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solution (A2 solution).................................................................................................................. 78 Figure 4.5 Lithium adsorption density of the resins which showed higher selectivity in LiCl solution. ........................................................................................................................................ 79 Figure 5.1 XRD patterns of ferric phosphate dihydrate calcined at 300, 500 and 600 °C. .. 80 Figure 5.2 XRD patterns of ferric phosphate obtained by calcination of ferric phosphate dihydrate at 600 °C and samples after lithium loading tests at 20 °C and 65 °C. ................ 81 Figure 5.3 XRD patterns of reagent-grade LFP and delithiated and lithiated ones at 65 °C in comparison with calcined FPD. ................................................................................................. 82 Figure 5.4 XRD patterns of battery-grade (BG) LFP and delithiated FP by PS oxidation. 83 Figure 5.5 XRD patterns of battery-grade (BG-) LFP and BG-FP (delithiated LFP by PS oxidation), and products after loading experiments by cuprous (Cu+) at room temperature (RoC), by cuprous (Cu+) at 65 °C (65C), by thiosulfate (TS) at 65 °C (65C), by sulfite (SF) at room temperature (RoC) and by sulfite (SF) at 65 °C (65C). All the loading experiments used B1 brine solution. ........................................................................................................................ 84 Figure 5.6 XRD patterns of battery-grade (BG-) LFP and BG-FP (delithiated LFP by PS oxidation), and products after loading experiments by thiosulfate (TS) at 25 °C. The loading experiments used B1–B8 brine solution.................................................................................... 86 Figure 5.7 XRD patterns of battery-grade (BG-) LFP and BG-FP (delithiated LFP by PS oxidation), and products after loading experiments by thiosulfate (TS) at 45 °C. The loading experiments used B1–B8 brine solution.................................................................................... 87 Figure 5.8 XRD patterns of battery-grade (BG-) LFP and BG-FP (delithiated LFP by PS oxidation), and products after loading experiments by thiosulfate (TS) at 65 °C. The loading experiments used B1–B8 brine solution.................................................................................... 88 Figure 5.9 XRD patterns of battery-grade (BG-) LFP and BG-FP (delithiated LFP by PS - xv -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)