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FIGURES LIST OF FIGURES Figure 1.1 The process scheme of Clayton Valley ....................................................10 Figure 1.2 Production scheme of LiCO3 in Salar de Atacama...................................12 Figure 1.3 Lithium insertion/extraction mechanisms (a) Lithium extraction (b) Lithium insertion O: redox side; □: ion exchange side..............................................21 Figure 1.4 Breakthrough curve for 150 days operation .............................................23 Figure 2.1 Continuous ultrafiltration set-up [92].......................................................32 Figure 2.2 Scheme of the set-up for column experiments .........................................34 Figure 2.3 Photos of the set-up for column experiments ...........................................35 Figure 2.4 Vapor pressure measurement set-up.........................................................37 Figure 3.1 Synthesis pathway of N-alkyl formamides...............................................40 Figure 3.2 Temperature dependence of viscosity for N-alkyl formamides ...............42 Figure 3.3 Temperature-vapor pressure relation for hexyl formamide......................43 Figure 3.4 Hydrothermal-1 procedure in ten steps.....................................................46 Figure 3.5 Heating curve for MnO and LiOHH2O reaction system ..........................52 Figure 3.6 Heating curve for MnO2 and LiOHH2O reaction system .........................52 Figure 3.7 Heating curve for MnCO3 and LiOHH2O reaction system ......................53 Figure 3.8 Heating curve for Mn3O4 and LiOHH2O reaction system........................54 Figure 3.9 FTIR spectrum of spinel lithium manganese oxide synthesized by MnCO3 and LiOHH2O (Li/Mn: 1/1) F30, before (LMO) and after (HMO) acid leaching .....55 Figure 3.10 FTIR spectrum of spinel lithium manganese oxide synthesized by MnCO3 and LiOHH2O (Li/Mn: 1/0.8 mole ratio) F31, before (LMO) and after (HMO) acid leaching..................................................................................................56 Figure 3.11 FTIR spectrum of spinel lithium manganese oxide synthesized via MnCO3 and LiOHH2O (Li/Mn: 0.8/1 mole ratio) F32, before (LMO) and after (HMO) acid leaching..................................................................................................57 xixPDF Image | SEPARATION OF LITHIUM FROM BRINES
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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 |