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Figure 3.12 FTIR spectra for three different adsorbents (after acid leaching) having different Li/Mn molar ratios(F30-Li/Mn:1, F31-Li/Mn:1/0.8, F32-Li/Mn:0.8)........58 Figure 3.13 Effect of acid leaching process on lattice proton at different times for adsorbents synthesized by Hydrothermal-1 procedure .............................................. 59 Figure 3.14 The adsorbents synthesized with three different methods......................59 Figure 3.15 XRD spectrum of the spinel lithium manganese oxide LMO (450 oC, Li/Mn=1)....................................................................................................................61 Figure 3.16 XRD spectrum of the spinel lithium manganese oxide HMO (450 oC, Li/Mn=1)....................................................................................................................61 Figure 3.17 Structure of poly maleic anhydride-styrene-glycidy methacrlate (PSMA) .................................................................................................................................... 67 Figure 3.18 FTIR spectra of poly (styrene-maleic anhydrid-glycidyl methacrylate) terpolymer (PSMA) ................................................................................................... 69 Figure 3.19 13C-NMR spectra of PSMA.................................................................... 70 Figure 3.20 SEM photographs for Bead T16.............................................................72 Figure 3.21 SEM photographs for Bead T16 after acid leaching .............................. 72 Figure 3.22 SEM photographs for Bead T18.............................................................73 Figure 3.23 SEM photographs for Bead T21.............................................................73 Figure 3.24 SEM photographs for Bead T22.............................................................74 Figure 3.25 Van’t Hoff Plots for hexyl formamide (a), octyl formamide (b), dibutyl formamide (c)............................................................................................................. 80 Figure 3.26 Effect of initial LiCl concentration on k of hexyl formamide at pH:4. The plots were drawn for three different water/formamide volume ratios (1:1, 1:2, 1:3) at 10 oC. .............................................................................................................. 81 Figure 3.27 The lithium concentration in extract (formamide) and raffinate (water) phases at 25 oC and pH:4 for 10 ml water/10 ml hexyl formamide...........................83 Figure 3.28 The kinetics of adsorption process ......................................................... 89 Figure 3.29 The equilibrium concentration of lithium in solution vs uptake of lithium ions ............................................................................................................................. 90 Figure 3.30 Langmuir isotherm curve for LiMnO at 25 oC.......................................91 Figure 3.31 Freundlich isotherm curve for LiMnO at 25 oC. .................................... 92 Figure 3.32 The breakthrough curves at different pH values .................................... 96 xxPDF 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 |