailings deposits registered in anational registry, compiled between 2016 and 2018. The registry isexpected to be updated as new mine tailings facilities are openedand old abandoned tailing deposits are discovered. AntofagastaRegion hosts larger mine tailings deposits (SERNAGEOMIN, 2018)because of the size of the mining sector in this region, which ac-counts for 47% of the contribution to Chilean mining activity. Themost serious problems associated with tailings and handling andstorage of tailings are related to the seismic nature of the country,and risks associated with tailings dam failure include fatalities,serious water contamination, and destruction of the land.

3.1. Characterization of mine tailings

The chemical composition of tailings in 477 mine tailings de-posits is available on the website of the National Service of Geologyand Mining of Chile (SERNAGEOMIN) (SERNAGEOMIN, 2018). Thisdatabase contains values for concentrations of 56 elements,including 22 CRMs featuring on the latest EC list. The CRMsanalyzed in the SERNAGEOMIN database are vanadium, cobalt,yttrium, niobium, scandium, hafnium, tantalum, antimony, bis-muth, tungsten, lanthanum, cerium, praseodymium, neodymium,samarium, europium, gadolinium, terbium, dysprosium, holmium,erbium, thulium, ytterbium and lutetium (SERNAGEOMIN, 2018).

Chemical composition in each mine tailings deposit is differentand it depends on the type of mineral rocks mined and the pro-cesses used in the plant. In the geochemical characterization ofChilean tailings, it can be noticed that most tailings deposits have ahigh percentage of silicon oxide or ferric oxide due to the type ofminerals processed (SERNAGEOMIN, 2018).

Data in the SERNAGEOMIN database are classified by the currentstatus of the tailings deposits: active, inactive, and abandoned. In themethodology used in this study, only inactive and abandoned tailingswere analyzed, because their volume and chemical composition donot change over time. In the case of active tailings, although theirvolume is greatest, their chemical composition may change over thecourse of years, which is why they have not been considered in thisstudy. Mine tailings of the Antofagasta Region are examined becausethe tailing volume storage is greater in this region than in other

Fig. 1. Simplified mining processes flowsheet featuring conventional processes to obtain metal and the re-processing of tailings to obtain CRMs.

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regions. The TSFs analyzed cover 16 inactive deposits. The location ofmine tailings of the Antofagasta Region can be seen in Fig. 2.

CRMs found in larger quantities are given in Table 1. The sum ofREEs was also calculated, to produce REE concentrate or mis-chmetal, which is an alloy of REEs. The sum of REEs does notconsider scandium because it is separated in a different process.

3.2. Technology assessment

A literature review was conducted to investigate the availabletechnologies for the recovery of critical raw materials from minetailings. If no technologies are available for tailings processing, thenthose used for processing of primary ores are considered as areference. It is important to notice that mine tailings are already inthe form of slurry or paste, depending on the percentage of waterpresent, so there are no mining costs, which represent approxi-mately 43% of operating cost in a mine (Curry et al., 2014).

Existing technologies for CRMs production are briefly describedin Table 2. Most of these technologies are for primary ores. Someapplications for secondary sources such as industrial waste andmine tailings exist (Abisheva et al., 2017; Binnemans et al., 2015;Figueiredo et al., 2018; Innocenzi et al., 2014; Jorjani and Shahbazi,2016; Peelman et al., 2016), but they should be treated as emergingtechnologies. Significant further development of these new tech-nologies is required before they are suitable for industrial-scaleusage (Kinnunen and Kaksonen, 2019).

In spite of the low concentration of REEs in comparison to end-of-life consumer goods, mine tailings are a potential source of REEsbecause of the large volumes of mine tailings, which mean that thetotal amount of recoverable REEs could be high (Binnemans et al.,2015). Several processes have been proposed for the recovery ofREEs from mine tailings. Peelman et al. (2018) have proposed amethod for the recovery of REEs from mine tailings from apatitemineral with an REE content of 1200e1500 ppm using acidicleaching followed by cryogenic crystallization and solvent extrac-tion. They achieved a 70e100% recovery of REE.

There are no processing plants using copper mine tailings as asource of CRMs. Therefore, technologies used for primary sources

are assumed to be also applicable to the processing of mine tailings.Based on the content of the mine tailings analyzed, two feasibilitystudies are conducted; the first for producing rare earth oxides andthe second for vanadium recovery, using mine tailings as a source.

The extraction process for REEs, in a general form, includes threesteps: mining and comminution; ore beneficiation processes con-sisting of flotation, gravity and magnetic techniques to generateREE concentrate; and hydrometallurgical methods to extract REEcompounds (Sadri et al., 2017). Hydrometallurgical methodsinclude cracking of REE concentrate; leaching, neutralization andprecipitation processes; and separation and purification techniquessuch as solvent extraction. Solvent extraction allows recoveringREEs with a high degree of purity, moreover, a variety of solventextraction reagents is available. For secondary waste, selectiveextraction of REEs is required from solutions with a high content ofother species (Tunsu et al., 2019).

A life cycle inventory and impact assessment of the productionof RE oxides from primary bastnasite and monazite has been pre-sented for the Bayan Obo mine in Inner Mongolia, China, in (Koltunand Tharumarajah, 2014). The study found out the mining andbeneficiation stage accounts for 6.98% of energy consumption and6.51% of water consumption. When processing mine tailings, thereis no mining stage, so the values were adapted. Adapted values ofenergy and water consumption to obtain RE oxides from wastematerial are included in the supplementary material.

Primary ores of REEs are usually treated with alkaline pressureleaching or sulfuric acid roasting. However, mine tailings are a low-grade source of REEs, so these technologiesmaynot be economicallyfeasible. Chloride-based hydrometallurgical processes may be apotential alternative to traditional capital intensive hydrometallur-gical processes based on high temperature and pressure (Onyedikaet al., 2012) and they could be a suitable option for REE recoveryfrom tailings at economically viable capital and operating cost.

In the case of vanadium, it is mainly produced as a co-productfrom the vanadium slag before the steel converter. The main va-nadium products are vanadium pentoxide (V2O5) and ferrovana-dium (FeV) (European Commission, 2017b). Other sources ofvanadium are stone coal, steel scrap, and fossil fuels.

The mine tailings analyzed in this study have a CRMs contentthat varies between 80 and 214,000 g per ton of tailing. In Chile,there are currently no projects providing for the use ofmine tailingsas a source of CRMs, nor approved initiatives for the production ofCRMs from primary ores.

3.3. Economic assessment

The economic assessment is done in two main steps. The firststep focuses on the economic potential of CRMs found in inactivemine tailings as an in-situ value, considering the monetary value ofthe CRMs to assess the feasibility of CRMs production. The secondstage concentrates on the analysis of the feasibility of CRMs pro-duction using mine tailings as a source.

Prices of critical materials may differ fromone source to another.In addition, the prices of some critical materials are not publiclyavailable as they are traded privately. To calculate the economicpotential of inactive mine tailings deposits, the following priceswere used, see Table 3.

The economic potential of CRMs recovery was calculated as thefraction of each CRM in the tailings multiplied by the mass of eachTSF for the 16 TSFs studied. The economic potential is a referencevalue for the total REE value of the mine tailings. The economicpotential of these TSFs is shown as supplementary material.

To assess the feasibility of CRMs recovery, the DFC method wasused to calculate the NPV and IRR for REOs production and V2O5productionusingmine tailings. TheNPV is thedifferencebetween the

Fig. 2. Tailings storage facilities in Antofagasta Region, blue represents inactive orabandoned deposits and red is for active deposits. (For interpretation of the referencesto colour in this figure legend, the reader is referred to the Web version of this article.)

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presentvalueof cash inflowsand thepresentvalueof cashoutflows inaparticularperiodof time. IRR is thediscount rate atwhich theNPVoffuture cash flows is equal to the initial investment. NPV and IRR aremetrics used in capital budgeting and decision-making. The calcula-tion does not include external factors such as inflation. To obtain theNPVand IRR for theoptionsassessed, capital costs andoperating costsof projects with similar characteristics were used.

Capital costs, also referred to as capital expenses or CAPEX,

represent the investment made for the project, which includescosts of the development phase which, among other costs, com-prises the purchase of the equipment, building a manufacturingplant and the cost of product launch. The investment represents thefirst cash flow in the DFC method.

Operating costs, operating expenses or OPEX, are expensesincurred during the lifetime of the project. In the case of a miningproject, these would include the cost of labor, water, and energy,

Table 1Total tonnage and uses of CRMs present in inactive tailings deposits of the Antofagasta Region (16 deposits).

CRMs Tons Uses

Vanadium (V) 46,110 Most of the vanadium produced is used in ferrovanadium or as a steel additive. Another use is as vanadium pentoxide.Cerium (Ce) 22,886 Cerium is used as a catalyst converter for carbon monoxide emissions, as an additive in glass for reducing UV transmission, and in carbon-arc

lighting.Cobalt (Co) 16,940 The main uses of cobalt are in battery chemicals for NieCd, Ni-metal hydride and Li-ion battery types, superalloys, hard materials, catalysts, and

magnets.Yttrium (Y) 16,039 Yttrium is used for energy-efficient fluorescent lamps, in the treatment of various cancers, in aerospace surface and barriers, as a superconductor,

in aluminum and magnesium alloys, and in-camera lenses.Neodymium

(Nd)14,880 Neodymium is used to create high-strength magnets for computers, cell phones, medical equipment, electric cars, wind turbines, and audio

systems. It is also used in the glass and ceramic industries.Lanthanum (La) 10,253 Lanthanum is used in nickel metal hydride rechargeable batteries for hybrid automobiles, in high-quality camera and telescope lenses, and in

petroleum cracking catalysts in oil refineries.Scandium (Sc) 9,359 Scandium is used to increase strength and corrosion resistance in aluminum alloys, in high-intensity discharge lamps, and in fuel cells to increase

efficiency at lower temperatures.Niobium (Nb) 4,823 Niobium is used in high strength low alloy (HSLA) steels as ferroniobium and in superconducting magnets.Antimony (Sb) 3,751 Principal uses for antimony are in alloys with lead and tin, and in lead-acid batteries.Samarium (Sm) 3,456 The main use of samarium is in cobalt-samarium alloy magnets for small motors, quartz watches, and camera shutters. Samarium is also used in

lasers.Gadolinium

(Gd)3,357 Gadolinium is mainly used for NdFeB permanent magnets, lightning applications and in metallurgy.

Praseodymium(Pr)

3,245 Praseodymium is used in NdFeB magnets, ceramics, batteries, catalysts, glass polishing and fiber amplifiers.

Dysprosium(Dy)

2,705 Dysprosium is used mainly and almost inclusively in NdFeB magnets.

REEs (total) 82,254

Table 2Available and emerging technologies for CRMs processing.

CRMs Production process

Rare earthelements

- Acidic leaching-cryogenic crystallization-solvent extraction from mine tailings with apatite and monazite. (Peelman et al., 2016).- Bioleaching for REEs extraction from low-grade sources. (Peelman et al., 2014).- Solvent extraction to recover REEs from mine tailings of gold and tellurium mining (Tunsu et al., 2019).-Use of solvent impregnated resins (SIR) to recover REEs from low concentration solutions (Onishi et al., 2010; Sun et al., 2009; Yoon et al., 2016)

Antimony - Crushing and pyrometallurgical methods for primary ores (Anderson, 2012).-Crushing and hydrometallurgical methods like leaching and electrodeposition (Anderson, 2012)

Cobalt - Bioleaching of sulfidic tailings of iron mines. (Ahmadi et al., 2015).- Mineral beneficiation, comminution, flotation, smelting, leaching or refining for sulfide ores (European Commission, 2017b).-Calcination, pyrometallurgical process, hydrometallurgical methods for lanthanides ores (European Commission, 2017b)

Niobium -Gravity separation, froth flotation, magnetic and electrostatic separation, and acid leaching depending on the ore (European Commission, 2017b)Vanadium - Extraction of vanadium as a co-product to iron from vanadium slag includes bearing, roasting, acid leaching solvent extraction, ion exchange, and

precipitation (Xiang et al., 2018).- Desliming-flotation from low-grade stone coal (European Commission, 2017b).-Preform reduction process (PRP) based on a metallothermic reduction of vanadium pentoxide (V2O5). (Miyauchi and Okabe, 2010).

Table 3CRMs prices in July 2018.

Critical material Price ($US/kg)a Critical material Price (US$/kg)a

Antimony 8.51 Neodymium metal � 99.5% 68.0Cerium metal � 99.5% 7.00 Neodymium oxide � 99.5% 66.7Cerium oxide � 99.5% 5.59 Praseodymium metal � 99% 125.00Cobalt 87.5 Praseodymium oxide � 99.5% 81.6Dysprosium metal � 99% 268.57 Samarium metal � 99.9% 15Dysprosium oxide � 99.5% 226.80 Scandium metal � 99.9% 3,458Gadolinium metal � 99.9% 44.00 Scandium oxide � 99.95% 1,079Gadolinium oxide � 99.5% 20.94 Vanadium (as V2O5 80%) 40.00Lanthanum metal � 99% 7.00 Yttrium metal � 99.9% 36.5Lanthanum oxide � 99.5% 7.80 Yttrium oxide � 99.99% 4.60

a Sources: (Mineralprices.com, 2018), (Thenorthernminer.com, 2018), (LME, 2018).

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maintenance, spare parts, and indirect costs (Bhojwani et al., 2019).The first option assessed is the production, using mine tailings

as a source, of the following rare earth oxides (REOs): cerium,lanthanum, neodymium, yttrium, samarium, gadolinium, praseo-dymium and dysprosium. Scandium is also considered as REE but ithas different properties and a different production process, whichis why it was not assessed togetherwith the abovementioned REEs.

The second option assessed is vanadium as the production ofvanadium pentoxide (V2O5). It is due to the fact that vanadium isthe main CRM found TSFs in the Antofagasta Region (see Table 1).

3.3.1. Feasibility of producing rare earth elements using minetailings as a source

For REOs production, we have considered only REEs found inlarger quantities. Due to the lack of data about similar projects thatuse mine tailings or industrial waste as source material, we useddata from a Canadian project that produces rare earth oxides(Hudson Resources Inc, 2013) from primary sources to produce ofneodymium, praseodymium, lanthanum, and cerium. Data used forNVP calculation are shown in Table 4.

The price used to calculate NPV corresponds to the weightedaverage for REOs; cerium, lanthanum, samarium, gadolinium,praseodymium, dysprosium, and yttrium oxide, which is 37 USD/kgof REOs produced, 40% was discounted to reflect the differencebetween REO concentrate and separated individual rare earth oxideprices, so the price used for NPV calculations is 22 USD/kg, as in thereport it was used as a reference price. The grade of REEs corre-sponds to the average REEs grade in all the deposits analyzed. In themine tailings covered by the analysis, the average grade is lowerthan in most primary ore processing projects, so the productionwas reduced accordingly.

It is important to note that operating costs and capital costs arereferential values. In the case of mine tailings, costs related toextracting mineral ores should not be considered since tailings arematerials that have already been mined and processed.

The NPV is 672,987 USD which means that the projected earn-ings generated for this proposed REOs production exceed theanticipated costs and the overall value for the project is positive.However, even though the NPV is positive, its value is too low toinvest in a project of such a magnitude. The IRR is 10.03% which isalmost the same as the discount rate chosen for the project, thisconfirms that the project is not highly profitable. Cash inflows andoutflows are included as supplementary material.

3.3.2. Feasibility of producing vanadium using mine tailings as asource

Vanadium is the main CRM found in mine tailings in the Anto-fagasta Region. There are 46,110 tons of vanadium in inactive TSFs,but active tailings in this area have the potential for ca. 900, 000tons of vanadium.

Capital and operating costs for vanadium production are takenfrom a preliminary economic assessment study for the Gibellini

vanadium project (Lee, 2018). This project has been designed as anopen pit heap leaching operation to obtain vanadium pentoxide(V2O5). The Gibellini project is designed for processing of low-grademinerals, so it is suitable for mine tailings, but in this study, pro-duction is reduced because the grade in mine tailings is lower inmine tailings. The values used for the calculation of NPV and IRR aregiven in Table 5. The values of NPV and IRR for vanadium produc-tion from Chilean mine tailings are shown in the supplementarymaterial.

The NPV is 76 million US$ and the IRR is 21%, these valuesindicate that the project is profitable as the NPV is positive and theIRR is higher than the discount rate. Cash inflows and outflows areshown as supplementary material.

3.4. Sensitivity analysis

In this study, a sensitivity analysis was performed on four pa-rameters: capital cost, operating cost, critical materials price, andthe effect of the discount rate on NPV for the examined options. Theobjective of the sensitivity analysis is to understand the uncertaintyin the NPV for the examined parameters. These parameters werechosen because they are the key components in the DCF method.

Sensitivity analysis determines how different values of one ormore independent variables affect a dependent variable under agiven set of assumptions. Sensitivity analysis is the last stage of theprocess of assessing and selecting a technological alternative(Ib�a~nez-For�es et al., 2014). Sensitivity analysis studies how severalsources of uncertainty contribute to the entire uncertainty of amathematical model.

In the DCF method, the discount rate is the rate used to convertthe future value of a project cash flows to today’s value. The dis-count rate is adjusted to the risk associated with a project. There-fore, the higher the risk, the higher the discount rate (Kodukula andPapudesu, 2006). Risk is associated with the uncertainty of aproject. In business, risks may have a positive or negative effect. Thediscount rate was varied to acknowledge that mining projects dealwith uncertainties that can be included in the model by choosing ahigher discount rate.

Mining commodity prices always show greater volatility thanthose of any other primary products (Foo et al., 2018). Prices ofcritical materials may experience price spikes due to their insta-bility caused by the risk of supply disruption. Critical materials haveinelasticity element in their prices, this means that the demand forthese materials is not highly affected by the price (Binnemans et al.,2013b; Leader et al., 2019). Critical materials are needed in tech-nologies, such as clean energy technologies, in which there are notsubstitutes for the critical materials needed (Leader et al., 2019).

The price of each critical material assessed was considered as animportant parameter that contributes to the overall uncertainty ofthe project.

Since capital costs and operating costs used in this study arereferential values, and they are further used as inputs in the DCF

Table 4Data for REOs project.

Data Value Unit

Capital cost 342,514,448 US$Life of mine 20 yearsOperating cost 13,080 US$/ton REOsREOs Price 22,000 US$/ton REOsProduction capacity 4,000 tons REOs/yearAnnual increase (OPEX) 1.5 %Annual increase (PRICE) 1.5 %Discount rate 10 %

Table 5Data for vanadium project.

Data Value Unit

Capital cost including 25% contingency 116,760,000 US$Life of mine 14 yearsOperating cost 14,767 US$/ton V2O5

Vanadium pentoxide price 40,000 US$/ton V2O5

Production capacity 1,000 tons V2O5/yearAnnual increase (OPEX) 1.5 %Annual increase (PRICE) 1.5 %Discount rate 10 %

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method, it was necessary to address the variability of the real valuesof these parameters vis-a-vis the values used here.

Capital cost, operating costs, and prices varied between�30 and30% of the original value. The discount rate varied between 0.05 and0.3.

The results of the sensitivity analysis for the REOs price areshown in Fig. 3. It can be seen that for every 5% increase in the priceof the REOs, the NPV increases by 38 million US$. NPV is highlysensitive to changes in REO prices. NPV becomes negativewhen theprice of REOs is below 22 US$/kg, making the project financiallyunviable.

The NPV is less sensitive to changes in operating costs thanprice; NPV decreases to 21 million US$ with an increase of 5% inoperating costs. The results of the sensitivity analysis of the NPV tothe capital cost show that as the investment cost increases by 5%,the NPV decreases by ca. 15 million US$.

The discount rate varied between 0.05 and 0.3. The NPV is not alinear function of the discount rate, the value considered was 0.1.When the discount rate is 0.11, NPV decreases by approximately 21million US$. With a discount rate higher than 0.1, NPV becomesnegative, making the project unviable.

Results of sensitivity analysis of NPV for vanadium pentoxideproduction are shown in Fig. 3. When the price increases by 5%,NPV increased by ca. 14 million US$. When the price drops by 26%,NPV becomes negative and the project unviable.

Results of the sensitivity analysis of NPV to operating costs showthat NPV is slightly sensitive to changes in operating costs. Whenoperating costs increase by 5%, the NPV decreases by ca. 5 millionUS$. Sensitivity analysis of the NPV to changes in capital cost showsthat with an increase of 5% in the capital cost, the NPV decreases byca. 5 million US$. The values of NPV are very similar for bothoperating costs and capital costs.

The sensitivity analysis of NPV to changes in the discount rate

shows that if the discount rate increases by 0.01 from the value of0.1 used to 0.11, the NPV decreases by 10million US$ approximately.When the discount rate is higher than 0.21, NPV becomes negative.

Results show that under certain prices, operating costs andcapital costs, it is possible to invest in producing CRMs using asecondary source such as mine tailings.

The parameters analyzed in the sensitivity study may changesimultaneously. Therefore, their interactions were analyzed usingdesign-of-experiments together with response surface methodol-ogy. In the analysis of the NPV of both projects, REOs productionand V2O5 production, four factors and three levels were considered.The factors are: the price, capital costs (CAPEX), operating costs(OPEX), and the discount rate (iÞ. The levels correspond to the valueused in the economic assessment, then low and high levels for thesame value were multiplied by 0.85 and 1.15, respectively, whichmeans the experimental design results are valid in the rangebetween�15% andþ15%. A percentage of 15%was chosen to ensurea good adjustment. The values tested for the discount rate are 0.05,0.1, and 0.15. ANOVA results show which parameters and in-teractions influence the NPV by analyzing the p-value. For the p-value < 0.01 all linear parameters and the interaction with thediscount rate were significant. Also, the statistical analysis confirmsthat price and the discount rate are the parameters exerting greaterinfluence. Regression models obtained have the following form:

NPV ¼ aþ b CAPEX þ c OPEX þ d priceþ e iþ f i2 þ g CAPEX i

þ h OPEX iþ j price i

The values for a; b; c; d; e; f ; g; h and j are �17.6, �0.9103,�59.55, 67.1, �1766, 14323, 0.0, 242.9, and �299.5 for REOs project,and 47.64, �0.9932, �12.572, 12.572, �1143.3, 5717, 0.828,49.63, �49.625 for V2O5 project, respectively. The units for NPV and

Fig. 3. Sensitivity analysis, a) Sensitivity of the NPV (REOs project) to the price of REOs, operating costs and capital costs; b) Sensitivity of NPV to discount rate in REOs project; c)sensitivity of NPV (vanadium project) to the price of V2O5, operating costs and capital costs; d) Sensitivity of NPV to discount rate in vanadium project.

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CAPEXaremillionUS$,OPEXandprice arekUS$/ton, and thediscountrate is dimensionless. The R-squared values or the coefficient of theregressions were R2 ¼ 98:17%, R2adj ¼ 97:99%, and R2pred ¼ 97:79%for REOs project, and R2 ¼ 99:95%, R2adj ¼ 99:95%, and R2pred ¼99:94% for the V2O5 project. The R2 for both projects are over 98%which means that at least 98% of the variation of the NPV can beexplained by the model. Also, excellent values of adjusted R2 andpredicted R2 were observed which suggests that the number of pa-rameters is themodel is correct and that themodel is able to producehigh quality predictions. The ANOVA results and Pareto graphics areincluded in the supplementary material. Also, supplementary mate-rial gives the results of the design-of-experiment and response sur-facemethodology for the IRRwhichbehavesdifferently fromtheNPV.

4. Discussion

Mine tailings are waste obtained from the processing of a rockwith a view to obtain one or more products that will be refined tofinally get a metal(s) that is needed. Tailings should be stored infacilities where they are disposed in accordance with the regula-tions binding in each region, otherwise, the consequences to theenvironment can be devastating.

The lack of a long-term consideration of the entire life-cycle of amine and the instability of mine projects contribute to irreversiblemineral losses and resource sterilization. With this knowledge inmind, further research should address new strategies to anticipatethe future use of material beyond the closing of a mine (L�ebre et al.,2017). Mine waste hierarchy goes from prevention as the mostfavorable option to treatment and disposal as the least favorableoptions; if waste cannot be prevented then reuse and recycling areneeded (Lottermoser, 2011). Nowadays most mine tailings go to thetreatment and disposal phase. In the Sustainable DevelopmentGoals, the World Economic Forum suggests the re-use of tailings,these goals are meant to be achieved by 2030 (World EconomicForum, 2016). The reprocessing of mine tailings is also anelement of the transformation from a linear to a circular economythat the mining industry must face. Reprocessing mine tailings toobtain critical materials reduces the dependency on reserveextraction (El Wali et al., 2019).

Other approaches to mine tailings management from a circulareconomy point of view include recovering water from mine tail-ings, which helps to reduce the reliance on seawater (Cisternas andG�alvez, 2018). Recovering water or reducing the amount of water intailing diminish the need to pump water, which decreases energyconsumption and greenhouse gas emissions involved in pumpingwater to high altitudes, where mines are usually located in Chile(Araya et al., 2018; Herrera-Le�on et al., 2019; Ramírez et al., 2019).Another approach is to use mine tailings as cementitious materialsand pigment for sustainable paints (Barros et al., 2018; Vargas andLopez, 2018).

There have been conducted several studies on new technologiesor processes to recover CRMs from secondary sources such as minewaste (Alcalde et al., 2018; Andersson et al., 2018; Figueiredo et al.,2018; Khalil et al., 2019; Markovaara-Koivisto et al., 2018; Peelmanet al., 2018). Most of these studies are carried out at laboratory andpilot plant scale. Nevertheless, the literature on the recovery ofCRMs from mine tailings is constantly growing. It is due to the factthat new sources of CRMs are urgently needed as their importancein the global economy is constantly growing. Moreover, the utili-zation of wastes such as mine tailings, instead of mineral deposits,is essential from a circular economy point of view. Therefore,extrapolation of the potential of these technologies is immenselyneeded.

Results show that mine tailings facilities of the copper industryin Chile store valuable elements such as CRMs. Therefore, the early

evaluation of geochemical content, identification of suitable tech-nologies, and an economic analysis will help to find more sus-tainable alternatives to CRMs production.

The DCF is a widely used method of financial assessment, but itis not a decisive metrics for making a final decision on real in-vestment. In order to ensure the robustness of assessment, sensi-tivity analysis was performed to analyze the effect of the possiblefluctuations of market prices, capital and operating costs on theanalyzed options of CRMs production. It has been found out thatthe discount rate and both capital and operating costs play criticalroles in economic decisions in different areas (Choi et al., 2018;Cisternas et al., 2014; Santander et al., 2014).

Reprocessing mine tailings will also have an impact on theenvironment. Due to the nature of chemical and physical processes,mineral processing is water and energy intensive, some quantitiesof solvents and reagents are used and at the end of the process,therewill still bewaste that should be stored in a tailing facility. Themining waste obtained after the reprocessing of tailings should bestored in a tailing facility complying with the regulations designedto protect people and the environment.

5. Conclusions

There are 696 tailings storage facilities in Chile, mainly fromcopper mining, which is the biggest mining industry in the country.The biggest TSF has the capacity to store 4,500,000,000 tons oftailings. Currently, there are some initiatives for recovering metalsof interest frommine tailings, but such initiatives are all in the earlystages of feasibility assessment. This study provides valuable in-formation for the assessment of the techno-economic feasibility ofindustrial-scale critical materials recovery from copper industrytailings.

Copper production will continue to grow as the copper gradedecrease. Therefore, the volume of mine tailings that are producedevery year will increase as well. Mine tailings are a worldwideenvironmental problem as they can generate acid drainage, andcause air pollution and soil contamination. Yet, mine tailingscontain several valuable elements, among them critical raw mate-rials. Therefore, the use of mine tailings as a secondary sourcewould help mitigate shortages in critical raw materials by mini-mizing the reliance on primary sources.

Chilean copper mine tailings have substantial economic poten-tial as a source of critical materials such as vanadium, cobalt, rareearth elements and antimony. Minerals contained in Chilean minetailings from copper production are mostly silicates with a lowgrade of CRMs; currently, no approved projects exist that considermine tailings as a source of CRMs. Although mine tailings have alow grade of CRMs, their already stored quantity is enormous. Inaddition, prices of critical rawmaterials can be very high, and thesefactors could make a future production of CRMs from mine tailingsfeasible.

Two options of producing CRMs using mine tailings wereassessed; production of rare earth oxides (REOs) and production ofvanadium pentoxide (V2O5). The DFC method was used to evaluatethe economic feasibility of both operations. The NPV and IRR for theproduction of REOs are positive, which means that the project isfeasible. Nevertheless, the NPV is low for an investment of this scaleand the IRR is close to the discount rate value. The sensitivityanalysis of the NPV of REOs production from mine tailings showedthat NPV is highly sensitive to the discount rate and REO prices.Results of the ANOVA confirm that the discount rate and price arethe most significant variables influencing the NPV behavior.

Vanadium pentoxide production is feasible for an investment of14 years, as the NPV is 76 million US$ and the IRR IS 21% for V2O5production. Vanadium is the main CRMs found in tailings in the

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Second Region in Chile. It is concluded that producing CRMs usinginactive tailings and later tailings from the active mining processesmay be a feasible option to ensure profitable use of mine tailingsand to diversify CRMs supply.

Declaration of competing interest

The authors declare that they have no known competingfinancial interests or personal relationships that could haveappeared to influence the work reported in this paper.

CRediT authorship contribution statement

Natalia Araya: Conceptualization, Methodology, Validation,Formal analysis, Investigation, Writing - original draft, Visualiza-tion. Andrzej Kraslawski: Conceptualization, Methodology,Writing - review & editing, Supervision. Luis A. Cisternas:Conceptualization, Validation, Formal analysis, Writing - review &editing, Visualization, Supervision, Funding acquisition.

Acknowledgments

This publication was supported by Agencia Nacional de Inves-tigaci�on y Desarrollo de Chile (ANID), AnilloeGrant ACM 170005. N.Araya thanks the ANID (2017, No. 21170815) for a scholarship insupport of her doctoral studies. L.A.C. thanks the supported ofMINEDUCUA project, code ANT1856 and Fondecyt program grantnumber 1180826. The authors are grateful to Peter Jones for his helpin editing the paper.

Appendix A. Supplementary data

Supplementary data to this article can be found online athttps://doi.org/10.1016/j.jclepro.2020.121555.

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PUBLICATION III

Araya, N., Ramírez, Y., Kraslawski, A., Cisternas, L.A.

Feasibility of re-processing mine tailings to obtain critical materials using real options

analysis (submitted)

Submitted in Sustainable Development

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For Peer ReviewFeasibility of re-processing mine tailings to obtain critical

materials using real options analysis

Journal: Sustainable Development

Manuscript ID SD-20-0738

Wiley - Manuscript type: Research Article

Keywords: critical materials, real options, circular economy, mine tailings valorization, mine tailings management, net present value

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For Peer Review

1

Feasibility of re-processing mine tailings to obtain critical materials using real

options analysis

Abstract

The re-processing of mine tailings to obtain critical materials could reduce the mining of new

deposits as well as ensure the profitable use of the waste materials. Though, it requires

large scale industrial installations and the development of specialized technologies to obtain

critical materials. New investment in mining activities is an operation, engaging for

considerable financial resources involved. The scale of such an endeavor makes a new

mining activity a high-risk operation due to several uncertainties present. Therefore, there is

an acute need to use new tools to assess the risk associated with the planning and

development of new mining activities.

This study introduces a framework to evaluate the economic risk related to the re-processing

of mine tailings to obtain critical materials. The framework, based on real options analysis

(ROA), and sensitivity and uncertainty analysis, was applied to analyze the profitability of

using mine tailings as a source of critical materials in the Chilean mining industry.

Results show that tailing storage facilities in Chile have some stocks of critical materials, like

scandium, whose extraction could be profitable. For the data used, the results of uncertainty

and sensitivity analyses show that capital expenditure has a more significant influence than

the other variables. Therefore, for the case of mine tailings re-processing, it is essential to

develop processes and technologies that enable lower capital expenses.

Keywords: Critical Materials; Real Options; Circular Economy; Mine Tailings Valorization; Mine

Tailings Management; Net Present Value

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1. Introduction

Critical materials (CMs) are vital for the functioning of modern society. They are fundamental

to the production of a broad range of goods and applications in our everyday life. Some raw

materials are more important than others due to their role in digital technologies, low-carbon

technologies, and sustainable mobility (David & Koch, 2019; Mathieux et al., 2017; X. Wang

et al., 2017). According to European Commission, critical raw materials are a group of raw

materials possessing two common characteristics: they have a high economic importance

to European Union and their supply is associated with high risk (European Commission,

2017b). The recent list made by European Commission includes elements such as rare

Earth Elements (REEs), vanadium, cobalt, platinum group metals, among others (European

Commission, 2017b).

Currently, extracting raw materials and metals from ore bodies of declining ore grade means

potentially bigger mine size generating more waste, overburden to the environment, higher

consumption of energy, water, and auxiliary materials which overall produce severe

environmental consequences and larger political risks (de Koning et al., 2018; Mudd, 2010;

Northey, Mudd, Saarivuori, Wessman-Jääskeläinen, & Haque, 2016; Žibret et al., 2020).

Furthermore, by 2050 the overall demand for metals will rise by a factor of 3-4 (de Koning

et al., 2018). When a mine has exhausted its resources whose extraction is economically

viable, an alternative is to close it and then reopen when the market and technology

conditions enable a profitable re-processing of tailings (Northey et al., 2016).

Long-term supply of metals highly depends on actual and expected prices, cumulative

availability curve, and new mining technologies (de Koning et al., 2018; Gordon, Bertram, &

Graedel, 2007; Tilton & Lagos, 2007; Yaksic & Tilton, 2009). Additionally, the development

of new high-tech technologies might lead to disruptive demand change (Tukker, 2014);

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meanwhile, it may take ten years or more to open new mines and adjust production (de

Koning et al., 2018).

Mine tailings are waste obtained after the processing of some minerals to acquire one or

more elements of interest. They are composed of a mixture of heavy metals, water, sand,

and fine-grained solid material, and generally are deposited in ponds without further

treatment (Babel, Chauhan, Ali, & Yadav, 2016; Santibañez et al., 2012; L. Wang, Ji, Hu,

Liu, & Sun, 2017).

Mine tailings deposits may contain many valuable elements as has been shown in several

studies (Alcalde, Kelm, & Vergara, 2018; Andersson, Finne, Jensen, & Eggen, 2018;

Figueiredo et al., 2018; Khalil et al., 2019; Khorasanipour & Jafari, 2017; Macías-Macías,

Ceniceros-Gómez, Gutiérrez-Ruiz, González-Chávez, & Martínez-Jardines, 2019;

Markovaara-Koivisto et al., 2018; Medas, Cidu, De Giudici, & Podda, 2013). In the particular

case of Chilean copper mine tailings, 0.82% are metals, non-metals, and metalloids, 0.01%

rare earth elements, and the rest major rock-forming elements (SERNAGEOMIN, 2017).

Nowadays, mine tailings are increasingly often seen as a potential source of raw materials,

and secondary sources are attracting more and more attention due to the benefits of a

circular economy approach (Jeswiet, 2017; Kinnunen & Kaksonen, 2019).

Mine tailings could be re-processed to extract CMs. This study aims to propose a framework

to assess the feasibility of re-processing mine tailings to obtain CMs. The presented

methodology is illustrated by the set of unique data applicable to Chilean mine tailings.

However, thanks to its generality, the proposed approach could be applied in other mine

tailings deposits where geochemical data are available. For example, the contents of CMs

in mine tailings have been already measured in some deposits in Finland, Sweden, Portugal,

Indonesia, and Mexico (Ceniceros-Gómez, Macías-Macías, de la Cruz-Moreno, Gutiérrez-

Ruiz, & Martínez-Jardines, 2018; Hällström, Alakangas, & Martinsson, 2018; Markovaara-

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Koivisto et al., 2018; Peelman, Kooijman, Sietsma, & Yang, 2018; Szamałek, Konopka,

Zglinicki, & Marciniak-Maliszewska, 2013; Tunsu, Menard, Eriksen, Ekberg, & Petranikova,

2019).

The research questions that this study seeks to answer are:

• Is it economically feasible to invest in a project developed around the idea of re-

processing mine tailings to obtain critical materials?

• How can real options analysis improve the decision to invest in a project using mine

tailings as a source of critical materials?

• How can the net present value variables influence real options performance?

The framework developed in this study is applied to a case study based on active mine

tailings located in northern Chile. This area features several mining projects based on

copper resources, leaving tremendous volumes of tailings that are stored without any

economical purpose.

The novel contribution of this article consists in considering ROA and sensitivity and

uncertainty analysis to give flexibility to the economic assessment of mine tailings re-

processing, acknowledging the uncertainties involved. Net present value (NPV) is calculated

using the DCF method as a starting point, then with ROA, different outcomes for an

investment project are estimated (Arnold, 2014; Brandão, Dyer, & Hahn, 2005; Kodukula &

Papudesu, 2006; Trigeorgis, 1996). The viability of mining investments depends on

variables that have high uncertainty as to market prices of metals. In the case of re-

processing mine tailings, technology developments and business model development are

still needed. To study the influence of several variables on NPV outcome, Monte Carlo

simulation is used to perform sensitivity and uncertainty analysis.

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1.1. The current state of mine tailings re-processing technologies

The annual amount of mine tailings generated by the mining industry exceeds 10 billion tons

(Adiansyah, Rosano, Vink, & Keir, 2015) and is expected to be growing because of the

increasing production forecast by 2035 the volume of tailings will double (CESCO, 2019).

Due to higher demand for mineral products and lower grades of ore as a result of which

more materials will have to be processed in more energy-intensive processes (C. Wang,

Harbottle, Liu, & Xu, 2014). Particularly, Chile has 6,500 million m3 of mine tailings and has

an approved capacity of over 14,470 million m3 (SERNAGEOMIN, 2019a).

Mine tailings contain several CMs, even if their content is low, the volumes of mine tailings

are big enough to consider re-processing (Binnemans, Jones, Blanpain, Van Gerven, &

Pontikes, 2015; Careddu, Dino, Danielsen, & Přikryl, 2018). Several studies analyze the

geochemical content of mine tailings to demonstrate that they contain CMs and point out

that tailings could be re-processed in the future (Ceniceros-Gómez et al., 2018; Dino, Mehta,

Rossetti, Ajmone-Marsan, & De Luca, 2018; Markovaara-Koivisto et al., 2018; Moran-

Palacios, Ortega-Fernandez, Lopez-Castaño, & Alvarez-Cabal, 2019; Tunsu et al., 2019).

Rare earth elements (REEs) are considered CMs due to their importance for generation of

clean energy and technologies essential for the transition to a low carbon economy. The

dominant position of China as the main producer, strong dependency of industrialized

countries on imports, geopolitical factors, and high specificity are additional factors

contributing to their criticality (European Commission, 2017a; Tunsu et al., 2019). The

world’s REEs reserves are found in the Inner Mongolia region of North China, with 59.3% of

world amount (Zhang, Liu, Li, & Jiang, 2014).

The prospect of using waste like metal scrap or mine tailings for obtaining REEs is gaining

attention since it reduces the dependency on primary sources. Several studies are drawing

attention to the possibility of re-processing mine tailings to get REEs using hydrometallurgy

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processes (Borra, Pontikes, Binnemans, & Van Gerven, 2015; Peelman et al., 2018;

Peelman, Sun, Sietsma, & Yang, 2016; Zhang et al., 2014).

Sustainable development components involved in mine tailings management strategy

should include energy, water, technology, environmental impact, cost (Adiansyah et al.,

2015), and policy. The valorization of mine tailings appears a critical component to achieving

a circular economy model in the mining industry, which needs to improve its processes to

minimize the environmental impacts of mining waste (Lèbre, Corder, & Golev, 2017; Tayebi-

Khorami, Edraki, Corder, & Golev, 2019). The valorization of tailings is still in the early

stages, but it is expected to improve in the future (Kinnunen & Kaksonen, 2019).

1.2. Project valuation tools

Traditional valuation tools, such as the DCF method, are static methods that do not consider

the uncertainty of the variables used to estimate the profitability of an investment (Arnold,

2014; Brandão et al., 2005; Kodukula & Papudesu, 2006; Trigeorgis, 1996).

Investments in the mining sector are capital intensive and mostly irrevocable with a limited

economic life span. Their economic viability depends on the uncertain world market price

and on how project risks emerge (Guj & Chandra, 2019). The project value is determined by

the commodity market and flexibility inherent in the metal mining system to respond to

uncertainties (Savolainen, Collan, & Luukka, 2017). The available future metal prices can

be used as certain in the project valuation process, where their maturity is maximum

between two to five years (Savolainen, 2016).

Project valuation techniques that ignore the real option nature of the project are widely used

in the mining industry, e.g., NPV, IRR, and static DCF (Savolainen, 2016). However, static

NPV is used as a benchmark for a real NPV option and option agreement methods (Arnold,

2014). DCF method treats future cash flows as deterministic values. Methods to include

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uncertainty in the result of NPV are: increasing the discount rate, applying sensitivity

analysis, comparing pessimistic and optimistic cash flows, or to use scenario planning to

estimate expected cash flows (Gaspars-Wieloch, 2019).

There are many approaches to analyze cost-intensive investments under the conditions of

uncertainty (Cristóbal et al., 2013). One of the methods gaining popularity is ROA as it is

being applied in different fields (Insley, 2002; Nelson, Howden, & Hayman, 2013; Regan et

al., 2015; Schatzki, 2003; Slade, 2001). Real options are a right, not an obligation, to

undertake business initiatives connected with tangible assets (Kodukula & Papudesu, 2006;

T. Wang & Neufville, 2005). Real options acknowledge managerial flexibility and readiness

to adjust investment projects due to future uncertainty and the changing environment,

involving possible managerial options that can reshape a project and adapt it to changing

conditions to maintain or enhance its profitability (Trigeorgis, 1993). Real options for a

project exploit the flexibility of sequential investment with flexible strategies and the

capability to delay decisions in an engineering system to react to an uncertain outcome;

where the changes depend on exogenous and endogenous uncertainties, so it is hard to

make credible value estimates (Guj & Chandra, 2019). Common attributes of real options

valuation design include identification of sources of uncertainty, available real options

recognition, modeling of uncertain variables, and real option valuation (Kozlova, 2017).

Methods used to evaluate real options are decision trees, Monte Carlo simulations, and the

Black-Scholes model (Arnold, 2014; Collan, 2011; Kodukula & Papudesu, 2006).

ROA is of rising importance in metal mining to assess possible future metal scenarios to

cope with mining projects under growing market uncertainty and project complexity. The real

options valuation method aims to protect and increase the economic return from a project

(Savolainen, 2016) and is applied predominantly in investment project valuation (Kozlova,

2017).

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1.3. Sensitivity and Uncertainty Analysis

A project is based on many inputs that are uncertain, such as production costs, price of

materials and equipment, and sales volume. The analysis and modeling of uncertainty

enhances the ability to make appropriate decisions. The need to analyze uncertainties

comes from the awareness that data abundance does not necessarily provide certitude, and

sometimes can lead to errors in the decision-making process (Attoh-Okine & Ayyub, 2005).

Due to uncertainty, there is no project without risk, and the uncertainty could be caused by

the different factors, e.g. lack of information or data (Munier, 2014).

Sensitivity analysis examines the response or reaction of an output variable, such as the

NPV to the variations of input variables, such as price or sales volume, etc. (Munier, 2014).

Sensitivity analysis methods explore and quantify the impact of possible errors in the input

data on predicted model outputs (Loucks & van Beek, 2005). Sensitivity analysis is used in

a broad spectrum of disciplines to study how various sources of uncertainty in a model

contribute to the model’s overall uncertainty. On the other hand, uncertainty analysis

assesses the impact of ambiguous values of parameters on the final results (Cacuci, 2003).

Sensitivity analysis may be performed together with uncertainty analysis to ensure the

quality of the model and the transparency of the decision-making process (Borgonovo,

2017).

Monte Carlo simulation methods are tools widely used to perform sensitivity and uncertainty

analysis (Attoh-Okine & Ayyub, 2005). Monte Carlo simulation can be used for risk analysis

by modeling the probability of the different outcomes of a process; it can be used as a

valuation tool for projects (Arnold, 2014; Collan, 2011; Kodukula & Papudesu, 2006). Monte

Carlo simulation randomly generates values of the uncertain variables within a certain range

to simulate the potential outcomes (Kodukula & Papudesu, 2006; Mun, 2002). Sensitivity

and uncertainty analysis can be used as complementary tool to the DCF method and ROA

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to study the effect of the inputs on NPV (De Reyck, Degraeve, & Vandenborre, 2008;

Gaspars-Wieloch, 2019; Kodukula & Papudesu, 2006; Pivorienė, 2017).

2. Methodology

The profitability analysis of mine tailings processing requires the identification of

geochemical characteristics of the tailing deposit, also named tailing storage facility (TSF).

Mineral characteristics and concentration of elements that are present in the TSF along with

the mass of tailings accumulated in the deposit allow estimating the quantity of each CM

(Araya, Kraslawski, & Cisternas, 2020; Markovaara-Koivisto et al., 2018; Moran-Palacios et

al., 2019).

In the economic analysis, in-situ value is estimated by multiplying the total mass of a specific

CM by its price. Total mass is calculated based on the average concentration and mass in

a TSF (Araya et al., 2020; Markovaara-Koivisto et al., 2018). DCF method is used to

estimate the NPV of a project for extracting one or more CMs from one of the TSF analyzed.

Criteria used to choose which CM could be extracted include concentration, total mass, and

price. In some cases, finding such data, as well as get access to data for estimating CAPEX

and OPEX for each CM is rather difficult.

Subsequently, an overview of technologies suitable for re-processing mine waste stored in

a TSF to extract the CMs is needed. If these technologies are still not applicable on an

industrial scale, then, technologies used to process primary ores to obtain such CM are

considered, the same goes for economic inputs such as CAPEX, OPEX, and production.

When dealing with mine waste, some consideration needs to be given to aspects, such as

a lower grade of elements contained in it (Araya et al., 2020; Binnemans et al., 2015;

Falagán, Grail, & Johnson, 2017). Mine tailings are already in the form of a paste or slurry,

so there are no mining costs, which usually represent 43% of operating costs in a mine

(Curry, Ismay, & Jameson, 2014).

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Sensitivity and uncertainty analysis is applied to the NPV estimated by the DCF method.

ROA is applied using the NPV obtained with the DCF method using the method of risk-

neutral probabilities presented in. The binomial tree analysis is used to apply ROA. A

binomial tree is built by using the method of risk-neutral probabilities presented by Kodukula

and Papudesu (2006); this methodology involves adjusting the risk of the cash flows across

the lattice with risk-neutral probabilities and discounting them at a risk-free rate (Kodukula

& Papudesu, 2006).

2.1. Discounted Cash Flow (DCF) method

DCF method is based on the calculation of NPV of a project over its entire life cycle

accounting for the investment and the free cash flows throughout its whole life (Kodukula &

Papudesu, 2006).

𝑃𝑟𝑜𝑗𝑒𝑐𝑡 𝑁𝑃𝑉 = 𝑃𝑉 𝑜𝑓 𝑓𝑟𝑒𝑒 𝑐𝑎𝑠ℎ 𝑓𝑙𝑜𝑤𝑠 𝑖𝑛 𝑝𝑟𝑜𝑑𝑢𝑐𝑡𝑖𝑜𝑛 𝑝ℎ𝑎𝑠𝑒 ― 𝑃𝑉 𝑜𝑓 𝑖𝑛𝑣𝑒𝑠𝑡𝑚𝑒𝑛𝑡𝑠 𝑐𝑜𝑠𝑡𝑠 (1)

According to the DCF method, if the project NPV is greater than zero, it means that the

project revenues are greater than the costs of the project, so it is financially attractive

(Arnold, 2014; Kodukula & Papudesu, 2006).

Present value (PV) is the estimation of costs and net revenues of the development

production phase. These are the free cash flows over the entire life cycle of the project

(Kodukula & Papudesu, 2006).

𝑃𝑉 =𝐹𝑉

(1 + 𝑟)𝑛 (2)

Where FV is the future value, r is the discount rate per time period, and n is the number of

the time period.

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To estimate NPV of a project, capital expenses (CAPEX) and operating expenses (OPEX)

of a project with similar characteristics in terms of ore grade and production capacity are

used. CAPEX may include treatment equipment, water intake structure, site preparation,

concentrate discharge system, auxiliary equipment, piping, valves, among other cost items

(Bhojwani, Topolski, Mukherjee, Sengupta, & El-Halwagi, 2019). OPEX include labor,

energy cost, chemicals, maintenance, spare parts, and indirect cost (Bhojwani et al., 2019).

The following equation was employed to estimate NPV and PV of a project based on the

use of mine tailings:

𝑐𝑎𝑠ℎ 𝑓𝑙𝑜𝑤 = (𝑝𝑟𝑖𝑐𝑒 ∙ 𝑝𝑟𝑜𝑑𝑢𝑐𝑡𝑖𝑜𝑛 ― 𝑂𝑃𝐸𝑋 ∙ 𝑝𝑟𝑜𝑑𝑢𝑐𝑡𝑖𝑜𝑛 ―𝐶𝐴𝑃𝐸𝑋

𝑛 ) ∙ (1 ― 𝑡𝑎𝑥𝑒𝑠) +𝐶𝐴𝑃𝐸𝑋

𝑛 (3)

𝐴𝑛𝑛𝑢𝑖𝑡𝑦 = 1 ―1

(1 + 𝑅)𝑛

𝑅

(4)

𝑃𝑉 = 𝑐𝑎𝑠ℎ 𝑓𝑙𝑜𝑤 ∙ 𝑎𝑛𝑛𝑢𝑖𝑡𝑦 (5)

𝑁𝑃𝑉 = 𝑃𝑉 ― 𝐶𝐴𝑃𝐸𝑋 (6)

Where n is the time of the project development, and r is the discount rate or interest rate.

The equations formulated replace calculating cash flows for every year of the project and

then adding them up to calculate the PV.

2.2. Real Options Analysis (ROA)

A ROA or real options valuation (ROV) is performed alongside with the DCF method; ROA

is applied using PV of free cash flows and NPV of a project calculated with DCF method as

a basis to estimate different outcomes (Kodukula & Papudesu, 2006). Traditional options

used in ROA are the option to defer or the option to wait to invest in a project, expand a

project, and an option to choose between projects (Kodukula & Papudesu, 2006).

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In this study, a binomial tree is used, which is a decision tree. The binomial model can be

solved using risk-neutral probabilities or market-replicating portfolios, both have the same

theoretical framework leading to the same solutions but with different mathematical

approaches (Kodukula & Papudesu, 2006). The inputs required to build a binomial tree and

calculate the option value are the risk-free rate (r), the value of the underlying asset (S0)

which is the PV of the expected free cash flows based on the DFC method, the cost of

exercising the option (X) which is the investment required, the life of the option (T), the

volatility factor (σ) which is a measure of the variability of the underlying asset during its

lifetime, and the time frame chosen for the calculations (δt) (Kodukula & Papudesu, 2006).

In Figure 1, a generic binomial tree of 2 steps is shown.

The up (u) and down (d) factors are functions of the volatility of the underlying asset, and

they are described as follows:

𝑢 = exp (𝜎 𝛿𝑡 ) (7)

𝑑 =1𝑢 (8)

The risk-neutral probability is a mathematical intermediate that allows for discounting the

cash flows using a risk-free interest rate. The risk-neutral probability (p) is defined as follows:

𝑝 =exp (𝑟𝛿𝑡) ― 𝑑

𝑢 ― 𝑑 (9)

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Figure 1: Generic recombining binomial tree (source: adapted from Kodukula and

Papudesu, 2006).

The option to wait also called the option to defer should be included in every project. A

company may prefer to wait before it invests in a project with either negative or marginal

NPV when it is highly uncertain that the project will achieve a high NPV in the future

(Kodukula & Papudesu, 2006). An example is a delay in mining a deposit until the market

conditions are favorable.

3. Case study

Chile has a large mining industry (Cisternas & Gálvez, 2014; Jane, 2003); mining represents

9.8% of the gross domestic product, and copper mining is responsible for 8.9% (COCHILCO,

2019). Chile has a rich territory endowed with porphyric deposits in terms of copper and

molybdenum (Oyarzún & Oyarzún, 2011). In 2018, Chile produced 5,872 million of fine

copper tons equivalent to 28.3% of global production, which made it the No. 1 world producer

of copper (SERNAGEOMIN, 2019a). The country is also the second world producer of

molybdenum, a copper by-product, with 60,248 tons representing 20.4% of the world

production.

The production of copper in Chile is concentrated mainly in the northern and central parts of

the country, where 40% of the worldwide reserves of copper are found (SERNAGEOMIN,

2019a). Copper can be found in sulfide ores and oxides. Sulfide ores are the primary source

of copper. Copper is obtained from sulfide ores by flotation to concentrate copper; mine

tailings are the waste of flotation.

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In Chile, there are 740 tailing storage facilities. Most of them come from copper mining, and

all are registered in a national cadaster kept by The National Service of Geology and Mining

- SERNAGEOMIN, out of which geochemical characteristics of 634 tailing deposits are

available online, 56 chemical elements have been analyzed, including 25 CMs. The content

of silicon dioxide is also analyzed because silicon metal is a CM that can be obtained from

silicon dioxide (SERNAGEOMIN, 2019c).

The Antofagasta Region is located in the Atacama Desert in northern Chile, and it holds the

largest tailings deposits of the country, including the biggest one with the capacity of 4,500

million tons (SERNAGEOMIN, 2019b). This study is focused on active tailing deposits, i.e.,

those currently used until they reach the legally allowed capacity. These tailing deposits are

Laguna Seca, Talabre, Esperanza, Sierra Gorda, and Mantos Blancos; the location of these

mine tailings deposits is shown in Figure 2. The capacity of the active mine tailings analyzed

in this study is presented in Error! Reference source not found..

Figure 2: Active TSF located in the Antofagasta Region, source: (SERNAGEOMIN,

2019b).

4. Results

Despite low concentrations of CMs found in mine tailings, these appear as possible sources

of CMs due to their availability in larger volumes and the ease with which they can be treated

on-site using the geochemical analysis provided by SERNAGEOMIN, which shows the

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average concentration of 56 chemical elements present in tailing facilities

(SERNAGEOMIN, 2019c). The total mass of each CM contained in the TSF was calculated

using its average concentration and the mass of the tailing facility. The in-situ values were

calculated using current prices, in some cases when it was not possible to find the price of

the CM as metal, the price of the oxide was used, so these are estimates based on the

available data provided by the United States Geological Survey in their report about

commodities released in 2019 (U.S. Geological Survey, 2019), the prices that were not

available in this report were taken from websites providing metal prices (Metal Prices, 2019;

Statista, 2019). The average concentration, total mass, and price of each CM of Esperanza

TSF appear in Error! Reference source not found. as an example. The same calculations

for the other four TSF analyzed can be found in Supplementary Material.

The profitability of using mine tailings as a source of CMs is analyzed using a ROA to

produce a CM using the examined TSF. The ROA is illustrated using the option to wait if the

investment is not an attractive option according to the results of the DFC method. Reasons

to wait include situations when capital cost and/or operating costs are too high, and the

prices of CMs are not high enough to obtain a positive NPV for the project.

The example used to illustrate this analysis is the production of scandium metal. Scandium

was chosen as a CM to be extracted from mine tailings out of Table 2 due to its elevated

price and the quantity present in the TSF, as well as the availability of data about CAPEX

and OPEX for a similar project of scandium production. Scandium is not reported to be

recovered from mine tailings; it is produced mainly from primary resources and the principal

source for scandium is metal imports from China (U.S. Geological Survey, 2019), from REE

and iron ore processing in Bayan Obo, China (European Commission,

2017b).Hydrometallurgy processes have been suggested to recover scandium from

secondary sources.

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4.1. Discounted cash flow method

Data from an actual scandium feasibility study were used to estimate PV and NPV of a

mining project consisting of producing scandium (Investorintel, 2014). The following

considerations were made to adapt the data to the case of mine tailings: concentration of

scandium in the tailing deposits is 26 ppm, ten times lower than in primary sources of

scandium, mining costs are discounted considering that there is no need to incur these costs

when dealing with mine tailings, lower production is considered according to the demand for

scandium metal, an updated price is considered. The input parameters are listed in Error!

Reference source not found..

The DCF method using a risk-adjusted discount rate for five years showed that the PV for

the project is 195 million USD, an NPV -138 million, for an investment of 333 million USD. If

the DCF method is screened for a longer period, e.g., ten years, it shows a higher value of

PV and NPV, 244 million USD, and -89 million USD, respectively. It is essential to point out

that traditional mining projects, planned for 15 or 20 years, are used for calculating NPV

because they are long term investment projects, but in the case of a project based on mine

tailings and CMs it is more reasonable to use a shorter period.

4.2. Uncertainty and sensitivity analysis of NPV

To study the effect of uncertainties of input variables and their distribution on NPV results

and their sensitivity. Sensitivity and uncertainty analysis was performed using Monte Carlo

simulation in RStudio. NPV was modeled using equations (6) to (9), which is a function of

the inputs used to calculate the NPV; in this analysis, taxes, and depreciation were included.

The inputs ranged between a minimum and maximum value, considering a range 20%, ±

the following values for each output were considered: price 4.4– 6.6 million USD/ton, CAPEX

268 – 402million USD/ton, OPEX 4400 – 6600 USD/ton, discount rate 0.08 – 0.12,

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production 6.4 – 9.6 ton, and the number of years of the project was constant since NPV is

highly sensitive to changes in the period of investment. The analysis was made for an

investment of five and ten years. Fifty thousand simulations were run.

Summary of results shows, for an investment of 5 years, a minimum value of -229.03 and

maximum value of -32.5 for NPV and a mean and median that are almost equal, - 137.33

and -137.47, respectively.

Histogram and boxplot are graphical methods to test normality. The histogram purpose is to

graphically summarize the distribution of a data set; it shows the frequency of NPV results.

The histogram is presented as supplementary material.

The Boxplot represents the summary and the representation of primary data; it allows to

visualize the minimum, lower quartile, median, upper quartile, and a maximum of a data set

(Spitzer, Wildenhain, Rappsilber, & Tyers, 2014). Boxplots as a visualization method enable

to see characteristics that might not be seen otherwise, and they are a straightforward and

informative method of data interpretation (Sun & Genton, 2011). 3 presents the boxplot, BC

stands for the base case which is the case using a ± 20% variation for each input, then in

the rest of the boxplots uncertainty of one input was expanded leaving the other inputs in

the ±20%previously settled, so in C1 the price was wider, between 3.3 and 7.7 million

USD/ton, leaving the rest of the variables in the previous range of ±20%. In C2 CAPEX was

varied between 201 and 469 million USD; in C3 OPEX was varied between 3300 and 7700

USD/ton; in C4 the return rate was varied between 0.06 and 0.14; and in C5 annual

production was varied between 4.8 and 11.2 tons.

.

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Figure 3: Boxplot of net present value uncertainties for different scenarios of a 5-year

investment scandium project.

To perform global sensitivity analysis, the function of R-studio Soboljansen implements the

Monte Carlo estimation of Sobol´-Jansen indices with independent inputs. Figure 4 shows

the main and total effects of the inputs. It can be seen that the main effect and the total effect

of each variable are very close which indicates that there are no significant interactions

between them, and it confirms results obtained by the boxplot that CAPEX in this investment

case has the most significant effect on NPV.

Figure 4: Sobol´-Jansen indexes for 5- years investment scandium project.

4.3. ROA using a binomial tree method

ROA is performed using a binomial decision tree methodology presented by Kodukula and

Papudesu (2006), for an investment of five years and an investment of ten years. The

input parameters and option parameters are shown in Error! Reference source not

found..

For the two cases, five years and ten years, option parameters are the same. Next, the

development of a decision tree for an investment of five years is explained; the procedure

is the same for both cases. With the option parameters, the binomial tree is built by

calculating asset values and options values over the life cycle of the option; asset values

are obtained after multiplying S0 to u and d raised to the power indicated in each node. Those

are the numbers on top of every node of the binomial tree. For example, in node S0u5, the

expected asset value is 874 million USD.

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Option values are the bottom numbers in the tree. The option to wait expires at the end of

the binomial tree, so a decision cannot be made after the time that the decision tree takes.

Option values at year five are calculated as the expected asset value of each node minus

the cost of exercising the option, which corresponds to the investment. So, for example, in

node S0u5, the expected asset value is 874 million USD, the investment is 333 million USD,

then the net asset value is 541 million USD. The decision in node S0u5 would be to invest.

If the option value is negative, then the option value is equal to zero, because a real option

is a choice, not an obligation. The option to invest is exercised at nodes where the option

value is not zero.

Option values are the numbers below each node, and they are calculated with backward

induction. Figure 5 and Figure 6 show the binomial tree for five years and ten years’

investment, respectively. Each node represents value maximization to invest in that point or

to wait until the next period; at every node, there is an option to either invest in the project

or the option to wait until the next period, until the option expires, the net asset value, in this

case, represents the NPV. Since the option is evaluated at five-year intervals, in node S0u5,

see Figure 5 the decision is to invest in this point, and the option value is 541 million USD,

but in year five, there are also nodes where the option value is zero. In node S0u3d2, the

expected asset value is 263 million, for an investment of 333 million, the net asset value is

-70 million. Hence, the option value in this point is zero, so the decision in this node would

be not to invest.

Figure 5: Binomial tree for the option to wait for five years to invest in the scandium

project.

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Next on the intermediate nodes, the expected asset value for keeping the option open is the

discounted weighted average of potential future option values using the risk-neutral

probability that value, e.g., at node S0u4 is:

𝑝(𝑆0𝑢5) + (1 ― 𝑝)(𝑆0𝑢4𝑑) ∙ 𝑒𝑥𝑝( ―𝑟𝛿𝑡) (10)

In this node, if the option is exercised the payoff would be 647 million, resulting in a net asset

value of 314 million, by investing 333 million, since the net asset value obtained by keeping

the option open is higher, 330 million, then the option to invest is not exercised. In some

intermediate nodes, the expected asset value is lower than the investment, which results in

a net loss, then the decision at that node is to wait, which means that the option value is $0.

The option valuation binomial tree is completed until year 0.

In each node, the upper numbers represent the expected future values of the underlying

asset during the option life cycle as it evolves according to its cone of uncertainty, see Figure

5. For example, in year 2, the project is estimated to produce a total payoff between 107

and 355 million USD, at the end of year five, the payoff is between 44 and 874 million. The

bottom numbers represent option values on the maximization of investing in that point or

applying the option to wait until the next period. The option expires in the fifth year because

it is framed in such a way that it considers competitive forces and uncertainty in the market.

Based strictly on DCF results, the payoff of the project will be 195 million USD, resulting in

a negative NPV of -38 million USD. If the decision is based exclusively on the NPV result,

then the decision would be not to invest.

Real options analysis provides an additional value of 33 million USD, considering a net

present value of -138 million USD, the added value with real options analysis is 171 million

USD. The same analysis was made for a 10-year investment as shown in Figure if the same

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investment is screened to 10 years, NPV based on the DCF method is -89 million, ROA

analysis gives an added value of 105 million.

Figure 6: Binomial tree for the option to wait for ten years to invest in the scandium project.

5. Discussion

Waste valorization is a crucial component that the mining industry must do to shift from a

linear economy to a circular economy (Khaldoun, Ouadif, Baba, & Bahi, 2016; Kinnunen &

Kaksonen, 2019). There are different approaches to mine tailings valorization, e.g., the

simplest and traditional one is to recover water or to decrease water usage in the tailing

stage. Other strategies consist in recovering metals from mine tailings or using mine tailings

as a construction material (Ahmari & Zhang, 2012; Lam, Zetola, Ramírez, Montofré, &

Pereira, 2020).

The cyclic nature of the supply and demand for specific metals whose production is

extremely concentrated in geographic terms and controlled, and where society cannot solely

rely on ore mining (Kirchherr, Reike, & Hekkert, 2017) makes sticking to circular economy

principles, such as effective recycling and processing of secondary sources, a must (Tunsu

et al., 2019). Mine tailings are now seen as a potential source of several metals and minerals

(Binnemans et al., 2015; Tunsu et al., 2019). The valorization of mine tailings is at an early

stage of research; there is a lack of technology that would enable transferring knowledge

from the laboratory scale to an industrial level (Kinnunen & Kaksonen, 2019).

Results show that tailing storage facilities of copper mines in Chile contain significant

quantities of CMs. Therefore, the early evaluation of the project's profitability and feasibility

to recover CMs from mine tailings help in finding alternatives, considering the flexibility given

by real options, even to postpone the investment. Additionally, it represents a secondary

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source of CMs, decreasing the dependence on reserve extraction (El Wali, Golroudbary, &

Kraslawski, 2019).

Economic gains from the recovery of CMs come with added benefits of reducing the volume

of mine waste. Additional benefits can be achieved if, as a result of the processing of mine

tailings, these can be chemically and physically stabilized, reducing the costs of mine

closure by decreasing environmental impact and health consequences. A significant

advantage is to recover water for mining reuse from mine tailings while reducing its reliance

on seawater (Cisternas & Gálvez, 2018; Ramírez, Cisternas, & Kraslawski, 2017). Another

essential factor is decreasing energy consumption and greenhouse gas emissions involved

in pumping seawater to high altitudes for hyperarid locations, where mining companies are

located (Araya, Lucay, Cisternas, & Gálvez, 2018; Ramírez, Kraslawski, & Cisternas, 2019).

It is also essential to notice that obtaining CMs from mine tailings reduces the processing of

comminution stages (Falagán et al., 2017), minimizing energy consumption and greenhouse

gas emissions. Notably, greenhouse gas emissions can vary for every CM, e.g., in the case

of phosphorus the greenhouse gas emissions rise gradually in the mining phase and

increase exponentially in the recycling stage (Rahimpour Golroudbary, El Wali, &

Kraslawski, 2019); in the case of niobium, mining represents 21% of greenhouse gas

emissions, 72% are generated in the production stage and recycling from scrap accounts

for only 7% (Rahimpour Golroudbary, Krekhovetckii, El Wali, & Kraslawski, 2019); on the

other hand, recycling of lithium from lithium-ion batteries generates greenhouse gas

emissions by 16-20% higher than its primary production (Rahimpour Golroudbary, Calisaya-

Azpilcueta, & Kraslawski, 2019).

The analysis made on the in-situ value of TSFs of active tailings of northern Chile shows

that they contain the considerable quantities of several critical metals such as REEs,

vanadium, cobalt, silicon metal and scandium. The advantages of mine tailings re-

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processing include the recovery of desirable metals in one location, ensuring land

reclamation, reduction of landfill areas, diminishing the concentration of harmful compounds,

and no need to open new mines (Binnemans et al., 2013; Farjana, Huda, Parvez Mahmud,

& Saidur, 2019; Ganguli & Cook, 2018).

Since mine tailings have been already part-processed, by comminution, the costs, both

CAPEX and OPEX, of extracting metals from tailings could be attractive in comparison to

development of a new project based on primary ores (Falagán et al., 2017). For the data

used, the results of the sensitivity and uncertainty analysis shows that CAPEX has a greater

influence than the other studied variables. Therefore, it is justified to develop processes and

technologies that enable lower capital expenses. If time is a variable in an investment

project, then time and CAPEX are both variables with greater influence.

ROA brings in additional value, so decision-makers can explore alternatives while waiting to

invest or decide to abandon a project. While waiting for the uncertainty to clear off, to re-

estimate the project payoff (Arnold, 2014; Kodukula & Papudesu, 2006). If the payoff

continues to be unfavorable, the decision may be to keep waiting; otherwise, if the conditions

to invest in scandium production from mine tailings are favorable with a high expected

payoff, the decision would be to invest. ROA calculations are a supplement to traditional

valuation methods such as DCF based NPV (Brandão & Dyer, 2005; Kodukula & Papudesu,

2006).

ROA is usually framed in shorter periods than the ones used for long term investments

(Kodukula & Papudesu, 2006), in this study five and ten-year time horizons were used to

frame the project; for both periods, NPV is negative, but if the uncertainty clears out, the

project may be feasible. Framing the investment in a longer period, such as ten years, but

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not as long as twenty years, allows decision-makers to wait to invest in a project when

investment can be regained.

The methodology presented in this study was validated using copper tailings of northern

Chile as case study. The geochemical content of tailings may vary from one geographical

area to another depending on the type of mineral deposits. In consequence, the content of

the valuable elements will be different depending on the mine tailing analyzed. The

geochemical results of mine tailings analysis are essential to perform profitability analysis of

their re-processing.

On the limitations of the study, it considers only the economic aspect of valorization of the

project to obtain CMs from mine tailings. However, it should be mentioned that the

valorization of the tailing may be profitable in the most cases if environmental, social and

safety factors are considered, e.g. chemical and physical stabilization, land reclamation,

social license to operate. As was previously stated by Kinnunen and Kaksonen (2019)

technology development is still much needed to add value to mine tailings. Therefore, a

multidisciplinary approach is imperative to develop projects based on re-processing mine

tailings. Future research should include the assessment of environmental impact of the re-

processing of mine tailings, as they can contain heavy metals that could be scattered during

the process. Some tailings deposits in Chile need urgent intervention due to the presence

of one or more heavy metal (Lam, Montofré, et al., 2020).

The main contribution of this study is to provide a methodology to assess the feasibility of

re-processing of mine tailings by taking into account the flexibility needed for investing in the

mining projects. This approach is based on use of DCF method combined with ROA and

sensitivity and uncertainty analysis.

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6. Conclusions

Mine tailings need to be adequately stored; otherwise, they can lead to massive

catastrophes that can affect human settlements and the ecosystem inflicting irreparable

damage. Proper mine tailings management includes their chemical and physical

stabilization; however, resource recovery can also add profitability to the last stage of mine

closure. Moreover, the re-processing of wastes contributes to limiting the number of new

mining projects based on virgin resources, which usually have a considerable environmental

impact. The assessment of the economic potential of wastes is a crucial activity facilitating

the implementation of the circular economy principles. This work presents universal,

quantitative methodology for the assessment of the economic potential for the recovery of

valuable elements from mine tailings.

In this study a novel approach to assess the profitability of mine tailings to obtain CM is

introduced. A framework that includes ROA, sensitivity and uncertainty analysis is proposed,

which allows for adding flexibility, contrary to traditional valuations tools.

The mine tailings deposits have usually lower concentrations of CMs than ore mines.

However, the mine tailings are an attractive alternative for exploitation as they are stored in

deposits with large volumes and hence, having a considerable potential for the production

of CMs.

The additional factor is the fact that tailings have been already pre-processed, e.g. in

comminution processes. The case study features Chilean copper mine tailings, to analyze

the ones with significant volume among the 740 tailing storage facilities present in the

country. Mine tailings deposits that are currently active were analyzed, using geochemical

content information provided by The National Service of Geology and Mining

(SERNAGEOMIN). These deposits contain important quantities of rare earths elements,

cobalt, vanadium, silicon, and barium. Therefore, these copper mine tailings could have

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substantial economic potential as secondary sources to obtain CMs. It is well-known that

some CMs are more economically attractive than others, due to their high market price.

Therefore, demand, supply risk and economic importance of each CM should be considered

when analyzing the profitability of mine tailings re-processing.

DCF and ROA were applied to analyze the feasibility of producing scandium by re-

processing the tailing deposits featured in the case study. Additionally, sensitivity and

uncertainty analysis was performed to study the influence of price of commodity, CAPEX,

OPEX, and discount rate. These evaluations were used as a complement to the DCF and

they include Monte Carlo simulation of the NPV and the representation of the results as

boxplot and Sobol´-Jansen indices. The DCF method showed a negative NPV for

investments of 5 and 10 years. The results of the sensitivity and uncertainty analysis indicate

that CAPEX has a greater influence on NPV. ROA adds flexibility and the possibility, as an

alternative, to choose to wait until the uncertainty is reduced. Based on the calculations, it

is concluded that using a real options approach to analyze an investment for the production

of CMs from mine tailings is a useful instrument, considering the high uncertainties in the

market and the development of process technology.

When traditional methods, such as the DCF method, indicate that a project is not

economically attractive, a ROA reevaluates the project by considering options such as wait

until the project is economically feasible. The option of waiting is an interesting alternative

in the case of resource valorization of mine tailings. It is due to the lack of technological

development and economic business models for treating mine tailings as a source of CMs.

Therefore, more research on these aspects is still needed.

Mine tailings as a secondary source for obtaining valuable elements is still a novel option

that needs to be developed on an industrial scale. Therefore, there are many opportunities

for improvement that may eventually lead to the successful valorization of mining waste. A

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multidisciplinary approach is essential to secure the success of re-processing of mine

tailings to obtain CMs.

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Table 1: Allowed capacity in active tailings storage facilities in Antofagasta Region,

source:(SERNAGEOMIN, 2019b).

Tailing storage facility (TSF) 106 t (until 23.04.2019) 106 t (allowed capacity)

Laguna Seca 1,302.24 4,500

Talabre 1,792.72 2,103.95

Sierra Gorda 142.80 1,350

Esperanza 240.50 750

Mantos Blancos 130.71 138.2

Table 2: Concentration, content, and in-situ values of critical materials in Esperanza tailing

storage facility.

Critical materials Average concentration (ppm)

Mass (t) Price (USD$/t)

CM in-situ value (10 6 USD$)

Vanadium 160 120,000 30,865 3,704

Cobalt 11 8,250 72,753 600

REE – Yttrium 49 36,750 36,000 1,323

Niobium 21 15,750 21,000 331

Barium 185 138,750 180 25

REE† – Scandium 26 19,500 5,420,000 105,690

Hafnium 3.88 2,910 775,000 2,255

Silicon metal 224,632 168,474,330 3,042 512,563

REE – Lanthanum 15.96 11,970 2,000 24

REE – Cerium 32.32 24,240 4,830 117

REE – Praseodymium 4.31 3,233 92,400 299

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REE – Neodymium 17.46 13,095 51,000 668

REE – Samarium 3.65 2,738 14,850 41

REE – Europium 1.06 795 56,000 45

REE – Gadolinium 3.43 2,573 22,330 57

REE – Terbium 0.49 368 647,500 238

REE – Dysprosium 2.87 2,153 280,700 604

REE – Holmium 0.55 413 38,000 16

REE – Erbium 1.71 1,283 140,000 180

REE – Thulium 0.26 195 not available 0

REE – Ytterbium 1.6 1,200 not available 0

REE – Lutetium 0.23 173 1,258,000 217

REE – mischmetal 85.9 63,630 20,300 1,292

†RRE: rare earth element

Table 3: Input parameters for the Discounted Cash Flow method

Input parameters Value Unit

Capital expenses 333 million USD

Operating expenses 5,700 USD/t

Price of scandium metal 5.42 million USD/ t

Ore grade 26 ppm

Production 8 Ton/year

Discount rate/ interest rate 0.1

Period 5 &10 years

Taxes rate 0.35

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Table 4: Input and option parameters for ROA.

Input parameters Unit

S0 (5 years) 195 million USD

S0 (10 years) 244 million USD

T (time to expiration) 5/10 years

X 333 million USD

σ (volatility) 30 %

r (risk-free rate) 5 %

Δt (time step) 1

Option parameters

u (up factor) 1.35

d (down factor) 0.74

P (risk-neutral probability) 0.51

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Generic recombining binomial tree (source: adapted from Kodukula and Papudesu, 2006).

109x85mm (96 x 96 DPI)

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Active TSF located in the Antofagasta Region, source: (SERNAGEOMIN, 2019b).

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Boxplot of the net present value uncertainties for different scenarios of a 5-year investment scandium project.

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Sobol´-Jansen indexes for 5- years investment scandium project.

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Binomial tree for the option to wait for five years to invest in the scandium project.

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Binomial tree for the option to wait for ten years to invest in the scandium project.

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