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Figure 5.20 Weight percentage of iron phosphate in solid after loading experiments by thiosulfate (TS) at 65 °C (B1–B3 brine solution). .................................................................. 103 Figure 5.21 Adsorption density vs. temperature in the case of thiosulfate (TS) reduction (B1– B4 brine solution). The theoretical maximum of the adsorption density is 46.0 mg/g. ...... 104 Figure 5.22 Weight percentage of lithium iron phosphate in solid vs. temperature in the case of thiosulfate (TS) reduction (B1–B4 brine solution)............................................................. 105 Figure 5.23 Adsorption density of Li, Na, K, Mg, Ca on ferric phosphate after loading experiments by sulfite (SF) at 25 °C (B2–B7 brine solution). ............................................... 106 Figure 5.24 Selectivity of lithium over Na, K, Mg, Ca after loading experiments by sulfite (SF) at 25 °C (B2 and B3 brine solution). ............................................................................... 107 Figure 5.25 Weight percentage of iron phosphate in solid after loading experiments by sulfite (SF) at 25 °C (B2 and B3 brine solution). ............................................................................... 108 Figure 5.26 Adsorption density of Li, Na, K, Mg, Ca on ferric phosphate after loading experiments by sulfite (SF) at 45 °C (B2–B7 brine solution). ............................................... 109 Figure 5.27 Selectivity of lithium over Na, K, Mg, Ca after loading experiments by sulfite (SF) at 45 °C (B2 and B3 brine solution). ................................................................................110 Figure 5.28 Weight percentage of iron phosphate in solid after loading experiments by sulfite (SF) at 45 °C (B2 and B3 brine solution). ................................................................................111 Figure 5.29 Adsorption density of Li, Na, K, Mg, Ca on ferric phosphate after loading experiments by sulfite (SF) at 65 °C (B2–B7 brine solution). ................................................112 Figure 5.30 Selectivity of lithium over Na, K, Mg, Ca after loading experiments by sulfite (SF) at 65 °C (B2 and B3 brine solution). ................................................................................113 Figure 5.31 Weight percentage of iron phosphate in solid after loading experiments by sulfite (SF) at 65 °C (B2 and B3 brine solution). ................................................................................114 - xvii -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)