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List of Figures Figure 2.1 Schematic illustration of charge-discharge in lithium ion batteries, Me= Co, Fe+P, Mn, Ni+Mn+Co, Ni+Co+Al, Ti, S, etc.2....................................................................................... 3 Figure 2.2 pH-Eh diagram for Li-H2O system at 25 °C, 1 atm, (a) [Li]=1 M or (b) [Li]=0.072 M (Drawn by HSC)....................................................................................................................... 5 Figure 2.3 pH-Eh diagram for Li-C-H2O system at 25 °C, 1 atm and (a) [Li]=[C]=1 M or (b) [Li]=[C]=0.072 M (Drawn by HSC). ........................................................................................... 7 Figure 2.4 Lithium supply/demand and price and their estimates.38 ....................................... 8 Figure 2.5 Annual use of lithium in tonnes in each of the primary lithium usage industries from 2002 to 2020.39 .................................................................................................................... 10 Figure 2.6 Lithium value chain.35 .............................................................................................. 12 Figure 2.7 (a) Resources and (b) Reserves in terms of deposit types in thousands metric tonnes Li metal equivalent.2 ....................................................................................................... 13 Figure 2.8 (a) Resources and (b) Reserves in terms of countries in thousands metric tonnes Li metal equivalent.3 ................................................................................................................... 14 Figure 2.9 An example of flow chart of Li2CO3 production from ores.41............................... 20 Figure 2.10 A simplified flow chart of Li2CO3 production from ores.42 ................................. 21 Figure 2.11 A schematic illustration of lithium production from brines.43 ............................ 22 Figure 2.12 A representative flow of lithium carbonate production from brines.40 .............. 22 Figure 2.13 Process flow of Salar de Atacama, Chile.42 ........................................................... 25 Figure 2.14 Process flow of Salar de Hombre Muerto, Argentina.42 ...................................... 26 Figure 2.15 Process flow of Salar de Oraroz, Argentina.42...................................................... 27 - xiii -PDF Image | LITHIUM EXTRACTION FROM BRINE using ion resin
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Product and Development Focus for Infinity Turbine
ORC Waste Heat Turbine and ORC System Build Plans: All turbine plans are $10,000 each. This allows you to build a system and then consider licensing for production after you have completed and tested a unit.Redox Flow Battery Technology: With the advent of the new USA tax credits for producing and selling batteries ($35/kW) we are focussing on a simple flow battery using shipping containers as the modular electrolyte storage units with tax credits up to $140,000 per system. Our main focus is on the salt battery. This battery can be used for both thermal and electrical storage applications. We call it the Cogeneration Battery or Cogen Battery. One project is converting salt (brine) based water conditioners to simultaneously produce power. In addition, there are many opportunities to extract Lithium from brine (salt lakes, groundwater, and producer water).Salt water or brine are huge sources for lithium. Most of the worlds lithium is acquired from a brine source. It's even in seawater in a low concentration. Brine is also a byproduct of huge powerplants, which can now use that as an electrolyte and a huge flow battery (which allows storage at the source).We welcome any business and equipment inquiries, as well as licensing our turbines for manufacturing.| CONTACT TEL: 608-238-6001 Email: greg@infinityturbine.com | RSS | AMP |