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Table 3.27 Capacity values of adsorbents at different pHs (Total volume: 100 ml, Adsorbent amount: 0.02 g).........................................................................................88 Table 3.28 Capacity value of the adsorbents at different initial lithium concentrations (pH:10.2 and adsorbent amount: 0.02 g )...................................................................88 Table 3.29 The stability of lithium manganese oxide particles in lithium recovery..93 Table 3.30 Selectivity of lithium manganese oxides with respect to Na, K and Mg. 94 Table 3.31 The column operating conditions for the pH dependency of adsorption process ........................................................................................................................ 96 Table 3.32 The column operating conditions for different initial lithium concentration in adsorption process...........................................................................97 Table 3.33 The column operating conditions for different flow rates in adsorption process ........................................................................................................................ 99 Table 3.34 The column operating conditions for different bead sizes in adsorption process ...................................................................................................................... 101 Table 3.35 The column operating conditions for feed solutions containing NaCl ..102 Table 3.36 The column operating conditions for feed solutions containing KCl .... 104 Table 3.37 The column operating conditions for feed solutions containing MgCl .105 Table 3.38 The column operating conditions for artificial brine solutions..............106 Table 3.39 The column operating conditions for concentrated brine solution taken from Çamaltı Salina .................................................................................................108 Table 3.40 The column operating conditions for boron clay extract taken form Bigadiç .....................................................................................................................109 Table 3.41 The initial and final concentrations in the feed tank before and after the operation...................................................................................................................109 Table 3.42 Elution process data of the column after Run 3.....................................111 Table 3.43 The elution of the column saturated with artificial brine solution and swept by tap water....................................................................................................114 Table 3.44 The comparison of the artificial brine and elution solution composition after sweeping by tap water......................................................................................114 Table 3.45 The second adsorption-sweeping-elution process composition with the feed solution having concentration of elution process in Run 18............................115 xviiPDF 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 |