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Figure 2.16 Process flowsheet for lithium recovery in China & Tibet.42 ............................... 28 Figure 2.17 Process flow of CITIC method.42........................................................................... 29 Figure 2.18 Process flow of POSCO method.42 ........................................................................ 30 Figure 2.19 Process flow of Bateman method.42 ....................................................................... 31 Figure 2.20 Chemical structure of SDB copolymer.................................................................. 37 Figure 2.21 Chemical structure of resin with (a) sulfonate, (b) quaternary ammonium. .... 38 Figure 2.22 A flow sheet of lithium production using solvent extraction by Tenova.9 .......... 44 Figure 2.23 Schematic illustrations of heterosite FP structure: (a) oblique view, (b) view along the c-axis (Drawn by VESTA).................................................................................................... 46 Figure 2.24 Schematic illustrations of triphylite structure: (a) oblique view, (b) view along the c-axis (Drawn by VESTA).................................................................................................... 48 Figure 2.25 pH-Eh diagram for TS-H2O system at 25 °C, 1 atm, [S]=1 M (Drawn by HSC). Sulfate species (SO42- and HSO4-) were excluded in this diagram.......................................... 50 Figure 2.26 pH-Eh diagram for PS-H2O system at 25 °C, 1 atm, [S]=1 M (Drawn by HSC). ....................................................................................................................................................... 51 Figure 2.27 pH-Eh diagram for I-H2O system at 25 °C, 1 atm, [I]=1 M (Drawn by HSC).. 53 Figure 2.28 pH-Eh diagram for SF-H2O system at 25 °C, 1 atm, [S]=1 M (Drawn by HSC). ....................................................................................................................................................... 55 Figure 4.1 Lithium adsorption density of resins in LiCl solution in mg-Li/g-dry resin. ...... 75 Figure 4.2 Correlation between results of loading and stripping tests in the case of lithium chloride solution (A1 solution)................................................................................................... 76 Figure 4.3 Lithium adsorption of resins in brine in mg-Li/g-dry resin. No Data = No experiment was conducted with brine because of its low capacity in pure LiCl solution. ... 77 Figure 4.4 Correlation between results of loading and stripping tests in the case of brine - xiv -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 (Standard Web Page)