Understanding the Basics of LITHIUM EXTRACTION
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Solution Mining and Salt Cavern Challenges- SMRI's Role And
Solution Mining Research Institute J. Voigt, L. Van Sambeek, R. Schneider Solution Mining and Salt Cavern Challenges, SMRI’s Role and Research Focus Session: Salt production Keywords: brine cavern, cavern storage, cavern design, cavern research, energy storage, abandonment Abstract Solution Mining Research Institute, Inc., (SMRI) is a world-wide, non-profit, member-driven organization with chief role of providing specialized education, technical reference information, and current issue research to those in the solution mining and storage cavern industries. SMRI has for over 50 years been actively researching subjects of current and future interest to our members and the cavern industry. We are helping train and develop your future industry experts and managers. SMRI technical conferences are held two times each year, one each in North America and Europe, where most SMRI member organizations are based and/or have operations. Each conference has a technical class, includes about 20 technical paper presentations, and provides field trip opportunities to see first-hand various mines, brine/salt production and storage facilities, or historic sites/features to learn how they have been operated and managed. This paper will briefly describe 20 SMRI research projects completed since the 9th World Salt Symposium 2009 in Beijing, list SMRI’s currently active research projects or ongoing programs, and discusses our focus on future cavern research on subjects of value to the industry. SMRI research projects and resulting research reports (“RR”s) are funded entirely by SMRI annual membership dues. Research contractors and host research facilities frequently provide critical access and/or services contributed to the projects at zero or reduced cost. -
Mixing-Induced Precipitation in Brine Mining: Reactive Transport Modeling / ALEJANDRO GARCÍA-GIL (1), MAR GARCÍA-ALCARAZ (2), ENRIC VAZQUEZ (2), CARLOS AYORA (2*)
macla nº 20. julio ‘15 revista de la sociedad española de mineralogía 59 Mixing-Induced Precipitation in Brine Mining: Reactive Transport Modeling / ALEJANDRO GARCÍA-GIL (1), MAR GARCÍA-ALCARAZ (2), ENRIC VAZQUEZ (2), CARLOS AYORA (2*) (1) Departamento de Geología. Universidad Zaragoza, Pedro Cerbuna, 12. 50009 Zaragoza (2) Grupo Hidrología Subterránea, UPC-CSIC, Instituto de Diagnóstico Ambiental y Estudios del Agua, Jordi Girona 18, 08034 Barcelona INTRODUCTION planes (probably stratification planes). It is 12 to 15 m thick and has high Continental brines have become the hydraulic conductivities. (II) A less leading raw material for lithium permeable body of 2 to 8 m thick acting production worldwide. Lithium-bearing as an aquitard which consist of halite brines are found in salt aquifers (mainly that may have gypsum levels. (III) Unit B halite) in the nucleus of salars (salt is a semi-confined aquifermade up of flats). Because of extremely high halite, 8 to 11 m thick and highly evaporation rates, the primary discharge conductive. (IV) A lowpermeability body occurs by evaporation keeping the water is at the bottom of the mined system. table below the surface. Two different brines are identified in Brines are exploited through pumping aquifers “A” and “B” with a transition wells or ditches excavated in halite brine in the aquitard separating those aquifers and evaporation of the brine in aquifers. Brine extraction is carried out solar ponds to further concentration. In via brine pumping fields, i.e. horizontal fig 2. Gypsum precipitates around in a well. this type of mining, such as that in drains (1 km length) connected with REACTIVE TRANSPORT MODELING Atacama (Chile), a fast and drastic loss vertical extraction well (Fig. -
Academic Year 2017- 2018 First Term Biology Revision Sheet
Academic Year 2017- 2018 First Term Biology Revision Sheet Name: ____________________________ Date: _______________ Grade 9 Section: ______________ Q1: Choose the letter of the best answer ___ 1.What is the main function of the Golgi apparatus? A. communicates with another cell B. convert solar energy to chemical energy C. process and deliver proteins D. copy genetic material. ___2. Which of the following organelles can be found in cytoplasm and on the surface of the endoplasmic reticulum A. mitochondria B. centrosomes C. ribosomes D.centrioles ___ 3. What type of membrane allows some, but not all materials A. diffusible B. permeable C. impermeable D. selectively permeable ____4. What materials makes up a cell membrane? A. Phospholipids and cholesterol B. Cholesterol and protein C. Phospholipid, cholesterol and protein D. Phospholipid, protein and amino acid Page 1 of 7 ____5. What type of receptor is within a cell? A. Membrane receptor B. Intracellular receptor C. Intercellular receptor D. Ligand receptor ____6. Which part of phospholipid is hydrophobic? A. Glycerol B. fatty acid tail C. entire phospholipid molecule D. phosphate group only ____7. A ligand produces a response in a cell if it finds the right kind of A. carbohydrate. B. hormone. C. membrane. D.receptor. ____8. What is the term for the diffusion of water across a semipermeable membrane? A. osmosis B.equilibrium C.transport D.isotonic ____9.The movement of molecules down a concentration gradient through transport proteins in the cell membrane is a type of A. selective transport. B.osmosis C.energy expenditure. D.facilitated diffusion. ___10.Nucleus act as a A. -
(WANA) WATER REGIME by MOHAMMAD ABU HAWAS
MINING BRINE AND WATER: DESALINATION IN THE CONTEXT OF THE WEST ASIA – NORTH AFRICA (WANA) WATER REGIME By MOHAMMAD ABU HAWASH Submitted to Central European University School of Public Policy In partial fulfilment for the degree of Master of Public Administration Supervisor: Thilo Bodenstein Budapest, Hungary / Vienna, Austria 2021 CEU eTD Collection Table of Contents Statement of Authorship ............................................................................................................................ 3 Abstract ........................................................................................................................................................ 4 Acknowledgements ..................................................................................................................................... 5 List of Figures .............................................................................................................................................. 6 List of Tables ............................................................................................................................................... 6 List of Illustrations ...................................................................................................................................... 7 List of Abbreviations .................................................................................................................................. 8 Introduction .............................................................................................................................................. -
1.4 Solar Cell Losses and Design in This Final Introduction Video on Photo
1.4 Solar cell losses and design In this final introduction video on photovoltaic energy conversion, we will discuss the various parts of a solar cell and the losses that occur in a solar cell. The losses in solar cells will provide an important framework to put everything we learn over the course of the next couple of weeks in context. The learning objective for this video are to understand the main function of the various parts of a solar cell. We will discuss the main losses that occur in solar cells and we will come to understand how these losses lead to the design rules for solar cells. Shown here is a standard silicon wafer based solar cell. These are the most common type of solar cells, accounting for about 93 % of the total production in 2015. We will base this solar cell on a p-type silicon absorber even though some silicon cells can be made with an n-type absorber layer. The purpose of this absorber layer, as its name implies, is to absorb light. Through this absorption, minority and majority charge charge carriers are formed. In the case of a p-type absorber, electrons are the minority carriers and holes are the majority carriers. Next is the emitter layer. The emitter layer is crucial for charge carrier separation and collection. The emitter layer functions as an selective membrane, that allows minority charge carriers, in this case electrons, to move through, but resists the movement of majority carriers, in this case holes. Without the emitter layer, generated charge carriers would simply move around in the absorber layer until they recombine. -
United States Patent to 11, 3,996,141 Updike 45 Dec
United States Patent to 11, 3,996,141 Updike 45 Dec. 7, 1976 54 DALYSIS MEMBRANE 2,971,850 2/1961 Barton ............................. 195/63 X 3, 158,532 11/1964 Pall et al. ... ... 210/503 X 75 Inventor: Stuart J. Updike, Madison, Wis. 3,282,702 1 1/1966 Schreiner ........................ 195/63 X (73) Assignee: Wisconsin Alumni Research 3,327,859 6/1967 Pall .............. ........ 210/266 3,526,481 9/1970 Rubricius ........... ... 210/321 X Foundation, Madison, Wis. 3,766,013 10/1973 Forgione et al. .................... 195/63 22) Filed: Jan. 17, 1974 3,809,613 5/1974 Vieth et al. ...................... 195/68 X 3,824, 150 7/1974 Lilly et al. ... ... 195/DIG. l l X 21 ) Appl. No.: 434,231 3,846,236 1 1/1974 Updike ......................... 23/258.5 X Related U.S. Application Data Primary Examiner-Frank A. Spear, Jr. (63) Continuation-in-part of Ser. No. 191,720, Oct. 22, Attorney, Agent, or Firm-McDougall, Hersh & Scott 1971, Pat. No. 3,846,236. 57 ABSTRACT 52 U.S. Cl. ................................ 210/501; 427/245 (51) Int. Cl. ......................................... B01D 13/04 A semi-permeable membrane containing a catalyst for 58 Field of Search .............. 210/22, 23, 321,500, conversion of hydrogen peroxide introduced from one side of the semi-permeable membrane to molecular 210/501, 502; 23/258.5; 195/18, 63; oxygen which is released from the opposite side of the 106/194; 264/41, 49; 427/245 semi-permeable membrane. The catalyst is preferably 56) References Cited in the form of a ruthenium oxide or sulfide and prefer UNITED STATES PATENTS ably in assymetrical distribution in the membrane. -
Electrochemistry: Elektrolytic and Galvanic Cell Co08 Galvanic Series (Beketov, Cca 1860)
1/26 Electrochemistry: Elektrolytic and galvanic cell co08 Galvanic series (Beketov, cca 1860): Li, Ca, Al, Mn, Cr Zn, Cd Fe, Pb, [H2], Cu, Ag, Au ≈ ≈ ⊕ Cell = system composed of two electrodes and an electrolyte. electrolytic cell: electric energy chemical reaction ! galvanic cell: chemical reaction electric energy ! reversible galvanic cell (zero current) Electrodes anode = electrode where oxidation occurs Cu Cu2+ + 2 e ! − 2 Cl Cl2 + 2 e − ! − cathode = electrode where reduction occurs 2 Cu + + 2 e Cu credit: Wikipedia (free) − ! Cl2 + 2 e 2 Cl − ! − Oxidation and reduction are separated in a cell. The charge flows through the circuit. 2/26 Anode and cathode co08 electrolytic cell galvanic cell '$ '$ - - ⊕&% &% ⊕ Cl2 Cu2+ Cu2+ Pt Cl ! ! 2 Cu Cl Cl − Cu − CuCl2(aq) CuCl2(aq) anode cathode anode cathode “anions go to the anode” 3/26 Galvanic cells: electrodes, convention co08 Electrodes(= half-cells) may be separated by a porous separator, polymeric mem- brane, salt bridge. Cathode is right (reduction) ⊕ Anode is left (oxidation) negative electrode (anode) positive electrode (cathode) ⊕ liquid junction phase boundary . (porous separator) j salt bridge .. semipermeable membrane k Examples: 3 Cu(s) CuCl2(c = 0.1 mol dm ) Cl2(p = 95 kPa) Pt j − j j ⊕ Ag s AgCl s NaCl m 4 mol kg 1 Na(Hg) ( ) ( ) ( = − ) j j j 1 NaCl(m = 0.1 mol kg ) AgCl(s) Ag(s) j − j j ⊕ 2 3 4 3 3 3 Pt Sn +(0.1 mol dm ) + Sn +(0.01 mol dm ) Fe +(0.2 mol dm ) Fe j − − jj − j ⊕ 4/26 Equilibrium cell potential co08 Also: electromotive potential/voltage, electromo- tive force (EMF). -
Biological Fuel Cells and Membranes
membranes Review Biological Fuel Cells and Membranes Zahra Ghassemi and Gymama Slaughter * Bioelectronics Laboratory, Department of Computer Science and Electrical Engineering, University of Maryland Baltimore County, 1000 Hilltop Circle, Baltimore, MD 21250, USA; [email protected] * Correspondence: [email protected]; Tel.: +1-410-455-8483 Academic Editor: Tongwen Xu Received: 31 October 2016; Accepted: 5 January 2017; Published: 17 January 2017 Abstract: Biofuel cells have been widely used to generate bioelectricity. Early biofuel cells employ a semi-permeable membrane to separate the anodic and cathodic compartments. The impact of different membrane materials and compositions has also been explored. Some membrane materials are employed strictly as membrane separators, while some have gained significant attention in the immobilization of enzymes or microorganisms within or behind the membrane at the electrode surface. The membrane material affects the transfer rate of the chemical species (e.g., fuel, oxygen molecules, and products) involved in the chemical reaction, which in turn has an impact on the performance of the biofuel cell. For enzymatic biofuel cells, Nafion, modified Nafion, and chitosan membranes have been used widely and continue to hold great promise in the long-term stability of enzymes and microorganisms encapsulated within them. This article provides a review of the most widely used membrane materials in the development of enzymatic and microbial biofuel cells. Keywords: biofuel cells; microbial fuel cells; semi-permeable membrane; chitosan; Nafion 1. Introduction A conventional fuel cell is an electrochemical power source that continuously converts the stored chemical energy in a fuel to electrical energy as long as there is a continuous supply of fuel. -
Indigenous Environmental Rights, Participation and Lithium Mining In
Indigenous Environmental Rights, Participation and Lithium Mining in Argentina and Bolivia: A Socio-Legal Analysis Helle Abelvik-Lawson A thesis submitted for the degree of PhD School of Law and Human Rights Centre and Interdisciplinary Studies Centre University of Essex Date of submission: May 2019 For my family, on Earth and in Heaven. i ACKNOWLEDGEMENTS First and foremost, I must thank my incredible husband-to-be Dauji Thomas, truly one of the world’s most amazing individuals, and without whom absolutely none of this would have been possible. Thank you for being there for me, and your understanding, through the hard times and the good. I am in fact wholly indebted to all my family, particularly my amazing Mama for showing me how to keep going even when the going is tough, and of course my stepdad Dean. Thanks also to Guy for giving me a wonderful place to study in the stunning Essex countryside. To my brother Frase, and Dix and Cos: I am so glad to have you all in my life. I am deeply grateful for the support of my dedicated, and encouraging and insightful supervisors, Professor Karen Hulme and Dr Jane Hindley, who went beyond the call of duty to help me achieve my aims. At Essex and elsewhere, I am incredibly fortunate to count a number of academics and experts in the field as mentors and friends, who continually pique my curiosities and inspire me to continue working in human rights. Dr Damien Short, Professor Colin Samson, Dr Corinne Lennox, Dr Julian Burger – thank you for showing me how it’s done. -
What Is the Difference Between Osmosis and Diffusion?
What is the difference between osmosis and diffusion? Students are often asked to explain the similarities and differences between osmosis and diffusion or to compare and contrast the two forms of transport. To answer the question, you need to know the definitions of osmosis and diffusion and really understand what they mean. Osmosis And Diffusion Definitions Osmosis: Osmosis is the movement of solvent particles across a semipermeable membrane from a dilute solution into a concentrated solution. The solvent moves to dilute the concentrated solution and equalize the concentration on both sides of the membrane. Diffusion: Diffusion is the movement of particles from an area of higher concentration to lower concentration. The overall effect is to equalize concentration throughout the medium. Osmosis And Diffusion Examples Examples of Osmosis: Examples of osmosis include red blood cells swelling up when exposed to fresh water and plant root hairs taking up water. To see an easy demonstration of osmosis, soak gummy candies in water. The gel of the candies acts as a semipermeable membrane. Examples of Diffusion: Examples of diffusion include perfume filling a whole room and the movement of small molecules across a cell membrane. One of the simplest demonstrations of diffusion is adding a drop of food coloring to water. Although other transport processes do occur, diffusion is the key player. Osmosis And Diffusion Similarities Osmosis and diffusion are related processes that display similarities. Both osmosis and diffusion equalize the concentration of two solutions. Both diffusion and osmosis are passive transport processes, which means they do not require any input of extra energy to occur. -
Global Lithium Sources—Industrial Use and Future in the Electric Vehicle Industry: a Review
resources Review Global Lithium Sources—Industrial Use and Future in the Electric Vehicle Industry: A Review Laurence Kavanagh * , Jerome Keohane, Guiomar Garcia Cabellos, Andrew Lloyd and John Cleary EnviroCORE, Department of Science and Health, Institute of Technology Carlow, Kilkenny, Road, Co., R93-V960 Carlow, Ireland; [email protected] (J.K.); [email protected] (G.G.C.); [email protected] (A.L.); [email protected] (J.C.) * Correspondence: [email protected] Received: 28 July 2018; Accepted: 11 September 2018; Published: 17 September 2018 Abstract: Lithium is a key component in green energy storage technologies and is rapidly becoming a metal of crucial importance to the European Union. The different industrial uses of lithium are discussed in this review along with a compilation of the locations of the main geological sources of lithium. An emphasis is placed on lithium’s use in lithium ion batteries and their use in the electric vehicle industry. The electric vehicle market is driving new demand for lithium resources. The expected scale-up in this sector will put pressure on current lithium supplies. The European Union has a burgeoning demand for lithium and is the second largest consumer of lithium resources. Currently, only 1–2% of worldwide lithium is produced in the European Union (Portugal). There are several lithium mineralisations scattered across Europe, the majority of which are currently undergoing mining feasibility studies. The increasing cost of lithium is driving a new global mining boom and should see many of Europe’s mineralisation’s becoming economic. The information given in this paper is a source of contextual information that can be used to support the European Union’s drive towards a low carbon economy and to develop the field of research. -
Case Studies on Copper and Lithium Mining in Chile
TEXTE 106 /2020 KlimRess – Impacts of climate change on mining, related environmental risks and raw material supply Case studies on copper and lithium mining in Chile TEXTE 106/2020 Environmental Research of the Federal Ministry for the Environment, Nature Conservation and Nuclear Safety Project No. (FKZ) 3716 48 324 0 Report No. FB000279/ANH,4,ENG KlimRess – Impacts of climate change on mining, related environmental risks and raw material supply Case studies on copper and lithium mining in Chile by Lukas Rüttinger, Christine Scholl, Pia van Ackern adelphi research gGmbh, Berlin and Glen Corder, Artem Golev, Thomas Baumgartl The University of Queensland, Sustainable Minerals Institute, Australia On behalf of the German Environment Agency Imprint Publisher: Umweltbundesamt Wörlitzer Platz 1 06844 Dessau-Roßlau Tel: +49 340-2103-0 Fax: +49 340-2103-2285 [email protected] Internet: www.umweltbundesamt.de /umweltbundesamt.de /umweltbundesamt Study performed by: adelphi research gGmbh Alt-Moabit 91, 10559 Berlin Study completed in: January 2018 Edited by: Section III 2.2 Resource Conservation, Material Cycles, Minerals and Metals Industry Jan Kosmol Publication as pdf: http://www.umweltbundesamt.de/publikationen ISSN 1862-4804 Dessau-Roßlau, June 2020 The responsibility for the content of this publication lies with the author(s). KlimRess – Climate change and mining in Chile: Case studies on copper and lithium Abstract The following case study is one of five country case studies carried out as part of the project ‘Impacts of climate change on the environmental criticality of Germany’s raw material demand‘ (KlimRess), commissioned by the German Federal Environment Agency (Umweltbundesamt, UBA). The project team comprised adelphi, ifeu Heidelberg and the Sustainable Minerals Institute of the University of Queensland.